CN201885249U - Gasifier for organic solvent fuel - Google Patents
Gasifier for organic solvent fuel Download PDFInfo
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- CN201885249U CN201885249U CN2010205726731U CN201020572673U CN201885249U CN 201885249 U CN201885249 U CN 201885249U CN 2010205726731 U CN2010205726731 U CN 2010205726731U CN 201020572673 U CN201020572673 U CN 201020572673U CN 201885249 U CN201885249 U CN 201885249U
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- organic solvent
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Abstract
The utility model relates to a gasifier for organic solvent fuel, which comprises a gasification barrel, an air pump and a storage barrel. The organic solvent in the gasification barrel can be gasified into gaseous fuel, which is supplied to a combustion apparatus and used for combustion. The air pump can pump the air into the gasification barrel in order to accelerate the gasification of the organic solvent. The storage barrel can automatically supply the organic solvent in the storage barrel into the gasification barrel in time, so that the volume of the organic solvent in the gasification barrel can be kept under the optimal gasification effect. At least one inclined air bubble disintegration plate is arranged in the gasification barrel, a plurality of small holes are distributed on the air bubble disintegration plate, and the air bubble disintegration plate can cut the air supplied into the gasification barrel into a plurality of small air bubbles in order to enhance the gasification effect, so that the effect of organic solvent gasification can be enhanced.
Description
Technical field
The utility model relates to and a kind of organic solvent is gasificated into the device of fuel, and it can be gasificated into organic solvent gaseous fuel output, can in time replenish organic solvent again, makes gasification installation keep normal operation.
Background technology
Development in science and technology reaches all the more, and human dependence to the energy is just serious, so the mankind constantly tap a new source of energy, by original timber, charcoal, coal, develops into natural gas, fossil fuel, and as for now nuclear energy.More than various fuel more or less all can destroy the ecological environment of the earth or cause environmental pollution.For example: the oil field fire event in the Gulf of Mexico, seriously cause seawater pollution, influence marine organisms ecology.In addition, automobile and industrial toxic emission, the processing of nuclear energy waste material all can cause environmental pollution.Therefore, in today of paying attention to environmental protection, the exploitation of the green energy becomes one of most important problem today.
The employed fuel of stove and accessory of family and catering trade mostly is natural gas or liquefaction barreled oil gas at present.Let us not go into the question now natural gas and barreled oil gas danger in the use, only single because the rising successively of fossil fuel price just allows the user must bear the expense of great number.The rising of fossil fuel price, with day by day consuming of earth fossil fuel also be closely bound up.Therefore, seeking alternative fuel also is instant thing.
The organic solvent vaporising fuel is exactly a kind of alternative fuel.As long as suitable equipment is arranged, organic solvent just can be gasificated into fuel.Described organic solvent can be divided into three classes such as solvent of hydrocarbon solvent, oxo solvent and other classes according to its chemical composition.Wherein, serve as appropriate with hydrocarbon solvent, the oxo solvent that can not produce noxious materials such as sulphur, chlorine after the burning.
Novel M338244 number of TaiWan, China (application case number be 097202069) " organic solvent fluid gas phase conversion burn application device ", for organic solvent is used in the preceding liquid gas phase conversion equipment of burning, though it can successfully convert organic solvent to fuel gas, but its spare part is many, structure is comparatively complicated, can improve cost of manufacture.Use this another shortcoming of patent case to exist, (for example: the flame stove and accessory that cooking is used) diminishes and when need adding organic solvent, just must close fire, and be added with the work of machine solvent, extreme inconvenience uses in when the burning facility.
Summary of the invention
Main purpose of the present utility model, at the gasification installation that a kind of organic solvent fuel is provided, it has the function that can add organic solvent automatically, enables to provide constantly the organic-fuel of gaseous state.
An of the present utility model purpose, at the gasification installation that a kind of organic solvent fuel is provided, its structure is simplified, and can reduce cost of manufacture.
A purpose more of the present utility model, at the gasification installation that a kind of organic solvent fuel is provided, it is removable, form gasification bucket and storage vat, and the volume of timber of gasification installation, weight all can be dwindled, with more convenient transportation, store.
For achieving the above object, the technical solution adopted in the utility model is:
A kind of gasification installation of organic solvent fuel is characterized in that, comprising:
One gasification bucket is equipped with organic solvent in it; One side of this gasification bucket bottom is provided with an air inlet, and this gasification bucket top is provided with combustion gas delivery outlet and output pipe; This gasification bucket more is provided with an organic solvent input pipe and a gas discharger that is penetrated by its top; The bottom of this organic solvent input pipe and this gas discharger is stretched in the gasification bucket, and the bottom of this gas discharger is higher than the bottom of organic solvent input pipe;
One air pump, it is communicated with the air inlet of pipeline with this gasification bucket bucket end, can deliver air in the gasification bucket; And,
One storage vat is equipped with organic solvent in it; This storage vat comprises an organic solvent efferent duct and a gas inlet pipe is set; This organic solvent efferent duct is connected with the organic solvent input pipe of this gasification bucket, organic solvent can be transported in the gasification bucket; This gas inlet pipe is connected with the gas discharger of this gasification bucket, and the liquid level of the organic solvent in the gasification bucket stops the conveying of organic solvent when sealing the lower end mouth of pipe of gas discharger of this gasification barrel automatically.
Wherein: the mouth of pipe on the gas inlet pipe top of this storage vat is higher than the liquid level of organic solvent in the storage vat.
Wherein: be provided with a control valve in the communication path between the organic solvent input pipe of this gasification bucket and the organic solvent efferent duct of storage vat, to control the unimpeded of this communication path or to close.
Wherein: this gasification bucket is communicated with a liquid level target tube, and this liquid level target tube subscript is shown with the height of the gas discharger lower end mouth of pipe of this gasification bucket.
Wherein: this air inlet place is provided with a non-return valve, is gone in the air intake line by the air inlet adverse current to prevent organic solvent.
Wherein: be provided with the fining air bubbles plate of the skewed setting of a slice at least in this gasification bucket, lay most little perforation on this fining air bubbles plate; Wherein, a minimum side of a slice fining air bubbles plate of lowermost end is near the air inlet place.
Wherein: the distribution of plurality of small holes on this skewed fining air bubbles plate is to be laid by few cumulative kenel by low and high work.
Wherein: the fining air bubbles plate more than two is with the kenel setting of upper and lower arrangement; In any two adjacent fining air bubbles plates, be positioned at the lower corresponding higher side of fining air bubbles plate of a side of fining air bubbles plate of top near its below.
Wherein: the bottom of this gasification bucket is provided with a constent temperature heater.
Wherein: the combustion gas output pipe of this gasification bucket is provided with a non-return valve, can prevent that fuel gas return-flow from going in the gasification bucket.
Compared with prior art, adopt the advantage that the utlity model has of technique scheme to be: it has the function that can replenish organic solvent automatically, the gasification efficiency of gasification bucket is maintained under the best situation, and can under the situation that need not to open the gasification bucket, replenish organic solvent automatically, can avoid overflowing of combustion gas, security significantly improves.Reach the purpose of cutting apart bubble and bubble homogenising so that the fining air bubbles plate to be set in the gasification bucket of the present utility model, its structure is simplified, reduce cost of manufacture.Gasification of the present utility model bucket, storage vat carry with air pump is removable, and mobility is good, are an ideal and a practical design in fact.
Description of drawings
Fig. 1 is the outside drawing of the utility model embodiment;
Fig. 2 is a structural representation embodiment illustrated in fig. 1;
Fig. 3 is the 3-3 profile of Fig. 2;
Fig. 4 is the 4-4 profile of Fig. 2.
Description of reference numerals: 10-gasify the bucket; The 11-air inlet; 12-combustion gas delivery outlet; The 13-output pipe; The 131-non-return valve; The 132-pressure sensor; The 133-delivery gauge; The 134-flow control valve; 14-organic solvent input pipe; 15-gas discharger; The 151-mouth of pipe; 16-liquid level target tube; The 17-constent temperature heater; The 18-support body; The 20-air pump; The 21-pipeline; The 22-dehydrater; The 23-electromagnetic switch; The 24-non-return valve; The 30-storage vat; 31-organic solvent delivery outlet; The 32-gas inlet pipe; The 321-mouth of pipe; The 33-pipeline; The 34-pipeline; The 35-control valve; The 36-control valve; The 40-organic solvent; The 50-organic solvent; 60-fining air bubbles plate; The 61-aperture; The side that 62-is lower; The side that 63-is higher; 70-fining air bubbles plate; The 71-aperture; The side that 72-is lower; The side that 73-is higher.
The specific embodiment
The applicant is because existing organic solvent fluid gas phase conversion burn application device, have complex structure and solvent to add the problem of inconvenience, and grind the gasification installation of a kind of organic solvent fuel of wound, its structure is simplified, and the function with automatic interpolation organic solvent has more convenience in the use.Now cooperate graphicly, the utility model device is described in detail in detail and uses effect.
See also Fig. 1, Fig. 2.The gasification installation of the organic solvent fuel that the utility model disclosed, it comprises: a gasification bucket 10, one air pump 20, a storage vat 30.Wherein, the organic solvent 40 annoying gaseous fuels that change in the gasification bucket 10, and export to the usefulness that burner (for example: home-use stove and accessory, not shown on the figure) is done ignition.This air pump 20 can be sent into air in the gasification bucket 10, to quicken the gasification of organic solvent 40.This storage vat 30 is mainly in the organic solvent that it is inner 50 in time is transported to gasification bucket 10.The bottom of this gasification bucket 10 is provided with a constent temperature heater 17, with to 40 heating of the organic solvent in the gasification bucket 10, organic solvent 40 is maintained carry out gasification under the constant temperature.
This storage vat 30 is a container, its built-in organic solvent 50.This storage vat 30 comprises an organic solvent delivery outlet 31 and a gas inlet pipe 32 is set.Is connected with pipeline 33 between the organic solvent input pipe 14 of this organic solvent delivery outlet 31 and this gasification bucket 10, organic solvent 50 can be transported in the gasification barrels 10.Be connected with pipeline 34 between the gas discharger 15 of this gas inlet pipe 32 and this gasification bucket 10, make the gases in the gasification bucket 10 can be by this gas discharger 15, by the road 34 and the gas inlet pipe 32 of this storage vat 10 and entering in the storage vat 30, to give organic solvent 50 1 output pressures in the storage vat 30, organic solvent 50 in this storage vat 30 can be automatically flowed in the gasification barrels 10 along the organic solvent input pipe 14 of organic solvent delivery outlet 31, pipeline 32, gasification bucket 10.The top that this storage vat 30 is arranged on this gasification bucket 10 is preferable, and can put this storage vat 20 by support body 18 framves that be fixed on gasification bucket 10 tops.
The gas inlet pipe 32 top mouths of pipe 321 of this storage vat 30 are higher than the liquid level of organic solvents 50 in the storage vat 30, and organic solvent 50 can not flowed out in this gas inlet pipe 32.When the liquid level of the organic solvent 40 in this gasification bucket 10 seals the bottom mouth of pipe 151 of this gas discharger 15, promptly form a confined space in this storage vat 30, make the organic solvents 50 in the storage vat 30 stop conveying automatically.Therefore, as long as also have remaining organic solvent 50 in the storage vat 30, the liquid level in this gasification bucket 10 promptly can maintain the height at these gas discharger 15 bottom mouths of pipe 151 places.So the bottom mouth of pipe 151 of the gas discharger 15 of this gasification bucket 10 highly, is the peak level of organic solvent 40.
This gasification bucket 10 is communicated with a liquid level target tube 16, and these liquid level target tube 16 subscripts are shown with the height (not shown on the figure) of the gas discharger 151 lower end mouths of pipe of this gasification bucket 10.When the liquid level in the gasification bucket 10 maintains the height of these gas discharger 15 bottom mouths of pipe 151, promptly represent to have remained in the storage vat 30 organic solvent 50 and can replenish automatically in the gasification bucket 10.When the liquid level in the gasification bucket 10 is lower than the height of these gas discharger 15 bottom mouths of pipe 151, promptly represent in the storage vat 30 organic solvent-free 50, promptly should change storage vat 30.But also to indicate the lowest water level (not shown on the figure) of gasification bucket 10 normal operations on this liquid level target tube 16 certainly, allow the user can in time change storage vat 30.
On the connecting pipeline 33 between the organic solvent input pipe 14 of this gasification bucket 10 and the organic solvent delivery outlet 31 of storage vat 30 control valve 35 can be set, with the unimpeded of control piper 33 or sealing.Before not using fuel and moving gasification installation of the present utility model again, suitable first closed control valve 35 to force to stop the conveying of organic solvent 50, is carried this gasification installation again.On the connecting pipeline 34 between the gas discharger 15 of this gasification bucket 10 and the gas inlet pipe 32 of storage vat 30 control valve 36 can be set also, with the unimpeded of control piper 34 or sealing.
On the connecting line 21 between the air inlet 11 of this air pump 20 and this gasification bucket 10, be provided with a dehydrater 22, an electromagnetic switch 23 and a non-return valve 24.This non-return valve 24 can prevent that organic solvent 40 from being gone in the air intake line 21 by air inlet 11 adverse currents.This dehydrater 22 can divide filtering with water in air.But the unimpeded or sealing of these electromagnetic switch 21 control pipers 21.When the air pressure in the gasification bucket 11 reached the hyperbar value of setting, this electromagnetic switch 23 and automatic closing pipe line 21 stopped gas input.
Be provided with the skewed fining air bubbles plate 60,70 that is provided with of a slice at least in this gasification bucket 10, this bubble produces and lays most little perforation 61,71 on the plate 60,70.Wherein, a minimum side 62 of a slice fining air bubbles plate 60 of lowermost end is near air inlet 11 places.The distribution of plurality of small holes 61 on this skewed fining air bubbles plate 60, the low and high work of serving as reasons is laid by few cumulative kenel, sees Fig. 3.After in air is sent into gasification bucket 10, can by each aperture 61,71 on this fining air bubbles plate 60,70 when rising, and form most individual minute bubbles.The setting of this fining air bubbles plate 60,70 except shredding the bubble, also can allow air rest on time lengthening in the organic solvent 40, to increase the probability of molecule attached on air of organic solvent 40, to improve gasification result.This fining air bubbles plate 60,70 is adopted skewed design, is in order to make air can be covered with whole.Aperture 61,71 distribution kenels on the fining air bubbles plate 60,70 are for bubble is evenly distributed.
Fining air bubbles plate 60,70 more than two is with the kenel setting of upper and lower arrangement.The bubble that is positioned at the top in wantonly two adjacent fining air bubbles plates 60,70 produces the higher side 63 of the corresponding fining air bubbles plate 60 near its below of the lower side 72 of plate 70, so that bubble can more evenly be covered with whole.Numbering 73 microbubbles produce the higher side 73 of plate 70 among Fig. 4.
The combustion gas output pipe 13 of this gasification bucket 10 is provided with a non-return valve 131, a pressure sensor 132, a delivery gauge 133, a flow control valve 134.This non-return valve 131 can prevent that fuel gas return-flow from going in the gasification bucket 10.This flow control valve 134 can be controlled the combustion gas output quantity, further controls flame size.
To sum up institute is old, the gasification installation of organic solvent fuel provided by the utility model, it has the function that can replenish organic solvent automatically, the gasification efficiency of gasification bucket is maintained under the best situation, and can under the situation that need not to open the gasification bucket, replenish organic solvent automatically, can avoid overflowing of combustion gas, security significantly improves.Reach the purpose of cutting apart bubble and bubble homogenising so that bubble generation plate to be set in the gasification bucket of the present utility model, its structure is simplified, reduce cost of manufacture.Gasification of the present utility model bucket, storage vat carry with air pump is removable, and mobility is good, are an ideal and a practical design in fact.
More than explanation is just illustrative for the utility model; and nonrestrictive, those of ordinary skills understand, under the situation of the spirit and scope that do not break away from claim and limited; can make many modifications, variation or equivalence, but all will fall within the protection domain of the present utility model.
Claims (10)
1. the gasification installation of an organic solvent fuel is characterized in that, comprising:
One gasification bucket is equipped with organic solvent in it; One side of this gasification bucket bottom is provided with an air inlet, and this gasification bucket top is provided with combustion gas delivery outlet and output pipe; This gasification bucket more is provided with an organic solvent input pipe and a gas discharger that is penetrated by its top; The bottom of this organic solvent input pipe and this gas discharger is stretched in the gasification bucket, and the bottom of this gas discharger is higher than the bottom of organic solvent input pipe;
One air pump, it is communicated with the air inlet of pipeline with this gasification bucket bucket end, can deliver air in the gasification bucket; And,
One storage vat is equipped with organic solvent in it; This storage vat comprises an organic solvent efferent duct and a gas inlet pipe is set; This organic solvent efferent duct is connected with the organic solvent input pipe of this gasification bucket, organic solvent can be transported in the gasification bucket; This gas inlet pipe is connected with the gas discharger of this gasification bucket, and the liquid level of the organic solvent in the gasification bucket stops the conveying of organic solvent when sealing the lower end mouth of pipe of gas discharger of this gasification barrel automatically.
2. the gasification installation of organic solvent fuel according to claim 1 is characterized in that: the mouth of pipe on the gas inlet pipe top of this storage vat is higher than the liquid level of organic solvent in the storage vat.
3. the gasification installation of organic solvent fuel according to claim 1, it is characterized in that: be provided with a control valve in the communication path between the organic solvent input pipe of this gasification bucket and the organic solvent efferent duct of storage vat, to control the unimpeded of this communication path or to close.
4. the gasification installation of organic solvent fuel according to claim 1 is characterized in that: this gasification bucket is communicated with a liquid level target tube, and this liquid level target tube subscript is shown with the height of the gas discharger lower end mouth of pipe of this gasification bucket.
5. the gasification installation of organic solvent fuel according to claim 1 is characterized in that: this air inlet place is provided with a non-return valve, is gone in the air intake line by the air inlet adverse current to prevent organic solvent.
6. the gasification installation of organic solvent fuel according to claim 1 is characterized in that: be provided with the fining air bubbles plate of the skewed setting of a slice at least in this gasification bucket, lay most little perforation on this fining air bubbles plate; Wherein, a minimum side of a slice fining air bubbles plate of lowermost end is near the air inlet place.
7. the gasification installation of organic solvent fuel according to claim 6 is characterized in that: the distribution of plurality of small holes on this skewed fining air bubbles plate is to be laid by few cumulative kenel by low and high work.
8. the gasification installation of organic solvent fuel according to claim 7 is characterized in that: the fining air bubbles plate more than two is with the kenel setting of upper and lower arrangement; In any two adjacent fining air bubbles plates, be positioned at the lower corresponding higher side of fining air bubbles plate of a side of fining air bubbles plate of top near its below.
9. the gasification installation of organic solvent fuel according to claim 1 is characterized in that: the bottom of this gasification bucket is provided with a constent temperature heater.
10. the gasification installation of organic solvent fuel according to claim 1 is characterized in that: the combustion gas output pipe of this gasification bucket is provided with a non-return valve, can prevent that fuel gas return-flow from going in the gasification bucket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205726731U CN201885249U (en) | 2010-10-20 | 2010-10-20 | Gasifier for organic solvent fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205726731U CN201885249U (en) | 2010-10-20 | 2010-10-20 | Gasifier for organic solvent fuel |
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| CN201885249U true CN201885249U (en) | 2011-06-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205726731U Expired - Fee Related CN201885249U (en) | 2010-10-20 | 2010-10-20 | Gasifier for organic solvent fuel |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN110449110A (en) * | 2018-05-07 | 2019-11-15 | 环创源科技股份有限公司 | The turning sludge into fuel method and device and modular reactor of spent organic solvent |
| CN115823611A (en) * | 2022-12-22 | 2023-03-21 | 绍兴市上虞区职业教育中心(上虞区技工学校) | Preheating-free pressurizing air pump of split furnace and oil supply method thereof |
-
2010
- 2010-10-20 CN CN2010205726731U patent/CN201885249U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN110449110A (en) * | 2018-05-07 | 2019-11-15 | 环创源科技股份有限公司 | The turning sludge into fuel method and device and modular reactor of spent organic solvent |
| CN110449110B (en) * | 2018-05-07 | 2021-09-14 | 环创源科技股份有限公司 | Method and device for fuelization of waste organic solvent and modular reactor |
| CN115823611A (en) * | 2022-12-22 | 2023-03-21 | 绍兴市上虞区职业教育中心(上虞区技工学校) | Preheating-free pressurizing air pump of split furnace and oil supply method thereof |
| CN115823611B (en) * | 2022-12-22 | 2023-11-03 | 绍兴市上虞区职业教育中心(上虞区技工学校) | Preheating-free pressurizing air pump of split furnace and oil supply method thereof |
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Legal Events
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110629 Termination date: 20171020 |