CN208471997U - A kind of gasoline recovery plant - Google Patents
A kind of gasoline recovery plant Download PDFInfo
- Publication number
- CN208471997U CN208471997U CN201820646744.4U CN201820646744U CN208471997U CN 208471997 U CN208471997 U CN 208471997U CN 201820646744 U CN201820646744 U CN 201820646744U CN 208471997 U CN208471997 U CN 208471997U
- Authority
- CN
- China
- Prior art keywords
- mouth
- interface
- distillation
- cooling cylinder
- river
- 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.)
- Active
Links
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
The utility model discloses a kind of gasoline recovery plants, including distillation case, cooling cylinder, receive bucket, distilling side above case is feed inlet, contains exclusion device in feed inlet conduit, filters out the object block impurity in waste oil, the other side is distillation mouth above, connect still head, below side be blowdown hydraulic fluid port, remaining other liquid discharge after distillation, it distills and is equipped with a steam pipe in case, for distilling heating;One jiao is the mouth of a river from the beginning above cooling cylinder, and corresponding one jiao is another the mouth of a river from the beginning below, by originally water condensation, saves condensation cost, is how curved condenser pipe, nozzle connection outside conduit in cooling cylinder;Receive the connection condenser pipe of bucket upper end one;The utility model includes that structure is simple, safe operation, can effectively reduce pollution of the waste oil to atmosphere using the present apparatus, improve the utilization rate of gasoline, energy saving, reduces economic loss, reports to obtain considerable benefit.
Description
Technical field
The utility model relates to gasoline recovery field, specially a kind of gasoline recovery plant.
Background technique
Automobile has a service life mostly, after reaching certain service life or certain mileage number, it is necessary to
When carrying out scrapping processing, and scrapping processing, usually need to disassemble in automobile, but before disassembling automobile, generally
It needs to recycle in waste oil remaining in automobile, not pollute the environment so, two can save a large amount of energy, subtract
Few economic loss is reported to obtain considerable benefit.
Utility model content
The purpose of the utility model is to provide a kind of gasoline recovery plants, and with structure, simple, safe operation, uses this dress
The pollution that can effectively reduce waste oil to atmosphere is set, the utilization rate of gasoline is improved, it is energy saving, economic loss is reduced, thus
It is reported to considerable benefit, solves deficiency in the prior art.
To achieve the above object, the utility model provides the following technical solutions: a kind of gasoline recovery plant, including distillation
Case, cooling cylinder, receives bucket at branch pipe still head;The distillation case includes feed inlet, steam pipe, blowdown hydraulic fluid port, distillation mouth, distillation
Side is feed inlet above case, above the other side be distillation mouth, below side be blowdown hydraulic fluid port, distill case in be a steam
Pipe, two nozzles of steam pipe extend to outside distillation case, and two layers of exclusion device is contained in feed inlet, and the exclusion device includes sea
Continuous layer, active carbon layer, above one layer be spongy layer, below one layer be active carbon layer;The branch pipe still head is 3 interface heads,
The first interface of branch pipe still head is equipped with thermometer, and is seal, and the distillation mouth on second interface connection distillation case, third connects
Mouth passes through the condenser pipe on conduit connection cooling cylinder;The cooling cylinder includes the mouth of a river from the beginning A, the mouth of a river from the beginning B, condenser pipe, condensation
One jiao is the mouth of a river from the beginning A above case, is diagonally another the mouth of a river from the beginning B below, is condenser pipe in cooling cylinder, two of condenser pipe
Nozzle extends to outside cooling cylinder, the third interface of nozzle connecting branch still head above condenser pipe, and nozzle below, which connects, to be received
The conduit of bucket;The bucket that receives includes a conduit, the conduit connection condenser pipe for receiving bucket upper end.
Preferably, point-blank, third interface is branch pipe for the first interface of the branch pipe still head and second interface
Interface, obliquely.
Preferably, the mercury head of the thermometer is placed on branch pipe still head third interface.
Preferably, the steam pipe, condenser pipe are all multilayer bend cycles structures.
Preferably, the tap water in the cooling cylinder is flowed into from the mouth of a river from the beginning B, is flowed out from the mouth of a river from the beginning A.
Part is not directed in the device to be the same as those in the prior art or can be realized by using the prior art.
Compared with prior art, the beneficial effects of the utility model are as follows: a kind of gasoline recovery plant, distillation cascade and condensation
Pipe all uses multilayer warp architecture, and distillation cascade makes to distill the waste oil thermally equivalent in case, reduces energy waste;In cooling cylinder from
Water makes the gas in condenser pipe, continues permanent condensation, makes condensation effect more preferably;The thermometer of still head installation, mercury head
Position accurately measures the temperature of retort gas in the intersection of three interfaces;The utility model simple, operation side with structure
Just, safety, can effectively reduce pollution of the waste oil to atmosphere using the present apparatus, improve the utilization rate of gasoline, energy saving, reduce
Economic loss is reported to obtain considerable benefit.
Detailed description of the invention
Upon reading the detailed description of non-limiting embodiments with reference to the following drawings, other spies of the utility model
Sign, objects and advantages will become more apparent upon.
Fig. 1 is a kind of gasoline recovery plant schematic diagram;
Figure label explanation: 1 be feed inlet, 2 be sponge, 3 be active carbon, 4 be steam pipe, 5 be distill case, 6 be blowdown
Hydraulic fluid port, 7 be distillation mouth, 8 be branch pipe still head, 9 be thermometer, 10 be condenser pipe, 11 be the mouth of a river from the beginning A, 12 be cooling cylinder, 13
It is the mouth of a river from the beginning B for reception bucket, 14.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment, based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
In the description of the present invention, it should be understood that term " on ", "lower", "front", "rear", "left", "right",
The orientation or positional relationship of the instructions such as "top", "bottom", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
For ease of description the utility model and simplify description, rather than the device or element of indication or suggestion meaning must have it is specific
Orientation, be constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.
Referring to Fig. 1, a kind of gasoline recovery plant, including distillation case 5, branch pipe still head 8, cooling cylinder 12, reception bucket 14;
The distillation case 5 includes feed inlet 1, steam pipe 4, blowdown hydraulic fluid port 6, distillation mouth 7, and side is feed inlet 1 to distillation case 5 above, on
The face other side be distillation mouth 7, below side be blowdown hydraulic fluid port 6, distill case 5 in be a steam pipe 4, steam pipe 4 is that multilayer is curved
Bent loop structure makes to distill the waste oil thermally equivalent in case 5, reduces thermal energy waste, improves efficiency, two nozzles of distillation cascade 4
It extends to outside distillation case 5, contains two layers of exclusion device in the feed inlet 1, the exclusion device includes spongy layer 2, active carbon
Layer 3, above one layer be spongy layer 2, below one layer be active carbon layer 3, filter out the object block impurity in waste oil;The branch pipe distillation
First 8 have 3 interface heads, and point-blank, third interface is branch pipe interface to two interface heads, and has gradient, and branch pipe steams
The first interface for evaporating first 8 is equipped with thermometer 9, and is seal, and the mercury head of thermometer 9 is placed on 8 third of branch pipe still head and connects
At mouthful, the temperature of retort gas is accurately measured, so that gas temperature is maintained at 70 degree or more, second interface connection is distilled on case 5
Distillation mouth 7, branch pipe still head 8 third interface connection cooling cylinder 12 on condenser pipe 10;The cooling cylinder 12 includes originally
Mouth of a river A11, the mouth of a river from the beginning B14, condenser pipe 10, cooling cylinder 12 above one jiao be the mouth of a river from the beginning A11, be diagonally another below from
Carry out mouth of a river B14, the tap water in cooling cylinder 12 is flowed into from the mouth of a river from the beginning B14, is flowed out from the mouth of a river from the beginning A11, is in cooling cylinder 12
Condenser pipe 10, condenser pipe 10 are multilayer bend cycles structures, reach condensation effect most preferably, and two nozzles of condenser pipe 10 extend
To outside cooling cylinder 12, an interface of nozzle connecting branch still head 8 above condenser pipe 10, nozzle connection below receives bucket 13
Conduit;The reception bucket 13 includes a conduit, receives 13 upper end of bucket and connects a conduit, connects condenser pipe 10.
In summary: a kind of gasoline recovery plant, when which works, waste oil is flowed into from feed inlet 1, is passed through
The article impurity of spongy layer 2, active carbon layer 3 filtered out in waste oil flows into distillation case 5, and volume must not exceed distillation case 5
2/3rds, steam pipe 4 carries out being evenly heated boiling, and gas enters branch pipe still head 8, by mouth of pipe flow into condenser pipe 10 into
Row is cooled to liquid, flows into and receives in bucket 14;There is structure to be simple and convenient to operate, is safe for the utility model, can using the present apparatus
The effective pollution for reducing waste oil to atmosphere, improves the utilization rate of gasoline, energy saving, economic loss is reduced, so that obtaining can
The benefit of sight is reported, and solves deficiency in the prior art.
The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above, for
For those skilled in the art, it is clear that the present invention is not limited to the details of the above exemplary embodiments, and without departing substantially from this
In the case where the spirit or essential attributes of utility model, the utility model can be realized in other specific forms;Therefore, no matter
From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the utility model is by institute
Attached claim rather than above description limit, it is intended that will fall within the meaning and scope of the equivalent elements of the claims
All changes are embraced therein, and should not treat any reference in the claims as limiting related right
It is required that.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (5)
1. a kind of gasoline recovery plant, it is characterised in that: including distillation case (5), branch pipe still head (8), cooling cylinder (12), receive
Bucket (13);The distillation case (5) includes feed inlet (1), steam pipe (4), blowdown hydraulic fluid port (6), distillation mouth (7), is distilled on case (5)
Face side is feed inlet (1), above the other side be distillation mouth (7), below side be blowdown hydraulic fluid port (6), distillation case (5) in be one
A steam pipe (4), two nozzles of steam pipe (4) extend to distillation case (5) outside, and two layers of removal of impurities is contained in the feed inlet (1)
Device, the exclusion device include spongy layer (2), active carbon layer (3), above one layer be spongy layer (2), below one layer be activity
Layer of charcoal (3);The branch pipe still head (8) is 3 interface heads, and the first interface of branch pipe still head (8) is equipped with thermometer (9), and
For seal, the distillation mouth (7) on case (5) is distilled in the connection of second interface head, and third interface passes through conduit and connects cooling cylinder (12)
On condenser pipe (10);The cooling cylinder (12) includes the mouth of a river from the beginning A(11), the mouth of a river from the beginning B(14), condenser pipe (10), condensation
Case (12) above one jiao be the mouth of a river from the beginning A(11), be diagonally another the mouth of a river from the beginning B(14 below), be cold in cooling cylinder (12)
Solidifying pipe (10), two nozzles of condenser pipe (10) extend to cooling cylinder (12) outside, and nozzle connecting branch steams condenser pipe (10) above
The third interface of head (8) is evaporated, nozzle connection below receives the conduit of bucket (13);The reception bucket (13) includes a conduit,
A conduit of bucket (13) upper end is received, is connected condenser pipe (10).
2. a kind of gasoline recovery plant according to claim 1, it is characterised in that: the first of the branch pipe still head (8)
Point-blank, third interface is branch pipe interface, obliquely for interface and second interface.
3. a kind of gasoline recovery plant according to claim 1, it is characterised in that: the mercury head of the thermometer (9) is put
Set the third interface in branch pipe still head (8).
4. a kind of gasoline recovery plant according to claim 1, it is characterised in that: the steam pipe (4), condenser pipe (10)
It is all multilayer bend cycles structure.
5. a kind of gasoline recovery plant according to claim 1, it is characterised in that: the interior the mouth of a river from the beginning of the cooling cylinder (12)
B(14) it is water inlet, the mouth of a river from the beginning A(11) it is water outlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820646744.4U CN208471997U (en) | 2018-05-03 | 2018-05-03 | A kind of gasoline recovery plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820646744.4U CN208471997U (en) | 2018-05-03 | 2018-05-03 | A kind of gasoline recovery plant |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208471997U true CN208471997U (en) | 2019-02-05 |
Family
ID=65220007
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820646744.4U Active CN208471997U (en) | 2018-05-03 | 2018-05-03 | A kind of gasoline recovery plant |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208471997U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110102076A (en) * | 2019-04-28 | 2019-08-09 | 朱福才 | A kind of automobile remnants gasoline recovery plant |
-
2018
- 2018-05-03 CN CN201820646744.4U patent/CN208471997U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110102076A (en) * | 2019-04-28 | 2019-08-09 | 朱福才 | A kind of automobile remnants gasoline recovery plant |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203131794U (en) | Highly efficient system for recycling heat energy and water resource of sewage continuously discharged from boiler | |
CN102249461A (en) | Supercritical water oxidation treatment system for high-salt high-chlorine organic wastewater | |
CN208471997U (en) | A kind of gasoline recovery plant | |
CN101423247A (en) | Method for removing vanadium impurity in titanic chloride by forced assisted-circulation heating | |
CN201715885U (en) | Wastewater heat recovering device | |
CN203360034U (en) | Vacuum distillation type sea water desalting equipment | |
CN207793187U (en) | A kind of amine liquid regenerative system applied to Floating Liquefied Natural Gas facility | |
CN213357465U (en) | Bamboo juice collecting device for bamboo carbonization forming and dry distillation equipment | |
CN211289994U (en) | Waste heat recovery system | |
CN203249525U (en) | Heat pipe type organic working medium falling film evaporator utilizing low temperature exhaust heat | |
CN104163461B (en) | A kind of novel water treatment purifier | |
CN209431393U (en) | The system of condensed water is recycled in a kind of gas washing in SA production | |
CN210448129U (en) | Online descaling methanol-water separation system in low-temperature methanol washing process | |
CN107598111A (en) | A kind of continuous casting cooling Water Sproading and afterheat utilizing system | |
CN207435084U (en) | A kind of compact distillation sea water desalting device | |
CN210813998U (en) | Rectification separation system | |
CN209508152U (en) | A kind of material filling type coke tar distillation tower | |
CN208038048U (en) | Dilute sulfuric acid MVR couples freeze concentration system | |
CN202297297U (en) | Condensate water purifying and recovering device for industrial boiler | |
CN207356849U (en) | A kind of NMP gas recovery systems | |
CN207050492U (en) | A kind of My heat recovery system of sewage | |
CN202358928U (en) | Trichlorosilane synthesis gas washing tower | |
CN220552300U (en) | Steam condensate heat energy recovery system | |
CN213266124U (en) | Portable seawater desalination equipment | |
CN216243607U (en) | Fractionating tower liquid nitrogen recovery system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |