CN201971900U - Oxyhydrogen machine - Google Patents
Oxyhydrogen machine Download PDFInfo
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- CN201971900U CN201971900U CN201120026066XU CN201120026066U CN201971900U CN 201971900 U CN201971900 U CN 201971900U CN 201120026066X U CN201120026066X U CN 201120026066XU CN 201120026066 U CN201120026066 U CN 201120026066U CN 201971900 U CN201971900 U CN 201971900U
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- regulating chamber
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- 230000001105 regulatory effect Effects 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 230000001276 controlling effect Effects 0.000 claims description 16
- 239000007789 gas Substances 0.000 abstract description 37
- 239000001257 hydrogen Substances 0.000 abstract description 11
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 11
- 239000007788 liquid Substances 0.000 abstract description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 7
- 239000001301 oxygen Substances 0.000 abstract description 7
- 229910052760 oxygen Inorganic materials 0.000 abstract description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 6
- 238000005516 engineering process Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 description 8
- 239000008151 electrolyte solution Substances 0.000 description 6
- 150000002431 hydrogen Chemical class 0.000 description 5
- 238000012544 monitoring process Methods 0.000 description 5
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 4
- 229910001882 dioxygen Inorganic materials 0.000 description 4
- 238000010992 reflux Methods 0.000 description 4
- 238000005520 cutting process Methods 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000008186 active pharmaceutical agent Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 230000005669 field effect Effects 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Classifications
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- 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
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
一种氢氧机，包括微电脑控制模块、开关电源、电解槽、加压循环泵、温度调节箱、分离塔、加液罐、加压水泵、气体干燥器、多级阻火罐。本实用新型对照现有技术的有益效果是：(1)由于采用了微电脑控制模块，对设备的电流、电压、温度、压力、液位等各种信号进行快速检测与监控，同时控制开关电源、加压水泵及其它设备等进行协调有序的工作，使设备人机操作介面简洁、灵活，操作自动化程度更高，设备工作性能更加稳定、安全，可以自动调节气体产量，有利于提高生产效率，降低能耗。(2)由于采用了国内具有领先技术的大功率IGBT型开关电源，因此可以保证设备工作更可靠、稳定、用电效率更高。
An oxygen hydrogen generator includes a microcomputer control module, a switching power supply, an electrolyzer, a pressurized circulation pump, a temperature regulating box, a separation tower, a liquid filling tank, a pressurized water pump, a gas dryer, and a multi-stage flame arresting tank. The beneficial effects of the utility model compared with the prior art are: (1) due to the adoption of the microcomputer control module, various signals such as current, voltage, temperature, pressure, and liquid level of the equipment are quickly detected and monitored, and at the same time, the switching power supply, The pressurized water pump and other equipment work in a coordinated and orderly manner, making the man-machine operation interface of the equipment simple and flexible, with a higher degree of automation in operation, more stable and safe equipment performance, and automatic adjustment of gas output, which is conducive to improving production efficiency. Reduce energy consumption. (2) Since the high-power IGBT switching power supply with domestic leading technology is adopted, it can ensure that the equipment works more reliably, stably, and has higher power consumption efficiency.
Description
Technical field
The utility model relates to a kind of oxyhydrogen machine.
Background technology
Since last century, along with the global economy fast development, the energy, environment and enjoy destruction naturally, limited resources is by unordered utilization, and in process of production by invisible waste, atmosphere is caused global warming by severe contamination, available stock is shortage gradually, and human survival and ecotope have been caused serious harm and immeasurable loss.The mankind have been fully recognized that the preciousness of resource at present, the importance of protection environment.After oxyhydrogen machine is the electrolyzer full of liquid, at supply current is the equipment of hydrogen and oxygen with water decomposition under the effect directly, mixed gas by gas-water separation, washing output hydrogen and oxygen, this mixed gas is with low cost, compare with acetylene gas can save more than 60% with pneumatolytic this, compare with other gas and to save 30% or more with pneumatolytic, mixed gas temperature of combustion height has improved working efficiency, has increased enterprise profit; Poisonous, the obnoxious flavoures of kind more than ten such as H2S, the P2S that other gas produced in when burning, NO have endangered the human health or safety, and severe contamination environment, and hydrogen and oxygen gas mixture is to be raw material with water, is reduced to water again after its burning generates, so smokeless, nontoxic, tasteless, do not have other pollution, therefore it is more and more wider to adopt oxyhydrogen machine to generate the range of application of mixed gas of hydrogen and oxygen, be applicable to mechanical industry, shipbuilding, bridge, steel construction, oil, electronics, chemical industry, medical, food and drink, automobile, building, electric power, metal processing, welding, a plurality of fields such as cutting.
Such as, the mixed gas that oxyhydrogen machine is generated hydrogen and oxygen is used for the metal cutting field, its advantage is: flame is concentrated, convergency is good, combustionvelocity is fast, the heat affected zone is little, directly flat, bright and clean, the no dross phenomenon of cut surface is stitched in a narrow margin more than the 30%-50% in cutting.
But there is the bigger shortcoming of energy consumption in prior oxyhydrogen machine, so production cost is higher.
Summary of the invention
The purpose of this utility model is that prior art is improved, and a kind of oxyhydrogen machine is provided, and can effectively reduce energy consumption, and the technical scheme of employing is as follows:
Oxyhydrogen machine of the present utility model, comprise microcomputer controlling module, switch power supply, electrolyzer, the pressurized circulation pump, temperature regulating chamber, knockout tower, add flow container, gas flow dryer, multistage back-fire relief jar, it is characterized in that: the described inlet that adds flow container connects the primary outlet of knockout tower, the outlet that adds flow container connects the inlet of pressurized circulation pump, the pressurized circulation pump outlet connects the inlet of electrolyzer, two outlets of electrolyzer connect first inlet of temperature regulating chamber respectively, second inlet, second outlet of knockout tower connects the 3rd inlet of temperature regulating chamber, first inlet of knockout tower, second inlet connects the primary outlet of temperature regulating chamber respectively, second outlet, the 3rd inlet of knockout tower connects an outlet of gas flow dryer, the 4th inlet of temperature regulating chamber connects recirculated water by the recirculated water magnetic valve, the 3rd outlet of temperature regulating chamber connects recirculated water, recirculated water is external, flow into from the 4th inlet, flow out from the 3rd outlet, the 4th outlet of temperature regulating chamber connects the inlet of gas flow dryer, and another outlet of gas flow dryer connects the inlet of multistage back-fire relief jar.
Described switch power supply, electrolyzer, pressurized circulation pump, temperature regulating chamber, knockout tower, the control signal input terminus that adds at least one equipment in flow container, gas flow dryer, the multistage back-fire relief jar connect a control signal output terminal of microcomputer controlling module correspondence.That is to say, switch power supply, electrolyzer, pressurized circulation pump, temperature regulating chamber, knockout tower, the control signal input terminus that adds the one or more equipment in flow container, gas flow dryer, the multistage back-fire relief jar connect a control signal output terminal of microcomputer controlling module correspondence, what control signal input terminuss are arranged, what corresponding control signal output terminals are just arranged, and each control signal input terminus connects the control signal output terminal corresponding with it.The control signal input terminus that therefore, can according to actual needs the control signal output terminal of microcomputer controlling module be connected the equipment that needs control.
For various signals such as the electric current of equipment, voltage, temperature, pressure, liquid level are carried out rapid detection and monitoring, so that control the work that each equipment carries out harmonious orderly, described switch power supply, electrolyzer, pressurized circulation pump, temperature regulating chamber, knockout tower, the signal output part that adds at least one equipment in flow container, gas flow dryer, the multistage back-fire relief jar connect a signal input part of microcomputer controlling module correspondence.That is to say, switch power supply, electrolyzer, pressurized circulation pump, temperature regulating chamber, knockout tower, the signal output part that adds the one or more equipment in flow container, pressure pump, gas flow dryer, the multistage back-fire relief jar connect a signal input part of microcomputer controlling module correspondence, what signal output parts are arranged, what corresponding signal input parts are just arranged, and each signal output part connects the signal input part corresponding with it.The signal output part that therefore, can according to actual needs the signal input part of microcomputer controlling module be connected the equipment that needs detection and monitoring.
In order to guarantee that equipment work is more reliable, stable, power consumption efficiency is higher, described switch power supply adopts high-power IGBT type switch power supply.Wherein, IGBT (Insulated Gate BipolarTransistor), the meaning is the insulated gate bipolar power tube, by the compound full-control type voltage driven type power electronic devices that BJT (double pole triode) and MOS (insulating gate type field effect tube) form, have the advantage of low conduction voltage drop two aspects of the high input impedance of MOSFET and GTR concurrently.
Under the monitoring of microcomputer controlling module, high-power IGBT type switch power supply is activated, and required volts DS produces electrolysis.Electrolyzer decomposes fully to the hot water in the electrolyzer under the effect of voltage, produces the mixed gas of a large amount of hydrogen, oxygen and water vapor.Temperature is stabilized in best aerogenesis state in the electrolyzer.Under the promotion of pressurized circulation pump, mix gas-liquid and electrolyte and sent in the temperature regulating chamber respectively.Electrolytic solution is sent knockout tower back to after constant temperature is handled, also sent back to knockout tower and mix gas-liquid after pre-cooled.The electrolytic solution that refluxes through connecting pipe suck add flow container after pressurized once more recycle pump send into electrolyzer, and the mixed gas that refluxes in knockout tower with after electrolytic solution separates, sent back to temperature regulating chamber once more, the cooling of lowering the temperature.Cooled mixed gas is sent to gas flow dryer, and gas flow dryer is sent isolated water back to knockout tower, and purified hydrogen, oxygen gas mixture are sent into the gas equipment pipeline through variable valve after isolating through multistage back-fire relief jar again.
The utility model beneficial effect against existing technologies is:
(1), owing to adopted microcomputer controlling module, various signals such as the electric current of equipment, voltage, temperature, pressure, liquid level are carried out rapid detection and monitoring, control switching, pressure pump and other equipment etc. carry out the work of harmonious orderly simultaneously, make equipment human-machine operation interface succinct, flexible, operating automation degree is higher, and the equipment work performance is stable more, safety, adjustments of gas output automatically, help enhancing productivity, cut down the consumption of energy.
(2) owing to adopted domestic high-power IGBT type switch power supply, therefore can guarantee that equipment work is more reliable, stable, power consumption efficiency is higher with leading technology.
Description of drawings
Accompanying drawing is the structural representation of the utility model preferred embodiment.
Embodiment
Preferred embodiment
As shown in drawings, the oxyhydrogen machine in this preferred embodiment comprises microcomputer controlling module 1, switch power supply 4, electrolyzer 6, pressurized circulation pump 5, temperature regulating chamber 8, knockout tower 11, adds flow container 3, gas flow dryer 10, multistage back-fire relief jar 9.
Described switch power supply 4, electrolyzer 6, pressurized circulation pump 5, temperature regulating chamber 8, knockout tower 11, the control signal input terminus that adds the equipment in flow container 3, gas flow dryer 10, the multistage back-fire relief jar 9 connect a control signal output terminal of microcomputer controlling module 1 correspondence.Described switch power supply 4, electrolyzer 6, pressurized circulation pump 5, temperature regulating chamber 8, knockout tower 11, the signal output part that adds the equipment in flow container 3, gas flow dryer 10, the multistage back-fire relief jar 9 connect a signal input part of microcomputer controlling module 1 correspondence.
The described inlet that adds flow container 3 connects the primary outlet 115 of knockout tower 11, the outlet that adds flow container 3 connects the inlet of pressurized circulation pump 5, the outlet of pressurized circulation pump 5 connects the inlet of electrolyzer 6, two outlets of electrolyzer 6 connect first inlet 801 of temperature regulating chamber 8 respectively, second inlet 804, second outlet 111 of knockout tower 11 connects the 3rd inlet 806 of temperature regulating chamber 8, first inlet 112 of knockout tower 11, second inlet 113 connects the primary outlet 808 of temperature regulating chamber 8 respectively, second outlet 807, the 3rd inlet 114 of knockout tower 11 connects an outlet of gas flow dryer 10, the 4th inlet 803 of temperature regulating chamber 8 connects external circulating water system by recirculated water magnetic valve 7, do the 3rd outlet 802 of temperature regulating chamber 8 connect external circulating water system? recirculated water is gone into from the 4th inlet 803, go out from the 3rd outlet 802, the 4th outlet 805 of temperature regulating chamber 8 connects the inlet of gas flow dryer 10, another outlet of gas flow dryer 10 connects the inlet 902 of multistage back-fire relief jar 9, and outlet 901 outputs of multistage back-fire relief jar 9 are dry, purified hydrogen, oxygen gas mixture.601 is the positive electrode of electrolyzer 6, and 602 is the negative potential of electrolyzer 6.
Described switch power supply 4 adopts high-power IGBT type switch power supply.
Under the monitoring of microcomputer controlling module 1, switch power supply 4 is activated, and required volts DS produces electrolysis.Electrolyzer 6 decomposes fully to the hot water in the electrolyzer 6 under the effect of voltage, produces the mixed gas of a large amount of hydrogen, oxygen and water vapor.Temperature is stabilized in best aerogenesis state in the electrolyzer 6.Under the promotion of pressurized circulation pump 5, mix gas-liquid and electrolyte and sent into respectively in the temperature regulating chamber 8.Electrolytic solution is sent knockout tower 11 back to after constant temperature is handled, also sent back to knockout tower 11 and mix gas-liquid after pre-cooled.The electrolytic solution that refluxes through connecting pipe suck add flow container 3 after pressurized once more recycle pump 5 send into electrolyzer 6, and the mixed gas that refluxes in knockout tower 11 with after electrolytic solution separates, sent back to temperature regulating chamber 8 once more, the cooling of lowering the temperature.Cooled mixed gas is sent to gas flow dryer 10, and gas flow dryer 10 is sent isolated water back to knockout tower 11, and purified hydrogen, oxygen gas mixture are sent into the gas equipment pipeline through variable valve after isolating through multistage back-fire relief jar 9 again.
The above is preferred embodiment of the present utility model only, is not to be used for limiting practical range of the present utility model; Be all equivalents of being done according to claim scope of the present utility model, be the utility model claim scope and cover.
Claims (4)
1. oxyhydrogen machine, comprise microcomputer controlling module, switch power supply, electrolyzer, the pressurized circulation pump, temperature regulating chamber, knockout tower, add flow container, gas flow dryer, multistage back-fire relief jar, it is characterized in that: the described inlet that adds flow container connects the primary outlet of knockout tower, the outlet that adds flow container connects the inlet of pressurized circulation pump, the pressurized circulation pump outlet connects the inlet of electrolyzer, two outlets of electrolyzer connect first inlet of temperature regulating chamber respectively, second inlet, second outlet of knockout tower connects the 3rd inlet of temperature regulating chamber, first inlet of knockout tower, second inlet connects the primary outlet of temperature regulating chamber respectively, second outlet, the 3rd inlet of knockout tower connects an outlet of gas flow dryer, the 4th inlet of temperature regulating chamber connects recirculated water by the recirculated water magnetic valve, the 3rd outlet of temperature regulating chamber connects recirculated water, the 4th outlet of temperature regulating chamber connects the inlet of gas flow dryer, and another outlet of gas flow dryer connects the inlet of multistage back-fire relief jar.
2. oxyhydrogen machine as claimed in claim 1 is characterized in that: described switch power supply, electrolyzer, pressurized circulation pump, temperature regulating chamber, knockout tower, the control signal input terminus that adds at least one equipment in flow container, gas flow dryer, the multistage back-fire relief jar connect a control signal output terminal of microcomputer controlling module correspondence.
3. oxyhydrogen machine as claimed in claim 2 is characterized in that: described switch power supply, electrolyzer, pressurized circulation pump, temperature regulating chamber, knockout tower, the signal output part that adds at least one equipment in flow container, gas flow dryer, the multistage back-fire relief jar connect a signal input part of microcomputer controlling module correspondence.
4. oxyhydrogen machine as claimed in claim 3 is characterized in that: described switch power supply adopts high-power IGBT type switch power supply.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120026066XU CN201971900U (en) | 2011-01-24 | 2011-01-24 | Oxyhydrogen machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120026066XU CN201971900U (en) | 2011-01-24 | 2011-01-24 | Oxyhydrogen machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201971900U true CN201971900U (en) | 2011-09-14 |
Family
ID=44577007
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120026066XU Expired - Fee Related CN201971900U (en) | 2011-01-24 | 2011-01-24 | Oxyhydrogen machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201971900U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102560523A (en) * | 2012-03-02 | 2012-07-11 | 广州华秦机械设备有限公司 | Low-reactance water electrolysis energy-saving device |
| CN107620643A (en) * | 2017-08-18 | 2018-01-23 | 广东卓梅尼技术股份有限公司 | An analysis and monitoring system for a hydrogen production unit |
| CN110441474A (en) * | 2019-07-15 | 2019-11-12 | 中国船舶重工集团公司第七一八研究所 | A kind of Portable oxyhydrogen calibrating installation and method |
-
2011
- 2011-01-24 CN CN201120026066XU patent/CN201971900U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102560523A (en) * | 2012-03-02 | 2012-07-11 | 广州华秦机械设备有限公司 | Low-reactance water electrolysis energy-saving device |
| CN107620643A (en) * | 2017-08-18 | 2018-01-23 | 广东卓梅尼技术股份有限公司 | An analysis and monitoring system for a hydrogen production unit |
| CN107620643B (en) * | 2017-08-18 | 2019-10-25 | 广东卓梅尼技术股份有限公司 | An analysis and monitoring system for a hydrogen production unit |
| CN110441474A (en) * | 2019-07-15 | 2019-11-12 | 中国船舶重工集团公司第七一八研究所 | A kind of Portable oxyhydrogen calibrating installation and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110914 Termination date: 20120124 |