CN2235447Y - High efficiency vaporizer for obtg. light hydrocarbon fuel oil by ambient temp. stripping method - Google Patents
High efficiency vaporizer for obtg. light hydrocarbon fuel oil by ambient temp. stripping method Download PDFInfo
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- CN2235447Y CN2235447Y CN 95229156 CN95229156U CN2235447Y CN 2235447 Y CN2235447 Y CN 2235447Y CN 95229156 CN95229156 CN 95229156 CN 95229156 U CN95229156 U CN 95229156U CN 2235447 Y CN2235447 Y CN 2235447Y
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- vaporizing
- hydrocarbon fuel
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- gas
- heating chamber
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Abstract
The utility model relates to a light hydrocarbon fuel oil vaporizer. The utility model provides a high-efficiency vaporizer for light hydrocarbon fuel oil by an ambient temp. stripping method, comprising a gas stripping vaporizing chamber, a vaporizing and heating chamber and a vaporizing tube, wherein, the gas stripping vaporizing chamber is sheathed in the vaporizing and heating chamber; a heater is arranged in the heat transfer medium of the vaporizing and heating chamber; the vaporizing tube is connected with an external compressed air source by a guide tube and arranged at the lower part of the vaporizing chamber. With the advantages of high efficiency of generating gas, low energy consumption, and simple equipment, the utility model can be used normally by users in the cold winter. Compared with the coal gas of the same volume, the gas generated by the light hydrocarbon fuel oil vaporizer has the advantages that the thermal value is high, and the operating cost is only 80% of the operating cost of the coal gas. Besides, the light hydrocarbon fuel oil is the byproduct of the oil industry and has low cost.
Description
The utility model relates to a kind of light-hydrocarbon fuel oil vapourizing unit, particularly relates to a kind of lightweight oil vapourizing unit at normal temperatures.
Light-hydrocarbon fuel oil is the byproduct in refinery and oil field, and its main component is pentane class and amylene class, and boiling point through heating, can be vaporized in 27 degree-36 degree scopes slightly, is used for daily life, can be used as the very high air mixture of calorific value and uses.At present, heating technique is mainly adopted in the vaporization of light-hydrocarbon fuel oil, but this method, energy consumption is big, and security is low, and the heating unit structure is complicated, and cost is higher.Simultaneously, the dew point height of the air mixture of generation, when ambient temperature was low, combustion gas was through the cold gas pipe line of long distance, and being easy to liquefies again causes backflow, and the user can not normally use, and influences orthobiosis and order of work.
It is a kind of not influenced by ambient temperature that the purpose of this utility model is to provide, and energy consumption is low, and is simple in structure, safe and reliable light-hydrocarbon fuel oil vapourizing unit.
The utility model is achieved in that a kind of normal temperature gas formulation light-hydrocarbon fuel innage effect vaporizer, comprise that gas is carried vaporizing chamber, vaporize heating chamber and vaporizing tube, gas is carried vaporizing chamber and is sleeved in the vaporization heating chamber, well heater is installed in the heat-transfer medium of vaporization in the heating chamber vaporizing chamber is heated, vaporizing tube communicates with extraneous compressed air source by conduit, and is installed on the bottom of vaporizing chamber.Vaporizing tube is a row or the above snakelike tubulation of a row, has breather hole or ventilative seam on the tube wall according to certain rules.The top of vaporizing chamber is equipped with air mixture outlet and relief valve connection, drain line and liquidometer are arranged at its bottom, the side is equipped with interface of the level gauge up and down, vaporization heating chamber top and bottom are separately installed with the filler and the relief outlet of heat-transfer medium, its top and bottom are respectively equipped with temperature sensor sniffing interface and electric heater interface, temperature sensor, well heater link to each other with temperature regulator and constitute the temperature closed loop automatic control device, and support bar is arranged at vaporization heating chamber bottom.
Compared with prior art, adopt the vaporization gas producing efficiency height of gas formulation, energy consumption is low, equipment is simple, and is safe and reliable, temperature automatically controlled, the most basic is the air mixture dew point height that this vaporizer produces, need not heat vaporization at normal temperatures, even in combustion gas in the winter of cold through the backflow of also can not liquefying again of the cold gas pipe line of very long distance, guarantee that the user normally uses.
Fig. 1 is the sectional structure synoptic diagram of the normal temperature gas formulation light-hydrocarbon fuel oil vaporizer that the utility model proposes;
Fig. 2 is the structural representation of snakelike shell and tube vaporizing tube in the normal temperature gas formulation light-hydrocarbon fuel oil vaporizer that the utility model proposes;
Fig. 3 is the structural representation of the snakelike shell and tube vaporizing tube of two rows.
Below in conjunction with accompanying drawing embodiment is described.
Embodiment 1, carry vaporizing chamber housing 11 by up and down two ellipse garden end sockets and end socket with the sealing vertical tank shape gas that the cylindrical shell of bore is welded, its volume can be decided according to the size of gas production rate, and vaporizing chamber 11 is sleeved in the vaporization heating chamber 6, and vaporizing tube 4 is single snakelike tubulation (specifically seeing accompanying drawing 2).The tube wall jet aperture 18 that gathers is installed in the vaporizing chamber bottom, links to each other with extraneous compressed air source by pipeline 2; Falling heat-transfer oil in the vaporization heating chamber, electric heater places thermal oil from installing port 14, temperature sensor places thermal oil by installing port 5, electric heater, temperature sensor and temperature regulator constitute the temperature closed loop automatic control device together, when external boundary envrionment temperature is low, start electric heater automatically, the heating thermal oil makes it to reach certain temperature, the latent heat that makes the vaporization of liquid light hydrocarbon fuel oil be consumed is replenished, and the temperature of keeping light-hydrocarbon fuel oil is not less than normal temperature.Liquid light hydrocarbon fuel oil 12 is injected vaporizing chamber by oil inlet pipe 10, and pressurized air enters single snakelike shell and tube vaporizing tube 4 through conduit 2, and is spouting by the aperture that gathers, and bubble enters and quickens vaporization in the light hydrocarbon oil, forms air mixture from exporting 1 output.The bottom of vaporizing chamber is equipped with evacuated tube 17 and 3,7 and is Link Port about the liquidometer, and a safety valve open holes 9 is established at its top in addition; Thermal oil can export 16 again and discharge from import 13 filling; Three feets 15,8 triangular in shape etc. are welded in bottom at the vaporization heating chamber.
Through experiment, the utility model effect is very good, even the winter of cold, user Also can normally use, the calorific value height of simultaneously air mixture is compared with the coal gas of equal volume, Can produce bigger heat energy, and expense only has 80% of coal gas, light-hydrocarbon fuel oil is oil The byproduct of industry, cheap, can produce huge economy effect by the utility model Benefit. This technology has wide prospect.
Claims (3)
1, a kind of normal temperature gas formulation light-hydrocarbon fuel innage is imitated vaporizer, comprise that gas is carried vaporizing chamber, vaporize heating chamber and vaporizing tube, feature of the present utility model is: gas is carried vaporizing chamber and is sleeved in the vaporization heating chamber, well heater be installed on the vaporization heating chamber heat-transfer medium in vaporizing chamber is heated, vaporizing tube communicates with extraneous compressed air source by conduit, and is installed on the bottom of vaporizing chamber.
2, normal temperature gas formulation light-hydrocarbon fuel vaporizer according to claim 1 is characterized in that vaporizing tube is a row or the above snakelike tubulation of a row, has breather hole or ventilative seam according to certain rules on the tube wall.
3, efficient vaporizer according to claim 1 and 2, it is characterized in that: the top of vaporizing chamber is equipped with air mixture outlet and relief valve connection, drain line is arranged at its bottom, the side is equipped with interface of the level gauge up and down, vaporization heating chamber top and bottom are separately installed with the filler and the relief outlet of heat-transfer medium, its top and bottom are respectively equipped with temperature sensing sniffing interface and electric heater interface, temperature sensor, well heater link to each other with temperature regulator and constitute the temperature closed loop automatic control device, and support bar is arranged at vaporization heating chamber bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95229156 CN2235447Y (en) | 1995-12-22 | 1995-12-22 | High efficiency vaporizer for obtg. light hydrocarbon fuel oil by ambient temp. stripping method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95229156 CN2235447Y (en) | 1995-12-22 | 1995-12-22 | High efficiency vaporizer for obtg. light hydrocarbon fuel oil by ambient temp. stripping method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2235447Y true CN2235447Y (en) | 1996-09-18 |
Family
ID=33874500
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 95229156 Expired - Fee Related CN2235447Y (en) | 1995-12-22 | 1995-12-22 | High efficiency vaporizer for obtg. light hydrocarbon fuel oil by ambient temp. stripping method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2235447Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104238520A (en) * | 2014-09-18 | 2014-12-24 | 安徽新力电业科技咨询有限责任公司 | Supercritical boiler fire coal heat value self-balance control loop distributed control system implementation method |
| CN108107162A (en) * | 2017-12-28 | 2018-06-01 | 宁夏宝塔化工中心实验室(有限公司) | A kind of immersion air lift simulation test device |
-
1995
- 1995-12-22 CN CN 95229156 patent/CN2235447Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104238520A (en) * | 2014-09-18 | 2014-12-24 | 安徽新力电业科技咨询有限责任公司 | Supercritical boiler fire coal heat value self-balance control loop distributed control system implementation method |
| CN104238520B (en) * | 2014-09-18 | 2016-09-28 | 安徽新力电业科技咨询有限责任公司 | Super critical boiler fire coal calorific value self-balancing controls loop scattered control system implementation method |
| CN108107162A (en) * | 2017-12-28 | 2018-06-01 | 宁夏宝塔化工中心实验室(有限公司) | A kind of immersion air lift simulation test 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 |