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CN203741277U - Waste oil treatment system - Google Patents

Waste oil treatment system Download PDF

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Publication number
CN203741277U
CN203741277U CN201420087534.8U CN201420087534U CN203741277U CN 203741277 U CN203741277 U CN 203741277U CN 201420087534 U CN201420087534 U CN 201420087534U CN 203741277 U CN203741277 U CN 203741277U
Authority
CN
China
Prior art keywords
main reaction
reaction still
waste oil
oil
treatment system
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
Application number
CN201420087534.8U
Other languages
Chinese (zh)
Inventor
贺昶明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chengdu Damo Petroleum Machinery Co Ltd
Original Assignee
Chengdu Damo Petroleum Machinery Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chengdu Damo Petroleum Machinery Co Ltd filed Critical Chengdu Damo Petroleum Machinery Co Ltd
Priority to CN201420087534.8U priority Critical patent/CN203741277U/en
Application granted granted Critical
Publication of CN203741277U publication Critical patent/CN203741277U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a waste oil treatment system. The waste oil treatment system comprises a main reaction kettle, wherein a motor is arranged at the center at the top end of the main reaction kettle, and is connected with a stirrer; the stirrer is arranged at the interior of the main reaction kettle; a fractionating tower is mounted at the top end of the main reaction kettle, is communicated with the interior of the interior of the main reaction kettle, and is communicated with a cooling device; the cooling device is connected with a dewaterer; the dewaterer is connected with an air collection tank and an oil collection tank; the air collection tank is connected with an induced air combustion gun; the cooling device, the dewaterer, the air collection tank, the oil collection tank and the induced air combustion gun are all arranged on the outside of the main reaction kettle. According to the system, waste oil can be treated to obtain different classifications of oil, and the recycling of the waste oil is realized, so that the economic benefits are increased, and the problem that in the prior art, waste oil is discharged directly to cause environmental pollution and resource waste is solved.

Description

A kind of waste oil treatment system
Technical field
The utility model relates to a kind of system, especially relates to a kind of waste oil treatment system, belongs to oil gas and reclaims field.
Background technology
Oil claims again crude oil, be a kind of thickness, Vandyke brown (sometimes a little green) liquid.It is mixed and is formed by different hydrocarbon polymers, and its chief component composition is alkane, goes back in addition the elements such as sulfur-bearing, oxygen, nitrogen, phosphorus, vanadium in oil.Oil is mainly used as fuel oil and gasoline, oil fuel and gasoline composition one of most important primary energy source in the world.Oil is also that many chemical industry products are as the raw material of solution, chemical fertilizer, sterilant and plastics etc.Oil is mainly hydrocarbon polymer.It is mixed and is formed by different hydrocarbon polymers, the chemical element of composition oil is mainly carbon (83% ~ 87%), hydrogen (11% ~ 14%), and all the other are sulphur (0.06% ~ 0.8%), nitrogen (0.02% ~ 1.7%), oxygen (0.08% ~ 1.82%) and micro-metals (Ni-V-Fe, antimony etc.).The chief component that is closed the hydro carbons forming and formed oil by carbon and hydrogenation, accounts for 95% ~ 99%, and various hydro carbons are divided into by its structure: alkane, naphthenic hydrocarbon, aromatic hydrocarbon.General natural oil does not often contain alkene and the alkynes that quantity does not wait in secondary processing product containing alkene.Sulfur-bearing, oxygen, nitrogen compound are harmful to petroleum products, in refining of petroleum, should remove as far as possible.Stone oil properties is different because of the place of production, and density is 0.8 ~ 1.0 gram per centimeter, and range of viscosities is very wide, zero pour difference very large (30 ~-60 degrees Celsius), boiling spread is more than normal temperature to 500 degree Celsius, dissolves in multiple organic solvent, water insoluble, but can form milk sap with water.But the composition of the oil in different oil fields and appearance can be distinguished very large.Oil is mainly used as fuel oil and gasoline, and oil fuel and gasoline form at present one of most important primary energy source in the world.Oil is also that many chemical industry products are as the raw material of solvent, chemical fertilizer, sterilant and plastics etc.Oil plant in use for some time, has just produced a lot of waste oil, the direct exhaust emission environment of waste oil, and caused the waste of resource.
Utility model content
The purpose of this utility model is to overcome the direct exhaust emission environment of above-mentioned existing waste oil, and cause the problem of the waste of resource, design a kind of waste oil treatment system, this system can be processed waste oil, obtain different classification, solve the direct exhaust emission environment of existing waste oil, and caused the problem of the waste of resource.
The purpose of this utility model is achieved through the following technical solutions: a kind of waste oil treatment system, comprise main reaction still, and the center, top of described main reaction still is provided with motor, and motor is connected with agitator, and agitator is arranged on main reaction still inside; The top of main reaction still is provided with separation column, and the internal communication of separation column and main reaction still, separation column is communicated with refrigerating unit, refrigerating unit is connected with water trap, water trap is connected with air collector and gathering tank, air collector is connected with air inducing burning rifle, and refrigerating unit, water trap, air collector, gathering tank and air inducing burning rifle are all arranged on main reaction still outside.
Between air collector and air inducing burning rifle, be provided with non-return valve, and non-return valve is communicated with air collector and air inducing burning rifle simultaneously.
Refrigerating unit is connected with water pump.
The top of main reaction still is provided with access hole, and motor is arranged between access hole and separation column.
On the sidewall of main reaction still, be provided with slag notch, and slag notch is arranged on sidewall and the bottom extremity place of main reaction still.
In sum, the beneficial effects of the utility model are: this system can be processed waste oil, obtain different classification, realize useless oil recovery, improve economic benefit, solved the direct exhaust emission environment of existing waste oil, and caused the problem of the waste of resource.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Mark and corresponding component title in accompanying drawing: 1-slag notch; 2-main reaction still; 3-access hole; 4-motor; 5-refrigerating unit; 6-air collector; 7-non-return valve; 8-air inducing burning rifle; 9-water pump; 10-water trap; 11-separation column; 12-gathering tank.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, but embodiment of the present utility model is not limited only to this.
Embodiment 1:
As shown in Figure 1, a kind of waste oil treatment system, comprises main reaction still 2, and the center, top of described main reaction still 2 is provided with motor 4, and motor 4 is connected with agitator, and agitator is arranged on main reaction still 2 inside; The top of main reaction still 2 is provided with separation column 11, and the internal communication of separation column 11 and main reaction still 2, separation column 11 is communicated with refrigerating unit 5, refrigerating unit 5 is connected with water trap 10, water trap 10 is connected with air collector 6 and gathering tank 12, air collector 6 is connected with air inducing burning rifle 8, and refrigerating unit 5, water trap 10, air collector 6, gathering tank 12 and air inducing burning rifle 8 are all arranged on main reaction still 2 outsides.Main reaction still 2 utilizes driven by motor agitator to stir, waste oil in main reaction still 2 is stirred, then the heating unit that main reaction still 2 belows arrange heats main reaction still 2, thereby waste oil is distilled to processing, utilize separation column 11 to realize fractionation, the oil gas distilling is cooling by refrigerating unit 5, obtain the mixture of liquids and gases, after water trap dehydration, the water mixing in liquid is departed from, obtain highly purified gas-oil mixture, liquid oils enters into gathering tank 12 and collects, gas enters into air collector 6 and collects, then by air inducing burn rifle 8 by air collector 6 collect gaseous combustion fall, the final oil handling that gives up of realizing, realize useless oil recovery, improve economic benefit, solve the direct exhaust emission environment of existing waste oil, and cause the problem of the waste of resource.
Embodiment 2:
As shown in Figure 1, between air collector 6 and air inducing burning rifle 8, be provided with non-return valve 7, and non-return valve 7 is communicated with air collector 6 and air inducing burning rifle 8 simultaneously.The preferential dry type non-return valve that adopts in the technical program, dry type non-return valve mainly contains valve body, rocking bar, valve gap, valve seat, the compositions such as sealing socket, when work, gas backs down valve gap and is entered in non-return valve by inlet mouth under certain pressure effect, flowed out by outlet, in the time that air pressure reduces suddenly, valve gap is under the drive of rocking bar, automatically valve seat is covered, play sealing function, gas can not flow backwards like this, and the flue gas and the air pressure that after 8 burnings of air inducing burning rifle, produce stop, prevent that it is back in air collector 6, impacts the work of system.
Refrigerating unit 5 is connected with water pump 9.The preferential water cooler that adopts of refrigerating unit 5, utilizes water pump that the cold water of circulation is provided, and makes the distillment of pass-out in separation column 11 cooling by the mode of water-cooled.
The top of main reaction still 2 is provided with access hole 3, and motor 4 is arranged between access hole 3 and separation column 11.Access hole 3 is that convenient operation personnel keep in repair main reaction still 2 and inner agitator, prevent in use, residual solids in waste oil causes after damage main reaction still 2 internal parts, serviceman need to spend plenty of time dismounting main reaction still 2, in the course of the work, access hole 3 all seals, and ensures that the safety of waste oil treatment work is carried out.
On the sidewall of main reaction still 2, be provided with slag notch 1, and slag notch 1 is arranged on sidewall and the bottom extremity place of main reaction still 2.Slag notch 1 is the passage that main reaction still 2 is reacted to the solid residue discharge of rear generation, and waste oil, after distillation is processed, exists residual solids in main reaction still 2, utilizes the slag notch 1 that is arranged on main reaction still 2 bottom positions to discharge.
The above; it is only preferred embodiment of the present utility model; not the utility model is done to any pro forma restriction; any simple modification, equivalent variations that every foundation technology of the present utility model, method are done above embodiment in fact, within all falling into protection domain of the present utility model.

Claims (5)

1. a waste oil treatment system, is characterized in that: comprise main reaction still (2), the center, top of described main reaction still (2) is provided with motor (4), and motor (4) is connected with agitator, and agitator is arranged on main reaction still (2) inside; The top of main reaction still (2) is provided with separation column (11), and the internal communication of separation column (11) and main reaction still (2), separation column (11) is communicated with refrigerating unit (5), refrigerating unit (5) is connected with water trap (10), water trap (10) is connected with air collector (6) and gathering tank (12), air collector (6) is connected with air inducing burning rifle (8), and refrigerating unit (5), water trap (10), air collector (6), gathering tank (12) and air inducing burning rifle (8) are all arranged on main reaction still (2) outside.
2. a kind of waste oil treatment system according to claim 1, is characterized in that: between described air collector (6) and air inducing burning rifle (8), be provided with non-return valve (7), and non-return valve (7) is communicated with air collector (6) and air inducing burning rifle (8) simultaneously.
3. a kind of waste oil treatment system according to claim 1, is characterized in that: described refrigerating unit (5) is connected with water pump (9).
4. a kind of waste oil treatment system according to claim 1, is characterized in that: the top of described main reaction still (2) is provided with access hole (3), and motor (4) is arranged between access hole (3) and separation column (11).
5. a kind of waste oil treatment system according to claim 1, is characterized in that: on the sidewall of described main reaction still (2), be provided with slag notch (1), and slag notch (1) is arranged on sidewall and the bottom extremity place of main reaction still (2).
CN201420087534.8U 2014-02-28 2014-02-28 Waste oil treatment system Expired - Fee Related CN203741277U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420087534.8U CN203741277U (en) 2014-02-28 2014-02-28 Waste oil treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420087534.8U CN203741277U (en) 2014-02-28 2014-02-28 Waste oil treatment system

Publications (1)

Publication Number Publication Date
CN203741277U true CN203741277U (en) 2014-07-30

Family

ID=51341103

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420087534.8U Expired - Fee Related CN203741277U (en) 2014-02-28 2014-02-28 Waste oil treatment system

Country Status (1)

Country Link
CN (1) CN203741277U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103834427A (en) * 2014-02-28 2014-06-04 成都大漠石油机械有限公司 System capable of treating waste oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103834427A (en) * 2014-02-28 2014-06-04 成都大漠石油机械有限公司 System capable of treating waste oil

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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

Granted publication date: 20140730

Termination date: 20150228

EXPY Termination of patent right or utility model