CN201615499U - Light hydrocarbon columnar gas mixing cabinet based on systematic technology - Google Patents
Light hydrocarbon columnar gas mixing cabinet based on systematic technology Download PDFInfo
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- CN201615499U CN201615499U CN2009202436113U CN200920243611U CN201615499U CN 201615499 U CN201615499 U CN 201615499U CN 2009202436113 U CN2009202436113 U CN 2009202436113U CN 200920243611 U CN200920243611 U CN 200920243611U CN 201615499 U CN201615499 U CN 201615499U
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- gas
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- vaporizer
- collecting tank
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Abstract
The utility model relates to a light hydrocarbon columnar gas mixing cabinet based on the systematic technology, which is mainly used for civil gas and can also be used for industrial fields such as gas for small-sized boilers and roasting kilns. To increase gas production efficiency and safety of gas mixing cabinets and lead the gas mixing cabinets to produce gas at normal temperature, the technical scheme includes that a gasification chamber is a cylinder made of steel plates, a light hydrocarbon pump is arranged at the end opening of the gasification chamber, a high-flow ejector is mounted on the upper side of the gasification chamber and connected with an air compressor, a cylindrical oil-gas mixer is arranged on the inner side of the gasification chamber, an gasifier is mounted between the gasification chamber and the oil-gas mixer, a gasification collecting tank is disposed inside the oil-gas mixer, an automatic shutter is arranged at one end of the oil-gas mixer, a filter is arranged at the input end of the gasification collecting tank, and an automatic rotary ejector is arranged at the output end. The light hydrocarbon columnar gas mixing cabinet has the advantages of realizing gas production at normal temperature and having high gas production efficiency and little investment.
Description
Technical field
The utility model is mainly used in domestic gas, also can be used as miniature boiler, and the roasting kiln is with industrial circles such as combustion gas.
Background technology
Existing lighter hydrocarbons column is mixed gas holder and is mainly adopted air bubbling system gas and two kinds of forms of lighter hydrocarbons heating and gasifying system gas.The former gas making efficiency is low, can not large-scale application.In gas-making process, there is potential safety hazard in the latter.
Summary of the invention
The utility model is in order to improve the gas making efficiency that mixes the device cabinet and to improve security performance, just can make gas at normal temperatures, the technical scheme that adopts is: comprise control valve, cascading water valve, float-ball type limit liquid level adjuster and Pressure gauge and safety valve, be installed in the outside of vaporizer, it is characterized in that: vaporizer is made cylindrical barrel by steel plate, and its port is provided with light hydrocarbon pump; At the vaporizer upside big flow injector is installed, big flow injector links to each other with air compressor machine; Be provided with cylindric oil gas blender in the vaporizer inboard, between vaporizer and the oil gas blender gasifier be installed; The oil gas mixer interior is provided with safety shutoff for the gasification collecting tank at oil gas blender one end; The input of gasification collecting tank is provided with filter, and output is provided with automatic rotary jet.
The spacing of described vaporizer and oil gas blender is 50cm, and the spacing of oil-gas mixer and gasification collecting tank is 50cm.
The thickness of the steel plate of described vaporizer, oil-gas mixer, gasification collecting tank is 10cm.
Operation principle of the present utility model is, by air compressor machine according to certain pressure, with the several times of lighter hydrocarbons volume, in the column that stores lighter hydrocarbons is mixed the device cabinet through big flow injector entrained air; Air is dispersed into countless bubbles by the lighter hydrocarbons fluid column time, bubble rises by the cross section, and liquid phase is constantly evaporated in bubble, and when reaching boiling temperature, seethe with excitement simultaneously in the liquid phase surface.Liquid phase transition is that gas phase is more accelerated, and gas phase fiercely increases severely, and quantity of steam increases increase rapidly.By this method, realized the normal temperature gasification of lighter hydrocarbons.
The beneficial effects of the utility model are: 1, lighter hydrocarbons C5 column is mixed gas holder and is not needed the chemical catalytic oxidation agent, need not heat, pipe network and kitchen range, water heater do not have condensate and produce, and only mix gas at normal temperatures and finish gasification, be not subjected to the temperature condition influence, still can round-the-clockly normally carry out.
2, safety.Supply station equipment operating pressure only needs conventional fire fighting device at 0.1-0.2Mpa; The pipe network distribution pressure is only at 0.02-0.04Mpa, and the safety coefficient of Gas Explosion Limits can not constitute a threat to the user more than 1.65 times.
3, pollution-free.Institute's exhaust gas discharged---carbonoxide, methyl alcohol, benzene,toluene,xylene concentration all do not surpass the standard (seeing " Sichuan Province's environmental monitoring report " numbering 20000-100 for details) of national environmental protection defined; Wherein total hydrocarbon content does not still have domestic standard, but also lower than Italian national atomosphere quality standard 55.3mg/ cubic meter, and peak only is the 8.5mg/ cubic meter.With natural gas, liquefied petroleum gas is compared, because of the probability of anthracemia much lower.Can claim not have waste residue, the clean energy resource of no waste water.
4, equipment is simple relatively, and its negligible amounts need not heater, has saved the energy, particularly water resource.Determine that the combustion gas parameter is is standard with natural gas 4T and 6T, existing lighter hydrocarbons C5 mixes gas and pipe network system thereof and can directly integrate with when changing source of the gas from now on.
Description of drawings
Fig. 1 is a structure diagram of the present utility model.
The specific embodiment
As shown in Figure 1, lighter hydrocarbons column based on systems technology is mixed gas holder, comprise control valve, cascading water valve 9, float-ball type limit liquid level adjuster 10, Pressure gauge and safety valve, be installed in the outside of vaporizer 6, it is characterized in that: make cylindrical barrel at vaporizer 6 by steel plate, its port is provided with light hydrocarbon pump; Inject light hydrocarbon liquid by light hydrocarbon pump in vaporizer, at the vaporizer upside big flow injector 2 is installed, big flow injector 2 links to each other with air compressor machine 1; Air compressor 1 is to certain pressure, and under the effect of big flow injector 2, entrained air in vaporizer is provided with cylindric oil gas blender 7 in the vaporizer inboard, between vaporizer 1 and the oil gas blender 7 gasifier 12 is installed; Oil gas blender 7 is inner for gasification collecting tank 8, is provided with safety shutoff 5 at oil gas blender 7 one ends; When air pressure is enough big, make the lighter hydrocarbons gaseous mixture enter oil-gas mixer 7 by atmospheric pressure, pressure hour this closer cuts out automatically.The input of gasification collecting tank 8 is provided with filter 4, is used for the impurity of filtering gas.Output is provided with automatic rotary jet 11.
The spacing of described vaporizer and oil gas blender is 50cm, and the spacing of oil-gas mixer and gasification collecting tank is 50cm.
The thickness of the steel plate of described vaporizer, oil-gas mixer, gasification collecting tank is 10cm.
Claims (3)
1. the lighter hydrocarbons column based on systems technology is mixed gas holder, comprise control valve, cascading water valve, float-ball type limit liquid level adjuster, Pressure gauge and safety valve, be installed in the outside of vaporizer, it is characterized in that: make cylindrical barrel at vaporizer by steel plate, its port is provided with light hydrocarbon pump; At the vaporizer upside big flow injector is installed, big flow injector links to each other with air compressor machine; Be provided with cylindric oil gas blender in the vaporizer inboard, between vaporizer and the oil gas mixed air gasifier be installed; The oil gas mixer interior is provided with safety shutoff for the gasification collecting tank at oil gas blender one end; The input of gasification collecting tank is provided with filter, and output is provided with automatic rotary jet.
2. the lighter hydrocarbons column based on systems technology according to claim 1 is mixed gas holder, and it is characterized in that: the spacing of described vaporizer and oil gas blender is 50cm, and the spacing of oil-gas mixer and gasification collecting tank is 50cm.
3. the lighter hydrocarbons column based on systems technology according to claim 1 and 2 is mixed gas holder, and it is characterized in that: the thickness of the steel plate of described vaporizer, oil-gas mixer, gasification collecting tank is 10cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202436113U CN201615499U (en) | 2009-12-01 | 2009-12-01 | Light hydrocarbon columnar gas mixing cabinet based on systematic technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202436113U CN201615499U (en) | 2009-12-01 | 2009-12-01 | Light hydrocarbon columnar gas mixing cabinet based on systematic technology |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201615499U true CN201615499U (en) | 2010-10-27 |
Family
ID=43001867
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202436113U Expired - Fee Related CN201615499U (en) | 2009-12-01 | 2009-12-01 | Light hydrocarbon columnar gas mixing cabinet based on systematic technology |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201615499U (en) |
-
2009
- 2009-12-01 CN CN2009202436113U patent/CN201615499U/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 | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101027 Termination date: 20111201 |