CN106222687A - A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution - Google Patents
A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution Download PDFInfo
- Publication number
- CN106222687A CN106222687A CN201610487321.8A CN201610487321A CN106222687A CN 106222687 A CN106222687 A CN 106222687A CN 201610487321 A CN201610487321 A CN 201610487321A CN 106222687 A CN106222687 A CN 106222687A
- Authority
- CN
- China
- Prior art keywords
- liquid
- electrolysis bath
- water tank
- hydro
- circulating pump
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 title claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 58
- 239000007788 liquid Substances 0.000 claims abstract description 57
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 52
- 238000010926 purge Methods 0.000 claims abstract description 9
- 230000005855 radiation Effects 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 19
- 238000010586 diagram Methods 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000036647 reaction Effects 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/05—Pressure cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
nullThe present invention provides a kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution，The problem that on existing equipment, the liquid of water tank cannot flow to electrolysis bath smoothly can be solved，Including frame，It is arranged on the water tank above this frame and multi-stage gas-liquid knockout drum，It is arranged on the chiller below frame、Water circulating pump、Check valve、Purge of gas tank、Air accumulator and electrolysis bath，Described water tank liquid outlet connects the liquid feeding end of described check valve，Described check valve liquid outlet is respectively connecting to the liquid outlet of described electrolysis bath and described water circulating pump by a threeway，Described water circulating pump connects described chiller，Described chiller is connected to the liquid feeding end of described electrolysis bath，The present invention is by being connected directly to the water inlet of water tank in the middle of the liquid circulation loop of electrolysis bath，The liquid in water tank is made to flow in electrolysis bath smoothly，Ensure that the liquid in electrolysis bath is abundant，Ensure the speed of electrolysis，Thus improve the production efficiency of gas.
Description
Technical field
The invention belongs to hydro-electrolytic hydroxide mixed gas equipment technical field, a kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution.
Background technology
Hydro-electrolytic hydroxide mixed gas equipment is a kind of water electrolysis technology that uses, and energising decomposites hydrogen and oxygen from water, and hydrogen is as fuel, and oxygen is as combustion-supporting, and two kinds of gas mixing, are a kind of high-tech novel environment friendly energy devices.nullIt is currently used for the equipment connecting line of hydro-electrolytic hydroxide mixed gas equipment as described in Figure 3，Water tank 4 is connected directly to the liquid feeding end of electrolysis bath 2，And the internal liquid circulation end of electrolysis bath 2 is individually provided with a closed circuit，Closed circuit is provided with check valve 5、Circulating pump 7 and chiller 3，There is a drawback in this pipeline，Liquid in electrolysis bath constantly is electrolysed out gas，Pressure in described electrolysis bath is bigger than the pressure of water tank 4，Although there is drop in water tank 4 and electrolysis bath 2，But still pressure reduction between the two can not be offset，The liquid in electrolysis bath 2 is caused to do alone the circulation cooled down，And the water of water tank 4 is unable to come down，Along with the liquid in electrolysis bath 2 reduces，Cell reaction speed reduces，Pressure in electrolysis bath reduces，The insufficient pressure being reduced in electrolysis bath 2 is when the drop offset in water tank 4，The water of water tank 4 just can slowly flow to electrolysis bath 2，This connecting line drastically influence the efficiency of electrolysis.
Summary of the invention
In order to solve prior art problem, the present invention provides a kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution, it is achieved the water of water tank preferentially participates in the liquid circulation of cooling, allows the water of water tank flow to electrolysis bath smoothly, ensure that the liquid in electrolysis bath is sufficient, it is ensured that production efficiency.
nullFor achieving the above object，Technical scheme provided by the present invention is: a kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution，Including frame，It is arranged on the water tank above this frame、Multi-stage gas-liquid knockout drum and gas purge tank，It is arranged on the chiller below described frame、Water circulating pump、Check valve、Air accumulator and the electrolysis bath of more than a group，Also include the control unit being arranged in described frame，The escape pipe of described upper part of the electrolytic cell is connected to described multi-stage gas-liquid knockout drum，Described knockout drum is sequentially connected with described purge of gas tank and described air accumulator，The liquid back pipe of described gas-liquid separation pot bottom is connected to described water tank，It is characterized in that: described water tank liquid outlet connects the liquid feeding end of described check valve，Described check valve liquid outlet is respectively connecting to the liquid outlet of described electrolysis bath and described water circulating pump by a threeway，Described water circulating pump connects described chiller，Described chiller is connected to the liquid feeding end of described electrolysis bath.
Preferably, described water circulating pump front end is also associated with a S type finned tube acceleration heat radiation.
Preferably, described electrolysis bath is also associated with a constant pressure pump.
Preferably, the minimum liquid level of described water tank is higher than the high level of described electrolysis bath.
Beneficial effects of the present invention:
By the liquid outlet of water tank is connected directly in the middle of the liquid circulation loop of electrolysis bath so that the liquid in water tank can flow in electrolysis bath smoothly, it is ensured that the liquid in electrolysis bath is abundant, it is ensured that the speed of electrolysis, thus improves the production efficiency of gas.
Accompanying drawing explanation
Fig. 1 is the three-dimensional structure diagram of the present invention；
Fig. 2 is the connection diagram of the present invention；
Fig. 3 is the connection diagram that electrolysis bath is two of the present invention；
Fig. 4 is the connection diagram of existing hydro-electrolytic hydroxide mixed gas equipment.
In figure: 1-frame, 2-electrolysis bath, 3-chiller, 4-water tank, 5-check valve, 6-air accumulator, 7-water circulating pump, 8-S type finned tube, 9-knockout drum, 10-purge of gas tank, 11-constant pressure pump, 12-controls unit.
Detailed description of the invention
Below in conjunction with the accompanying drawings and specific embodiment, the invention will be further described:
nullReferring to figs. 1 through Fig. 4，A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution，Including frame 1，It is arranged on the water tank 4 above this frame 1、Multi-stage gas-liquid knockout drum 9 and gas purge tank 10，It is arranged on the chiller 3 below above-mentioned frame 1、Water circulating pump 7、Check valve 5、Air accumulator 6 and the electrolysis bath 2 of more than a group，Also include the control unit 12 being arranged in above-mentioned frame 1，The escape pipe on above-mentioned electrolysis bath 2 top is connected to above-mentioned multi-stage gas-liquid knockout drum 9，Above-mentioned knockout drum 9 is sequentially connected with above-mentioned gas purge tank 10 and above-mentioned air accumulator 6，Liquid back pipe bottom above-mentioned knockout drum 9 is connected to above-mentioned water tank 4，Above-mentioned water tank 4 liquid outlet connects the liquid feeding end of above-mentioned check valve 5，Above-mentioned check valve 5 liquid outlet is respectively connecting to liquid outlet and the above-mentioned water circulating pump 7 of above-mentioned electrolysis bath 2 by a threeway，Above-mentioned water circulating pump 7 connects above-mentioned chiller 3，Above-mentioned chiller 3 is connected to the liquid feeding end of above-mentioned electrolysis bath 2，It should be understood that the position of above-mentioned water circulating pump 7 and above-mentioned chiller 3 can be exchanged.
Concrete, above-mentioned water circulating pump 7 front end is also associated with a S type finned tube 8 and accelerates heat radiation, and the S type finned tube 8 of setting can reduce the use pressure of chiller 3, extends the service life of chiller 3.
Concrete, above-mentioned electrolysis bath 2 is also associated with a constant pressure pump 11, and constant pressure pump 11 mainly ensures the pressure of internal system so that the pressure in electrolysis bath 2 is beneficial to quickly carry out cell reaction in suitable scope.
Concrete, the minimum liquid level of above-mentioned water tank 4, higher than the high level of above-mentioned electrolysis bath 2, by arranging the minimum liquid level of water tank 4 and ensureing more than minimum liquid level, can keep the liquid in electrolysis bath 2 abundant, is beneficial to electrolysis.
When the present invention works: liquid-consumed in electrolysis bath 2, the liquid of water tank 4 flows down supplementary, the interior high-temp liquid of electrolysis bath 2 dispels the heat through S type finned tube 8, again through water circulating pump 7, enter chiller 3 to cool down, guarantee that the temperature of liquid is less than 85 degree, because of beyond 85 degree, the components and parts of whole equipment are injured big, so being limited in less than 85 degree, the service life of the components and parts in guarantee equipment, the gas-carrying portion aqueous vapor of electrolysis bath 2 enters knockout drum 9, liquid in knockout drum 9 has returned to water tank 4, gas continues to enter forward above-mentioned gas purge tank 10 and removes water, enter back into air accumulator 6.
The present invention is by changing the pipeline of existing equipment so that the liquid in water tank 4 can be quickly added in electrolysis bath 2, it is ensured that electrolytic efficiency.
The examples of implementation of the above are only the preferred embodiments of the invention, not limit the practical range of the present invention with this, therefore the change that all shapes according to the present invention, principle are made, all should contain within the scope of the present invention.
Claims (4)
- null1. the hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution，Including frame (1)，It is arranged on the water tank (4) of this frame (1) top、Multi-stage gas-liquid knockout drum (9) and gas purge tank (10)，It is arranged on the chiller (3) of described frame (1) lower section、Water circulating pump (7)、Check valve (5)、Air accumulator (6) and the electrolysis bath (2) of more than a group，Also include the control unit (12) being arranged in described frame (1)，The escape pipe on described electrolysis bath (2) top is connected to described multi-stage gas-liquid knockout drum (9)，Described knockout drum (9) is sequentially connected with described purge of gas tank (10) and described air accumulator (6)，The liquid back pipe of described knockout drum (9) bottom is connected to described water tank (4)，It is characterized in that: described water tank (4) liquid outlet connects the liquid feeding end of described check valve (5)，Described check valve (5) liquid outlet is respectively connecting to liquid outlet and the described water circulating pump (7) of described electrolysis bath (2) by a threeway，Described water circulating pump (7) connects described chiller (3)，Described chiller (3) is connected to the liquid feeding end of described electrolysis bath (2).
- A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution the most according to claim 1, it is characterised in that: described water circulating pump (7) front end is also associated with S type finned tube (8) and accelerates heat radiation.
- A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution the most according to claim 1, it is characterised in that: described electrolysis bath (2) is also associated with a constant pressure pump (11).
- A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution the most according to claim 1, it is characterised in that: the minimum liquid level of described water tank (4) is higher than the high level of described electrolysis bath (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610487321.8A CN106222687B (en) | 2016-06-29 | 2016-06-29 | A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610487321.8A CN106222687B (en) | 2016-06-29 | 2016-06-29 | A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106222687A true CN106222687A (en) | 2016-12-14 |
| CN106222687B CN106222687B (en) | 2018-07-06 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610487321.8A Active CN106222687B (en) | 2016-06-29 | 2016-06-29 | A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106222687B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107188290A (en) * | 2017-05-11 | 2017-09-22 | 玉灵华科技有限公司 | A kind of preparation method of high concentration elementary gas and many matter gas aqueous solution |
| CN112501633A (en) * | 2020-12-28 | 2021-03-16 | 陕西华秦新能源科技有限责任公司 | Large-gas-production-rate oxyhydrogen generator and use method thereof |
| CN112553645A (en) * | 2020-12-28 | 2021-03-26 | 陕西华秦新能源科技有限责任公司 | Electrolytic tank of oxyhydrogen generator and use method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2352544Y (en) * | 1998-05-20 | 1999-12-08 | 王宜清 | Low voltage large current apparatus for producing hydrogen and oxygen |
| JP2002053989A (en) * | 2000-08-03 | 2002-02-19 | Shinko Pantec Co Ltd | System for purifying gas formed by water electrolysis and method for purifying the same gas |
| CN200964440Y (en) * | 2006-10-18 | 2007-10-24 | 郭正则 | Water electrolyte hydrogen-oxygen generation device equipped with connection flow tube |
| CN203602727U (en) * | 2013-12-04 | 2014-05-21 | 柳二宝 | Hydrogen-oxygen generator |
| CN104674291A (en) * | 2013-11-28 | 2015-06-03 | 哈尔滨市三和佳美科技发展有限公司 | Mixed hydrogen-oxygen generator |
| CN205710943U (en) * | 2016-06-29 | 2016-11-23 | 唐以松 | A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution |
-
2016
- 2016-06-29 CN CN201610487321.8A patent/CN106222687B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2352544Y (en) * | 1998-05-20 | 1999-12-08 | 王宜清 | Low voltage large current apparatus for producing hydrogen and oxygen |
| JP2002053989A (en) * | 2000-08-03 | 2002-02-19 | Shinko Pantec Co Ltd | System for purifying gas formed by water electrolysis and method for purifying the same gas |
| CN200964440Y (en) * | 2006-10-18 | 2007-10-24 | 郭正则 | Water electrolyte hydrogen-oxygen generation device equipped with connection flow tube |
| CN104674291A (en) * | 2013-11-28 | 2015-06-03 | 哈尔滨市三和佳美科技发展有限公司 | Mixed hydrogen-oxygen generator |
| CN203602727U (en) * | 2013-12-04 | 2014-05-21 | 柳二宝 | Hydrogen-oxygen generator |
| CN205710943U (en) * | 2016-06-29 | 2016-11-23 | 唐以松 | A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107188290A (en) * | 2017-05-11 | 2017-09-22 | 玉灵华科技有限公司 | A kind of preparation method of high concentration elementary gas and many matter gas aqueous solution |
| CN112501633A (en) * | 2020-12-28 | 2021-03-16 | 陕西华秦新能源科技有限责任公司 | Large-gas-production-rate oxyhydrogen generator and use method thereof |
| CN112553645A (en) * | 2020-12-28 | 2021-03-26 | 陕西华秦新能源科技有限责任公司 | Electrolytic tank of oxyhydrogen generator and use method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106222687B (en) | 2018-07-06 |
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Effective date of registration: 20230920 Address after: 528051 Office 03, Room 1403, Building T8, Smart New City, Jihua 1st Road, Zhangcha Street, Chancheng District, Foshan City, Guangdong Province Patentee after: Foshan Hanbo Hydrogen New Energy Technology Co.,Ltd. Address before: 528000 Dormitory of Bobo Mosaic Factory in Luoge Yongguang Industrial Zone, Nanzhuang Town, Chancheng District, Foshan City, Guangdong Province Patentee before: Tang Yisong Patentee before: Tang Liqian |
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Effective date of registration: 20240118 Address after: 528051 South C Factory Building, Chongnan Village Industrial Park Central Road, Xiqiao Town, Nanhai District, Foshan City, Guangdong Province Patentee after: GUANGDONG LANXIN HYDROGEN ENERGY TECHNOLOGY CO.,LTD. Address before: 528051 Office 03, Room 1403, Building T8, Smart New City, Jihua 1st Road, Zhangcha Street, Chancheng District, Foshan City, Guangdong Province Patentee before: Foshan Hanbo Hydrogen New Energy Technology Co.,Ltd. |