GB2172521A - A reactivateable adsorption filter assembly - Google Patents

A reactivateable adsorption filter assembly Download PDF

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Publication number
GB2172521A
GB2172521A GB08604165A GB8604165A GB2172521A GB 2172521 A GB2172521 A GB 2172521A GB 08604165 A GB08604165 A GB 08604165A GB 8604165 A GB8604165 A GB 8604165A GB 2172521 A GB2172521 A GB 2172521A
Authority
GB
United Kingdom
Prior art keywords
fluid
filter assembly
valve
assembly
filter element
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.)
Granted
Application number
GB08604165A
Other versions
GB2172521B (en
GB8604165D0 (en
Inventor
Douglas Stuart Balfour Marr
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.)
Dowty Fuel Systems Ltd
Original Assignee
Dowty Fuel Systems Ltd
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
Application filed by Dowty Fuel Systems Ltd filed Critical Dowty Fuel Systems Ltd
Publication of GB8604165D0 publication Critical patent/GB8604165D0/en
Publication of GB2172521A publication Critical patent/GB2172521A/en
Application granted granted Critical
Publication of GB2172521B publication Critical patent/GB2172521B/en
Expired legal-status Critical Current

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Classifications

    • 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
    • B01D53/02Separation 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 by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation 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 by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0454Controlling adsorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/40Further details for adsorption processes and devices
    • B01D2259/40003Methods relating to valve switching
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/40Further details for adsorption processes and devices
    • B01D2259/40083Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
    • B01D2259/40086Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by using a purge gas
    • 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
    • B01D53/02Separation 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 by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation 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 by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407Constructional details of adsorbing systems
    • B01D53/0446Means for feeding or distributing gases

Description

1 GB 2 172 521 A 1
SPECIFICATION
A reactivateable adsorption filter assembly This invention relates to a reactivateable 5 adsorption filter assembly.
It is known that it is possible to reactivate an adsorption filter element by purging the filter element with fluid containing adsorbate at a partial pressure belowthe partial pressure at which the adsorbate was originally adsorbed from the fluid passed through the filter element.
Such reactivateable adsorption systems commonly include two adsorber vessels, one of which is kept on stream while the other is being reactivated.
Such systems have the disadvantage that complicated valving arrangements are often required to change overfrom supply to reactivation.
It is a further disadvantage that the size of such systems is often largerthan that strictly required due to the need to have two adsorber vessels.
It is an object of this invention to provide a smaller and simpler reactivateable absorption filter assembly.
According to the invention there is provided a reactivateable adsorption filter assembly comprising of a high pressure ads6rption filter element, a storage vessel to store filtered fluid containing adsorbate at low partial pressure, a flow restrictor and a purge valve selectively operable to vent the filter assembly to a source of fluid at a lower pressure, the arrangement being such that when the purge valve is opened filtered fluid containing adsorbate at a very low partial pressure flows back from the storage vessel through the filter 100 element to the source of fluid at lower pressure thereby reactivating the filter element.
The filter assembly may further comprise valve means to prevent the flow of fluid into the storage vessel before the pressure in the filter element has 105 reached a predetermined level.
The invention will now be described by way of example with reference to the accompanying drawings in which:- Fig. 1 shows in schematic form a reactivateable adsorption filter assembly according to the invention.
Fig. 2 shows in schematic form a reactivateable adsorption filter assembly similar to that of Figure 1 but including a first modification.
Fig. 3 shows in schematic form a reactivateable adsorption filter assembly similar to that of Fig. 1 but including a second modification.
With reference to Figure 1 there is shown a source 10 of impure fluid to beflitered arranged to be 120 supplied to a reactivateable adsorption filter assembly by means of the compressor 24 which is driven by a motor 25, the filter assembly being connected to the compressor by means of the fluid inlet 12. The fluid inlet 12 connects the source 10 of impure fluid to an inlet side of an adsorption filter element 11. A coalescer 20 is situated upstream of the filter element 11 to pre-treatthe impure fluid before it reaches the filter element 11.
A purge valve 15 is arranged to selectively 130 connect the filter assembly and in particularthe fluid inlet 12 to a source.14 of fluid at a pressure lower than that normally prdsent in the filter element 11. The purge valve 15 is opened or closed in response to an external control signal sent from an electronic control unit 30.
A fluid outlet 13 is provided to connect the filter element 11 to an isolation valve 28. The isolation valve 28 is used to selectively connect or disconnect the filter assembly from a fluid receiving means 23 for which filtered fluid is required.
The isolation valve 28 is opened in response to a control signal from the electronic control unit 30 when the pressure in the fluid outlet 13 reaches a predetermined pressure. The pressure in the fluid outlet 13 is measured by a pressure transducer 27 which sends a feedback signal to the electronic control unit 30.
A reservoir 16 is connected to the fluid outlet 13 between the isolation valve 28 and the filter element 11 at a position of connection 21. A non-return or check valve 17 is connected into the fluid outlet 13 between the position of connection 21 and the filter element 11 to allow filtered fluid to pass downstream towards the isolation valve 28 and into the reservoir 16 but prevent flow f rom the reservoir back towards the filter element 11. The reservoir 16 provides a source of filtered fluid which is immediately available upon opening the isolation valve 28 and which dan be used to maintain a continuity of f low during reactivation of the filter element.
A storage vessel 18 is connected to the fluid outlet 13 upstream of the check valve 17 at a position of connection 22. A restrictor 19 is connected between the storage vessel 18 and the fluid outlet 13 to restrict the flow into and out of the storage vessel 18. The restrictor 19 enables a small mass of filtered fluid to be used to effect reactivation of the filter element.
During normal operation of the filter assembly impure fluid containing adsorbate at high partial pressure will Oass from the source 10 into the filter assembly through the filter element 11 and filtered fluid containing the adsorbate at low partial pressure will pass out of the filter assemblythrough the isolation valve 28,the purge valve 15 being kept closed.
When, however it is necessary to reactivate the filter element 11 the supply of impurefluid is halted by stopping the comp-dsor 24 and the purge valve 15 is opened allowing filtered fluid containing adsorbate at very low partial pressure to flow back through the filter element 11 from the storage vessel 18. The presence of the restrictor 19 ensures that as fluid flows back from the storage vessel 18 it will expand thereby providing a large volume of fluid containing adsorbate at very low partial pressure to reactivate the filter element 11. When sufficient fluid as passed through the filter element 11 to reduce the amount of adsorbate trapped in the filter element 11 to an acceptable level the purge valve 15 is closed and the supply of impure fluid can be resumed by starting the compressor 24.
To prevent fluid flowing back into the compressor 2 GB 2 172 521 A 2 24 when it is stopped, to allow the filter element 11 to be reactivated, a non-return valve 29 is fitted into the fluid inlet 12.
With reference to Fig. 2 there is shown a reactivateable adsorption filter assembly which is 70 in many respects similar to that previously described with respect to Fig. 1 and will function in a similar manner.
In Fig. 2 there is shown a source 110 of impure fluid for supply to the reactivateable adsorption filter assembly by a compressor 124 driven by a motor 125 the compressor supplying fluid to a fluid inlet 112 of the filter assembly.
The fluid inlet 112 is connected through a non return valve 129 to a reactivateable adsorption filter 80 element 111 and through a purge valve 115 to an external source 114 of fluid at a pressure lower than that normally present in the filter element 111.
The purge valve 115 is opened or closed in response to a control signal sent from an external 85 electronic control unit, unit 130.
A fluid outlet 113 connects the element 11 to a reservoir 116 and a storage vessel 118. An isolation valve 128 is connected to the fluid outlet 113 to selectively isolate the filter assembly from an external fluid receiving means 123 for which filtered fluid is required.
A non-return valve 117 is connected into the fluid outlet 113 between a position of connection 121 of the reservoir 116 to the f!uid outlet 113 and a 95 position of 122 of the storage vessel 118 to the fluid outlet 113.
A pressure transducer 127 is connected to the fluid outlet 113 and provides a feedback of outlet pressure to the electronic control unit 130.
A restrictor 119 is positioned between the storage vessel 118 and the fluid outlet 113 to restrict the flow of fluid into and out of the storage vessel 118. Valve means in the form of a valve arrangement comprising a shut off valve 126 and a 105 non-return valve 133 is provided to prevent fluid entering the storage vessel 118 or the reservoir 116 before sufficient pressure level has been reached in the filter element 111. The non-return valve 133 being arranged to allow fluid to flow from the 110 storage vessel 118 towards the filter element 111 but to prevent flow in the opposite direction. The arrangement is therefore such that fluid can only flow into the storage vessel 118 when the shut off valve 12 is open.
Operation of the filter assembly is substantially as described with reference to Fig. 1 the filter element 111 being reactivateable by opening the purge valve 115 and stopping the compressor 124 thereby allowing filtered fluid to flow back from the 120 storage vessel 118 to the sou rce 114.
With reference to Fig. 3 there is shown a second modified reactivateable adsorption filter assembly which in many respects is similar to that previously described with respect to Fig. 1 and which will 125 function in a similar manner.
In Fig. 3 there is shown a source 210 of impure fluid for supply to the reactivateable adsorption filter assembly by means of a compressor 224 driven by a motor 225, the compressor 224 supplying fluid to a fluid inlet 212 of the filter assembly.
The fluid inlet 212 is connected through a nonreturn valve 229 to a reactivateable adsorption filter element 211 and through a purge valve 215 to an external source 214 of fluid at a pressure lower than that normally present in the filter element 211.
The purge valve 215 is opened or closed in response to a control signal sent from an external 75 electronic control unit 230.
A fluid outlet 213 connects the filter element 211 to a reservoir 216 and to a storage vessel 218 used to store filtered fluid.
An isolation valve 228 is connected to the fluid outlet 213 to selectively isolate the filter assembly from an external fluid receiving means 223 for which filtered fluid is required.
A non-return valve 217 is connected in the fluid outlet 213 between a position of connection 221 of the reservoir 216 to the fluid outlet 213 and a position of connection 222 of the storage vessel 218 to the fluid outlet 213.
A pressure transducer 227 is connected to the fluid outlet 213 to provide a feedback of outlet 90 pressure to the electronic control unit 230.
A restrictor 219 is positioned between the storage vessel 218 and the fluid outlet 213 to restrict the flow of fluid into and out of the storage vessel 218.
A Valve means, in the form of a valve arrangement comprising a non-return valve 231 and a pressure relief valve 232 connected in parallel, is located between the restrictor 219 and the fluid outlet 213.
The arrangement of the non-return valve 231 and the pressure relief valve 232 is such that a predetermined pressure is always maintained in the storage vessel 218. This is achieved by arranging for the pressure relief valve 232 to close at this predetermined pressure preventing any further loss of fluid from the storage vessel 218. The residual pressure remaining in the storage vessel 218 will prevent any fluid from entering the storage vessel 218 until the pressure in the fluid outlet 213 exceeds the residual pressure in the storage vessel 218. When the pressure in the fluid outlet 213 does exceed the residual pressure in the storage vessel 218, it will open the non-return valve 231 and fluid will flow into the storage vessel 218.
The non-return valve 231 and the pressure relief valve 232 therefore operate to prevent fluid entering the storage vessel 218 until a predetermined pressure has been reached.
Operation of the reactivateable adsorption filter assembly is substantially as desccribed with reference to Fig. 1, to reactivate the filter element 211 the purge valve 215 is opened and the compressor 224 is stopped thereby allowing fluid to flow back from the storage vessel 218 through the restrictor 219, the pressure relief valve 232 and the filter element 211 to the low pressure source 214.
Although the invention has been described with reference to three specific embodiments in which in each case the purge valve and the isolation valve 3 GB 2 172 521 A 3 have been controlled by an electronic control unit it will be appreciated by those skilled in the art that these valves could be manually controlled without reducing the advantageous effects of the invention.
In addition the source of low pressure could be merely the surrounding atmosphere or it could be a chamber or tank evacuated to provide a partial vacuum.

Claims (11)

1. A reactivateable adsorption filter assembly comprising a high pressure adsorption filter element, a storage vessel to store filtered fluid, containing adsorbate at low partial pressure, a flow restrictor and a purge valve selectively operable to 45 vent the filter assembly to a source of fluid at a lower pressure, the arrangement being such that when the purge valve is opened filtered fluid containing adsorbate at a very low partial pressure flows back from the storage vessel through the filter element to the source of fluid at lower pressure thereby reactivating the filter element.
2. A filter assembly as claimed in claim 1 in which the assembly further comprises a fluid inlet to which is connected the purge valve.
3. A filter assembly as claimed in claim 1 or in claim 2 in which the assembly furfher comprises a fluid outlet to which is connected the storage vessel.
4. A filter assembly as claimed in any preceding claim in which the assembly further comprises a reservoir connected to the fluid outlet.
5. A filter assembly as claimed in claim 4 in which the assembly further comprises means to prevent liquid flowing from the reservoir towards the filter element.
6. A filter assembly as claimed in any preceding claim in which the assembly further comprises a coalescer connected to the fluid inlet upstream from the filter element.
7. A filter assembly as claimed in any preceding claim in which the assembly further comprises an isolation valve connected to the fluid downstream from the reservoir.
8. A filter assembly as claimed in any preceding claim in which the assembly further comprises valve means to prevent the flow of fluid into the storage vessel before the pressure in the filter element has reached a pre-determined level.
9. A filter assembly as claimed in claim 8 in which the valve means comprises a pressure relief valve and a non-return valve arranged in parallel and connected to the fluid outlet.
10. A filter assembly as claimed in claim 8 in which the valve means comprises of shut-off valve connected in the fluid outlet between the storage vessel and the filter element.
11. A reactivateable adsorption filter assembly substantially as described herein with reference to the accompanying drawings.
Printed for Her Majesty's Stationery Office by Courier Press, Leamington Spa, 911986. Demand No. 8817356. Published by the Patent Office, 25 Southampton Buildings, London, WC2A lAY, from which copies may be obtained.
GB8604165A 1985-03-21 1986-02-20 A reactivateable adsorption filter assembly Expired GB2172521B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB858507397A GB8507397D0 (en) 1985-03-21 1985-03-21 Reactivateable adsorption filter

Publications (3)

Publication Number Publication Date
GB8604165D0 GB8604165D0 (en) 1986-03-26
GB2172521A true GB2172521A (en) 1986-09-24
GB2172521B GB2172521B (en) 1989-07-12

Family

ID=10576403

Family Applications (2)

Application Number Title Priority Date Filing Date
GB858507397A Pending GB8507397D0 (en) 1985-03-21 1985-03-21 Reactivateable adsorption filter
GB8604165A Expired GB2172521B (en) 1985-03-21 1986-02-20 A reactivateable adsorption filter assembly

Family Applications Before (1)

Application Number Title Priority Date Filing Date
GB858507397A Pending GB8507397D0 (en) 1985-03-21 1985-03-21 Reactivateable adsorption filter

Country Status (5)

Country Link
US (1) US4663033A (en)
EP (1) EP0199430A3 (en)
CA (1) CA1289482C (en)
GB (2) GB8507397D0 (en)
NO (1) NO861011L (en)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5096598A (en) * 1990-02-26 1992-03-17 Sullair Corporation Pressurized purging of a liquid drain for a vacuum system
DE19618022A1 (en) * 1996-05-04 1997-11-06 Bluecher Gmbh Restoring the activity of adsorption filters made e.g. of carbon@ filter
CA2784047C (en) 2011-07-29 2015-08-11 Milwaukee Electric Tool Corporation Tape measure
US9080849B2 (en) 2011-07-29 2015-07-14 Milwaukee Electric Tool Corporation Tape measure
US8863399B2 (en) 2011-08-26 2014-10-21 Milwaukee Electric Tool Corporation Tape measure
US9267778B2 (en) 2012-01-19 2016-02-23 Milwaukee Electric Tool Corporation Tape measure
USD733597S1 (en) 2012-07-30 2015-07-07 Milwaukee Electric Tool Corporation Tape measure
USD785475S1 (en) 2015-12-10 2017-05-02 Milwaukee Electric Tool Corporation Tape measure
USD785476S1 (en) 2015-12-10 2017-05-02 Milwaukee Electric Tool Corporation Tape measure
USD783430S1 (en) 2016-01-07 2017-04-11 Milwaukee Electric Tool Corporation Tape measure
USD787347S1 (en) 2016-01-07 2017-05-23 Milwaukee Electric Tool Corporation Tape measure
USD783429S1 (en) 2016-01-07 2017-04-11 Milwaukee Electric Tool Corporation Tape measure
USD788611S1 (en) 2016-06-01 2017-06-06 Milwaukee Electric Tool Corporation Tape measure

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1120483A (en) * 1965-03-01 1968-07-17 Union Carbide Canada Ltd Natural gas purification
GB1230833A (en) * 1967-07-12 1971-05-05
GB1238325A (en) * 1968-08-02 1971-07-07
GB1388256A (en) * 1972-03-20 1975-03-26 Fortuna Werke Maschf Ag Backflush filter apparatus
GB2024035A (en) * 1978-03-06 1980-01-09 Antipoll Recycling Consult Removing residual moisture from adsorbers
US4317732A (en) * 1980-09-08 1982-03-02 Andrew Engineering, Inc. Liquid reconditioning system
GB2106798A (en) * 1981-10-03 1983-04-20 Ceag Verfahrenstechnik Gmbh Apparatus for adsorbing and desorbing a substance and recovering the desorbed substance substantially free of water

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1054373A (en) * 1963-05-17
US3395511A (en) * 1963-10-03 1968-08-06 Atlas Copco Ab Method and means for obtaining dry gas or air
US3778967A (en) * 1971-01-18 1973-12-18 Air Technologies Inc Apparatus and process for the fractionation by the adsorption of a compressed gas
US3922149A (en) * 1974-01-30 1975-11-25 Garrett Corp Oxygen air enrichment method
EP0046369B2 (en) * 1980-08-18 1990-02-28 Normalair-Garrett (Holdings) Limited Molecular sieve type gas separation systems
EP0108140A1 (en) * 1982-05-07 1984-05-16 Marathon Medical Equipment Corporation Oxygen concentrator
US4561865A (en) * 1983-11-01 1985-12-31 Greene & Kellogg, Inc. Single bed pressure swing adsorption gas separation system

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1120483A (en) * 1965-03-01 1968-07-17 Union Carbide Canada Ltd Natural gas purification
GB1230833A (en) * 1967-07-12 1971-05-05
GB1238325A (en) * 1968-08-02 1971-07-07
GB1388256A (en) * 1972-03-20 1975-03-26 Fortuna Werke Maschf Ag Backflush filter apparatus
GB2024035A (en) * 1978-03-06 1980-01-09 Antipoll Recycling Consult Removing residual moisture from adsorbers
US4317732A (en) * 1980-09-08 1982-03-02 Andrew Engineering, Inc. Liquid reconditioning system
GB2106798A (en) * 1981-10-03 1983-04-20 Ceag Verfahrenstechnik Gmbh Apparatus for adsorbing and desorbing a substance and recovering the desorbed substance substantially free of water

Also Published As

Publication number Publication date
EP0199430A2 (en) 1986-10-29
US4663033A (en) 1987-05-05
GB2172521B (en) 1989-07-12
CA1289482C (en) 1991-09-24
GB8507397D0 (en) 1985-05-01
GB8604165D0 (en) 1986-03-26
NO861011L (en) 1986-09-22
EP0199430A3 (en) 1987-09-30

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Legal Events

Date Code Title Description
732 Registration of transactions, instruments or events in the register (sect. 32/1977)
732E Amendments to the register in respect of changes of name or changes affecting rights (sect. 32/1977)
732E Amendments to the register in respect of changes of name or changes affecting rights (sect. 32/1977)
PE20 Patent expired after termination of 20 years

Effective date: 20060219