CN208406513U - A kind of organic solvent circulator and the active carbon adsorber for being equipped with circulator - Google Patents
A kind of organic solvent circulator and the active carbon adsorber for being equipped with circulator Download PDFInfo
- Publication number
- CN208406513U CN208406513U CN201820471538.4U CN201820471538U CN208406513U CN 208406513 U CN208406513 U CN 208406513U CN 201820471538 U CN201820471538 U CN 201820471538U CN 208406513 U CN208406513 U CN 208406513U
- Authority
- CN
- China
- Prior art keywords
- organic solvent
- chamber
- circulator
- active carbon
- storage chamber
- 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
Links
- 239000003960 organic solvent Substances 0.000 title claims abstract description 118
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 48
- 238000003860 storage Methods 0.000 claims abstract description 30
- 239000007788 liquid Substances 0.000 claims abstract description 29
- 239000003463 adsorbent Substances 0.000 claims abstract description 27
- 239000007921 spray Substances 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000005086 pumping Methods 0.000 claims abstract description 4
- 239000002699 waste material Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000001802 infusion Methods 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- 239000008236 heating water Substances 0.000 claims 1
- 239000012535 impurity Substances 0.000 abstract description 19
- 238000000926 separation method Methods 0.000 abstract description 3
- 238000004821 distillation Methods 0.000 abstract description 2
- 238000011065 in-situ storage Methods 0.000 abstract 1
- 239000002156 adsorbate Substances 0.000 description 10
- 239000007789 gas Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000002912 waste gas Substances 0.000 description 3
- 239000006096 absorbing agent Substances 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000000935 solvent evaporation Methods 0.000 description 2
- 238000001994 activation Methods 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides organic solvent circulator and the active carbon adsorber for being equipped with circulator, organic solvent circulator includes the organic solvent collecting chamber with having heaters, organic solvent collecting chamber is communicated with condenser, and condenser is connected to organic solvent storage chamber by liquid back pipe.The active carbon adsorber for being equipped with circulator includes adsorbent chamber, is provided with circulating pump in adsorbent chamber；The inlet tube of circulating pump extends to organic solvent storage chamber, and the water pumping pipe of circulating pump is connected to the spray head on adsorbent chamber roof.A kind of above-mentioned organic solvent circulator, organic solvent collecting chamber collects the organic solvent for having impurity, then Separation of Organic and impurity by way of distillation, realize organic solvent and impurity separation, finally by the organic solvent after withdrawing deposit be back to organic solvent storage chamber carry out using.When being equipped with that organic solvent contains a large amount of impurities in the active carbon adsorber of circulator, can withdraw deposit organic solvent in situ, and organic solvent is recycled.
Description
Technical field
The utility model relates to a kind of organic solvent circulator and the active carbon of the organic solvent circulator is installed
Absorber, and in particular to one kind can recycle the circulator of organic solvent and the active carbon suction for being equipped with the circulator
Adnexa.
Background technique
In existing exhaust-gas treatment, especially in active carbon activation process, the organic solvent being often required to, You Jirong
Agent, which absorbs, to be needed to be further continued for after handling after exhaust gas using but the circulating treatment procedure of organic solvent is complicated, and need to will be organic molten
Agent taking-up carries out processing of withdrawing deposit elsewhere, and the processing of withdrawing deposit of organic solvent takes time and effort, and increases the labour of staff
Amount.
Utility model content
In order to solve the problems, such as that organic solvent circulating treatment procedure is complicated in the prior art, takes time and effort, the utility model
A kind of organic solvent circulator is provided and the active carbon adsorber of circulator is installed.
A kind of organic solvent circulator provided by the utility model, including organic solvent collecting chamber, organic solvent are collected
Intracavitary setting having heaters, the heater are communicated with condenser by appendix, and the condenser is connected to by liquid back pipe
Organic solvent storage chamber.
Preferably, the heater is made of water-bath heater.It is heated, can be prevented organic molten by water-bath heater
Agent fires, and increases the safety of organic solvent circulator.
Preferably, the organic solvent storage chamber is connected with organic solvent collecting chamber by waste liquid delivery pipe, and waste liquid is defeated
It send and valve and infusion pump is installed on pipe.The organic solvent of impurity is had by infusion pump transport, conevying efficiency is high.
Preferably, the organic solvent storage chamber is connected with organic solvent collecting chamber by waste liquid delivery pipe, You Jirong
Agent collecting chamber is located at organic solvent storage chamber lower part, is provided with valve in waste liquid delivery pipe.By the way that organic solvent collecting chamber is arranged
With the high and low position of organic solvent storage chamber, valve can be opened, is made containing the organic of impurity when organic solvent is impure excessive
Solvent is flowed directly to organic solvent collecting chamber by waste liquid delivery pipe, no setting is required infusion pump, reduces organic solvent circulation dress
The cost set.
Preferably, the condenser is also connected with exhaust pipe.The setting of the exhaust pipe can be easier to wave by boiling point is lower
The exhaust gas of hair drains into other waste gas treatment equipments.
Organic solvent circulator provided by the utility model compared with prior art, has the advantages that
A kind of above-mentioned organic solvent circulator, can be directly mounted in other equipment, organic solvent collecting chamber can be received
Collection has the organic solvent of impurity, then by the processing of the equipment such as heater and condenser, has been separated by way of distillation
Solvent and impurity realize the separation of organic solvent and impurity, the organic solvent after withdrawing deposit finally are back to organic solvent and is deposited
Put chamber carry out using.
The utility model also provides a kind of active carbon adsorber for being equipped with organic solvent circulator, active carbon adsorber
Including adsorbent chamber, the lower part of the adsorbent chamber is provided with air inlet, and the top of adsorbent chamber is provided with exhaust outlet；Setting in adsorbent chamber
Active charcoal storing frame is placed with active carbon in active carbon storing frame；Circulating pump, the setting of adsorbent chamber top are provided in adsorbent chamber
There is spray head；The inlet tube of circulating pump extends to organic solvent storage chamber, and the water pumping pipe of circulating pump is connected to spray head.
Preferably, the lower part of adsorbent chamber is connected with steam generator, and the steam generator includes liquid storage chamber, in liquid storage chamber
It is provided with heating device, the steam generator is also connected with the air blower by dry drum to active carbon.Steam generator generates
Hot steam can be heated by heat steam, hot steam dissolves partial adsorbates object and hot steam is blown three kinds of modes and removed in active carbon
Adsorbate.Hot steam can uniformly be circulated to each aperture of active carbon, and the adsorbate in aperture is dissolved and blown out, and removal is lived
Adsorbate in property charcoal, can be realized regenerating active carbon.
Preferably, it is additionally provided in the adsorbent chamber for the drier that active carbon is dry.The drier can be
The device of similar hair dryer, drier may include air heating chamber, and heating member is arranged in heating chamber, then will be hot by blower
Wind goes out；Drier blows hot gas to active carbon, can remove water, organic solvent evaporation in active carbon.
Active carbon adsorber provided by the utility model compared with prior art, has the advantages that
In the prior art, active carbon need to be generally taken out, then the high-temperature baking in particular device, and then by activated carbon adsorption
Substance removal, operating process is complicated, time-consuming, energy consumption is big, loss is big, and is also easy to produce secondary pollution.In the utility model, nothing
The active carbon in adsorbing regenerator need to be moved, the adsorbate in active carbon can be dissolved into removal by the organic solvent of spray,
The undissolvable pollutant adhered on active carbon can also be scrubbed simultaneously.
Detailed description of the invention
Fig. 1 is each component connection relationship diagram for being equipped with the active carbon adsorber of organic solvent circulator.
1 organic solvent storage chamber；2 organic solvent collecting chambers；3 condensers；4 incinerators；5 adsorbent chambers；6 circulating pumps；7 sprays
Head；8 steam generators；9 driers；10 chimneys.
Specific embodiment
The utility model is described in detail below with reference to Fig. 1.
Embodiment 1
A kind of organic solvent circulator provided in this embodiment, including organic solvent collecting chamber 2, organic solvent collecting chamber
The heater made of water-bath heater is provided in 2.Organic solvent collecting chamber 2 is communicated with condenser 3 by appendix, condensation
3 top of device is provided with exhaust pipe；Condenser 3 is connected to organic solvent storage chamber 1, the organic solvent storage chamber by liquid back pipe
1 is connected with organic solvent collecting chamber 2 by waste liquid delivery pipe, valve and infusion pump is equipped in waste liquid delivery pipe, by defeated
Liquid pump transport has the organic solvent of impurity.
A kind of organic solvent circulator provided in this embodiment, can be directly mounted in other equipment, organic solvent is deposited
Put the organic solvent that 1 memory of chamber is placed in use process.When organic solvent contain impurity it is excessive when, will have by infusion pump first
Solvent is delivered to organic solvent collecting chamber 2；Then by heater heat the organic solvent containing impurity, make organic solvent and
Volatile impurity forms gas and steam, not volatile impurity stay in organic solvent collecting chamber 2；Subsequently organic solvent exists
Liquid is condensed into condenser 3；The organic solvent of last liquid flows back to organic solvent storage chamber 1 and continues to use, and can not condense
Volatile gas drains into other waste gas treatment equipments.
Embodiment 2
A kind of organic solvent circulator provided in this embodiment, including organic solvent collecting chamber 2, organic solvent collecting chamber
The heater made of water-bath heater is provided in 2.Organic solvent collecting chamber 2 is communicated with condenser 3 by appendix, condensation
3 top of device is provided with exhaust pipe；Condenser 3 is connected to organic solvent storage chamber 1, the organic solvent storage chamber by liquid back pipe
1 is connected with organic solvent collecting chamber 2 by waste liquid delivery pipe, and organic solvent collecting chamber 2 is located under organic solvent storage chamber 1
Portion is provided with valve in waste liquid delivery pipe.
A kind of organic solvent circulator provided in this embodiment, can be directly mounted in other equipment, organic solvent is deposited
Put the organic solvent that 1 memory of chamber is placed in use process.When organic solvent contain impurity it is excessive when, first by open valve,
Organic solvent flow to organic solvent collecting chamber 2；Then by heater heat the organic solvent containing impurity, make organic solvent and
Volatile impurity forms gas and steam, not volatile impurity stay in organic solvent collecting chamber 2；Subsequently organic solvent exists
Liquid is condensed into condenser 3；The organic solvent of last liquid flows back to organic solvent storage chamber 1 and continues to use, and can not condense
Volatile gas drains into other waste gas treatment equipments.
Embodiment 3
The present embodiment provides a kind of active carbons for being equipped with the organic solvent circulator as described in embodiment 1 or embodiment 2
Absorber, active carbon adsorber include adsorbent chamber 5, and the lower part of the adsorbent chamber 5 is provided with air inlet, and the top of adsorbent chamber 5 is set
It is equipped with exhaust outlet；It is provided with active carbon storing frame in adsorbent chamber 5, is placed with active carbon in active carbon storing frame.It is set in adsorbent chamber 5
It is equipped with circulating pump 6,5 top of adsorbent chamber is provided with spray head 7.The inlet tube of circulating pump 6 extends to organic solvent storage chamber 1, follows
The water pumping pipe of ring pump 6 is connected to spray head 7.The lower part of adsorbent chamber 5 is connected with steam generator 8, and the steam generator 8 includes
Liquid storage chamber is provided with heating device in liquid storage chamber, and the steam generator 8 is also connected with the air blast by dry drum to active carbon
Machine.
Preferably, it is additionally provided in the adsorbent chamber 5 for the drier 9 that active carbon is dry.The drier 9 can be with
It is the device of similar hair dryer, drier 9 may include air heating chamber, and heating member is arranged in heating chamber, then passes through blower
Hot wind is blown out；Drier 9 blows hot gas to active carbon, can remove water, organic solvent evaporation in active carbon.
In the present embodiment, organic solvent storage chamber 1 is made using circulating pump 6 for organic nature adsorbate not soluble in water
Interior organic solvent cycling elution active carbon removes adsorbate in surface adsorbate and hole；Then pass to the generation of steam generator 8
Hot water and steam blowout active carbon hole in remaining adsorbate；When being provided with drier 9, it is finally passed through the heat of the generation of drier 9
Air is dried, and blows out adsorbate, heated-air drying collective effect for active carbon by organic solvent dissolution, hot water and steam physics
Regeneration.Regenerating active carbon process is not necessarily to the active carbon in mobile adsorbing regenerator, and when organic solvent contains a large amount of impurities, can
Original position is withdrawn deposit organic solvent, and organic solvent is recycled.
Certainly, the above description is not intended to limit the present invention, and the utility model is also not limited to the example above,
The variations, modifications, additions or substitutions that those skilled in the art are made in the essential scope of the utility model, are also answered
Belong to the protection scope of the utility model.
Claims (8)
1. a kind of organic solvent circulator, which is characterized in that including organic solvent collecting chamber, be arranged in organic solvent collecting chamber
Having heaters, organic solvent collecting chamber are communicated with condenser by appendix, and the condenser is connected to organic by liquid back pipe
Solvent storage chamber.
2. a kind of organic solvent circulator as described in claim 1, which is characterized in that the heater is by heating water bath
Made of device.
3. a kind of organic solvent circulator as described in claim 1, which is characterized in that the organic solvent storage chamber and have
Solvent collecting chamber is connected by waste liquid delivery pipe, is equipped with valve and infusion pump in waste liquid delivery pipe.
4. a kind of organic solvent circulator as described in claim 1, which is characterized in that the organic solvent storage chamber and have
Solvent collecting chamber is connected by waste liquid delivery pipe, and organic solvent collecting chamber is located at organic solvent storage chamber lower part, and waste liquid is defeated
It send and is provided with valve on pipe.
5. a kind of organic solvent circulator as described in claim 1, which is characterized in that the condenser is also connected with exhaust
Pipe.
6. installing the active carbon adsorber just like claim 1 to 5 any one organic solvent circulator, which is characterized in that
Active carbon adsorber includes adsorbent chamber, and the lower part of the adsorbent chamber is provided with air inlet, and the top of adsorbent chamber is provided with exhaust outlet；
It is provided with active carbon storing frame in adsorbent chamber, is placed with active carbon in active carbon storing frame；It is provided with circulating pump in adsorbent chamber, inhales
Attached chamber top is provided with spray head；The inlet tube of circulating pump extends to organic solvent storage chamber, and the water pumping pipe of circulating pump is connected to
Spray head.
7. being equipped with the active carbon adsorber of circulator as claimed in claim 6, which is characterized in that the lower part of adsorbent chamber connects
It is connected to steam generator, the steam generator includes liquid storage chamber, and heating device, the steam generator are provided in liquid storage chamber
It is also connected with the air blower by dry drum to active carbon.
8. being equipped with the active carbon adsorber of circulator as claimed in claim 6, which is characterized in that in the adsorbent chamber also
It is provided with for the drier that active carbon is dry.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820471538.4U CN208406513U (en) | 2018-04-04 | 2018-04-04 | A kind of organic solvent circulator and the active carbon adsorber for being equipped with circulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820471538.4U CN208406513U (en) | 2018-04-04 | 2018-04-04 | A kind of organic solvent circulator and the active carbon adsorber for being equipped with circulator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208406513U true CN208406513U (en) | 2019-01-22 |
Family
ID=65119511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820471538.4U Expired - Fee Related CN208406513U (en) | 2018-04-04 | 2018-04-04 | A kind of organic solvent circulator and the active carbon adsorber for being equipped with circulator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208406513U (en) |
-
2018
- 2018-04-04 CN CN201820471538.4U patent/CN208406513U/en not_active Expired - Fee Related
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| 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: 20190122 |