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WO2014049791A1 - Dispositif de filtration rotatif à chambres multiples mis sous pression et son procédé de fonctionnement - Google Patents

Dispositif de filtration rotatif à chambres multiples mis sous pression et son procédé de fonctionnement Download PDF

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Publication number
WO2014049791A1
WO2014049791A1 PCT/JP2012/074972 JP2012074972W WO2014049791A1 WO 2014049791 A1 WO2014049791 A1 WO 2014049791A1 JP 2012074972 W JP2012074972 W JP 2012074972W WO 2014049791 A1 WO2014049791 A1 WO 2014049791A1
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WIPO (PCT)
Prior art keywords
filtration
chamber
gas
rotary filter
filtrate
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/JP2012/074972
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English (en)
Japanese (ja)
Inventor
昭男 山下
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.)
Mitsubishi Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha Ltd
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Filing date
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Application filed by Mitsubishi Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to PCT/JP2012/074972 priority Critical patent/WO2014049791A1/fr
Priority to JP2013513457A priority patent/JP5282182B1/ja
Publication of WO2014049791A1 publication Critical patent/WO2014049791A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/06—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums
    • B01D33/073—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for inward flow filtration
    • B01D33/09—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for inward flow filtration with surface cells independently connected to pressure distributors
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation

Definitions

  • the present invention relates to a rotary filter and a method for operating the same, and more specifically, for example, an acetic acid solvent containing a reaction product such as terephthalic acid as a crystal component can be filtered to efficiently recover the crystal component.
  • the present invention relates to a pressurized multi-chamber rotary filter capable of constructing a system at low cost and an operating method thereof.
  • terephthalic acid can be produced by oxidizing p-xylene at high temperature and high pressure in an acetic acid solvent.
  • the terephthalic acid obtained by the oxidation reaction is further crystallized in an acetic acid solvent, lowered to a predetermined temperature and pressure, terephthalic acid is recovered as a crystal component by a filtration system, and acetic acid solvent is recovered as a filtrate.
  • acetic acid solvent containing terephthalic acid as a crystal component will be described as a slurry.
  • this vacuum type single-chamber rotary filter is a rotating drum that is rotationally driven by a variable speed reducer (not shown) having both end faces sealed and a large number of filtrate holes formed in the peripheral surface. 1, a center pipe 2 that rotatably supports the rotating drum 1, and a stock solution bat 3 disposed below the rotating drum 1.
  • a filter cloth is stretched on the outer peripheral surface of the rotating drum 1 as a filtering portion via a filter bridge (not shown), and the lower portion of the rotating drum 1 is immersed in the stock solution slurry S filled with the stock solution bat 3 to thereby filter the filtration region.
  • a cake layer composed of the crystal components of the raw slurry S is formed on the surface of the filter cloth in the filtration region, and the reaction solvent permeates the filter cloth and enters the rotating drum 1 as a filtrate.
  • the filtrate in the rotary drum 1 is sucked by a vacuum device (not shown) through the filtrate pipe 4 connected to the center pipe 2 and led out of the apparatus.
  • a plurality of valve shoes 5 made of a synthetic resin such as a tetrafluoroethylene resin are disposed in the rotating drum 1 along the axial direction of the center pipe 2, and a slit is formed on the inner peripheral surface of the rotating drum 1. Are in sliding contact. Narrow first and second slits are formed in the upper and lower portions of the valve shoe 5 along the axial direction of the rotary drum 1, and a blow gas such as nitrogen gas is blown out from these slits to form a cake layer from the rotary drum 1. After the peeling, the rotating drum 1 is washed to eliminate clogging. Vacuum single-chamber rotary filters are widely used because of their excellent processing capabilities.
  • C ′ is a cake-like crystal component peeled from the rotating drum 1.
  • the pressure of the slurry is lowered during filtration because the pressure is reduced to normal pressure after the oxidation reaction and then vacuum filtration is performed at a temperature of 85 to 95 ° C. Impurities such as by-products of terephthalic acid and metal catalysts dissolved in the solvent are deposited to lower the purity of the crystal components, and the filter cloth is clogged and scales are formed in the system. Therefore, it is necessary to frequently stop the vacuum single-chamber rotary filter and perform maintenance such as internal cleaning, and the operation efficiency of the filtration system is not always good.
  • the vacuum single-chamber rotary filter is provided with a valve shoe 5 interposed between the rotary drum 1 and the rotary drum 1 inside the rotary drum 1, so that the rotary drum 1 has severe roundness. Required. Therefore, it is necessary to perform cutting for obtaining the roundness of the rotary drum 1, and the manufacturing cost of the vacuum type single-chamber rotary filter itself is increased accordingly.
  • Patent Document 1 proposes a filtration system for recovering terephthalic acid.
  • a pressurized filter device is used to pressurize at a high pressure (2 to 5 bar) at a high temperature (for example, 110 to 160 ° C.) higher than the atmospheric pressure boiling point of acetic acid, and to slurry at a high temperature and high pressure.
  • the crystalline component is again dried using a dryer under a pressure of 0 to 5 bar.
  • the slurry is filtered under high temperature and pressure as described above, so that precipitation of impurities such as reaction by-products and metal catalysts can be suppressed, and clogging of the pressure filter device can be suppressed. , The number of maintenance can be reduced.
  • the temperature at the time of filtration is set higher than the normal pressure boiling point of the acetic acid solvent, so that the steel materials such as stainless steel normally used in the pressure filter device are resistant to the acetic acid solvent heated to the normal pressure boiling point. Therefore, it is impossible to use a steel material such as stainless steel, and it is necessary to use an expensive corrosion-resistant material. In this case, the manufacturing cost of the pressure filter device is significantly increased. Moreover, since the high pressure is maintained in the pressure filter device even in the drying process of the crystal components, the filtration process and the drying process must be maintained in a high pressure environment, and a large amount of gas is required for operation. There was a problem of high costs.
  • the present invention has been made to solve the above-described problems.
  • a reaction solvent (slurry) containing a crystal component generated by a chemical reaction is filtered to suppress contamination of impurities and efficiently recover the crystal component.
  • the pressurization type multi-chamber rotary filter according to claim 1 of the present invention includes a rotary drum having a plurality of filtration chambers that are defined in an axially elongated shape with a predetermined width along an outer peripheral surface, and the rotation A center shaft penetrating the center of each side surface of the drum, a pair of left and right rotating shafts provided at both ends of the center shaft, a driving mechanism for rotating the rotating drum via the rotating shafts, and the rotation A container that is disposed below the drum and receives a reaction solvent containing a crystal component as a slurry; and a housing that houses the rotating drum and the container to form a sealed space, and a part of the plurality of filtration chambers
  • a pressurization type multi-chamber rotary filter that immerses in a slurry in a container and collects the crystalline component by filtering the slurry through the plurality of filtration chambers, the longitudinal direction of the inner surface of the filtration chamber Along the filtrate
  • the communication pipe a hole provided at an end near the other rotation axis of the inner surface of the filtration chamber, and the first rotation axis along the axial direction of the other rotation axis corresponding to the filtration chamber
  • a second communication pipe connecting a second flow path formed to exclude filtrate remaining in the communication pipe, and a plurality of first flow paths in accordance with filtration from each of the plurality of filtration chambers.
  • a first switching valve that switches simultaneously for opening and closing; And a second switching valve that simultaneously switches a plurality of second flow paths for opening and closing in accordance with filtration from each of the plurality of filtration chambers.
  • the pressurized multi-chamber rotary filter according to the first aspect, wherein the second flow path and the second communication pipe are at least the first communication tube.
  • the gas supply means is configured to supply a gas for extruding the filtrate remaining in the communication pipe and the first flow path.
  • the pressurization type multi-chamber rotary filter according to the first or second aspect, wherein the first flow path and the first communication pipe are the first communication pipe. It is comprised as a gas supply means which supplies the gas for peeling the said cake layer through 2 communicating pipes and the said 2nd flow path.
  • a method for operating a pressurized multi-chamber rotary filter wherein the pressurized multi-chamber rotary filter according to any one of the first to third aspects is operated.
  • the slurry is fed into the pressurized multi-chamber rotary filter based on the pressure difference between the second step of supplying the reaction solvent containing the slurry into the container of the pressurized multi-chamber rotary filter and the pressure of the gas in the housing.
  • the operation method of the pressure type multi-chamber rotary filter according to claim 5 of the present invention is the operation method of the pressure multi-chamber rotary filter according to claim 4, wherein the third step is the step of the pressurization type multi-chamber rotary filter.
  • Cleaning the cake layer by spraying washing water onto the cake layer, supplying the gas into the filtration chamber via the second flow path and the second communication pipe, and at least the first And a step of discharging the washing filtrate remaining in the first communication pipe and the first flow path.
  • the operation method of the pressurization type multi-chamber rotary filter according to claim 6 of the present invention is the invention according to claim 4 or claim 5, wherein in the fourth step, the first flow path is used. And the said gas is supplied into the said filtration chamber through the said 1st communicating pipe, and the said cake layer is peeled from the said filtration chamber, It is characterized by the above-mentioned.
  • a seventh aspect of the present invention there is provided a method for operating a pressurized multi-chamber rotary filter according to any one of the fourth to sixth aspects, wherein the gas supplied to the housing is the same. Is characterized in that it is recycled.
  • a method for operating a pressurized multi-chamber rotary filter according to any one of the fourth to sixth aspects, wherein the gas supplied to the housing is the same. Is released to the outside.
  • the operation method of the pressure type multi-chamber rotary filter according to claim 9 of the present invention is the invention according to any one of claims 4 to 8, wherein the temperature of the slurry is 95 to 95. The temperature is adjusted to 109 ° C.
  • the operation method of the pressurized multi-chamber rotary filter according to claim 10 of the present invention is the pressure of the gas in the housing according to any one of claims 4 to 9. Is adjusted to 0.05 to 0.19 MpaG.
  • a reaction solvent (slurry) containing a crystal component generated by a chemical reaction can be filtered to prevent impurities from being mixed and the crystal component can be efficiently recovered, and a filtration system can be constructed at a low cost. It is possible to provide a pressurized multi-chamber rotary filter that can be operated and a method of operating the same.
  • FIG. 4B is a cross-sectional view of the main part passing through the axis of the rotating drum.
  • A), (b) is a figure which shows the process following the filtration process shown in FIG. 2, respectively, and is sectional drawing equivalent to (a), (b) of FIG.
  • (A), (b) is a figure which shows the process following the 1st liquid removal process shown in FIG. 3, respectively, and is sectional drawing equivalent to (a), (b) of FIG. (A), (b) is a figure which shows the process following the 1st spot blow process shown in FIG. 4, respectively, and is sectional drawing equivalent to (a), (b) of FIG. (A), (b) is a figure which shows the process following the washing
  • (A), (b) is a figure which shows the process following the 2nd spot blow process shown in FIG. 7, respectively, and is sectional drawing equivalent to (a), (b) of FIG. It is a block diagram which shows other embodiment of the filtration system using the pressurization type multi-chamber rotary filter of this invention. It is sectional drawing which shows an example of the single chamber type vacuum rotary filter used for the conventional filtration system.
  • the pressurized multi-chamber rotary filter 10 of the present embodiment is configured as a main part of the filtration system shown in FIG. 1, for example.
  • This filtration system is configured as part of a terephthalic acid production plant, for example.
  • this filtration system includes a pressurized multi-chamber rotary filter 10 and ancillary equipment 100.
  • an acetic acid solvent containing terephthalic acid obtained by oxidation reaction of p-xylene as a crystal component is added at a low level. Filtration is performed under pressure, and a crystal component of terephthalic acid and an acetic acid solvent as a reaction solvent are recovered.
  • the acetic acid solvent containing terephthalic acid obtained by the oxidation reaction as a crystal component is handled as a slurry.
  • the temperature of the slurry obtained by the oxidation reaction under high temperature and high pressure is lower than the normal pressure boiling point (approximately 118 ° C.) of acetic acid. It is preferable to adjust the temperature at which impurities are hardly deposited (for example, 95 to 109 ° C.) and the pressure during filtration to, for example, 0.05 to 0.19 Mpa.
  • Adjusting the temperature of the slurry during filtration to the above temperature suppresses the precipitation of impurities during filtration and reduces the corrosiveness due to the acetic acid solvent, and adjusts the pressure during filtration to the above pressure to increase the pressure type
  • the chamber type rotary filter 10 can be excluded from the second type pressure vessel and contribute to the cost reduction of the apparatus.
  • the pressurized multi-chamber rotary filter 10 of the present embodiment will be described with reference to FIGS. 1 and 2.
  • the pressurization type multi-chamber rotary filter 10 has a plurality of sections formed in an elongated shape in the axial direction with a predetermined width along the outer peripheral surface.
  • a rotating drum 11 having a filtration chamber 11A, a center shaft 12 penetrating the center of both end faces that seal the rotating drum 11 from both ends, and a pair of left and right rotating shafts 13A provided at both ends of the center shaft 12, 13B, bearings 14A and 14B that support these rotating shafts 13A and 13B, a drive mechanism 15 that rotates the rotating drum 11 that is supported by the bearings 14A and 14B via the rotating shafts 13A and 13B, and a rotating drum 11, and a slurry bat (hereinafter simply referred to as “butt”) 16 that receives the slurry S, and a housing 17 that houses the rotating drum 11 and the bat 16 and forms a sealed space.
  • butt slurry bat
  • a part of the plurality of filtration chambers 11A is immersed in the slurry S in the bat 16, and the crystal component is filtered from the slurry S in the plurality of filtration chambers 11A by the differential pressure between the gas pressure in the housing and the atmospheric pressure. Has been.
  • the plurality of filtration chambers 11A are covered with a filter cloth (not shown) and are independent from each other, and are all formed as elongated chambers parallel to the center shaft 12.
  • a partition wall is formed between adjacent filtration chambers 11A and 11A.
  • a large number of holes (not shown) are uniformly distributed on the outer surface (upper surface) of the filtration chamber 11A, and the outer surface is covered with a filter cloth to form a filtration surface.
  • two rows of first holes are formed at equal intervals over the entire length in the axial direction on the inner surface (hereinafter referred to as “lower surface”) of the filtration chamber 11A. ing.
  • a first connecting pipe 11B (see FIG. 2A) is connected to each of two rows of first holes formed in the longitudinal direction of the filtration chamber 11A.
  • the first connecting pipe 11B includes a plurality of branch pipes 11B1 having one end branched into two branches and connected to the two rows of first holes and the other end extending toward the center shaft 12, and these branch pipes.
  • the other end of the 11B 1 is connected filtrate from the filtration chamber 11A is formed from the confluent pipe 11B 2 merging.
  • the merge pipe 11B 2 includes a first axial part to which a plurality of branch pipes 11B 1 are connected, a radial part extending from the central part of the first axial part toward the center shaft 12, and a radial part.
  • a second axial portion extending parallel to the center shaft 12 toward the rotation shaft 13A from the extended end to the right side.
  • the second axial portion is connected to a first flow path 11C formed through the rotary shaft 13A in the axial direction.
  • a plurality of first flow paths 11C are formed at equal intervals from each other in a concentric manner with the outer periphery of the rotating shaft 13 so as to correspond to the plurality of filtration chambers 11A.
  • a multi-chamber rotary filter generally has a narrow filtrate flow path and a large flow resistance, and therefore has a smaller filtration amount per unit time than a single-chamber rotary filter, and is not suitable for a large amount of filtration.
  • each filtration chamber 11A is provided with a plurality of first connecting pipes 11B, and the flow rate of the filtrate is remarkably increased, so that filtration comparable to a single-chamber rotary filter can be performed. It has become.
  • one hole (not shown) is formed in the left end portion of the lower surface of the filtration chamber 11A, and one end of the second communication pipe 11D extending toward the center shaft 12 is connected to this hole, and the other end is on the left side. Is connected to a second flow path 11E formed through the rotation shaft 13B in the axial direction. Similarly to the first flow path 11C, a plurality of second flow paths 11E are formed on the rotating shaft 13 in a circular shape. The second communication pipe 11D and the second flow path 11E are configured to forcibly discharge the filtrate remaining in the first communication pipe 11B and the first flow path 11C to the outside when the pressurized gas is supplied. is there.
  • the circle drawn by the plurality of second flow paths 11E is set to have a smaller diameter than the circle drawn by the plurality of first flow paths 11C.
  • the forcibly draining means of the remaining filtrate is also used when the washing filtrate described later is discharged.
  • first and second switching valves 18A and 18B respectively, and pass through the first and second switching valves 18A and 18B in accordance with the filtration process of the slurry S.
  • each of the first and second flow paths 11C and 11E is switched to another flow path.
  • the first switching valve 18A is switched to the pressurized gas side at the timing when the cake layer C deposited in the filtration chamber 11A is peeled off.
  • the second switching valve 18B is switched to the pressurized gas side at the timing when the remaining filtrate is discharged from the first connecting pipe 11B and the first flow path 11C to a filtrate separator described later.
  • a plurality of cleaning sprays 19 extend obliquely above the rotary drum 11 over the entire length in the axial direction of the rotary drum 11 and are arranged at predetermined intervals in the circumferential direction of the rotary drum 11. Washing water is sprayed onto the cake layer C formed on the surface to wash the cake layer C. The washing water permeates into the filtration chamber 11A in combination with the action of the gas pressure in the housing 17. The washing filtrate in the filtration chamber 11A is discharged to the outside through the first communication pipe 11B and the first flow path 11C in the same manner as the filtrate.
  • the above-described second switching valve 18B is operated to introduce pressurized gas into the second communication pipe 11D and the second flow path 11E, and this pressurized gas causes The washing filtrate remaining in the first communication pipe 11B and the first flow path 11C is discharged.
  • An inflow pipe 16A for slurry S is provided at the bottom of the bat 16, and an overflow pipe 16B is provided at the open end of the bat 16.
  • the cake layer C deposited on the filtration surface of each filtration chamber 11A of the rotary drum 11 is operated by the first switching valve 18A and the filtration chamber 11A via the first flow path 11C and the first communication pipe 11B. It peels from the filtration surface of the filtration chamber 11 ⁇ / b> A through the pressurized gas that is uniformly supplied to the entire interior, and is discharged to the outside through the cake discharge pipe 20 adjacent to the rotary drum 11.
  • the cake discharge pipe 20 is provided with a cakelet down system, which will be described later, including a rotary valve 21.
  • the inside and outside of the housing 17 are shut off via the cakelet down system, and the gas pressure in the housing 17 is kept constant. ing. Therefore, the cake in the housing 17 peeled from the rotating drum 11 is supplied to a conveying means such as a screw conveyor described later in the atmosphere and a drying means via the cakelet down system.
  • the auxiliary equipment 100 of the pressurization type multi-chamber rotary filter 10 includes a slurry pump 101, a gas supply source 102, a filtrate separator 103, a filtrate pump 104, an acetic acid recovery unit 105, a vapor acetic acid recovery unit 106, a circulation blower 107, a mist separator 108, a sealing liquid.
  • a circulation pump 109, a sealing liquid circulation cooler 110, a gas heater 111, a cakelet down system 112, a screw conveyor 113, and a dryer 114 are provided.
  • the slurry pump 101 is connected to the inflow pipe 16A of the bat 16 of the pressurization type multi-chamber rotary filter 10, and the slurry S adjusted to a predetermined temperature and pressure by the slurry pump 101 is supplied into the bat 16, and extra
  • the slurry S is discharged from the overflow pipe 16B.
  • a gas supply source 102 is connected to the housing 17, and a predetermined gas (for example, nitrogen gas or off gas) is supplied from the gas supply source 102 into the housing 17, and the temperature in the housing 17 is adjusted to a predetermined temperature and pressure. Filtration is started in the state.
  • a predetermined gas for example, nitrogen gas or off gas
  • a filtrate separator 103 is switchably connected to the plurality of first flow paths 11C of the rotary drum 11 via a first switching valve 18A.
  • a circulation pump 104 and an acetic acid recovery unit 105 are connected to the downstream side of the filtration separator 103. Are connected sequentially. Therefore, while the plurality of filtration chambers 11A are immersed in the slurry S, a cake layer C is formed on the filtration surface of each filtration chamber 11A by filtration of the slurry S, and the filtrate permeates each filtration surface, and the filtration is performed. It is discharged from the chamber 11A to the filtrate separator 103 via the first communication pipe 11B and the first flow path 11C.
  • the filtration chamber 11A comes out of the slurry S and is exposed to the gas in the housing 17 by the counterclockwise rotation of the rotary drum 11, the gas passes through the filtration surface accompanied by the filtrate remaining in the cake layer C, These gases and filtrate are discharged from the filtration chamber 11A to the filtrate separator 103 via the first communication pipe 11B and the first flow path 11C.
  • the filtrate separator 103 gas-liquid separates the filtrate and gas, and the filtrate is recovered as an acetic acid solvent by the acetic acid recovery unit 105 via the filtrate pump 104.
  • a vapor acetic acid recovery unit 106, a circulation blower 107, and a mist separator 108 are connected to the downstream side of the filtrate separator 103 in this order, and gas containing filtrate vapor is separated into gas and liquid in this system. Therefore, the gas containing the vapor of the filtrate separated by the filtrate separator 103 is cooled in the paper acetic acid recovery unit 106, and the vapor of the filtrate becomes mist and is supplied to the mist separator 108 through the circulation blower 107 together with the gas. Is done.
  • the mist separator 108 captures the mist-like filtrate and removes the filtrate from the gas.
  • the gas from which the filtrate has been removed is returned to the pressurized multi-chamber rotary filter 10 side through the circulation blower 107 and circulated for use.
  • a sealing liquid circulation pump 109 and a sealing liquid circulation cooler 110 are connected to the downstream side of the mist separator 108 in this order, and the filtrate captured by the mist separator 108 is passed through the sealing liquid circulation pump 109 to the sealing liquid circulation cooler 110. It is cooled by circulating.
  • the sealing liquid circulation cooler 110 is connected to the circulation blower 107, and the filtrate captured by the mist separator 108 is circulated between the circulation blower 107, the mist separator 108 and the sealing liquid circulation cooler 110 via the sealing liquid circulation pump 109. The mist of the filtrate is more reliably removed from the gas directed to the gas heater 111.
  • a gas heater 111 is connected to the downstream side of the mist separator 108, and the gas heater 111 is a temperature required for filtering the gas from the mist separator 108 through the circulation blower 107 in the pressurization type multi-chamber rotary filter 10. Until heated.
  • the gas heated to a predetermined temperature by the gas heater 111 merges with the gas from the gas supply source 102 and is supplied into the housing 17.
  • the filtration system is activated, and a predetermined gas such as nitrogen gas is supplied into the housing 17 of the pressurized multi-chamber rotary filter 10.
  • a predetermined gas such as nitrogen gas is supplied into the housing 17 of the pressurized multi-chamber rotary filter 10.
  • the nitrogen gas is heated to a temperature lower than the boiling point of the acetic acid solvent, for example, to a temperature at which impurities of terephthalic acid, which is a crystalline component, hardly precipitate, for example, 95 to 109 ° C.
  • the nitrogen gas inside is pressurized to a pressure higher than the external pressure, for example, a pressure of 0.05 to 0.19 MPaG not subject to the application of the second type pressure vessel, and the pressurized multi-chamber rotary filter 10 is suitable for filtering the slurry S. Set the operating conditions.
  • the temperature of the pressurized gas in the housing 17 (see FIGS. 2A and 2B)
  • the slurry S whose temperature is lowered to the same level as 95 to 109 ° C. is supplied into the bat 16 via the slurry pump 101, and the rotating drum 11 rotates at a rotational speed of 1 to 6 rpm, for example.
  • the filtration chamber 11 ⁇ / b> A immersed in the slurry S is filtered based on the pressure difference between the nitrogen gas in the housing 17 and the pressure in the filtration chamber 11 ⁇ / b> A covered with the filter medium on which the filtrate is deposited. Is done.
  • the filtrate in the filtration separator 103 is fed to the acetic acid recovery unit 105 via the filtrate pump 104, where it is recovered as an acetic acid solvent. Further, the vapor from the filtrate in the filtrate separator 103 passes through the vapor acetic acid recovery unit 106 via the circulation blower 107, where the vapor is cooled to become a mist, and then trapped as a filtrate in the mist separator 108. The The filtrate captured by the mist separator 108 is further cooled and collected by the sealing liquid circulation cooler 110 via the sealing liquid circulation pump 109, and the filtrate returns to the circulation blower 107, and nitrogen gas passes through the mist separator 108 and is a gas heater. After being heated to a predetermined temperature (95 to 109 ° C.), it is combined with nitrogen gas supplied from the gas supply source 102 and supplied into the housing 17.
  • a predetermined temperature 95 to 109 ° C.
  • Rotating drum 11 rotates and filtration chamber 11A in which cake layer C is formed as shown in FIGS. 3 (a) and 3 (b) comes out of slurry S and is exposed to the pressurized gas environment of housing 17.
  • the pressurized gas passes through the cake layer C on the filtration surface, but the pressurized gas reaches the inside of the filtration chamber 11A with the filtrate remaining in the cake layer C, and the filtrate is removed from the cake layer C.
  • the layer C is dried, and the filtrate of the cake layer C accompanying the pressurized gas and the filtrate remaining in the filtration chamber 11A are combined together as shown in black in FIGS. 3 (a) and 3 (b).
  • the filtrate separator 103 is discharged to the filtrate separator 103 via the first connecting pipe 11B and the first flow path 11C.
  • the filtrate is separated from the pressurized gas as described above, and is recovered as an acetic acid solvent in the acetic acid recovery unit 105.
  • the pressurized gas is supplied to the gas heater 111 via the paper blower 107 and the paper acetic acid recovery unit 106 and the mist separator 108, and merges with the gas from the gas supply source 102.
  • the filtrate that has passed through the mist separator 108 is collected in the sealing liquid circulation cooler 110 via the sealing liquid circulation pump 109.
  • the rotating drum 11 continues to rotate, and the filtrate remaining in the cake layer C is pressurized gas until the filtration chamber 11A in which the cake layer C is formed reaches the cleaning spray 19 as shown in FIGS. 4 (a) and 4 (b). And the cake layer C is gradually dried.
  • the filtrate in the filtration chamber 11A is discharged to the filtration separator 103 via the first communication pipe 11B and the first flow path 11C, but these flow paths are thin and have high flow resistance, and are sufficiently supplied to the filtration separator 103. Can not be discharged.
  • the second switching valve 18B is operated so that the pressurized gas is supplied to the second flow path 11E and the second communication pipe 11D corresponding to the filtration chamber 11A. 4 (a) and (b) in FIG. 4 are blown in a spot manner (hereinafter referred to as “spot blow”). ) And the filtrate remaining in at least the first communication pipe 11B and the first flow path 11C is completely pushed out to the filtration separator 103 to be emptied. When the filtrate is completely discharged, the second switching valve 18B closes the second flow path 11E and stops introducing the pressurized gas.
  • the filtration efficiency improves by forcibly discharging the remaining filtrate by the spot blow of the pressurized gas, the rotation speed of the rotary drum 11 can be increased, and the filtration processing capacity is increased.
  • the filtration chamber 11A from which the filtrate has been completely discharged reaches the washing spray 19, and the cake layer C is washed with washing water.
  • the cleaning water permeates the cake layer C in combination with the action of the pressurized gas, as indicated by the black arrows and the black lines, and the filtration chamber 11A, the first communication pipe. It is discharged to the filtrate separator 103 via 11B and the first flow path 11C.
  • the washing water remaining in the cake layer C is again removed as a washing filtrate by the action of the pressurized gas, as shown by thin arrows and arrows in FIGS. 6 (a) and 6 (b).
  • the cake layer C is dried.
  • the washing filtrate is not sufficiently discharged, and the washing filtrate remains in at least the first communication pipe 11B and the first flow path 11C. Therefore, before the cake layer C is peeled off from the filtration chamber 11A, the second switching valve 18B is operated so that the pressurized gas is supplied to the second flow path 11E and the second communication pipe 11D corresponding to the filtration chamber 11A. 7 (a) and (b) are supplied by spot blow as indicated by arrows and hunting, and at least the washing filtrate remaining in the first communication pipe 11B and the first flow path 11C is completely filtered. Extrude to separator 103 to empty. When the washing filtrate is completely discharged, the second switching valve 18B closes the second flow path 11E. This treatment improves the filtrate recovery rate.
  • the first valve 18A switches the first flow path 11C to the pressurized gas side, and the first flow path 11C and the first connection.
  • a pressurized gas is introduced into the tube 11B and the filtration chamber 11A.
  • the pressurized gas is ejected from the filtration chamber 11A into the housing 17, and the cake layer C is peeled off from the filtration surface as shown in FIGS. Discharge.
  • the cake C ′ is supplied from the pressurized environment in the housing 17 to the screw conveyor 113 under the atmospheric pressure environment via the cakelet down system 112 including the rotary valve 21.
  • the cake C ′ is crushed by the screw conveyor 113 and then supplied to the dryer 114 as a powdery crystal component. Crystal components dried by the dryer 114 are transported from the dryer 114 to a predetermined storage and stored.
  • the slurry S is filtered at a temperature of 95 to 109 ° C. and a low pressure of 0.05 to 0.19 MpaG using the pressurized multi-chamber rotary filter 10. Therefore, impurities such as by-products of crystal components and metal catalysts are deposited in the filtration chamber 11A, and the filtration surface is less likely to be clogged, and the viscosity of the acetic acid solvent is low and the filter can be smoothly filtered and impurities are mixed. Can be recovered.
  • the pressurized multi-chamber rotary filter 10 of the present embodiment has a lower viscosity of the slurry S than the vacuum single-chamber rotary filter, so that the filtration capacity is improved by, for example, about 20%. Further, since the pressurized multi-chamber rotary filter 10 has a smaller volume of the filtration chamber 11A than the vacuum single-chamber rotary filter, the amount of pressurized gas used can be reduced to, for example, about 40%. . In addition, since the pressurization type multi-chamber rotary filter 10 is less likely to be clogged than the vacuum single-chamber rotary filter, the number of maintenance can be reduced, and thus the pressurization multi-chamber rotary filter can be reduced. The operating efficiency of the machine 10 can be increased.
  • the pressure-type multi-chamber rotary filter 10 is made of a steel material such as stainless steel normally used in this type of filter, and a filtration system is constructed at a relatively low cost. Can do.
  • the high pressure gas is used to forcibly discharge the filtrate and washing filtrate remaining in the filtration chamber 11A, the first connecting pipe 11B, and the first flow path 11C, the filtration efficiency can be improved.
  • FIG. 9 is a block diagram showing another filtration system to which the pressurized multi-chamber rotary filter of the present invention is applied.
  • the filtration system shown in FIG. 1 is a system that circulates and uses pressurized gas
  • the filtration system of this embodiment is a system that does not circulate and use pressurized gas.
  • the pressurized multi-chamber rotary filter 10 is configured in the same manner as in the above embodiment, but the incidental equipment 200 does not circulate and use pressurized gas. It is configured. Therefore, in the present embodiment, the incidental facility 200 will be described, and the description of the pressurized multi-chamber rotary filter 10 having the same configuration as that of the above embodiment will be omitted.
  • the incidental equipment 200 includes a slurry pump 201, a gas supply source 202, a filtrate separator 203, a filtrate pump 204, an acetic acid recovery unit 205, a cakelet down system 207, a screw conveyor 208, and a dryer 209. It is configured.
  • this pressurization system does not circulate and use the pressurizing gas, unlike the filtration system shown in FIG. 1, an apparatus or gas heater for removing the mist of the filtrate from the circulating gas is not required.
  • Others are configured according to the filtration system shown in FIG.
  • the pressurized multi-chamber rotary filter 10 is the same as the system in which the pressurized gas circulates, the filtration process is the same as the above embodiment.
  • off-gas is used as the gas supplied from the gas supply source 202.
  • the filtrate separator 203 and the vapor acetic acid recovery unit 205 are passed through.
  • the filtrate and its vapor are recovered and only off-gas is discharged. Therefore, since a mist separator and a gas heater are unnecessary on the downstream side of the vapor acetic acid recovery unit 205, the equipment cost can be reduced by that amount compared with the incidental equipment 100 of the above embodiment.
  • the crystal component recovered by the pressurized multi-chamber rotary filter 10 is supplied to the screw conveyor 208 in a state where the crystal component is returned to the atmospheric pressure in the cakelet down system 207, and dried in the dryer 209. To the hangar.
  • an acetic acid solvent containing terephthalic acid as a crystal component has been described as an example of a slurry.
  • the present invention is not limited to the above embodiment, and a reaction product generated by a chemical reaction is converted into a crystal component.
  • the method can be widely applied to the case where the crystal component is filtered from the slurry composed of the reaction solvent.
  • the present invention can be widely applied to recover crystal components in the field of general chemical industry.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Filtration Of Liquid (AREA)
PCT/JP2012/074972 2012-09-27 2012-09-27 Dispositif de filtration rotatif à chambres multiples mis sous pression et son procédé de fonctionnement Ceased WO2014049791A1 (fr)

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PCT/JP2012/074972 WO2014049791A1 (fr) 2012-09-27 2012-09-27 Dispositif de filtration rotatif à chambres multiples mis sous pression et son procédé de fonctionnement
JP2013513457A JP5282182B1 (ja) 2012-09-27 2012-09-27 加圧式多室型回転濾過機及びその運転方法

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017529226A (ja) * 2014-07-25 2017-10-05 ビーピー・コーポレーション・ノース・アメリカ・インコーポレーテッド 減少した圧力変動を有するロータリープレッシャーフィルター装置
WO2022076962A1 (fr) * 2020-10-07 2022-04-14 Blanchard Kenneth Dispositif de tamisage rotatif à paliers

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH038404A (ja) * 1989-03-08 1991-01-16 Iijima Seimitsu Kogyo Kk 遠心式自浄フィルタ付液体浄化装置
JPH078718A (ja) * 1993-06-29 1995-01-13 Mitsubishi Chem Corp 濾過脱水機
JPH1057722A (ja) * 1996-08-20 1998-03-03 Tsukishima Kikai Co Ltd 固液分離方法およびこれを用いた回転円筒型真空濾過機

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH038404A (ja) * 1989-03-08 1991-01-16 Iijima Seimitsu Kogyo Kk 遠心式自浄フィルタ付液体浄化装置
JPH078718A (ja) * 1993-06-29 1995-01-13 Mitsubishi Chem Corp 濾過脱水機
JPH1057722A (ja) * 1996-08-20 1998-03-03 Tsukishima Kikai Co Ltd 固液分離方法およびこれを用いた回転円筒型真空濾過機

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017529226A (ja) * 2014-07-25 2017-10-05 ビーピー・コーポレーション・ノース・アメリカ・インコーポレーテッド 減少した圧力変動を有するロータリープレッシャーフィルター装置
WO2022076962A1 (fr) * 2020-10-07 2022-04-14 Blanchard Kenneth Dispositif de tamisage rotatif à paliers

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