CN207871611U - A kind of solvent separation unit - Google Patents
A kind of solvent separation unit Download PDFInfo
- Publication number
- CN207871611U CN207871611U CN201721684302.0U CN201721684302U CN207871611U CN 207871611 U CN207871611 U CN 207871611U CN 201721684302 U CN201721684302 U CN 201721684302U CN 207871611 U CN207871611 U CN 207871611U
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- Prior art keywords
- chamber
- overflow
- solvent
- plate
- separation unit
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0211—Separation of non-miscible liquids by sedimentation with baffles
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- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a kind of solvent separation unit, including solvent recovery case, overflow chamber, separation chamber and reservoir chamber；Separation chamber's antetheca top is arranged with mixed liquor import, and the reservoir chamber is equipped with discharge outlet, and the solvent recovery case side wall is equipped with solvent outlet；The overflow chamber and separation chamber, reservoir chamber are separated by the first overflow plate, and the solvent recovery case and overflow chamber are separated by the second overflow plate, and the separation chamber and the reservoir chamber are separated by separating plate；First overflow plate is equipped with overflow port, the overflow port connection overflow chamber and separation chamber；Second overflow plate is open equipped with overflow chamber, overflow chamber's open communication solvent recovery case and overflow chamber；The separating plate is equipped with water passage, and the height of the water passage is less than the overflow port.Solvent separation unit provided by the utility model is simple in structure, and cost is relatively low, can preferably detach water phase and organic phase.
Description
Technical field
The utility model is related to VOCs treatment field, especially a kind of solvent separation unit.
Background technology
Major part Chemical Manufacture producer can all generate tail gas in process of production at present, in order not to pollute air, be required for
The tail gas that it is produced is handled, then could be emptied, however at present in the Chemical Manufacture producer of some organics, they
The tail gas of generation is often with a large amount of low-boiling-point organic compound, however the tail gas absorbing system that they use but can not be effective
These organic matters are recycled, and have been exhausted directly in air, bring atmosphere pollution, while also resulting in the waste of material.
Carbon adsorption is most widely used recovery technology, and principle is the porous structure using adsorbent, will be discarded
In VOC captures, the organic exhaust gas containing VOC is made into VOC absorption by active-carbon bed, exhaust gas is purified and is discharged into air
In.After carbon adsorption reaches saturation, desorption and regeneration is carried out to the carbon bed of saturation；It is passed through vapor to release VOC strippings, and and water
Steam forms vapour mixture, leaves adsorbent bed together；It is liquid with condenser cooling steam mixture, is then detached again
Recycling.
And organic phase and water phase are certainly existed in mixture liquid, the separation of organic phase and water phase is also certainly existed, if making
It is obviously uneconomical with rectifying column, thus require a kind of organic phase be mixed with water close liquid separating effect it is preferable, split-phase speed
Comparatively fast, solvent separation unit simple in structure.
Utility model content
In view of the deficiencies of the prior art, the utility model aim is to provide a kind of solvent separation unit.
In order to solve the above technical problems, the utility model provides a kind of solvent separation unit, including solvent recovery case, overflow
Room, separation chamber and reservoir chamber；Separation chamber's antetheca top is arranged with mixed liquor import, and the reservoir chamber is equipped with discharge outlet,
The solvent recovery case side wall is equipped with solvent outlet；The overflow chamber and separation chamber are separated by the first overflow plate, described molten
Agent recycling bins and overflow chamber are separated by the second overflow plate, and the separation chamber and the reservoir chamber are separated by separating plate；It is described
First overflow plate is equipped with overflow port, the overflow port connection overflow chamber and separation chamber；Second overflow plate is equipped with overflow
Room is open, overflow chamber's open communication solvent recovery case and overflow chamber；The separating plate be equipped be connected to the separation chamber and
The height of the water passage of reservoir chamber, the water passage is less than the overflow port.
Preferably, the separation chamber is equipped with the first baffle plate and the second baffle plate；First baffle plate is equipped with first
Solution channel is crossed, second baffle plate is equipped with second and crosses solution channel, first baffle plate, the second baffle plate and separation
Plate is set gradually.
Preferably, the first baffle plate number is 1-5；The second baffle plate number is 1-5.
Preferably, the solvent separation unit further includes waste gas recovery mouth.
Preferably, solvent recovery case is equipped with first liquid level gauge interface and second liquid level gauge interface, the first liquid level gauge
Interface is set to solvent recovery case lower half portion, and the second liquid level gauge interface is set to solvent recovery case top half.
Preferably, the overflow port is equipped with overflow erosion control cover.
Preferably, the mixed liquor import is equipped with impingement baffle.
Preferably, the solvent separation unit further includes manhole.
Preferably, the top of the separating plate connects the top of the solvent separation unit, and the water passage is set to
The bottom of the separating plate.
Preferably, the separation chamber is equipped with thermometer boss.
Preferably, guiding gutter is equipped in the reservoir chamber, the guiding gutter connects the discharge outlet.
Solvent separation unit provided by the utility model is simple in structure, and cost is relatively low, can preferably detach water phase and have
Machine phase.
Description of the drawings
Fig. 1 provides the schematic front view of solvent separation unit for the utility model；
Fig. 2 provides the schematic top plan view of solvent separation unit for the utility model；
Fig. 3 provides the left view schematic diagram of solvent separation unit for the utility model.
Specific implementation mode
Technical solutions of the utility model work is further retouched in detail in the following with reference to the drawings and specific embodiments with reference to figure 1-3
It states, so that those skilled in the art can be better understood from the utility model and can be practiced, but illustrated embodiment is not made
For the restriction to the utility model.
With reference to figure 1-3, the present embodiment provides a kind of solvent separation units, including solvent recovery case 1, overflow chamber 2, separation chamber
3 and reservoir chamber 4；3 antetheca top of separation chamber is arranged with mixed liquor import 31, and reservoir chamber 4 is equipped with discharge outlet 32, solvent recovery case
1 side wall is equipped with solvent outlet 11.Organic mixed solvent containing water phase and organic phase enters separation chamber 3 from mixed liquor import 31
In, carry out water phase and organic phase separation.Water phase after separation is discharged through discharge outlet 32, and organic phase flows into overflow chamber 2, then flows into
In solvent recovery case 1, recycled finally by solvent outlet 11.Overflow chamber 2 and separation chamber 3 are separated by the first overflow plate 33, molten
Agent recycling bins 1 and overflow chamber 2 are separated by the second overflow plate 34, and separation chamber 3 and reservoir chamber 4 are separated by separating plate 35；First
Overflow plate 33 is equipped with overflow port 331, and overflow port 331 is connected to overflow chamber 2 and separation chamber 3；Second overflow plate 34 is equipped with overflow
Room opening 341,341 connection solvent recovery case 1 of overflow chamber's opening and overflow chamber 2；Separating plate 35 is equipped with connection separation chamber 3 and storage
The height of the water passage 351 of hydroecium 4, water passage 351 is less than overflow port 331.Specifically, the top connection of separating plate 35
The top of solvent separation unit, water passage 351 are set to the bottom of separating plate 35.Organic mixing containing water phase and organic phase
Solvent enters from mixed liquor import 31 in separation chamber 3, under the action of separating plate 35, is located at the water phase of organic mixed solvent lower layer
It flows into reservoir chamber 4 through water passage 351, and is discharged through discharge outlet 32；Organic phase positioned at organic mixed solvent lower layer upper layer
It flows into overflow chamber 2, is then entered in recycling bins 1 by overflow chamber's opening 341, finally by solvent outlet through overflow port 331
11 recycling
Referring to figs. 2 and 3, in a preferred embodiment, separation chamber 3 is equipped with the first baffle plate 36 and the second baffle plate 37；The
One baffle plate 36 is equipped with first and crosses solution channel 361, and the second baffle plate 37 is equipped with second and crosses solution channel 371, mixed liquor
Import 31, the first baffle plate 36, the second baffle plate 37 and separating plate 35 are set gradually.Organic mixing containing water phase and organic phase
Solvent enters from mixed liquor import 31 in separation chamber 3.Under the blocking of the first baffle plate 36, organic mixed solvent crosses solution from first
Channel 361 flows to the second baffle plate 37, and crossing solution channel 371 by second under the blocking of the second baffle plate 37 flows to separating plate 35,
Because of the effect of the first baffle plate 36 and the second baffle plate 37, organic mixed solvent flowing velocity slows down, organic mixed solvent
Organic phase and water phase are gradually layered before flowing to separating plate 35, and organic phase and water phase are carried out after flowing to water passage 351
Separation, the water phase of lower layer flows by water passage 351 in reservoir chamber 4, and the organic phase on upper layer flows into overflow chamber through overflow port 331
In 2.
With reference to figure 2, in a preferred embodiment, it is 1-5 to state 36 numbers of the first baffle plate；Second number of baffle plate 37 is 1-
5, in further preferred embodiments, the first baffle plate 36 and the setting of the second baffle plate 37 interval.Rationally the first baffling of setting
The number of plate 36 and the second baffle plate 37 can make organic mixed solvent realize preferable layering.
Further include waste gas recovery mouth 38 in a preferred embodiment with reference to figure 1-3, in further preferred embodiments, exhaust gas
Recovery port 38 may be configured as 2-5, for discharging exhaust gas caused by solvent separation unit.
With reference to figure 1, in a preferred embodiment, solvent recovery case 1 is equipped with first liquid level gauge interface 12 and second liquid level gauge
Interface 13, first liquid level gauge interface 12 are set to 1 lower half portion of solvent recovery case, and second liquid level gauge interface 13 is set to solvent and returns
1 top half of case is received, situation is collected for monitoring the organic phase in solvent recovery case 1.
With reference to figure 1 and Fig. 2, in a preferred embodiment, overflow port 331 is equipped with overflow erosion control cover 332.
Referring to figs. 2 and 3, in a preferred embodiment, mixed liquor import 31 be equipped with impingement baffle 311, to by mixed liquor into
Organic mixed solvents that mouth 31 flows into separation chambers 3 play the role of buffering.
Further include manhole 30 in a preferred embodiment, manhole 30 is set to the top of solvent recovery case 1 with reference to figure 1-3
Portion, for overhauling inside solvent recovery case 1.Further include the second inspection being set in separation chamber 3 in further preferred embodiments
Hole 300 is repaiied, for overhauling inside separation chamber 3.
With reference to figure 1, in a preferred embodiment, separation chamber 3 is equipped with thermometer boss 391, and thermometer boss 391 is set to
3 side wall of separation chamber, for detecting the temperature conditions in separation chamber 3.
Further include guiding gutter 321 in a preferred embodiment, in reservoir chamber 4 with reference to figure 2-3, guiding gutter 321 connects discharge outlet
32。
Solvent separation unit provided by the utility model, because of rational structure setting, can preferably detach water phase and
Organic phase.
It these are only the preferred embodiment of the utility model, it does not limit the scope of the patent of the present invention, every
Equivalent structure or equivalent flow shift made based on the specification and figures of the utility model, is applied directly or indirectly in
Other related technical areas are equally included in the patent within the scope of the utility model.
Claims (10)
1. a kind of solvent separation unit, which is characterized in that including solvent recovery case, overflow chamber, separation chamber and reservoir chamber；Described point
It is arranged with mixed liquor import from room antetheca top, the reservoir chamber is equipped with discharge outlet, and the solvent recovery case side wall is equipped with
Solvent outlet；The overflow chamber and separation chamber are separated by the first overflow plate, and the solvent recovery case and overflow chamber pass through second
Overflow plate separates, and the separation chamber and the reservoir chamber are separated by separating plate；First overflow plate is equipped with overflow port, institute
State overflow port connection overflow chamber and separation chamber；Second overflow plate is open equipped with overflow chamber, overflow chamber's open communication
Solvent recovery case and overflow chamber；The separating plate is equipped with the water passage for being connected to the separation chamber and reservoir chamber, described to cross water
The height in channel is less than the overflow port.
2. solvent separation unit as described in claim 1, which is characterized in that the separation chamber is equipped with the first baffle plate and second
Baffle plate；First baffle plate is equipped with first and crosses solution channel, and second baffle plate is equipped with second and crosses solution channel,
First baffle plate, the second baffle plate and separating plate are set gradually.
3. solvent separation unit as claimed in claim 2, which is characterized in that the first baffle plate number is 1-5；It is described
Second baffle plate number is 1-5.
4. solvent separation unit as described in claim 1, which is characterized in that further include waste gas recovery mouth.
5. solvent separation unit as described in claim 1, which is characterized in that solvent recovery case is equipped with first liquid level gauge interface
With second liquid level gauge interface, the first liquid level gauge interface is set to solvent recovery case lower half portion, and the second liquid level gauge connects
Mouth is set to solvent recovery case top half.
6. solvent separation unit as described in claim 1, which is characterized in that the overflow port is equipped with overflow erosion control cover.
7. solvent separation unit as described in claim 1, which is characterized in that the mixed liquor import is equipped with impingement baffle.
8. solvent separation unit as described in claim 1, which is characterized in that the top of the separating plate connects the solvent point
Top from device, the water passage are set to the bottom of the separating plate.
9. solvent separation unit as described in claim 1, which is characterized in that the separation chamber is equipped with thermometer boss.
10. solvent separation unit as described in claim 1, which is characterized in that guiding gutter is equipped in the reservoir chamber, it is described to lead
Sink connects the discharge outlet.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2017212314244 | 2017-09-22 | ||
| CN201721231424 | 2017-09-22 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207871611U true CN207871611U (en) | 2018-09-18 |
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ID=61773109
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711275358.5A Pending CN107875678A (en) | 2017-09-22 | 2017-12-06 | A kind of solvent separation unit |
| CN201721684302.0U Active CN207871611U (en) | 2017-09-22 | 2017-12-06 | A kind of solvent separation unit |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711275358.5A Pending CN107875678A (en) | 2017-09-22 | 2017-12-06 | A kind of solvent separation unit |
Country Status (1)
| Country | Link |
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| CN (2) | CN107875678A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107875678A (en) * | 2017-09-22 | 2018-04-06 | 广东林顿重工股份有限公司 | A kind of solvent separation unit |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3883903D1 (en) * | 1987-09-24 | 1993-10-14 | Nikolaus Hammerschmitt | Light liquid separator. |
| JPH06319903A (en) * | 1993-05-10 | 1994-11-22 | Kimihiko Okanoe | Mixed solution separator |
| DE102006043468B4 (en) * | 2006-09-15 | 2009-03-26 | Fülling, Rainer, Dr. | Device for preventing odor development and for improving oil separation in oil separation plants operating according to the phase separation principle |
| CN101011635A (en) * | 2006-12-27 | 2007-08-08 | 傅太平 | Solvent recovery-separation apparatus |
| CN201410311Y (en) * | 2009-03-20 | 2010-02-24 | 大连举扬科技有限公司 | Oil-water separating device for oil-gas recovery system |
| CN102210944A (en) * | 2010-04-09 | 2011-10-12 | 张步芳 | Solvent recycling and separating device |
| CN102652884A (en) * | 2012-04-16 | 2012-09-05 | 宜兴市灵人机械有限公司 | Oil-water separation chamber with multi-circuitous channels |
| CN205925051U (en) * | 2016-01-30 | 2017-02-08 | 江西胜富化工有限公司 | Solvent recovery device |
| CN107875678A (en) * | 2017-09-22 | 2018-04-06 | 广东林顿重工股份有限公司 | A kind of solvent separation unit |
-
2017
- 2017-12-06 CN CN201711275358.5A patent/CN107875678A/en active Pending
- 2017-12-06 CN CN201721684302.0U patent/CN207871611U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107875678A (en) * | 2017-09-22 | 2018-04-06 | 广东林顿重工股份有限公司 | A kind of solvent separation unit |
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| Publication number | Publication date |
|---|---|
| CN107875678A (en) | 2018-04-06 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 510000 No. 2, floor 2, type C 1 plant, No. 179, tulaowan village, Nansha street, Nansha District, Guangzhou City, Guangdong Province Patentee after: Guangdong Linton Heavy Industry Co.,Ltd. Address before: 511458 No. 10, Huanshi Avenue North, Nansha District, Guangzhou, Guangdong Patentee before: GUANGDONG LINTON HEAVY INDUSTRY CO.,LTD. |
|
| CP03 | Change of name, title or address | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A solvent separation device Effective date of registration: 20230511 Granted publication date: 20180918 Pledgee: Zhaoqing Rural Commercial Bank Co.,Ltd. Pledgor: Guangdong Linton Heavy Industry Co.,Ltd. Registration number: Y2023980040288 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20230921 Granted publication date: 20180918 Pledgee: Zhaoqing Rural Commercial Bank Co.,Ltd. Pledgor: Guangdong Linton Heavy Industry Co.,Ltd. Registration number: Y2023980040288 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |