CN2791498Y - Automatic gusifying device for liquid state light hydrocarbon fuel - Google Patents
Automatic gusifying device for liquid state light hydrocarbon fuel Download PDFInfo
- Publication number
- CN2791498Y CN2791498Y CN 200520015846 CN200520015846U CN2791498Y CN 2791498 Y CN2791498 Y CN 2791498Y CN 200520015846 CN200520015846 CN 200520015846 CN 200520015846 U CN200520015846 U CN 200520015846U CN 2791498 Y CN2791498 Y CN 2791498Y
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- CN
- China
- Prior art keywords
- tank body
- pressure
- valve
- ball valve
- light hydrocarbon
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- 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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- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Feeding And Controlling Fuel (AREA)
Abstract
The utility model belongs to a liquid fuel gasifying device range, particularly an automatic gasifying device for liquid state light hydrocarbon fuel. A pressure-reducing valve and a pressure gauge are installed on an upper plane of a tank body, and an air inlet is arranged on the pressure gauge. An oil inlet pipe is communicated with the upper plane of the tank body through a ball valve, and a liquid level meter is installed at the lateral face of the tank body. A waste valve is installed at the bottom of the tank body, and an anti-leakage alarm device is communicated with the upper plane of the tank body. The device has simple structure, and has no explosion hidden trouble when working in normal temperature and pressure. The utility model is the multifunctional fuel automatic gasifying device with high safety. The heat value of gaseous light hydrocarbon can be reached by 18000 kcal, and is equivalent to 1.5 times of the liquefied gas, and energy is saved. The source of raw materials is extensive, and more than 99 percent is sufficiently burnt, and the utility model is convenient for environment protection. The utility model can all be used in industrial production, a medicine industry and a food production industry, and can also be popularized in the industries, such as a hotel, a guesthouse, a bath, a school, etc.
Description
Technical field
The utility model belongs to liquid fuel gasification device scope, particularly a kind of liquid light hydrocarbon fuel automatic gasifying device.
Background technology
Existing liquid fuel majority is a liquefied petroleum gas, and liquid gas storage pressure is big, and it is high pressure resistant, air tight that caisson requires, and structure is very complicated, and no anti-leak warning device uses dangerously, once leak, easily generation is exploded, and causes fire, has potential safety hazard.
Summary of the invention
The purpose of this utility model provides a kind of liquid light hydrocarbon fuel automatic gasifying device, by tank body, and Pressure gauge, pressure-reducing valve, liquid level gauge, ball valve and tube connector are formed, it is characterized in that: pressure-reducing valve 2 is installed on plane on the tank body 1, control pressure by air pressure table 3 is housed on the pressure-reducing valve 2; Air intake 5 is on Pressure gauge 3, air inlet ball valve 4 is installed between air intake 5 and the pressure-reducing valve 2, the pressure-reducing valve 2 of leading up to is connected with air inlet pipe 6 through tube connector 9, anti-backflow escape pipe 11 is below ball valve 24, have on anti-backflow escape pipe 11 towards what have a down dip and be not less than 45 ° venthole 23 with the horizontal line angle, aft cover plate 12 is connected with the lower end of anti-backflow escape pipe 11; Another road by tube connector 21 through being connected by tube connector 22 and the bubbling pipe flowline 14 of holding concurrently again behind the three-way valves 15, the hold concurrently opening 16 of flowline 14 of its bubbling pipe enters in the tank body lighter hydrocarbons liquid level below 20, connects ball valve 25 and oil-out 13 at the port of export of three-way valve 15; Ball valve 24 tops are gas outlet 10.Oil inlet pipe 7 is connected by the last plane of ball valve 8 and tank body 1, and liquid level gauge 18 is installed in the side of tank body 1, and waste valve 17 is contained in the bottom of tank body 1, and on tank body 1 anti-leak warning device 19 is set.
The beneficial effects of the utility model are to have automatically liquid light hydrocarbon to be converted into the mixed burning of gaseous state lighter hydrocarbons and air, also liquid light hydrocarbon directly can be extruded, and send in the automatic gasifying stove and burn.Bubble type automatic gasifying method and plunder floating automatic gasifying method both can be according to outside air temperature, conditions such as environment are used separately, also the multifunctional characteristics that can use simultaneously.Simplify the structure, and need not complex appts; Work at normal temperatures and pressures, no hidden peril of explosion, safe.Gaseous state lighter hydrocarbons and air mixed proportion only are 15%-35%, and calorific value can reach 18000 kilocalories, are equivalent to 1.5 times of liquefied gas, save the energy.Raw material sources are in the byproduct of petrochemical industry, and fully burning helps environmental protection more than 99%.In process industries such as glass, pottery, refractory materials, medicine, food production industry all can be used, in the hotel, and the hotel, bathing pool, industries such as school also can extensively be promoted.
Description of drawings
Fig. 1 is a liquid light hydrocarbon fuel automatic gasifying apparatus structure schematic diagram.
Fig. 2 is the enlarged drawing of anti-backflow escape pipe 11 in this device.
The specific embodiment
The utility model provides a kind of liquid light hydrocarbon fuel automatic gasifying device.In structure shown in Figure 1, pressure-reducing valve 2 is installed on plane on the tank body 1, control pressure by air pressure table 3 is housed on the pressure-reducing valve 2; Air intake 5 is on Pressure gauge 3, air inlet ball valve 4 is installed between air intake 5 and the pressure-reducing valve 2, the pressure-reducing valve 2 of leading up to is connected with air inlet pipe 6 through tube connector 9, anti-backflow escape pipe 11 is below ball valve 24, have on anti-backflow escape pipe 11 towards what have a down dip and be not less than 45 ° venthole 23 (as shown in Figure 2) with the horizontal line angle, aft cover plate 12 is connected with the lower end of anti-backflow escape pipe 11; Another road by tube connector 21 through being connected by tube connector 22 and the bubbling pipe flowline 14 of holding concurrently again behind the three-way valves 15, the hold concurrently opening 16 of flowline 14 of its bubbling pipe enters in the tank body lighter hydrocarbons liquid level below 20, connects ball valve 25 and oil-out 13 at the port of export of three-way valve 15; Ball valve 24 tops are gas outlet 10.Oil inlet pipe 7 is connected by the last plane of ball valve 8 and tank body 1, and liquid level gauge 18 is installed in the side of tank body 1, and waste valve 17 is contained in the bottom of tank body 1, and on tank body 1 anti-leak warning device 19 is set.Below in conjunction with accompanying drawing the utility model is illustrated.
One, plunders floating function (as Fig. 1).Pressure-reducing valve 2 is installed on plane on the tank body 1 that fills liquid light hydrocarbon, is equipped with high precision on the pressure-reducing valve 2 and can controls pressure by air pressure table 3.With external air blast air is sent into air inlet 5, the pressure that configures in advance with Pressure gauge 3 enters pressure-reducing valve 2, enters air inlet pipe 6 by pressure-reducing valve 2 through tube connector 9 again, thereby enters tank body 1.In tank body 1, plunder floating lighter hydrocarbons liquid level 20, principle according to the liquid light hydrocarbon volatilization, the gaseous state lighter hydrocarbons that can the ratio of taking up account for 15%-35%, form air accounting example 65%-85%, the gaseous state lighter hydrocarbons account for the combustible mist of 15%-35%, mist is discharged tank body by gas outlet 10 through anti-backflow escape pipe 11 under the control of ball valve 24, this mist can be used as high-grade fuel gas and supplies with converter, and the restaurant uses with various burners such as gas kitchens.
Two, bubbling function, air is sent into air inlet 5 by air blast, and air inlet ball valve 4 has the function that the control air enters.Pass through pressure-reducing valve 2 at the pressure that configures in advance with Pressure gauge 3, enter bubbling pipe 14 by tube connector 22 by tube connector 21 again through behind the three-way valve 15 again, the air of certain pressure enters in the tank body lighter hydrocarbons liquid level below 20 by the bubbling pipe flowline 14 of holding concurrently, by opening 16 (opening 16 can be a word or cross, also can be black scraper) enter liquid light hydrocarbon, in liquid light hydrocarbon, produce a large amount of bubbles, principle according to the liquid light hydrocarbon volatilization, gaseous state lighter hydrocarbons after the volatilization with jar in air mix after aft cover plate 12 enters anti-backflow escape pipe 11 again, by the control of ball valve 24,10 enter burner and burn from the gas outlet.Anti-backflow escape pipe 11 has certain thickness, have thereon a lot of down be not less than 45 ° venthole 23 with the horizontal line angle, venthole 23 is to enter anti-backflow escape pipe 11 towards the purpose that has a down dip with preventing the lighter hydrocarbons droplet that produces in the bubbling process, even the setting of venthole 23 is exactly to consider that the lighter hydrocarbons droplet enters anti-backflow escape pipe 11, also can takes advantage of a situation and in time flow back in the jar.
Three, go out functional oil, air enters air inlet 5 by external air blast, cross ball valve 4, the pressure that configures in advance with Pressure gauge 3 enters tank body 1 through pressure-reducing valve 2 again, after giving lighter hydrocarbons liquid level 20 immense pressures, liquid light hydrocarbon will be held concurrently by bubbling pipe, and (opening 16 can be a cross to flowline opening 16, it can be a word, also can be black scraper) enter the bubbling pipe flowline 14 of holding concurrently, again through tube connector 22 and three-way valve 15, under ball valve 25 controls, flow out, can enter in the burner with automatic gasifying function by conveyance conduit and burn from oil-out 13.
This device adopts above which kind of function operation all to control input liquid lighter hydrocarbons by oil inlet pipe 7 through ball valve 8, measure a jar interior lighter hydrocarbons capacity residue by liquid level gauge 18, tank body 1 inner issuable refuse all can be by outside waste valve 17 drain tanks, and anti-leak warning device 19 is set on tank body 1, the warning in case gas leakage in jar, anti-leak warning device 19 can pipe automatically.More than three kinds of functions can use simultaneously, also can be used in combination according to external condition.
Claims (1)
1. liquid light hydrocarbon fuel automatic gasifying device, by tank body, Pressure gauge, pressure-reducing valve, liquid level gauge, ball valve and tube connector are formed, it is characterized in that: pressure-reducing valve (2) is installed on the last plane of tank body (1), control pressure by air pressure table (3) is housed on the pressure-reducing valve (2); Air intake (5) is on Pressure gauge (3), air inlet ball valve (4) is installed between air intake (5) and the pressure-reducing valve (2), the pressure-reducing valve (2) of leading up to is connected with air inlet pipe (6) through tube connector (9), anti-backflow escape pipe (11) is below ball valve (24), have on anti-backflow escape pipe (11) towards what have a down dip and be not less than 45 ° venthole (23) with the horizontal line angle, aft cover plate (12) is connected with the lower end of anti-backflow escape pipe (11); Another road is connected by tube connector (22) and the bubbling pipe flowline (14) of holding concurrently again after through three-way valve (15) by tube connector (21), the hold concurrently opening (16) of flowline (14) of its bubbling pipe enters in the tank body below the lighter hydrocarbons liquid level (20), connects ball valve (25) and oil-out (13) at the port of export of three-way valve (15); Ball valve (24) top is gas outlet (10); Oil inlet pipe (7) is connected by the last plane of ball valve (8) and tank body (1), and liquid level gauge (18) is installed in the side of tank body (1), and waste valve (17) is contained in the bottom of tank body (1), and on tank body (1) anti-leak warning device (19) is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520015846 CN2791498Y (en) | 2005-04-27 | 2005-04-27 | Automatic gusifying device for liquid state light hydrocarbon fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520015846 CN2791498Y (en) | 2005-04-27 | 2005-04-27 | Automatic gusifying device for liquid state light hydrocarbon fuel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2791498Y true CN2791498Y (en) | 2006-06-28 |
Family
ID=36807564
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520015846 Expired - Fee Related CN2791498Y (en) | 2005-04-27 | 2005-04-27 | Automatic gusifying device for liquid state light hydrocarbon fuel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2791498Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101893907A (en) * | 2010-07-21 | 2010-11-24 | 湖南万通达燃气技术有限公司 | Electric control cabinet for light hydrocarbon gas supply station |
-
2005
- 2005-04-27 CN CN 200520015846 patent/CN2791498Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101893907A (en) * | 2010-07-21 | 2010-11-24 | 湖南万通达燃气技术有限公司 | Electric control cabinet for light hydrocarbon gas supply station |
| CN101893907B (en) * | 2010-07-21 | 2012-07-25 | 湖南万通达燃气技术有限公司 | Electric control cabinet for light hydrocarbon gas supply station |
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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 |