CN109603315A - A kind of vacuum system automatic draining device - Google Patents
A kind of vacuum system automatic draining device Download PDFInfo
- Publication number
- CN109603315A CN109603315A CN201811547838.7A CN201811547838A CN109603315A CN 109603315 A CN109603315 A CN 109603315A CN 201811547838 A CN201811547838 A CN 201811547838A CN 109603315 A CN109603315 A CN 109603315A
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- tank
- liquid separation
- gas
- area
- tank body
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- 239000007788 liquid Substances 0.000 claims abstract description 77
- 238000000926 separation method Methods 0.000 claims abstract description 58
- 238000005192 partition Methods 0.000 claims abstract description 41
- 241000521257 Hydrops Species 0.000 claims abstract description 40
- 206010030113 Oedema Diseases 0.000 claims abstract description 40
- 239000012530 fluid Substances 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 8
- 239000007789 gas Substances 0.000 claims description 33
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- 238000012423 maintenance Methods 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 239000000945 filler Substances 0.000 claims description 4
- 238000007747 plating Methods 0.000 claims description 4
- 238000011044 inertial separation Methods 0.000 claims description 3
- 238000010079 rubber tapping Methods 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 2
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 2
- 230000001154 acute effect Effects 0.000 claims description 2
- 238000009826 distribution Methods 0.000 claims description 2
- 239000004571 lime Substances 0.000 claims description 2
- 238000012216 screening Methods 0.000 claims description 2
- 238000001727 in vivo Methods 0.000 claims 1
- 238000009833 condensation Methods 0.000 abstract description 3
- 230000005494 condensation Effects 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 238000001816 cooling Methods 0.000 abstract description 2
- 230000004888 barrier function Effects 0.000 description 6
- 238000013461 design Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000004080 punching Methods 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000019771 cognition Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- External Artificial Organs (AREA)
Abstract
The invention discloses a kind of vacuum system automatic draining devices, including closed hollow vessel, a partition board tilted with horizontal plane are equipped in the middle part of tank body, partition top is liquid separation area, lower part is hydrops area；Tank body left end in the middle part of liquid separation area is equipped with air inlet, in being equipped with air flap in tank body at air inlet, enters liquid separation area in air flap lower end by the gas that air inlet flows into tank body；Top of the tank in liquid separation area is equipped with gas outlet；Drain through-hole is equipped in partition board left end；Catheter is equipped in drain through-hole lower end；Tank body right end in hydrops area top is equipped with gas balance mouth at partition, and gas balance mouth is connected by gas-guide tube with liquid separation area；Leakage fluid dram is equipped in the tank body lower end in hydrops area.The present apparatus is equipped with complete automatic control system, can effectively collect material medium in vacuum pipe automatically since cooling condensation forms drop, avoid the formation of hydrops and enter vacuum pump, pump is caused to damage.
Description
Technical field
The invention discloses a kind of vacuum system automatic draining device and mating automatic control systems.
Background technique
During vacuumizing, such as in rectification under vacuum operating process, often due to pipeline is longer, heat insulation measure
Be not good at, the operation factors such as operating parameter is unstable cause the material medium in vacuum pipe to congeal into drop, ultimately form hydrops into
Enter vacuum equipment, adverse effect is caused to equipment, even results in equipment damage, and then not can guarantee system vacuum, influence just
Often production.
Vacuum equipment is usually placed on ground, is arranged in certain height if being evacuated equipment (such as overhead condensate reflux tank)
Degree, to meet the net positive suction head requirement of reflux pump.Since vacuum equipment inlet duct is too long, pipe insulation provision for thermal insulation is not good at,
The material medium carried secretly in vacuum pipe is easy condensation and forms drop, ultimately forms hydrops.Therefore, it is transported to guarantee that equipment is stablized
Often liquid separation tank is arranged in mechanical compression equipment entrance in row.
For traditional liquid separation tank due to the presence of vacuum condition, equipment, which is arranged height and put, will meet breaking vacuum between net point
The requirement of pressure at receiving device is spent and meets, therefore equipment position is higher.Meanwhile to guarantee that each pressure system separates,
To guarantee that certain liquid level as fluid-tight, avoids " altering pressure ", causes vacuum system unstable in liquid separation tank.
Summary of the invention
Automatic vacuum liquid-drainaged device of the invention increases demarcation plate realization one and sets inside traditional liquid separation tank base
For two interior pressure, automatic drain, while matched with self-control control valve system are realized by potential difference inside equipment, realized entirely certainly
Dynamicization operation.Meanwhile purged by inert gas pressure, ground can be placed a device in, so on present apparatus face with vacuum equipment
Arrangement recently, it is too long to avoid pipeline between liquid separation tank and vacuum pump, forms time condensation.
Present apparatus design scheme is as follows: liquid separation tank integrally suggests being designed as vertical storage tank, is arranged inside liquid separation tank and tilts
Partition board, partition top is liquid separation area, and lower part is hydrops area, is connected between two regions by pipeline, realize that high point is vented,
Low spot drain, is arranged automatic stop valve in connecting pipe, needs to realize connection according to operation and separates, system is avoided " to alter
Pressure ".
A kind of vacuum system automatic draining device is equipped with one and horizontal plane including closed hollow vessel in the middle part of tank body
Tank interior is separated into upper and lower two by the partition board tilted, partition edge and inner tank wall face airtight connection, partition
A mutually disconnected chamber, partition top is liquid separation area, lower part is hydrops area, and the right end of partition upper surface is located above left end,
Liquid separation area bottom is set to form right high left low inclined surface；
Tank body left end in the middle part of liquid separation area is equipped with air inlet, in being equipped with air flap in tank body at air inlet, by air inlet
The gas that mouth flows into tank body enters liquid separation area in air flap lower end；Top of the tank in liquid separation area is equipped with gas outlet；
It is equipped with drain through-hole in partition board left end, or in partition board left end equipped with the groove as collecting tank, liquid collecting
The bottom of slot is equipped with drain through-hole；Catheter is equipped in drain through-hole lower end；
In hydrops area top tank body right end at partition be equipped with gas balance mouth, gas balance mouth by gas-guide tube with
Liquid separation area is connected；Leakage fluid dram is equipped in the tank body lower end in hydrops area.
The present apparatus can use a variety of intake methods, and design scheme is as follows:
Intake method one: spiral deflector is arranged in device air inlet, and vacuum gas is set from the side rotary-cut of liquid separation area to entrance
It is standby, rotation tangential admission is realized by spiral deflector, carries out gas-liquid separation using the density contrast of gas and material, advantage is gas-liquid
Separative efficiency is high, the disadvantage is that device structure is complicated, requirement on machining accuracy is high, and equipment difficulty of processing and processing cost increase；
Intake method two: flow apron is arranged in device air inlet, realizes that the inertial separation of gas-liquid, advantage are equipment difficult processings
Spend small, disadvantage is to realize efficiently separating for gas and material, according to droplet size, to there is the liquid separation area of enough height.
Collecting tank is arranged in inclined clapboard low spot inside equipment, and the two sides of spikes/low- points collecting tank are realized by connecting pipe to be filled
Set being connected to for liquid separation area and hydrops area.Partition is uniformly arranged fan-shaped drain groove, to facilitate baffle surface liquid to partition low spot
Collecting tank confluence.
Since liquid separation area and hydrops area carry out even energy by connecting pipe, two area's static pressure are identical, the liquid in liquid separation area
Cognition is slipped in inclined clapboard low spot collecting tank along inclined clapboard diversion trench, by flowing to hydrops area communicating pipe.
Such structure design, has liquid separation area space compared with high separating efficiency, to reduce equipment volume.When hydrops area
When interior liquid level reach a certain height, automatic interlock carries out vacuum breaker drain.
Drain automatically control: when hydrops area liquid level is higher (LSHH001), starting interlocking, close communicating valve XV001 and
XV002 separates in liquid separation area and hydrops from two valve position feedbacks open nitrogen valve XV003 without mistaking, and hydrops area pressure reaches pre-
When definite value, interlocking close XV003 opens tapping valve XV004 and carries out drain, when the emptying rate of liquid in hydrops area, closes
XV004.At this point, the pressure rate in hydrops area is maintained to be greater than downstream pressure.After liquid empties, XV001 and XV002 are reopened.
Hydrops area volume is small as far as possible, on the one hand reduces liquid residence time, on the other hand reduces hydrops area to vacuum
System causes excessive pressure to fluctuate, this depends on vacuum system ability etc. and liquid measure factor is divided to determine.
Ripple hydraulic barrier is arranged in present apparatus liquid separation tank deck, and two of liquid separation area gas before entering vacuum pump may be implemented
Secondary gas-liquid separation.
Ripple hydraulic barrier low spot goes out drainage hole by machinery, as shown in Fig. 2, hydraulic barrier lower edge machinery punching
Protrusion retains, and corrugated baffle inner product advantageous in this way flows down.
Ripple hydraulic barrier is arranged in present apparatus liquid separation tank deck, using ripple hydraulic barrier, can be kept off in gas by baffling
When plate, flow-disturbing is generated, gas-liquid separation is more conducive to.
Detailed description of the invention
Fig. 1 is device structure schematic diagram of the invention.
The reference numerals are as follows:
1. liquid separation area；2. hydrops area；3. inner part is every inclined clapboard；4. catheter；5. air inlet spiral deflector or water conservancy diversion gear
Plate；6. ripple baffle plate
Fig. 2 is inclined clapboard diversion trench schematic diagram of the invention.
Fig. 3 is the ripple hydraulic barrier punching schematic diagram of invention.Specific embodiment.
Specific embodiment
Embodiment 1
A kind of vacuum system automatic draining device is equipped in the middle part of tank body including closed hollow cylindrical vertical storage tank
One partition board tilted with horizontal plane, partition edge and inner tank wall face airtight connection, partition divide tank interior
Two mutual disconnected chambers up and down are divided into, partition top is liquid separation area, lower part is hydrops area, and the right end of partition upper surface is located at
Above left end, liquid separation area bottom is made to form right high left low inclined surface；
Tank body left end in the middle part of liquid separation area is equipped with air inlet, in being equipped with air flap in tank body at air inlet, by air inlet
The gas that mouth flows into tank body enters liquid separation area in air flap lower end；Top of the tank in liquid separation area is equipped with gas outlet；
It is equipped with drain through-hole in partition board left end, is equipped with catheter in drain through-hole lower end；
In hydrops area top tank body right end at partition be equipped with gas balance mouth, gas balance mouth by gas-guide tube with
Liquid separation area is connected；
Leakage fluid dram is equipped in the tank body lower end in hydrops area.
The gas outlet is connected with the vacuum pump of vacuum system.
In being respectively equipped with communicating valve on catheter and gas-guide tube；Tapping valve is equipped at leakage fluid dram；
Tank wall in hydrops area is equipped with the interface being connected through nitrogen valve with Nitrogen source gases.
It is described to refer to the upper surface of partition board and horizontal plane angle at an acute angle with the partition board that horizontal plane tilts,
Angle is 30 degree.
The air flap is flow apron, and the vertical cross-section of flow apron is inverted L-shaped, realizes the inertial separation of gas-liquid.
Embodiment 2
Difference from Example 1 is,
3 or more the curbs stretched to upper right side edge from drain through-hole for starting point are equipped in the partition upper surface
Slot, diversion channel slot on partition in being uniformly arranged, at radial fan-shaped distribution, to facilitate baffle surface liquid to partition low spot
Drain through-hole or collecting tank converge.
Embodiment 3
Difference from Example 1 is,
In being equipped with gas baffling baffle in liquid separation area between air flap air flap lower end and gas outlet, to increase gas
In the intracorporal process of liquid separation area tank；The gas baffling baffle is corrugated plating, and drain through-hole is offered at the trough of corrugated plating.
Embodiment 4
Difference from Example 1 is,
In being filled with granular filler in catheter, the supporting screening plate with through-hole is equipped with below filler；
The air flap be spiral deflector, vacuum gas by air inlet by liquid separation area tank wall face tangentially into
Enter in tank body, rotation tangential flow is realized by spiral deflector, carries out gas-liquid centrifuge separation using the density contrast of gas and material；
It is equipped with pressure vacuum gauge in liquid separation area top of the tank, and installs pressure gage valve between Yu Qiyu tank body additional to facilitate vacuum
Pressure gauge maintenance replacement；
Top of the tank in liquid separation area is equipped with absolute pressure transducer, and installs pressure gage valve between Yu Qiyu tank body additional with side
Just absolute pressure transducer maintenance replacement；
Tank wall in hydrops area is equipped with pressure vacuum gauge, and installs pressure gage valve between Yu Qiyu tank body additional with convenient
Pressure vacuum gauge maintenance and replacement；
In hydrops area tank wall be equipped with absolute pressure transducer, and between Yu Qiyu tank body install additional pressure gage valve with
Facilitate the maintenance and replacement of absolute pressure transducer；
In on the tank wall lower part in hydrops area and leakage fluid dram, fluid level transmitter is installed additional, hydrops area lime set liquid level is carried out
Measurement, two interfaces of liquidometer install valve additional to facilitate the maintenance and replacement of fluid level transmitter.
The present apparatus is equipped with complete automatic control system, can effectively condense material medium in vacuum pipe due to cooling
It forms drop to be collected automatically, avoids the formation of hydrops and enter vacuum pump, pump is caused to damage.
The present apparatus can be realized automatic drain, and for mounting height there is no limit being not necessarily to breaking vacuum degree when, drain,
It can be achieved all to put hydrops into the operation requirement for changing only and fluid-tight being arranged in traditional liquid separation tank.
Claims (10)
1. a kind of vacuum system automatic draining device, it is characterised in that: including closed hollow vessel, one is equipped in the middle part of tank body
The partition board tilted with horizontal plane, partition edge and inner tank wall face airtight connection, partition separate tank interior
At upper and lower two mutual disconnected chambers, partition top is liquid separation area, lower part is hydrops area, and the right end of partition upper surface is located at a left side
End top makes liquid separation area bottom form right high left low inclined surface；
Tank body left end in the middle part of liquid separation area is equipped with air inlet, in being equipped with air flap in tank body at air inlet, by air inlet stream
The gas for entering tank body enters liquid separation area in air flap lower end；Top of the tank in liquid separation area is equipped with gas outlet；
It in partition board left end is equipped with drain through-hole, or is equipped in partition board left end as the groove of collecting tank, collecting tank
Bottom is equipped with drain through-hole；Catheter is equipped in drain through-hole lower end；
Tank body right end in hydrops area top is equipped with gas balance mouth at partition, and gas balance mouth passes through gas-guide tube and liquid separation
Area is connected；
Leakage fluid dram is equipped in the tank body lower end in hydrops area.
2. according to vacuum system automatic draining device described in claim 1, it is characterised in that: the gas outlet and vacuum system
Vacuum pump is connected.
3. according to vacuum system automatic draining device described in claim 1, it is characterised in that: Yu Suoshu partition upper surface be equipped with from
Drain through-hole or collecting tank are 3 or more the diversion channel slots of starting point stretched to upper right side edge, and diversion channel slot is in uniform on partition
Setting, at radial fan-shaped distribution, to facilitate baffle surface liquid to converge to the drain through-hole or collecting tank of partition low spot.
4. according to vacuum system automatic draining device described in claim 1, it is characterised in that:
In in liquid separation area between air flap air flap lower end and gas outlet be equipped with gas baffling baffle, with increase gas in point
The intracorporal process of liquid zone tank；The gas baffling baffle is corrugated plating, and drain through-hole is offered at the trough of corrugated plating.
5. according to vacuum system automatic draining device described in claim 1, it is characterised in that:
In being filled with granular filler in catheter, supporting screening plate or sieve with through-hole are equipped with below filler.
6. according to vacuum system automatic draining device described in claim 1, it is characterised in that: point tilted with horizontal plane
Refer to the upper surface of partition board and horizontal plane angle at an acute angle every partition, angle is between 10-70 degree, preferred 20-40 degree.
7. according to vacuum system automatic draining device described in claim 1, it is characterised in that:
The air flap is spiral deflector, and vacuum gas is by air inlet by liquid separation area tank wall face tangentially into tank
In vivo, rotation tangential flow is realized by spiral deflector, carries out gas-liquid centrifuge separation using the density contrast of gas and material；
Or, the air flap is flow apron, the vertical cross-section of flow apron is inverted L-shaped, realizes the inertial separation of gas-liquid.
8. according to vacuum system automatic draining device described in claim 1, it is characterised in that:
In being respectively equipped with communicating valve on catheter and gas-guide tube；Tapping valve is equipped at leakage fluid dram；
Tank wall in hydrops area is equipped with the interface being connected through nitrogen valve with Nitrogen source gases.
9. according to vacuum system automatic draining device described in claim 1, it is characterised in that:
It is equipped with pressure vacuum gauge in liquid separation area top of the tank, and installs pressure gage valve between Yu Qiyu tank body additional to facilitate vacuum pressure
Table maintenance replacement；
Top of the tank in liquid separation area is equipped with absolute pressure transducer, and installs pressure gage valve between Yu Qiyu tank body additional to facilitate absolutely
Pressure transmitter is overhauled and is replaced；
Tank wall in hydrops area is equipped with pressure vacuum gauge, and installs pressure gage valve between Yu Qiyu tank body additional to facilitate vacuum
Pressure gauge maintenance and replacement；
Tank wall in hydrops area is equipped with absolute pressure transducer, and installs pressure gage valve between Yu Qiyu tank body additional with convenient
The maintenance and replacement of absolute pressure transducer；
In on the tank wall lower part in hydrops area and leakage fluid dram, installs fluid level transmitter additional, hydrops area lime set liquid level is measured,
Two interfaces of liquidometer install valve additional to facilitate the maintenance and replacement of fluid level transmitter.
10. according to vacuum system automatic draining device described in claim 1, it is characterised in that: liquid separation tank is generally cylindric vertical
Formula storage tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811547838.7A CN109603315A (en) | 2018-12-18 | 2018-12-18 | A kind of vacuum system automatic draining device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811547838.7A CN109603315A (en) | 2018-12-18 | 2018-12-18 | A kind of vacuum system automatic draining device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109603315A true CN109603315A (en) | 2019-04-12 |
Family
ID=66009662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811547838.7A Pending CN109603315A (en) | 2018-12-18 | 2018-12-18 | A kind of vacuum system automatic draining device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109603315A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111569535A (en) * | 2020-05-22 | 2020-08-25 | 重庆开山压缩机有限公司 | But accurate control's dewatering jar |
| CN111807592A (en) * | 2020-07-17 | 2020-10-23 | 河北兰升生物科技有限公司 | Continuous liquid separation device and organic solvent separation method using same |
| CN116706346A (en) * | 2023-08-02 | 2023-09-05 | 德阳市东新机电有限责任公司 | Aluminum fuel cell power generation system and method |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5215560A (en) * | 1992-02-10 | 1993-06-01 | Lee Nam H | Air filtering system |
| CN2516222Y (en) * | 2001-12-13 | 2002-10-16 | 武汉三联节能设备制造有限公司 | Gas-liquid or gas-solid separation device |
| CN201832492U (en) * | 2010-10-14 | 2011-05-18 | 艾伦塔斯电气绝缘材料(珠海)有限公司 | Vacuum knockout drum |
| CN202182053U (en) * | 2011-08-04 | 2012-04-04 | 博山精工泵业有限公司 | Improved electromagnetic valve controlled water ring vacuum pump preposed gas-water separator |
| CN203060972U (en) * | 2013-02-20 | 2013-07-17 | 王�锋 | Vapor-liquid separator |
| CN203577475U (en) * | 2013-10-24 | 2014-05-07 | 湖北同方高科泵业有限公司 | Front-mounted-type unblocked unpowered gas-liquid separation tank |
| CN206513361U (en) * | 2017-03-01 | 2017-09-22 | 崔嘉成 | Oil well casing air separation |
| CN206809914U (en) * | 2017-03-27 | 2017-12-29 | 国网天津市电力公司 | A kind of run-in index boiler smoke dehydration device |
| CN107529446A (en) * | 2017-09-13 | 2018-01-02 | 江苏新凯晟机械设备有限公司 | Can be from the Vacuum gas-liquid separator of discharge opeing |
| CN206996071U (en) * | 2017-05-03 | 2018-02-13 | 岳阳聚成化工有限公司 | Knockout drum |
| US20180223201A1 (en) * | 2017-02-09 | 2018-08-09 | General Electric Company | Gasification quench system |
-
2018
- 2018-12-18 CN CN201811547838.7A patent/CN109603315A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5215560A (en) * | 1992-02-10 | 1993-06-01 | Lee Nam H | Air filtering system |
| CN2516222Y (en) * | 2001-12-13 | 2002-10-16 | 武汉三联节能设备制造有限公司 | Gas-liquid or gas-solid separation device |
| CN201832492U (en) * | 2010-10-14 | 2011-05-18 | 艾伦塔斯电气绝缘材料(珠海)有限公司 | Vacuum knockout drum |
| CN202182053U (en) * | 2011-08-04 | 2012-04-04 | 博山精工泵业有限公司 | Improved electromagnetic valve controlled water ring vacuum pump preposed gas-water separator |
| CN203060972U (en) * | 2013-02-20 | 2013-07-17 | 王�锋 | Vapor-liquid separator |
| CN203577475U (en) * | 2013-10-24 | 2014-05-07 | 湖北同方高科泵业有限公司 | Front-mounted-type unblocked unpowered gas-liquid separation tank |
| US20180223201A1 (en) * | 2017-02-09 | 2018-08-09 | General Electric Company | Gasification quench system |
| CN206513361U (en) * | 2017-03-01 | 2017-09-22 | 崔嘉成 | Oil well casing air separation |
| CN206809914U (en) * | 2017-03-27 | 2017-12-29 | 国网天津市电力公司 | A kind of run-in index boiler smoke dehydration device |
| CN206996071U (en) * | 2017-05-03 | 2018-02-13 | 岳阳聚成化工有限公司 | Knockout drum |
| CN107529446A (en) * | 2017-09-13 | 2018-01-02 | 江苏新凯晟机械设备有限公司 | Can be from the Vacuum gas-liquid separator of discharge opeing |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111569535A (en) * | 2020-05-22 | 2020-08-25 | 重庆开山压缩机有限公司 | But accurate control's dewatering jar |
| CN111807592A (en) * | 2020-07-17 | 2020-10-23 | 河北兰升生物科技有限公司 | Continuous liquid separation device and organic solvent separation method using same |
| CN111807592B (en) * | 2020-07-17 | 2022-04-15 | 河北兰升生物科技有限公司 | Continuous liquid separation device and organic solvent separation method using same |
| CN116706346A (en) * | 2023-08-02 | 2023-09-05 | 德阳市东新机电有限责任公司 | Aluminum fuel cell power generation system and method |
| CN116706346B (en) * | 2023-08-02 | 2023-10-13 | 德阳市东新机电有限责任公司 | Aluminum fuel cell power generation system and method |
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Application publication date: 20190412 |
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| RJ01 | Rejection of invention patent application after publication |