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WO2020175470A1 - Air supply system, control method for air supply system, and control program for air supply system - Google Patents

Air supply system, control method for air supply system, and control program for air supply system Download PDF

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Publication number
WO2020175470A1
WO2020175470A1 PCT/JP2020/007469 JP2020007469W WO2020175470A1 WO 2020175470 A1 WO2020175470 A1 WO 2020175470A1 JP 2020007469 W JP2020007469 W JP 2020007469W WO 2020175470 A1 WO2020175470 A1 WO 2020175470A1
Authority
WO
WIPO (PCT)
Prior art keywords
air
filter
regeneration
amount
compressor
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2020/007469
Other languages
French (fr)
Japanese (ja)
Inventor
卓也 杉尾
和也 除田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nabtesco Automotive Corp
Original Assignee
Nabtesco Automotive Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=72239196&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO2020175470(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Nabtesco Automotive Corp filed Critical Nabtesco Automotive Corp
Priority to CN202080030113.XA priority Critical patent/CN113710552B/en
Priority to CN202411096523.0A priority patent/CN119078773A/en
Priority to JP2021502268A priority patent/JP7568610B2/en
Publication of WO2020175470A1 publication Critical patent/WO2020175470A1/en
Anticipated expiration legal-status Critical
Priority to JP2024174622A priority patent/JP2024177424A/en
Ceased legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60TVEHICLE BRAKE CONTROL SYSTEMS OR PARTS THEREOF; BRAKE CONTROL SYSTEMS OR PARTS THEREOF, IN GENERAL; ARRANGEMENT OF BRAKING ELEMENTS ON VEHICLES IN GENERAL; PORTABLE DEVICES FOR PREVENTING UNWANTED MOVEMENT OF VEHICLES; VEHICLE MODIFICATIONS TO FACILITATE COOLING OF BRAKES
    • B60T17/00Component parts, details, or accessories of power brake systems not covered by groups B60T8/00, B60T13/00 or B60T15/00, or presenting other characteristic features
    • B60T17/002Air treatment devices
    • B60T17/004Draining and drying devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/266Drying gases or vapours by filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60TVEHICLE BRAKE CONTROL SYSTEMS OR PARTS THEREOF; BRAKE CONTROL SYSTEMS OR PARTS THEREOF, IN GENERAL; ARRANGEMENT OF BRAKING ELEMENTS ON VEHICLES IN GENERAL; PORTABLE DEVICES FOR PREVENTING UNWANTED MOVEMENT OF VEHICLES; VEHICLE MODIFICATIONS TO FACILITATE COOLING OF BRAKES
    • B60T17/00Component parts, details, or accessories of power brake systems not covered by groups B60T8/00, B60T13/00 or B60T15/00, or presenting other characteristic features
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60TVEHICLE BRAKE CONTROL SYSTEMS OR PARTS THEREOF; BRAKE CONTROL SYSTEMS OR PARTS THEREOF, IN GENERAL; ARRANGEMENT OF BRAKING ELEMENTS ON VEHICLES IN GENERAL; PORTABLE DEVICES FOR PREVENTING UNWANTED MOVEMENT OF VEHICLES; VEHICLE MODIFICATIONS TO FACILITATE COOLING OF BRAKES
    • B60T17/00Component parts, details, or accessories of power brake systems not covered by groups B60T8/00, B60T13/00 or B60T15/00, or presenting other characteristic features
    • B60T17/02Arrangements of pumps or compressors, or control devices therefor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B41/00Pumping installations or systems specially adapted for elastic fluids
    • F04B41/02Pumping installations or systems specially adapted for elastic fluids having reservoirs

Definitions

  • Air supply system control method of air supply system, and control program of air supply system
  • the present disclosure relates to an air supply system, an air supply system control method, and an air supply system control program.
  • pneumatic systems including a braking system and a suspension system are controlled by using compressed air sent from a compressor.
  • This compressed air contains liquid impurities such as moisture contained in the atmosphere and oil that lubricates the inside of the compressor. If compressed air that contains a large amount of water and oil enters the pneumatic system, it may lead to malfunction and malfunction of the rubber member. For this reason, a compressed air dryer is installed downstream of the compressor to remove impurities such as water and oil in the compressed air.
  • the compressed air drying device includes a filter containing a desiccant and various valves.
  • the compressed air drying device performs a dehumidifying operation of passing compressed air through a filter to remove moisture and the like from the compressed air.
  • the compressed dry air generated by the dehumidifying operation is stored in the air tank.
  • the cleaning function of the compressed air dryer decreases with the amount of compressed dry air supplied. Therefore, the compressed air drying device removes the oil and water adsorbed in the filter from the filter, and performs the regenerating operation of discharging the removed oil and water as drain (for example, see Patent Document 1).
  • Prior art documents for example, see Patent Document 1.
  • Patent Document 1 Japanese Unexamined Patent Publication No. 2 0 1 0 _ 2 0 1 3 2 3
  • Execution conditions such as the time for executing the regeneration operation, the amount of regeneration air to be passed through the filter, etc. are set to be constant, or are determined according to the amount of compressed air sent from the compressor. Has been done. However, it has been found by the inventors that in either case, excess or deficiency occurs. If the regeneration time or the amount of regenerated air is insufficient, the moisture trapping ability of the desiccant may not return to its original level, and the amount of moisture contained in the air sent from the compressed air drying device may increase. On the other hand, if the regeneration time or the amount of regenerated air becomes excessive, the compressed dry air in the air tank, which originally supplies the pneumatic system, is wastefully consumed. Compressed dry air is generated by a compressor driven by a rotary drive source such as an engine, so excessive consumption of compressed dry air increases the load on the rotary drive source and reduces fuel consumption of the vehicle.
  • An object of the present disclosure is to reduce the amount of compressed dry air consumed by the air supply system while maintaining the dehumidification performance of the air supply system.
  • An air supply system that solves the above problems is provided between a compressor that delivers compressed air and a storage unit that stores compressed dry air, and has an air drying circuit that has a filter that traps moisture.
  • a control device for controlling the air drying circuit the control device performing a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in the forward direction to be supplied to the storage section.
  • the air drying circuit is controlled so that the compressed dry air stored in the storage section is passed through the filter in the reverse direction, and the fluid that has passed through the filter is discharged from the discharge port.
  • the air drying circuit is controlled so that the amount of regenerated air consumed in one regenerating operation is set according to the operating state of the compressor.
  • An air supply system control method that solves the above-mentioned problem is provided with a filter that captures water, which is provided between a compressor that delivers compressed air and a reservoir that stores compressed dry air. Circuit and control the air drying circuit ⁇ 2020/175 470 3 ⁇ (:171? 2020 /007469
  • a control method of an air supply system comprising: a control device for performing a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in a forward direction to be supplied to the storage section.
  • the air drying circuit is controlled so that the compressed dry air stored in the storage section is passed through the filter in the reverse direction, and the fluid that has passed through the filter is discharged from the discharge port.
  • the air drying circuit is controlled to set the amount of regeneration air consumed in one regeneration operation according to the operating state of the compressor.
  • a control program for an air supply system that solves the above-mentioned problems is provided between a compressor that delivers compressed air and a storage section that stores compressed dry air, and has a filter that captures moisture.
  • a control program for an air supply system comprising a drying circuit and a control device for controlling the air drying circuit, the control device causing the compressed air sent from the compressor to pass through the filter in a forward direction.
  • a dehumidifying operation executing unit that controls the air drying circuit to execute a dehumidifying operation to be supplied to the storage unit, and allows the compressed dry air stored in the storage unit to pass through the filter in the reverse direction and through the filter.
  • a regeneration operation execution unit that controls the air drying circuit to perform a regeneration operation that discharges the fluid from the discharge port, and a regeneration air that is consumed by one regeneration operation according to the operating state of the compressor. Function as a setting unit, which sets the amount
  • the control device sets the amount of regeneration air consumed in the regeneration operation based on the operating state of the compressor.
  • the compressor is driven according to the supply condition of compressed dry air to devices other than the air drying circuit.Therefore, by changing the amount of regenerated air, it is possible to supply compressed dry air from the storage unit to devices other than the air drying circuit. Either cleaning of the filter can be prioritized.
  • the control device reduces the regeneration air amount when the operation rate of the compressor is high within a certain period, and when the operation rate of the compressor is low, It may be configured to increase the regeneration air amount. ⁇ 2020/175 470 (:171? 2020 /007469
  • the controller increases the amount of regenerated air when the index indicating the wet state of the compressed dry air in the storage section is high, When the index indicating the wet state is low, the amount of regenerated air may be reduced.
  • the control device sets a high upper limit pressure for starting the regeneration operation, which is the pressure of the storage section when the operation rate of the compressor is high, When the operating rate is low, the upper limit pressure is set low, when the upper limit pressure is high, the regeneration air amount is reduced, and when the upper limit pressure is low, the regeneration air amount is increased. May be done
  • the upper limit pressure for starting the regeneration operation is set according to the operating state of the compressor. Also, the amount of regenerated air is determined according to the upper limit pressure.
  • the operating rate of the compressor is high, the upper limit pressure is set high and the amount of regenerated air is reduced, so that the frequency of regenerating operations is reduced and the consumption of compressed dry air stored in the storage section is suppressed, thereby reducing air drying.
  • the supply of compressed dry air to equipment other than the circuit can be prioritized.
  • the operating rate of the combreza is low. ⁇ 2020/175 470 5 ⁇ (:171? 2020 /007469
  • the upper limit pressure is set low and the amount of regeneration air is increased, so that it is possible to increase the frequency of regeneration operations and enhance the effect of purifying the filter.
  • An air supply system that solves the above problems is provided between a compressor that delivers compressed air and a storage unit that stores compressed dry air, and has an air drying circuit that has a filter that traps moisture.
  • a control device for controlling the air drying circuit the control device performing a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in the forward direction to be supplied to the storage section.
  • the air drying circuit is controlled so that the compressed dry air stored in the storage section is passed through the filter in the reverse direction, and the fluid that has passed through the filter is discharged from the discharge port.
  • the air drying circuit is controlled so that the amount of regenerated air consumed in one regenerating operation is set according to the temperature of the compressed air or the compressed dried air.
  • An air supply system control method that solves the above-mentioned problem is provided with a filter that traps water, which is provided between a compressor that delivers compressed air and a reservoir that stores compressed dry air.
  • a control method for an air supply system comprising a circuit and a control device for controlling the air drying circuit, wherein the control device allows the compressed air sent from the compressor to pass through the filter in a forward direction to store the compressed air.
  • the air drying circuit is controlled so as to execute a dehumidifying operation for supplying the compressed dry air stored in the storage section to the filter in the reverse direction, and the fluid passing through the filter is discharged from the outlet.
  • the air drying circuit is controlled so as to execute the discharging operation for discharging, and the amount of the reproducing air consumed by one time of the reproducing operation is set according to the temperature of the compressed air or the temperature of the compressed dry air.
  • An air supply system control program that solves the above-mentioned problems is provided between a compressor for delivering compressed air and a reservoir for storing compressed dry air, and has a filter for trapping moisture.
  • a control program for an air supply system comprising a drying circuit and a control device for controlling the air drying circuit, wherein the control device controls the compressed air sent from the compressor. ⁇ 2020/175 470 6 ⁇ (:171? 2020 /007469
  • Dehumidifying operation execution unit that controls the air drying circuit so as to perform a dehumidifying operation that allows the air to pass through the filter in the forward direction and supplies the dehumidifying operation to the storage unit; And a temperature of the compressed dry air or a temperature of the compressed dry air that controls the air drying circuit to perform a regeneration operation of discharging the fluid that has passed through the filter and is discharged from the outlet.
  • it functions as a setting unit that sets the amount of regeneration air consumed in one regeneration operation.
  • the control device sets the amount of regenerated air consumed in the regenerating operation according to the temperature of the compressed air or the temperature of the compressed dry air.
  • the amount of water contained in the air also increases.Therefore, by changing the amount of regenerated air according to the amount of water contained in the air, Either supply of compressed dry air to equipment other than the air drying circuit or cleaning of the filter can be prioritized.
  • control device is configured to reduce the amount of regenerated air when the temperature is low, and increase the amount of regenerated air when the temperature is high. Good.
  • FIG. 1 is a configuration diagram showing a schematic configuration of a first embodiment of an air supply system.
  • Figs. 28 to 2 are views showing first to sixth operation modes of the air drying circuit of the embodiment of Fig. 1, respectively. ⁇ 2020/175 470 7 ⁇ (: 171? 2020 /007469
  • FIG. 3A is a map of a standard regenerated air amount for calculating the regenerated air amount of the embodiment of FIG. 1, and FIG. 3 is a correction for calculating the regenerated air amount of the embodiment of FIG. Map of unit air volume.
  • FIG. 4 is a schematic diagram of excess/deficiency coefficient information of the embodiment of FIG.
  • FIG. 5 A flow chart showing an example of a procedure for supplying compressed air in the embodiment of FIG. 1.
  • FIG. 6 A flow chart showing an example of a procedure for performing a reproducing operation in the embodiment of FIG. 1.
  • FIG. 7 is a flow chart showing an example of a procedure for determining the regeneration air amount in the embodiment of FIG.
  • FIG. 8A is a map of the standard regenerated air amount for calculating the regenerated air amount of the second embodiment
  • FIG. 8 is a correction unit air for calculating the regenerated air amount of the second embodiment. Quantity map.
  • FIG. 9 is a flow chart showing an example of a procedure for determining the regeneration air amount in the embodiment of FIG.
  • the air supply system is installed in automobiles such as trucks, buses, and construction machines.
  • the compressed dry air generated by the air supply system is used in a pneumatic system such as a brake system (braking device) or a suspension system (suspension device) of an automobile.
  • the air supply system 10 will be described with reference to FIG.
  • the air supply system 10 is provided with a compressor 4, an air drying circuit 11 and an ECU (Electronic Control Unit) 80.
  • the ECU 80 functions as a control device, a dehumidification operation execution unit, a regeneration operation execution unit, and a setting unit. [0027]
  • the ECU 80 is connected to the air drying circuit 11 via a plurality of wirings E61 to E67. ⁇ 2020/175 470 8 ⁇ (:171? 2020 /007469
  • the ECU 80 includes a calculation unit, a communication interface unit, a volatile storage unit, and a non-volatile storage unit.
  • the arithmetic unit is a computer processor and is configured to control the air drying circuit 11 according to an air supply program stored in a non-volatile storage unit (storage medium).
  • the arithmetic unit may realize at least a part of the processing executed by itself by a circuit such as AS IC.
  • the air supply program may be executed by one computer processor or may be executed by a plurality of computer processors.
  • the ECU 80 includes a storage unit 80A that stores information for determining the execution frequency of each operation of the air drying circuit 11.
  • the storage unit 80A is a non-volatile storage unit or a volatile storage unit, and may be the same as or different from the storage unit in which the control program is stored.
  • the ECU 80 is connected to other ECUs (not shown) mounted on the vehicle, such as an engine ECU and a brake ECU, via an in-vehicle network such as CAN (Controller Area Network). Has been done.
  • the ECU 80 acquires information indicating the vehicle state from those ECUs.
  • the information indicating the vehicle state includes, for example, ignition switch OFF information, vehicle speed, engine drive information, and the like.
  • the state of the compressor 4 is based on a command from the ECU 80 between an operating state in which air is compressed and sent (load operation) and a non-operating state in which air is not compressed (idle operation). Can be switched.
  • the compressor 4 operates by the power transmitted from a rotary drive source such as an engine.
  • the air drying circuit 11 is a so-called air dryer.
  • the air drying circuit 11 is connected to the ECU 80, and removes moisture and the like contained in the compressed air sent from the compressor 4 during load operation.
  • the air drying circuit 11 supplies the dried compressed air (hereinafter, compressed dry air) to the supply circuit 12.
  • the compressed dry air supplied to the supply circuit 12 is stored in the air tank 30.
  • the air drying circuit 11 has a maintenance port 12.
  • the maintenance port 12 is a port for supplying air to the air drying circuit 11 through it during maintenance.
  • the air drying circuit 11 has a filter 1 inside the case 1 18 (see Fig. 28).
  • the filter 17 is provided in the middle of the air supply passage 18 which connects the compressor 4 and the supply circuit 12.
  • Filter 17 contains a desiccant.
  • the filter 17 also includes an oil trap portion that traps oil.
  • the oil capturing part may be a foam such as urethane foam, a metal material having a large number of ventilation holes, a glass fiber filter, or the like as long as it can capture the oil while allowing air to pass therethrough.
  • the filter 17 removes the water contained in the compressed air from the compressed air to dry the compressed air by passing the compressed air sent from the compressor 4 through the desiccant. Further, the oil trap portion traps oil contained in the compressed air to purify the compressed air.
  • the compressed air that has passed through the filter 17 is supplied to the supply circuit 12 via the downstream check valve 19.
  • the downstream check valve 19 allows only air flow from upstream to downstream when the filter 17 side is upstream and the supply circuit 12 side is downstream. Since the downstream check valve 19 has a predetermined valve opening pressure (sealing pressure), the upstream pressure becomes higher than the downstream pressure by the valve opening pressure when compressed air flows.
  • bypass passage 20 as a bypass for bypassing the downstream check valve 19 is provided downstream of the filter 17 in parallel with the downstream check valve 19.
  • a regeneration control valve 21 is provided in the bypass passage 20.
  • the regeneration control valve 21 is a solenoid valve controlled by the valve 311800. ⁇ 2020/175 470 10 ⁇ (:171? 2020 /007469
  • the MII II 80 controls the regeneration control valve 2 1 power on/off (driving/non-driving) via the wiring date 6 4 to switch the regeneration control valve 2 1 operation.
  • the regeneration control valve 21 is closed when the power is off to seal the bypass passage 20 and opened when the power is on to communicate the bypass passage 20.
  • the MII II 80 receives the value of the air pressure in the air tank 30 and operates the regeneration control valve 21 when the value of the air pressure exceeds a predetermined range.
  • An orifice 22 is provided in the bypass passage 20 between the regeneration control valve 21 and the filter 17.
  • the regeneration control valve 21 When the regeneration control valve 21 is energized, the compressed dry air on the side of the supply circuit 12 is sent to the filter 17 through the bypass passage 20 while the flow rate is regulated by the orifice 22.
  • the compressed dry air sent to the filter 17 flows backward through the filter 17 from the downstream side to the upstream side, and passes through the filter 17.
  • Such processing is an operation of regenerating the filter 17 and is called a regenerating operation of the air drying circuit 11.
  • the compressed dry air sent to the filter 17 is the dried and purified air supplied to the supply circuit 12 from the air supply passage 18 through the filter 17 etc.
  • the water and oil trapped in 7 can be removed from the filter 17.
  • the No. 1 1 180 opens the regeneration control valve 21 when the pressure in the air tank 30 reaches the upper limit value (cutout pressure). On the other hand, when the pressure in the air tank 30 reaches the lower limit (cut-in pressure), the opened regeneration control valve
  • a branch passage 16 is branched from a portion between the combiner 4 and the filter 17.
  • a drain discharge valve 25 is provided in the branch passage 16 and a drain discharge port 27 is connected to the end of the branch passage 16.
  • the drain which is a fluid containing water and oil removed from the filter 17 is sent to the drain discharge valve 25 together with compressed air.
  • the drain discharge valve 25 is a pneumatically driven valve driven by air pressure, and is provided in the branch passage 16 between the filter 17 and the drain discharge port 27.
  • the drain discharge valve 25 is a 2-port 2-position valve that changes its position between a closed position and an open position. ⁇ 2020/175 470 1 1 ⁇ (:171? 2020 /007469
  • drain discharge valve 25 When the drain discharge valve 25 is in the open position, the drain is sent to the drain discharge port 27.
  • the drain discharged from the drain outlet 27 may be collected by an oil separator (not shown).
  • the drain corresponds to the fluid passing through the filter 17 in the opposite direction.
  • the drain discharge valve 25 is controlled by the governor 2 68.
  • the II II 80 switches the operation of the governor 2 68 by controlling the turning on/off (drive/non-drive) of the governor 2 68 via the wiring 6 3.
  • the governor 268 switches to the input position where the pneumatic signal is input to the drain discharge valve 25, thereby opening the drain discharge valve 25.
  • the governor 26 8 switches the drain discharge valve 25 port to the open position where the drain discharge valve 25 port is opened to atmospheric pressure without inputting an air pressure signal to the drain discharge valve 25. Close valve 2 5.
  • the drain discharge valve 25 is maintained in the closed position where the branch passage 16 is shut off in the state where the air pressure signal is not input from the governor 26, and the air pressure signal is input from the governor 26. And the valve is opened to connect the branch passage 16 with each other.
  • the drain discharge valve 25 is forcibly switched to the open position.
  • An upstream check valve 15 is provided between the compressor 4 and the filter 17 and between the compressor 4 and the branch passage 16.
  • the upstream check valve 15 allows only the air flow from upstream to downstream when the compressor 4 side is upstream and the filter 17 side is downstream. Since the upstream check valve 15 has a predetermined valve opening pressure (sealing pressure), when the compressed air flows, the upstream pressure becomes higher than the downstream pressure by the valve opening pressure.
  • a reed valve at the outlet of the compressor 4 is provided upstream of the upstream check valve 15.
  • a branch passage 16 and a filter 17 are provided downstream of the upstream check valve 15. ⁇ 2020/175 470 12 boxes (:171? 2020 /007469
  • the combiner 4 is controlled by the unload control valve 26.
  • the unload control valve 26 is a solenoid valve controlled by ⁇ 118.
  • the ⁇ ⁇ ⁇ 1 800 switches off the operation of the unload control valve 2 ⁇ 6 by controlling the power on/off (drive/non-drive) of the unload control valve 2 6 ⁇ via the wiring switch 6 2. Change.
  • the unload control valve 2 6 switches to the open position, and opens the flow path between the unload control valve 2 6 and the compressor 4 to the atmosphere. Further, when the power is turned on, the unload control valve 26 switches to the supply position and sends an air pressure signal consisting of compressed air to the compressor 4.
  • the state of the compressor 4 is switched to a non-operation state (idle operation) when an air pressure signal is input from the unload control valve 26. For example, when the pressure in the air tank 30 reaches the cutout pressure, it is not necessary to supply compressed dry air. When the pressure on the supply circuit 1 2 side reaches the cutout pressure and the power is turned on (3 11 800 turns on the unload control valve 26 6 (drives the unload control valve 2 6)), the unload control is performed. Valve 26 is switched to the supply position, which causes the pneumatic control valve 26 to supply the pneumatic signal to the compressor 4 and switch the state of the compressor 4 to the non-operational state.
  • a pressure sensor 50 is provided between the compressor 4 and the upstream check valve 15.
  • the pressure sensor 50 is connected to the air supply passage 18 and measures the air pressure in the air supply passage 18 and transmits the measurement result to the wire II II 80 via the wiring wire 6 1. To do.
  • a humidity sensor 51 and a temperature sensor 52 are provided between the downstream check valve 19 and the supply circuit 12.
  • the humidity sensor 51 may detect absolute humidity or may detect relative humidity.
  • the humidity sensor 51 and the temperature sensor 52 measure the humidity of the compressed air downstream of the filter 17 and the temperature of the compressed air, respectively, and the measurement results are sent via wiring days 6 5 and 6 6 respectively. Output to 80.
  • MII II 80 determines the wet state of compressed dry air based on the humidity and temperature input from humidity sensor 51 and temperature sensor 52. ⁇ 2020/175 470 13 ⁇ (:171? 2020 /007469
  • a pressure sensor 5 is provided between the downstream check valve 19 and the supply circuit 12.
  • the pressure sensor 53 is provided so as to detect the air pressure in the air tank 30 and outputs the detected pressure value to the ECU 80 via the wiring E67.
  • the pressure between the downstream check valve 19 and the supply circuit 12 is the same as the pressure in the air tank 30.
  • the detection result of the pressure sensor 53 can be used as the pressure in the air tank 30.
  • the pressure sensor 53 may be provided in the supply circuit 12 or the air tank 30.
  • the air drying circuit 11 has a plurality of operation modes including at least a first operation mode to a sixth operation mode.
  • the first operation mode is a mode for performing a normal dehumidifying operation (mouth operation).
  • the regeneration control valve 21 and the unload control valve 26B are each closed (indicated as “CLOSE” in the figure), the governor 26A is opened, and no air pressure signal is input to the compressor 4. Position (marked as “CLOSE” in the figure).
  • power is not supplied to the regeneration control valve 21, the governor 26 A, and the unload control valve 26 A.
  • the governor 26 A and the unload control valve 26 6 open the port of the compressor 4 and the port of the drain discharge valve 25, which are connected downstream of them, to the atmosphere, respectively.
  • the filter 17 removes water and other components, and compressed air is supplied to the supply circuit 12 2. ..
  • the second operation mode is a mode in which the compressed dry air in the air drying circuit 11 is passed through the filter 17 to perform the purging operation to purify the filter 17.
  • the regeneration control valve 21 is closed, the unload control valve 26 B is in the supply position (marked as "OPEN” in the figure), and the governor 26 A is in the input position ("OPEN” in the figure). And)).
  • the drain discharge valve 25 is opened.
  • the compressed dry air between the downstream check valve 19 and the filter 17 flows in the filter 17 in the direction opposite to the air flow in the first operation mode (dehumidification mode) (backflow), Moisture and the like captured by the filter 17 is discharged as drain from the drain outlet 27.
  • the air pressure in the filter 17 and the air supply passage 18 is released to atmospheric pressure.
  • the third operation mode is a mode for performing the reproduction operation for reproducing the filter 17.
  • the regeneration control valve 21 is opened, the governor 26 is set as the input position, and the unload control valve 26 is set as the supply position (indicated as " ⁇ " in each figure). ).
  • power is supplied to the regeneration control valve 2 1 in addition to the governor 26 8 and the inlet control valve 26 6.
  • the compressor 4 is deactivated and the compressed dry air stored in the supply circuit 12 or the air tank 30 is caused to flow back to the filter 17 and is discharged from the drain outlet 27. Let As a result, the water and the like captured by the filter 17 are removed.
  • the second operation mode and the third operation mode are both modes for purifying the filter 17, but the third operation mode is different from the second operation mode in that the regeneration control valve 21 is opened at least. different.
  • the third operation mode the compressed dry air in the air tank 30 can be passed through the supply circuit 12 and the bypass passage 20 to the filter 17. Therefore, the effect of cleaning the filter 17 is higher than that of the second operation mode. Also in the third operation mode, the air pressure in the filter 17 and the air supply passage 18 is released to the atmospheric pressure.
  • the fourth operation mode is the oil cut operation mode. ⁇ 2020/175 470 15 ⁇ (:171? 2020/007469
  • the excess oil air sent from the compressor 4 is discharged from the drain outlet 27 without passing through the filter 17.
  • oil may accumulate in the compression chamber of the compressor 4.
  • the state of the compressor 4 is switched to the operating state while the oil is accumulated in the compression chamber, the amount of oil contained in the compressed air sent from the compression chamber increases.
  • the dehumidification performance of the desiccant decreases. Therefore, the oil cut operation is performed to discharge the compressed air that contains too much oil.
  • the regeneration control valve 21 is closed, the unload control valve 26B is in the open position (denoted as “CLOSE” in the figure), and the governor 26A is opened after a certain period of operation. Position (marked as “CLOSE” in the figure).
  • the fifth operation mode is a mode in which the compressor stops without purging.
  • the regeneration control valve 21 is closed, the governor 26A is in the open position (indicated as “CLOSE” in the figure), and the unload control valve 26B is in the supply position (see the figure). "OPEN").
  • the compressed air or the compressed dry air remaining in the desiccant in the air supply passage 18 or the filter 17 should not be discharged from the drain outlet 27. The air pressure is maintained at.
  • the sixth operation mode is the assist operation for pressurization processing. ⁇ 2020/175 470 16 ⁇ (:171? 2020/007469
  • the regeneration control valve 21 is opened, the inlet control valve 26 B is set to the supply position (indicated as “OPEN” in the figure), and the governor 26 A is set to the open position (in the figure, CLOS E”).
  • the compressor 4 when the compressor 4 is in the non-operational state, the compressed air in the supply circuit 12 is supplied (backflowed) into the desiccant in the air supply passage 18 and the filter 17 to generate air.
  • the pressure in the supply passage 18 and the filter 17 is made higher than the atmospheric pressure to maintain the back pressure (air pressure) of the upstream check valve 15 at a pressure higher than the atmospheric pressure.
  • the ECU 80 executes the control program to calculate the regeneration air amount Am according to the following equation (1).
  • the amount of regenerated air Am may be calculated in volume units or mass units. Note that various coefficients for converting the unit may be used for the right side (or the left side) of this equation (1).
  • Standard regeneration air volume Am 1 correction unit air volume A m2 X excess/deficiency coefficient a (1) Note that “standard regeneration air volume A m 1” is calculated from “correction unit air volume A m 2 X excess/deficiency coefficient a”. Is also set to be large, and the amount of regenerated air Am exceeds “0”.
  • the standard regeneration air volume Am 1 is basically the air volume determined by the specifications of the air drying circuit 11 but is changed according to the cutout pressure which is the upper limit of the pressure of the air tank 30. As described above, the cutout pressure is the pressure that is the condition for starting the regeneration operation and the purge operation, and the higher the operating rate of the compressor 4, the higher the value is set and stored in the storage unit 80A.
  • the cutout pressure P ⁇ 1 that is a relatively low value is set, and the operating rate is the specified value R 1 or more and the specified value R 2 (for example, 60%. )
  • a cutout pressure P ⁇ 2 higher than the cutout pressure P o 1 is set (P ⁇ 2>P ⁇ 1).
  • the cutout pressure is higher than the cutout pressure, and the cutout pressure is set to 0 (3).
  • the cutout pressure is set in three stages according to the operating rate of the compressor 4, but it may be set in two stages or in four or more stages. Good. Alternatively, the cutout pressure may be continuously changed according to the operating rate of the compressor 4.
  • the cutout pressure ⁇ is increased as the operating rate of the compresser 4 is increased. Since the compressor 4 is driven according to the amount of compressed dry air in the air tank 30 and the like, when the operating rate is low, the compressed dry air consumption by the pneumatic system such as the brake system is relatively low. It is estimated that the situation is under. In such a situation, the cutout pressure is set to a relatively low value, the frequency of regenerating operation is set to be relatively high, and the filter 17 is actively cleaned. On the other hand, when the operating rate of the Compressor 4 is high, it is estimated that the compressed dry air consumption by the pneumatic system such as the brake system is relatively high. In such a situation, the cutout pressure is set to a relatively high value, the frequency of regeneration operation is performed relatively low, and the supply of compressed dry air to the pneumatic system is prioritized.
  • Fig. 38 shows a map 100 in which the standard regeneration air amount 80! 1 is set according to the limit ventilation amount and the cutout pressure.
  • This map 100 is stored in the storage unit 808.
  • the horizontal axis of the map 100 is the limit air flow rate, and the vertical axis is the standard regeneration air volume 81 01.
  • the unit is volume (liter), but the unit may be mass.
  • the limit air flow rate is a value that indicates the limit of the amount of air that passes through the air drying circuit 11 and is determined according to the specifications of the air drying circuit 11 (air dryer).
  • the standard regeneration air volume 80!1 decreases as the critical air flow rate increases, and increases as the critical air flow rate decreases.
  • the standard regeneration air volume 80!1 becomes smaller as the cutout pressure becomes higher, and becomes larger as the cutout pressure becomes lower, when the limit air flow rate is constant.
  • the cutout pressure is set to a high value as the operating rate of the Compressor 4 increases.
  • the standard regeneration air volume of 81 1 decreases as the operating rate of the Combressa 4 increases.
  • the operating rate of the compressor 4 when the operating rate of the compressor 4 is high, it is estimated that the compressed dry air consumption by the pneumatic system such as the brake system is relatively high. For this reason, when the operating rate of the compressor 4 is high, it is prioritized to reduce the standard regeneration air volume 81 and supply compressed dry air to the pneumatic system.
  • the standard regeneration air volume 1 increases as the operating rate of the compressor 4 decreases. If the operating rate is low, it is estimated that the compressed dry air consumption by the pneumatic system such as the brake system is relatively small. Therefore, when the operating rate of the compressor 4 is low, the standard regeneration air volume 0! 1 is increased to enhance the cleaning effect of the filter 17 per regeneration operation.
  • Fig. 3 is a map 101 showing the relationship between the corrected unit air amount 82 depending on the cutout pressure and the limit ventilation amount.
  • This map 1 0 1 is stored in the storage unit 8 0 8.
  • the horizontal axis is the limit air flow rate, and the vertical axis is the correction unit air volume 2.
  • the unit is volume in the figure, the unit may be mass.
  • the corrected unit air volume 0!2 becomes smaller as the limit air flow rate becomes larger like the standard regeneration air volume 0!1, but becomes larger as the cutout pressure becomes higher when the limit air volume is constant. , It becomes smaller as the cutout pressure becomes lower.
  • the excess/deficiency coefficient ⁇ (regeneration excess/deficiency coefficient) is the correction unit air amount. Is a coefficient that is multiplied by and is set to a negative value, a positive value or "0". This excess/deficiency coefficient is set based on the tendency of the compressed dry air stored in the air tank 30 to be in a wet state.
  • the excess or deficiency of the regeneration operation can be determined by the amount of water captured by the filter 17, but the amount of water contained in the compressed air changes depending on the temperature and humidity of the air, so the amount of water captured by the filter 17 can be determined. It is difficult to estimate the amount using only the execution time of the regeneration operation and the amount of air that has passed through the filter 17. It is also difficult to directly measure the amount of water captured by the filter 17. As in this embodiment, ⁇ 2020/175 470 19 ⁇ (:171? 2020/007469
  • the excess or deficiency of the regeneration operation can be appropriately determined indirectly.
  • the tendency of the wet state which is the basis of the excess/deficiency coefficient ⁇ , is determined for the period from the previous reproduction operation to the next reproduction operation.
  • the index for determining the wet state is not limited, but in the present embodiment, the saturation degree of the water content (hereinafter, the water content) contained in the compressed dry air in the air tank 30 is calculated, and the previous regeneration is performed. Subtract the saturation of the moisture content this time from the saturation of the moisture content at the end of the operation. If the saturated moisture content is higher at the end of this regeneration than at the end of the previous regeneration, that is, if the wet state of compressed dry air tends to increase, the filter 17 captures it. It is judged that the water content is increasing. Therefore, in equation (1) above, the excess/deficiency coefficient ⁇ is a negative value that is not "0". When the excess/deficiency coefficient ⁇ is a negative value, the regeneration air amount is corrected to be larger than the standard regeneration air amount.
  • the filter 1 It is judged that the amount of water captured by 7 tends to decrease. Therefore, the excess/deficiency coefficient ⁇ is set to a positive value larger than "0", and the regenerated air amount is corrected to be smaller than the standard regenerated air amount. When it is determined that the compressed dry air is in a suitable wet state, the excess/deficiency coefficient is set to “ ⁇ ” and the regenerated air amount 01 is not corrected from the standard regenerated air amount 01 1.
  • FIG. 4 is excess/deficiency coefficient information 200 showing an example of excess/deficiency coefficient ⁇ .
  • the excess/deficiency coefficient information 200 is stored in the storage unit 80.
  • the excess/deficiency coefficient information 200 includes the excess/deficiency condition 200, and the excess/deficiency coefficient 200(3. State 2 00 0 indicates the state indicated by the excess/deficiency condition 2 0 0 for convenience.
  • the range of regeneration excess/deficiency is set in the excess/deficiency condition 200.
  • the regeneration excess/deficiency indicates the amount of water contained in the compressed dry air in the air tank 30. It is an index that indicates whether the degree of saturation is increasing or decreasing.
  • the excess/deficiency coefficient 200 (3 is the reproduction excess/deficiency multiplied by the weighting coefficient. ⁇ 2020/175 470 20 ⁇ (:171? 2020 /007469
  • the excess/deficiency coefficient 103 corresponds to the excess/deficiency condition 208, which is the range of the reproduction excess/deficiency.
  • the weighting coefficient is a positive integer in FIG. 4, it does not have to be a positive integer.
  • the regeneration excess/deficiency degree is, for example, "_ 1" or less, which is a negative value. It is a value and its absolute value is large. In this case, the weighting coefficient is also set to a relatively large value such as “2”. In addition, if the amount of regeneration air is insufficient, even if it cannot be said to be “significantly insufficient,” the regeneration insufficient degree is, for example, greater than “_ 1” and less than “_ 0.5”. However, the absolute value is smaller than the "significant lack”. Also, the value of the weighting coefficient is set to a value smaller than "significantly insufficient” such as "1".
  • the regeneration excess/deficiency degree is, for example, "1" or more, and the positive value and absolute value are large.
  • the weighting coefficient is also set to a relatively large value such as “2”.
  • the regeneration excess/deficiency is, for example, “0.5” or more, which is less than “1”.
  • the absolute value is smaller than that of "significant excess”.
  • the value of the weighting coefficient is set to a value smaller than "significantly insufficient" such as "1".
  • the excess/deficiency coefficient is set to "0".
  • the wet state in the air tank 30 is shown when the operating rate of the compressor 4 is low and high. The explanation will be made separately for the case of low and the case of high. It is assumed that the limit ventilation is constant.
  • the regenerated air volume 1 increases as the cutout pressure is set low.
  • the correction unit air amount ⁇ !2 becomes smaller by setting the cutout pressure low. Further, the excess/deficiency coefficient ⁇ becomes a "significantly insufficient” or "insufficient” state, which is a negative value, because the wet state in the air tank 30 is high. Therefore, a positive correction value is added to the standard regeneration air volume, and the regeneration air volume 01 becomes large. In addition, the amount of regeneration air in the “largely shortage” state is larger than that in the “shortage” state.
  • the correction unit air amount 82 is increased by setting the cutout pressure high. Further, the excess/deficiency coefficient ⁇ becomes a "significantly insufficient” or "insufficient” state, which is a negative value, because the wet state in the air tank 30 is high. For this reason, a positive correction value is added to the standard regenerated air amount, but the regenerated air amount ⁇ ! becomes smaller than the regenerated air amount in state (). It should be noted that the regenerated air amount 01 in the state ( ⁇ ) may be smaller or larger than the regenerated air amount 01 in the state (Min). Also, the regenerated air amount 0 in the state (Min) and the state (The regeneration air volume in (3) 801 may be the same.
  • the standard regeneration air volume ⁇ ! 1 and the correction unit air volume 0 ⁇ 2 are the same as the above conditions ( ⁇ ).
  • the excess/deficiency coefficient ⁇ is because the wet state in the air tank 30 is low, "Or” Excess” and becomes a positive value. Therefore, the correction value is subtracted from the standard regenerated air amount, and the regenerated air amount becomes smaller than the regenerated air amount 0! in the state ( ⁇ 3).
  • the regenerated air volume 0! is the largest in the state () and the smallest in the state (mouth).
  • the MII II 80 performs the air supply process of supplying the compressed air output from the compressor 4 to the supply circuit 12 (step 31).
  • the air supply process is started under predetermined conditions such as when the engine is driven.
  • the air supply process may be started when the pressure in the air tank 30 reaches a predetermined pressure such as the cut-in pressure which is the lower limit value.
  • the air drying circuit 11 is in the first operation mode and is performing the dehumidifying operation.
  • the day (3 1 180) determines whether or not to stop the air supply (step 3 2).
  • the pressure in the air tank 30 detected by the sensor 5 3 is acquired and it is determined whether or not the pressure reaches the cutout pressure.MII ⁇ II 80 indicates that the pressure in the air tank 30 is the cutout pressure.
  • the process is returned to the air supply process (step 31).
  • Step 3 2 When it is judged that the pressure in the air tank 30 has reached the cutout pressure (Step 3 2 :Mimi 3), the II II 80 finishes the air supply process and puts the compressor 4 into the non-operational state. And perform the purification process (step 33).
  • the (311800 determines whether or not the regenerating operation and the purging operation are necessary according to the preset conditions. ⁇ 2020/175 470 23 ⁇ (:171? 2020 /007469
  • the process (31180 performs the air non-supplying process (step 34).
  • the upstream check valve is operated when the compressor 4 is in the non-operating state.
  • Adjust the pressure of the air drying circuit 11 such as adjusting the back pressure of 15.
  • at least one of the second operation mode, the fifth operation mode, and the sixth operation mode is set to 1 to Execute multiple times to adjust the air pressure in the air drying circuit 11.
  • o01 ⁇ 80 determines whether or not to stop the air supply based on the vehicle condition (step 35).
  • the end of the air supply is determined based on the vehicle state such as the engine stop of the vehicle.
  • step 31 If 0, the process is returned to step 31, and the following processes of the air supply process (step 31) are executed. On the other hand, when it is determined that the air supply is to be ended (step 35: No. 3), the air supply is stopped.
  • a value of 0 determines whether or not a reproducing operation is necessary according to a predetermined condition (step 3100).
  • Min 1180 determines whether or not the regenerating operation is necessary based on the wet state of the compressed dry air in the air tank 30. For example, the MII II 80 calculates the amount of water contained in the compressed dry air in the air tank 30 (the amount of water contained in the tank). If the water content in the tank is less than the predetermined value, it is determined that the regenerating operation is unnecessary.
  • Step 31 00: Mimi 3 the determined amount of regeneration air is acquired (Step 31 01). Switch the air drying circuit 1 1 to the 3rd operation mode by using the regenerated air volume and execute the regenerating operation. ⁇ 2020/175 470 24 ⁇ (: 171? 2020 /007469
  • Step 3 102 the change in the pressure value detected by the pressure sensor 53 is converted into the amount of air consumed in the regenerating operation, and even if the regenerating operation is terminated when the converted air amount reaches the regenerating air amount.
  • the regenerating operation may be performed by switching the air drying circuit 11 1 to the third operation mode for the regenerating time corresponding to the regenerated air amount.
  • the regeneration time is calculated using a map that associates the regeneration air amount with the regeneration time, or is calculated using a conversion formula assuming that the amount of air per unit time that passes through the filter 17 during regeneration is constant. You may do it.
  • the purification process step 33
  • the process proceeds to the next step.
  • day (3 1 180) is defined as one cycle from the end of the regenerating operation to the start of the next regenerating operation. Then, the regenerated air amount is updated at a predetermined timing in one cycle.
  • the update timing of the amount is not particularly limited, for example, the update of the regeneration air amount may be performed at the start of one cycle,
  • the M1 1 180 determines whether or not the regeneration air amount is updated (step 3 1
  • Minao II 80 determines whether or not the predetermined timing of the new cycle has been reached. If the MII II 80 determines that the predetermined timing has not been reached (step 311 0: N 0), it ends the process.
  • the regeneration excess/deficiency is calculated (step 3 1 1 1).
  • the regeneration excess/deficiency may be calculated based on the change in the tank air moisture saturation, as described above.
  • the tank air moisture saturation can be calculated from the humidity detected by the humidity sensor 51, the temperature detected by the temperature sensor 52, and the like.
  • Mitsumi (3 1 180 obtains the excess/deficiency factor by using the excess/deficiency factor information 2 0 0 after calculating the reproduction excess/deficiency (step 3 1 1 2).
  • 0 is ⁇ 2020/175 470 25 ⁇ (:171? 2020 /007469
  • Min. 1180 acquires the standard amount of regenerated air using map 100 (step 3 1 1 4) and the correction unit using map 1 0 1. Get the air volume (step 3 1 1 5). Then, MII II 80 calculates the amount of regenerated air according to the above equation (1) using the standard amount of regenerated air, the corrected unit air amount, and the excess/deficiency coefficient (steps 3 1 1 6). The regenerated air amount calculated here is used in step 3101 of FIG. The tan 80 performs a regeneration operation using the regeneration air amount calculated here.
  • MI (3 1 180 sets the amount of regenerated air consumed in the regenerating operation based on the operating state of the compressor 4.
  • the compressor 4 is compressed dry air to the pneumatic system other than the air drying circuit 1 1. It is driven according to the supply state of the air conditioner.Therefore, by changing the amount of regenerated air, it is possible to give priority to either the supply of compressed dry air from the air tank 30 to the other pneumatic systems or the cleaning of the filter 17. You can
  • the cleaning of the filter 17 can be prioritized by increasing the amount of regenerated air. Further, when the wet state of the compressed dry air is low, it is possible to give priority to the supply of the compressed dry air to the pneumatic system by suppressing the consumption of the compressed dry air stored in the air tank 30.
  • the cutout pressure which is the pressure, is set, and the amount of regenerated air is determined according to the cutout pressure.
  • the cutout pressure is set high and the amount of regenerated air is reduced, so that the frequency of regenerating operation is reduced and the consumption of compressed dry air stored in the air tank 30 is reduced. Can be suppressed and the supply of compressed dry air to the pneumatic system can be prioritized.
  • the cutout pressure is set low and the amount of regenerated air is increased.Therefore, the frequency of regenerating operation should be increased to enhance the effect of purifying the filter 17. You can
  • the second embodiment will be described with reference to FIGS. 8 and 9.
  • the second embodiment is similar to the first embodiment in that the standard regeneration air amount and the correction unit air amount are changed according to the state of the air drying circuit 11 to calculate the regeneration air amount. Further, in the first embodiment, the standard regeneration air amount and the correction unit air amount are changed according to the cutout pressure, but in the second embodiment, the standard regeneration air amount and the correction unit air amount are changed according to the temperature of the compressed dry air. It differs from the first embodiment in that the unit air amount is changed. Therefore, in the following, the configuration different from that of the first embodiment will be mainly described in detail, and the detailed description of the same configuration will be omitted for convenience of description.
  • FIG. 8 is a map 110 in which the standard regeneration air amount 1 is set according to the limit ventilation amount and the temperature, and is stored in the storage unit 808.
  • Map 110 determines the standard regeneration air amount according to the cutout pressure
  • map 110 (see FIG. 3) of the first embodiment determines the standard regeneration air amount according to the temperature.
  • the points that have been decided are different.
  • the temperature the value detected by the temperature sensor 52 can be used.
  • a temperature sensor may be provided on the inlet side of the air drying circuit 11 and upstream of the filter 17 and the temperature detected by the temperature sensor may be used.
  • the standard regeneration air volume 1 becomes smaller as the temperature becomes lower and becomes larger as the temperature becomes higher, when the limit ventilation volume is fixed.
  • the standard regeneration air amount 1 is increased to enhance the effect of removing moisture from the filter 17 in one regeneration operation.
  • the amount of saturated steam in the air saturated steam pressure
  • the amount of water contained in the compressed air tends to decrease. Therefore, it is assumed that the amount of water trapped in the filter 17 will also decrease. Reduce.
  • Fig. 8 is a map 11 1 in which the correction unit air amount ⁇ ! 2 is set according to the limit ventilation amount and the temperature, and is stored in the storage unit 808. Since the correction unit air volume 82 is a value subtracted from the standard regeneration air volume 1, as the standard regeneration air volume 8! At that time, it becomes smaller as the temperature rises and becomes larger as the temperature falls.
  • the process for determining the amount of regenerated air in the second embodiment is common to steps 311 10 to 3 1 1 2 and steps 3 1 1 4 to 3 1 1 6 of the process of the first embodiment. Detailed description is omitted.
  • Mino 1180 obtains the temperature of the compressed dry air detected by the temperature sensor 52 (step 3120). Then, M. 1 1 180 obtains the standard amount of regenerated air by using the obtained temperature and map 1 110 (step 3 1 1 1 4). In addition, MII II 80 uses the acquired temperature and map 1 1 1 1 to acquire the corrected unit air amount (step 3 1 1 5). Then, MII II 80 calculates the amount of regenerated air using the standard amount of regenerated air, the corrected unit air amount, and the excess/deficiency coefficient (steps 311 and 6).
  • MI (3 1 180 sets the amount of regeneration air consumed in regeneration operation according to the temperature of compressed air or the temperature of compressed dry air. The temperature of compressed air or the temperature of compressed dry air rises. Then, the amount of water contained in the air also increases, ⁇ 2020/175 470 28 ⁇ (:171? 2020 /007469
  • the regeneration air amount is determined according to the regeneration excess/deficiency, but the regeneration time may be determined according to the regeneration excess/deficiency.
  • the corrected playback time is calculated by multiplying the corrected unit time by the excess/deficiency coefficient, and the corrected playback time is added to the standard playback time.
  • the excess/deficiency coefficient ⁇ is calculated by multiplying the reproduction excess/deficiency degree by a weighting coefficient, but the reproduction excess/deficiency degree itself may be used as the excess/deficiency coefficient ⁇ . Even in this case, the amount of regenerated air can be increased or decreased depending on the excess or deficiency of regeneration.
  • the regeneration excess/deficiency is an index indicating whether the saturation of water contained in the compressed dry air in the air tank 30 has an increasing tendency or a decreasing tendency.
  • the humidity may be used as an index instead of the regeneration excess/deficiency.
  • the water content in the tank may be used as an index instead of the excess or deficiency of regeneration.
  • an average value over several cycles may be used. If the average value is a negative value, it is estimated that the amount of water in the air tank 30 has increased, so it is determined that the amount of regenerated air is insufficient.
  • the cutout pressure is set according to the operating rate of the compressor 4. ⁇ 2020/175 470 29 ⁇ (:171? 2020 /007469
  • the standard regeneration air amount and the correction unit air amount that constitute the regeneration air amount were set according to the cutout pressure.
  • the standard regeneration air amount and the correction unit air amount may be set using a map or the like in which the operating rate of the compressor 4 is associated with the standard regeneration air amount and the correction unit air amount.
  • the standard regeneration air amount and the correction unit air amount are set according to the temperature.
  • the standard regeneration air amount and the correction unit air amount may be set by using the temperature and the humidity.
  • the standard regeneration air amount and the correction unit air amount may be set by using only the humidity detected by the humidity sensor 51 or the like.
  • the excess/deficiency coefficient when the compressed dry air in the air tank 30 is in a high wet state, the excess/deficiency coefficient is set to a negative value to increase the amount of regenerated air, and the compressed dry air in the air tank 30 is in a wet state. When is low, the excess/deficiency coefficient is set to a positive value to reduce the amount of regenerated air. In addition to this mode, the amount of regenerated air may be changed by using the wet state of the compressed dry air sent from the combiner 4 or the wet state of the outside air.
  • the regeneration air amount may be determined based on the cutout pressure and the temperature of the compressed air or the compressed dry air.
  • a map in which cutout pressure, temperature, and standard regeneration air amount are associated with each other, a map in which cutout pressure, temperature, and correction unit air amount are associated with each other are used.
  • the standard regeneration air amount is corrected by the correction amount obtained by multiplying the correction unit air amount by the excess/deficiency coefficient to calculate the regeneration air amount, but the regeneration air amount is directly calculated from the map or the like. It may be calculated as follows.
  • the map may correspond to cutout pressure (or temperature), an index showing the wet state of compressed dry air, and the amount of regenerated air.
  • the filter 17 includes an oil trap
  • the oil trap may be omitted from 17.
  • the air drying circuit is not limited to the one having the above configuration.
  • the air drying circuit need only have a configuration capable of performing the dehumidifying operation and the regenerating operation. Therefore, the air drying circuit must have the second operation mode and the fourth to sixth operation modes. ⁇ 2020/175 470 30 boxes (: 171-1? 2020 /007469
  • the air supply system 10 has been described as being installed in a vehicle such as a truck, a bus, or a construction machine.
  • the air supply system 10 may be mounted on another moving body such as a passenger car, a railway vehicle, or the like.
  • the ECU 80 is not limited to the software processing for all the processing executed by itself.
  • the ECU 80 may include a dedicated hardware circuit (for example, an application specific integrated circuit: AS IC) that performs hardware processing for at least a part of the processing performed by the ECU 80.
  • AS IC application specific integrated circuit
  • the EC U 80 consists of 1) one or more processors that operate according to a computer program (software), 2) one or more dedicated hardware circuits that perform at least some of the various processes, or 3 ) A combination of them can be configured as a circuit including.
  • the processor includes a CPU and memories such as RAM and ROM, and the memory stores program code or instructions configured to cause the CPU to perform a process.
  • Memory or computer-readable media includes any available media that can be accessed by a general purpose or special purpose computer.

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Abstract

The present invention decreases the consumption of compressed dry air while maintaining excellent dehumidification performance. This air supply system (10) comprises: an air drying circuit (11) that is provided between a compressor (4) for sending compressed air and an air tank (30) for storing compressed dry air, and that comprises a filter (17) for capturing moisture; and an ECU (80) that controls the air drying circuit (11). The ECU (80): performs a dehumidification operation in which the air drying circuit (11) is controlled and the compressed air sent from the compressor (4) is passed through the filter (17) in the forward direction and supplied to the air tank (30); performs a regeneration operation in which the air drying circuit (11) is controlled and the compressed dry air stored in the air tank (30) is passed through the filter (17) in the reverse direction and the fluid that passes through the filter is discharged from a drain discharge port (27); and sets the amount of regeneration air consumed in the regeneration operation in response to the operating state of the compressor (4).

Description

\¥0 2020/175470 1 ?<:17 2020 /007469 明 細 書 \¥0 2020/175470 1 ?<:17 2020/007469 Clarification

発明の名称 : Title of invention:

空気供給システム、 空気供給システムの制御方法、 及び空気供給システム の制御プログラム Air supply system, control method of air supply system, and control program of air supply system

技術分野 Technical field

[0001 ] 本開示は、 空気供給システム、 空気供給システムの制御方法、 及び空気供 給システムの制御プログラムに関する。 The present disclosure relates to an air supply system, an air supply system control method, and an air supply system control program.

背景技術 Background technology

[0002] トラック、 バス、 建機等の車両においては、 コンブレッサから送られる圧 縮空気を利用して、 ブレーキシステム及びサスペンションシステム等を含む 、 空気圧システムが制御されている。 この圧縮空気には、 大気中に含まれる 水分及びコンプレッサ内を潤滑する油分等、 液状の不純物が含まれている。 水分及び油分を多く含む圧縮空気が空気圧システム内に入ると、 鲭の発生及 びゴム部材の膨潤等を招き、 作動不良の原因となる可能性がある。 このため 、 コンブレッサの下流には、 圧縮空気中の水分及び油分等の不純物を除去す る圧縮空気乾燥装置が設けられている。 [0002] In vehicles such as trucks, buses, and construction machines, pneumatic systems including a braking system and a suspension system are controlled by using compressed air sent from a compressor. This compressed air contains liquid impurities such as moisture contained in the atmosphere and oil that lubricates the inside of the compressor. If compressed air that contains a large amount of water and oil enters the pneumatic system, it may lead to malfunction and malfunction of the rubber member. For this reason, a compressed air dryer is installed downstream of the compressor to remove impurities such as water and oil in the compressed air.

[0003] 圧縮空気乾燥装置は、 乾燥剤を含むフィルタと各種バルブとを備えている 。 圧縮空気乾燥装置は、 圧縮空気をフィルタに通過させて圧縮空気から水分 等を除去する除湿動作を行う。 除湿動作によって生成された圧縮乾燥空気は 、 エアタンクに貯留される。 また、 圧縮空気乾燥装置の清浄機能は、 圧縮乾 燥空気の供給量に応じて低下する。 このため、 圧縮空気乾燥装置は、 フィル 夕に吸着された油分及び水分をフィルタから取り除き、 取り除いた油分及び 水分をドレンとして放出する再生動作を行う (例えば、 特許文献 1参照) 。 先行技術文献 The compressed air drying device includes a filter containing a desiccant and various valves. The compressed air drying device performs a dehumidifying operation of passing compressed air through a filter to remove moisture and the like from the compressed air. The compressed dry air generated by the dehumidifying operation is stored in the air tank. In addition, the cleaning function of the compressed air dryer decreases with the amount of compressed dry air supplied. Therefore, the compressed air drying device removes the oil and water adsorbed in the filter from the filter, and performs the regenerating operation of discharging the removed oil and water as drain (for example, see Patent Document 1). Prior art documents

特許文献 Patent literature

[0004] 特許文献 1 :特開 2 0 1 0 _ 2 0 1 3 2 3号公報 [0004] Patent Document 1: Japanese Unexamined Patent Publication No. 2 0 1 0 _ 2 0 1 3 2 3

発明の概要 〇 2020/175470 2 卩(:171? 2020 /007469 発明が解決しようとする課題 Summary of the invention 〇 2020/175470 2 (:171? 2020/007469) Problems to be solved by the invention

[0005] 例えば再生動作を実行する時間、 フィルタを通過させる再生空気量等とい った実行条件は、 一定であるように設定されるか、 又はコンブレッサから送 出される圧縮空気量等に応じて決定されている。 しかし、 いずれの場合も、 過不足が生じることが発明者らによって判明している。 再生時間や再生空気 量が不足すると、 乾燥剤の水分捕捉能力が本来の程度まで復帰せず、 圧縮空 気乾燥装置から送出される空気に含有される水分量が多くなる可能性がある 。 一方、 再生時間や再生空気量が過剰となる場合には、 本来、 空気圧システ ムに供給するものであるエアタンク内の圧縮乾燥空気を無駄に消費すること につながる。 圧縮乾燥空気は、 エンジン等の回転駆動源によって駆動される コンブレッサによって生成されるため、 圧縮乾燥空気の過剰な消費は回転駆 動源の負荷を増加させ、 車両の燃費を低下させることとなる。 [0005] Execution conditions such as the time for executing the regeneration operation, the amount of regeneration air to be passed through the filter, etc. are set to be constant, or are determined according to the amount of compressed air sent from the compressor. Has been done. However, it has been found by the inventors that in either case, excess or deficiency occurs. If the regeneration time or the amount of regenerated air is insufficient, the moisture trapping ability of the desiccant may not return to its original level, and the amount of moisture contained in the air sent from the compressed air drying device may increase. On the other hand, if the regeneration time or the amount of regenerated air becomes excessive, the compressed dry air in the air tank, which originally supplies the pneumatic system, is wastefully consumed. Compressed dry air is generated by a compressor driven by a rotary drive source such as an engine, so excessive consumption of compressed dry air increases the load on the rotary drive source and reduces fuel consumption of the vehicle.

[0006] 本開示の目的は、 空気供給システムの除湿性能を維持しつつ、 空気供給シ ステムによる圧縮乾燥空気の消費量を低減することにある。 [0006] An object of the present disclosure is to reduce the amount of compressed dry air consumed by the air supply system while maintaining the dehumidification performance of the air supply system.

課題を解決するための手段 Means for solving the problem

[0007] 上記課題を解決する空気供給システムは、 圧縮空気を送出するコンブレッ サ及び圧縮乾燥空気を貯留する貯留部の間に設けられており、 水分を捕捉す るフィルタを有する、 空気乾燥回路と、 前記空気乾燥回路を制御する制御装 置と、 を備え、 前記制御装置は、 前記コンブレッサから送出された前記圧縮 空気を前記フィルタに順方向に通過させて前記貯留部に供給する除湿動作を 実行するように前記空気乾燥回路を制御し、 前記貯留部に貯留された前記圧 縮乾燥空気を前記フィルタに逆方向に通過させて前記フィルタを通過した流 体を排出口から排出する再生動作を実行するように前記空気乾燥回路を制御 し、 前記コンブレッサの稼働状態に応じて、 1回の前記再生動作で消費する 再生空気量を設定するように構成されている。 [0007] An air supply system that solves the above problems is provided between a compressor that delivers compressed air and a storage unit that stores compressed dry air, and has an air drying circuit that has a filter that traps moisture. A control device for controlling the air drying circuit, the control device performing a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in the forward direction to be supplied to the storage section. The air drying circuit is controlled so that the compressed dry air stored in the storage section is passed through the filter in the reverse direction, and the fluid that has passed through the filter is discharged from the discharge port. The air drying circuit is controlled so that the amount of regenerated air consumed in one regenerating operation is set according to the operating state of the compressor.

[0008] 上記課題を解決する空気供給システムの制御方法は、 圧縮空気を送出する コンブレッサ及び圧縮乾燥空気を貯留する貯留部の間に設けられており、 水 分を捕捉するフィルタを有する、 空気乾燥回路と、 前記空気乾燥回路を制御 〇 2020/175470 3 卩(:171? 2020 /007469 [0008] An air supply system control method that solves the above-mentioned problem is provided with a filter that captures water, which is provided between a compressor that delivers compressed air and a reservoir that stores compressed dry air. Circuit and control the air drying circuit 〇 2020/175 470 3 卩 (:171? 2020 /007469

する制御装置とを備える空気供給システムの制御方法であって前記制御装置 が、 前記コンブレッサから送出された前記圧縮空気を前記フィルタに順方向 に通過させて前記貯留部に供給する除湿動作を実行するように前記空気乾燥 回路を制御し、 前記貯留部に貯留された前記圧縮乾燥空気を前記フィルタに 逆方向に通過させて前記フィルタを通過した流体を排出口から排出する再生 動作を実行するように前記空気乾燥回路を制御し、 前記コンプレッサの稼働 状態に応じて、 1回の前記再生動作で消費する再生空気量を設定する。 A control method of an air supply system, comprising: a control device for performing a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in a forward direction to be supplied to the storage section. The air drying circuit is controlled so that the compressed dry air stored in the storage section is passed through the filter in the reverse direction, and the fluid that has passed through the filter is discharged from the discharge port. The air drying circuit is controlled to set the amount of regeneration air consumed in one regeneration operation according to the operating state of the compressor.

[0009] 上記課題を解決する空気供給システムの制御プログラムは、 圧縮空気を送 出するコンブレッサ及び圧縮乾燥空気を貯留する貯留部の間に設けられてお り、 水分を捕捉するフィルタを有する、 空気乾燥回路と、 前記空気乾燥回路 を制御する制御装置とを備える空気供給システムの制御プログラムであって 前記制御装置を、 前記コンプレッサから送出された前記圧縮空気を前記フィ ルタに順方向に通過させて前記貯留部に供給する除湿動作を実行するように 前記空気乾燥回路を制御する除湿動作実行部、 前記貯留部に貯留された前記 圧縮乾燥空気を前記フィルタに逆方向に通過させて前記フィルタを通過した 流体を排出口から排出する再生動作を実行するように前記空気乾燥回路を制 御する再生動作実行部、 及び、 前記コンブレッサの稼働状態に応じて、 1回 の前記再生動作で消費する再生空気量を設定する設定部、 として機能させる A control program for an air supply system that solves the above-mentioned problems is provided between a compressor that delivers compressed air and a storage section that stores compressed dry air, and has a filter that captures moisture. A control program for an air supply system comprising a drying circuit and a control device for controlling the air drying circuit, the control device causing the compressed air sent from the compressor to pass through the filter in a forward direction. A dehumidifying operation executing unit that controls the air drying circuit to execute a dehumidifying operation to be supplied to the storage unit, and allows the compressed dry air stored in the storage unit to pass through the filter in the reverse direction and through the filter. A regeneration operation execution unit that controls the air drying circuit to perform a regeneration operation that discharges the fluid from the discharge port, and a regeneration air that is consumed by one regeneration operation according to the operating state of the compressor. Function as a setting unit, which sets the amount

[0010] 上記構成によれば、 制御装置は、 コンブレッサの稼働状態に基づき、 再生 動作で消費される再生空気量を設定する。 コンブレッサは空気乾燥回路以外 の装置への圧縮乾燥空気の供給状態に応じて駆動されるので、 再生空気量を 変更することにより、 貯留部から空気乾燥回路以外の装置への圧縮乾燥空気 の供給及びフィルタの清浄化のいずれかを優先することができる。 [0010] According to the above configuration, the control device sets the amount of regeneration air consumed in the regeneration operation based on the operating state of the compressor. The compressor is driven according to the supply condition of compressed dry air to devices other than the air drying circuit.Therefore, by changing the amount of regenerated air, it is possible to supply compressed dry air from the storage unit to devices other than the air drying circuit. Either cleaning of the filter can be prioritized.

[001 1 ] 上記空気供給システムについて、 前記制御装置は、 一定期間内の前記コン プレッサの稼働率が高い場合には、 前記再生空気量を小さく し、 前記コンブ レッサの稼働率が低い場合には、 前記再生空気量を大きくするように構成さ れてよい。 〇 2020/175470 卩(:171? 2020 /007469 [001 1] In the air supply system, the control device reduces the regeneration air amount when the operation rate of the compressor is high within a certain period, and when the operation rate of the compressor is low, It may be configured to increase the regeneration air amount. 〇 2020/175 470 (:171? 2020 /007469

[0012] 上記構成によれば、 コンブレッサの稼働率が高く、 貯留部から空気乾燥回 路以外の装置への圧縮乾燥空気の供給の度合いが大きい場合には、 再生空気 量を小さくすることにより、 貯留部に貯留された圧縮乾燥空気の消費を抑制 し、 空気乾燥回路以外の装置への圧縮乾燥空気の供給を優先させることがで きる。 また、 コンブレッサの稼働率が低く、 貯留部から空気乾燥回路以外の 装置への圧縮乾燥空気の供給の度合いが小さい場合にはフィルタの清浄化を 優先させることができる。 [0012] According to the above configuration, when the operating rate of the compressor is high and the degree of supply of compressed dry air from the storage section to devices other than the air drying circuit is large, the amount of regenerated air is reduced to It is possible to suppress the consumption of the compressed dry air stored in the storage section and give priority to the supply of the compressed dry air to devices other than the air drying circuit. In addition, if the operating rate of the compressor is low and the degree of supply of compressed dry air from the storage section to devices other than the air drying circuit is small, the filter cleaning can be prioritized.

[0013] 上記空気供給システムについて、 前記制御装置は、 前記貯留部内の圧縮乾 燥空気の湿潤状態を示す指標が高い場合には、 前記再生空気量を大きく し、 前記貯留部内の圧縮乾燥空気の湿潤状態を示す指標が低い場合には、 前記再 生空気量を小さくするように構成されてよい。 [0013]In the air supply system, the controller increases the amount of regenerated air when the index indicating the wet state of the compressed dry air in the storage section is high, When the index indicating the wet state is low, the amount of regenerated air may be reduced.

[0014] 上記構成によれば、 圧縮乾燥空気の湿潤状態が高い場合には、 再生空気量 を大きくすることにより、 フィルタの清浄化を優先させることができる。 ま た、 湿潤状態が低い場合には、 貯留部に貯留された圧縮乾燥空気の消費を抑 制することによって、 空気乾燥回路以外の装置への圧縮乾燥空気の供給を優 先させることができる。 [0014] According to the above configuration, when the wet state of the compressed dry air is high, it is possible to give priority to the cleaning of the filter by increasing the amount of regenerated air. Further, when the wet condition is low, the consumption of the compressed dry air stored in the storage section can be suppressed to give priority to the supply of the compressed dry air to devices other than the air drying circuit.

[0015] 上記空気供給システムについて、 前記制御装置は、 前記コンブレッサの稼 働率が高い場合には前記貯留部の圧力であって前記再生動作を開始するため の上限圧を高く設定し、 前記コンブレッサの稼働率が低い場合には前記上限 圧を低く設定し、 前記上限圧が高い場合には前記再生空気量を小さく し、 前 記上限圧が低い場合には前記再生空気量を大きくするように構成されてよい [0015]In the air supply system, the control device sets a high upper limit pressure for starting the regeneration operation, which is the pressure of the storage section when the operation rate of the compressor is high, When the operating rate is low, the upper limit pressure is set low, when the upper limit pressure is high, the regeneration air amount is reduced, and when the upper limit pressure is low, the regeneration air amount is increased. May be done

[0016] 上記構成によれば、 コンブレッサの稼働状態に応じて再生動作を開始する ための上限圧が設定される。 また、 上限圧に応じて再生空気量が決定される 。 コンブレッサの稼働率が高い場合には上限圧を高く設定し且つ再生空気量 を小さくするので、 再生動作の実行頻度を低下させるとともに貯留部に貯留 された圧縮乾燥空気の消費を抑制し、 空気乾燥回路以外の装置への圧縮乾燥 空気の供給を優先させることができる。 また、 コンブレッサの稼働率が低い 〇 2020/175470 5 卩(:171? 2020 /007469 According to the above configuration, the upper limit pressure for starting the regeneration operation is set according to the operating state of the compressor. Also, the amount of regenerated air is determined according to the upper limit pressure. When the operating rate of the compressor is high, the upper limit pressure is set high and the amount of regenerated air is reduced, so that the frequency of regenerating operations is reduced and the consumption of compressed dry air stored in the storage section is suppressed, thereby reducing air drying. The supply of compressed dry air to equipment other than the circuit can be prioritized. Also, the operating rate of the combreza is low. 〇 2020/175 470 5 卩 (:171? 2020 /007469

場合には上限圧を低く設定し且つ再生空気量を大きくするので、 再生動作の 実行頻度を高く してフィルタを浄化する効果を高めることができる。 In this case, the upper limit pressure is set low and the amount of regeneration air is increased, so that it is possible to increase the frequency of regeneration operations and enhance the effect of purifying the filter.

[0017] 上記課題を解決する空気供給システムは、 圧縮空気を送出するコンブレッ サ及び圧縮乾燥空気を貯留する貯留部の間に設けられており、 水分を捕捉す るフィルタを有する、 空気乾燥回路と、 前記空気乾燥回路を制御する制御装 置と、 を備え、 前記制御装置は、 前記コンブレッサから送出された前記圧縮 空気を前記フィルタに順方向に通過させて前記貯留部に供給する除湿動作を 実行するように前記空気乾燥回路を制御し、 前記貯留部に貯留された前記圧 縮乾燥空気を前記フィルタに逆方向に通過させて前記フィルタを通過した流 体を排出口から排出する再生動作を実行するように前記空気乾燥回路を制御 し、 前記圧縮空気又は前記圧縮乾燥空気の温度に応じて、 1回の前記再生動 作で消費する再生空気量を設定するように構成されている。 An air supply system that solves the above problems is provided between a compressor that delivers compressed air and a storage unit that stores compressed dry air, and has an air drying circuit that has a filter that traps moisture. A control device for controlling the air drying circuit, the control device performing a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in the forward direction to be supplied to the storage section. The air drying circuit is controlled so that the compressed dry air stored in the storage section is passed through the filter in the reverse direction, and the fluid that has passed through the filter is discharged from the discharge port. The air drying circuit is controlled so that the amount of regenerated air consumed in one regenerating operation is set according to the temperature of the compressed air or the compressed dried air.

[0018] 上記課題を解決する空気供給システムの制御方法は、 圧縮空気を送出する コンブレッサ及び圧縮乾燥空気を貯留する貯留部の間に設けられており、 水 分を捕捉するフィルタを有する、 空気乾燥回路と、 前記空気乾燥回路を制御 する制御装置とを備える空気供給システムの制御方法であって前記制御装置 が、 前記コンブレッサから送出された前記圧縮空気を前記フィルタに順方向 に通過させて前記貯留部に供給する除湿動作を実行するように前記空気乾燥 回路を制御し、 前記貯留部に貯留された前記圧縮乾燥空気を前記フィルタに 逆方向に通過させて前記フィルタを通過した流体を排出口から排出する再生 動作を実行するように前記空気乾燥回路を制御し、 前記圧縮空気の温度又は 前記圧縮乾燥空気の温度に応じて、 1回の前記再生動作で消費する再生空気 量を設定する。 [0018] An air supply system control method that solves the above-mentioned problem is provided with a filter that traps water, which is provided between a compressor that delivers compressed air and a reservoir that stores compressed dry air. A control method for an air supply system comprising a circuit and a control device for controlling the air drying circuit, wherein the control device allows the compressed air sent from the compressor to pass through the filter in a forward direction to store the compressed air. The air drying circuit is controlled so as to execute a dehumidifying operation for supplying the compressed dry air stored in the storage section to the filter in the reverse direction, and the fluid passing through the filter is discharged from the outlet. The air drying circuit is controlled so as to execute the discharging operation for discharging, and the amount of the reproducing air consumed by one time of the reproducing operation is set according to the temperature of the compressed air or the temperature of the compressed dry air.

[0019] 上記課題を解決する空気供給システムの制御プログラムは、 圧縮空気を送 出するコンブレッサ及び圧縮乾燥空気を貯留する貯留部の間に設けられてお り、 水分を捕捉するフィルタを有する、 空気乾燥回路と、 前記空気乾燥回路 を制御する制御装置とを備える空気供給システムの制御プログラムであって 前記制御装置を、 前記コンプレッサから送出された前記圧縮空気を前記フィ 〇 2020/175470 6 卩(:171? 2020 /007469 [0019] An air supply system control program that solves the above-mentioned problems is provided between a compressor for delivering compressed air and a reservoir for storing compressed dry air, and has a filter for trapping moisture. A control program for an air supply system comprising a drying circuit and a control device for controlling the air drying circuit, wherein the control device controls the compressed air sent from the compressor. 〇 2020/175 470 6 卩 (:171? 2020 /007469

ルタに順方向に通過させて前記貯留部に供給する除湿動作を実行するように 前記空気乾燥回路を制御する除湿動作実行部、 前記貯留部に貯留された前記 圧縮乾燥空気を前記フィルタに逆方向に通過させて前記フィルタを通過した 流体を排出口から排出する再生動作を実行するように前記空気乾燥回路を制 御する再生動作実行部、 及び、 前記圧縮空気の温度又は前記圧縮乾燥空気の 温度に応じて、 1回の前記再生動作で消費する再生空気量を設定する設定部 、 として機能させる。 Dehumidifying operation execution unit that controls the air drying circuit so as to perform a dehumidifying operation that allows the air to pass through the filter in the forward direction and supplies the dehumidifying operation to the storage unit; And a temperature of the compressed dry air or a temperature of the compressed dry air that controls the air drying circuit to perform a regeneration operation of discharging the fluid that has passed through the filter and is discharged from the outlet. According to the above, it functions as a setting unit that sets the amount of regeneration air consumed in one regeneration operation.

[0020] 上記構成によれば、 制御装置は、 圧縮空気の温度又は圧縮乾燥空気の温度 に応じて、 再生動作で消費される再生空気量を設定する。 圧縮空気の温度又 は圧縮乾燥空気の温度が上昇すると、 空気に含まれる水分量も多くなるため 、 空気に含まれる水分量の多さに応じて再生空気量を変更することにより、 貯留部から空気乾燥回路以外の装置への圧縮乾燥空気の供給、 及びフィルタ の清浄化のいずれかを優先することができる。 According to the above configuration, the control device sets the amount of regenerated air consumed in the regenerating operation according to the temperature of the compressed air or the temperature of the compressed dry air. When the temperature of the compressed air or the temperature of the compressed dry air rises, the amount of water contained in the air also increases.Therefore, by changing the amount of regenerated air according to the amount of water contained in the air, Either supply of compressed dry air to equipment other than the air drying circuit or cleaning of the filter can be prioritized.

[0021 ] 上記空気供給システムについて、 前記制御装置は、 前記温度が低い場合に は、 前記再生空気量を小さく し、 前記温度が高い場合には、 前記再生空気量 を大きくするように構成されてよい。 [0021] In the air supply system, the control device is configured to reduce the amount of regenerated air when the temperature is low, and increase the amount of regenerated air when the temperature is high. Good.

[0022] 上記構成によれば、 空気の温度が低く、 飽和水蒸気量が小さい場合には再 生空気量を小さくすることにより、 貯留部に貯留された圧縮乾燥空気の消費 を抑制し、 空気乾燥回路以外の装置への圧縮乾燥空気の供給を優先させるこ とができる。 また、 空気の温度が高く、 飽和水蒸気量が大きい場合には再生 空気量を大きく してフィルタの清浄化を優先させることができる。 [0022] According to the above configuration, when the temperature of air is low and the amount of saturated steam is small, the amount of regenerated air is reduced, thereby suppressing the consumption of the compressed dry air stored in the storage unit and performing air drying. The supply of compressed dry air to devices other than the circuit can be prioritized. When the temperature of air is high and the amount of saturated steam is large, the amount of regenerated air can be increased to prioritize the filter cleaning.

発明の効果 Effect of the invention

[0023] 本開示によれば、 空気供給システムの除湿性能を維持しつつ、 空気供給シ ステムによる圧縮乾燥空気の消費量を低減することができる。 [0023] According to the present disclosure, it is possible to reduce the amount of compressed dry air consumed by the air supply system while maintaining the dehumidification performance of the air supply system.

図面の簡単な説明 Brief description of the drawings

[0024] [図 1 ]空気供給システムの第 1実施形態の概略構成を示す構成図。 FIG. 1 is a configuration diagram showing a schematic configuration of a first embodiment of an air supply system.

[図 2]図 2八〜図 2 はそれぞれ図 1の実施形態の空気乾燥回路の第 1〜第 6 動作モードを示す図。 〇 2020/175470 7 卩(:171? 2020 /007469 [Fig. 2] Figs. 28 to 2 are views showing first to sixth operation modes of the air drying circuit of the embodiment of Fig. 1, respectively. 〇 2020/175 470 7 卩 (: 171? 2020 /007469

[図 3]図 3 Aは、 図 1の実施形態の再生空気量を算出するための標準再生空気 量のマップ、 図 3巳は、 図 1の実施形態の再生空気量を算出するための補正 単位空気量のマップ。 [FIG. 3] FIG. 3A is a map of a standard regenerated air amount for calculating the regenerated air amount of the embodiment of FIG. 1, and FIG. 3 is a correction for calculating the regenerated air amount of the embodiment of FIG. Map of unit air volume.

[図 4]図 1の実施形態の過不足係数情報の模式図。 FIG. 4 is a schematic diagram of excess/deficiency coefficient information of the embodiment of FIG.

[図 5]図 1の実施形態における圧縮空気を供給する手順の一例を示すフローチ ヤート。 [FIG. 5] A flow chart showing an example of a procedure for supplying compressed air in the embodiment of FIG. 1.

[図 6]図 1の実施形態における再生動作を行う手順の一例を示すフローチヤー 卜。 [FIG. 6] A flow chart showing an example of a procedure for performing a reproducing operation in the embodiment of FIG. 1.

[図 7]図 1の実施形態における再生空気量を決定する手順の一例を示すフロー チヤート。 FIG. 7 is a flow chart showing an example of a procedure for determining the regeneration air amount in the embodiment of FIG.

[図 8]図 8 Aは、 第 2実施形態の再生空気量を算出するための標準再生空気量 のマップ、 図 8巳は、 第 2実施形態の再生空気量を算出するための補正単位 空気量のマップ。 [FIG. 8] FIG. 8A is a map of the standard regenerated air amount for calculating the regenerated air amount of the second embodiment, and FIG. 8 is a correction unit air for calculating the regenerated air amount of the second embodiment. Quantity map.

[図 9]図 8の実施形態における再生空気量を決定する手順の一例を示すフロー チヤート。 FIG. 9 is a flow chart showing an example of a procedure for determining the regeneration air amount in the embodiment of FIG.

発明を実施するための形態 MODE FOR CARRYING OUT THE INVENTION

[0025] (第 1実施形態) [0025] (First Embodiment)

図 1〜図 6を参照して、 空気供給システムの第 1実施形態について説明す る。 空気供給システムは、 トラック、 バス、 建機等の自動車に搭載されてい る。 空気供給システムにより生成された圧縮乾燥空気は、 例えば、 自動車の ブレーキシステム (制動装置) 又はサスペンションシステム (懸架装置) 等 の空気圧システムに用いられる。 A first embodiment of the air supply system will be described with reference to FIGS. 1 to 6. The air supply system is installed in automobiles such as trucks, buses, and construction machines. The compressed dry air generated by the air supply system is used in a pneumatic system such as a brake system (braking device) or a suspension system (suspension device) of an automobile.

[0026] <空気供給システム 1 0> [0026] <Air supply system 10>

図 1 を参照して空気供給システム 1 〇について説明する。 空気供給システ ム 1 0は、 コンブレッサ 4と、 空気乾燥回路 1 1 と、 ECU (E l e c t r o n i c Co n t r o l U n i t) 80とを備える。 なお、 E C U 80 が、 制御装置、 除湿動作実行部、 再生動作実行部、 設定部として機能する。 [0027] E C U 80は、 複数の配線 E 6 1〜 E 67を介して空気乾燥回路 1 1 と接 〇 2020/175470 8 卩(:171? 2020 /007469 The air supply system 10 will be described with reference to FIG. The air supply system 10 is provided with a compressor 4, an air drying circuit 11 and an ECU (Electronic Control Unit) 80. The ECU 80 functions as a control device, a dehumidification operation execution unit, a regeneration operation execution unit, and a setting unit. [0027] The ECU 80 is connected to the air drying circuit 11 via a plurality of wirings E61 to E67. 〇 2020/175 470 8 卩 (:171? 2020 /007469

続されている。 ECU 80は、 演算部、 通信インターフェース部、 揮発性記 憶部、 不揮発性記憶部を備えている。 演算部は、 コンピュータプロセッサで あって、 不揮発性記憶部 (記憶媒体) に記憶された空気供給プログラムにし たがって、 空気乾燥回路 1 1 を制御するように構成されている。 演算部は、 自身が実行する処理の少なくとも一部を、 AS I C等の回路により実現して もよい。 空気供給プログラムは、 一つのコンビュータプロセッサによって実 行されてもよいし、 複数のコンビュータプロセッサによって実行されてもよ い。 また、 E C U 80は、 空気乾燥回路 1 1の各動作の実行頻度を決定する ための情報を記憶する記憶部 80 Aを備える。 記憶部 80 Aは、 不揮発性記 憶部又は揮発性記憶部であり、 上記制御プログラムが記憶された記憶部と同 —のものであってもよいし、 異なるものであってもよい。 Has been continued. The ECU 80 includes a calculation unit, a communication interface unit, a volatile storage unit, and a non-volatile storage unit. The arithmetic unit is a computer processor and is configured to control the air drying circuit 11 according to an air supply program stored in a non-volatile storage unit (storage medium). The arithmetic unit may realize at least a part of the processing executed by itself by a circuit such as AS IC. The air supply program may be executed by one computer processor or may be executed by a plurality of computer processors. In addition, the ECU 80 includes a storage unit 80A that stores information for determining the execution frequency of each operation of the air drying circuit 11. The storage unit 80A is a non-volatile storage unit or a volatile storage unit, and may be the same as or different from the storage unit in which the control program is stored.

[0028] ECU 80は、 CAN (Co n t r o l l e r A r e a N e t wo r k) 等の車載ネッ トワークを介して、 例えばエンジン ECU、 ブレーキ EC U等、 車両に搭載された他の ECU (図示略) に接続されている。 ECU 8 0は、 それらの ECUから、 車両状態を示す情報を取得する。 車両状態を示 す情報には、 例えば、 イグニッシヨンスイッチのオフ情報、 車速、 エンジン の駆動情報等が含まれる。 [0028] The ECU 80 is connected to other ECUs (not shown) mounted on the vehicle, such as an engine ECU and a brake ECU, via an in-vehicle network such as CAN (Controller Area Network). Has been done. The ECU 80 acquires information indicating the vehicle state from those ECUs. The information indicating the vehicle state includes, for example, ignition switch OFF information, vehicle speed, engine drive information, and the like.

[0029] コンブレッサ 4の状態は、 ECU 80からの指令に基づいて、 空気を圧縮 して送出する稼働状態 (負荷運転) と、 空気の圧縮を行わない非稼働状態 ( 空運転) との間で切り替えられる。 コンブレッサ 4は、 エンジン等の回転駆 動源から伝達された動力で稼働する。 [0029] The state of the compressor 4 is based on a command from the ECU 80 between an operating state in which air is compressed and sent (load operation) and a non-operating state in which air is not compressed (idle operation). Can be switched. The compressor 4 operates by the power transmitted from a rotary drive source such as an engine.

[0030] 空気乾燥回路 1 1は、 いわゆる、 エアドライヤである。 空気乾燥回路 1 1 は、 ECU 80に接続され、 負荷運転中のコンブレッサ 4から送られた圧縮 空気から該圧縮空気に含まれる水分等を除去する。 空気乾燥回路 1 1は、 乾 燥された後の圧縮空気 (以下、 圧縮乾燥空気) を、 供給回路 1 2に供給する 。 供給回路 1 2に対し供給された圧縮乾燥空気は、 エアタンク 30に貯留さ れる。 [0030] The air drying circuit 11 is a so-called air dryer. The air drying circuit 11 is connected to the ECU 80, and removes moisture and the like contained in the compressed air sent from the compressor 4 during load operation. The air drying circuit 11 supplies the dried compressed air (hereinafter, compressed dry air) to the supply circuit 12. The compressed dry air supplied to the supply circuit 12 is stored in the air tank 30.

[0031] エアタンク 30に貯留された圧縮乾燥空気は、 車両に搭載されたブレーキ 〇 2020/175470 9 卩(:171? 2020 /007469 [0031] The compressed dry air stored in the air tank 30 is supplied to the brake installed in the vehicle. 〇 2020/175 470 9 卩 (:171? 2020 /007469

システム等の空気圧システムに供給される。 例えば、 車両が降坂路又は市街 地を走行する状況等、 ブレーキが作動される頻度が高い場合には、 エアタン ク 3 0に貯留された圧縮乾燥空気の消費量が多くなる。 逆に、 ブレーキが作 動される頻度が低い場合には、 エアタンク 3 0に貯留された圧縮乾燥空気の 消費量が少なくなる。 Supply to pneumatic system such as system. For example, when the frequency of braking is high, such as when a vehicle travels on a downhill road or an urban area, the amount of compressed dry air stored in the air tank 30 increases. On the contrary, when the brake is operated infrequently, the amount of compressed dry air stored in the air tank 30 is reduced.

[0032] 空気乾燥回路 1 1は、 メンテナンス用ポート 1 2を有している。 メンテ ナンス用ポート 1 2は、 メンテナンスの際にそれを通じて空気乾燥回路 1 1 に空気を供給するためのポートである。 The air drying circuit 11 has a maintenance port 12. The maintenance port 12 is a port for supplying air to the air drying circuit 11 through it during maintenance.

[0033] 空気乾燥回路 1 1は、 ケース 1 1 八 (図 2八参照) の内部等にフィルタ 1 [0033] The air drying circuit 11 has a filter 1 inside the case 1 18 (see Fig. 28).

7を備えている。 フィルタ 1 7は、 コンブレッサ 4と供給回路 1 2とを接続 する空気供給通路 1 8の途中に設けられている。 フィルタ 1 7は、 乾燥剤を 含む。 また、 フィルタ 1 7は、 乾燥剤とは別に、 油分を捕捉する油分捕捉部 を含む。 油分捕捉部は、 ウレタンフォーム等の発泡体、 多数の通気孔を有す る金属材、 ガラス繊維フィルタ等、 空気を通過させながら油分を捕捉できる ものであればよい。 Equipped with 7. The filter 17 is provided in the middle of the air supply passage 18 which connects the compressor 4 and the supply circuit 12. Filter 17 contains a desiccant. In addition to the desiccant, the filter 17 also includes an oil trap portion that traps oil. The oil capturing part may be a foam such as urethane foam, a metal material having a large number of ventilation holes, a glass fiber filter, or the like as long as it can capture the oil while allowing air to pass therethrough.

[0034] フィルタ 1 7は、 コンブレッサ 4から送出された圧縮空気を乾燥剤に通過 させることによって、 圧縮空気に含まれる水分を圧縮空気から除去して圧縮 空気を乾燥させる。 また、 油分捕捉部は、 圧縮空気に含まれる油分を捕捉し て圧縮空気を清浄化する。 フィルタ 1 7を通過した圧縮空気は、 下流チェッ クバルブ 1 9を介して供給回路 1 2へ供給される。 下流チェックバルブ 1 9 は、 フィルタ 1 7側を上流、 供給回路 1 2側を下流としたとき、 上流から下 流への空気の流れのみを許容する。 なお、 下流チェックバルブ 1 9は、 所定 の開弁圧 (封止圧) を有していることから、 圧縮空気が流れるとき、 上流の 圧力は下流の圧力よりも開弁圧だけ高くなる。 [0034] The filter 17 removes the water contained in the compressed air from the compressed air to dry the compressed air by passing the compressed air sent from the compressor 4 through the desiccant. Further, the oil trap portion traps oil contained in the compressed air to purify the compressed air. The compressed air that has passed through the filter 17 is supplied to the supply circuit 12 via the downstream check valve 19. The downstream check valve 19 allows only air flow from upstream to downstream when the filter 17 side is upstream and the supply circuit 12 side is downstream. Since the downstream check valve 19 has a predetermined valve opening pressure (sealing pressure), the upstream pressure becomes higher than the downstream pressure by the valve opening pressure when compressed air flows.

[0035] また、 フィルタ 1 7の下流には、 下流チェックバルブ 1 9を迂回する迂回 路としてのバイパス流路 2 0が下流チェックバルブ 1 9に対して並列に設け られている。 バイパス流路 2 0には、 再生制御弁 2 1が設けられている。 Further, a bypass passage 20 as a bypass for bypassing the downstream check valve 19 is provided downstream of the filter 17 in parallel with the downstream check valve 19. A regeneration control valve 21 is provided in the bypass passage 20.

[0036] 再生制御弁 2 1は、 巳(3 11 8 0によって制御される電磁弁である。 巳〇11 〇 2020/175470 10 卩(:171? 2020 /007469 [0036] The regeneration control valve 21 is a solenoid valve controlled by the valve 311800. 〇 2020/175 470 10 卩 (:171? 2020 /007469

8 0は、 配線日 6 4を介して再生制御弁 2 1の電源の入り切り (駆動/非駆 動) を制御することによって、 再生制御弁 2 1の動作を切り替える。 再生制 御弁 2 1は、 電源が切れた状態において閉弁してバイパス流路 2 0を封止し 、 電源が入った状態において開弁してバイパス流路 2 0を連通させる。 巳〇 II 8 0は、 例えば、 エアタンク 3 0内の空気圧の値を受けて、 空気圧の値が 所定の範囲を超えたとき再生制御弁 2 1 を動作させる。 80 controls the regeneration control valve 2 1 power on/off (driving/non-driving) via the wiring date 6 4 to switch the regeneration control valve 2 1 operation. The regeneration control valve 21 is closed when the power is off to seal the bypass passage 20 and opened when the power is on to communicate the bypass passage 20. The MII II 80, for example, receives the value of the air pressure in the air tank 30 and operates the regeneration control valve 21 when the value of the air pressure exceeds a predetermined range.

[0037] バイパス流路 2 0には、 再生制御弁 2 1 とフィルタ 1 7との間にオリフィ ス 2 2が設けられている。 再生制御弁 2 1が通電されると、 供給回路 1 2側 の圧縮乾燥空気が、 バイパス流路 2 0を介して、 オリフィス 2 2によって流 量を規制された状態でフィルタ 1 7に送られる。 フィルタ 1 7に対し送られ た圧縮乾燥空気は、 フィルタ 1 7を下流から上流に向けて逆流し、 フィルタ 1 7を通過する。 このような処理は、 フィルタ 1 7を再生させる動作であり 、 空気乾燥回路 1 1の再生動作という。 このとき、 フィルタ 1 7に対し送ら れる圧縮乾燥空気は、 空気供給通路 1 8からフィルタ 1 7等を通過して供給 回路 1 2に供給された乾燥及び清浄化された空気であるため、 フィルタ 1 7 に捕捉された水分及び油分をフィルタ 1 7から除去することができる。 巳〇 11 8 0は、 通常の制御において、 エアタンク 3 0内の圧力が上限値 (カッ ト アウト圧) に到達すると、 再生制御弁 2 1 を開弁する。 一方、 エアタンク 3 0内の圧力が下限値 (カッ トイン圧) に到達すると、 開弁した再生制御弁 2 1 を閉弁する。 An orifice 22 is provided in the bypass passage 20 between the regeneration control valve 21 and the filter 17. When the regeneration control valve 21 is energized, the compressed dry air on the side of the supply circuit 12 is sent to the filter 17 through the bypass passage 20 while the flow rate is regulated by the orifice 22. The compressed dry air sent to the filter 17 flows backward through the filter 17 from the downstream side to the upstream side, and passes through the filter 17. Such processing is an operation of regenerating the filter 17 and is called a regenerating operation of the air drying circuit 11. At this time, the compressed dry air sent to the filter 17 is the dried and purified air supplied to the supply circuit 12 from the air supply passage 18 through the filter 17 etc. The water and oil trapped in 7 can be removed from the filter 17. In the normal control, the No. 1 1 180 opens the regeneration control valve 21 when the pressure in the air tank 30 reaches the upper limit value (cutout pressure). On the other hand, when the pressure in the air tank 30 reaches the lower limit (cut-in pressure), the opened regeneration control valve 21 is closed.

[0038] コンブレッサ 4とフィルタ 1 7との間の部分から、 分岐通路 1 6が分岐し ている。 分岐通路 1 6にはドレン排出弁 2 5が設けられており、 分岐通路 1 6の末端にはドレン排出口 2 7が接続されている。 [0038] A branch passage 16 is branched from a portion between the combiner 4 and the filter 17. A drain discharge valve 25 is provided in the branch passage 16 and a drain discharge port 27 is connected to the end of the branch passage 16.

[0039] フィルタ 1 7から除去された水分及び油分を含む流体であるドレンは、 圧 縮空気とともにドレン排出弁 2 5に対し送られる。 ドレン排出弁 2 5は、 空 気圧により駆動される空気圧駆動式の弁であって、 分岐通路 1 6において、 フィルタ 1 7とドレン排出口 2 7との間に設けられている。 ドレン排出弁 2 5は、 閉弁位置及び開弁位置の間で位置を変更する 2ポート 2位置弁である 〇 2020/175470 1 1 卩(:171? 2020 /007469 The drain, which is a fluid containing water and oil removed from the filter 17 is sent to the drain discharge valve 25 together with compressed air. The drain discharge valve 25 is a pneumatically driven valve driven by air pressure, and is provided in the branch passage 16 between the filter 17 and the drain discharge port 27. The drain discharge valve 25 is a 2-port 2-position valve that changes its position between a closed position and an open position. 〇 2020/175 470 1 1 卩 (:171? 2020 /007469

。 ドレン排出弁 2 5が開弁位置にあるとき、 ドレンはドレン排出口 2 7へ送 られる。 ドレン排出口 2 7から排出されたドレンは、 図示しないオイルセパ レータによって回収されてもよい。 なお、 ドレンがフィルタ 1 7を逆方向に 通過した流体に相当する。 .. When the drain discharge valve 25 is in the open position, the drain is sent to the drain discharge port 27. The drain discharged from the drain outlet 27 may be collected by an oil separator (not shown). The drain corresponds to the fluid passing through the filter 17 in the opposite direction.

[0040] ドレン排出弁 2 5は、 ガバナ 2 6八によって制御される。 ガバナ 2 6八は [0040] The drain discharge valve 25 is controlled by the governor 2 68. Governor 2 6 8

、 巳〇 II 8 0によって制御される電磁弁である。 巳〇 II 8 0は、 配線巳 6 3 を介してガバナ 2 6八の電源の入り切り (駆動/非駆動) を制御することに よって、 ガバナ 2 6八の動作を切り替える。 ガバナ 2 6八は、 電源が入れら れると、 ドレン排出弁 2 5に空気圧信号を入力する入力位置に切り替わるこ とによって、 ドレン排出弁 2 5を開弁させる。 また、 ガバナ 2 6八は、 電源 が切られると、 ドレン排出弁 2 5に空気圧信号を入力せずにドレン排出弁 2 5のポートを大気圧に開放する開放位置に切り替わることによって、 ドレン 排出弁 2 5を閉弁させる。 , Is a solenoid valve controlled by Ⅱ II 80. The Ⅱ II 80 switches the operation of the governor 2 68 by controlling the turning on/off (drive/non-drive) of the governor 2 68 via the wiring 6 3. When the power is turned on, the governor 268 switches to the input position where the pneumatic signal is input to the drain discharge valve 25, thereby opening the drain discharge valve 25. When the power is turned off, the governor 26 8 switches the drain discharge valve 25 port to the open position where the drain discharge valve 25 port is opened to atmospheric pressure without inputting an air pressure signal to the drain discharge valve 25. Close valve 2 5.

[0041 ] ドレン排出弁 2 5は、 ガバナ 2 6 から空気圧信号が入力されていない状 態では、 分岐通路 1 6を遮断する閉弁位置に維持され、 ガバナ 2 6 から空 気圧信号が入力されると、 分岐通路 1 6を連通する開弁位置に切り替わる。 また、 ドレン排出弁 2 5においてコンブレッサ 4に接続されている入カポー 卜の圧力が上限値を超えた場合、 ドレン排出弁 2 5が強制的に開弁位置に切 り替えられる。 [0041] The drain discharge valve 25 is maintained in the closed position where the branch passage 16 is shut off in the state where the air pressure signal is not input from the governor 26, and the air pressure signal is input from the governor 26. And the valve is opened to connect the branch passage 16 with each other. When the pressure of the inlet casing connected to the compressor 4 at the drain discharge valve 25 exceeds the upper limit value, the drain discharge valve 25 is forcibly switched to the open position.

[0042] コンブレッサ 4とフィルタ 1 7との間であって、 かつ、 コンブレッサ 4と 分岐通路 1 6の間には、 上流チェックバルブ 1 5が設けられている。 上流チ ェックバルブ 1 5は、 コンブレッサ 4側を上流、 フィルタ 1 7側を下流とし たとき、 上流から下流への空気の流れのみを許容する。 上流チェックバルブ 1 5は、 所定の開弁圧 (封止圧) を有していることから、 圧縮空気が流れる とき、 上流の圧力は下流の圧力よりも開弁圧だけ高くなる。 なお、 上流チェ ックバルブ 1 5の上流には、 コンブレッサ 4の出口のリード弁が設けられて いる。 上流チェックバルブ 1 5の下流には、 分岐通路 1 6やフィルタ 1 7が 設けられている。 〇 2020/175470 12 卩(:171? 2020 /007469 An upstream check valve 15 is provided between the compressor 4 and the filter 17 and between the compressor 4 and the branch passage 16. The upstream check valve 15 allows only the air flow from upstream to downstream when the compressor 4 side is upstream and the filter 17 side is downstream. Since the upstream check valve 15 has a predetermined valve opening pressure (sealing pressure), when the compressed air flows, the upstream pressure becomes higher than the downstream pressure by the valve opening pressure. A reed valve at the outlet of the compressor 4 is provided upstream of the upstream check valve 15. A branch passage 16 and a filter 17 are provided downstream of the upstream check valve 15. 〇 2020/175 470 12 boxes (:171? 2020 /007469

[0043] コンブレッサ 4は、 アンロード制御弁 2 6巳によって制御される。 アンロ —ド制御弁 2 6巳は、 巳〇11 8 0によって制御される電磁弁である。 巳〇11 8 0は、 配線巳 6 2を介してアンロード制御弁 2 6巳の電源の入り切り (駆 動/非駆動) を制御することによって、 アンロード制御弁 2 6巳の動作を切 り替える。 アンロード制御弁 2 6巳は、 電源が切られると、 開放位置に切り 替わり、 アンロード制御弁 2 6巳とコンブレッサ 4との間の流路を大気開放 する。 また、 アンロード制御弁 2 6巳は、 電源が入れられると、 供給位置に 切り替わり、 コンブレッサ 4に圧縮空気からなる空気圧信号を送る。 [0043] The combiner 4 is controlled by the unload control valve 26. The unload control valve 26 is a solenoid valve controlled by 〇118. The ∙ ∙ ∙ 1 800 switches off the operation of the unload control valve 2 ∙ 6 by controlling the power on/off (drive/non-drive) of the unload control valve 2 6 ∘ via the wiring switch 6 2. Change. When the power is turned off, the unload control valve 2 6 switches to the open position, and opens the flow path between the unload control valve 2 6 and the compressor 4 to the atmosphere. Further, when the power is turned on, the unload control valve 26 switches to the supply position and sends an air pressure signal consisting of compressed air to the compressor 4.

[0044] コンブレッサ 4の状態は、 アンロード制御弁 2 6巳から空気圧信号が入力 されると、 非稼働状態 (空運転) に切り替わる。 例えば、 エアタンク 3 0内 の圧力がカッ トアウト圧に到達したとき、 圧縮乾燥空気の供給は不要である 。 供給回路 1 2側の圧力がカッ トアウト圧に到達し、 巳(3 11 8 0がアンロー ド制御弁 2 6巳の電源を入れる (アンロード制御弁 2 6巳を駆動する) と、 アンロード制御弁 2 6巳は、 供給位置に切り替わる。 これにより、 アンロー ド制御弁 2 6巳から、 コンブレッサ 4に空気圧信号が供給され、 コンブレッ サ 4の状態が非稼働状態に切り替わる。 [0044] The state of the compressor 4 is switched to a non-operation state (idle operation) when an air pressure signal is input from the unload control valve 26. For example, when the pressure in the air tank 30 reaches the cutout pressure, it is not necessary to supply compressed dry air. When the pressure on the supply circuit 1 2 side reaches the cutout pressure and the power is turned on (3 11 800 turns on the unload control valve 26 6 (drives the unload control valve 2 6)), the unload control is performed. Valve 26 is switched to the supply position, which causes the pneumatic control valve 26 to supply the pneumatic signal to the compressor 4 and switch the state of the compressor 4 to the non-operational state.

[0045] コンブレッサ 4と上流チェックバルブ 1 5との間には、 圧カセンサ 5 0が 設けられている。 圧カセンサ 5 0は、 空気供給通路 1 8に対し接続されてお り、 空気供給通路 1 8の空気圧を測定して、 測定した結果を配線巳 6 1 を介 して巳〇 II 8 0に伝達する。 A pressure sensor 50 is provided between the compressor 4 and the upstream check valve 15. The pressure sensor 50 is connected to the air supply passage 18 and measures the air pressure in the air supply passage 18 and transmits the measurement result to the wire Ⅱ II 80 via the wiring wire 6 1. To do.

[0046] 下流チェックバルブ 1 9と供給回路 1 2との間には、 湿度センサ 5 1及び 温度センサ 5 2が設けられている。 湿度センサ 5 1は、 絶対湿度を検出する ものであってもよく、 相対湿度を検出するものであってもよい。 湿度センサ 5 1及び温度センサ 5 2はそれぞれ、 フィルタ 1 7の下流の圧縮空気の湿度 、 圧縮空気の温度を測定して、 測定した結果を配線日 6 5 , 日 6 6を介して 巳〇 II 8 0に出力する。 巳〇 II 8 0は、 湿度センサ 5 1及び温度センサ 5 2 から入力された湿度及び温度に基づいて圧縮乾燥空気の湿潤状態を判定する 〇 2020/175470 13 卩(:171? 2020 /007469 A humidity sensor 51 and a temperature sensor 52 are provided between the downstream check valve 19 and the supply circuit 12. The humidity sensor 51 may detect absolute humidity or may detect relative humidity. The humidity sensor 51 and the temperature sensor 52 measure the humidity of the compressed air downstream of the filter 17 and the temperature of the compressed air, respectively, and the measurement results are sent via wiring days 6 5 and 6 6 respectively. Output to 80. MII II 80 determines the wet state of compressed dry air based on the humidity and temperature input from humidity sensor 51 and temperature sensor 52. 〇 2020/175 470 13 卩 (:171? 2020 /007469

[0047] さらに下流チェックバルブ 1 9と供給回路 1 2との間には、 圧カセンサ 5 [0047] Further, a pressure sensor 5 is provided between the downstream check valve 19 and the supply circuit 12.

3が設けられている。 圧カセンサ 5 3は、 エアタンク 3 0内の空気圧を検出 可能に設けられ、 検出した圧力値を、 配線 E 6 7を介して E C U 8 0に出力 する。 下流チェックバルブ 1 9及び供給回路 1 2の間の圧力は、 エアタンク 3 0の圧力と同じであり、 圧カセンサ 5 3の検出結果はエアタンク 3 0内の 圧力として用いることができる。 なお、 圧カセンサ 5 3は、 供給回路 1 2に 設けられてもよいし、 エアタンク 3 0に設けられてもよい。 Three are provided. The pressure sensor 53 is provided so as to detect the air pressure in the air tank 30 and outputs the detected pressure value to the ECU 80 via the wiring E67. The pressure between the downstream check valve 19 and the supply circuit 12 is the same as the pressure in the air tank 30. The detection result of the pressure sensor 53 can be used as the pressure in the air tank 30. The pressure sensor 53 may be provided in the supply circuit 12 or the air tank 30.

[0048] <空気乾燥回路 1 1の動作説明 > [0048] <Explanation of operation of air drying circuit 11>

図 2 A〜図 2 Fに示すように、 空気乾燥回路 1 1は、 少なくとも第 1動作 モード〜第 6動作モードを含む、 複数の動作モードを有する。 As shown in FIGS. 2A to 2F, the air drying circuit 11 has a plurality of operation modes including at least a first operation mode to a sixth operation mode.

[0049] (第 1動作モード) [0049] (First operation mode)

図 2 Aに示すように、 第 1動作モードは、 通常の除湿動作 (口ード運転) を行うモードである。 第 1動作モードでは、 再生制御弁 2 1及びアンロード 制御弁 2 6 Bをそれぞれ閉弁し (図において 「C L O S E」 と記載) 、 ガバ ナ 2 6 Aを、 コンブレッサ 4に空気圧信号を入力しない開放位置とする (図 において 「C L O S E」 と記載) 。 このとき、 再生制御弁 2 1、 ガバナ 2 6 A、 及びアンロード制御弁 2 6巳には、 電源が供給されない。 また、 ガバナ 2 6 A及びアンロード制御弁 2 6巳は、 それらの下流に接続されるコンブレ ッサ 4のポート及びドレン排出弁 2 5のポートをそれぞれ大気開放する。 第 1動作モードでは、 コンブレッサ 4から圧縮空気が供給されているとき (図 において 「〇N」 と記載) 、 フィルタ 1 7で水分等が除去され、 供給回路 1 2に対し圧縮空気が供給される。 As shown in FIG. 2A, the first operation mode is a mode for performing a normal dehumidifying operation (mouth operation). In the first operation mode, the regeneration control valve 21 and the unload control valve 26B are each closed (indicated as "CLOSE" in the figure), the governor 26A is opened, and no air pressure signal is input to the compressor 4. Position (marked as “CLOSE” in the figure). At this time, power is not supplied to the regeneration control valve 21, the governor 26 A, and the unload control valve 26 A. Further, the governor 26 A and the unload control valve 26 6 open the port of the compressor 4 and the port of the drain discharge valve 25, which are connected downstream of them, to the atmosphere, respectively. In the first operation mode, when compressed air is being supplied from the compressor 4 (denoted as "○N" in the figure), the filter 17 removes water and other components, and compressed air is supplied to the supply circuit 12 2. ..

[0050] (第 2動作モード) [0050] (Second operation mode)

図 2 Bに示すように、 第 2動作モードは、 空気乾燥回路 1 1内の圧縮乾燥 空気を、 フィルタ 1 7に通過させてフィルタ 1 7を浄化するパージ動作を行 うモードである。 第 2モードでは、 再生制御弁 2 1 を閉弁し、 アンロード制 御弁 2 6 Bを供給位置とし (図において 「O P E N」 と記載) 、 ガバナ 2 6 Aを入力位置 (図において 「O P E N」 と記載) とする。 このとき、 ガバナ 〇 2020/175470 14 卩(:171? 2020 /007469 As shown in FIG. 2B, the second operation mode is a mode in which the compressed dry air in the air drying circuit 11 is passed through the filter 17 to perform the purging operation to purify the filter 17. In the second mode, the regeneration control valve 21 is closed, the unload control valve 26 B is in the supply position (marked as "OPEN" in the figure), and the governor 26 A is in the input position ("OPEN" in the figure). And)). At this time, the governor 〇 2020/175 470 14 卩 (:171? 2020 /007469

2 6 及びアンロード制御弁 2 6巳にはそれぞれ、 電源が供給されるととも に、 それらの下流に接続されるコンブレッサ 4のポート及びドレン排出弁 2 5のポートはそれぞれ上流 (供給回路 1 2側) に接続される。 これにより、 コンブレッサ 4が非稼働状態に切り替わり (図において 「〇 」 と記載)2 6 and the unload control valve 2 6 are both supplied with power, and the ports of the compressor 4 and the drain discharge valve 25, which are connected downstream of them, are respectively connected to the upstream side (supply circuit 1 2 Side). As a result, the Comblator 4 switches to the non-operational state (marked as "○" in the figure).

、 ドレン排出弁 2 5が開弁される。 その結果、 下流チェックバルブ 1 9とフ ィルタ 1 7との間の圧縮乾燥空気が、 フィルタ 1 7内を、 第 1動作モード ( 除湿モード) の空気の流れとは逆方向に流れ (逆流) 、 フィルタ 1 7によっ て捕捉された水分等が、 ドレンとしてドレン排出口 2 7から排出される。 ま た、 フィルタ 1 7及び空気供給通路 1 8の空気圧が大気圧に開放される。 , The drain discharge valve 25 is opened. As a result, the compressed dry air between the downstream check valve 19 and the filter 17 flows in the filter 17 in the direction opposite to the air flow in the first operation mode (dehumidification mode) (backflow), Moisture and the like captured by the filter 17 is discharged as drain from the drain outlet 27. Moreover, the air pressure in the filter 17 and the air supply passage 18 is released to atmospheric pressure.

[0051 ] (第 3動作モード) [0051] (Third operation mode)

図 2〇に示すように、 第 3動作モードは、 フィルタ 1 7を再生する再生動 作を行うモードである。 第 3動作モードでは、 再生制御弁 2 1 を開弁し、 ガ バナ 2 6 を入力位置とし、 アンロード制御弁 2 6巳を供給位置とする (そ れぞれ図において 「〇 巳 」 と記載) 。 このとき、 ガバナ 2 6八及びアン 口ード制御弁 2 6巳に加え、 再生制御弁 2 1 にも電源が供給される。 第 3動 作モードでは、 コンブレッサ 4を非稼働状態とさせるとともに、 供給回路 1 2又はエアタンク 3 0に貯留された圧縮乾燥空気を、 フィルタ 1 7に逆流さ せて、 ドレン排出口 2 7から排出させる。 これによって、 フィルタ 1 7に捕 捉された水分等が除去される。 第 2動作モード及び第 3動作モードは、 いず れもフィルタ 1 7を浄化させるモードであるが、 第 3動作モードは、 少なく とも再生制御弁 2 1 を開弁する点で第 2動作モードと異なる。 これにより、 第 3動作モードでは、 エアタンク 3 0内の圧縮乾燥空気を、 供給回路 1 2及 びバイパス流路 2 0を介して、 フィルタ 1 7に通過させることができる。 そ のため、 フィルタ 1 7を浄化する効果が第 2動作モードよりも高い。 また、 第 3動作モードでも、 フィルタ 1 7及び空気供給通路 1 8の空気圧が大気圧 に開放される。 As shown in Fig. 20, the third operation mode is a mode for performing the reproduction operation for reproducing the filter 17. In the third operation mode, the regeneration control valve 21 is opened, the governor 26 is set as the input position, and the unload control valve 26 is set as the supply position (indicated as "○" in each figure). ). At this time, power is supplied to the regeneration control valve 2 1 in addition to the governor 26 8 and the inlet control valve 26 6. In the third operation mode, the compressor 4 is deactivated and the compressed dry air stored in the supply circuit 12 or the air tank 30 is caused to flow back to the filter 17 and is discharged from the drain outlet 27. Let As a result, the water and the like captured by the filter 17 are removed. The second operation mode and the third operation mode are both modes for purifying the filter 17, but the third operation mode is different from the second operation mode in that the regeneration control valve 21 is opened at least. different. Thus, in the third operation mode, the compressed dry air in the air tank 30 can be passed through the supply circuit 12 and the bypass passage 20 to the filter 17. Therefore, the effect of cleaning the filter 17 is higher than that of the second operation mode. Also in the third operation mode, the air pressure in the filter 17 and the air supply passage 18 is released to the atmospheric pressure.

[0052] (第 4動作モード) [0052] (Fourth operation mode)

図 2 0に示すように、 第 4動作モードは、 オイルカッ ト動作を行うモード 〇 2020/175470 15 卩(:171? 2020 /007469 As shown in Fig. 20, the fourth operation mode is the oil cut operation mode. 〇 2020/175 470 15 卩(:171? 2020/007469

である。 第 4動作モードでは、 コンブレッサ 4を稼働させながら、 コンプレ ッサ 4から送られた油分過多な空気を、 フィルタ 1 7を通過させることなく ドレン排出口 2 7から排出する。 コンブレッサ 4が非稼働状態である場合、 コンブレッサ 4の圧縮室に油分が溜まることがある。 圧縮室内に油分が溜ま った状態でコンブレッサ 4の状態が稼働状態に切り替えられると、 圧縮室か ら送られる圧縮空気に含まれる油分量が多くなる。 油分が乾燥剤に付着する と、 乾燥剤の除湿性能が低下する。 そのため、 油分過多な圧縮空気を排出す るオイルカッ ト動作が実行される。 第 4動作モードでは、 再生制御弁 2 1 を 閉弁し、 アンロード制御弁 2 6 Bを開放位置 (図において 「C L O S E」 と 記載) とするとともに、 ガバナ 2 6 Aを一定期間の駆動後に開放位置とする (図において 「C L O S E」 と記載) 。 これにより、 コンブレッサ 4から比 較的多くの油分を含む圧縮空気が送出されても、 その圧縮空気をフィルタ 1 7に通過させることなく、 ドレン排出口 2 7から排出することができる。 し たがって、 コンブレッサ 4が非稼働状態から稼働状態へ切り替えられた直後 にフィルタ 1 7の除湿性能が低下することを抑制することができる。 稼働状 態でエンジン回転数が大きくなるとき及びエンジンの高負荷時等にコンブレ ッサ 4からの油分が増加するときには、 オイルカッ ト動作を行うこともでき る。 Is. In the fourth operation mode, while the compressor 4 is operating, the excess oil air sent from the compressor 4 is discharged from the drain outlet 27 without passing through the filter 17. When the compressor 4 is not in operation, oil may accumulate in the compression chamber of the compressor 4. When the state of the compressor 4 is switched to the operating state while the oil is accumulated in the compression chamber, the amount of oil contained in the compressed air sent from the compression chamber increases. When oil adheres to the desiccant, the dehumidification performance of the desiccant decreases. Therefore, the oil cut operation is performed to discharge the compressed air that contains too much oil. In the fourth operation mode, the regeneration control valve 21 is closed, the unload control valve 26B is in the open position (denoted as "CLOSE" in the figure), and the governor 26A is opened after a certain period of operation. Position (marked as “CLOSE” in the figure). As a result, even if compressed air containing a relatively large amount of oil is sent out from the compressor 4, the compressed air can be discharged from the drain outlet 27 without passing through the filter 17. Therefore, it is possible to prevent the dehumidification performance of the filter 17 from decreasing immediately after the combustor 4 is switched from the non-operating state to the operating state. The oil cutting operation can also be performed when the engine speed increases in the operating state and when the oil content from the compressor 4 increases when the engine is under heavy load.

[0053] (第 5動作モード) [0053] (Fifth Operation Mode)

図 2 Eに示すように、 第 5動作モードは、 パージ無しのコンブレッサ停止 動作を行うモードである。 第 5動作モードでは、 再生制御弁 2 1 を閉弁し、 ガバナ 2 6 Aを開放位置 (図において 「C L O S E」 と記載) とするととも に、 アンロード制御弁 2 6 Bを供給位置 (図において 「O P E N」 と記載) とする。 第 5動作モードでは、 コンブレッサ 4が非稼働状態であるとき、 空 気供給通路 1 8又はフィルタ 1 7の乾燥剤中に残留する圧縮空気又は圧縮乾 燥空気をドレン排出口 2 7から排出させないことで空気圧が維持される。 As shown in Fig. 2E, the fifth operation mode is a mode in which the compressor stops without purging. In the fifth operation mode, the regeneration control valve 21 is closed, the governor 26A is in the open position (indicated as "CLOSE" in the figure), and the unload control valve 26B is in the supply position (see the figure). "OPEN"). In the fifth operation mode, when the compressor 4 is not operating, the compressed air or the compressed dry air remaining in the desiccant in the air supply passage 18 or the filter 17 should not be discharged from the drain outlet 27. The air pressure is maintained at.

[0054] (第 6動作モード) [0054] (Sixth operation mode)

図 2 Fに示すように、 第 6動作モードは、 与圧処理のためにアシスト動作 〇 2020/175470 16 卩(:171? 2020 /007469 As shown in Fig. 2F, the sixth operation mode is the assist operation for pressurization processing. 〇 2020/175 470 16 卩(:171? 2020/007469

を行うモードである。 第 6動作モードでは、 再生制御弁 2 1 を開弁し、 アン 口ード制御弁 26 Bを供給位置 (図において 「O P E N」 と記載) とすると ともに、 ガバナ 26 Aを開放位置 (図において 「CLOS E」 と記載) とす る。 第 6動作モードでは、 コンブレッサ 4が非稼働状態であるとき、 空気供 給通路 1 8及びフィルタ 1 7の乾燥剤中に供給回路 1 2の圧縮空気を供給す る (逆流させる) ことで、 空気供給通路 1 8及びフィルタ 1 7の圧力を大気 圧よりも高く して、 上流チェックバルブ 1 5の背圧 (空気圧) を大気圧より も高い圧力に維持させる。 It is a mode to do. In the sixth operation mode, the regeneration control valve 21 is opened, the inlet control valve 26 B is set to the supply position (indicated as “OPEN” in the figure), and the governor 26 A is set to the open position (in the figure, CLOS E”). In the sixth operation mode, when the compressor 4 is in the non-operational state, the compressed air in the supply circuit 12 is supplied (backflowed) into the desiccant in the air supply passage 18 and the filter 17 to generate air. The pressure in the supply passage 18 and the filter 17 is made higher than the atmospheric pressure to maintain the back pressure (air pressure) of the upstream check valve 15 at a pressure higher than the atmospheric pressure.

[0055] (実行条件の設定) [0055] (Setting execution conditions)

次に図 3を参照して、 再生動作 (第 3動作モード) で消費される空気量 ( 以下、 再生空気量という) の決定方法について説明する。 ECU 80は、 制 御プログラムを実行することにより、 再生空気量 Amを、 以下の式 (1) に したがって算出する。 なお、 再生空気量 Amは、 体積単位で算出されても質 量単位で算出されてもよい。 なお、 この式 (1) の右辺 (又は左辺) に単位 を変換する各種の係数を用いてもよい。 Next, with reference to FIG. 3, a method of determining the amount of air consumed in the regeneration operation (third operation mode) (hereinafter referred to as the amount of regeneration air) will be described. The ECU 80 executes the control program to calculate the regeneration air amount Am according to the following equation (1). The amount of regenerated air Am may be calculated in volume units or mass units. Note that various coefficients for converting the unit may be used for the right side (or the left side) of this equation (1).

[0056] 再生空気量 Am [0056] Regenerated air volume Am

=標準再生空気量 Am 1 _補正単位空気量 A m2X過不足係数 a (1) なお、 「標準再生空気量 A m 1」 は、 「補正単位空気量 A m 2 X過不足係 数 a」 よりも大きくなるように設定されており、 再生空気量 Amが 「0」 を 超えるようになっている。 標準再生空気量 Am 1は、 基本的に空気乾燥回路 1 1の仕様 (スペック) で決められる空気量であるが、 エアタンク 30の圧 力の上限値であるカッ トアウト圧に応じて変更される。 上述したようにカッ トアウト圧は、 再生動作及びパージ動作が開始される条件となる圧力であり 、 コンブレッサ 4の稼働率が高いほど、 高い値が設定され、 記憶部 80 Aに 記憶されている。 例えば、 稼働率が所定値 R 1 (例えば 30%) 未満では、 相対的に低い値であるカッ トアウト圧 P〇 1が設定され、 稼働率が所定値 R 1以上所定値 R 2 (例えば 60%) 未満では、 カッ トアウト圧 P o 1 よりも 高いカッ トアウト圧 P〇 2が設定されている (P〇 2>P〇 1) 。 さらに、 〇 2020/175470 17 卩(:171? 2020 /007469 = Standard regeneration air volume Am 1 _ correction unit air volume A m2 X excess/deficiency coefficient a (1) Note that “standard regeneration air volume A m 1” is calculated from “correction unit air volume A m 2 X excess/deficiency coefficient a”. Is also set to be large, and the amount of regenerated air Am exceeds “0”. The standard regeneration air volume Am 1 is basically the air volume determined by the specifications of the air drying circuit 11 but is changed according to the cutout pressure which is the upper limit of the pressure of the air tank 30. As described above, the cutout pressure is the pressure that is the condition for starting the regeneration operation and the purge operation, and the higher the operating rate of the compressor 4, the higher the value is set and stored in the storage unit 80A. For example, if the operating rate is less than the specified value R 1 (for example, 30%), the cutout pressure P○ 1 that is a relatively low value is set, and the operating rate is the specified value R 1 or more and the specified value R 2 (for example, 60%. ) Below, a cutout pressure P 〇 2 higher than the cutout pressure P o 1 is set (P 〇 2>P 〇 1). further, 〇 2020/175 470 17 卩 (:171? 2020 /007469

稼働率が所定値 2以上では、 カッ トアウト圧 〇 2よりも高いカッ トアウ 卜圧 〇 3が設定されている (?〇 3> 〇 2) 。 本実施形態では、 カッ ト アウト圧を、 コンブレッサ 4の稼働率に応じて 3段階に設定しているが、 こ れを 2段階に設定してもよく、 4つ以上の段階で設定してもよい。 又は、 コ ンプレッサ 4の稼働率に応じて、 カッ トアウト圧を連続的に変化させてもよ い。 When the operating rate is 2 or more, the cutout pressure is higher than the cutout pressure, and the cutout pressure is set to 0 (3). In the present embodiment, the cutout pressure is set in three stages according to the operating rate of the compressor 4, but it may be set in two stages or in four or more stages. Good. Alternatively, the cutout pressure may be continuously changed according to the operating rate of the compressor 4.

[0057] カッ トアウト圧 〇をコンブレッサ 4の稼働率が高くなるに伴い高くする 理由について説明する。 コンブレッサ 4は、 エアタンク 3 0内の圧縮乾燥空 気の量等に応じて駆動されるため、 その稼働率が低い場合には、 ブレーキシ ステム等の空気圧システムによる圧縮乾燥空気の消費量が比較的少ない状況 下にあると推定される。 このような状況では、 カッ トアウト圧を相対的に低 い値にして、 再生動作の実行頻度を相対的に高く し、 フィルタ 1 7の清浄化 を積極的に行う。 一方、 コンブレッサ 4の稼働率が高い場合には、 ブレーキ システム等の空気圧システムによる圧縮乾燥空気の消費量が比較的多い状況 下にあると推定される。 このような状況では、 カッ トアウト圧を相対的に高 い値にして、 再生動作の実行頻度を相対的に低く し、 空気圧システムへの圧 縮乾燥空気の供給を優先する。 [0057] The reason why the cutout pressure ◯ is increased as the operating rate of the compresser 4 is increased will be described. Since the compressor 4 is driven according to the amount of compressed dry air in the air tank 30 and the like, when the operating rate is low, the compressed dry air consumption by the pneumatic system such as the brake system is relatively low. It is estimated that the situation is under. In such a situation, the cutout pressure is set to a relatively low value, the frequency of regenerating operation is set to be relatively high, and the filter 17 is actively cleaned. On the other hand, when the operating rate of the Compressor 4 is high, it is estimated that the compressed dry air consumption by the pneumatic system such as the brake system is relatively high. In such a situation, the cutout pressure is set to a relatively high value, the frequency of regeneration operation is performed relatively low, and the supply of compressed dry air to the pneumatic system is prioritized.

[0058] 図 3八は、 標準再生空気量八〇! 1 を、 限界通気量及びカッ トアウト圧に応 じて設定したマップ 1 0 0である。 このマップ 1 0 0は、 記憶部 8 0八に記 憶されている。 マップ 1 0 0の横軸は限界通気量であり、 縦軸は標準再生空 気量八 01 1である。 図では単位は体積 (リッ トル) であるが、 単位が質量で あってもよい。 限界通気量は、 空気乾燥回路 1 1 を通過する空気量の限界を 示す値であり、 空気乾燥回路 1 1 (エアドライヤ) の仕様に応じて決まる量 である。 標準再生空気量八0! 1は、 限界通気量が大きくなるに伴い小さくな り、 限界通気量が小さくなるに伴い大きくなる。 また、 標準再生空気量八 0! 1は、 限界通気量を一定としたとき、 カッ トアウト圧が高くなるに伴い小さ くなり、 カッ トアウト圧が低くなるに伴い大きくなる。 つまり、 カッ トアウ 卜圧にはコンブレッサ 4の稼働率が高くなるに伴い高い値が設定されている 〇 2020/175470 18 卩(:171? 2020 /007469 [0058] Fig. 38 shows a map 100 in which the standard regeneration air amount 80! 1 is set according to the limit ventilation amount and the cutout pressure. This map 100 is stored in the storage unit 808. The horizontal axis of the map 100 is the limit air flow rate, and the vertical axis is the standard regeneration air volume 81 01. In the figure, the unit is volume (liter), but the unit may be mass. The limit air flow rate is a value that indicates the limit of the amount of air that passes through the air drying circuit 11 and is determined according to the specifications of the air drying circuit 11 (air dryer). The standard regeneration air volume 80!1 decreases as the critical air flow rate increases, and increases as the critical air flow rate decreases. Further, the standard regeneration air volume 80!1 becomes smaller as the cutout pressure becomes higher, and becomes larger as the cutout pressure becomes lower, when the limit air flow rate is constant. In other words, the cutout pressure is set to a high value as the operating rate of the Compressor 4 increases. 〇 2020/175 470 18 卩 (: 171? 2020 /007469

ので、 標準再生空気量八〇1 1は、 コンブレッサ 4の稼働率が高くなるに伴い 小さくなるといえる。 上述したように、 コンブレッサ 4の稼働率が高い場合 には、 ブレーキシステム等の空気圧システムによる圧縮乾燥空気の消費量が 比較的多い状況下にあると推定される。 このため、 コンブレッサ 4の稼働率 が高い場合には、 標準再生空気量八 1 を小さく して、 空気圧システムへ圧 縮乾燥空気を供給することを優先する。 また、 標準再生空気量 1は、 コ ンプレッサ 4の稼働率が低くなるに伴い大きくなる。 稼働率が低い場合には 、 ブレーキシステム等の空気圧システムによる圧縮乾燥空気の消費量が比較 的少ない状況下にあると推定される。 このため、 コンブレッサ 4の稼働率が 低い場合には、 標準再生空気量 0! 1 を大きく して、 1回の再生動作あたり のフィルタ 1 7の清浄効果を高める。 Therefore, it can be said that the standard regeneration air volume of 81 1 decreases as the operating rate of the Combressa 4 increases. As mentioned above, when the operating rate of the compressor 4 is high, it is estimated that the compressed dry air consumption by the pneumatic system such as the brake system is relatively high. For this reason, when the operating rate of the compressor 4 is high, it is prioritized to reduce the standard regeneration air volume 81 and supply compressed dry air to the pneumatic system. Also, the standard regeneration air volume 1 increases as the operating rate of the compressor 4 decreases. If the operating rate is low, it is estimated that the compressed dry air consumption by the pneumatic system such as the brake system is relatively small. Therefore, when the operating rate of the compressor 4 is low, the standard regeneration air volume 0! 1 is increased to enhance the cleaning effect of the filter 17 per regeneration operation.

[0059] 図 3巳は、 カッ トアウト圧に応じた補正単位空気量八 2と限界通気量と の関係を示しているマップ 1 〇 1である。 このマップ 1 0 1は、 記憶部 8 0 八に記憶されている。 横軸が限界通気量、 縦軸が補正単位空気量 2であ る。 図では単位は体積 (リッ トル) であるが、 単位が質量であってもよい。 補正単位空気量 0! 2は、 標準再生空気量 0! 1 と同様に限界通気量が大き くなるほど小さくなる一方で、 限界通気量を一定としたとき、 カッ トアウト 圧が高くなるに伴い大きくなり、 カッ トアウト圧が低くなるに伴い小さくな る。 [0059] Fig. 3 is a map 101 showing the relationship between the corrected unit air amount 82 depending on the cutout pressure and the limit ventilation amount. This map 1 0 1 is stored in the storage unit 8 0 8. The horizontal axis is the limit air flow rate, and the vertical axis is the correction unit air volume 2. Although the unit is volume in the figure, the unit may be mass. The corrected unit air volume 0!2 becomes smaller as the limit air flow rate becomes larger like the standard regeneration air volume 0!1, but becomes larger as the cutout pressure becomes higher when the limit air volume is constant. , It becomes smaller as the cutout pressure becomes lower.

[0060] 過不足係数《 (再生過不足係数) は、 補正単位空気量

Figure imgf000020_0001
に乗算される 係数であり、 負の値、 正の値又は 「0」 に設定されている。 この過不足係数 «は、 エアタンク 3 0内に貯留された圧縮乾燥空気の湿潤状態の傾向に基づ き設定されるものである。 再生動作の過不足は、 フィルタ 1 7によって捕捉 された水分量によって判定することができるが、 圧縮空気に含まれる水分量 は空気の温度や湿度によって変化するため、 フィルタ 1 7によって捕捉され た水分量を、 再生動作の実行時間やフィルタ 1 7を通過した空気量だけを用 いて推定するのは困難である。 また、 フィルタ 1 7によって捕捉された水分 量を直接的に計測することも困難である。 本実施形態のように、 貯留部内の 〇 2020/175470 19 卩(:171? 2020 /007469 [0060] The excess/deficiency coefficient << (regeneration excess/deficiency coefficient) is the correction unit air amount.
Figure imgf000020_0001
Is a coefficient that is multiplied by and is set to a negative value, a positive value or "0". This excess/deficiency coefficient is set based on the tendency of the compressed dry air stored in the air tank 30 to be in a wet state. The excess or deficiency of the regeneration operation can be determined by the amount of water captured by the filter 17, but the amount of water contained in the compressed air changes depending on the temperature and humidity of the air, so the amount of water captured by the filter 17 can be determined. It is difficult to estimate the amount using only the execution time of the regeneration operation and the amount of air that has passed through the filter 17. It is also difficult to directly measure the amount of water captured by the filter 17. As in this embodiment, 〇 2020/175 470 19 卩(:171? 2020/007469

圧縮乾燥空気の湿潤状態に基づき再生動作の過不足を判定することによって 、 再生動作の過不足を間接的ではあっても適切に判定することができる。 By determining the excess or deficiency of the regeneration operation based on the wet state of the compressed dry air, the excess or deficiency of the regeneration operation can be appropriately determined indirectly.

[0061 ] 過不足係数《の根拠となる湿潤状態の傾向は、 前回行われた再生動作から 次の再生動作を行う前までの期間を対象として判定される。 また、 湿潤状態 を判定するための指標は限定されないが、 本実施形態ではエアタンク 3 0内 の圧縮乾燥空気に含有される水分量 (以下、 含有水分量) の飽和度を算出し 、 前回の再生動作の終了時における含有水分量の飽和度から今回の含有水分 量の飽和度を減算する。 前回の再生終了時よりも今回の再生終了時の方が含 有水分量の飽和度が高い場合、 すなわち圧縮乾燥空気の湿潤状態が高まる傾 向にある場合には、 フィルタ 1 7が捕捉している水分量が増加傾向にあると 判定される。 このため、 上記式 (1) において、 過不足係数《は、 「0」 未 満の負の値とされる。 過不足係数《が負の値である場合には、 再生空気量は 標準再生空気量よりも大きくなるように補正される。 The tendency of the wet state, which is the basis of the excess/deficiency coefficient <<, is determined for the period from the previous reproduction operation to the next reproduction operation. In addition, the index for determining the wet state is not limited, but in the present embodiment, the saturation degree of the water content (hereinafter, the water content) contained in the compressed dry air in the air tank 30 is calculated, and the previous regeneration is performed. Subtract the saturation of the moisture content this time from the saturation of the moisture content at the end of the operation. If the saturated moisture content is higher at the end of this regeneration than at the end of the previous regeneration, that is, if the wet state of compressed dry air tends to increase, the filter 17 captures it. It is judged that the water content is increasing. Therefore, in equation (1) above, the excess/deficiency coefficient << is a negative value that is not "0". When the excess/deficiency coefficient << is a negative value, the regeneration air amount is corrected to be larger than the standard regeneration air amount.

[0062] _方、 前回の再生終了時よりも今回の再生終了時の方が含有水分量の飽和 度が低い場合、 すなわち圧縮乾燥空気の湿潤状態が低下する傾向にある場合 には、 フィルタ 1 7が捕捉している水分量が減少傾向にあると判定される。 このため、 過不足係数《は、 「0」 よりも大きい正の値とされ、 再生空気量 は標準再生空気量よりも小さくなるように補正される。 また、 圧縮乾燥空気 の湿潤状態が適した状態にあると判定した場合には、 過不足係数は 「〇」 と され、 再生空気量 01は標準再生空気量 01 1から補正されない。 [0062] On the other hand, if the saturation of the water content at the end of this regeneration is lower than that at the end of the previous regeneration, that is, if the wet state of compressed dry air tends to decrease, the filter 1 It is judged that the amount of water captured by 7 tends to decrease. Therefore, the excess/deficiency coefficient << is set to a positive value larger than "0", and the regenerated air amount is corrected to be smaller than the standard regenerated air amount. When it is determined that the compressed dry air is in a suitable wet state, the excess/deficiency coefficient is set to “◯” and the regenerated air amount 01 is not corrected from the standard regenerated air amount 01 1.

[0063] 図 4は、 過不足係数《の一例を示す過不足係数情報 2 0 0である。 過不足 係数情報 2 0 0は、 記憶部 8 0 に記憶されている。 過不足係数情報 2 0 0 は、 過不足条件 2 0 0 、 過不足係数 2 0 0(3を含んでいる。 状態 2 0 0巳 は、 過不足条件 2 0 0 が示す状態を便宜的に示したものであり、 省略可能 である。 過不足条件 2 0 0 には、 再生過不足度の範囲が設定されている。 再生過不足度は、 エアタンク 3 0内の圧縮乾燥空気に含まれる水分の飽和度 が、 増加傾向にあるか減少傾向にあるかを示す指標である。 FIG. 4 is excess/deficiency coefficient information 200 showing an example of excess/deficiency coefficient <<. The excess/deficiency coefficient information 200 is stored in the storage unit 80. The excess/deficiency coefficient information 200 includes the excess/deficiency condition 200, and the excess/deficiency coefficient 200(3. State 2 00 0 indicates the state indicated by the excess/deficiency condition 2 0 0 for convenience. The range of regeneration excess/deficiency is set in the excess/deficiency condition 200. The regeneration excess/deficiency indicates the amount of water contained in the compressed dry air in the air tank 30. It is an index that indicates whether the degree of saturation is increasing or decreasing.

[0064] 過不足係数 2 0 0(3は、 再生過不足度に重み付け係数を乗算したものであ 〇 2020/175470 20 卩(:171? 2020 /007469 [0064] The excess/deficiency coefficient 200 (3 is the reproduction excess/deficiency multiplied by the weighting coefficient. 〇 2020/175 470 20 卩 (:171? 2020 /007469

る。 過不足係数 1 0 3は、 再生過不足度の範囲である過不足条件 2 0 0八に それぞれ対応している。 なお、 図 4では重み付け係数を正の整数としている が、 正の整数でなくてもよい。 It The excess/deficiency coefficient 103 corresponds to the excess/deficiency condition 208, which is the range of the reproduction excess/deficiency. Although the weighting coefficient is a positive integer in FIG. 4, it does not have to be a positive integer.

[0065] 過不足係数情報 2 0 0において、 再生空気量が大幅に不足している場合、 すなわち含有水分量が大きい場合は、 再生過不足度が、 例えば 「_ 1」 以下 であり、 負の値であって且つ絶対値が大きい。 この場合には、 重み付け係数 も、 例えば 「2」 等の相対的に大きい値が設定されている。 また、 「大幅に 不足」 とまではいえなくとも再生空気量が不足している場合には、 再生過不 足度は、 例えば 「_ 1」 よりも大きく 「_ 0 . 5」 よりも小さい範囲であっ て、 「大幅に不足」 よりも絶対値が小さい。 また、 重み付け係数の値も、 例 えば 「1」 など、 「大幅に不足」 よりも小さい値が設定されている。 [0065] In the excess/deficiency coefficient information 200, when the regeneration air amount is significantly insufficient, that is, when the water content is large, the regeneration excess/deficiency degree is, for example, "_ 1" or less, which is a negative value. It is a value and its absolute value is large. In this case, the weighting coefficient is also set to a relatively large value such as “2”. In addition, if the amount of regeneration air is insufficient, even if it cannot be said to be “significantly insufficient,” the regeneration insufficient degree is, for example, greater than “_ 1” and less than “_ 0.5”. However, the absolute value is smaller than the "significant lack". Also, the value of the weighting coefficient is set to a value smaller than "significantly insufficient" such as "1".

[0066] また、 再生空気量が大幅に過剰である場合、 すなわち含有水分量が小さい 場合は、 再生過不足度が、 例えば 「1」 以上であり、 正の値であって且つ絶 対値が大きい。 この場合には、 重み付け係数にも例えば 「2」 等の相対的に 大きい値が設定されている。 また、 「大幅に過剰」 とまではいえなくとも再 生空気量が過剰である場合には、 再生過不足度は、 例えば 「0 . 5」 以上で あり 「 1」 よりも小さい範囲であって、 「大幅に過剰」 よりも絶対値が小さ い。 また、 重み付け係数の値も、 例えば 「1」 など、 「大幅に不足」 よりも 小さい値が設定されている。 [0066] Further, when the amount of regenerated air is significantly excessive, that is, when the water content is small, the regeneration excess/deficiency degree is, for example, "1" or more, and the positive value and absolute value are large. In this case, the weighting coefficient is also set to a relatively large value such as “2”. In addition, if the amount of regenerated air is excessive even if it cannot be said to be “significantly excessive,” the regeneration excess/deficiency is, for example, “0.5” or more, which is less than “1”. , The absolute value is smaller than that of "significant excess". Also, the value of the weighting coefficient is set to a value smaller than "significantly insufficient" such as "1".

[0067] 再生過不足度が、 例えば 「一〇. 5」 以上 「0 . 5」 未満の範囲である場 合には、 過不足係数には 「0」 が設定されている。 [0067] When the reproduction excess/deficiency is in a range of, for example, "10. 5" or more and less than "0.5", the excess/deficiency coefficient is set to "0".

これらの標準再生空気量、 補正単位空気量、 及び過不足係数を用いて算出 される再生空気量八 について、 コンブレッサ 4の稼働率が低い場合及び高 い場合と、 エアタンク 3 0内の湿潤状態が低い場合及び高い場合にと場合分 けして説明する。 なお、 限界通気量は一定であることを前提とする。 With respect to the regenerated air volume calculated using these standard regenerated air volume, corrected unit air volume, and excess/deficiency coefficient, the wet state in the air tank 30 is shown when the operating rate of the compressor 4 is low and high. The explanation will be made separately for the case of low and the case of high. It is assumed that the limit ventilation is constant.

[0068] (八) コンブレッサ 4の稼働率:低、 エアタンク 3 0内の湿潤状態:高 コンブレッサ 4の稼働率が低い場合、 カッ トアウト圧は低く設定される。 これにより、 再生動作及びパージ動作の実行頻度は高められる。 また、 標準 \¥0 2020/175470 21 卩(:17 2020 /007469 [0068] (8) Comblator 4 operating rate: low, wet condition in air tank 30: high If the operating rate of the combustor 4 is low, the cutout pressure is set low. As a result, the frequency of execution of the regeneration operation and the purging operation is increased. Also the standard \\0 2020/175 470 21 (: 17 2020/007469

再生空気量 1は、 カッ トアウト圧が低く設定されることにより大きくな る。 The regenerated air volume 1 increases as the cutout pressure is set low.

[0069] さらに、 補正単位空気量 〇! 2は、 カッ トアウト圧が低く設定されること により小さくなる。 また、 過不足係数《は、 エアタンク 3 0内の湿潤状態が 高いため、 「大幅不足」 又は 「不足」 の状態となり、 負の値となる。 このた め、 標準再生空気量に、 正の値の補正値が加算され、 再生空気量 01は大き くなる。 なお、 「大幅不足」 の状態の方が、 「不足」 の状態よりも再生空気 量八 01は大きくなる。 [0069] Further, the correction unit air amount 〇!2 becomes smaller by setting the cutout pressure low. Further, the excess/deficiency coefficient << becomes a "significantly insufficient" or "insufficient" state, which is a negative value, because the wet state in the air tank 30 is high. Therefore, a positive correction value is added to the standard regeneration air volume, and the regeneration air volume 01 becomes large. In addition, the amount of regeneration air in the “largely shortage” state is larger than that in the “shortage” state.

[0070] (巳) コンブレッサ 4の稼働率:低、 エアタンク 3 0内の湿潤状態:低

Figure imgf000023_0001
上記の状態 ( ) と 同様である。 一方、 過不足係数《は、 エアタンク 3 0内の湿潤状態が低いた め、 「大幅過剰」 又は 「過剰」 の状態となり、 正の値となる。 このため、 標 準再生空気量から補正値が減算され、 状態 ( ) の再生空気量 01に比べ、 再生空気量八 01が小さくなる。 [0070] (Mitsumi) Comblator 4 operation rate: low, air tank 30 wet condition: low
Figure imgf000023_0001
It is similar to the above state (). On the other hand, the excess/deficiency coefficient << is a "significant excess" or "excessive" state because the wet state in the air tank 30 is low, and is a positive value. Therefore, the correction value is subtracted from the standard regenerated air amount, and the regenerated air amount 801 becomes smaller than the regenerated air amount 01 in the state ().

[0071 ] (〇 コンブレッサ 4の稼働率:高、 エアタンク 3 0内の湿潤状態:高 コンブレッサ 4の稼働率が高い場合、 カッ トアウト圧は高く設定される。 これにより、 再生動作及びパージ動作の実行頻度が低くなる。 また、 標準再 生空気量八 1は、 カッ トアウト圧が高く設定されることにより小さくなる [0071] (○ Comblator 4 operating rate: high, wet condition in air tank 30: high When the operating rate of the compressor 4 is high, the cutout pressure is set high. In addition, the standard regeneration air volume 81 becomes smaller due to the higher cutout pressure.

[0072] さらに、 補正単位空気量八 2は、 カッ トアウト圧が高く設定されること により大きくなる。 また、 過不足係数《は、 エアタンク 3 0内の湿潤状態が 高いため、 「大幅不足」 又は 「不足」 の状態となり、 負の値となる。 このた め、 標準再生空気量に、 正の値の補正値が加算されるが、 状態 ( ) の再生 空気量 に比べ、 再生空気量 〇!は小さくなる。 なお、 状態 (〇 の再生 空気量 01は、 状態 (巳) の再生空気量 01に比べて小さくてもよいし、 大 きくてもよい。 また、 状態 (巳) の再生空気量 0!及び状態 ((3) の再生空 気量八 01は同じであってもよい。 [0072] Further, the correction unit air amount 82 is increased by setting the cutout pressure high. Further, the excess/deficiency coefficient << becomes a "significantly insufficient" or "insufficient" state, which is a negative value, because the wet state in the air tank 30 is high. For this reason, a positive correction value is added to the standard regenerated air amount, but the regenerated air amount ◯! becomes smaller than the regenerated air amount in state (). It should be noted that the regenerated air amount 01 in the state (○) may be smaller or larger than the regenerated air amount 01 in the state (Min). Also, the regenerated air amount 0 in the state (Min) and the state (The regeneration air volume in (3) 801 may be the same.

[0073] (0) コンブレッサ 4の稼働率:高、 エアタンク 3 0内の湿潤状態:低 〇 2020/175470 22 卩(:171? 2020 /007469 [0073] (0) Comblator 4 operating rate: high, wet condition in air tank 30: low 〇 2020/175 470 22 卩 (:171? 2020 /007469

標準再生空気量 〇! 1及び補正単位空気量 0^ 2は、 上記の状態 (〇 と 同様である。 一方、 過不足係数《は、 エアタンク 3 0内の湿潤状態が低いた め、 「大幅過剰」 又は 「過剰」 の状態となり、 正の値となる。 このため、 標 準再生空気量から補正値が減算され、 状態 (<3) の再生空気量 0!に比べ、 再生空気量 が小さくなる。 つまり、 過不足係数《の設定値にもよるが、 基本的に、 再生空気量 0!は、 状態 ( ) の場合が最も大きく、 状態 (口) の場合が最も小さい。 The standard regeneration air volume ◯! 1 and the correction unit air volume 0^2 are the same as the above conditions (◯). On the other hand, the excess/deficiency coefficient << is because the wet state in the air tank 30 is low, "Or" Excess" and becomes a positive value. Therefore, the correction value is subtracted from the standard regenerated air amount, and the regenerated air amount becomes smaller than the regenerated air amount 0! in the state (<3). In other words, depending on the set value of the excess/deficiency coefficient, basically, the regenerated air volume 0! is the largest in the state () and the smallest in the state (mouth).

[0074] (空気乾燥回路 1 1の制御) [0074] (Control of air drying circuit 11)

次に図 5〜図 7を参照して、 º01\80が空気乾燥回路 1 1 を制御する手 順について説明する。 Next, with reference to FIG. 5 to FIG. 7, the procedure by which the control unit 80 controls the air drying circuit 11 will be described.

[0075] 図 5を参照して、 全体的な制御の手順について説明する。 巳〇 II 8 0は、 コンプレッサ 4の出力する圧縮空気を供給回路 1 2に供給する空気供給工程 を行う (ステップ 3 1) 。 空気供給工程は、 例えばエンジンが駆動されたと き等、 所定の条件で開始される。 また、 空気供給工程は、 エアタンク 3 0の 圧力が、 下限値であるカッ トイン圧力等の所定圧力に到達したとき等に開始 されてもよい。 空気供給工程では、 空気乾燥回路 1 1が第 1動作モードにあ り、 除湿動作を実行している。 [0075] With reference to Fig. 5, an overall control procedure will be described. The MII II 80 performs the air supply process of supplying the compressed air output from the compressor 4 to the supply circuit 12 (step 31). The air supply process is started under predetermined conditions such as when the engine is driven. The air supply process may be started when the pressure in the air tank 30 reaches a predetermined pressure such as the cut-in pressure which is the lower limit value. In the air supply process, the air drying circuit 11 is in the first operation mode and is performing the dehumidifying operation.

[0076] 空気供給工程が開始されると、 日(3 11 8 0は、 空気の供給を停止するか否 かを判断する (ステップ 3 2) 。 詳述すると、 巳〇11 8 0は、 圧カセンサ 5 3が検出したエアタンク 3 0内の圧力を取得し、 圧力がカッ トアウト圧に到 達したか否かを判断する。 巳〇 II 8 0が、 エアタンク 3 0内の圧力がカッ ト アウト圧に到達していないと判断すると (ステップ 3 2 : N0) 、 処理を空 気供給工程に戻す (ステップ 3 1) 。 [0076] When the air supply process is started, the day (3 1 180) determines whether or not to stop the air supply (step 3 2). The pressure in the air tank 30 detected by the sensor 5 3 is acquired and it is determined whether or not the pressure reaches the cutout pressure.MII 〇 II 80 indicates that the pressure in the air tank 30 is the cutout pressure. When it is judged that the temperature has not reached (step 32: N0), the process is returned to the air supply process (step 31).

[0077] 巳〇 II 8 0は、 エアタンク 3 0内の圧力がカッ トアウト圧に到達したと判 断すると (ステップ 3 2 : 丫巳3) 、 空気供給工程を終了し、 コンブレッサ 4を非稼働状態にさせるとともに、 浄化工程を実行する (ステップ 3 3) 。 浄化工程では、 巳(3 11 8 0は、 予め設定された条件にしたがって、 再生動作 及びパージ動作の要否を判定し、 再生動作が必要であると判定すると、 再生 〇 2020/175470 23 卩(:171? 2020 /007469 [0077] When it is judged that the pressure in the air tank 30 has reached the cutout pressure (Step 3 2 :Mimi 3), the Ⅱ II 80 finishes the air supply process and puts the compressor 4 into the non-operational state. And perform the purification process (step 33). In the cleaning process, the (311800 determines whether or not the regenerating operation and the purging operation are necessary according to the preset conditions. 〇 2020/175 470 23 卩 (:171? 2020 /007469

動作を実行し、 パージ動作が必要であると判定するとパージ動作を実行する Execute the operation and execute the purge operation when it is determined that the purge operation is necessary

[0078] 浄化工程 (ステップ 33) が終了すると、 巳(31180は、 空気非供給工程 を行う (ステップ 34) 。 空気非供給工程では、 コンブレッサ 4が非稼働状 態であるときに、 上流チェックバルブ 1 5の背圧の調整等、 空気乾燥回路 1 1の圧力調整を行う。 例えば、 空気非供給工程では、 第 2動作モード、 第 5 動作モード、 及び第 6動作モードの少なくとも一つを 1乃至複数回実行して 空気乾燥回路 1 1の空気圧の調整を行う。 圧力調整が終了すると、 º01\8 0は、 車両状態に基づいて、 空気供給を終了するか否かを判断する (ステッ プ35) 。 空気供給の終了は、 例えば、 車両のエンジン停止等の車両状態に 基づいて判定される。 [0078] When the cleaning process (step 33) is completed, the process (31180 performs the air non-supplying process (step 34).) In the air non-supplying process, the upstream check valve is operated when the compressor 4 is in the non-operating state. Adjust the pressure of the air drying circuit 11 such as adjusting the back pressure of 15. For example, in the air non-supply process, at least one of the second operation mode, the fifth operation mode, and the sixth operation mode is set to 1 to Execute multiple times to adjust the air pressure in the air drying circuit 11. When the pressure adjustment is completed, º01\80 determines whether or not to stop the air supply based on the vehicle condition (step 35). ) The end of the air supply is determined based on the vehicle state such as the engine stop of the vehicle.

[0079] 空気供給を終了しないと判定した場合 (ステップ 35 : N0) 、 º0^8 [0079] When it is determined that the air supply is not terminated (step 35: N0), º0^8

0は、 ステップ 31 に処理を戻し、 空気供給工程 (ステップ 31) 以下の処 理を実行する。 一方、 空気供給を終了すると判定した場合 (ステップ 35 : 丫巳3) 、 空気の供給を停止する。 If 0, the process is returned to step 31, and the following processes of the air supply process (step 31) are executed. On the other hand, when it is determined that the air supply is to be ended (step 35: No. 3), the air supply is stopped.

[0080] 次に図 6を参照して、 再生動作の制御の手順について説明する。 巳〇118 Next, with reference to FIG. 6, a procedure of controlling the reproducing operation will be described. Mitsu 118

0は、 予め決められた条件にしたがって、 再生動作が必要であるか否かを判 断する (ステップ 31 00) 。 このとき、 巳〇1180は、 エアタンク 30内 の圧縮乾燥空気の湿潤状態に基づいて再生動作の要否を判断する。 例えば、 巳〇 II 80は、 エアタンク 30内の圧縮乾燥空気に含まれる水分量 (タンク 含有水分量) を算出し、 タンク含有水分量が所定値以上である場合には、 再 生動作が必要であると判断し、 タンク含有水分量が所定値未満である場合に は、 再生動作が不要であると判断する。 A value of 0 determines whether or not a reproducing operation is necessary according to a predetermined condition (step 3100). At this time, Min 1180 determines whether or not the regenerating operation is necessary based on the wet state of the compressed dry air in the air tank 30. For example, the MII II 80 calculates the amount of water contained in the compressed dry air in the air tank 30 (the amount of water contained in the tank). If the water content in the tank is less than the predetermined value, it is determined that the regenerating operation is unnecessary.

[0081] 巳〇1180は、 再生動作が必要ではないと判断すると (ステップ 31 00 [0081] Michi 1180 judges that the reproducing operation is not necessary (step 31 00

: N0) 、 処理を終了する。 一方、 巳(31180は、 再生動作が必要であると 判断すると (ステップ 31 00 : 丫巳3) 、 決定された再生空気量を取得す る (ステップ 31 01) 。 そして、 巳〇1180は、 取得した再生空気量を用 いて、 空気乾燥回路 1 1 を第 3動作モードに切り替え、 再生動作を実行する 〇 2020/175470 24 卩(:171? 2020 /007469 :N0), end the process. On the other hand, when Mitsumi (31180 determines that the regeneration operation is necessary (Step 31 00: Mimi 3), the determined amount of regeneration air is acquired (Step 31 01). Switch the air drying circuit 1 1 to the 3rd operation mode by using the regenerated air volume and execute the regenerating operation. 〇 2020/175 470 24 卩 (: 171? 2020 /007469

(ステップ 3 1 0 2) 。 ここで、 圧カセンサ 5 3が検出した圧力値の変化を 、 再生動作で消費された空気量に換算して、 換算した空気量が再生空気量に 到達した場合に、 再生動作を終了してもよい。 又は、 再生空気量に対応する 再生時間だけ、 空気乾燥回路 1 1 を第 3動作モードに切り替え、 再生動作を 行ってもよい。 再生時間は、 再生空気量と再生時間とを関連付けたマップを 用いて算出したり、 再生時にフィルタ 1 7を通過する単位時間当たりの空気 量が一定であることを前提に換算式を用いて算出したりしてもよい。 再生動 作が終了すると、 浄化工程 (ステップ 3 3) が終了し、 処理が次のステップ に進められる。 (Step 3 102). Here, the change in the pressure value detected by the pressure sensor 53 is converted into the amount of air consumed in the regenerating operation, and even if the regenerating operation is terminated when the converted air amount reaches the regenerating air amount. Good. Alternatively, the regenerating operation may be performed by switching the air drying circuit 11 1 to the third operation mode for the regenerating time corresponding to the regenerated air amount. The regeneration time is calculated using a map that associates the regeneration air amount with the regeneration time, or is calculated using a conversion formula assuming that the amount of air per unit time that passes through the filter 17 during regeneration is constant. You may do it. When the regeneration operation is completed, the purification process (step 33) is completed and the process proceeds to the next step.

[0082] 次に図 7を参照して、 再生空気量を決定するための処理について説明する 。 なお、 日(3 11 8 0は、 再生動作終了時から、 次の再生動作開始時までを 1 サイクルと定義する。 そして、 1サイクルにおける所定のタイミングで再生 空気量を更新する。 なお、 再生空気量の更新タイミングは特に限定されない 。 例えば、 再生空気量の更新が、 1サイクルの開始時に行われてもよいし、 Next, with reference to FIG. 7, a process for determining the regeneration air amount will be described. In addition, day (3 1 180) is defined as one cycle from the end of the regenerating operation to the start of the next regenerating operation. Then, the regenerated air amount is updated at a predetermined timing in one cycle. The update timing of the amount is not particularly limited, for example, the update of the regeneration air amount may be performed at the start of one cycle,

1サイクルの終了時に行われてもよいし、 1サイクルの開始時と終了時との 間に行われてもよいし、 例えば 1サイクルの平均時間よりも短い期間等、 所 定の期間毎に行われてもよい。 It may be performed at the end of one cycle, between the start and end of one cycle, or at regular intervals such as a period shorter than the average time of one cycle. You may be broken.

[0083] 巳〇11 8 0は、 再生空気量の更新を行うか否かを判断する (ステップ 3 1 [0083] The M1 1 180 determines whether or not the regeneration air amount is updated (step 3 1

1 0) 。 例えば、 巳〇 II 8 0は、 新たなサイクルの所定のタイミングに到達 したか否かを判断する。 巳〇 II 8 0は、 所定のタイミングに到達していない と判断すると (ステップ 3 1 1 0 : N 0) 、 処理を終了する。 Ten) . For example, Minao II 80 determines whether or not the predetermined timing of the new cycle has been reached. If the MII II 80 determines that the predetermined timing has not been reached (step 311 0: N 0), it ends the process.

[0084] 巳〇 II 8 0は、 再生空気量を更新すると判断すると (ステップ 3 1 1 0 : 丫巳3) 、 再生過不足度を算出する (ステップ 3 1 1 1) 。 再生過不足度は 、 上述したように、 タンク空気水分飽和度の変化に基づき算出されてもよい 。 タンク空気水分飽和度は、 湿度センサ 5 1 により検出された湿度、 温度セ ンサ 5 2により検出された温度等から算出することができる。 [0084] When the MI II 80 determines to update the regeneration air amount (step 311 0: Mimi 3), the regeneration excess/deficiency is calculated (step 3 1 1 1). The regeneration excess/deficiency may be calculated based on the change in the tank air moisture saturation, as described above. The tank air moisture saturation can be calculated from the humidity detected by the humidity sensor 51, the temperature detected by the temperature sensor 52, and the like.

[0085] 巳(3 11 8 0は、 再生過不足度を算出すると、 過不足係数情報 2 0 0を用い て、 過不足係数を取得する (ステップ 3 1 1 2) 。 さらに、 巳〇11 8 0は、 〇 2020/175470 25 卩(:171? 2020 /007469 [0085] Mitsumi (3 1 180 obtains the excess/deficiency factor by using the excess/deficiency factor information 2 0 0 after calculating the reproduction excess/deficiency (step 3 1 1 2). 0 is 〇 2020/175 470 25 卩 (:171? 2020 /007469

再生動作の開始圧力であるカッ トアウト圧を取得する (ステップ 3 1 1 3)Obtain the cutout pressure, which is the start pressure of the regenerating operation (step 3 1 1 3)

。 また、 巳〇11 8 0は、 取得したカッ トアウト圧に基づいて、 マップ 1 0 0 を用いて標準再生空気量を取得するとともに (ステップ 3 1 1 4) 、 マップ 1 0 1 を用いて補正単位空気量を取得する (ステップ 3 1 1 5) 。 そして、 巳〇 II 8 0は、 標準再生空気量、 補正単位空気量、 過不足係数を用いて、 上 記した式 (1) にしたがって再生空気量を算出する (ステップ 3 1 1 6) 。 ここで算出された再生空気量は、 図 6のステップ 3 1 0 1で用いられる。 巳 8 0は、 ここで算出された再生空気量を用いて再生動作を行う。 .. In addition, based on the cutout pressure acquired, Min. 1180 acquires the standard amount of regenerated air using map 100 (step 3 1 1 4) and the correction unit using map 1 0 1. Get the air volume (step 3 1 1 5). Then, MII II 80 calculates the amount of regenerated air according to the above equation (1) using the standard amount of regenerated air, the corrected unit air amount, and the excess/deficiency coefficient (steps 3 1 1 6). The regenerated air amount calculated here is used in step 3101 of FIG. The tan 80 performs a regeneration operation using the regeneration air amount calculated here.

[0086] 以上説明したように、 第 1実施形態によれば、 以下の効果が得られる。 As described above, according to the first embodiment, the following effects can be obtained.

(1) 巳(3 11 8 0は、 コンブレッサ 4の稼働状態に基づき、 再生動作で消 費される再生空気量を設定する。 コンブレッサ 4は空気乾燥回路 1 1以外の 空気圧システムへの圧縮乾燥空気の供給状態に応じて駆動されるので、 再生 空気量を変更することにより、 エアタンク 3 0から空他の空気圧システムへ の圧縮乾燥空気の供給及びフィルタ 1 7の清浄化のいずれかを優先すること ができる。 (1) MI (3 1 180 sets the amount of regenerated air consumed in the regenerating operation based on the operating state of the compressor 4. The compressor 4 is compressed dry air to the pneumatic system other than the air drying circuit 1 1. It is driven according to the supply state of the air conditioner.Therefore, by changing the amount of regenerated air, it is possible to give priority to either the supply of compressed dry air from the air tank 30 to the other pneumatic systems or the cleaning of the filter 17. You can

[0087] (2) コンブレッサ 4の稼働率が高く、 エアタンク 3 0から空気圧システ ムへの圧縮乾燥空気の供給の度合いが大きい場合には、 再生空気量を小さく することにより、 エアタンク 3 0に貯留された圧縮乾燥空気の消費を抑制し 、 空気圧システムへの圧縮乾燥空気の供給を優先させることができる。 また 、 コンブレッサ 4の稼働率が低く、 エアタンク 3 0から空気圧システムへの 圧縮乾燥空気の供給の度合いが小さい場合にはフィルタ 1 7の清浄化を優先 させることができる。 (2) When the operating rate of the compressor 4 is high and the supply of compressed dry air from the air tank 30 to the pneumatic system is large, the amount of regenerated air is reduced to store the air in the air tank 30. It is possible to reduce the consumption of compressed dry air that has been stored and to give priority to the supply of compressed dry air to the pneumatic system. Further, when the operating rate of the compressor 4 is low and the supply of compressed dry air from the air tank 30 to the pneumatic system is small, the cleaning of the filter 17 can be prioritized.

[0088] (3) エアタンク 3 0内の圧縮乾燥空気の湿潤状態が高い場合には、 再生 空気量を大きくすることにより、 フィルタ 1 7の清浄化を優先させることが できる。 また、 圧縮乾燥空気の湿潤状態が低い場合には、 エアタンク 3 0に 貯留された圧縮乾燥空気の消費を抑制することによって、 空気圧システムへ の圧縮乾燥空気の供給を優先させることができる。 (3) When the compressed dry air in the air tank 30 has a high wet state, the cleaning of the filter 17 can be prioritized by increasing the amount of regenerated air. Further, when the wet state of the compressed dry air is low, it is possible to give priority to the supply of the compressed dry air to the pneumatic system by suppressing the consumption of the compressed dry air stored in the air tank 30.

[0089] (4) コンブレッサ 4の稼働状態に応じて再生動作を開始するための上限 〇 2020/175470 26 卩(:171? 2020 /007469 [0089] (4) Upper limit for starting the playback operation according to the operating state of the comblator 4 〇 2020/175 470 26 卩 (:171? 2020 /007469

圧であるカッ トアウト圧が設定され、 カッ トアウト圧に応じて再生空気量が 決定される。 コンブレッサ 4の稼働率が高い場合には、 カッ トアウト圧が高 く設定され且つ再生空気量が小さくされるので、 再生動作の実行頻度を低下 させるとともにエアタンク 3 0に貯留された圧縮乾燥空気の消費を抑制し、 空気圧システムへの圧縮乾燥空気の供給を優先させることができる。 また、 コンブレッサ 4の稼働率が低い場合には、 カッ トアウト圧が低く設定され且 つ再生空気量が大きくされるので、 再生動作の実行頻度を高く してフィルタ 1 7を浄化する効果を高めることができる。 The cutout pressure, which is the pressure, is set, and the amount of regenerated air is determined according to the cutout pressure. When the operating rate of the compressor 4 is high, the cutout pressure is set high and the amount of regenerated air is reduced, so that the frequency of regenerating operation is reduced and the consumption of compressed dry air stored in the air tank 30 is reduced. Can be suppressed and the supply of compressed dry air to the pneumatic system can be prioritized. When the operating rate of the compressor 4 is low, the cutout pressure is set low and the amount of regenerated air is increased.Therefore, the frequency of regenerating operation should be increased to enhance the effect of purifying the filter 17. You can

[0090] (第 2実施形態) [0090] (Second Embodiment)

図 8及び図 9に従って、 第 2実施形態について説明する。 第 2実施形態は 、 標準再生空気量及び補正単位空気量を空気乾燥回路 1 1の状態に応じて変 更して、 再生空気量を算出する点で、 第 1実施形態と共通している。 また、 第 1実施形態では、 カッ トアウト圧に応じて標準再生空気量及び補正単位空 気量を変更したが、 第 2実施形態では、 圧縮乾燥空気の温度に応じて標準再 生空気量及び補正単位空気量を変更する点で第 1実施形態と異なる。 そこで 、 以下では、 主に第 1実施形態と相違する構成について詳細に説明すること とし、 説明の便宜上、 同様の構成については詳細な説明を割愛する。 The second embodiment will be described with reference to FIGS. 8 and 9. The second embodiment is similar to the first embodiment in that the standard regeneration air amount and the correction unit air amount are changed according to the state of the air drying circuit 11 to calculate the regeneration air amount. Further, in the first embodiment, the standard regeneration air amount and the correction unit air amount are changed according to the cutout pressure, but in the second embodiment, the standard regeneration air amount and the correction unit air amount are changed according to the temperature of the compressed dry air. It differs from the first embodiment in that the unit air amount is changed. Therefore, in the following, the configuration different from that of the first embodiment will be mainly described in detail, and the detailed description of the same configuration will be omitted for convenience of description.

[0091 ] 図 8 は、 標準再生空気量 1 を、 限界通気量及び温度に応じて設定し たマップ 1 1 0であり、 記憶部 8 0八に記憶されている。 マップ 1 1 0は、 第 1実施形態のマップ 1 〇〇 (図 3参照) がカッ トアウト圧に応じて標準再 生空気量を決定しているのに対し、 温度に応じて標準再生空気量を決定して いる点が異なる。 温度には、 温度センサ 5 2により検出された値を用いるこ とができる。 又は、 空気乾燥回路 1 1の入口側であってフィルタ 1 7の上流 側に温度センサを設け、 その温度センサが検出した温度を用いてもよい。 標 準再生空気量 1は、 限界通気量を一定としたとき、 温度が低くなるに伴 い小さくなり、 温度が高くなるに伴い大きくなる。 つまり、 温度が高い場合 には、 空気の飽和水蒸気量 (飽和水蒸気圧) が大きくなるため、 圧縮空気に 含まれる水分量も多くなる傾向にある。 したがって、 フィルタ 1 7に捕捉さ 〇 2020/175470 27 卩(:171? 2020 /007469 FIG. 8 is a map 110 in which the standard regeneration air amount 1 is set according to the limit ventilation amount and the temperature, and is stored in the storage unit 808. Map 110 determines the standard regeneration air amount according to the cutout pressure, while map 110 (see FIG. 3) of the first embodiment determines the standard regeneration air amount according to the temperature. The points that have been decided are different. As the temperature, the value detected by the temperature sensor 52 can be used. Alternatively, a temperature sensor may be provided on the inlet side of the air drying circuit 11 and upstream of the filter 17 and the temperature detected by the temperature sensor may be used. The standard regeneration air volume 1 becomes smaller as the temperature becomes lower and becomes larger as the temperature becomes higher, when the limit ventilation volume is fixed. In other words, when the temperature is high, the saturated water vapor content (saturated water vapor pressure) of the air increases, so that the amount of water contained in the compressed air also tends to increase. Therefore, it is captured in filter 17 〇 2020/175 470 27 卩 (:171? 2020 /007469

れる水分量も多くなることが想定されるため、 標準再生空気量 1 を大き く して、 1回の再生動作でのフィルタ 1 7から水分を除去する効果を高める 。 また、 温度が低い場合には、 空気の飽和水蒸気量 (飽和水蒸気圧) が小さ くなるため、 圧縮空気に含まれる水分量が少なくなる傾向にある。 したがっ て、 フィルタ 1 7に捕捉される水分量も少なくなることが想定されるため、 標準再生空気量八 1 を小さくすることによって、 1回の再生動作により消 費される圧縮乾燥空気の量を低減する。 Since it is assumed that the amount of water that is retained will also increase, the standard regeneration air amount 1 is increased to enhance the effect of removing moisture from the filter 17 in one regeneration operation. In addition, when the temperature is low, the amount of saturated steam in the air (saturated steam pressure) becomes small, so that the amount of water contained in the compressed air tends to decrease. Therefore, it is assumed that the amount of water trapped in the filter 17 will also decrease. Reduce.

[0092] 図 8巳は、 補正単位空気量 〇! 2を、 限界通気量及び温度に応じて設定し たマップ 1 1 1であり、 記憶部 8 0八に記憶されている。 補正単位空気量八 2は、 標準再生空気量 1から減算される値であるため、 標準再生空気 量八0! 1 と同様に限界通気量が大きくなるほど小さくなる一方で、 限界通気 量を一定としたとき、 温度が高くなるに伴い小さくなり、 温度が低くなるに 伴い大きくなる。 [0092] Fig. 8 is a map 11 1 in which the correction unit air amount 〇! 2 is set according to the limit ventilation amount and the temperature, and is stored in the storage unit 808. Since the correction unit air volume 82 is a value subtracted from the standard regeneration air volume 1, as the standard regeneration air volume 8! At that time, it becomes smaller as the temperature rises and becomes larger as the temperature falls.

[0093] 次に図 9を参照して、 再生空気量を決定するための処理について説明する 。 第 2実施形態における再生空気量を決定するための処理は、 第 1実施形態 の処理のステップ 3 1 1 0 ~ 3 1 1 2、 ステップ 3 1 1 4〜ステップ 3 1 1 6と共通とするので詳細な説明を省略する。 Next, with reference to FIG. 9, a process for determining the regeneration air amount will be described. The process for determining the amount of regenerated air in the second embodiment is common to steps 311 10 to 3 1 1 2 and steps 3 1 1 4 to 3 1 1 6 of the process of the first embodiment. Detailed description is omitted.

[0094] ステップ 3 1 2 0において、 巳〇11 8 0は、 温度センサ 5 2が検出した圧 縮乾燥空気の温度を取得する (ステップ 3 1 2 0) 。 そして、 巳〇11 8 0は 、 取得した温度と、 マップ 1 1 0を用いて、 標準再生空気量を取得する (ス テップ3 1 1 4) 。 さらに、 巳〇 II 8 0は、 取得した温度とマップ 1 1 1 と を用いて、 補正単位空気量 (ステップ 3 1 1 5) を取得する。 そして、 巳〇 II 8 0は、 標準再生空気量、 補正単位空気量、 過不足係数とを用いて、 再生 空気量を算出する (ステップ 3 1 1 6) 。 [0094] In step 3120, Mino 1180 obtains the temperature of the compressed dry air detected by the temperature sensor 52 (step 3120). Then, M. 1 1 180 obtains the standard amount of regenerated air by using the obtained temperature and map 1 110 (step 3 1 1 1 4). In addition, MII II 80 uses the acquired temperature and map 1 1 1 1 to acquire the corrected unit air amount (step 3 1 1 5). Then, MII II 80 calculates the amount of regenerated air using the standard amount of regenerated air, the corrected unit air amount, and the excess/deficiency coefficient (steps 311 and 6).

[0095] 第 2実施形態では、 以下の効果を得ることができる。 [0095] In the second embodiment, the following effects can be obtained.

(5) 巳(3 11 8 0は、 圧縮空気の温度又は圧縮乾燥空気の温度に応じて、 再生動作で消費される再生空気量を設定する。 圧縮空気の温度又は圧縮乾燥 空気の温度が上昇すると、 空気に含まれる水分量も多くなるため、 空気に含 〇 2020/175470 28 卩(:171? 2020 /007469 (5) MI (3 1 180 sets the amount of regeneration air consumed in regeneration operation according to the temperature of compressed air or the temperature of compressed dry air. The temperature of compressed air or the temperature of compressed dry air rises. Then, the amount of water contained in the air also increases, 〇 2020/175 470 28 卩 (:171? 2020 /007469

まれる水分量の多さに応じて再生空気量を変更することにより、 エアタンク 3 0から空気圧システムへの圧縮乾燥空気の供給、 及びフィルタ 1 7の清浄 化のいずれかを優先することができる。 By changing the amount of regenerated air depending on the amount of water contained, it is possible to give priority to either the supply of compressed dry air from the air tank 30 to the pneumatic system or the cleaning of the filter 17.

[0096] ( 6 ) 空気の温度が低く、 飽和水蒸気量が小さい場合には再生空気量を小 さくすることにより、 エアタンク 3 0に貯留された圧縮乾燥空気の消費を抑 制し、 空気圧システムへの圧縮乾燥空気の供給を優先させることができる。 また、 空気の温度が高く、 飽和水蒸気量が大きい場合には再生空気量を大き く してフィルタ 1 7の清浄化を優先させることができる。 [0096] (6) When the temperature of air is low and the amount of saturated steam is small, the amount of regenerated air is reduced to suppress the consumption of compressed dry air stored in the air tank 30 and transfer it to the pneumatic system. The compressed dry air supply can be prioritized. When the temperature of air is high and the amount of saturated water vapor is large, the amount of regenerated air can be increased to prioritize the cleaning of the filter 17.

[0097] 上記各実施形態は、 以下のように変更して実施することができる。 上記各 実施形態及び以下の変更例は、 技術的に矛盾しない範囲で互いに組み合わせ て実施することができる。 The above-described embodiments can be implemented with the following modifications. The above-described embodiments and the following modifications can be implemented in combination with each other within a technically consistent range.

第 1実施形態では、 再生過不足度に応じて再生空気量を決定したが、 再 生過不足度に応じて再生時間を決定してもよい。 この場合、 補正単位時間に 過不足係数を乗算して補正再生時間を算出し、 補正再生時間を標準となる再 生時間に加算する。 In the first embodiment, the regeneration air amount is determined according to the regeneration excess/deficiency, but the regeneration time may be determined according to the regeneration excess/deficiency. In this case, the corrected playback time is calculated by multiplying the corrected unit time by the excess/deficiency coefficient, and the corrected playback time is added to the standard playback time.

[0098] 第 1実施形態では、 再生過不足度に重み付け係数を乗算することによっ て過不足係数《を算出したが、 過不足係数《として、 再生過不足度そのもの を用いてもよい。 この場合でも、 再生の過不足に応じて、 再生空気量を増大 させたり減少させたりすることができる。 In the first embodiment, the excess/deficiency coefficient << is calculated by multiplying the reproduction excess/deficiency degree by a weighting coefficient, but the reproduction excess/deficiency degree itself may be used as the excess/deficiency coefficient <<. Even in this case, the amount of regenerated air can be increased or decreased depending on the excess or deficiency of regeneration.

[0099] 第 1実施形態では、 再生過不足度は、 エアタンク 3 0内の圧縮乾燥空気 に含まれる水分の飽和度が、 増加傾向にあるか減少傾向にあるかを示す指標 であるとしたが、 再生過不足度の代わりに湿度を指標として用いてもよい。 また、 再生過不足度の代わりにタンク含有水分量を指標として用いてもよい In the first embodiment, the regeneration excess/deficiency is an index indicating whether the saturation of water contained in the compressed dry air in the air tank 30 has an increasing tendency or a decreasing tendency. The humidity may be used as an index instead of the regeneration excess/deficiency. Further, the water content in the tank may be used as an index instead of the excess or deficiency of regeneration.

[0100] 第 1実施形態の再生過不足度は、 数サイクルの間の平均値を用いてもよ い。 平均値が負の値であれば、 エアタンク 3 0内の水分量が上昇していると 推定されるため、 再生空気量が不足していると判断する。 [0100] As the regeneration excess/deficiency in the first embodiment, an average value over several cycles may be used. If the average value is a negative value, it is estimated that the amount of water in the air tank 30 has increased, so it is determined that the amount of regenerated air is insufficient.

[0101 ] 第 1実施形態では、 コンブレッサ 4の稼働率に応じてカッ トアウト圧を 〇 2020/175470 29 卩(:171? 2020 /007469 [0101] In the first embodiment, the cutout pressure is set according to the operating rate of the compressor 4. 〇 2020/175 470 29 卩 (:171? 2020 /007469

設定し、 再生空気量を構成する標準再生空気量及び補正単位空気量をカッ ト アウト圧に応じて設定した。 この態様以外に、 コンブレッサ 4の稼働率と標 準再生空気量及び補正単位空気量とを関連付けたマップ等を用いて、 標準再 生空気量及び補正単位空気量を設定してもよい。 The standard regeneration air amount and the correction unit air amount that constitute the regeneration air amount were set according to the cutout pressure. In addition to this mode, the standard regeneration air amount and the correction unit air amount may be set using a map or the like in which the operating rate of the compressor 4 is associated with the standard regeneration air amount and the correction unit air amount.

[0102] 第 2実施形態では、 温度に応じて標準再生空気量及び補正単位空気量を 設定した。 この態様以外に、 温度に加え湿度を用いて標準再生空気量及び補 正単位空気量を設定してもよい。 又は湿度センサ 5 1等が検出した湿度のみ を用いて、 標準再生空気量及び補正単位空気量を設定してもよい。 [0102] In the second embodiment, the standard regeneration air amount and the correction unit air amount are set according to the temperature. In addition to this mode, the standard regeneration air amount and the correction unit air amount may be set by using the temperature and the humidity. Alternatively, the standard regeneration air amount and the correction unit air amount may be set by using only the humidity detected by the humidity sensor 51 or the like.

[0103] 上記各実施形態では、 エアタンク 3 0の圧縮乾燥空気の湿潤状態が高い 場合には、 過不足係数を負の値として再生空気量を大きく し、 エアタンク 3 0の圧縮乾燥空気の湿潤状態が低い場合には、 過不足係数を正の値として再 生空気量を小さく した。 この態様以外に、 コンブレッサ 4から送出される圧 縮乾燥空気の湿潤状態や、 外気の湿潤状態を用いて再生空気量を変化させて もよい。 [0103] In each of the above embodiments, when the compressed dry air in the air tank 30 is in a high wet state, the excess/deficiency coefficient is set to a negative value to increase the amount of regenerated air, and the compressed dry air in the air tank 30 is in a wet state. When is low, the excess/deficiency coefficient is set to a positive value to reduce the amount of regenerated air. In addition to this mode, the amount of regenerated air may be changed by using the wet state of the compressed dry air sent from the combiner 4 or the wet state of the outside air.

[0104] 再生空気量は、 カッ トアウト圧と圧縮空気又は圧縮乾燥空気の温度とに 基づいて決定されてもよい。 この態様では、 カッ トアウト圧、 温度、 及び標 準再生空気量を対応付けたマップや、 カッ トアウト圧、 温度、 及び補正単位 空気量を対応付けたマップ等が用いられる。 [0104] The regeneration air amount may be determined based on the cutout pressure and the temperature of the compressed air or the compressed dry air. In this embodiment, a map in which cutout pressure, temperature, and standard regeneration air amount are associated with each other, a map in which cutout pressure, temperature, and correction unit air amount are associated with each other are used.

[0105] 上記各実施形態では、 標準再生空気量を、 補正単位空気量に過不足係数 を乗算した補正量で補正して再生空気量を算出したが、 マップ等から再生空 気量を直接的に算出するようにしてもよい。 この場合、 マップは、 カッ トア ウト圧 (又は温度) 、 圧縮乾燥空気の湿潤状態を示す指標、 再生空気量を対 応付けたものであってもよい。 In each of the above embodiments, the standard regeneration air amount is corrected by the correction amount obtained by multiplying the correction unit air amount by the excess/deficiency coefficient to calculate the regeneration air amount, but the regeneration air amount is directly calculated from the map or the like. It may be calculated as follows. In this case, the map may correspond to cutout pressure (or temperature), an index showing the wet state of compressed dry air, and the amount of regenerated air.

[0106] 上記各実施形態では、 フィルタ 1 7は、 油分捕捉部を含むが、 フィルタ In each of the above embodiments, the filter 17 includes an oil trap,

1 7から油分捕捉部を省略してもよい。 The oil trap may be omitted from 17.

空気乾燥回路は、 上記した構成のものに限られない。 空気乾燥回路は、 要は、 除湿動作と再生動作とを実行できる構成であればよい。 したがって、 空気乾燥回路は、 第 2動作モード、 第 4動作モード〜第 6動作モードを必須 〇 2020/175470 30 卩(:171? 2020 /007469 The air drying circuit is not limited to the one having the above configuration. The air drying circuit need only have a configuration capable of performing the dehumidifying operation and the regenerating operation. Therefore, the air drying circuit must have the second operation mode and the fourth to sixth operation modes. 〇 2020/175 470 30 boxes (: 171-1? 2020 /007469

の動作とするものではない。 Is not intended to be the behavior of.

[0107] 上記各実施形態では、 空気供給システム 1 0は、 トラック、 バス、 建機 等の車両に搭載されるものとして説明した。 これ以外の態様として、 空気供 給システム 1 0は、 乗用車、 鉄道車両等、 他の移動体に搭載されてもよい。 [0107] In each of the above embodiments, the air supply system 10 has been described as being installed in a vehicle such as a truck, a bus, or a construction machine. As an aspect other than this, the air supply system 10 may be mounted on another moving body such as a passenger car, a railway vehicle, or the like.

[0108] . ECU 80は、 自身が実行する全ての処理についてソフトウェア処理を 行うものに限られない。 たとえば、 ECU 80は、 自身が実行する処理の少 なくとも一部についてハードウェア処理を行う専用のハードウェア回路 (た とえば特定用途向け集積回路: AS I C) を備えてもよい。 すなわち、 EC U 80は、 1) コンビュータプログラム (ソフトウェア) に従って動作する 1つ以上のプロセッサ、 2) 各種処理のうち少なくとも一部の処理を実行す る 1つ以上の専用のハードウェア回路、 或いは 3) それらの組み合わせ、 を 含む回路 (c i r c u i t r y) として構成し得る。 プロセッサは、 C P U 並びに、 RAM及び ROM等のメモリを含み、 メモリは、 処理を C P Uに実 行させるように構成されたプログラムコードまたは指令を格納している。 メ モリすなわちコンピュータ可読媒体は、 汎用または専用のコンピュータでア クセスできるあらゆる利用可能な媒体を含む。 [0108] The ECU 80 is not limited to the software processing for all the processing executed by itself. For example, the ECU 80 may include a dedicated hardware circuit (for example, an application specific integrated circuit: AS IC) that performs hardware processing for at least a part of the processing performed by the ECU 80. In other words, the EC U 80 consists of 1) one or more processors that operate according to a computer program (software), 2) one or more dedicated hardware circuits that perform at least some of the various processes, or 3 ) A combination of them can be configured as a circuit including. The processor includes a CPU and memories such as RAM and ROM, and the memory stores program code or instructions configured to cause the CPU to perform a process. Memory or computer-readable media includes any available media that can be accessed by a general purpose or special purpose computer.

符号の説明 Explanation of symbols

[0109] 4 コンブレッサ、 1 0 空気供給システム、 1 1 空気乾燥回路、 1 2 供給回路、 1 5 上流チェックバルブ、 1 6 分岐通路、 1 7 フィルタ 、 1 8 空気供給通路、 1 9 下流チェックバルブ、 20 バイパス流路、 [0109] 4 Compressors, 10 Air Supply System, 1 1 Air Drying Circuit, 1 2 Supply Circuit, 1 5 Upstream Check Valve, 1 6 Branch Passage, 1 7 Filter, 1 8 Air Supply Passage, 1 9 Downstream Check Valve, 20 bypass channels,

2 1 再生制御弁、 22 オリフィス、 25 ドレン排出弁、 26 A ガバ ナ、 26 B アンロード制御弁、 27 排出口としてのドレン排出口、 30 貯留部としてのエアタンク、 50 圧カセンサ、 5 1 湿度センサ、 52 温度センサ、 53 圧カセンサ、 80 ECU、 80 A 記憶部、 E 6 1 〜 E 67 配線。 2 1 Regeneration control valve, 22 orifice, 25 drain discharge valve, 26 A governor, 26 B unload control valve, 27 drain discharge port, 30 storage air tank, 50 pressure sensor, 5 1 humidity sensor , 52 temperature sensor, 53 pressure sensor, 80 ECU, 80 A memory, E 61 to E 67 wiring.

Claims

〇 2020/175470 31 卩(:171? 2020 /007469 請求の範囲 〇 2020/175 470 31 卩(:171? 2020/007469 Claims [請求項 1 ] 圧縮空気を送出するコンブレッサ及び圧縮乾燥空気を貯留する貯留 部の間に設けられており、 水分を捕捉するフィルタを有する、 空気乾 燥回路と、 [Claim 1] An air drying circuit, which is provided between a compressor for delivering compressed air and a storage section for storing compressed dry air, and has a filter for trapping moisture. 前記空気乾燥回路を制御する制御装置と、 を備え、 A control device for controlling the air drying circuit, 前記制御装置は、 The control device is 前記コンブレッサから送出された前記圧縮空気を前記フィルタに順 方向に通過させて前記貯留部に供給する除湿動作を実行するように前 記空気乾燥回路を制御し、 Controlling the air drying circuit so as to perform a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in the forward direction and is supplied to the storage section; 前記貯留部に貯留された前記圧縮乾燥空気を前記フィルタに逆方向 に通過させて前記フィルタを通過した流体を排出口から排出する再生 動作を実行するように前記空気乾燥回路を制御し、 前記コンブレッサの稼働状態に応じて、 1回の前記再生動作で消費 する再生空気量を設定するように構成されている、 空気供給システム。 Controlling the air drying circuit to execute a regeneration operation in which the compressed dry air stored in the storage section is passed through the filter in the reverse direction and the fluid passing through the filter is discharged from an outlet, An air supply system configured to set the amount of regeneration air consumed in one regeneration operation according to the operating state of. [請求項 2] 前記制御装置は、 [Claim 2] The control device is 一定期間内の前記コンブレッサの稼働率が高い場合には、 前記再生 空気量を小さく し、 前記コンブレッサの稼働率が低い場合には、 前記 再生空気量を大きくするように構成されている、 When the operating rate of the compressor is high within a certain period of time, the regeneration air amount is reduced, and when the operating rate of the compressor is low, the regeneration air amount is increased. 請求項 1 に記載の空気供給システム。 The air supply system according to claim 1. [請求項 3] 前記制御装置は、 [Claim 3] The control device is 前記貯留部内の圧縮乾燥空気の湿潤状態を示す指標が高い場合には 、 前記再生空気量を大きく し、 前記貯留部内の圧縮乾燥空気の湿潤状 態を示す指標が低い場合には、 前記再生空気量を小さくするように構 成されている、 When the index indicating the wet state of the compressed dry air in the reservoir is high, the amount of the regenerated air is increased, and when the index indicating the wet state of the compressed dry air in the reservoir is low, the regenerated air is Configured to reduce volume, 請求項 1又は 2に記載の空気供給システム。 The air supply system according to claim 1 or 2. [請求項 4] 前記制御装置は、 [Claim 4] The control device is 前記コンブレッサの稼働率が高い場合には、 前記貯留部の圧力であ 〇 2020/175470 32 卩(:171? 2020 /007469 If the operating rate of the compressor is high, the pressure in the storage unit 〇 2020/175 470 32 卩 (:171? 2020 /007469 って前記再生動作を開始するための上限圧を高く設定し、 前記コンブ レッサの稼働率が低い場合には前記上限圧を低く設定し、 Therefore, the upper limit pressure for starting the regeneration operation is set high, and when the operating rate of the compressor is low, the upper limit pressure is set low, 前記上限圧が高い場合には、 前記再生空気量を小さく し、 前記上限 圧が低い場合には前記再生空気量を大きくするように構成されている 請求項 1〜 3のいずれか 1項に記載の空気供給システム。 It is configured such that when the upper limit pressure is high, the regeneration air amount is decreased, and when the upper limit pressure is low, the regeneration air amount is increased. Air supply system. [請求項 5] 圧縮空気を送出するコンブレッサ及び圧縮乾燥空気を貯留する貯留 部の間に設けられており、 水分を捕捉するフィルタを有する、 空気乾 燥回路と、 [Claim 5] An air drying circuit, which is provided between a compressor for delivering compressed air and a storage unit for storing compressed dry air, and has a filter for capturing water, 前記空気乾燥回路を制御する制御装置と、 を備え、 A control device for controlling the air drying circuit, 前記制御装置は、 The control device is 前記コンブレッサから送出された前記圧縮空気を前記フィルタに順 方向に通過させて前記貯留部に供給する除湿動作を実行するように前 記空気乾燥回路を制御し、 Controlling the air drying circuit so as to perform a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in the forward direction and is supplied to the storage section; 前記貯留部に貯留された前記圧縮乾燥空気を前記フィルタに逆方向 に通過させて前記フィルタを通過した流体を排出口から排出する再生 動作を実行するように前記空気乾燥回路を制御し、 前記圧縮空気又は前記圧縮乾燥空気の温度に応じて、 1回の前記再 生動作で消費する再生空気量を設定するように構成されている、 空気供給システム。 Controlling the air drying circuit to execute a regeneration operation of passing the compressed dry air stored in the storage section through the filter in the reverse direction and discharging the fluid that has passed through the filter from an outlet; An air supply system configured to set the amount of regenerated air consumed in one regeneration operation according to the temperature of air or the compressed dry air. [請求項 6] 前記制御装置は、 [Claim 6] The control device is 前記温度が低い場合には、 前記再生空気量を小さく し、 前記温度が 高い場合には、 前記再生空気量を大きくするように構成されている、 請求項 5に記載の空気供給システム。 The air supply system according to claim 5, wherein when the temperature is low, the regeneration air amount is reduced, and when the temperature is high, the regeneration air amount is increased. [請求項 7] 圧縮空気を送出するコンブレッサ及び圧縮乾燥空気を貯留する貯留 部の間に設けられており、 水分を捕捉するフィルタを有する、 空気乾 燥回路と、 前記空気乾燥回路を制御する制御装置とを備える空気供給 システムの制御方法であって 〇 2020/175470 33 卩(:171? 2020 /007469 [Claim 7] An air drying circuit provided between a compressor for delivering compressed air and a storage section for storing compressed dry air, having a filter for trapping moisture, and a control for controlling the air drying circuit A method for controlling an air supply system including a device 〇 2020/175 470 33 卩(:171? 2020/007469 前記制御装置が、 The control device is 前記コンブレッサから送出された前記圧縮空気を前記フィルタに順 方向に通過させて前記貯留部に供給する除湿動作を実行するように前 記空気乾燥回路を制御し、 Controlling the air drying circuit so as to perform a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in the forward direction and is supplied to the storage section; 前記貯留部に貯留された前記圧縮乾燥空気を前記フィルタに逆方向 に通過させて前記フィルタを通過した流体を排出口から排出する再生 動作を実行するように前記空気乾燥回路を制御し、 前記コンブレッサの稼働状態に応じて、 1回の前記再生動作で消費 する再生空気量を設定する、 Controlling the air drying circuit to execute a regeneration operation in which the compressed dry air stored in the storage section is passed through the filter in the reverse direction and the fluid passing through the filter is discharged from an outlet, Depending on the operating state of, the amount of regeneration air consumed in one regeneration operation is set. 空気供給システムの制御方法。 Air supply system control method. [請求項 8] 圧縮空気を送出するコンブレッサ及び圧縮乾燥空気を貯留する貯留 部の間に設けられており、 水分を捕捉するフィルタを有する、 空気乾 燥回路と、 前記空気乾燥回路を制御する制御装置とを備える空気供給 システムの制御方法であって [Claim 8] An air drying circuit provided between a compressor for delivering compressed air and a storage section for storing compressed dry air, having a filter for trapping moisture, and a control for controlling the air drying circuit A method for controlling an air supply system including a device 前記制御装置が、 The control device is 前記コンブレッサから送出された前記圧縮空気を前記フィルタに順 方向に通過させて前記貯留部に供給する除湿動作を実行するように前 記空気乾燥回路を制御し、 Controlling the air drying circuit so as to perform a dehumidifying operation in which the compressed air sent from the compressor is passed through the filter in the forward direction and is supplied to the storage section; 前記貯留部に貯留された前記圧縮乾燥空気を前記フィルタに逆方向 に通過させて前記フィルタを通過した流体を排出口から排出する再生 動作を実行するように前記空気乾燥回路を制御し、 前記圧縮空気の温度又は前記圧縮乾燥空気の温度に応じて、 1回の 前記再生動作で消費する再生空気量を設定する、 Controlling the air drying circuit to execute a regeneration operation of passing the compressed dry air stored in the storage section through the filter in the reverse direction and discharging the fluid that has passed through the filter from an outlet; According to the temperature of the air or the temperature of the compressed dry air, set the amount of regeneration air consumed in one regeneration operation, 空気供給システムの制御方法。 Air supply system control method. [請求項 9] 圧縮空気を送出するコンブレッサ及び圧縮乾燥空気を貯留する貯留 部の間に設けられており、 水分を捕捉するフィルタを有する、 空気乾 燥回路と、 前記空気乾燥回路を制御する制御装置とを備える空気供給 システムの制御プログラムであって 〇 2020/175470 34 卩(:171? 2020 /007469 [Claim 9] An air drying circuit provided between a compressor for delivering compressed air and a storage section for storing compressed dry air, having a filter for trapping moisture, and a control for controlling the air drying circuit And a control program for an air supply system including 〇 2020/175 470 34 卩 (: 171? 2020 /007469 前記制御装置を、 The control device, 前記コンブレッサから送出された前記圧縮空気を前記フィルタに順 方向に通過させて前記貯留部に供給する除湿動作を実行するように前 記空気乾燥回路を制御する除湿動作実行部、 A dehumidification operation execution unit that controls the air drying circuit to execute a dehumidification operation in which the compressed air sent from the compressor is passed through the filter in the forward direction and is supplied to the storage unit; 前記貯留部に貯留された前記圧縮乾燥空気を前記フィルタに逆方向 に通過させて前記フィルタを通過した流体を排出口から排出する再生 動作を実行するように前記空気乾燥回路を制御する再生動作実行部、 及び Execution of a regeneration operation that controls the air drying circuit to perform a regeneration operation in which the compressed dry air stored in the storage section is passed through the filter in the reverse direction and the fluid that has passed through the filter is discharged from an outlet. Department, and 前記コンブレッサの稼働状態に応じて、 1回の前記再生動作で消費 する再生空気量を設定する設定部、 として機能させる、 A setting unit for setting the amount of regeneration air consumed in one regeneration operation according to the operating state of the compressor, 空気供給システムの制御プログラム。 Air supply system control program. [請求項 10] 圧縮空気を送出するコンブレッサ及び圧縮乾燥空気を貯留する貯留 部の間に設けられており、 水分を捕捉するフィルタを有する、 空気乾 燥回路と、 前記空気乾燥回路を制御する制御装置とを備える空気供給 システムの制御プログラムであって [Claim 10] An air drying circuit provided between a compressor for delivering compressed air and a storage section for storing compressed dry air, having a filter for trapping moisture, and a control for controlling the air drying circuit A control program for an air supply system comprising 前記制御装置を、 The control device, 前記コンブレッサから送出された前記圧縮空気を前記フィルタに順 方向に通過させて前記貯留部に供給する除湿動作を実行するように前 記空気乾燥回路を制御する除湿動作実行部、 A dehumidification operation execution unit that controls the air drying circuit to execute a dehumidification operation in which the compressed air sent from the compressor is passed through the filter in the forward direction and is supplied to the storage unit; 前記空気乾燥回路を制御して前記貯留部に貯留された前記圧縮乾燥 空気を前記フィルタに逆方向に通過させて前記フィルタを通過した流 体を排出口から排出する再生動作を実行するように前記空気乾燥回路 を制御する再生動作実行部、 及び The air drying circuit is controlled so that the compressed dry air stored in the storage section is passed through the filter in the reverse direction and the fluid that has passed through the filter is discharged from the discharge port. A regeneration operation execution unit that controls the air drying circuit, and 前記圧縮空気の温度又は前記圧縮乾燥空気の温度に応じて、 1回の 前記再生動作で消費する再生空気量を設定する設定部、 として機能さ せる A setting unit that sets the amount of regeneration air consumed in one regeneration operation according to the temperature of the compressed air or the temperature of the compressed dry air. 空気供給システムの制御プログラム。 Air supply system control program.
PCT/JP2020/007469 2019-02-25 2020-02-25 Air supply system, control method for air supply system, and control program for air supply system Ceased WO2020175470A1 (en)

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