GB2122105A - Water-gas separator - Google Patents

Water-gas separator Download PDF

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Publication number
GB2122105A
GB2122105A GB08217489A GB8217489A GB2122105A GB 2122105 A GB2122105 A GB 2122105A GB 08217489 A GB08217489 A GB 08217489A GB 8217489 A GB8217489 A GB 8217489A GB 2122105 A GB2122105 A GB 2122105A
Authority
GB
United Kingdom
Prior art keywords
liquid
inlet
collector
casing
gas flow
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.)
Withdrawn
Application number
GB08217489A
Inventor
Robert Steuart Gladstone
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.)
Coopers Filters Ltd
Original Assignee
Coopers Filters 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 Coopers Filters Ltd filed Critical Coopers Filters Ltd
Priority to GB08217489A priority Critical patent/GB2122105A/en
Priority to GB08315853A priority patent/GB2122106B/en
Priority to SE8303386A priority patent/SE8303386L/en
Priority to FR8309808A priority patent/FR2528716B1/en
Priority to DE3321688A priority patent/DE3321688A1/en
Priority to IT8348507A priority patent/IT8348507A0/en
Priority to ES523329A priority patent/ES523329A0/en
Publication of GB2122105A publication Critical patent/GB2122105A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/04Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
    • B01D45/06Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by reversal of direction of flow
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M35/00Combustion-air cleaners, air intakes, intake silencers, or induction systems specially adapted for, or arranged on, internal-combustion engines
    • F02M35/02Air cleaners
    • F02M35/022Air cleaners acting by gravity, by centrifugal, or by other inertial forces, e.g. with moistened walls

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Separation Of Particles Using Liquids (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Electrostatic Separation (AREA)

Abstract

Water droplets are removed from air being fed to an I.C. engine by causing the air to change direction, in passage from inlet slot 7 to outlet 6, adjacent to a wire mesh pad 9 backed by impervious wall 8, so that entrained water droplets impinge on the pad and flow down it to outlet 11. <IMAGE>

Description

SPECIFICATION Improvements in and relating to air cleaners This invention relates to air cleaners and in particular to apparatus for at least reducing the amount of liquid entrained in an airstream entering an air cleaner. Where a conventional air - cleaner is used two filter the airflow to an internal combustion engine, it is often important to remove entrained liquid to -at least reduce it to an acceptable level. Paper air filters are not wellsuited to handling mixed liquid air flows. Water vapour is fairly well tolerated and may improve combustion efficiency. On the other hand, the levels of entrained liquid are often extremely high in the vicinity of road vehicles travelling at speed in wet weather.
Known liquid separators make use of centrifugal force and/or a sudden change of airstream direction which causes the heavier water particles/droplets to become ballistically separated from the airstream onto some form of collector surface which is connected to a drain aperture or channel. These known separators are not particularly efficient and it has been proposed that the airstream should be passed through a coarse wire mesh. The latter is known for its ability to coalesce droplets of liquid from an airstream, but where the throughput of wet air is high, the mesh may become "plugged" releasing quantities of water in the downstream direction At low temperatures the mesh may also-ice up.
According to the present invention a liquid separator comprises a casing containing liquid collector means in the form of a foraminous reticulated structure, and having an inlet and an outlet, the inlet being configured to create an inlet gas flow towards said collector means whereat said flow is caused to undergo a change of direction such that said droplets are ballistically separated from the gas flow and are received on the collector means. Preferably the inlet is in the form of a slot effective to accelerate the liquid droplet containing gas flow towards the collector means. The collector means is preferably constituted by a wire mesh pad on an impermeable support.
Preferably also, the liquid collector is so disposed as to be self-draining, liquid outlet means being provided for removing collected liquid to the outside of the casing.
Where the inlet communicates directly with a liquid-laden gaseous atmosphere, it is preferred that the margins of the inlet are shaped to deflect and/or exclude liquid which may collect on the external or internal surface of the casing. In particular, it is important to minimise the amount of such liquid which becomes entrained by the gas flow into the inlet.
As previously stated, it is advantageous to make the liquid collector means self-draining, under gravity. It is also convenient to make the gas flow generally upwardly over the liquid collector, i.e. against gravity, to enhance the separation effect.
In order that the invention be better understood preferred embodiments of it will now be described with reference to the accompanying drawing in which:~ Figure 1 is a cross-sectional side view of a liquid separator according to the invention, and Figure 2 is a cross-sectional side view of a modified liquid separator according to the invention.
In the figures, a casing 5 has an outlet 6 and a slot inlet 7. A liquid collector comprising an impermeable support 8 and a layer of steel wire mesh 9 is mounted inside the casing so that gas entering through the slot 7 has to undergo an abrupt change of.direction from slightly downwards (relative to the top of the casing) to a vertical or near vertical path along the surface of the-mesh 9, before passing around the end of an impermeable retaining cap 4, towards the outlet.
The cap 4 serves to minimise re-entrainment of liquid collected on the mesh, whilst an outlet 11 serves to drain the latter. In Figure 2 collector tubes 12 serve to accomplish this function, to the sides of the casing.
The slot has an upper lip in the form of an external channel 3 disposed to prevent liquid dripping directly into the inlet. The lip also has an internal channel 13 to serve the same purpose internally of the casing. The opposed edge 14 of the slot is also rounded, to smooth the inlet gas flow.
It will be appreciated that Figure 2 features two slots and two liquid collectors, as well as a differently directed outlet. Two slots enable a greater throughput.
In one practical embodiment based on Figure 1, the casing was generally rectangular with a slot dimension 2 in the range 20 to 30 mm, the exact size being selected so that for a given slot width, the peak flow velocity into the casing was about 20 m/s. The dimension 1 was about 40 mm, the wire mesh 9 being about 12 mm thick. The separator exhibited an overall pressure drop (from inlet to outlet) of about 55 mm of water.
On test with air artificially loaded with large quantities of water (by spraying), the separator removed about 85% of the water supplied to it. It was extremely effective.
1. Apparatus for separating liquid from a gas flow containing liquid droplets, the apparatus comprising a casing containing liquid collector means in the form of a foraminous reticulated structure having an inlet and an outlet, the inlet being configured to create an inlet gas flow towards said collector means whereat said flow is caused to undergo a change of direction such that said droplets are ballistically separated from the gas flow and are received on the collector means.
2. Apparatus according to claim 1 wherein the inlet is in the form of a slot effective to accelerate the liquid droplet containing gas flow towards the collector means.
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (7)

**WARNING** start of CLMS field may overlap end of DESC **. SPECIFICATION Improvements in and relating to air cleaners This invention relates to air cleaners and in particular to apparatus for at least reducing the amount of liquid entrained in an airstream entering an air cleaner. Where a conventional air - cleaner is used two filter the airflow to an internal combustion engine, it is often important to remove entrained liquid to -at least reduce it to an acceptable level. Paper air filters are not wellsuited to handling mixed liquid air flows. Water vapour is fairly well tolerated and may improve combustion efficiency. On the other hand, the levels of entrained liquid are often extremely high in the vicinity of road vehicles travelling at speed in wet weather. Known liquid separators make use of centrifugal force and/or a sudden change of airstream direction which causes the heavier water particles/droplets to become ballistically separated from the airstream onto some form of collector surface which is connected to a drain aperture or channel. These known separators are not particularly efficient and it has been proposed that the airstream should be passed through a coarse wire mesh. The latter is known for its ability to coalesce droplets of liquid from an airstream, but where the throughput of wet air is high, the mesh may become "plugged" releasing quantities of water in the downstream direction At low temperatures the mesh may also-ice up. According to the present invention a liquid separator comprises a casing containing liquid collector means in the form of a foraminous reticulated structure, and having an inlet and an outlet, the inlet being configured to create an inlet gas flow towards said collector means whereat said flow is caused to undergo a change of direction such that said droplets are ballistically separated from the gas flow and are received on the collector means. Preferably the inlet is in the form of a slot effective to accelerate the liquid droplet containing gas flow towards the collector means. The collector means is preferably constituted by a wire mesh pad on an impermeable support. Preferably also, the liquid collector is so disposed as to be self-draining, liquid outlet means being provided for removing collected liquid to the outside of the casing. Where the inlet communicates directly with a liquid-laden gaseous atmosphere, it is preferred that the margins of the inlet are shaped to deflect and/or exclude liquid which may collect on the external or internal surface of the casing. In particular, it is important to minimise the amount of such liquid which becomes entrained by the gas flow into the inlet. As previously stated, it is advantageous to make the liquid collector means self-draining, under gravity. It is also convenient to make the gas flow generally upwardly over the liquid collector, i.e. against gravity, to enhance the separation effect. In order that the invention be better understood preferred embodiments of it will now be described with reference to the accompanying drawing in which:~ Figure 1 is a cross-sectional side view of a liquid separator according to the invention, and Figure 2 is a cross-sectional side view of a modified liquid separator according to the invention. In the figures, a casing 5 has an outlet 6 and a slot inlet 7. A liquid collector comprising an impermeable support 8 and a layer of steel wire mesh 9 is mounted inside the casing so that gas entering through the slot 7 has to undergo an abrupt change of.direction from slightly downwards (relative to the top of the casing) to a vertical or near vertical path along the surface of the-mesh 9, before passing around the end of an impermeable retaining cap 4, towards the outlet. The cap 4 serves to minimise re-entrainment of liquid collected on the mesh, whilst an outlet 11 serves to drain the latter. In Figure 2 collector tubes 12 serve to accomplish this function, to the sides of the casing. The slot has an upper lip in the form of an external channel 3 disposed to prevent liquid dripping directly into the inlet. The lip also has an internal channel 13 to serve the same purpose internally of the casing. The opposed edge 14 of the slot is also rounded, to smooth the inlet gas flow. It will be appreciated that Figure 2 features two slots and two liquid collectors, as well as a differently directed outlet. Two slots enable a greater throughput. In one practical embodiment based on Figure 1, the casing was generally rectangular with a slot dimension 2 in the range 20 to 30 mm, the exact size being selected so that for a given slot width, the peak flow velocity into the casing was about 20 m/s. The dimension 1 was about 40 mm, the wire mesh 9 being about 12 mm thick. The separator exhibited an overall pressure drop (from inlet to outlet) of about 55 mm of water. On test with air artificially loaded with large quantities of water (by spraying), the separator removed about 85% of the water supplied to it. It was extremely effective. CLAIMS
1. Apparatus for separating liquid from a gas flow containing liquid droplets, the apparatus comprising a casing containing liquid collector means in the form of a foraminous reticulated structure having an inlet and an outlet, the inlet being configured to create an inlet gas flow towards said collector means whereat said flow is caused to undergo a change of direction such that said droplets are ballistically separated from the gas flow and are received on the collector means.
2. Apparatus according to claim 1 wherein the inlet is in the form of a slot effective to accelerate the liquid droplet containing gas flow towards the collector means.
3. Apparatus according to claim 1 or claim 2 wherein the collector means is a foraminous reticulated structure constituted by a wire mesh pad on an impermeable support.
4. Apparatus according to any preceding claim wherein the collector is so disposed as to be selfdraining, liquid outlet means being provided for removing collected liquid to the outside of the casing.
5. Apparatus according to any preceding claim wherein the margins of the inlet are shaped to deflect and/or exclude liquid which may collect on the external and/or internal surface of the casing and flow towards said inlet.
6. Apparatus according to any preceding claim wherein the collector is at least in part approximately vertically disposed and the gas flow is initially directed towards the collector and is then caused to flow generally upwardly over the surface of the collector.
7. Apparatus for separating liquid from a gas flow containing liquid droplets substantially as herein before described with reference to and.as illustrated by the accompanying drawing.
GB08217489A 1982-06-16 1982-06-16 Water-gas separator Withdrawn GB2122105A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
GB08217489A GB2122105A (en) 1982-06-16 1982-06-16 Water-gas separator
GB08315853A GB2122106B (en) 1982-06-16 1983-06-09 Water-air separator
SE8303386A SE8303386L (en) 1982-06-16 1983-06-14 AIR CLEANER
FR8309808A FR2528716B1 (en) 1982-06-16 1983-06-14 IMPROVEMENTS ON AIR FILTERS
DE3321688A DE3321688A1 (en) 1982-06-16 1983-06-15 DEVICE FOR SEPARATING LIQUID DROPS TAKEN IN A GAS FLOW
IT8348507A IT8348507A0 (en) 1982-06-16 1983-06-15 APPARATUS TO SEPARATE DROPLETS OF LIQUID ENTRAINED BY A FLOW OF GAS
ES523329A ES523329A0 (en) 1982-06-16 1983-06-16 IMPROVEMENTS IN A DEVICE TO SEPARATE FROM A GAS FLOW LIQUID DROPS DRAGGED BY THE SAME.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB08217489A GB2122105A (en) 1982-06-16 1982-06-16 Water-gas separator

Publications (1)

Publication Number Publication Date
GB2122105A true GB2122105A (en) 1984-01-11

Family

ID=10531093

Family Applications (2)

Application Number Title Priority Date Filing Date
GB08217489A Withdrawn GB2122105A (en) 1982-06-16 1982-06-16 Water-gas separator
GB08315853A Expired GB2122106B (en) 1982-06-16 1983-06-09 Water-air separator

Family Applications After (1)

Application Number Title Priority Date Filing Date
GB08315853A Expired GB2122106B (en) 1982-06-16 1983-06-09 Water-air separator

Country Status (6)

Country Link
DE (1) DE3321688A1 (en)
ES (1) ES523329A0 (en)
FR (1) FR2528716B1 (en)
GB (2) GB2122105A (en)
IT (1) IT8348507A0 (en)
SE (1) SE8303386L (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5114322A (en) * 1986-08-22 1992-05-19 Copeland Corporation Scroll-type machine having an inlet port baffle
US5219281A (en) * 1986-08-22 1993-06-15 Copeland Corporation Fluid compressor with liquid separating baffle overlying the inlet port
CN1056911C (en) * 1994-12-08 2000-09-27 日野自动车工业株式会社 Channel unit structure for duct
CN1056910C (en) * 1994-09-27 2000-09-27 日野自动车工业株式会社 Structure for preventing water from entering into duct
FR2857058A1 (en) * 2003-07-03 2005-01-07 Coutier Moulage Gen Ind Water sedimentation device for air inlet line, has air inlet pipe with bend towards downstream end where water recuperation hole traversing wall of air inlet pipe is provided
EP2401055A2 (en) * 2009-02-27 2012-01-04 Nano-porous Solutions Limited A fluid separation device
EP4154965A1 (en) * 2021-09-24 2023-03-29 Hamilton Sundstrand Corporation Passive phase separator with liquid removal chamber

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009024662A1 (en) * 2009-03-06 2010-09-09 Audi Ag Air filter assembly of a motor vehicle unit
DE102009055958A1 (en) * 2009-11-27 2011-06-01 Afc Air Filtration & Containment Gmbh Device for separating impurities from an air stream
CN115244337A (en) * 2020-01-29 2022-10-25 杰弗瑞·艾伦·泰勒 Kitchen exhaust system and method for removing grease from grease-containing steam

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB251522A (en) *
GB378133A (en) * 1931-06-05 1932-08-11 John Cartmell Improvements in or relating to air cleaners
GB547607A (en) * 1941-04-17 1942-09-03 Talboys Mfg Company Ltd Improvements in and relating to air cleaners
GB808806A (en) * 1954-11-15 1959-02-11 Solomon Saunders Improvements in filters for use in removing noxious gases and solid matter contained in the exhaust gases of internal combustion engines
GB1109693A (en) * 1964-06-05 1968-04-10 Alcatel Sa Method and apparatus for arresting mist entrained in gas currents
GB1594524A (en) * 1977-05-12 1981-07-30 Lerner B J Apparatus for the removal of undesired components from fluids

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE272183C (en) *
US3920422A (en) * 1971-10-18 1975-11-18 Purity Corp Pollution control apparatus and method
DE2501538A1 (en) * 1975-01-16 1976-07-22 Ferroplast Ges Fuer Metallund Droplet separator - esp. for wet scrubbers for dust removal in underground mining machinery
CH621490A5 (en) * 1978-06-02 1981-02-13 Alsthom Atlantique Device used for phase separation in a fluid exhibiting a gaseous phase and a liquid phase

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB251522A (en) *
GB378133A (en) * 1931-06-05 1932-08-11 John Cartmell Improvements in or relating to air cleaners
GB547607A (en) * 1941-04-17 1942-09-03 Talboys Mfg Company Ltd Improvements in and relating to air cleaners
GB808806A (en) * 1954-11-15 1959-02-11 Solomon Saunders Improvements in filters for use in removing noxious gases and solid matter contained in the exhaust gases of internal combustion engines
GB1109693A (en) * 1964-06-05 1968-04-10 Alcatel Sa Method and apparatus for arresting mist entrained in gas currents
GB1594524A (en) * 1977-05-12 1981-07-30 Lerner B J Apparatus for the removal of undesired components from fluids

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5114322A (en) * 1986-08-22 1992-05-19 Copeland Corporation Scroll-type machine having an inlet port baffle
US5219281A (en) * 1986-08-22 1993-06-15 Copeland Corporation Fluid compressor with liquid separating baffle overlying the inlet port
CN1056910C (en) * 1994-09-27 2000-09-27 日野自动车工业株式会社 Structure for preventing water from entering into duct
CN1056911C (en) * 1994-12-08 2000-09-27 日野自动车工业株式会社 Channel unit structure for duct
FR2857058A1 (en) * 2003-07-03 2005-01-07 Coutier Moulage Gen Ind Water sedimentation device for air inlet line, has air inlet pipe with bend towards downstream end where water recuperation hole traversing wall of air inlet pipe is provided
EP2401055A2 (en) * 2009-02-27 2012-01-04 Nano-porous Solutions Limited A fluid separation device
EP4154965A1 (en) * 2021-09-24 2023-03-29 Hamilton Sundstrand Corporation Passive phase separator with liquid removal chamber

Also Published As

Publication number Publication date
ES8404869A1 (en) 1984-05-16
ES523329A0 (en) 1984-05-16
GB2122106A (en) 1984-01-11
SE8303386D0 (en) 1983-06-14
FR2528716B1 (en) 1986-11-28
GB8315853D0 (en) 1983-07-13
FR2528716A1 (en) 1983-12-23
DE3321688A1 (en) 1983-12-22
GB2122106B (en) 1986-01-22
IT8348507A0 (en) 1983-06-15
SE8303386L (en) 1983-12-17

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WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)