CN208032232U - Integrated multiphase extracts repair system - Google Patents
Integrated multiphase extracts repair system Download PDFInfo
- Publication number
- CN208032232U CN208032232U CN201820273453.5U CN201820273453U CN208032232U CN 208032232 U CN208032232 U CN 208032232U CN 201820273453 U CN201820273453 U CN 201820273453U CN 208032232 U CN208032232 U CN 208032232U
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- China
- Prior art keywords
- gas
- liquid
- process chamber
- liquid phase
- pipeline
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- 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.)
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- 239000000284 extract Substances 0.000 title claims description 9
- 239000007791 liquid phase Substances 0.000 claims abstract description 35
- 239000007788 liquid Substances 0.000 claims abstract description 34
- 238000000034 method Methods 0.000 claims abstract description 33
- 239000012071 phase Substances 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 12
- 238000001179 sorption measurement Methods 0.000 claims description 11
- 239000003463 adsorbent Substances 0.000 claims description 9
- 238000002955 isolation Methods 0.000 claims description 8
- 230000010354 integration Effects 0.000 claims 4
- 239000003610 charcoal Substances 0.000 claims 1
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 38
- 238000000926 separation method Methods 0.000 description 10
- 238000000605 extraction Methods 0.000 description 7
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 238000003911 water pollution Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
Abstract
The utility model is related to mask technical fields,Refer in particular to integrated multiphase extracting repair system,Including system body,WKA water and gas dual-purposes are equipped with outside the system body to pump,The inside of the system body includes mixing chamber,Gas phase treatment room,Liquid phase process chamber,SP gas-liquid separators and collecting chamber,The WKA water and gas dual-purposes pump is connect with mixing chamber by pipeline,The mixing chamber is connect with SP gas-liquid separators by pipeline,The side of the SP gas-liquid separators is equipped with gas phase treatment room,The lower section of the SP gas-liquid separators is equipped with liquid phase process chamber,The gas phase treatment room and liquid phase process chamber are fixedly connected with SP gas-liquid separators by pipeline,The lower section of the liquid phase process chamber is equipped with collecting chamber,The collecting chamber is fixedly connected with liquid phase process chamber by pipeline,The SP gas-liquid separators of system body being internally provided with,Effectively gas and liquid can be detached,To bring great convenience to extracting.
Description
Technical field
The utility model is related to extraction technique fields, refer in particular to integrated multiphase extracting repair system.
Background technology
With China's industrialization development, pollution is also increasingly severe, wherein be to the pollution effect of water it is very big, for
People's lives bring great harm.More and more extraction and separation technologies have been applied in the processing to pollutant,
In have a water pollution, gaseous contamination, but is more individually to handle water pollution and gaseous contamination now causes
Trouble ignores that the harm of gaseous contamination when handling water pollution, from being unable to that the effect of extraction is fully achieved, and also it is existing
Extracting there is also some problems, extraction effect is not fine, thus causes the various troubles of people when in use.
Utility model content
In view of the above problems, the utility model provides integrated multiphase extracting repair system, in the inside of system body
The SP gas-liquid separators being equipped with, can effectively detach gas and liquid, to bring great convenience to extracting；
It is equipped with condenser pipe and activated carbon adsorption layer in gas phase treatment chamber interior, can be more preferably stripped faster so that extracting
Effect is more ideal；Diatomite layer there are three being set in liquid phase process chamber, can carry out continuous adsorbing separation, improve extracting
Efficiency and the further separation and Extraction of activated carbon adsorption layer.
To achieve the goals above, the technical solution adopted in the utility model is as follows：
Integrated multiphase extracts repair system, including system body, and WKA water and gas dual-purposes are equipped with outside the system body
Pump, the inside of the system body includes mixing chamber, gas phase treatment room, liquid phase process chamber, SP gas-liquid separators and collecting chamber, institute
It states WKA water and gas dual-purposes pump to connect by pipeline with mixing chamber, the mixing chamber is connect with SP gas-liquid separators by pipeline, described
The side of SP gas-liquid separators is equipped with gas phase treatment room, and the lower section of the SP gas-liquid separators is equipped with liquid phase process chamber, the gas
Phase processor room and liquid phase process chamber are fixedly connected with SP gas-liquid separators by pipeline, and the lower section of the liquid phase process chamber is equipped with
Collecting chamber, the collecting chamber are fixedly connected with liquid phase process chamber by pipeline.
Furthermore, the gas phase treatment room is internally provided with condenser pipe, and the condenser pipe passes through with gas phase treatment room
Fixed frame is fixedly connected, and one end of the condenser pipe is connected to pipeline, and the other end of the condenser pipe is equipped with exhaust pipe, the row
The bottom of tracheae one end is equipped with Isolation net cover, and the lower section of the Isolation net cover is equipped with activated carbon adsorption layer, the activated carbon adsorption
Floor and the inner wall of gas phase treatment room bond.
Furthermore, diatomite layer, the diatomite layer and liquid there are three being set above the liquid phase inner treatment chamber
The inner wall of phase processor room bonds, and the lower section of the diatomite layer is equipped with adsorbent layer, and the bottom of the adsorbent layer is equipped with strainer,
The strainer is bonded with adsorbent layer, and is fixedly connected with liquid phase process chamber.
Furthermore, the bottom side of the gas phase treatment room and the liquid phase process chamber is equipped with gate valve.
Furthermore, the side of the pipeline is equipped with gate valve.
The utility model advantageous effect：
1. in the SP gas-liquid separators of system body being internally provided with, effectively gas and liquid can be detached,
To bring great convenience to extracting；
2. being equipped with condenser pipe and activated carbon adsorption layer in gas phase treatment chamber interior, can more preferably be stripped faster,
So that the effect of extracting is more ideal；
3. being set in liquid phase process chamber, there are three diatomite layers, can carry out continuous adsorbing separation, improve extracting
Efficiency and the further separation and Extraction of activated carbon adsorption layer.
Description of the drawings
Fig. 1 is Tthe utility model system agent structure schematic diagram；
Fig. 2 is the utility model gas phase treatment cell structure schematic diagram；
Fig. 3 is the utility model liquid phase process chamber configurations schematic diagram.
1. system body；2. gas phase treatment room；3.SP gas-liquid separators；4. mixing chamber；5.WKA water and gas dual-purposes pump；6.
Valve；7. pipeline；8. collecting chamber；9. liquid phase process chamber；10. adsorbent layer；11. activated carbon adsorption layer；12. condenser pipe；13. exhaust
Pipe；14. Isolation net cover；15. strainer；16. diatomite layer.
Specific implementation mode
The technical solution of the utility model is illustrated with embodiment below in conjunction with the accompanying drawings.
As shown in Figure 1 to Figure 3, integrated multiphase described in the utility model extracts repair system, including system body 1, institute
State the outside of system body 1 and be equipped with WKA water and gas dual-purposes and pump 5, the inside of the system body 1 include mixing chamber 4, gas phase treatment room 2,
Liquid phase process chamber 9, SP gas-liquid separators 3 and collecting chamber 8, the WKA water and gas dual-purposes pump 5 are connect with mixing chamber 4 by pipeline 7,
The mixing chamber 4 is connect with SP gas-liquid separators 3 by pipeline 7, and the side of the SP gas-liquid separators 3 is equipped with gas phase treatment room
2, the lower sections of the SP gas-liquid separators 3 is equipped with liquid phase process chamber 9, the gas phase treatment room 2 and liquid phase process chamber 9 with SP gas
Liquid/gas separator 3 is fixedly connected by pipeline 7, and the lower section of the liquid phase process chamber 9 is equipped with collecting chamber 8.The above constitutes this reality
With novel basic structure.
The utility model uses such structure setting, and being equipped with WKA water and gas dual-purposes by 1 outside of the system body pumps 5,
The inside of the system body 1 includes mixing chamber 4, gas phase treatment room 2, liquid phase process chamber 9, SP gas-liquid separators 3 and collecting chamber
8, WKA water and gas dual-purposes pump 5 collects waste water and exhaust gas, and the WKA water and gas dual-purposes pump 5 is connect with mixing chamber 4 by pipeline 7, is led to
Piping 7 is transferred in mixing chamber, and the mixing chamber 4 is connect with SP gas-liquid separators 3 by pipeline 7, mixing chamber 4 by waste water and
Exhaust gas is transferred to the SP gas-liquid separators 3 by pipeline, and SP gas-liquid separators 3 detach gas and liquid, pass through pipe
Liquids and gases after separation are transferred to liquid phase process chamber 9 and gas phase treatment room 2 by road 7 respectively, and liquid phase process chamber 9, which will pass through, to be taken out
Water from after is transferred to collecting chamber 8.
More specifically, the gas phase treatment room 2 is internally provided with condenser pipe 12, the condenser pipe 12 and gas phase treatment room
2 are fixedly connected by fixed frame, exhaust gas be introduced directly into condenser pipe 12 through absorption, absorption, solution plate, separation, it is recyclable valuable
Organic matter, the other end of the condenser pipe 12 is equipped with exhaust pipe 13, and also some exhaust gas will pass through exhaust pipe 13, the exhaust
The bottom of 13 one end of pipe is equipped with Isolation net cover 14, after Isolation net cover 14 carries out a degree of separation, the Isolation net cover 14
Lower section be equipped with activated carbon adsorption layer 11, the activated carbon adsorption layer 11 can carry out absorption exhaust gas, leave valuable gas.
More specifically, the top inside the liquid phase process chamber 9 is set there are three diatomite layer 16, three diatomite layers 16
Have the effect of continuously adsorbing pollutant, preferably carries out separation and Extraction, some waste water can stay in liquid phase separation chamber interior, described
The lower section of diatomite layer 16 is equipped with adsorbent layer 10, and the bottom of the adsorbent layer 10 is equipped with strainer 15, can be simultaneously to pollution
Object is absorbed and filter so that the effect of separation is more preferable.
The embodiments of the present invention are described above in association with attached drawing, but the utility model be not limited to it is above-mentioned
Specific implementation mode, the above mentioned embodiment is only schematical, rather than restrictive, the common skill of this field
Art personnel are not departing from the utility model aims and scope of the claimed protection situation under the enlightenment of the utility model
Under, many forms can be also made, these are belonged within the scope of protection of the utility model.
Claims (5)
1. integrated multiphase extracts repair system, including system body (1), it is characterised in that：It is set outside the system body (1)
There are WKA water and gas dual-purposes to pump (5), the inside of the system body (1) includes mixing chamber (4), gas phase treatment room (2), liquid phase processing
Room (9), SP gas-liquid separators (3) and collecting chamber (8), the WKA water and gas dual-purposes pump (5) are connected with mixing chamber (4) by pipeline (7)
It connects, the mixing chamber (4) is connect with SP gas-liquid separators (3) by pipeline (7), and the side of the SP gas-liquid separators (3) is set
There are gas phase treatment room (2), the lower section of the SP gas-liquid separators (3) to be equipped with liquid phase process chamber (9), the gas phase treatment room (2)
It is fixedly connected by pipeline (7) with SP gas-liquid separators (3) with liquid phase process chamber (9), the lower section of the liquid phase process chamber (9)
Equipped with collecting chamber (8), the collecting chamber (8) is fixedly connected with liquid phase process chamber (9) by pipeline (7).
2. integration multiphase according to claim 1 extracts repair system, it is characterised in that：The gas phase treatment room (2)
Be internally provided with condenser pipe (12), the condenser pipe (12) is fixedly connected with gas phase treatment room (2) by fixed frame, the condensation
One end of pipe (12) is connected to pipeline (7), and the other end of the condenser pipe (12) is equipped with exhaust pipe (13), the exhaust pipe (13)
The bottom of one end is equipped with Isolation net cover (14), and the lower section of the Isolation net cover (14) is equipped with activated carbon adsorption layer (11), the work
Property charcoal adsorption layer (11) bonded with the inner wall of gas phase treatment room (2).
3. integration multiphase according to claim 1 extracts repair system, it is characterised in that：The liquid phase process chamber (9)
Internal top is set there are three diatomite layer (16), the inner wall bonding of the diatomite layer (16) and liquid phase process chamber (9), described
The lower section of diatomite layer (16) is equipped with adsorbent layer (10), and the bottom of the adsorbent layer (10) is equipped with strainer (15), the filter
Net (15) is bonded with adsorbent layer (10), and is fixedly connected with liquid phase process chamber (9).
4. integration multiphase according to claim 1 extracts repair system, it is characterised in that：The gas phase treatment room (2)
It is equipped with gate valve (6) with the bottom side of the liquid phase process chamber (9).
5. integration multiphase according to claim 1 extracts repair system, it is characterised in that：The side of the pipeline (7)
It is equipped with gate valve (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820273453.5U CN208032232U (en) | 2018-02-27 | 2018-02-27 | Integrated multiphase extracts repair system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820273453.5U CN208032232U (en) | 2018-02-27 | 2018-02-27 | Integrated multiphase extracts repair system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208032232U true CN208032232U (en) | 2018-11-02 |
Family
ID=63950115
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820273453.5U Expired - Fee Related CN208032232U (en) | 2018-02-27 | 2018-02-27 | Integrated multiphase extracts repair system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208032232U (en) |
-
2018
- 2018-02-27 CN CN201820273453.5U patent/CN208032232U/en not_active Expired - Fee Related
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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: 20181102 |