CN2303852Y - Hydrogen-oxygen fuel production apparatus for medicine industry - Google Patents
Hydrogen-oxygen fuel production apparatus for medicine industry Download PDFInfo
- Publication number
- CN2303852Y CN2303852Y CN 97202992 CN97202992U CN2303852Y CN 2303852 Y CN2303852 Y CN 2303852Y CN 97202992 CN97202992 CN 97202992 CN 97202992 U CN97202992 U CN 97202992U CN 2303852 Y CN2303852 Y CN 2303852Y
- Authority
- CN
- China
- Prior art keywords
- double
- raw material
- material storage
- reactor
- pipeline
- 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
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- 239000001301 oxygen Substances 0.000 title claims abstract description 11
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 11
- 239000000446 fuel Substances 0.000 title claims abstract description 10
- 239000003814 drug Substances 0.000 title description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000002994 raw material Substances 0.000 claims abstract description 19
- 239000012530 fluid Substances 0.000 claims description 19
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 239000007788 liquid Substances 0.000 abstract description 7
- 239000007789 gas Substances 0.000 abstract description 6
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 238000005192 partition Methods 0.000 abstract 3
- 239000000126 substance Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 3
- QFXZANXYUCUTQH-UHFFFAOYSA-N ethynol Chemical group OC#C QFXZANXYUCUTQH-UHFFFAOYSA-N 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
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000004438 eyesight Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model discloses a hydrogen-oxygen fuel production apparatus. A partition board is arranged in a frame to divide the frame into an upper and a lower two layers, the upper face of the partition board is fixedly provided with a water raw material storage tank, a gas-liquid separating tank, a gas storage tank and a pressure dividing tank which are orderly connected with each other through pipelines, a double-flow double-layer reactor is arranged under the partition board, the water raw material storage tank is connected with one end of the lower layer of double-flow double-layer reactor through the pipelines and a physical and chemical power-assisted propeller, the other end of the lower layer of double-flow double-layer reactor is connected with one end of the upper layer of double-flow double-layer reactor through the pipelines and a cooler, and the other end of the upper layer of double-flow double-layer reactor is connected with the water raw material storage tank through the pipelines and the cooler. The utility model has high energy conversion rate and safe and stable operation.
Description
The utility model relates to a kind of hydrogen-oxygen fuel production equipment, particularly a kind of hydrogen-oxygen fuel production equipment that is used for pharmaceutical industries.
At present, the medicine industry that has seals with vial, on the make, make fuel with oxy-acetylene, because acetylene produces sulfide, carbide, nitride and carcinogens after burning, therefore contaminate environment not only, also very harmful to the person, workers with long time is worked under this environment, and eyesight can descend gradually, easily sends out diseases such as carninomatosis; Its flame temperature is difficult for regulating simultaneously, the temperature regulation height, easily produce back draft, influence production schedule; Temperature is low, and to seal rate lower again; Moreover also need establish special adjustment personnel in the production process, and auxiliary facilitys such as air compressor, exhaust blower, so oxy-acetylene is used in pharmaceutical industries, not only expensive big, efficient is low, and to environment with harmful and unhelpful per capita.
The purpose of this utility model is to improve the shortcoming of prior art, and a kind of hydrogen-oxygen fuel production equipment that is used for pharmaceutical industries is provided, and its energy conversion rate height is simple in structure, is easy to make, and operating safety is stable.
For achieving the above object, the utility model is taked following design: in a framework, there have a dividing plate that framework is divided into to be upper and lower two-layer, install above the dividing plate and be mixed with electrolytical water raw material storage tanks, knockout drum, gas-holder and wikipedia type safety regulating valve, manometric dividing potential drop jar are housed, and be connected successively by pipeline; The column of tube support plate is housed below the dividing plate, is fixed with double-current double-deck reactor by fixing catch on the column, the anode and cathode terminals of a direct current power supply inserts a utmost point of a double-current double-deck reactor of the utmost point and upper strata of the double-deck reactor of lower floor's double fluid respectively; Described water raw material storage tanks is connected through the end of a physics and chemistry power-assisted thruster with the double-deck reactor of lower floor's double fluid by pipeline, its the other end is connected through the end of a water cooler with the double-deck reactor of upper strata double fluid by pipeline, and the other end of the double-deck reactor of upper strata double fluid is connected with the water raw material storage tanks through water cooler by pipeline again.
During use, be equipped with and be mixed with the interior synthetic fluid of ionogen water raw material storage tanks through the effect of physics and chemistry power-assisted thruster, the water raw material is sent in the double-current double-deck reactor, under the effect of the double-deck reactor positive and negative electrode of double fluid, the reaction that produces electrolysis of the synthetic liquid of water source material, make it reach isolating purpose, produce hydrogen or oxygen gas, liquid mixture, after the water cooler cooling, be input in the double-deck reactor of second layer double fluid, carry out the re-electrolysis reaction, the liquid that the reaction back produces, gas is input to by the double-deck reactor of double fluid and mixes in the water cooler, after cooling off by the water cooler output tube with cooled liquid, gas is sent back in the former water raw material storage tanks, and the gas in this jar is through knockout drum, gas-holder delivers gas in the dividing potential drop jar standby, and isolated liquid is then participated in cyclic electrolysis through physics and chemistry power-assisted thruster once more.
The utility model is with pharmaceutical industries hydrogen-oxygen fuel production equipment, the effciency of energy transfer height, simple in structure, be easy to make, operating safety is stable.
The utility model is described in further detail with accompanying drawing to quote embodiment below.
Fig. 1 is the utility model structural representation
Embodiment
In a framework 1, be fixed with a dividing plate 2, framework is divided into two-layer up and down, install above the dividing plate and be mixed with electrolytical water raw material storage tanks 3, knockout drum 4, gas-holder 5, with the dividing potential drop jar 8 that pressure-controlling table 6, voltage-divider 7 are housed, and be connected in turn by pipeline 9,10,11,12, the column 13 of tube support plate is housed below the dividing plate, be fixed with double-deck double-current reactor 15,16 by fixing catch 14 on the column.The anode and cathode terminals 18,19 of one direct current power supply 17 inserts the positive pole 20 of the double-deck reactor 15 of lower floor's double fluid and the negative pole 21 of the double-deck reactor of upper strata double fluid, (side two double-deck reactors of double fluid up and down only are shown among the figure, and opposite side also has, and structure is identical) respectively; Described water raw material storage tanks 3 is passed through pipeline 22 through physics and chemistry power-assisted thruster 23, pipeline 24 is connected with an end of the double-deck reactor of lower floor's double fluid, its the other end passes through pipeline 25 through water cooler 26, pipeline 27 is connected with an end of the double-deck reactor 16 of upper strata double fluid, and the other end of the double-deck reactor of upper strata double fluid is again by pipeline 28, threeway 29 is through water cooler 30, pipeline 31 is connected with the water raw material storage tanks, another pipeline of threeway 29 connects the pipeline from the double-deck reactor of opposite side lower floor double fluid, water cooler 26 and the 30 other fans 32 that are provided with respectively, 33 blowings are so that cooling.After the flap 34 of water raw material storage tanks 3 is opened, pour into the water raw material through this mouth, pressure limiting explosion trap 35 is arranged on the gas-holder, the rupture disk that surpasses behind the pressure store on it as gaseous tension can break automatically, the danger of avoiding superpressure to cause, after reaching output pressure, the pressure in the gas-holder then can export to dividing potential drop jar 8 through output tube 12, the dividing potential drop jar is provided with pressure-controlling table 6, after being pressed into above specified pressure, and the effect of pressure-controlling table, power supply disconnects, after pressure drops to authorized pressure, power connection, medical hydrogen-oxygen generating unit normally moves, voltage-divider is exported to medical combustion equipment with gas and is carried out burning work under the control of its wikipedia type safety regulating valve.As the generation tempering of burning, the wikipedia type safety regulating valve can go out fire resistance, guarantees that medical hydrogen-oxygen generating unit safety and stability carries out.Water cooler 26,30 is fixed on framework 1 and the dividing plate 2 by screw 36, liquid typotron 37 is housed in order to observe water raw material add-on on the water raw material storage tanks 3.
Claims (2)
1, a kind of hydrogen-oxygen fuel production equipment that is used for pharmaceutical industries, it is characterized in that: in a framework, there have a dividing plate that framework is divided into to be upper and lower two-layer, install above the dividing plate and be mixed with electrolytical water raw material storage tanks, knockout drum, gas-holder and wikipedia type safety regulating valve, manometric dividing potential drop jar are housed, and be connected successively by pipeline; The column of tube support plate is housed below the dividing plate, is fixed with double-current double-deck reactor by fixing catch on the column, the anode and cathode terminals of a direct current power supply inserts a utmost point of a double-current double-deck reactor of the utmost point and upper strata of the double-deck reactor of lower floor's double fluid respectively; Described water raw material storage tanks is connected through the end of a physics and chemistry power-assisted thruster with the double-deck reactor of lower floor's double fluid by pipeline, its the other end is connected through the end of a water cooler with the double-deck reactor of upper strata double fluid by pipeline, and the other end of the double-deck reactor of upper strata double fluid is connected with the water raw material storage tanks through water cooler by pipeline again.
2, a kind of hydrogen-oxygen fuel production equipment that is used for pharmaceutical industries according to claim 1 is characterized in that: the water cooler next door is provided with fan respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 97202992 CN2303852Y (en) | 1997-04-04 | 1997-04-04 | Hydrogen-oxygen fuel production apparatus for medicine industry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 97202992 CN2303852Y (en) | 1997-04-04 | 1997-04-04 | Hydrogen-oxygen fuel production apparatus for medicine industry |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2303852Y true CN2303852Y (en) | 1999-01-13 |
Family
ID=33923984
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 97202992 Expired - Fee Related CN2303852Y (en) | 1997-04-04 | 1997-04-04 | Hydrogen-oxygen fuel production apparatus for medicine industry |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2303852Y (en) |
-
1997
- 1997-04-04 CN CN 97202992 patent/CN2303852Y/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent for invention or patent application | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: PATENTEE ADDRESS; FROM: 201, BUILDING 4, KEJI STREET, WANGHUA DISTRICT, FUSHUN CITY, LIAONING PROVINCE, 113001 TO: LVSEGONGCHENGJISHUYANJIU INSTITUTE, LIUXUESHENGCHUANGYEYUAN DISTRICT, NO. 10, ZHU JIANG ROAD, YINTAI CITY DEVELOPMENT AREA, SHANDONG PROVINCE, 264006 |
|
| CP03 | Change of name, title or address |
Address after: 264006 Green Engineering Technology Research Institute, Zhujianglu Road 10 Development Zone, Yantai, Shandong Patentee after: Hu Xiuying Address before: Science and Technology Street Wanghua District 113001 Liaoning city of Fushun province No. 4 Building 201 Patentee before: Hu Xiuying |
|
| C53 | Correction of patent for invention or patent application | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: PATENTEE ADDRESS; FROM: NO. 10, ZHU JIANG ROAD, YINTAI CITY DEVELOPMENT AREA TO: LVSENENGYUANKEJIKAIFAYOUXIAN COMPANY, DONGSHENZHEN CITY, HOUSE 3, BUILDING 2, SHANGMEILINDUOLIGONGYE DISTRICT, SHENZHEN CITY, 518049 |
|
| CP03 | Change of name, title or address |
Address after: 518049 Shenzhen City Meilin Li Industrial Zone two floor east of Shenzhen City Green Energy Technology Development Co Ltd Patentee after: Hu Xiuying Address before: No. 10, Zhujianglu Road, Yantai Development Zone Patentee before: Hu Xiuying |
|
| C53 | Correction of patent for invention or patent application | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: PATENTEE; FROM: HU XIUYING TO: LUSE ENERGY SCI. + TECH. DEV. CO., LTD., SHENZHEN CITY |
|
| CP01 | Change in the name or title of a patent holder |
Patentee after: Shenzhen Green Energy Source Science and Technology Development Co., Ltd. Patentee before: Hu Xiuying |
|
| 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 |