CN101539301A - Liquid light hydrocarbon vaporizing device - Google Patents
Liquid light hydrocarbon vaporizing device Download PDFInfo
- Publication number
- CN101539301A CN101539301A CN200910031145A CN200910031145A CN101539301A CN 101539301 A CN101539301 A CN 101539301A CN 200910031145 A CN200910031145 A CN 200910031145A CN 200910031145 A CN200910031145 A CN 200910031145A CN 101539301 A CN101539301 A CN 101539301A
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- China
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- light hydrocarbon
- liquid light
- tank body
- vaporizing device
- vaporization
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Abstract
The invention discloses a liquid light hydrocarbon vaporizing device which has the advantages of fast heat exchange and remarkably improved vaporization efficiency and comprises a can body. The upper part of the can body is provided with an oil inlet and a plurality of gas outlets. The bottom of the can body is provided with a heating device. At least one hollow vaporization disk communicated with a gas through pipe is arranged in the can body. The periphery wall of the vaporization disk is respectively provided with a plurality of though holes. The vaporization disk is communicated with at least one gas extraction pump through the gas through pipe which is respectively provided with check valves. The invention is applicable to places for gas supply.
Description
Technical field
The present invention relates to a kind of is the liquid light hydrocarbon vaporizing device that raw material is produced the lighter hydrocarbons air mixture with the liquid light hydrocarbon.
Background technology
At present, liquid light hydrocarbon vaporizing device is one of capital equipment in the lighter hydrocarbons air mixture air supply system, Chinese patent CN201069046Y, June 4 2008 Granted publication day, denomination of invention is: a kind of liquid light hydrocarbon bump formatting carburettor, a kind of liquid light hydrocarbon bump formatting carburettor is disclosed in this Granted publication, this carburetor structure is: comprise horizontal tank body, be installed with two dividing plates in the horizontal tank body inside of horizontal tank body is separated into three cavitys, be respectively the raw material chamber, vaporization chamber and surplus sap cavity, the raw material chamber is installed with the gas phase pipe, oil-in and flowline, vaporization chamber is installed with air hose, fuel feed pump and thermometric are taken over, the bottom of vaporization chamber is installed with laminal air puck of being of several through holes that distributing, the terminal mouth of pipe of air hose places the below of air puck, surplus sap cavity is installed with oil pick-up tube and overflow pipe, be connectivity structure between the top of vaporization chamber and surplus sap cavity, vaporization chamber or surplus sap cavity are installed with the gas outlet pipe, the middle part and the bottom of the corresponding vaporization chamber of horizontal tank external body position are the double-decker that is closed state, be installed with water inlet pipe and outlet pipe in double-deck outside, water inlet pipe and outlet pipe are communicated with the closed inner chamber that double-decker is surrounded, the liquid light hydrocarbon bump formatting carburettor of said structure is simple in structure, the process of liquid light hydrocarbon vaporization is the process of a heat absorption, this just makes the temperature of liquid light hydrocarbon to reduce, the liquid light hydrocarbon at liquid level place is especially obvious, in order to replenish the heat that is absorbed, just need in double-decker, feed hot water, hot water is given liquid lighter hydrocarbons with energy supplement, but because the obstruction of air puck, on the air puck, heat exchange between the liquid light hydrocarbon of following both sides is very slow, efficient is low, has finally influenced the vaporization effect of liquid light hydrocarbon.
Summary of the invention
The object of the present invention is to provide the liquid light hydrocarbon vaporizing device that a kind of heat exchange is fast, vaporization efficency obviously improves.
Further purpose of the present invention is to provide a kind of heater to be convenient to the accurately liquid light hydrocarbon vaporizing device of control.
For realizing purpose of the present invention, a kind of liquid light hydrocarbon vaporizing device, comprise tank body, the top of tank body is provided with oil-in and several gas outlets, the bottom of described tank body is provided with heater, is provided with a hollow gasifying disk that is connected with breather pipe in the described tank body at least, is respectively arranged with several through holes on the perisporium of gasifying disk, gasifying disk is connected with at least one aspiration pump by breather pipe, is respectively arranged with check-valves on the breather pipe;
For realizing further purpose of the present invention, a kind of liquid light hydrocarbon vaporizing device, the structure of described heater is: comprise the water tank that combines with tank base, be provided with electric heater and temperature sensor in the water tank, temperature sensor links to each other with heating control apparatus, and the other end of heating control apparatus links to each other with electric heater.
The invention has the beneficial effects as follows: heat transmit fast, vaporization effect is good, the gaseous state Light hydrocarbon burner after the vaporization is steady.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Fig. 2 is the left view of Fig. 1;
Fig. 3 is the connection layout of gasifying disk and breather pipe.
Among the figure: 1, tank body, 2, oil-in, 3, the gas outlet, 4, water tank, 5, water inlet, 6, delivery port, 7, electric heater, 8, temperature sensor, 9, left spout hole, 10, right spout hole, 11, breather pipe, 12, gasifying disk, 13, through hole, 14, aspiration pump, 15, check-valves, 16, oil-out.
The specific embodiment
Below in conjunction with accompanying drawing, the structure and the operation principle of liquid light hydrocarbon vaporizing device of the present invention is described in further detail.
As Fig. 1, shown in 2 and 3, comprise tank body 1, the top of tank body 1 is provided with oil-in 2 and three gas outlets 3, the quantity of gas outlet 3 can set up on their own according to demand, the bottom of tank body 1 is provided with heater, the structure of heater is: comprise the water tank 4 that combines with tank body 1 bottom, water tank 4 is provided with water inlet 5 and delivery port 6, be provided with electric heater 7 and temperature sensor 8 in the water tank 4, temperature sensor 8 links to each other with heating control apparatus (not drawing among the figure), the other end of heating control apparatus links to each other with electric heater 7, the effect of temperature sensor 8 is: measure the water temperature in the water tank 4, and signal is passed to heating control apparatus, heating control apparatus control electric heater 7 work then, accurately the water temperature in the water tank 4 is controlled at about 30 ℃, because the liquid light hydrocarbon vaporization effect about 30 ℃ is best.For the water that makes injection is full of whole water tank 4, make the heat of water in the water tank 4 and tank body 1 transmit contact area and reach maximum, be respectively arranged with spout hole in the both sides, top of water tank 4---left spout hole 9, right spout hole 10.Be provided with three hollow gasifying disks 12 that are connected with corresponding breather pipe 11 separately in tank body 1, gasifying disk 12 can be designed to square ring-type, circular or cylindrical shape etc., and it is fixed that its concrete quantity can be come according to vaporization efficency.Be respectively arranged with several through holes 13 on the perisporium of gasifying disk 12, gasifying disk 12 links to each other with each self-corresponding aspiration pump 14 respectively by breather pipe 11, be respectively arranged with check-valves 15 on the breather pipe 11, the effect of check-valves 15 is: when aspiration pump 14 stops to bleed, check-valves 15 cuts out, can prevent to be pushed back aspiration pump 14 under the pressure of liquid light hydrocarbon in tank body 1 in the tank body 1, cause the waste of raw material, even damage aspiration pump.For the ease of discharging excessive fuel consumption, be provided with oil-out 16 in the bottom of tank body 1.
The course of work of the present invention is: liquid light hydrocarbon is injected into the tank body 1 from oil-in 2, when injection rate be the tank body volume 2/3 the time, stop to inject, then with oil-in 2 sealings, temperature sensor 8 is measured the temperature of water in the water tank 4, when water temperature was lower than 30 ℃, electric heater 7 work kept water temperature about 30 ℃.Start aspiration pump 14, air continuously enters in the gasifying disk 12 by breather pipe 11 through aspiration pump 14, behind process gasifying disk 12, form all directions around gasifying disk 12 with bubble are sprayed, and come-up is broken behind the liquid level that breaks away from liquid light hydrocarbon in the liquid light hydrocarbon in tank body 1 then.In the bubble floating process, evaporation takes place and produce the gaseous state lighter hydrocarbons with operative liquid lighter hydrocarbons on the boundary that liquid light hydrocarbon contacts at bubble, discharge the mixture of air and gaseous state lighter hydrocarbons in the bubble after promptly breaking, break after breaking away from the liquid level of the liquid light hydrocarbon mixture of the air that discharged and gaseous state lighter hydrocarbons of a large amount of bubbles uses for the user being transported in the gas ductwork by gas outlet 3.Liquid light hydrocarbon can absorb heat in the process of vaporization, the temperature of remaining liquid lighter hydrocarbons will reduce, this moment, liquid light hydrocarbon and water tank 4 interior water will form a temperature difference, heat in the water will import the liquid light hydrocarbon of bottom through the body wall of tank body 1 into, simultaneously, bubble is when spraying around gasifying disk 12, stir liquid light hydrocarbon, quickened the heat exchange between the liquid light hydrocarbon upper and lower, make the lower liquid lighter hydrocarbons can be faster with the liquid light hydrocarbon on the heat transferred top that from water, passes over, finally make the bulk temperature of liquid light hydrocarbon remain unchanged.
Advantage of the present invention is: heat transmit fast, vaporization effect is good, the gaseous state Light hydrocarbon burner after the vaporization is steady.
Claims (6)
1, a kind of liquid light hydrocarbon vaporizing device, comprise tank body, the top of tank body is provided with oil-in and several gas outlets, it is characterized in that: the bottom of described tank body is provided with heater, at least be provided with a hollow gasifying disk that is connected with breather pipe in the described tank body, be respectively arranged with several through holes on the perisporium of gasifying disk, gasifying disk is connected with at least one aspiration pump by breather pipe, is respectively arranged with check-valves on the breather pipe.
2, liquid light hydrocarbon vaporizing device according to claim 1, it is characterized in that: the structure of described heater is: comprise the water tank that combines with tank base, be provided with electric heater and temperature sensor in the water tank, temperature sensor links to each other with heating control apparatus, and the other end of heating control apparatus links to each other with electric heater.
3, liquid light hydrocarbon vaporizing device according to claim 2 is characterized in that: described water tank is provided with water inlet and delivery port, and the top of water tank is provided with spout hole.
4, liquid light hydrocarbon vaporizing device according to claim 1 is characterized in that: the described gasifying disk circulus that is square.
5, according to claim 1 or 4 described liquid light hydrocarbon vaporizing devices, it is characterized in that: described gasifying disk links to each other with each self-corresponding aspiration pump respectively.
6, liquid light hydrocarbon vaporizing device according to claim 1 is characterized in that: described tank body is provided with oil-out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910031145A CN101539301A (en) | 2009-04-28 | 2009-04-28 | Liquid light hydrocarbon vaporizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910031145A CN101539301A (en) | 2009-04-28 | 2009-04-28 | Liquid light hydrocarbon vaporizing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101539301A true CN101539301A (en) | 2009-09-23 |
Family
ID=41122621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200910031145A Pending CN101539301A (en) | 2009-04-28 | 2009-04-28 | Liquid light hydrocarbon vaporizing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101539301A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106244271A (en) * | 2016-08-19 | 2016-12-21 | 钱维洁 | The mixed empty control system of flash distillation |
| CN106568227A (en) * | 2016-11-09 | 2017-04-19 | 安徽启东热能科技有限公司 | Gas phase evaporation refrigerating device |
| CN107631171A (en) * | 2017-10-20 | 2018-01-26 | 山东理工大学 | A kind of negative-pressure type liquefaction gas preparation technology |
| CN113842650A (en) * | 2021-10-28 | 2021-12-28 | 江苏永旺新能源科技有限公司 | Liquid light hydrocarbon gasification generating tank |
-
2009
- 2009-04-28 CN CN200910031145A patent/CN101539301A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106244271A (en) * | 2016-08-19 | 2016-12-21 | 钱维洁 | The mixed empty control system of flash distillation |
| CN106568227A (en) * | 2016-11-09 | 2017-04-19 | 安徽启东热能科技有限公司 | Gas phase evaporation refrigerating device |
| CN107631171A (en) * | 2017-10-20 | 2018-01-26 | 山东理工大学 | A kind of negative-pressure type liquefaction gas preparation technology |
| CN113842650A (en) * | 2021-10-28 | 2021-12-28 | 江苏永旺新能源科技有限公司 | Liquid light hydrocarbon gasification generating tank |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20090923 |