CN202849341U - Waste oil, tyre oil and plastic oil distilling device - Google Patents
Waste oil, tyre oil and plastic oil distilling device Download PDFInfo
- Publication number
- CN202849341U CN202849341U CN 201220531243 CN201220531243U CN202849341U CN 202849341 U CN202849341 U CN 202849341U CN 201220531243 CN201220531243 CN 201220531243 CN 201220531243 U CN201220531243 U CN 201220531243U CN 202849341 U CN202849341 U CN 202849341U
- Authority
- CN
- China
- Prior art keywords
- oil
- tower
- distillation
- connects
- condenser
- 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.)
- Withdrawn - After Issue
Links
Images
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses a waste oil, tyre oil and plastic oil distilling device which comprises a preheater, a hot blast heater, a distillation still, a distillation tower, a fractionating tower, condensers, oil storage tanks, an oil scrubbing tower, a filter tower and a product tank, wherein the preheater is connected with the oil inlet of the distillation kettle, the hot blast heater is connected with the distillation still, the distillation tower is arranged on the distillation still, the oil gas outlet in the top of the distillation tower is connected with the fractionating tower, the reflowing hole in the lower part of the fractionating tower is connected with the distillation tower, the light component oil gas port and the intermediate component oil gas port of the fractionating tower are respectively connected with the corresponding condensers, the condensers are respectively connected with corresponding extraction towers and the oil storage tanks, and the oil storage tanks are connected with the product tank through an oil pump, the oil scrubbing tower and the filter tower. The waste oil, tyre oil and plastic oil distilling device has the advantages of simple structure, convenience in operation, high processing precision, no leakage, improved working environment, high production efficiency, and thoroughly eliminated secondary pollution; and the processed oil is better than the oil obtained by common distillation, is capable of replacing raw materials in a production plant of oil for large ships, and is larger in economic benefit, and thus resources and energies can be effectively saved.
Description
Technical field
The utility model relates to a kind of by distillation processing treatment used oil, tire oil, plastic oil, obtains the equipment of purer oil product.
Background technology
Process solid refuse and reclaim the technology that oil product recycles with junked tire, waste or used plastics thermo-cracking, worldwide obtained Rapid Popularization, not only eliminated the pollution of part solid refuse to environment, and realized the regeneration of the energy, but the crude oil that produces behind damaged tire, the Pyrolysis of Plastics Wastes and used oil, major applications are as heat energy fuel.Because producing carbon black in the cracking process, carbon black is along with oil gas enters condenser system, therefore the oil product color is more black, impurity is more, and calorific value is not high, and utilization ratio is lower; And minority adopts the simple distillation technology that oil product is carried out simple and easy processing, and this technical finesse precision is lower, and the oil product loss is serious in the course of processing, and distillation oil product unstable chemcial property later, as easy as rolling off a log oxidized, cause the blackening of oil product color, impurity produces serious, and the economic interests loss is larger.In still-process, can produce the dregs of fat unavoidably, it endangers operator's safety and environment is caused secondary pollution.
Summary of the invention
The purpose of this utility model is: a kind of used oil, tire oil, plastic oil distillation plant are provided, this equipment carries out distilation to used oil, tire oil, plastic oil under full-closed environment, raising with the oil product technical indicator that realizes used oil, tire oil, plastic oil overcomes the problem of bringing when prior art is processed waste oil simultaneously.
Realize that the technical scheme that the utility model purpose is taked is: this equipment is comprised of preheater, strong atomizing tower, hotblast stove, still kettle, distillation tower, separation column, condenser, storage tank, extractor, washing oil tower, filtration tank and product tank, the preheater oil outlet is connected with the still kettle oil-in, the hotblast stove air outlet is connected with still kettle flue mouth, and the preheater smoke outlet connects the strong atomizing tower; Distillation tower is located at above the still kettle, and the fuel-displaced gas port at distillation tower top connects separation column, and the refluxing opening of separation column bottom connects still kettle; Separation column light constituent oil gas mouth be connected the component oil gas port and connect respectively corresponding condenser, condenser is connected with corresponding extraction column respectively, extraction column is connected with storage tank respectively; The storage tank oil outlet is connected to washing oil tower bottom through an injection pump, and washing oil tower oil outlet is connected with filtration tank, and filtration tank connects product tank through pipeline.
Top at preheater connects one group of condenser through pipeline, and condenser connects corresponding extractor and storage tank.
Below the condenser that connects separation column top light constituent oil gas, be provided with a reflux line and be connected on the still kettle.
The exhaust outlet of extractor is connected with the hotblast stove gas gun through water seal.
Positively effect of the present utility model is: equipment is simple, and fitting operation is convenient, and processing accuracy is high, and without leaking, oil quality is good, and added value is higher; The utilization of this equipment has not only improved Working environment, and production efficiency is high, and has thoroughly eliminated the secondary pollution to environment, oil product after the processing is better than the oil product of common distillation gained, can replace large ship with the raw material of oily factory, economic interests are larger, and saved resource and the energy.
Description of drawings
Accompanying drawing 1 is equipment pie graph of the present utility model.
Embodiment
As shown in Figure 1, this equipment is comprised of preheater 1, strong atomizing tower 11, hotblast stove 12, still kettle 14, distillation tower 2, separation column 3, pipe bundle condenser 4,18,6, storage tank 17,20,22, extractor 16,19,21, washing oil tower 8, filtration tank 9 and product tank 5, preheater 1 oil outlet is connected with still kettle 14 oil-ins, hotblast stove 12 air outlets are connected with still kettle 14 flue mouths, preheater 1 smoke outlet connects strong atomizing tower 11, strong atomizing tower 11 smoke outlets are connected with chimney 10 through induced draft fan, and the useless flue gas after processing is discharged; Distillation tower 2 is located at above the still kettle 14, and the fuel-displaced gas port at distillation tower 2 tops connects separation column 3, and the refluxing opening of separation column 3 bottoms connects still kettle 14; Below the pipe bundle condenser 18 that connects separation column 3 top light constituent oil gas, be provided with a reflux line 13 and be connected on the still kettle 14; Separation column 3 light constituent oil gas mouths be connected the component oil gas port and connect respectively corresponding pipe bundle condenser 18,4; Top at preheater 1 connects one group of pipe bundle condenser 6 through pipeline; Each pipe bundle condenser 4,18,6 is connected with corresponding extractor 16,19,21 respectively, and each extractor 16,19,21 is connected with corresponding storage tank 17,20,22 respectively; The storage tank oil outlet is connected to washing oil tower 8 bottoms through an injection pump 23, and washing oil tower 8 oil outlets are connected with filtration tank 9, and filtration tank 9 connects product tank 5 through pipeline.The exhaust outlet of extractor is connected with hotblast stove 12 gas guns through water seal 7.
Principle of work of the present utility model and working process thereof are: first combustion heat wind furnace 12, add thermal still 14 with flue, its smoke outlet passes into preheater 1, then the waste oil after preheater 1 preheating is pumped into still kettle 14 with oil pump, waste oil Pintsch process after the heating, enter separation column 3 by distillation tower 2,3 pairs of high-temperature oil gas of separation column are carried out primary fractionation, its air outlet, top is mainly light constituent oil gas, being introduced into one group of pipe bundle condenser 18 cools off, the air outlet, middle part is mainly middle component oil gas, is introduced into another group pipe bundle condenser 4; An air outlet is established at preheater 1 top, and the oil gas of gasification is directly introduced one group of pipe bundle condenser 6, and pipe bundle condenser cools off pour point depression to above three part oil gas respectively.Three groups of pipe bundle condensers 4,18,6 are corresponding three extractors 16,19,21 respectively; oil droplet and oil gas to first one-tenth extract; oil droplet enters corresponding storage tank 17,20,22; oil gas enters two-stage anti-backfire protection water seal 7 by compiling; water seal waste gas is out introduced the waste-gas burning spray gun of hotblast stove 12 by pipeline 15,12 burnings of heat supply wind furnace.The oil of three storage tank is pumped into from washing oil tower 8 bottoms through injection pump 23, pass catalyzer and additive in the washing oil tower 8, the oil after processed enters filtration tank 9 through oil pump again, obtains after filtration processed oil, and end product oil is admitted to product tank 5.
Claims (4)
1. a used oil, tire oil, plastic oil distillation plant, it is characterized in that: it is comprised of preheater, strong atomizing tower, hotblast stove, still kettle, distillation tower, separation column, condenser, storage tank, extractor, washing oil tower, filtration tank and product tank, the preheater oil outlet is connected with the still kettle oil-in, the hotblast stove air outlet advances mouth with still kettle and is connected, and the preheater smoke outlet connects the strong atomizing tower; Distillation tower is located at above the still kettle, and the fuel-displaced gas port at distillation tower top connects separation column, and the refluxing opening of separation column bottom connects still kettle; Separation column light constituent oil gas mouth be connected the component oil gas port and connect respectively corresponding condenser, condenser is connected with corresponding extractor respectively, extractor is connected with corresponding storage tank respectively; The storage tank oil outlet is connected to washing oil tower bottom through an injection pump, and washing oil tower oil outlet is connected with filtration tank, and filtration tank connects product tank through pipeline.
2. used oil according to claim 1, tire oil, plastic oil distillation plant, it is characterized in that: the top at preheater connects one group of condenser through pipeline, and condenser connects corresponding extractor and storage tank.
3. used oil according to claim 1, tire oil, plastic oil distillation plant is characterized in that: below the condenser that connects separation column top light constituent oil gas, be provided with a reflux line and be connected on the still kettle.
4. used oil according to claim 1, tire oil, plastic oil distillation plant, it is characterized in that: the exhaust outlet of extractor is connected with the hotblast stove gas gun through water seal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220531243 CN202849341U (en) | 2012-10-17 | 2012-10-17 | Waste oil, tyre oil and plastic oil distilling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220531243 CN202849341U (en) | 2012-10-17 | 2012-10-17 | Waste oil, tyre oil and plastic oil distilling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202849341U true CN202849341U (en) | 2013-04-03 |
Family
ID=47980561
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220531243 Withdrawn - After Issue CN202849341U (en) | 2012-10-17 | 2012-10-17 | Waste oil, tyre oil and plastic oil distilling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202849341U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102851065A (en) * | 2012-10-17 | 2013-01-02 | 商丘亿龙机械设备有限公司 | Waste machine oil/tire oil/plastic oil distillation device and technique |
| CN108441251A (en) * | 2018-03-28 | 2018-08-24 | 商丘中清环保科技有限公司 | Cryogenic distillation process |
| CN108441252A (en) * | 2018-03-28 | 2018-08-24 | 商丘中清环保科技有限公司 | Cryogenic distillation apparatus |
-
2012
- 2012-10-17 CN CN 201220531243 patent/CN202849341U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102851065A (en) * | 2012-10-17 | 2013-01-02 | 商丘亿龙机械设备有限公司 | Waste machine oil/tire oil/plastic oil distillation device and technique |
| CN102851065B (en) * | 2012-10-17 | 2014-06-11 | 商丘亿龙机械设备有限公司 | Waste machine oil/tire oil/plastic oil distillation device and technique |
| CN108441251A (en) * | 2018-03-28 | 2018-08-24 | 商丘中清环保科技有限公司 | Cryogenic distillation process |
| CN108441252A (en) * | 2018-03-28 | 2018-08-24 | 商丘中清环保科技有限公司 | Cryogenic distillation apparatus |
| CN108441251B (en) * | 2018-03-28 | 2021-02-23 | 商丘中清环保科技有限公司 | Cryogenic distillation process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US10422583B2 (en) | Method for recycling residual heat and dust in flue gas during reclaimed copper refining | |
| CN106281396B (en) | Waste plastic cracking equipment and method | |
| CN104438297B (en) | A kind of method and apparatus processing organic waste | |
| CN205261566U (en) | Solid organic waste resource is made up and is put | |
| CN202849341U (en) | Waste oil, tyre oil and plastic oil distilling device | |
| CN101671572A (en) | Oil shale dry distillation recovery technology | |
| CN207904180U (en) | The environmentally friendly recycling system of waste tire | |
| CN102851065B (en) | Waste machine oil/tire oil/plastic oil distillation device and technique | |
| CN104560151B (en) | A kind of method that employing waste lubricating oil refines petrol and diesel oil | |
| CN104099140A (en) | Industrial environment-friendly fuel oil and preparation method thereof | |
| CN203866254U (en) | Atmospheric and vacuum device adopting combined catalytic flue gas and oil slurry | |
| CN103173238B (en) | Thermal pyrolysis method for Fischer-Tropsch synthesis reaction wax residue | |
| CN206295742U (en) | A kind of dust-laden is pyrolyzed the full oil wash system of oil gas | |
| CN202666675U (en) | High-temperature flue gas recovery and purification process device | |
| CN204589076U (en) | The resinous shale utilization system of a kind of coupled gas and solid thermal carriers | |
| CN105484716B (en) | Oil field produced liquid heat energy recovery device and method | |
| CN103725307B (en) | Continuous flash process equipment for waste oil | |
| CN204543615U (en) | A kind of industrial continuous used oil process distillation equipment | |
| CN103265973B (en) | Method and equipment for producing automotive diesel fuel from medium temperature coal tar light oil as raw material | |
| CN212246908U (en) | A regeneration processing system for waste mineral oil | |
| CN203187622U (en) | Biomass carbonization and dry distillation central medium calorific value gas supply system | |
| CN203187502U (en) | Skid-mounted sludge pyrolysis system for preparing three-phase combustion product | |
| CN202193771U (en) | Device for refining waste machine oil into diesel oil | |
| CN206244730U (en) | Waste lubricant oil regeneration and production diesel device | |
| CN102851064B (en) | Continuous purification and distillation apparatus for combustible waste oil |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130403 Effective date of abandoning: 20140611 |
|
| RGAV | Abandon patent right to avoid regrant |