CN2456037Y - Liquid fuel gasifier at atmosphere - Google Patents
Liquid fuel gasifier at atmosphere Download PDFInfo
- Publication number
- CN2456037Y CN2456037Y CN 00259889 CN00259889U CN2456037Y CN 2456037 Y CN2456037 Y CN 2456037Y CN 00259889 CN00259889 CN 00259889 CN 00259889 U CN00259889 U CN 00259889U CN 2456037 Y CN2456037 Y CN 2456037Y
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- gasification
- liquid fuel
- gas
- post
- screen
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Abstract
The utility model provides a liquid fuel atmospheric temperature gasifier which comprises an air compressor, a gasification column, a balance tank, a connecting pipeline, a pipe network meter and a gas conveying pipeline, wherein grid plates and a gripper rings are arranged in the gasification column, and a spiral cellular network is arranged between each two-layer grid plates. The apparatus can increase liquid gasification flow path and has the advantages of sufficient gasification, high gas production, good gasification effect, low cost and long service life. Especially, sufficient gasification can also be carried out in the situation of lower air temperature in winter, and the gas fired quality and firing effect is increased greatly.
Description
The utility model relates to a kind of gasification installation of liquid fuel, especially for the normal temperature gasification installation of light hydrocarbon liquid fuel.
Because China's subterranean oil, gas reservoir skewness, resource-constrained causes gas supply day to be becoming tight, and has driven the development and use of novel gas thus.These novel gas are broadly divided into pure type combustion gas, the combustion gas of lighter hydrocarbons type, the combustion gas of ether type, hydrolysis-type combustion gas, are combustion gas of lighter hydrocarbons type and the combustion gas of ether type and use more at present.In the combustion gas of lighter hydrocarbons type, lighter hydrocarbons C
3(carbon 3) class, C
4(carbon 4) general boiling point of class I liquid I fuel is lower, automatic gasifying at normal temperatures, and C
5The general boiling point of (carbon 5) class light hydrocarbon liquid fuel is all higher, and automatic gasifying must gasify by gasification installation at normal temperatures.Existing gasification installation such as electrothermal gasification installation exist energy consumption height, shortcoming that gas production is low, cause the combustion gas cost up; Oxidation reinforced dose of gasification installation of lighter hydrocarbons, gasification result is better, but exists the problem serious to metallic material corrosion, makes device and pipeline shortening in service life; And lighter hydrocarbons add the air gasification device, by in the gasification post, corrugated sheet or cellular board or Bao earrings being set liquid fuel is gasified, overcome the defective of above-mentioned two kinds of devices preferably, but flow process is short because this kind gasification rod structure causes gasifying, contact area is little, and frictional resistance is little, can not make the liquid lighter hydrocarbons reach sufficient gasification, gasification result was poorer when particularly temperature was low in the winter time, thereby had influenced the quality and the combustion efficiency of combustion gas.
The purpose of this utility model is to provide a kind of liquid fuel normal temperature gasification installation, this kind gasification installation can increase the flow process of liquid gasification, and gasification result is good, the gasification cost is low to reach, the service life of extension fixture and pipeline, improve the purpose of combustion gas quality and combustion efficiency.
Solution of the present utility model is that liquid fuel normal temperature gasification installation comprises air compressor machine, gasification post, compensator, connecting pipe, pipe network instrument, gas transmission pipeline, it is characterized in that gasifying and be provided with screen in the post, and between every two-layer screen, the spirality Cellular Networks is set, and screen is arranged on the support ring, and support ring then is fixed on the gasification column wall.
Above-mentioned Cellular Networks is provided with 2～4 layers, and its volume is 1/2～3/4 of the gasification column volume.
Above-mentioned Cellular Networks is the stainless steel honeycomb net.
When advantage of the present utility model is to enter the gasification post by the compressed air that air compressor is carried, make the C in the gasification post
5(carbon 5) class light hydrocarbon liquid forms countless micro air bubbles, these bubbles rise when passing the spirality Cellular Networks, have compressed-air actuated light hydrocarbon liquid and form turbulent flow, be in false fluidized state, impel light hydrocarbon liquid volatilization, thereby constantly be converted into gaseous state, and mixes formation with air and have flammable light-hydrocarbon gas by liquid state, enter in the compensator, use for the user by gas transmission pipeline at last.Owing to be provided with the multi-layer honeycomb net, the gasification flow process of liquid is increased, big with the contact area of Cellular Networks, frictional resistance is big, therefore gasification is abundant, the gas production height, and gasification result is good, especially in the winter time also can gasify fully under the situation that temperature is lower, improve the quality and the combustion efficiency of combustion gas widely.Because employing compressed air gasifies, so cost is lower, and low to the Corrosion of Metallic Materials degree, correspondingly prolonged the service life of device and pipeline.
Accompanying drawing 1 is the utility model gasification rod structure schematic diagram.
Accompanying drawing 2 is the utility model gasification installation schematic diagrames.
Below in conjunction with accompanying drawing the utility model embodiment is further described.
Embodiment one: the utility model is made up of air compressor 1, gasification post 2, compensator 3, tube connector and air shooter 16 etc.Air compressor 1 adopts W-1.2/5.5 type unit, and compensator 3 volumes are 14m
3, tube connector and carrier pipe 16 adopt the fluid hose of diameter 50mm to make.The gasification post adopts 16 manganese steel to make, internal diameter 500mm, and high 1300mm, wall thickness 8mm, its volume are 0.25m
3, two ends all are provided with end socket 11.Gasification post 2 bottoms are provided with leg 4, and the gas outlet that is provided with diameter 50mm at the cylinder top takes over 10, the bottom is provided with the compressed air access tube 14 of diameter 57mm, be provided with light hydrocarbon liquid access tube 8 in one side side wall upper part, the bottom is provided with light hydrocarbon liquid discharge connection 5, its diameter is 25mm, then be respectively equipped with the level instrumentation nozzle 11,14 that diameter is 20mm at the another side sidewall, and diameter is the hand hole 13 of 150mm.Be provided with four layers of screen 6 in the gasification post 2, screen 6 is shelved on the support ring 9, and evenly and loosely is filled with three layers of stainless steel cloth between every two-layer screen, and its weight is 35kg, and shared volume is 0.15m in post
3This device is to move every day 3～5 times, and 6～15 minutes meters of each run then can produce 400～900m every day
3Light-hydrocarbon gas use for the user.
Embodiment two: air compressor 1 adopts W-3/15 type unit, and compensator 3 volumes are 16m
3, tube connector and carrier pipe 16 adopt the fluid hose of diameter 100mm to make, gasification post 2 internal diameter 500mm, and high 1600mm, wall thickness 8mm, its volume are 0.35m
3, screen 6 still is provided with four layers, and the weight of the stainless steel cloth 7 that is provided with between screen is 41kg, and shared volume is 0.21m in post
3This device is to move every day 3～5 times, and 12～30 minutes meters of each run then can produce light-hydrocarbon gas 2000～4500m every day
3Flowing to the user through pipeline uses.
Claims (3)
1, a kind of liquid fuel normal temperature gasification installation, comprise air compressor machine, gasification post, compensator, connecting pipe, pipe network instrument, gas transmission pipeline, it is characterized in that gasifying and be provided with screen in the post, and between every two-layer screen, the spirality Cellular Networks is set, and screen is arranged on the support ring, and support ring then is fixed on the gasification column wall.
2, liquid fuel normal temperature gasification installation according to claim 1 is characterized in that described Cellular Networks is provided with 2～4 layers, and its volume is 1/2～3/4 of the gasification column volume.
3, liquid fuel normal temperature gasification installation according to claim 1 is characterized in that described Cellular Networks is the stainless steel honeycomb net.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00259889 CN2456037Y (en) | 2000-12-19 | 2000-12-19 | Liquid fuel gasifier at atmosphere |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00259889 CN2456037Y (en) | 2000-12-19 | 2000-12-19 | Liquid fuel gasifier at atmosphere |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2456037Y true CN2456037Y (en) | 2001-10-24 |
Family
ID=33615806
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00259889 Expired - Fee Related CN2456037Y (en) | 2000-12-19 | 2000-12-19 | Liquid fuel gasifier at atmosphere |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2456037Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100429458C (en) * | 2005-07-05 | 2008-10-29 | 吴世苏 | Jet absorption type pressure-less gasoline gasification generator containing rectification device |
-
2000
- 2000-12-19 CN CN 00259889 patent/CN2456037Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100429458C (en) * | 2005-07-05 | 2008-10-29 | 吴世苏 | Jet absorption type pressure-less gasoline gasification generator containing rectification device |
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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 |