CN205036454U - Utilize oxyhydrogen and ultraviolet ozone body to mix device that removes carbon deposit - Google Patents

Utilize oxyhydrogen and ultraviolet ozone body to mix device that removes carbon deposit Download PDF

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Publication number
CN205036454U
CN205036454U CN201520606748.6U CN201520606748U CN205036454U CN 205036454 U CN205036454 U CN 205036454U CN 201520606748 U CN201520606748 U CN 201520606748U CN 205036454 U CN205036454 U CN 205036454U
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China
Prior art keywords
pipeline
communicated
threeway
gas
gas cooling
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Expired - Fee Related
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CN201520606748.6U
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Chinese (zh)
Inventor
周德宏
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Dalian An Keruisi Energy Science Co Ltd
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Dalian An Keruisi Energy Science Co Ltd
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Priority to CN201520606748.6U priority Critical patent/CN205036454U/en
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Publication of CN205036454U publication Critical patent/CN205036454U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses an utilize oxyhydrogen and ultraviolet ozone body to mix device that removes carbon deposit belongs to car technical field. The utility model discloses a pressure control appearance and electrolysis trough, the pressure control appearance passes through the gas outlet no. 1 that the pipeline leads to the electrolysis trough in a row, the gas outlet no. 2 of electrolysis trough and the one end intercommunication of pipeline no. 2, and the other end of pipeline no. 2 is in the inside of gas -cooled bottle and be close to the inside bottom of gas -cooled bottle, is close to to have the venthole on the pipeline no. 2 of two other ends of pipeline, and pipeline no. 2 gets into the inside of gas -cooled bottle from the upper portion of gas -cooled bottle, the fluviograph has on the outer wall of gas -cooled bottle, the one end of the upper portion connecting line no. 3 of gas -cooled bottle.

Description

A kind of device utilizing oxyhydrogen gas and ultraviolet and ozone gas and vapor permeation carbon remover
Technical field
The utility model relates to a kind of device utilizing oxyhydrogen gas and ultraviolet and ozone gas and vapor permeation carbon remover, belongs to automobile technical field.
Background technique
Current hydrogen-oxygen automobile carbon removing machine is that the principle that make use of brine electrolysis generation hydrogen or oxygen gas carries out carbon cleaning to motor car engine inside and related accessories.Hydrogen burns together with oxygen, air, fuel oil, carbon distribution.Reach de-carbon object.Ozone reaction activity is far away than oxygen (O 2) strong, found by research, oxyhydrogen gas is mixed by a certain proportion of with ozone, makes it have more combustion catalytic, reaches oxygen-enriched combusting, has more active a kind of mixed gas than single oxyhydrogen gas.
Summary of the invention
The utility model for the proposition of above problem, and develops a kind of device utilizing oxyhydrogen gas and ultraviolet and ozone gas and vapor permeation carbon remover.
The utility model takes following technological scheme:
Utilize a device for oxyhydrogen gas and ultraviolet and ozone gas and vapor permeation carbon remover, comprise pressure controller and electrolytic bath, pressure controller is communicated with the air outlet one of electrolytic bath by pipeline one, the air outlet two of electrolytic bath is communicated with one end of pipeline two, the bottom of the other end in the inside of gas cooling bottle also near gas cooling bottle inside of pipeline two, on the pipeline two of pipeline two the other end, have air outlet hole, pipeline two enters the inside of gas cooling bottle from the top of gas cooling bottle, the outer wall of gas cooling bottle has water-level gauge, one end of the top connecting pipeline three of gas cooling bottle, one end of the pipeline three on gas cooling bottle top is communicated with the inside of gas cooling bottle, and the other end of pipeline three is communicated with one end of solenoid valve four, one end of the other end connecting pipeline 13 of solenoid valve four, the top of gas cooling bottle is connected with one end of pipeline four, one end of gas cooling bottle upper pipeline four is communicated with the inside of gas cooling bottle, the other end of pipeline four is communicated with one end of voltage regulating meter, the other end of voltage regulating meter is communicated with one end of pipeline 17, the other end of pipeline 17 is communicated with threeway three, threeway three is communicated with one end of pipeline five, the other end of pipeline five is communicated with one end of air valve Flow valve, one end of the other end connecting pipeline ten of air valve Flow valve, the other end of pipeline ten is communicated with one end of ozonizer, the other end of ozonizer is communicated with air pump, air pump is connected with the ABAP Adapter in control box, there is in control box ABAP Adapter and control terminal, air pump is connected with the control terminal in control box, threeway three is communicated with threeway one by pipeline 18, and threeway one is communicated with one end of solenoid valve one by pipeline five, and the other end of solenoid valve one is communicated with threeway four by pipeline 14, threeway one is communicated with threeway two by pipeline seven, threeway two is communicated with one end of solenoid valve two by pipeline 15, the other end of solenoid valve two is communicated with threeway five by pipeline 16, and threeway five-way is crossed pipeline 11 and is communicated with threeway four, and one end of pipeline nine is communicated with threeway four, threeway two is communicated with one end of solenoid valve three by pipeline eight, and the other end of solenoid valve three is communicated with threeway five by pipeline 12.
Utility model works principle: utilize electrolytic tank electrolysis purified water to produce hydrogen and oxygen, lead to and control its outlet pressure at 1.5kgf/cm by pressure controller 2, hydrogen and oxygen export dry pure hydrogen and oxygen by gas cooling bottle.Ozonizer is controlled by control box, and ozonizer controls to produce ozone gas by control terminal.Hydrogen and oxygen control gas output size by voltage regulating meter, and ozone gas controls the discharge capacity of output ozone gas by air valve Flow valve.Hydrogen, oxygen and ozone are by becoming mixed gas after threeway three.Automobile equipment for different air displacement selects different gas outputs, controls respectively to export high, medium and low third gear gas output by solenoid valve one, solenoid valve two and solenoid valve three.After de-carbon terminates, powered-down, hydrogen and oxygen are exhausted by the solenoid valve four on the pipeline three of gas cooling bottle, and the hydrogen stored in emptying equipment and oxygen, prevent tempering from occurring.
The utility model beneficial effect: hydrogen or oxygen gas and ozone are the gas mixed completely, low cost, only uses water, cooling liquid and electric power.Ozone reaction activity is far away than oxygen (O 2) strong, found by research, oxyhydrogen gas is mixed by a certain proportion of with ozone, makes it have more combustion catalytic, reaches oxygen-enriched combusting, has more active a kind of mixed gas than single oxyhydrogen gas.
Accompanying drawing explanation
Fig. 1 is structure diagram of the present utility model.
In figure: 1. pressure controller, 2. electrolytic bath, 3. gas cooling bottle, 4. water-level gauge, 5. air outlet hole, 6. threeway one, 7. threeway two, 8. voltage regulating meter, 9. threeway three, 10. ozonizer, 11. air pumps, 12. control boxs, 13. ABAP Adapter, 14. control terminals, 15. air valve Flow valves, 16. solenoid valves one, 18. solenoid valves three, 19. solenoid valves four, 20. pipelines one, 21. pipelines two, 22. pipelines three, 23. pipelines four, 24. pipelines five, 25. pipelines six, 26. pipelines seven, 27. pipelines eight, 28. pipelines nine, 29. pipelines ten, 30. threeways four, 31. pipelines 11, 32. threeways five, 33. pipelines 12, 34. pipelines 13, 35. pipelines 14, 36. pipelines 15, 37. solenoid valves two, 38. pipelines 16, 39. pipelines 17, 40. pipelines 18, 41. air outlets one, 42. air outlets two.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described further:
As shown in Figure 1: a kind of device utilizing oxyhydrogen gas and ultraviolet and ozone gas and vapor permeation carbon remover, comprises pressure controller 1 and electrolytic bath 2, pressure controller 1 is communicated with the air outlet 1 of electrolytic bath 2 by pipeline 1, the air outlet 2 42 of electrolytic bath 2 is communicated with one end of pipeline 2 21, the bottom of the other end in the inside of gas cooling bottle 3 also near gas cooling bottle 3 inside of pipeline 2 21, on the pipeline 2 21 of pipeline 2 21 the other end, have air outlet hole 5, pipeline 2 21 enters the inside of gas cooling bottle 3 from the top of gas cooling bottle 3, the outer wall of gas cooling bottle 3 has water-level gauge 4, one end of the top connecting pipeline 3 22 of gas cooling bottle 3, one end of the pipeline 3 22 on gas cooling bottle 3 top is communicated with the inside of gas cooling bottle 3, the other end of pipeline 3 22 is communicated with one end of solenoid valve 4 19, one end of the other end connecting pipeline 13 of solenoid valve 4 19, the top of gas cooling bottle 3 is connected with one end of pipeline 4 23, one end of gas cooling bottle 3 upper pipeline 4 23 is communicated with the inside of gas cooling bottle 3, the other end of pipeline 4 23 is communicated with one end of voltage regulating meter 8, the other end of voltage regulating meter 8 is communicated with one end of pipeline 17, the other end of pipeline 17 is communicated with threeway 39, threeway 39 is communicated with one end of pipeline 5 24, the other end of pipeline 5 24 is communicated with one end of air valve Flow valve 15, one end of the other end connecting pipeline 10 of air valve Flow valve 15, the other end of pipeline 10 is communicated with one end of ozonizer 10, the other end of ozonizer 10 is communicated with air pump 11, air pump 11 is connected with the ABAP Adapter 13 in control box 12, ABAP Adapter 13 is 220 volts of ac power supplys, there is in control box 12 ABAP Adapter 13 and control terminal 14, air pump 11 is connected with the control terminal 14 in control box 12, threeway 39 is communicated with threeway 1 by pipeline 18, and threeway 1 is communicated with one end of solenoid valve 1 by pipeline 5 25, and the other end of solenoid valve 1 is communicated with threeway 4 30 by pipeline 14, threeway 1 is communicated with threeway 27 by pipeline 7 26, threeway 27 is communicated with one end of solenoid valve 2 37 by pipeline 15, the other end of solenoid valve 2 37 is communicated with threeway 5 32 by pipeline 16, threeway 5 32 is communicated with threeway 4 30 by pipeline 11, and one end of pipeline 9 28 is communicated with threeway 4 30, threeway 27 is communicated with one end of solenoid valve 3 18 by pipeline 8 27, and the other end of solenoid valve 3 18 is communicated with threeway 5 32 by pipeline 12.
The above; be only the utility model preferably embodiment; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; be equal to according to the technical solution of the utility model and inventive concept thereof and replace or change, all should be encompassed within protection domain of the present utility model.

Claims (1)

1. one kind utilizes the device of oxyhydrogen gas and ultraviolet and ozone gas and vapor permeation carbon remover, comprise pressure controller (1) and electrolytic bath (2), it is characterized in that: pressure controller (1) is communicated with the air outlet one (41) of electrolytic bath (2) by pipeline one (20), the air outlet two (42) of electrolytic bath (2) is communicated with one end of pipeline two (21), the other end bottom that also close gas cooling bottle (3) is inner in the inside of gas cooling bottle (3) of pipeline two (21), on the pipeline two (21) of pipeline two (21) the other end, there is air outlet hole (5), pipeline two (21) enters the inside of gas cooling bottle (3) from the top of gas cooling bottle (3), the outer wall of gas cooling bottle (3) has water-level gauge (4), one end of the top connecting pipeline three (22) of gas cooling bottle (3), one end of the pipeline three (22) on gas cooling bottle (3) top is communicated with the inside of gas cooling bottle (3), the other end of pipeline three (22) is communicated with one end of solenoid valve four (19), one end of the other end connecting pipeline ten three (34) of solenoid valve four (19), the top of gas cooling bottle (3) is connected with one end of pipeline four (23), one end of gas cooling bottle (3) upper pipeline four (23) is communicated with the inside of gas cooling bottle (3), the other end of pipeline four (23) is communicated with one end of voltage regulating meter (8), the other end of voltage regulating meter (8) is communicated with one end of pipeline ten seven (39), the other end of pipeline ten seven (39) is communicated with threeway three (9), threeway three (9) is communicated with one end of pipeline five (24), the other end of pipeline five (24) is communicated with one end of air valve Flow valve (15), one end of the other end connecting pipeline ten (29) of air valve Flow valve (15), the other end of pipeline ten (29) is communicated with one end of ozonizer (10), the other end of ozonizer (10) is communicated with air pump (11), air pump (11) is connected with the ABAP Adapter (13) in control box (12), there is in control box (12) ABAP Adapter (13) and control terminal (14), air pump (11) is connected with the control terminal (14) in control box (12), threeway three (9) is communicated with threeway one (6) by pipeline ten eight (40), threeway one (6) is communicated with by pipeline five (25) one end with solenoid valve one (16), and the other end of solenoid valve one (16) is communicated with threeway four (30) by pipeline ten four (35), threeway one (6) is communicated with threeway two (7) by pipeline seven (26), threeway two (7) is communicated with by pipeline ten five (36) one end with solenoid valve two (37), the other end of solenoid valve two (37) is communicated with threeway five (32) by pipeline ten six (38), threeway five (32) is communicated with threeway four (30) by pipeline ten one (31), and one end of pipeline nine (28) is communicated with threeway four (30), threeway two (7) is communicated with by pipeline eight (27) one end with solenoid valve three (18), and the other end of solenoid valve three (18) is communicated with threeway five (32) by pipeline ten two (33).
CN201520606748.6U 2015-08-13 2015-08-13 Utilize oxyhydrogen and ultraviolet ozone body to mix device that removes carbon deposit Expired - Fee Related CN205036454U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520606748.6U CN205036454U (en) 2015-08-13 2015-08-13 Utilize oxyhydrogen and ultraviolet ozone body to mix device that removes carbon deposit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520606748.6U CN205036454U (en) 2015-08-13 2015-08-13 Utilize oxyhydrogen and ultraviolet ozone body to mix device that removes carbon deposit

Publications (1)

Publication Number Publication Date
CN205036454U true CN205036454U (en) 2016-02-17

Family

ID=55295363

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520606748.6U Expired - Fee Related CN205036454U (en) 2015-08-13 2015-08-13 Utilize oxyhydrogen and ultraviolet ozone body to mix device that removes carbon deposit

Country Status (1)

Country Link
CN (1) CN205036454U (en)

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

Granted publication date: 20160217

Termination date: 20170813

CF01 Termination of patent right due to non-payment of annual fee