CN2310770Y - Porous oxyhydrogen generator - Google Patents
Porous oxyhydrogen generator Download PDFInfo
- Publication number
- CN2310770Y CN2310770Y CN 97229417 CN97229417U CN2310770Y CN 2310770 Y CN2310770 Y CN 2310770Y CN 97229417 CN97229417 CN 97229417 CN 97229417 U CN97229417 U CN 97229417U CN 2310770 Y CN2310770 Y CN 2310770Y
- Authority
- CN
- China
- Prior art keywords
- generator
- electrolyzer
- contain
- transformer
- model
- 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
Links
- 210000005056 cell body Anatomy 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 9
- 238000005868 electrolysis reaction Methods 0.000 abstract description 9
- 239000001301 oxygen Substances 0.000 abstract description 9
- 229910052760 oxygen Inorganic materials 0.000 abstract description 9
- 239000007789 gas Substances 0.000 abstract description 7
- 239000001257 hydrogen Substances 0.000 abstract description 5
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 4
- 239000012267 brine Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000004033 plastic Substances 0.000 description 4
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 4
- 210000004027 cell Anatomy 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000005611 electricity Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000005276 aerator Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model provides a porous oxyhydrogen generator, its electrolysis trough body comprises a plurality of electrolytic bath cluster to have simple and convenient water supply and exhaust channel, a cluster group is made to every 60 ~ 70 electrolytic baths, according to the different models and the size of generator, can contain 1 or a plurality of cluster group in an electrolytic bath body, a generator can contain 1 again to a plurality of electrolytic bath. The hydrogen and oxygen generator does not need a transformer to reduce the voltage, so that the structure is simpler, the generator is not limited by the power of the transformer, the electrolytic power of the generator is larger, and the continuously generated gas quantity is large.
Description
The utility model relates to the preparation apparatus of a kind of oxygen, hydrogen, especially a kind of microporous oxyhydrogen generator.
At present, producing of oxygen is many based on compression system oxygen, and the work of filling the jar ventilation each time is quite cumbersome, and is more inconvenient for the user away from the urban district.Produce hydrogen and oxygen by brine electrolysis, be fundamental method, but for a long time, brine electrolysis need transformer to come step-down, be subjected to the restriction of transformer efficiency size, volume, cost, never produce the brine electrolysis producer that volume is little, cost is little, the gas generating capacity is big." one is flat " aerator series that Jinan City, Shandong Province China scientific and technological development company produces, it is the last word that brine electrolysis is produced oxygen, but it does not still break away from transformer step-down process, still be subjected to the restriction of transformer efficiency, the electrolysis power of this machine has only between 20~50 watts, produces gas volume continuously and is no more than 200 ml/min.
The purpose of this utility model provides a kind of simple for structure, and volume is little, does not need to come step-down with transformer, and electrolysis power is big, produces the big microporous oxyhydrogen generator of gas volume continuously.
The technical solution of the utility model is: adopt and be composed in series cell body by a plurality of electrolyzers, and be provided with easy water supply and exhaust channel, be connected in series between intravital electrolytic cell electrode of electrolyzer and the electrode, per 60~70 electrolyzers are made a polyphone group, different model and size according to producer, can contain 1 or several series connection groups in the cell body, 1 producer can contain 1 or several cell body again.By the series connection of a plurality of electrolyzers, the voltage distribution that makes fixed power source is to each electrolyzer, people and reduced the dipolar voltage of each electrolyzer.
The utility model does not need transformer to adopt step-down, makes one-piece construction more succinct, volume-diminished, owing to be not subjected to the restriction of transformer efficiency, the electrolysis power of this producer is bigger, and the gas volume that produces is big continuously.
Be described in further detail below in conjunction with accompanying drawing.
Fig. 1 is the utility model stereoscopic synoptic diagram.
Fig. 2 is the utility model I-I face sectional view.
Fig. 3 is the utility model II-II face sectional view.
Fig. 4 is an electrode plate structure synoptic diagram in the utility model II-II section.
Fig. 5 is a card tip mouth structure synoptic diagram in the utility model II-II section.
Fig. 6 is the utility model III-III face sectional view.
Fig. 7 is the utility model schematic circuit.
Shown in the figure, 1. 4. rectifications of electrolyzer 2. handles 3. oxygen doors are closed 18. anolyte compartments, 7. top covers, 8. cell body, 9. electrolyzers, 10. water supply lines, 11. heating panels, 12. rectifiers, 13. positive plates, 14. negative plates, 15. barrier films 16. card tip mouths 17. water holes, 5. hydrogen doors, 6. filler, 19. cathode compartments, 20. newspapers and are shown device electrode slice 21. diaphragm seals 22. pores.
This oxyhydrogen generator is closed by rectification, and electrolyzer two big entities constitute.Wherein including the newspaper that supplies water show device, waterworks and exhaust by way of.
Rectification closes 4 a plastic casing, sieve aperture is worn in outer one side and two sides, is convenient to heat radiation, simultaneously has the aperture that is communicated with electrolyzer the end of a thread by electrolyzer, the heating panel 11 that will be fixed with rectifier 12 with screw is fastened on rectification and closes inwall, and rectification is closed on the shell that is fixed on electrolyzer.Electrical lead wire hole from the side enters rectification and closes, fixedly behind the end of a thread, the anodal switch that connects is through the direct contact rectifier positive pole of heating panel, draw a lead from the rectifier negative pole again and be connected into first electrolytic cell anode plate in the electrolyzer, the negative plate that negative wire the end of a thread is directly connected to last electrolyzer in the placed in-line electrolyzer group is connected to power cathode.The surface-area of heating panel is bigger, wears sieve aperture, installs with " U " type that falls.
Electrolyzer 1 is made up of cell body 8 that contains a plurality of electrolyzers 9 and plastic roof 7.Handle 3 is established in top cover 7 tops, and opens collection and the ejection door of an aperture 4 as oxygen.Cell body 8 contains a plurality of electrolyzers 9 and water supply line 10.
Fitly arrange a plurality of square holes and a few row's feeding conduit in the cell body, load onto battery lead plate in each square hole, promptly positive plate 13, positive plate 14, and barrier film 15 is pasted the sealed plastic plate above cathode compartment 19, form electrolyzer 9.There is the card tip mouth 16 of protrusion on the inwall both sides of electrolyzer to give as security solid battery lead plate and diaphragm.Below electrolyzer, open an aperture and be communicated with feeding conduit, the water of feeding conduit can be infiltrated in the pond.Separated by plastic wall between the electrolyzer, directly be not communicated with.Between per two row's electrolyzers, Packed water supply line 10 is installed all.Electrode between the electrolyzer is contacted mutually, the negative pole of getting an electrolyzer connects the positive pole of next electrolyzer, continuous 60~70 electrolyzers can contain 1 or several polyphone groups as a polyphone group in the cell body, a producer can contain 1 again to several electrolyzers.
Open an aperture above cathode compartment 19, connection supplies the not neutral gear of pipeline top, and hydrogen is discharged.Above anolyte compartment 18, do not seal and leave opening, make directly upwards circulation of oxygen.
Connect filler 5 in total feeding conduit bottom to exterior open cell near outer wall.
Feedwater newspaper show device by be fixed on rectification close face fluorescent tube and place the electrode slice 20 of feeding conduit to form.On the electrode plastic sheet, fix a negative potential for one, three positive electrodes are fixed in the other end, and first positive electricity is point-like very, is fixed on high point, connects an amber light pipe, and amber light is bright when water level arrives this, and the expression water level is full, should stop to add water; Second positive electricity very encircles the semicircle sheet, connects the green light pipe, and this electrode lower-most point is the dividing point of ordinary water-level, and green light is bright when water level is higher than this, and expression is normal, is lower than this green light and does not work, the expression water shortage.The 3rd positive electricity is the lengthy motion picture shape very, is fixed in the arch semicircle of second positive electrode, and lower-most point connects red light than low 3~5 millimeters slightly of second positive electrodes.The circuit that feedwater newspaper shows device positive pole of the 58th electrolyzer in the electrolyzer draws a lead and makes power supply, and main track is divided into three branch lines and connects Huang, green, red light pipe respectively.Main track and negative wire are together introduced in the feeding conduit, respectively three positive poles and a negative pole of receiving electrode sheet.Newspaper shows that the negative wire head of device directly is communicated with rectification and closes interior negative wire.
Operating process of the present utility model:
At first inject and contain the electrolytical aqueous solution, make water level reach normal to electrolyzer.With plug insertion socket, press switch, make closing of circuit, electrolysis takes place.Admit gas with gas-storing bag at blast gate, large-scale producer is air feed directly, needn't gas storage.
Claims (2)
1, a kind of microporous oxyhydrogen generator comprises electrolyzer, and water channel and exhaust channel is characterized in that: cell body (8) is composed in series by a plurality of electrolyzers (9).
2, oxyhydrogen generator as claimed in claim 1 is characterized in that: 60~70 electrolyzers are made a polyphone group, can contain 1 or several series connection groups in the cell body, and 1 producer can contain 1 or several cell body.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 97229417 CN2310770Y (en) | 1997-10-16 | 1997-10-16 | Porous oxyhydrogen generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 97229417 CN2310770Y (en) | 1997-10-16 | 1997-10-16 | Porous oxyhydrogen generator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2310770Y true CN2310770Y (en) | 1999-03-17 |
Family
ID=33942223
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 97229417 Expired - Fee Related CN2310770Y (en) | 1997-10-16 | 1997-10-16 | Porous oxyhydrogen generator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2310770Y (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106014703A (en) * | 2016-06-30 | 2016-10-12 | 东莞市绿能宝汽车用品科技有限公司 | Hydrogen and oxygen gas generator system for vehicle |
CN106014704A (en) * | 2016-06-30 | 2016-10-12 | 东莞市绿能宝汽车用品科技有限公司 | Oxyhydrogen gas generator system for vehicles |
CN106014702A (en) * | 2016-06-30 | 2016-10-12 | 东莞市绿能宝汽车用品科技有限公司 | Hydrogen-oxygen gas generator used for vehicles |
CN106014705A (en) * | 2016-06-30 | 2016-10-12 | 东莞市绿能宝汽车用品科技有限公司 | Oxyhydrogen gas generator for vehicles |
-
1997
- 1997-10-16 CN CN 97229417 patent/CN2310770Y/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106014703A (en) * | 2016-06-30 | 2016-10-12 | 东莞市绿能宝汽车用品科技有限公司 | Hydrogen and oxygen gas generator system for vehicle |
CN106014704A (en) * | 2016-06-30 | 2016-10-12 | 东莞市绿能宝汽车用品科技有限公司 | Oxyhydrogen gas generator system for vehicles |
CN106014702A (en) * | 2016-06-30 | 2016-10-12 | 东莞市绿能宝汽车用品科技有限公司 | Hydrogen-oxygen gas generator used for vehicles |
CN106014705A (en) * | 2016-06-30 | 2016-10-12 | 东莞市绿能宝汽车用品科技有限公司 | Oxyhydrogen gas generator for vehicles |
CN106014703B (en) * | 2016-06-30 | 2019-01-25 | 东莞市绿麒麟环保科技有限公司 | Oxy-hydrogen gas generator system used for vehicle |
CN106014704B (en) * | 2016-06-30 | 2019-01-25 | 东莞市绿麒麟环保科技有限公司 | Oxy-hydrogen gas generator system used for vehicle |
CN106014702B (en) * | 2016-06-30 | 2019-02-05 | 东莞市绿麒麟环保科技有限公司 | Oxy-hydrogen gas generator used for vehicle |
CN106014705B (en) * | 2016-06-30 | 2019-03-05 | 东莞市绿麒麟环保科技有限公司 | A kind of oxy-hydrogen gas generator used for vehicle |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |