CN2636104Y - Light hydrocarbon gasifier - Google Patents
Light hydrocarbon gasifier Download PDFInfo
- Publication number
- CN2636104Y CN2636104Y CN 03272082 CN03272082U CN2636104Y CN 2636104 Y CN2636104 Y CN 2636104Y CN 03272082 CN03272082 CN 03272082 CN 03272082 U CN03272082 U CN 03272082U CN 2636104 Y CN2636104 Y CN 2636104Y
- Authority
- CN
- China
- Prior art keywords
- tank
- amortize
- light hydrocarbon
- surge tank
- gasifier
- 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
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Abstract
The utility model discloses a light end gasify device, which comprises a controller, a heat conducting oil tank and an electric heater in the tank. A helix pipe coil gasifier is positioned over the electric heater and inlet of the helix pipe coil is connected with a solution phrase entrance outside the tank and the outlet is connected with the lower side part of an amortize tank arranged at the center of the pipe coil; the amortize tank is also internally provided with a floating ball whose outer diameter is corresponded to the inner diameter of the amortize tank; an exhausting pipe passes through the floating ball and is communicated with gas phrase outlet at upper section of the amortize tank. The device integrates the heater, the gasifier and the amortize tank and features compact and simple structure, reliable air supply pressure, adjustable supply amount, good operation elastic, energy-saving and safety.
Description
One, technical field: the utility model relates to a kind of gasification installation of liquid fuel, is specifically related to the light hydrocarbon device.
Two, background technology: the light-hydrocarbon fuel boiling point is higher, and vapour pressure is lower, is liquid at normal temperatures, and the heat gasification around can not absorbing as liquefied gas is combustion gas.Therefore must adopt effective ways to make its gasification, could use.Domestic relevant light hydrocarbon device research aspect, existing more patent report.Patent CN2422543Y has introduced a kind of light hydrocarbon liquid fuel gasification installation, comprise material storaging tank, bubbling generating means, electric constant-temp device and gas outlet, special is also to comprise a combustion gas basin, combustion gas basin device is on fuel tank, it with the material storaging tank that is communicated with between be provided with the combustion gas filter screen, gas outlet is arranged on the top of combustion gas basin.Patent CN2367915Y has proposed a kind of light hydrocarbon fuel gasification unit.This unit has housing, hot-air coil pipe, hot water heat cycles device, vaporizer.The hot-air coil device is in housing, and the aperture with a plurality of jets of heated air.The used for air compressor hot-air duct that is located on the housing links to each other with the hot-air coil pipe by electric heater.Patent CN1247890A has introduced a kind of C
5The Gas Pipe generation systems and the using method thereof of class light-hydrocarbon fuel, this system is mainly by the manometric gasification tank of charged node, fuel system, compressed air system, heating system and venturi induction tunnel, the manometric mixed pressure jar of charged node and controller for electric consumption are formed, by the work of controller for electric consumption control system with close.Common characteristic of above Patent equipment is all to be provided with compressed air system, promotes light hydrocarbon by bubbling.This gasification mode has its weak point, because light-hydrocarbon fuel is a multicomponent mixture, lighter hydrocarbons all change at any time with the ratio of air, so just can not guarantee the stable of heat vale of mixture.Patent CN2367900Y has introduced a kind of light hydrocarbon fuel combustion device, it is characterized in that light-hydrocarbon fuel is gasified by post bake through the gasification pot that the fuel of electric preheating laggard promoting the circulation of qiization enters in the combustion head again, when temperature reaches 90-100 ℃, but ignition, this moment, two electric heating bodies stopped heating, and fuel can continue gasification by flame in the tube, reaches stable burning.But gasification pot places the combustion head hot environment for a long time, ties the charcoal green coke easily.Patent CN2327685Y has introduced a kind of light hydrocarbon oil dynamic heat gasification installation, be made up of gasification tank A, gasification tank B, gas phase cross over pipe, UNICOM's overflow pipe, backflow overflow pipe, electrothermal tube, liquid level gauge and contact force table, whole gas generation process is heating and gasifying in dynamically.But this device directly places liquid fuel with electrothermal tube, has major hidden danger on safety.
Three, summary of the invention: technical problem to be solved in the utility model provides a kind of lighter hydrocarbons simple and compact for structure for raw material that utilize, and aerogenesis is reliable and stable, the adjustable light hydrocarbon device of amount of vaporization.
For solving the art technical problem, the technical scheme that the utility model light hydrocarbon device is adopted is: it comprises electric heater in controller, heat conduction fuel tank and the case, above electric heater, be provided with helical disk tubular type gasifier, the import of this spiral coil is connected with case liquid phase inlet outward, outlet is connected with the surge tank following side that is located at the coil pipe central part, also be provided with a ball float in the surge tank, the external diameter of ball float is suitable with the internal diameter of surge tank, and escape pipe passes ball float and leads to the gaseous phase outlet on surge tank top.
The bottom of above-mentioned surge tank also connects a liquid phase delivery pipe.
For reducing heat loss, outside above-mentioned heat conduction fuel tank, also be provided with heat-insulation layer.
Technique scheme adopts electric heater heating conduction oil, and conduction oil makes light hydrocarbon in the spiral coil, and gas enters surge tank, enters combustion system again, and current collection heater, gasifier, surge tank are simple and compact for structure in one.Special is to make gaseous-pressure stable by the motion of the ball float in the surge tank, and ball float also can prevent that liquid fuel from entering combustion system, avoids accident when heating control system is malfunctioning simultaneously.
The utility model effect be embodied in following some:
1, because without the air compressor and the conduction oil circulatory system, so cost is lower than existing gasification installation.
2, because compact conformation has reduced heat radiation, so the gasification energy consumption is lower than existing gasification installation.
3, because this gasification installation is the integrated design, so volume is little, floor space is little, and is easy to use.
4, this device supply gas pressure is stable, and air demand is adjustable, and operating flexibility is good.
5, owing to having avoided the use air, without the conduction oil circulatory system, so security greatly improves as gasifying medium.
The utility model is applicable to pottery, the various kiln liquid fuel gasifications of metallurgy industry, also is applicable to the liquid fuel gasification in places such as hotel, restaurant.
Four, description of drawings: Fig. 1 is the utility model light hydrocarbon apparatus structure schematic diagram.
Five, the specific embodiment: as seen from Figure 1, the utility model light hydrocarbon device comprises heat conduction fuel tank 1, electric heater 2 is installed in the case, one helical disk tubular type gasifier 3 is installed in the case above electric heater 2, the import of spiral coil is connected with the liquid fuel inlet pipe, outlet is connected with surge tank 4 following sides that are located at the coil pipe central part, be provided with ball float 5 in the surge tank 4, the internal diameter of the external diameter of ball float 5 and surge tank 4 is suitable, for movingly, escape pipe 6 passes the gaseous phase outlet that ball float 5 leads to surge tank 4 tops, and gaseous phase outlet is connected with gas pipeline, and safety valve 7 and Pressure gauge 8 are installed on the gas pipeline.Connect a liquid phase delivery pipe 9 in surge tank 4 bottoms, heat conduction fuel tank 1 is installed on the framework 10, and the case top is provided with conduction oil and adds inlet 11, is provided with conduction oil floss hole 12 at the bottom of the case, and case also is provided with thermometer 13 and conduction oil liquid level gauge 14 outward.For reducing heat radiation, heat conduction fuel tank 1 outer wall also is provided with heat-insulation layer 15, and heat-insulation layer 15 is outer fixing with shell 16 again.Thermometer 13 is connected with controller 17 leads with electric heater 2.
Claims (4)
1, a kind of light hydrocarbon device, comprise electric heater, gasifier in controller, heat conduction fuel tank and the case, it is characterized in that: be provided with helical disk tubular type gasifier (3) in said electric heater (2) top, the import of this spiral coil is connected with case liquid phase inlet outward, outlet is connected with the surge tank that is located at the coil pipe central part (4) following side, also be provided with a ball float (5) in the surge tank (4), the internal diameter of the external diameter of ball float (5) and surge tank (4) is suitable, the gaseous phase outlet that escape pipe (6) passes ball float (5) and leads to surge tank (4) top.
2, according to the said light hydrocarbon device of claim 1, it is characterized in that: the bottom of said surge tank (4) connects a liquid phase delivery pipe (9).
3, according to the said light hydrocarbon device of claim 1, it is characterized in that: outside said heat conduction fuel tank (1), also be provided with heat-insulation layer (15).
4, according to the said light hydrocarbon device of claim 1, it is characterized in that: said controller (17) is installed on the shell (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03272082 CN2636104Y (en) | 2003-06-20 | 2003-06-20 | Light hydrocarbon gasifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03272082 CN2636104Y (en) | 2003-06-20 | 2003-06-20 | Light hydrocarbon gasifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2636104Y true CN2636104Y (en) | 2004-08-25 |
Family
ID=34300974
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03272082 Expired - Fee Related CN2636104Y (en) | 2003-06-20 | 2003-06-20 | Light hydrocarbon gasifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2636104Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102062294A (en) * | 2010-11-02 | 2011-05-18 | 湖南万通达燃气技术有限公司 | Light hydrocarbon gas supply station with performance of safe and continuous production |
| CN104214791A (en) * | 2014-06-16 | 2014-12-17 | 汤伟荣 | Methanol gasifying machine and methanol gasifying method |
| CN104950055A (en) * | 2015-03-30 | 2015-09-30 | 常州磐诺仪器有限公司 | Online gasification device |
| CN105107433A (en) * | 2015-08-28 | 2015-12-02 | 徐振良 | High-energy air-light hydrocarbon mixed fuel gas reaction kettle |
-
2003
- 2003-06-20 CN CN 03272082 patent/CN2636104Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102062294A (en) * | 2010-11-02 | 2011-05-18 | 湖南万通达燃气技术有限公司 | Light hydrocarbon gas supply station with performance of safe and continuous production |
| CN102062294B (en) * | 2010-11-02 | 2012-11-07 | 湖南万通达燃气技术有限公司 | Light hydrocarbon gas supply station with performance of safe and continuous production |
| CN104214791A (en) * | 2014-06-16 | 2014-12-17 | 汤伟荣 | Methanol gasifying machine and methanol gasifying method |
| CN104214791B (en) * | 2014-06-16 | 2016-07-20 | 汤伟荣 | Methanol gasifying machine and methanol gasifying method |
| CN104950055A (en) * | 2015-03-30 | 2015-09-30 | 常州磐诺仪器有限公司 | Online gasification device |
| CN105107433A (en) * | 2015-08-28 | 2015-12-02 | 徐振良 | High-energy air-light hydrocarbon mixed fuel gas reaction kettle |
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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 |