CN106245052B - A kind of hydro-electrolytic hydroxide mixed gas equipment - Google Patents
A kind of hydro-electrolytic hydroxide mixed gas equipment Download PDFInfo
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- CN106245052B CN106245052B CN201610487373.5A CN201610487373A CN106245052B CN 106245052 B CN106245052 B CN 106245052B CN 201610487373 A CN201610487373 A CN 201610487373A CN 106245052 B CN106245052 B CN 106245052B
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- electrolytic cell
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- liquid
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- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 80
- 239000007788 liquid Substances 0.000 claims abstract description 40
- 238000001816 cooling Methods 0.000 claims abstract description 31
- 238000006243 chemical reaction Methods 0.000 claims abstract description 11
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 10
- 238000010926 purge Methods 0.000 claims abstract description 10
- 230000000740 bleeding effect Effects 0.000 claims description 10
- 238000009413 insulation Methods 0.000 claims description 6
- 230000005611 electricity Effects 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 2
- 230000000737 periodic effect Effects 0.000 claims description 2
- 230000036647 reaction Effects 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 27
- 238000010586 diagram Methods 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 229920001084 poly(chloroprene) Polymers 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 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
- 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
- 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
- C25B15/00—Operating or servicing cells
- C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
-
- 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
The present invention provides a kind of hydro-electrolytic hydroxide mixed gas equipment, can solve the problems, such as that existing equipment electrolytic efficiency is low, including rack, cell reaction mechanism, solution cooling body, gas treatment means and the control unit being separately positioned in the rack；The gas treatment means include knockout drum group, purge of gas tank and air accumulator；It is characterized in that：The water tank outlet end connects the liquid feeding end of one second check valve, the second check valve outlet end is respectively connected to the outlet end of the electrolytic cell and the water circulating pump by a threeway, the water circulating pump is connected to the cooling device, and the cooling device is connected to the liquid feeding end of the electrolytic cell.The present invention is by being connected directly to the water inlet end of water tank among the liquid cooling circulation loop of electrolytic cell, liquid in water tank is smoothly flowed in electrolytic cell, ensure that the liquid in electrolytic cell is abundant, ensure the speed of electrolysis, so as to improve the production efficiency of gas.
Description
Technical field
The invention belongs to hydro-electrolytic hydroxide mixed gas equipment technical field, particularly a kind of hydro-electrolytic hydroxide mixed gas
Equipment.
Background technology
Hydro-electrolytic hydroxide mixed gas equipment is that one kind uses water electrolysis technology, is powered from water and decomposites hydrogen and oxygen
Gas, hydrogen, as combustion-supporting, two kinds of gas mixings, are a kind of high-tech novel environment friendly energy devices as fuel, oxygen.Existing use
In hydro-electrolytic hydroxide mixed gas equipment equipment connecting line as described in Figure 4, water tank 4 be connected directly to electrolytic cell 2 into
Liquid end, and the internal liquid circulation end of electrolytic cell 2 is individually equipped with a circulation loop, circulation loop is equipped with check valve 5, circulating pump
7 and cooling device 3, this pipeline is there are a drawback, and the liquid constantly electrolysis in electrolytic cell comes out gas so that the electrolysis
Pressure in groove is bigger than the pressure of water tank 4, and the shipwreck of water tank 4 is to flow into electrolytic cell 2, so can only be added using shutdown
Solubilization liquid, the mode of this addition solution drastically influence the efficiency of electrolysis.
The content of the invention
In order to solve prior art problem, the present invention provides a kind of hydro-electrolytic hydroxide mixed gas equipment, realizes equipment not
Automatic addition solution is shut down, substantially increases production efficiency.
To achieve the above object, technical solution provided by the present invention is：A kind of hydro-electrolytic hydroxide mixed gas equipment, bag
Including rack, cell reaction mechanism, solution cooling body, gas treatment means and the control machine being separately positioned in the rack
Group；The cell reaction mechanism includes water tank and more than one group of electrolytic cell, and the second limnimeter is equipped with the water tank, described
Include multiple spaced circular pole pieces in electrolytic cell；The solution cooling body includes water circulating pump and cooling
Device；The gas treatment means include knockout drum group, purge of gas tank and air accumulator；The upper part of the electrolytic cell goes out
Tracheae is connected to the knockout drum group, and the knockout drum group is sequentially connected the purge of gas tank and the gas storage
Tank, the liquid back pipe of the knockout drum group bottom are connected to the water tank, it is characterised in that：The water tank outlet end connects
The liquid feeding end of one second check valve is connect, the second check valve outlet end is respectively connected to going out for the electrolytic cell by a threeway
Liquid end and the water circulating pump, the water circulating pump are connected to the cooling device, and the cooling device is connected to the electrolysis
The liquid feeding end of groove.
Preferably, a solution addition mechanism for being arranged on the reaction mechanism front end is further included, the solution adds mechanism
Including tank body, water inlet and the first check valve arranged on the inlet end are equipped with the top of the tank body, the water inlet front end is set
There is a water pump, for the opening direction of first check valve by being directed toward outside the tank of the tank body in tank, the tank base is equipped with solution
Outlet and the electronic valve arranged on the taphole, the water inlet lower section are equipped with a solute filter screen bucket, the solute filter screen
Bucket is other to be equipped with a solute dispensing port and launches switch, and the solute dispensing port is connected to the solute filter screen by a passage
Bucket, the first filter screen is respectively equipped between the solute filter screen bucket and the taphole and positioned at the tank inner chamber bottom
With the second filter screen, the tank body top is additionally provided with pressure sensor, electronics air bleeding valve and the first limnimeter, the pressure sensing
Device, the electronics air bleeding valve, first limnimeter, the dispensing switch and the electronic valve are electrically connected to the control respectively
Unit processed is simultaneously controlled by it.
Preferably, a constant pressure pump for connecting the electrolytic cell and the tank body respectively is further included.
Preferably, the pole piece outer edge is stamped with the rough annular wave channel of multiple tracks.
Preferably, the solution cooling body has further included a S type finned tubes, and the S types finned tube is connected to institute
State water circulating pump front end.
Preferably, the connecting tube between the knockout drum group and the electrolytic cell is not to be shorter than the insulation tube of 2m,
Electricity-preventing wall device is installed on insulation tube.
Preferably, a temperature sensor is additionally provided with the electrolytic cell.
Preferably, a manual threshold switch is also connected by a threeway at the electrobath liquid outlet end and is used for periodic cleaning.
In addition, all electronic components are all by control unit allocation.
Beneficial effects of the present invention：
The present invention adds mechanism and constant pressure pump by adding a solution, then coordinates the cooperation of electronic component, by controller
Control, realizes the purpose of efficiently production mixed gas, and relative to existing production equipment, producing one cubic metre of mixed gas needs
3.5 degree of electricity are wanted, and improved equipment only needs 2.8 degree of electricity, greatlys save energy consumption, meanwhile, equipment can ensure electricity always
The liquid solved in groove is full, makes it in most appropriate pressure with temperature by control system come the pressure in regulating electrolytic tank
With in temperature range, improving production efficiency.
Brief description of the drawings
Fig. 1 is the three-dimensional structure diagram of the present invention；
Fig. 2 is the front view of the present invention；
Fig. 3 is the connection diagram of the present invention；
Fig. 4 is the connection diagram of existing equipment；
Fig. 5 is the three-dimensional structure diagram of electrolytic cell 302；
Fig. 6 is the front view of pole piece 302a；
Fig. 7 is the A-A faces view of Fig. 6；
Fig. 8 is the structure diagram that solution adds mechanism 200.
In figure：100- racks, 200- solution addition mechanism, 300- cell reactions mechanism, 400- solution cooling bodies,
500- gas treatment means, 600- control units, 700- constant pressure pumps, 201- tank bodies, 202- water inlets, the first check valves of 202a-,
203- water outlets, 203a- electronic valves, 204- pressure sensors, 205- air bleeding valves, 206- additive dispensing ports, 206a- are launched and opened
Close, 207- passages, 208- solute filter screen buckets, the first filter screens of 209-, the second filter screens of 210-, the first limnimeters of 211-,
212- water pumps, 301- water tanks, the second limnimeters of 301a-, 302- electrolytic cells, 302a- pole pieces, the second check valves of 401-, 402-S
Type finned tube, 403- water circulating pumps, 404- cooling devices, 501- knockout drums, 502- purge of gas tanks, 503- air accumulators.
Embodiment
Below in conjunction with the accompanying drawings and specific embodiment, the invention will be further described：
Referring to figs. 1 to Fig. 3, Fig. 5, a kind of hydro-electrolytic hydroxide mixed gas equipment, including rack 100, it is separately positioned on this
Cell reaction mechanism 300, solution cooling body 400, gas treatment means 500 and control unit 600 in rack 100；
Above-mentioned cell reaction mechanism 300 includes water tank 301 and more than one group of electrolytic cell 302, and the second water is equipped with the water tank 301
Position instrument 301a, includes multiple spaced circular pole piece 302a in above-mentioned electrolytic cell 302；Above-mentioned solution cooling body
400 include water circulating pump 403 and cooling device 404；Above-mentioned gas processing mechanism 500 includes knockout drum group 501, gas
Body purge tank 502 and air accumulator 503；The air outlet pipe on above-mentioned 302 top of electrolytic cell is connected to above-mentioned knockout drum group 501, on
State knockout drum group 501 and be sequentially connected above-mentioned gas purge tank 502 and above-mentioned air accumulator 503, above-mentioned knockout drum group 501
The liquid back pipe of bottom is connected to above-mentioned water tank 301, and above-mentioned 301 outlet end of water tank connects the feed liquor of one second check valve 401
End, above-mentioned second check valve, 401 outlet end are respectively connected to the outlet end of above-mentioned electrolytic cell 302 and above-mentioned circulation by a threeway
Water pump 403, above-mentioned water circulating pump 403 are connected to above-mentioned cooling device 404, and above-mentioned cooling device 404 is connected to above-mentioned electrolytic cell
302 liquid feeding end.
Fig. 8 is referred again to, further includes a solution addition mechanism 200 for being arranged on above-mentioned 300 front end of reaction mechanism, above-mentioned solution
Addition mechanism 200 includes tank body 201, the above-mentioned top of tank body 201 equipped with water inlet 202 and arranged on 202 end of water inlet first
The opening direction of check valve 202a, first check valve 202a outside the tank of above-mentioned tank body 201 by being directed toward in tank, above-mentioned tank body 201
Bottom is equipped with taphole 203 and the electronic valve 203a arranged on the taphole 203, and above-mentioned 202 front end of water inlet is equipped with a water
Pump 212, the above-mentioned lower section of water inlet 202 are equipped with a solute filter screen bucket 208, and the above-mentioned side of solute filter screen bucket 208 is equipped with a solute
Dispensing port 206 and dispensing switch 206a, above-mentioned solute dispensing port 206 are connected to above-mentioned solute filter screen by a passage 207
Bucket 208, sets respectively between above-mentioned solute filter screen bucket 208 and above-mentioned taphole 203 and positioned at above-mentioned 201 intracavity bottom of tank body
There are the first filter screen 209 and the second filter screen 210, the above-mentioned top of tank body 201 is additionally provided with pressure sensor 204, electronics air bleeding valve
205 and first limnimeter 211, it is above-mentioned pressure sensor 204, above-mentioned electronics air bleeding valve 205, above-mentioned first limnimeter 211, above-mentioned
Switch 206a and above-mentioned electronic valve 203a is launched to be electrically connected to above-mentioned control machine group 600 and be controlled by it respectively.
With reference to Fig. 3, a constant pressure pump 700 for connecting above-mentioned electrolytic cell 302 and above-mentioned tank body 201 respectively, above-mentioned perseverance are further included
Press pump 700 gives 201 pressure supply of above-mentioned electrolytic cell 302 and above-mentioned tank body respectively.
Fig. 6 and Fig. 7 are referred again to, above-mentioned pole piece 302a outer edges are stamped with the rough annular wave channel of multiple tracks, wave
The design of groove, with the neoprene side that pole piece 302a coordinates with being arranged to matched rough wave slot structure,
So that pole piece 302a and the neoprene of 302 side of electrolytic cell are more firm in combination, the pressure resistance of electrolytic cell 302 is strengthened
Degree.
Specifically, above-mentioned solution cooling body 400 has further included a S types finned tube 402, above-mentioned S types finned tube 402
Above-mentioned 403 front end of water circulating pump is connected to, above-mentioned S types finned tube 402 effectively cools down liquid, and the liquid after cooling is again
Into cooling device 404, the operating pressure of cooling device 404 is alleviated, extends the service life of cooling device 404.
Specifically, the minimum liquid level of above-mentioned water tank 301 is higher than the top of above-mentioned electrolytic cell 302, so in water tank 301
Liquid on minimum level when, it is ensured that the liquid in electrolytic cell 302 is full.
Specifically, the connecting tube between above-mentioned knockout drum group 501 and above-mentioned electrolytic cell 302 is not to be shorter than the insulation of 2m
Pipe, is provided with electricity-preventing wall device on insulation tube, and so setting can effectively prevent electric charge reflux in electrolytic cell to above-mentioned
Among knockout drum group 501, cause back draft.
Specifically, being additionally provided with a temperature sensor in above-mentioned electrolytic cell 302, temperature sensor gives controller transmission temperature letter
Number.
During present invention work：When the liquid level positioned at water tank 301 is in default lowest water level, above-mentioned second limnimeter
301a monitors that the water level of above-mentioned water tank 301 has arrived minimum point, and above-mentioned second limnimeter 301a is sent out to above-mentioned control unit 600
Go out signal, control unit 600 sends order：Electronic valve 203a is closed, and air bleeding valve 205 is opened, and is launched switch 206a and is opened, gets ready
Quantitative solute drop into above-mentioned solute filter screen bucket 208 along above-mentioned passage 207, water pump 212 works, and above-mentioned first is unidirectional
Valve 202a is opened, and tap water has directly been flushed to above-mentioned solute filter screen bucket 208, solute has been dissolved, until the liquid of tank body 201
Position reaches highest order, and above-mentioned first limnimeter 211 sends signal to control unit 600, and control unit sends order：Air bleeding valve
205 close, and water pump 212 is stopped, and above-mentioned constant pressure pump 700 pressurizes to tank body 201, until the pressure and water storage in tank body 201
When pressure in tank 301 is equal, above-mentioned electronic valve 203a is opened, and under the effect of gravity, liquid flow into water tank 301, with
Liquid-consumed in electrolytic cell 302, when the water of water tank 301 reaches lowest water level again, above-mentioned second limnimeter 301a gives
Control unit 600 sends signal, and control unit 600 sends order：Above-mentioned electronic valve 203a is closed, and air bleeding valve 205 is opened, and is launched
Switch 206a to open, water pump 212 works, and solution adds the cycle operation successively of mechanism 200.
Specifically, after liquid-consumed in above-mentioned electrolytic cell 302, because 302 port of export of electrolytic cell and water tank 301 are phases
Logical, and water tank 301 is located at the top of electrolytic cell 302, and water tank 301 and the connectivity port position of threeway are less than electrolytic cell
302 with the connectivity port of threeway, under the suction of water circulating pump 403, liquid in water tank 301 is excellent to participate in the whole circulatory system
Circulation and give 302 liquid make-up of electrolytic cell in time, so that it is guaranteed that the water of water tank 301 can be flowed down smoothly, ensure electrolytic cell
Liquid in 302 is full all the time, ensures the speed of cell reaction, and the gas of electrolytic cell 302 enters above-mentioned by air outlet pipe
Knockout drum group 501, gas continues forward, after purge of gas tank 502, air accumulator 503 of having arrived, and above-mentioned gas-liquid separation
The liquid of tank group 501 and purge of gas tank 502 has flowed back to above-mentioned water tank 301 by the liquid back pipe of above-mentioned knockout drum 501
In the middle.Liquid in electrolytic cell 302 cools down by its outlet into S types finned tube 403, then is carried out to cooling device 404
Cooling, then be back among electrolytic cell 302, it is ensured that the temperature of liquid is below 85 degree, to protect the component among equipment, separately
Outside, pressure gauge is equipped with above-mentioned solution cooling body 400 with thermometer, when insufficient pressure, above-mentioned constant pressure pump 700 is
System pressurization, to ensure faster water electrolysis reaction speed, is additionally provided with a threeway and connection one at the outlet end of above-mentioned electrolytic cell 302
Manual threshold switch is used to periodically discharge the residual liquid in electrolytic cell and is cleaned.
The present invention realizes non-stop-machine addition solution, improves the water electrolysis efficiency of whole equipment, saves energy consumption.
The examples of implementation of the above are only the preferred embodiments of the invention, and the implementation model of the present invention is not limited with this
Enclose, therefore the change that all shape, principles according to the present invention are made, it should all cover within the scope of the present invention.
Claims (7)
1. a kind of hydro-electrolytic hydroxide mixed gas equipment, including rack (100), the electrolysis being separately positioned in the rack (100)
Reaction mechanism (300), solution cooling body (400), gas treatment means (500) and control unit (600)；The electrolysis
Reaction mechanism (300) includes water tank (301) and more than one group of electrolytic cell (302), and the second water is equipped with the water tank (301)
Position instrument (301a), the electrolytic cell (302) is interior to include multiple spaced circular pole pieces (302a)；The solution circulation is cold
But mechanism (400) includes water circulating pump (403) and cooling device (404)；The gas treatment means (500) include gas-liquid
Knockout drum group (501), purge of gas tank (502) and air accumulator (503)；The air outlet pipe on electrolytic cell (302) top is connected to
The knockout drum group (501), the knockout drum group (501) are sequentially connected the purge of gas tank (502) and described
Air accumulator (503), the liquid back pipe of knockout drum group (501) bottom are connected to the water tank (301), its feature exists
In：Water tank (301) outlet end connects the liquid feeding end of one second check valve (401), and second check valve (401) goes out liquid
End is respectively connected to the outlet end and the water circulating pump (403) of the electrolytic cell (302), the water circulating pump by a threeway
(403) cooling device (404) is connected to, the cooling device (404) is connected to the liquid feeding end of the electrolytic cell (302),
Further include a solution addition mechanism (200) for being arranged on the reaction mechanism (300) front end, the solution addition mechanism (200)
Water inlet (202) is equipped with including tank body (201), at the top of the tank body (201) and arranged on the first unidirectional of the water inlet (202) end
Valve (202a), water inlet (202) front end are equipped with a water pump (212), and the opening direction of first check valve (202a) is by institute
State and be directed toward outside the tank of tank body (201) in tank, tank body (201) bottom is equipped with taphole (203) and arranged on the taphole
(203) electronic valve (203a), water inlet (202) lower section are equipped with a solute filter screen bucket (208), the solute filter screen
Struggling against, (208) are other to be equipped with a solute dispensing port (206) and launches switch (206a), and the solute dispensing port (206) passes through a guide
Pipe (207) is connected to the solute filter screen bucket (208), the solute filter screen bucket (208) and the taphole (203) it
Between and positioned at the tank body (201) intracavity bottom be respectively equipped with the first filter screen (209) and the second filter screen (210), the tank
Pressure sensor (204), electronics air bleeding valve (205) and the first limnimeter (211) are additionally provided with the top of body (201), the pressure passes
Sensor (204), the electronics air bleeding valve (205), first limnimeter (211), described launch switch (206a) and the electricity
Sub- valve (203a) is electrically connected to the control unit (600) and is controlled by it respectively.
A kind of 2. hydro-electrolytic hydroxide mixed gas equipment according to claim 1, it is characterised in that：One is further included respectively to connect
Connect the constant pressure pump (700) of the electrolytic cell (302) and the tank body (201).
A kind of 3. hydro-electrolytic hydroxide mixed gas equipment according to claim 1 or 2, it is characterised in that：The pole piece
(302a) outer edge is stamped with the rough annular wave channel of multiple tracks.
A kind of 4. hydro-electrolytic hydroxide mixed gas equipment according to claim 1 or 2, it is characterised in that：The solution follows
Ring cooling body (400) has further included a S types finned tube (402), and the S types finned tube (402) is connected to the water circulating pump
(403) front end.
A kind of 5. hydro-electrolytic hydroxide mixed gas equipment according to claim 1 or 2, it is characterised in that：The gas-liquid point
It is not to be shorter than the insulation tube of 2m from the connecting tube between tank group (501) and the electrolytic cell (302), is provided with insulation tube anti-
Electricity wall device.
A kind of 6. hydro-electrolytic hydroxide mixed gas equipment according to claim 1, it is characterised in that：The electrolytic cell
(302) temperature sensor is additionally provided with.
A kind of 7. hydro-electrolytic hydroxide mixed gas equipment according to claim 1, it is characterised in that：The electrolytic cell
(302) a manual threshold switch is also connected by a threeway at outlet end and is used for periodic cleaning.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610487373.5A CN106245052B (en) | 2016-06-29 | 2016-06-29 | A kind of hydro-electrolytic hydroxide mixed gas equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610487373.5A CN106245052B (en) | 2016-06-29 | 2016-06-29 | A kind of hydro-electrolytic hydroxide mixed gas equipment |
Publications (2)
| Publication Number | Publication Date |
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| CN106245052A CN106245052A (en) | 2016-12-21 |
| CN106245052B true CN106245052B (en) | 2018-04-17 |
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| CN201610487373.5A Active CN106245052B (en) | 2016-06-29 | 2016-06-29 | A kind of hydro-electrolytic hydroxide mixed gas equipment |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108251856A (en) * | 2018-02-11 | 2018-07-06 | 深圳市量子氢生物技术有限公司 | A kind of electrolytic cell and electrolysis unit |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3837354A1 (en) * | 1988-11-03 | 1990-05-10 | Werner Ziem | Method and appliance for safeguarding a high-pressure water electrolysis system |
| CN2128898Y (en) * | 1992-09-28 | 1993-03-31 | 北京市海淀区伍行电子技术研究所 | Liquor proportioning meter |
| CN2352544Y (en) * | 1998-05-20 | 1999-12-08 | 王宜清 | Low voltage large current apparatus for producing hydrogen and oxygen |
| JP3604620B2 (en) * | 2000-08-03 | 2004-12-22 | 株式会社神鋼環境ソリューション | Water electrolysis product gas purification system and purification method |
| CN200964440Y (en) * | 2006-10-18 | 2007-10-24 | 郭正则 | Water electrolyte hydrogen-oxygen generation device equipped with connection flow tube |
| CN201749906U (en) * | 2010-05-28 | 2011-02-16 | 浙江飞狮电器工业有限公司 | Preparation device of potassium hydroxide electrolyte |
| CN203602727U (en) * | 2013-12-04 | 2014-05-21 | 柳二宝 | Hydrogen-oxygen generator |
| CN205839145U (en) * | 2016-06-29 | 2016-12-28 | 唐以松 | A kind of hydro-electrolytic hydroxide mixed gas equipment |
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2016
- 2016-06-29 CN CN201610487373.5A patent/CN106245052B/en active Active
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| CN106245052A (en) | 2016-12-21 |
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