CN201543353U - Hydrogen oxygen gas-water separator - Google Patents

Hydrogen oxygen gas-water separator Download PDF

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Publication number
CN201543353U
CN201543353U CN2009202120500U CN200920212050U CN201543353U CN 201543353 U CN201543353 U CN 201543353U CN 2009202120500 U CN2009202120500 U CN 2009202120500U CN 200920212050 U CN200920212050 U CN 200920212050U CN 201543353 U CN201543353 U CN 201543353U
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CN
China
Prior art keywords
gas
separator
cylinder
water
separation
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.)
Expired - Fee Related
Application number
CN2009202120500U
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Chinese (zh)
Inventor
包秀敏
吕国爱
宋维生
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Shanghai COCH Energy Co Ltd
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Shanghai COCH Energy Co 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.)
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Publication date
Application filed by Shanghai COCH Energy Co Ltd filed Critical Shanghai COCH Energy Co Ltd
Priority to CN2009202120500U priority Critical patent/CN201543353U/en
Application granted granted Critical
Publication of CN201543353U publication Critical patent/CN201543353U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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Abstract

The utility model belongs to an oxy-hydrogen machine, in particular to a hydrogen oxygen gas-water separator. The gas-water separator of an oxy-hydrogen machine in prior art adopts simple gas-water separation and has the disadvantages that: the gas for gas-water separation enters a separator cylinder to form eddy, if the drainage is not carried out in time, the gas discharged from the gas outlet on top can contain alkaline liquor, so the purity of the gas produced by the separator is greatly reduced, and the alkaline liquor has stronger erosive effect on the internal pipelines and the external parts. The hydrogen oxygen gas-water separator is composed of a gas outlet (1), a gas inlet (6), a separation cylinder (7) and a drain outlet (8), wherein a separator inner cylinder (4) is arranged in the separation cylinder (7), and water is filled in the inner lower part of a scrubber (2). The utility model has the advantages that: the content of alkaline liquor in the gas is reduced, and the quality and purity of the gas are accordingly improved; the gas separation purity is improved; the gas productivity is improved; the structure is simple and the production is easy; the gas separation effect is improved and the labor power is saved.

Description

The oxyhydrogen separator
Technical field
The utility model belongs to oxyhydrogen machine, specifically a kind of oxyhydrogen separator.
Background technology
Hydrogen is a kind of efficient, free of contamination novel energy, has extensively and important use in technical fields such as national defense industry, communications and transportation, Metal Cutting, medical and health.Oxyhydrogen machine is to utilize water electrolysis to produce the electrochemical apparatus of hydrogen and oxygen.The oxyhydrogen machine steam-water separator is an equipment of separation of hydrogen oxygen, with having the hydrogen and the oxygen electrolyte of pressurization in the oxyhydrogen machine, is transported in the moisture trap and separates.The oxyhydrogen machine moisture trap adopts simple tubular gas-water separation, air inlet is arranged on highly place of tube last 2/3, the gas outlet is at the top, sewage draining exit is in the bottom of tube, after entering separator, in separator, rotate the air inlet of the gas that has water by separator, according to the difference of the gentle proportion of water, light gas is discharged by the top steam vent of separator, and the water of separation is discharged by the sewage draining exit of separator bottom.Its shortcoming is: the gas for the treatment of gas-water separation enters formation whirlpool shape in the separator cartridge, untimely as blowdown, the gas that can cause the gas outlet, top to be discharged is carried alkali lye secretly, its gas purity that produces is reduced greatly, and can cause stronger corrosion to internal duct and outside workpiece.Mix in gas so invent a kind of minimizing alkali lye, improve gas separation effect, the quality and the purity of gas are improved, and the oxyhydrogen separator of free electrolyte is with practical value and social effect.
The utility model content
The purpose of this utility model provides a kind of minimizing alkali lye and mixes in gas, improves gas separation effect, and the quality and the purity of gas are improved, the oxyhydrogen separator of free electrolyte.
The purpose of this utility model is achieved in that
The oxyhydrogen separator is made up of gas outlet, air inlet, cylinder and sewage draining exit, and cylinder inside is provided with the separator inner core, and the bottom is added with water in the washer on cylinder top.
Add the multiple layer metal silk screen in the separator inner core.
Link to each other by pipeline between washer and cylinder.
Main points of the present utility model are: cylinder inside is provided with the separator inner core, and adds the multiple layer metal silk screen in the separator inner core.
Gas is rotated down along the cylinder inwall after entering cylinder from air inlet, and contained humidity in the gas makes the gas in the gas be separated with moisture because himself gravity effect is moved vertically downward; The water of separating is discharged by sewage draining exit, gas separated enters the separator inner core, adds the multiple layer metal silk screen in the separator inner core, removes the foam that produces in the gas, play the foam removal filtration, the foam that produces in the gas outputs to oxyhydrogen separator outside by sewage draining exit; Gas enters after foam removal in the washer, is added with water seal in the washer and enters in the second-stage separator when oxyhydrogen, and the alkaline droplet in the washer in water filtration and the washing gas obtains pure hydrogen or oxygen from the washer gas outlet.
Link to each other by pipeline between washer and cylinder, the washer bottom prevents that the structure that water flows into the cylinder place from being the known technology of this area.
Advantage of the present utility model is as follows:
1. reduce alkali lye and mix in gas, the quality and the purity of gas are improved.
2. improve the gas separation purity.
3. improve the production efficiency of gas.
4. simple in structure, produce easily.
5. the lift gas separating effect has been saved manpower.
Description of drawings
Fig. 1 is the utility model oxyhydrogen separator structure chart.
Among the figure: 1 is the gas outlet, and 2 is washer, and 3 is water, and 4 is the separator inner core, and 5 is woven wire, and 6 is air inlet, and 7 is cylinder, and 8 is sewage draining exit.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described further by specific embodiment.
Embodiment 1:
Air inlet 6 is arranged on the cylinder 7 2/3 place highly, washer 2 links to each other by pipeline with 7 of cylinders, separator inner core 4 is located in the bottom cylinder 7 of pipeline, and gas outlet 1 is located at washer 2 tops, and sewage draining exit 8 is located on the cylinder 7 side relative with air inlet 6.
Hydrogen is rotated down along cylinder 7 inwalls after entering cylinder 7 from oxyhydrogen separator air inlet 6, and contained humidity in the hydrogen makes the hydrogen in the hydrogen that contains moisture be separated with moisture because himself gravity effect is moved vertically downward; The water of separating is discharged by sewage draining exit 8, and the hydrogen that separates moisture enters in the separator inner core 4, and the three-layer metal silk screen 5 of separator inner core is removed the foam that produces in the hydrogen, and the foam that produces in the hydrogen outputs to oxyhydrogen separator outside by sewage draining exit 8; Hydrogen enters after foam removal in the washer 2, and 1/2 water 3 is equipped with in washer 2 inside, and water 3 filters and wash the alkaline droplet in the hydrogen, when the hydrogen that contains alkaline droplet enters in the second-stage separator, obtains pure hydrogen from washer gas outlet 1.
Embodiment 2:
Air inlet 6 is arranged on the cylinder 7 2/3 place highly, washer 2 links to each other by pipeline with 7 of cylinders, separator inner core 4 is located at the bottom of cylinder 7 interior conduits, and gas outlet 1 is located at washer 2 tops, and sewage draining exit 8 is located on the cylinder 7 side relative with air inlet 6.
Oxygen is rotated down along cylinder 7 inwalls after entering cylinder 7 from oxyhydrogen separator air inlet 6, and contained humidity in the oxygen makes the oxygen in the oxygen that contains moisture be separated with moisture because himself gravity effect is moved vertically downward; The water of separating is discharged by sewage draining exit 8, and the oxygen that separates moisture enters in the separator inner core 4, and the three-layer metal silk screen 5 of separator inner core is removed the foam that produces in the oxygen, and the foam that produces in the oxygen outputs to oxyhydrogen separator outside by sewage draining exit 8; Oxygen enters after foam removal in the washer 2, and 1/2 water 3 is equipped with in washer 2 inside, and water 3 filters and wash the alkaline droplet in the oxygen, when the oxygen that contains alkaline droplet enters in the second-stage separator, obtains pure oxygen from washer gas outlet 1.
The above is a preferred embodiment of the present utility model only, is not limited to the utility model.For a person skilled in the art any change and conversion can be arranged.All any changes of in spirit of the present utility model and principle scope, being made, change or be equal to replacement etc. and all should be included in the protection domain of the present utility model.

Claims (3)

1. an oxyhydrogen separator is made up of gas outlet (1), air inlet (6), cylinder (7) and sewage draining exit (8), it is characterized in that: cylinder (7) inside is provided with separator inner core (4), and the interior bottom of washer (2) on cylinder (7) top is added with water (3).
2. oxyhydrogen separator according to claim 1 is characterized in that: add multiple layer metal silk screen (5) in the separator inner core (4).
3. oxyhydrogen separator according to claim 1 is characterized in that: link to each other by pipeline between washer (2) and cylinder (7).
CN2009202120500U 2009-11-10 2009-11-10 Hydrogen oxygen gas-water separator Expired - Fee Related CN201543353U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009202120500U CN201543353U (en) 2009-11-10 2009-11-10 Hydrogen oxygen gas-water separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009202120500U CN201543353U (en) 2009-11-10 2009-11-10 Hydrogen oxygen gas-water separator

Publications (1)

Publication Number Publication Date
CN201543353U true CN201543353U (en) 2010-08-11

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009202120500U Expired - Fee Related CN201543353U (en) 2009-11-10 2009-11-10 Hydrogen oxygen gas-water separator

Country Status (1)

Country Link
CN (1) CN201543353U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102061485A (en) * 2010-11-23 2011-05-18 苏州竞立制氢设备有限公司 Disc separator
CN103480227A (en) * 2013-09-30 2014-01-01 延吉市意来净水机制造有限公司 Gas-water separator of hydrogen generation device
CN103526222A (en) * 2013-10-11 2014-01-22 苏州竞立制氢设备有限公司 Oxyhydrogen scrubber used in water electrolysis for hydrogen production
CN107008096A (en) * 2017-05-24 2017-08-04 武汉轻工大学 A kind of hydrogen from methyl alcohol vacuum desorption qi exhaustion removes mist water system
CN113828124A (en) * 2021-11-01 2021-12-24 佛山市益发智能科技有限公司 Gas-water separator assembly

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102061485A (en) * 2010-11-23 2011-05-18 苏州竞立制氢设备有限公司 Disc separator
CN102061485B (en) * 2010-11-23 2013-01-02 苏州竞立制氢设备有限公司 Disc separator
CN103480227A (en) * 2013-09-30 2014-01-01 延吉市意来净水机制造有限公司 Gas-water separator of hydrogen generation device
CN103480227B (en) * 2013-09-30 2015-04-22 延吉市意来净水机制造有限公司 Gas-water separator of hydrogen generation device
CN103526222A (en) * 2013-10-11 2014-01-22 苏州竞立制氢设备有限公司 Oxyhydrogen scrubber used in water electrolysis for hydrogen production
CN107008096A (en) * 2017-05-24 2017-08-04 武汉轻工大学 A kind of hydrogen from methyl alcohol vacuum desorption qi exhaustion removes mist water system
CN113828124A (en) * 2021-11-01 2021-12-24 佛山市益发智能科技有限公司 Gas-water separator assembly

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100811

Termination date: 20151110

EXPY Termination of patent right or utility model