CN206138948U - Kerosene separation and recovery unit - Google Patents
Kerosene separation and recovery unit Download PDFInfo
- Publication number
- CN206138948U CN206138948U CN201621061140.0U CN201621061140U CN206138948U CN 206138948 U CN206138948 U CN 206138948U CN 201621061140 U CN201621061140 U CN 201621061140U CN 206138948 U CN206138948 U CN 206138948U
- Authority
- CN
- China
- Prior art keywords
- oil
- cooling tower
- kerosene
- oil separator
- separated
- 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
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model relates to a kerosene separation and recovery unit, cooling tower, oil and gas separator and filter including the order setting, air inlet channel qi pipe, air -blower and the workshop of cooling tower are linked together, the gas outlet channel qi pipe of cooling tower is linked together with oil and gas separator's air inlet, oil and gas separator's gas outlet channel qi pipe is linked together with the air inlet of filter, the oil -out of the oil -out of cooling tower, oil and gas separator's oil -out and filter is linked together through oil pipe and recovery oil tank respectively. The utility model discloses structural design is simple, compactness, reasonable, and mixed have the gaseous of kerosene to isolate the kerosene that mixes in the gas through cooling tower completion first order segregate, through oil and gas separator completion grade separation, retrieves to in will reaching the gaseous atmospheric dilution that accords with emission standard, green, it is high -efficient convenient.
Description
Technical field
This utility model is related to a kind of kerosene and separates and retracting device.
Background technology
In the production of fluorine material, such as the production technology of polytetrafluoroethylraw raw material band commonly uses kerosene mixture as propellant,
Kerosene is filled with the air in workshop, if this gas is directly discharged in air, not only contaminated air, and slattern
Kerosene therein.
Utility model content
In view of the deficiencies in the prior art, technical problem to be solved in the utility model is to provide a kind of kerosene and separates and return
Receiving apparatus, not only reasonable in design, and also it is efficiently convenient.
In order to solve above-mentioned technical problem, the technical solution of the utility model is：A kind of kerosene is separated and retracting device, bag
Include cooling tower, gs-oil separator and filter that order is arranged, the air inlet transtracheal of the cooling tower, aerator and workshop
It is connected, the gas outlet transtracheal of the cooling tower is connected with the air inlet of gs-oil separator, the gs-oil separator goes out
QI KOU transtracheal is connected with the air inlet of filter, the oil-out of the cooling tower, the oil-out of gs-oil separator and mistake
Jing oil pipes are connected the oil-out of filter with fuel tank is reclaimed respectively.
Preferably, the gs-oil separator includes outer tube, and the inner chamber top of the outer tube is provided with coarse separation layer, described
In the middle part of the inner chamber of outer tube, center is equipped with inner core, and centrifugal chamber, the inner chamber bottom of the outer tube are formed between the outer tube and inner core
Liquid collecting recess is provided with, the centrifugal chamber Jing liquid collecting recess, inner core are connected to coarse separation layer.
Preferably, the air inlet of the gs-oil separator be arranged on the side wall of outer tube so as to access centrifugal chamber and with centrifugation
Chamber is tangent, and the gas outlet of the gs-oil separator is arranged on the top of coarse separation layer, and the oil-out of the gs-oil separator sets
Put in the bottom of liquid collecting recess.
Preferably, switch valve is provided with the oil-out of the gs-oil separator.
Preferably, spiral cloth is equipped with spiral board to the centrifugation intracavity from top to bottom.
Preferably, the oil-out of the cooling tower is arranged on its bottom.
Preferably, the filter adopts microfilter, and its oil-out is arranged on its bottom.
Compared with prior art, this utility model has the advantages that：This utility model structure design is simple, tight
Gather, rationally, the gas for being mixed with kerosene completes primary separation, completes the second-order separation through gs-oil separator through cooling tower, will
The kerosene mixed in gas is separated, and is reclaimed, and is up to meet the gas of discharge standard and is entered in air, green ring
Protect, it is efficiently convenient.
The utility model is described in more detail with reference to the accompanying drawings and detailed description.
Description of the drawings
Organigrams of the Fig. 1 for this utility model embodiment.
Organigrams of the Fig. 2 for this utility model embodiment gs-oil separator.
In figure：1- cooling towers, 2- gs-oil separators, 21- outer tube, 22- coarse separation layers, 23- inner cores, 24- liquid collecting recesses,
25- spiral boards, 3- filters, 4- tracheas, 5- aerators, 6- oil pipes, 7- reclaim fuel tank.
Specific embodiment
It is that features described above of the present utility model and advantage can be become apparent, special embodiment below, and coordinate accompanying drawing,
It is described in detail below.
As shown in Figure 1 and 2, a kind of kerosene is separated and retracting device, including cooling tower 1, the gs-oil separator 2 of order setting
And filter 3, the air inlet transtracheal 4 of the cooling tower 1, aerator 5 be connected with workshop, the outlet of the cooling tower 1
Mouth transtracheal 4 is connected with the air inlet of gs-oil separator 2, gas outlet transtracheal 4 and the filter 3 of the gs-oil separator 2
Air inlet be connected, the oil-out of the oil-out, the oil-out of gs-oil separator 2 and filter 3 of the cooling tower 1 difference
Jing oil pipes 6 are connected with fuel tank 7 is reclaimed.
In this utility model embodiment, the gs-oil separator 2 includes outer tube 21, and the inner chamber top of the outer tube 21 sets
Coarse separation layer 22 is equipped with, center is equipped with inner core 23 in the middle part of the inner chamber of the outer tube 21, between the outer tube 21 and inner core 23
Centrifugal chamber is formed, the inner chamber bottom of the outer tube 21 is provided with liquid collecting recess 24, the centrifugal chamber Jing liquid collecting recess 24, inner core 23
It is connected to coarse separation layer 22；The structure of the coarse separation layer 22 is close with the structure of existing coalescing separator or similar.
In this utility model embodiment, the air inlet of the gs-oil separator 2 be arranged on the side wall of outer tube 21 so as to
Access centrifugal chamber is simultaneously tangent with centrifugal chamber, and the gas outlet of the gs-oil separator 2 is arranged on the top of coarse separation layer 22, described
The oil-out of gs-oil separator 2 is arranged on the bottom of liquid collecting recess 24.
In this utility model embodiment, at the oil-out of the gs-oil separator 2, switch valve is provided with.
In this utility model embodiment, spiral cloth is equipped with spiral board 25, the eddy flow to the centrifugation intracavity from top to bottom
Gas is rotated down at a high speed by plate 25, and under the influence of centrifugal force, in gas, fine liquid is thrown on barrel and downstream to collection
Liquid recess 24.
In this utility model embodiment, the oil-out of the cooling tower 1 is arranged on its bottom.
In this utility model embodiment, the filter 3 adopts microfilter 3.
Specific work process of the present utility model is as follows：Workshop collected high-temperature gas is pressurizeed by the aerator 5,
Contain substantial amounts of gaseous state kerosene, the liquid kerosene of very small diameter in the high-temperature gas, be subject to when gas is passed through the cooling tower 1
The cooling of room temperature current so as to which middle part gaseous state kerosene condenses into major diameter liquid kerosene, the major diameter liquid kerosene Jing for obtaining
Oil pipe 6 is entered and reclaims fuel tank 7；Remaining is still mixed with substantial amounts of gaseous state kerosene, the gas of the gaseous state kerosene of minute diameter continues
Trachea 4 described in Jing introduces gs-oil separator 2, and gas is introduced into the centrifugal chamber, and in gas, the liquid kerosene of minute diameter is got rid of
To on barrel and downstream to liquid collecting recess 24, gas continues on through inner core 23 and obtains substantial amounts of major diameter liquid into coarse separation layer 22
State kerosene, the major diameter liquid kerosene for obtaining fall to liquid collecting recess 24 in the presence of deadweight, and remaining gas were eventually passed
After filter 3 is separated by filtration, reaches and meet the gas of discharge standard and enter the liquid kerosene Jing oil pipes 6 in air, obtaining and enter back
Fuel tank 7 is received, switch valve is opened after a period of time the kerosene Jing oil pipes 6 in liquid collecting recess 24 is entered into recovery fuel tank 7.
This utility model is not limited to above-mentioned preferred forms, and anyone can be obtained under enlightenment of the present utility model
Go out other various forms of kerosene to separate and retracting device.All impartial changes done according to this utility model claim with
Modification, should all belong to covering scope of the present utility model.
Claims (7)
1. a kind of kerosene is separated and retracting device, it is characterised in that：Cooling tower, gs-oil separator and the mistake arranged including order
Filter, the air inlet transtracheal of the cooling tower, aerator are connected with workshop, gas outlet transtracheal and the oil of the cooling tower
The air inlet of gas separating device is connected, and the gas outlet transtracheal of the gs-oil separator is connected with the air inlet of filter, institute
The oil-out difference Jing oil pipes for stating the oil-out of cooling tower, the oil-out of gs-oil separator and filter are connected with fuel tank is reclaimed
It is logical.
2. kerosene according to claim 1 is separated and retracting device, it is characterised in that：The gs-oil separator is comprising outer
Cylinder, the inner chamber top of the outer tube are provided with coarse separation layer, and in the middle part of the inner chamber of the outer tube, center is equipped with inner core, described outer
Centrifugal chamber is formed between cylinder and inner core, the inner chamber bottom of the outer tube is provided with liquid collecting recess, the centrifugal chamber Jing liquid collecting recess,
Inner core is connected to coarse separation layer.
3. kerosene according to claim 2 is separated and retracting device, it is characterised in that：The air inlet of the gs-oil separator
It is arranged on the side wall of outer tube so as to access centrifugal chamber tangent with centrifugal chamber, the gas outlet of the gs-oil separator is arranged on poly-
The top of knot stratum disjunctum, the oil-out of the gs-oil separator are arranged on the bottom of liquid collecting recess.
4. kerosene according to claim 3 is separated and retracting device, it is characterised in that：The oil-out of the gs-oil separator
Place is provided with switch valve.
5. kerosene according to claim 2 is separated and retracting device, it is characterised in that：It is described that intracavity spiral shell from top to bottom is centrifuged
Rotation is disposed with spiral board.
6. kerosene according to claim 1 is separated and retracting device, it is characterised in that：The oil-out of the cooling tower is arranged
In its bottom.
7. kerosene according to claim 1 is separated and retracting device, it is characterised in that：The filter adopts microporous filter
Device, its oil-out are arranged on its bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621061140.0U CN206138948U (en) | 2016-09-19 | 2016-09-19 | Kerosene separation and recovery unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621061140.0U CN206138948U (en) | 2016-09-19 | 2016-09-19 | Kerosene separation and recovery unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206138948U true CN206138948U (en) | 2017-05-03 |
Family
ID=58618456
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621061140.0U Expired - Fee Related CN206138948U (en) | 2016-09-19 | 2016-09-19 | Kerosene separation and recovery unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206138948U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113036255A (en) * | 2021-02-26 | 2021-06-25 | 广东邦普循环科技有限公司 | Method for preparing silicon-carbon composite material by using waste lithium ion battery cathode and application |
-
2016
- 2016-09-19 CN CN201621061140.0U patent/CN206138948U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113036255A (en) * | 2021-02-26 | 2021-06-25 | 广东邦普循环科技有限公司 | Method for preparing silicon-carbon composite material by using waste lithium ion battery cathode and application |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170503 Termination date: 20190919 |