CN2421537Y - Accelerating volatilizing device for liquid oil - Google Patents
Accelerating volatilizing device for liquid oil Download PDFInfo
- Publication number
- CN2421537Y CN2421537Y CN 00205011 CN00205011U CN2421537Y CN 2421537 Y CN2421537 Y CN 2421537Y CN 00205011 CN00205011 CN 00205011 CN 00205011 U CN00205011 U CN 00205011U CN 2421537 Y CN2421537 Y CN 2421537Y
- Authority
- CN
- China
- Prior art keywords
- oil product
- vessel shell
- liquid oil
- liquid
- blast pipe
- 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
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 70
- 238000002309 gasification Methods 0.000 claims abstract description 22
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 230000000694 effects Effects 0.000 claims abstract description 14
- 238000005096 rolling process Methods 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims abstract description 3
- 238000001035 drying Methods 0.000 claims description 13
- 230000008676 import Effects 0.000 claims description 8
- 239000000446 fuel Substances 0.000 claims description 7
- 230000003116 impacting effect Effects 0.000 claims description 5
- 239000000428 dust Substances 0.000 claims description 3
- 239000012535 impurity Substances 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 239000008236 heating water Substances 0.000 claims description 2
- 230000002787 reinforcement Effects 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 abstract description 10
- 238000005192 partition Methods 0.000 abstract 2
- 230000000903 blocking effect Effects 0.000 abstract 1
- 238000009413 insulation Methods 0.000 abstract 1
- 239000002893 slag Substances 0.000 abstract 1
- 239000012530 fluid Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000001133 acceleration Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to a liquid oil product volatilizer which is arranged in a casing container which is in a sealed and insulation state, and an air inlet pipe, a heating tank, a liquid level measuring pipe, a pressure gauge, an oil filling pipe, a slag discharging mouth, a plurality of layers of partition nets and an exhaust pipe are arranged. The dry and hot air enters the air inlet pipe and is guided into the casing container, liquid oil product which is contained in the casing container generates rolling bubbles, the volatility is accelerated, the heat energy is conducted to the liquid oil product by the heating tank, the speed of volatilization is accelerated, and the liquid oil product is blocked by a plurality of layers of partition nets and is spilled by the exhaust pipe. The function of mutual blocking impact is provided, the effects of volatilization and gasification are reinforced, the gasified oil product is evenly discharged by the exhaust pipe, and the purposes of complete volatilization and combustion are achieved.
Description
The utility model relates to a kind of liquid oil product and quickens volatilizer, is meant the application heated drying air especially, produces the rolling bubble with the liquid towards oil product, and the liquid oil product that quickens its volatilization gasification result quickens volatilizer.
Usually, with liquid oil product (as alcohol, kerosene ... Deng) be the combustion system of object, prior art is that the stamen heart is drawn liquid oil product, the stamen heart that liquid oil product is drawn in suction is lighted and is burnt again.But with this kind combustion system, draw liquid oil product, in combustion process, also be difficult for fully to its burning because of being difficult for inhaling fully, and have unburned waste gas generation completely, suck virtually in the human body, the accident that can damage takes place, and limited burning resource also causes meaningless waste.
The utility model is to utilize heated drying air that the liquid oil product of splendid attire in the vessel shell is produced the rolling bubble, quickens the oil product that it converts the volatilization gasification to, discharges via blast pipe, to reach the volatilization complete combustion effect again.This is a basic theory of the present utility model.
In the preliminary theory of the utility model in theory, design concrete composed component, so that the utility model reaches the efficient of high volatilization.For example in vessel shell, install heating tank and multilayer filter; By heating tank liquid towards oil product conduction heat energy, make it accelerate the speed of volatilization; And this multilayer filter intercepts liquid oil product and is overflowed by blast pipe, and intercepts the effect of impacting mutually, and tool is strengthened the effect of volatilization gasification.
In addition, airstream deflector (pneumatic fan) is set in air inlet pipe and blast pipe, can improves the efficient that air imports and the gasification oil product is discharged; And at the air inlet pipe of vessel shell inner bottom part and the blast pipe at top, be parallel corresponding and equidistant length, and each has a plurality of little air-vents in the outer rim place, when making liquid oil product convert the oil product of gasification to, linearly the counterparty reaches uniform volatilization characteristic completely to being discharged by blast pipe in uniform way.
Above-mentioned heating tank and heated drying air be liquid towards oil product conduction heat energy all, makes its quickening evaporation rate, and so the temperature that both heated needs control to be set in and is preceding topic under the liquid oil product burning-point, makes the utility model have more safe usability.
Main purpose of the present utility model is to propose a kind of liquid oil product to quicken volatilizer, improving the problem of liquid oil product incomplete combustion, and makes liquid oil product utilize air to quicken its volatility, and then reaches the complete effect of combustion of volatilization.
Secondary objective of the present utility model is quickened volatilizer for a kind of liquid oil product is provided, and can make liquid oil product quicken the volatilization gasification, makes it reach the peak efficiency of volatilization completing combustion.
The purpose of this utility model is achieved in that a kind of liquid oil product quickens volatilizer, it is characterized in that being in the vessel shell that seals keeping warm mode installing air inlet pipe, heating tank, liquid level gauge line, Pressure gauge, oil fuel tube, slag-drip opening, multilayer filter and blast pipe one; This air inlet pipe extends to the vessel shell inner bottom part by the vessel shell outside and is " L " type body; This heating tank tool one inlet and outlet, and configuration heater for heating water temperature conduction heat energy liquid oil product to the vessel shell, are accelerated the speed of its volatilization; This multilayer filter is made up of the individual layer filter screen of the multiple pore of plural pieces tool, is overflowed by blast pipe as intercepting liquid oil product, and intercepts the effect of impacting mutually, has the Volatile Gas of reinforcement voltinism; This blast pipe is to extend to the vessel shell inner top by the vessel shell outside to be " L " type body; The mat heated drying air imports in the vessel shell in air inlet pipe, makes the liquid oil product of splendid attire in vessel shell produce the rolling bubble and quickens its volatility, converts the oil product of gasification to, is discharged by blast pipe.Wherein the air inlet pipe of the bottom in the vessel shell and the blast pipe at top are parallel corresponding and equidistant length, and each has a plurality of little air-vents in the outer rim place, the oil product that makes gasification linearly the counterparty to discharging by blast pipe in uniform way.Wherein air inlet pipe and blast pipe respectively are provided with airstream deflector and control valve in the pipe of vessel shell outside, and air imports and the gasification oil product is discharged to quicken, and reaches gas pressure in the Synchronization Control adjustment vessel shell.Wherein the liquid oil product of oil fuel tube supply enters in the vessel shell, by in the ball float that is provided with in vessel shell control flow assembly and the liquid level gauge line liquid level detector being set, for once, the supply of secondary safety controls liquid oil product and enters in the vessel shell and cut off oil product make-up system power supply.Wherein slag-drip opening is to place the vessel shell bottom, also can be used as oil drain out, and is provided with filter screen, makes the contained band of liquid oil product and heated drying air be deposited in the impurity and the dust of bottom, is convenient to collect and gets rid of.
In sum, the utlity model has following effect: the utility model is owing to be provided with heating tank and filter screen in vessel shell, can make the fluid oil heating and accelerate vaporization rate, in air inlet pipe and blast pipe, be provided with airstream deflector, quickened the process that fluid oil converts gaseous state oil to, therefore make fluid oil vaporize fully and burn, improved the use value on its industry, reduced pollution atmosphere.
Figure 1 shows that the plane of the utility model embodiment.
Figure 2 shows that the motion flow schematic plan view of the utility model embodiment.
Figure 3 shows that the plane of another preferred embodiment of the utility model.
The utility model is described in further detail with embodiment below in conjunction with accompanying drawing:
See also Figure 1 and Figure 2, the utility model is to be in the vessel shell 1 that seals keeping warm mode one, installing air inlet pipe 11, heating tank 12, liquid level gauge line 13, Pressure gauge 14, oil fuel tube 15, slag-drip opening 16, multilayer filter 17 and blast pipe 18; Wherein air inlet pipe 11 extends to vessel shell 1 inner bottom part by vessel shell 1 outside, is one " L " type body; This heating tank 12 be set in the bottom, tool one inlet 121 and outlet 122, and dispose a heater 2 for water or the air in the heat tracing heating tank 12, and are set under liquid oil product 3 burning-points temperature control of water or air; This liquid level gauge line 13 be set in vessel shell 1 left side, the capacity of its pipe flange tool scale metering fluid oil product 3, and liquid level detector 131 is set in pipe detects for the highest upper safety limit of splendid attire liquid state oil product 3 in the vessel shell 1; This Pressure gauge 14 is to be arranged in vessel shell 1 top, for the pressure state in the caution vessel shell 1, as the flow foundation of regulating heated drying air; This oil fuel tube 15 is to be arranged at middle section, vessel shell 1 right side, feed flow attitude oil product 3 is in this injects vessel shell 1, and configuration ball float control flow assembly 4 controls in vessel shell 1 as the liquid oil product 3 of automatic supply, if it is malfunctioning that ball float control flow assembly 4 is controlled, this liquid oil product 3 that injects in the vessel shell 1 also can cut off oil product make-up system power supply by aforesaid liquid level detector 131, as secondary safety supply safeguard measure: this slag-drip opening 16 is to place vessel shell 1 bottom, also can be used as oil drain out, and be provided with filter screen 161, as impurity and the dust that the liquid oil product 3 that injects and the contained band of heated drying air are deposited in vessel shell 1 bottom, be convenient to collect be excluded in outside; This multilayer filter 17 is set middle sections in vessel shell 1, is made up of the individual layer filter screen 171 of the multiple pore of multi-disc tool, is overflowed by blast pipe 18 as intercepting liquid oil product 3, and intercepts the effect of impacting mutually, has the effect of strengthening the volatilization gasification; This blast pipe 18 is to extend to vessel shell 1 inner top by vessel shell 1 outside, is one " L " type body.
Aforesaid air inlet pipe 11 and blast pipe 18, each in vessel shell 1 outer setting airstream deflector 5 (pneumatic fan) and control valve 6 in pipe, can improve the efficient that air imports and the gasification oil product is discharged, and the entering variable that makes air is can be according to the demand of balance, regulate via two control valves, 6 Synchronization Control, satisfy gas pressure balancing condition in the vessel shell 1; Moreover, this places the air inlet pipe 11 of vessel shell 1 inner bottom part and the blast pipe 18 at top, be parallel corresponding and equidistant length, and each has a plurality of little air-vents 7 in the outer rim place, so that liquid oil product 3 converts the oil product of gasification to, linearly the counterparty reaches uniform volatilization characteristic completely to being discharged by blast pipe 18 in uniform way.
See also shown in Figure 2ly, be the motion flow schematic diagram of the utility model embodiment.Wherein this air inlet pipe 11 infeeds heated drying air by air compressor and enters in the pipe, import in the vessel shell 1 fast through airstream deflector 5, liquid oil product 3 is through the 4 control supplies of ball float control flow assembly, enter vessel shell 1 by oil fuel tube 15, liquid level gauge line 13 can show the capacity of the liquid oil product 3 of splendid attire in its vessel shell 1, this moment, heated drying air was entered in the vessel shell 1 by the little air-vent 7 of air inlet pipe 11, make liquid oil product 3 produce the rolling bubble, quicken its volatility, heating tank 12 injection water or air through the bottom heated by heater 2 again, make the water of heating or air transmitted heat energy to liquid oil product 3, accelerate the speed of volatilization, and bubble that rolls and liquid oil product 3 intercept through multilayer filter 17, prevent that liquid oil product 3 from being overflowed by blast pipe 18, and intercept the effect of impacting mutually, tool is strengthened the effect of volatilization gasification, the oil product that converts gasification at last to is entered in the pipe by the little air-vent 7 of blast pipe 18 in uniform way, discharges the oil product that gasifies completely that volatilizees fast by airstream deflector 5 again.
The utility model utilizes heated drying air that the liquid oil product 3 of splendid attire in the vessel shell 1 is produced the rolling bubble, quicken the oil product that it converts the volatilization gasification to, discharge via blast pipe 18 again, to reach the oil product form of volatilization completing combustion, also extendible peripheral equipment, set igniter 8 in the outlet of blast pipe 18 outermost end, the oil product of some gasification makes the utensil that becomes a kind of heating.
See also shown in Figure 3, be another embodiment of the present utility model, wherein this blast pipe 18 extends to another again and organizes in the small-sized acceleration volatilizer, the liquid oil product 3 that becomes a primary-secondary type quickens volatilizer, heated drying air imports in the large-scale acceleration volatilizer, makes liquid oil product 3 convert the oil product of gasification to, is entered in the small-sized acceleration volatilizer by blast pipe 18, increase the effect of its volatilization gasification again, to reach the effect of the more completing combustion of volatilizing.
Claims (5)
1. a liquid oil product quickens volatilizer, it is characterized in that being in the vessel shell that seals keeping warm mode one installing air inlet pipe, heating tank, liquid level gauge line, Pressure gauge, oil fuel tube, slag-drip opening, multilayer filter and blast pipe; This air inlet pipe extends to the vessel shell inner bottom part by the vessel shell outside and is " L " type body; This heating tank tool one inlet and outlet, and configuration heater for heating water temperature conduction heat energy liquid oil product to the vessel shell, are accelerated the speed of its volatilization; This multilayer filter is made up of the individual layer filter screen of the multiple pore of plural pieces tool, is overflowed by blast pipe as intercepting liquid oil product, and intercepts the effect of impacting mutually, has the Volatile Gas of reinforcement voltinism; This blast pipe is to extend to the vessel shell inner top by the vessel shell outside to be " L " type body; The mat heated drying air imports in the vessel shell in air inlet pipe, makes the liquid oil product of splendid attire in vessel shell produce the rolling bubble and quickens its volatility, converts the oil product of gasification to, is discharged by blast pipe.
2. liquid oil product as claimed in claim 1 quickens volatilizer, it is characterized in that: the air inlet pipe of the bottom in the vessel shell and the blast pipe at top, be parallel corresponding and equidistant length, and each has a plurality of little air-vents in the outer rim place, the oil product that makes gasification linearly the counterparty to discharging by blast pipe in uniform way.
3. liquid oil product as claimed in claim 1 quickens volatilizer, it is characterized in that: each is provided with airstream deflector and control valve air inlet pipe and blast pipe in the pipe of vessel shell outside, air imports and the gasification oil product is discharged to quicken, and gas pressure in the Synchronization Control adjustment vessel shell.
4. liquid oil product as claimed in claim 1 quickens volatilizer, it is characterized in that: the liquid oil product of oil fuel tube supply enters in the vessel shell, by in the ball float that is provided with in vessel shell control flow assembly and the liquid level gauge line liquid level detector being set, for once, the supply of secondary safety controls liquid oil product and enters in the vessel shell and cut off oil product make-up system power supply.
5. liquid oil product as claimed in claim 1 quickens volatilizer, it is characterized in that: slag-drip opening is to place the vessel shell bottom, also can be used as oil drain out, and is provided with filter screen, make the contained band of liquid oil product and heated drying air be deposited in the impurity and the dust of bottom, be convenient to collect and get rid of.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00205011 CN2421537Y (en) | 2000-03-16 | 2000-03-16 | Accelerating volatilizing device for liquid oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00205011 CN2421537Y (en) | 2000-03-16 | 2000-03-16 | Accelerating volatilizing device for liquid oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2421537Y true CN2421537Y (en) | 2001-02-28 |
Family
ID=33573260
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00205011 Expired - Fee Related CN2421537Y (en) | 2000-03-16 | 2000-03-16 | Accelerating volatilizing device for liquid oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2421537Y (en) |
Cited By (4)
| 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 |
| CN104776443A (en) * | 2015-03-20 | 2015-07-15 | 佛山市伟华文五金机械制造有限公司 | Natural heat exchange type welding and cutting oil-gas converter |
| CN109945225A (en) * | 2019-03-13 | 2019-06-28 | 张梅 | Combustion gas generation device |
| CN116006359A (en) * | 2023-03-28 | 2023-04-25 | 北京凌空天行科技有限责任公司 | Liquid fuel tank valve control method, control system and bubble detection device |
-
2000
- 2000-03-16 CN CN 00205011 patent/CN2421537Y/en not_active Expired - Fee Related
Cited By (5)
| 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 |
| CN104776443A (en) * | 2015-03-20 | 2015-07-15 | 佛山市伟华文五金机械制造有限公司 | Natural heat exchange type welding and cutting oil-gas converter |
| CN109945225A (en) * | 2019-03-13 | 2019-06-28 | 张梅 | Combustion gas generation device |
| CN116006359A (en) * | 2023-03-28 | 2023-04-25 | 北京凌空天行科技有限责任公司 | Liquid fuel tank valve control method, control system and bubble detection device |
| CN116006359B (en) * | 2023-03-28 | 2023-07-18 | 北京凌空天行科技有限责任公司 | Liquid fuel tank valve control method, control system and bubble detection 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 |