CN117448857A - Hydrogen electrolysis manufacturing equipment - Google Patents
Hydrogen electrolysis manufacturing equipment Download PDFInfo
- Publication number
- CN117448857A CN117448857A CN202311465140.1A CN202311465140A CN117448857A CN 117448857 A CN117448857 A CN 117448857A CN 202311465140 A CN202311465140 A CN 202311465140A CN 117448857 A CN117448857 A CN 117448857A
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- China
- Prior art keywords
- electrolysis
- bin
- hydrogen
- fixedly arranged
- bevel gear
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- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 90
- 239000001257 hydrogen Substances 0.000 title claims abstract description 66
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 66
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000001301 oxygen Substances 0.000 claims abstract description 41
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 41
- 238000003756 stirring Methods 0.000 claims abstract description 34
- 150000001875 compounds Chemical class 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 238000000227 grinding Methods 0.000 claims description 10
- 230000005540 biological transmission Effects 0.000 claims description 8
- 230000005611 electricity Effects 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 5
- 239000002351 wastewater Substances 0.000 claims description 5
- 239000002994 raw material Substances 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims 2
- -1 main support (101) Chemical class 0.000 claims 1
- 238000004065 wastewater treatment Methods 0.000 claims 1
- 239000008399 tap water Substances 0.000 abstract description 20
- 235000020679 tap water Nutrition 0.000 abstract description 20
- 239000007789 gas Substances 0.000 abstract description 19
- 239000000203 mixture Substances 0.000 abstract description 11
- 150000002431 hydrogen Chemical class 0.000 abstract description 6
- 239000012258 stirred mixture Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910001882 dioxygen Inorganic materials 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004200 deflagration Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000012216 screening 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
- C25B9/70—Assemblies comprising two or more 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
- C25B9/60—Constructional parts of cells
-
- 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 invention discloses a hydrogen electrolysis manufacturing device, which relates to the technical field of gas production equipment and comprises a support frame, a tank body, an electrolysis bin and an electrolysis plate, wherein the tank body is welded on the support frame, the tank body is provided with a feeding bin, the feeding bin is provided with a crushing wheel, the crushing wheel can crush a compound with larger size, the compound is fully absorbed by tap water, the tank body is internally provided with a stirring shaft, the stirring shaft drives the stirring shaft to rotate in a pipe body through the rotation of a motor, the mixture is fully stirred, the compound is fully fused in the tap water, the stirred mixture is pumped into the electrolysis bin through a water pump for electrolysis treatment, two electrolysis bins are arranged, one electrolysis bin is connected with an anode and a cathode, the electrolysis bin connected with the anode produces hydrogen, the electrolysis bin connected with the cathode produces oxygen, the hydrogen and the oxygen are not interfered with each other, the purity is improved, the electrolysis bin is provided with a storage tank, a gas outlet pipe is directly connected to the bottom of the storage tank, and the liquid at the bottom of the storage tank is not passed through the outlet pipe, so that the safety of hydrogen storage is improved.
Description
Technical Field
The invention relates to the technical field of gas production, in particular to hydrogen electrolysis manufacturing equipment
Background
The electrolysis of water can obtain two gases of hydrogen and oxygen which are very commonly used in life, if the hydrogen and the oxygen can be manufactured on a large scale by using the method, a lot of energy sources can be saved, the hydrogen can be used as a new energy source without pollution, and if the produced hydrogen can be automatically collected and has no potential safety hazard, the energy sources can be greatly saved, so that an electrolysis production gas device is required to be designed to solve the problems.
The Chinese patent with publication number of CN110656340A discloses an electrolysis production gas device, which comprises a machine body, wherein the machine body comprises a gas storage cavity, a collecting mechanism for collecting produced gas is arranged in the gas storage cavity, the device collects hydrogen and oxygen through electrolysis water, the collected hydrogen and oxygen are directly collected into a gas tank, the device directly presses the gas in the cavity into the gas tank through extrusion, meanwhile, the transmission system of the device is compact in cooperation, the operation is simple, and the process is safe and rapid.
Although the patent can produce hydrogen and oxygen at the same time, the purity is not high, the equipment design is very compact, the later maintenance is inconvenient, the production efficiency is not high, the hydrogen is inflammable gas, and the collecting device of the patent has potential safety hazard of hydrogen deflagration.
Disclosure of Invention
Aiming at the technical problems, the invention adopts a positive and negative electrode electrolysis mode to improve the purity of the hydrogen.
The technical scheme of the invention is as follows: the hydrogen-oxygen compound feeding device comprises a main support, wherein a tank body is fixedly arranged on the main support, the main support is used for supporting the tank body, a first support is fixedly arranged on the tank body, a feeding bin is fixedly arranged on the first support, the first support is used for supporting the feeding bin, a screen is fixedly arranged on the feeding bin, the screen is used for filtering the hydrogen-oxygen compound, the hydrogen-oxygen compound is mixed in liquid to improve the conductivity of the hydrogen-oxygen compound, hydrogen in the liquid is fully electrolyzed, and a vibrator is arranged on the feeding bin and is used for vibrating to prevent the hydrogen-oxygen compound from adhering to the feeding bin.
Further, a motor I is fixedly installed on the feeding bin, the motor I improves power for the feeding bin, a spiral overlapping is rotatably installed on the motor I, the motor I drives the spiral overlapping, the spiral overlapping drives a material to a feeding pipe, a threaded gear is fixedly installed on the spiral overlapping, the spiral overlapping drives the threaded gear to rotate, a gear III is installed on the threaded gear in a meshed mode, the threaded gear drives the gear III to rotate, a transmission shaft is fixedly installed on the gear III, the gear III drives the transmission shaft to rotate, a bevel gear II is fixedly installed on the transmission shaft, a bevel gear I is installed on the bevel gear II in a meshed mode, the bevel gear II drives the bevel gear I to rotate, a crushing wheel II is fixedly installed on the crushing wheel II, a gear II is installed on the 240 in a meshed mode, the gear II drives the gear II to rotate, the crushing wheel II rotates clockwise, the crushing wheel I rotates anticlockwise, coarse crushing of the material is achieved, the crushing wheel I and the crushing wheel II rotate and are installed on the feeding bin, and the feeding pipe is fixedly installed on the feeding bin.
Further, a motor II is fixedly arranged on the tank body, the motor II improves power for the stirring shaft, a bevel gear III is rotatably arranged on the motor II, a bevel gear IV is meshed with the bevel gear III, the bevel gear III drives the bevel gear IV to rotate, a stirring shaft II is fixedly arranged on the bevel gear IV, the bevel gear IV drives the stirring shaft II to rotate, a bevel gear V is meshed with the bevel gear III, the bevel gear III drives the bevel gear V to rotate, a stirring shaft I is fixedly arranged on the bevel gear V, the stirring shaft V drives the stirring shaft I to rotate with the stirring shaft II in the tank body, and the rotation directions of the stirring shaft I and the stirring shaft II are opposite, so that liquid and a compound are fully stirred and fused together.
Further, a second support is fixedly arranged on the tank body, the second support is used for supporting a fourth bevel gear, a third support is fixedly arranged on the second support, the third support is further supported by the second support, a hydraulic pump is fixedly arranged on the third support, the third support is used for supporting the hydraulic pump, a hydraulic rod is fixedly arranged on the hydraulic pump, a piston is fixedly arranged on the hydraulic rod, and the piston moves upwards to discharge a mixture.
Further, a water inlet bin is fixedly arranged on the tank body, a leakage net is fixedly arranged on the water inlet bin and used for filtering liquid raw materials, impurities in liquid are prevented from being mixed into equipment, a pipeline is fixedly arranged on the tank body, discharged liquid passes through the pipeline, a water pump is fixedly arranged on the pipeline, an electrolysis bin is fixedly arranged on the pipeline, the liquid passes through the water pump to the electrolysis bin, a water outlet is fixedly arranged on the electrolysis bin, the electrolyzed liquid is discharged through the water outlet, a third switch is arranged on the water outlet, and the third switch is used for controlling the discharge of wastewater.
Further, a hydrogen electrolysis bin and an oxygen electrolysis bin are fixedly arranged in the electrolysis bin, an electrolysis plate I is fixedly arranged on the hydrogen electrolysis bin and is used for electrolyzing hydrogen, an anode interface is fixedly arranged on the electrolysis plate I, an electrolysis plate II is fixedly arranged on the oxygen electrolysis bin and is used for electrolyzing oxygen, a cathode interface is fixedly arranged on the electrolysis plate II, the anode interface is connected with anode electricity, and the cathode interface is connected with cathode electricity.
Further, a first air pipe is fixedly arranged on the electrolysis bin, a first hydrogen bin is fixedly arranged on the first air pipe and used for storing hydrogen, a first air outlet is fixedly arranged on the first hydrogen bin, a second switch is arranged on the first air outlet and used for controlling hydrogen to be discharged, a second air pipe is fixedly arranged on the electrolysis bin, an oxygen bin is fixedly arranged on the second air pipe, a second air outlet is fixedly arranged on the oxygen bin, a first switch is fixedly arranged on the second air outlet and used for controlling oxygen to be discharged.
Compared with the prior art, the invention has the beneficial effects that: (1) Through the two electrolysis bins, not only can the hydrogen and the oxygen be electrolyzed separately, but also the purity of the hydrogen and the oxygen can be improved, and the storage safety of the hydrogen is greatly improved through the unique storage tank; (2) The oxyhydrogen compound with larger size is crushed by the crushing wheel, so that the oxyhydrogen compound can be fully absorbed by tap water, the conductivity of the tap water is improved, and the content of hydrogen and oxygen in the water is improved; (3) The oxyhydrogen compound is fully stirred with tap water by stirring of a stirring shaft, and tap water can fully absorb the oxyhydrogen compound.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present invention.
FIG. 2 is a cross-sectional view of a portion of the feed bin of the invention.
FIG. 3 is a schematic diagram of the feed bin drive structure of the present invention.
FIG. 4 is a schematic view of the stirring shaft of the present invention.
Fig. 5 is a schematic view of a partial structure of the can body according to the present invention.
Fig. 6 is a cross-sectional view of the structure of the can body of the present invention.
FIG. 7 is a schematic view of the structure of the electrolysis chamber of the invention.
FIG. 8 is a cross-sectional view of the overall structure of the electrolysis chamber of the invention.
Fig. 9 is a cross-sectional view of the overall structure of the present invention.
FIG. 10 is a schematic view of the drive structure of the stirring shaft of the present invention.
FIG. 11 is a partial sectional view of the electrolytic cartridge of the present invention.
Fig. 12 is a schematic view of the structure of the pulverizing wheel of the present invention.
101-a main support; 102-bracket I; 103-a second bracket; 104-a third bracket; 105-tank body; 201-a feeding bin; 202-a screen; 203-a vibrator; 204-gear one; 205-gear two; 206-motor one; 207-azido; 208-gear three; 209-a threaded gear; 210-feeding pipe; 211-first bevel gears; 212-a second bevel gear; 213-a drive shaft; 215-crushing wheel one; 216-crushing wheel II; 301-a second motor; 302-bevel gears III; 303-bevel gear IV; 304-bevel gear five; 305-stirring shaft I; 306-stirring shaft II; 401-a hydraulic pump; 402-a water inlet bin; 403-a hydraulic rod; 404-a piston; 405-leaking net; 501-a pipeline; 502-a water pump; 503-electrolysis bin; 504-trachea one; 505-hydrogen bin; 506-gas outlet I; 507-trachea two; 508-an oxygen bin; 509-outlet two; 601-a hydrogen electrolysis bin; 602-first electrolytic plate; 603-positive electrode interface; 604-an oxygen electrolysis bin; 605-electrolytic plate two; 606-negative electrode interface; 607-water outlet; 701-switch one; 702-switch two; 703-switch three.
Detailed Description
The invention is described in detail below with reference to the attached drawings:
as shown in fig. 1-3 and 12, the oxyhydrogen compound enters from the feeding bin 201, in order to make the oxyhydrogen compound fully absorbed by the liquid, the oxyhydrogen compound with smaller size passes through the screen 202, and the oxyhydrogen compound with larger size passes through the screen 202 to be screened and crushed between the crushing wheel two 216 and the crushing wheel one 215, and the running structure is that the motor one 206 rotates, and the motor one 206 drives the spiral shell 207 to rotate in the feeding tube 210, and the spiral shell 207 is used for conveying the material into the tank 105.
As shown in fig. 2, 3 and 12, the spiral shell 207 drives the threaded gear 209 to rotate, the threaded gear 209 rotates to drive the third gear 208 to rotate, the third gear 208 drives the transmission shaft 213 to rotate, the transmission shaft 213 drives the second bevel gear 212 to rotate, the second bevel gear 212 drives the first bevel gear 211 to rotate, the first bevel gear 211 drives the second grinding wheel 216 to rotate clockwise, the second grinding wheel 216 drives the first gear 204 to rotate clockwise, the first gear 204 drives the second gear 205 to rotate anticlockwise, the second gear 205 rotates anticlockwise to drive the first grinding wheel 215 to rotate anticlockwise, the grinding wheel 216 and the first grinding wheel 215 grind coarse compounds, and the vibrator 203 is further mounted on the feeding bin 201 and is used for preventing the compounds from adhering to the inner wall of the feeding bin 201 and preventing blockage.
As shown in fig. 4-6, fig. 9 and fig. 10, tap water is poured in from a water inlet bin 402, impurities in the tap water are prevented from being mixed into the tank body 105 through a drain screen 405, the tap water passes through the drain screen 405 and enters the tank body 105 to be mixed with the compound, a motor II 301 is started, the motor II 301 rotates to drive a bevel gear III 302 to rotate, the bevel gear III 302 drives a bevel gear IV 303 to rotate, the bevel gear IV 303 drives a stirring shaft II 306 to rotate in the tank body 105, the bevel gear III 302 drives a bevel gear V304 to rotate, the bevel gear V304 drives a stirring shaft I305 to rotate in the tank body 105, the rotation direction of the stirring shaft I305 is opposite to that of the stirring shaft II 306, and the effect is to enable the mixture to be fully stirred, so that the tap water fully absorbs the compound and conductivity is improved.
As shown in fig. 5 and fig. 6, when the stirred liquid needs to be discharged, the hydraulic pump 401 needs to be started, the hydraulic pump 401 drives the hydraulic rod 403 to move upwards, the hydraulic rod 403 drives the piston 404 to move upwards, the mixture is discharged, the installation position of the hydraulic rod 403 is in the stirring shaft two 306, the bracket two 103 is used for supporting the stirring shaft two 306, and the bracket three 104 is used for supporting the hydraulic pump 401.
7-9 and 11, the stirred mixture is fed into a pipeline 501, and is fed into an electrolysis bin 503 through a water pump 502, the water pump 502 is started to fill the electrolysis bin 503 with eighty percent, twenty percent of space is needed to be reserved above the water pump, the water pump is used for preventing liquid in the electrolysis bin 503 from entering a first air pipe 504 and a second air pipe 507, two electrolysis bins are arranged in the electrolysis bin 503, namely a hydrogen electrolysis bin 601 and an oxygen electrolysis bin 604, the hydrogen electrolysis bin 601 is used for electrolyzing hydrogen, the oxygen electrolysis bin 604 is used for electrolyzing oxygen, after the mixture enters the hydrogen electrolysis bin 601 and the oxygen electrolysis bin 604, positive electrode interfaces 603 are respectively electrified, negative electrode interfaces 606 are electrified, the positive electrode interfaces 603 are fixedly connected with the first electrolysis plate 602, the negative electrode interfaces 606 are fixedly connected with the second electrolysis plate 605, the electrolyzed gas is oxygen, and the electrolyzed gas can reach the upper part of the liquid.
As shown in fig. 7 and 8, hydrogen passes through the first air pipe 504 to the hydrogen chamber 505, oxygen passes through the second air pipe 507 to the oxygen chamber 508, the first air pipe 504 and the second air pipe 507 are respectively fixed on the hydrogen chamber 505 and the oxygen chamber 508 and are internally extended to the bottom, tap water is required to be filled into the hydrogen chamber 505 and the oxygen chamber 508 before the equipment is started, and water is required to pass through the water outlets of the first air pipe 504 and the second air pipe 507, so that the safety of the hydrogen is improved, and the hydrogen is inflammable gas.
As shown in fig. 7 and 11, the hydrogen gas in the hydrogen bin 505 needs to be discharged by opening the switch two 702, the hydrogen gas needs to be discharged by opening the switch one 701 through the gas outlet one 506, the oxygen gas needs to be discharged by opening the gas outlet two 509, when the hydrogen gas and the oxygen gas in the liquid are electrolyzed, the waste water needs to be discharged, the switch three 703 needs to be opened, and the liquid is discharged by the water outlet 607.
As shown in fig. 9, this is the installation position of each functional device.
The working principle of the invention is as follows: before the equipment is started, tap water needs to be filled into the hydrogen bin 505 and the oxygen bin 508, and the water surface of the tap water is provided with air outlets which pass through the first air pipe 504 and the second air pipe 507.
Before starting the equipment, the tank 105 is also required to be filled with tap water, the tap water is filled from the water inlet bin 402, impurities in the tap water are filtered through the filtering of the drain screen 405, after the equipment is started, oxyhydrogen compounds are required to be put into the screen 202 from the feeding bin 201, screening of the screen 202 is improved, small-size compounds directly pass through the screen 202, larger-size compounds pass through the screen 202 and pass between the crushing wheel two 216 and the crushing wheel one 215, and in order to enable the compounds to be fully absorbed by the tap water, the large-size compounds are required to be crushed, and the crushed compounds are required to be returned into the feeding bin 201.
The compound in the feeding bin 201 is rotated to the feeding pipe 210 through the lap screw 207, the power of the lap screw 207 is derived from the motor I206, the compound is fused with tap water in the tank body 105 through the feeding pipe 210, then the motor II 301 is started to stir the compound with the tap water, the compound is fully absorbed by the tap water, the stirring shaft II 306 and the stirring shaft I305 rotate in opposite directions, the stirring effect is more sufficient, the stirring shaft I305 contacts with the inner wall of the tank body 105, the effect is to scrape the mixture on the inner wall of the tank body 105, and the mixture is prevented from adhering to the inner wall of the tank body 105.
The stirred mixture needs to be discharged into the electrolysis bin 503, the hydraulic pump 401 needs to be started, the hydraulic pump 401 drives the hydraulic rod 403, the hydraulic rod 403 drives the piston 404 to lift upwards, the mixture is discharged, the mixture passes through the pipeline 501 and is conveyed into the electrolysis bin 503 through the water pump 502, two electrolysis bins are arranged in the electrolysis bin 503, the two electrolysis bins are respectively a hydrogen electrolysis bin 601 and an oxygen electrolysis bin 604, the hydrogen electrolysis bin 601 is electrolyzed with hydrogen, the oxygen electrolysis bin 604 is electrolyzed with oxygen, the discharged mixture needs to be soaked through the first electrolysis plate 602 and the second electrolysis plate 605 after entering the electrolysis bin 503, the discharged mixture has the effect of fully electrolyzing the liquid hydrogen and oxygen, the first electrolysis plate 602 is connected with positive electrode electricity, the positive electrode electrolyzed out hydrogen, the second electrolysis plate 605 is connected with negative electrode electricity, and the negative electrode electrolyzed out oxygen.
Hydrogen passes through the first air pipe 504 to the hydrogen bin 505, oxygen passes through the second air pipe 507 to the oxygen bin 508, when the hydrogen and the oxygen in the liquid are electrolyzed, the waste water is required to be discharged, the third switch 703 is required to be opened, and the waste water is required to be discharged through the water outlet 607.
Claims (8)
1. A hydrogen electrolysis manufacturing apparatus comprising a main support (101), characterized in that: the utility model discloses a feeding device for oxyhydrogen compound, including main support (101), main support (101) and vibrator (203), main support (101) are used for supporting jar body (105), fixed mounting has support one (102) on jar body (105), fixed mounting has feeding storehouse (201) on support one (102), and its support one (102) is used for supporting feeding storehouse (201), fixed mounting has screen cloth (202) on feeding storehouse (201), and screen cloth (202) are used for filtering oxyhydrogen compound, still fixed mounting has vibrator (203) on feeding storehouse (201), vibrator (203) are used for vibrating, prevent oxyhydrogen compound adhesion on feeding storehouse (201).
2. A hydrogen electrolysis production apparatus according to claim 1, wherein: the feeding bin is characterized in that a first motor (206) is fixedly arranged on the feeding bin (201), a first lap screw (207) is rotatably arranged on the first motor (206), a threaded gear (209) is fixedly arranged on the first lap screw (207), a third gear (208) is meshed with the threaded gear (209), a transmission shaft (213) is fixedly arranged on the third gear (208), a second bevel gear (212) is fixedly arranged on the transmission shaft (213), a first bevel gear (211) is meshed with the second bevel gear (212), a second grinding wheel (216) is fixedly arranged on the first bevel gear (211), a first gear (204) is fixedly arranged on the second grinding wheel (216), a second gear (205) is meshed with the first grinding wheel (215), the first grinding wheel (215) and the second grinding wheel (216) are rotatably arranged on the feeding bin (201), and a feeding pipe (210) is fixedly arranged on the feeding bin (201).
3. A hydrogen electrolysis production apparatus according to claim 1, wherein: the novel stirring device is characterized in that a motor II (301) is fixedly arranged on the tank body (105), a bevel gear III (302) is rotatably arranged on the motor II (301), a bevel gear IV (303) is arranged on the bevel gear III (302) in a meshed mode, a stirring shaft II (306) is fixedly arranged on the bevel gear IV (303), a bevel gear V (304) is also arranged on the bevel gear III (302) in a meshed mode, a stirring shaft I (305) is fixedly arranged on the bevel gear V (304), and the stirring shaft I (305) and the stirring shaft II (306) rotate in the tank body (105) in opposite rotation directions.
4. A hydrogen electrolysis production apparatus according to claim 3, wherein: the novel hydraulic cylinder is characterized in that a second bracket (103) is fixedly installed on the cylinder body (105), a third bracket (104) is fixedly installed on the second bracket (103), a fourth bevel gear (303) is rotatably installed on the second bracket (103), a hydraulic pump (401) is fixedly installed on the third bracket (104), a hydraulic rod (403) is fixedly installed on the hydraulic pump (401), and a piston (404) is fixedly installed on the hydraulic rod (403).
5. The hydrogen electrolysis production apparatus according to claim 4, wherein: the tank body (105) is fixedly provided with a water inlet bin (402), the water inlet bin (402) is fixedly provided with a leakage net (405), and the leakage net (405) is used for filtering liquid raw materials.
6. A hydrogen electrolysis production apparatus according to claim 1, wherein: the utility model discloses a waste water treatment device, including jar body (105), pipeline (501) are gone up to fixed mounting, fixed mounting has water pump (502) on pipeline (501), still fixed mounting has electrolysis storehouse (503) on pipeline (501), there is liquid in electrolysis storehouse (503), fixed mounting has delivery port (607) on electrolysis storehouse (503), install switch three (703) on delivery port (607), switch three (703) are control waste water emission.
7. The hydrogen electrolysis production apparatus according to claim 6, wherein: the hydrogen electrolysis device comprises an electrolysis bin (503), a hydrogen electrolysis bin (601) and an oxygen electrolysis bin (604) are fixedly arranged in the electrolysis bin (503), an electrolysis plate I (602) is fixedly arranged on the hydrogen electrolysis bin (601), an anode interface (603) is fixedly arranged on the electrolysis plate I (602), an electrolysis plate II (605) is fixedly arranged on the oxygen electrolysis bin (604), a cathode interface (606) is fixedly arranged on the electrolysis plate II (605), and the anode interface (603) is connected with anode electricity, and the cathode interface (606) is connected with cathode electricity.
8. The hydrogen electrolysis production apparatus according to claim 6, wherein: the hydrogen storage device comprises an electrolysis bin (503), wherein an air pipe I (504) is fixedly arranged on the electrolysis bin (503), a hydrogen bin (505) is fixedly arranged on the air pipe I (504), an air outlet I (506) is fixedly arranged on the hydrogen bin (505), a switch II (702) is arranged on the air outlet I (506), the switch II (702) is used for controlling hydrogen emission, an air pipe II (507) is fixedly arranged on the electrolysis bin (503), an oxygen bin (508) is fixedly arranged on the air pipe II (507), an air outlet II (509) is fixedly arranged on the oxygen bin (508), a switch I (701) is fixedly arranged on the air outlet II (509), and the switch I (701) is used for controlling oxygen emission.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311465140.1A CN117448857B (en) | 2023-11-07 | 2023-11-07 | Hydrogen electrolysis manufacturing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311465140.1A CN117448857B (en) | 2023-11-07 | 2023-11-07 | Hydrogen electrolysis manufacturing equipment |
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| Publication Number | Publication Date |
|---|---|
| CN117448857A true CN117448857A (en) | 2024-01-26 |
| CN117448857B CN117448857B (en) | 2024-06-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202311465140.1A Active CN117448857B (en) | 2023-11-07 | 2023-11-07 | Hydrogen electrolysis manufacturing equipment |
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