CN201545812U - Waste oil refining device - Google Patents
Waste oil refining device Download PDFInfo
- Publication number
- CN201545812U CN201545812U CN2009202579028U CN200920257902U CN201545812U CN 201545812 U CN201545812 U CN 201545812U CN 2009202579028 U CN2009202579028 U CN 2009202579028U CN 200920257902 U CN200920257902 U CN 200920257902U CN 201545812 U CN201545812 U CN 201545812U
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- oil
- agitated reactor
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- combustion chamber
- waste
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Abstract
The utility model relates to a waste oil refining device. An agitated reactor is a vertical agitated reactor, a spiral heating air channel is formed on the outer surface of the agitated reactor, a combustion chamber is connected with the bottom of the agitated reactor, and a draught fan is connected with an air outlet of the spiral heating air channel on the outer surface of the agitated reactor; an oil gas outlet at the top end of the agitated reactor is connected with a distillation tower which is connected with a middle oil storage tank through a pipe bundle condenser; the middle oil storage tank is connected with a vacuum generator , and a waste gas filter is connected with the combustion chamber beside the agitated reactor. In the utility model, by adopting totally closed reduced pressure distillation, production efficiency increases to more than 3 times in comparison of traditional equipment; by adopting spiral hot air heating of the air channel, the production process is safe and environment friendly; by adopting an automatic feeding and deslagging system, a furnace can be continuously fed without being cooled after deslagging; combustible gas incapable of being liquefied can directly enters the combustion chamber to be combusted, thereby greatly saving the energy; and waste plastic passes through the device, produced fuel oil is required to be distilled twice, therefore, the waste oil refining device has the advantages of good quality of oil, high oil yield and the like.
Description
Technical field
The utility model relates to a kind of equipment that utilizes waste oil oil refining.
Background technology
Along with developing rapidly of plastic waste, waste rubber oil refining industry, the application of the oil fuel of its production also more and more widely and has been penetrated in the every field and daily life of national economy.Because the fast development of industry and practitioner's increase, raw-material price also significantly improves thereupon but simultaneously.On the basis that does not reduce material cost, how to improve the added value of oil fuel? the simplest method be useless mould, the thick oil of glue production distills (perhaps being called rectifying) once more, be generally faint yellow or for pink liquid by the oil product color after the rectifying, the major technology index can reach the standard of high quality fuel lance, the life-span of spray gun is prolonged, and free from extraneous odour, price also can be than 1500 yuan of thick oil increases per ton.The device of producing this regenerated fuel oil has the selection of 2 directions at present, and the one, investment reaches the large-scale petrochemical refining plant more than 1,000,000,000, and another direction is that popular investment at present has only 50,000 to 100,000 native stove.But the working efficiency of native stove, security, the feature of environmental protection are poor.Less investment how, and can overcome some weakness of native stove, be a current important problem.
The native stove that adopt at present the China's Mainland mainly adopts horizontal stationary processors, technical process is as follows: the thick oil that useless mould, glue produces at first manually adds from the top of cracking treater, then seal opening for feed, beginning to do fuel with coal or firewood then at the bottom of the treater slowly heats, the cracking treater has the volume of 20 cubic meters usually, reinforced 15 tons, generally need fortnight could refine a stove.After the end, stopped 12 hours.After fully descending Deng temperature of processor, open the slag notch of treater bottom and slag tap.From the treater throat-fed, enter next circulation again.
Domestic horizontal stationary processors, the three wastes are in process of production handled can't reach environmental requirement, adopts the method for air distillation, and the oil quality of being produced is poor, and rate ratio is lower.
Summary of the invention
The purpose of this utility model is a kind of waste oil a refining unit of design, and smell of product is diminished, and reduces oil density, improves oil refining efficient, to overcome the problem that prior art exists.
Realize that the technical scheme that the utility model purpose is taked is: reactor is the vertical response still, and the reactor outside is provided with the spiral heating air channel. the combustion chamber is connected the reactor bottom, and induced draft fan is connected on the air outlet in spiral heating air channel, reactor outside; The oil gas vent of reactor Xiang Duan connects a distillation tower, and distillation tower is storage tank in the middle of a shell-and tube condenser connects; Middle storage tank is connected with vacuum generator, the combustion chamber that waste gas filter ligation still is other.
Positively effect of the present utility model is: adopt totally-enclosed, decompression distillation system. be more than 3 times of the rotary production efficiency of equipment of traditional batch; The production process of complete assembly is to move in the environment of smoke-free and tasteless, has the superior safety and the feature of environmental protection; Because this treatment unit adopts atmospheric and vacuum distillation unit, open decompression and can make distillation speed accelerate 3 times, need not the labor cleaning when slagging tap, can slag tap automatically, having gone out slag need not continue charging by cool stove again; The inflammable gas that can not liquefy in the production process directly enters combustion chambers burn, has saved the energy greatly; The oil fuel inclusion-free that this device fabrication goes out, smell is little, and density is low, and color is bright, has that oil quality is good, the oil yield advantages of higher.
Description of drawings
Accompanying drawing is a synoptic diagram of the present utility model
Embodiment
The utility model as shown in drawings, reactor 2 is provided with the vertical response still in spiral heating air channel for the outside, combustion chamber 1 is connected reactor 2 bottoms, and induced draft fan 4 is connected on the air outlet in spiral heating air channel, reactor 2 outside, adopts high-temperature gas reacting by heating still 2; At reactor 2 tops one opening for feed is arranged, one slag tapping equipment is arranged in reactor 2 bottoms; The oil gas vent of 2 ends of reactor connects a distillation tower 3, and distillation tower 3 is storage tank 6 in the middle of a shell-and tube condenser 5 connects, and with pump 7 oil product is sent into treatment tank 8 flavor that decolours then; Middle storage tank 6 is connected with vacuum generator 8, the combustion chamber 1 on waste gas filter 9 ligation stills 2 sides.
The raw material that the utility model is suitable for has: used oil, waste lubricating oil, tire oil, the multiple waste oil of plastics wet goods.
Claims (1)
1. waste oil a refining unit, it is characterized in that: reactor is the vertical response still that the outside is provided with the spiral heating air channel, and the combustion chamber is connected the reactor bottom, and induced draft fan is connected on the air outlet in spiral heating air channel, reactor outside; The oil gas vent of reactor Xiang Duan connects a distillation tower, and distillation tower is storage tank in the middle of a shell-and tube condenser connects; Middle storage tank is connected with vacuum generator, the combustion chamber that waste gas filter ligation still is other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202579028U CN201545812U (en) | 2009-11-06 | 2009-11-06 | Waste oil refining device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202579028U CN201545812U (en) | 2009-11-06 | 2009-11-06 | Waste oil refining device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201545812U true CN201545812U (en) | 2010-08-11 |
Family
ID=42600980
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202579028U Expired - Fee Related CN201545812U (en) | 2009-11-06 | 2009-11-06 | Waste oil refining device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201545812U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104289073A (en) * | 2014-09-17 | 2015-01-21 | 涂晶 | Waste gas recovery device of chemical reaction kettle |
| CN106590713A (en) * | 2016-11-28 | 2017-04-26 | 玉门市云华再生资源有限责任公司 | Waste tire pyrolysis recycling treatment system |
-
2009
- 2009-11-06 CN CN2009202579028U patent/CN201545812U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104289073A (en) * | 2014-09-17 | 2015-01-21 | 涂晶 | Waste gas recovery device of chemical reaction kettle |
| CN106590713A (en) * | 2016-11-28 | 2017-04-26 | 玉门市云华再生资源有限责任公司 | Waste tire pyrolysis recycling treatment system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100811 Termination date: 20131106 |