CN107158879A - The adjustable activated carbon adsorption/desorption complexes of Wet-dry - Google Patents
The adjustable activated carbon adsorption/desorption complexes of Wet-dry Download PDFInfo
- Publication number
- CN107158879A CN107158879A CN201710409055.1A CN201710409055A CN107158879A CN 107158879 A CN107158879 A CN 107158879A CN 201710409055 A CN201710409055 A CN 201710409055A CN 107158879 A CN107158879 A CN 107158879A
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- desorption
- nitrogen
- activated carbon
- wet
- 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.)
- Pending
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 238000002336 sorption--desorption measurement Methods 0.000 title claims abstract description 26
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 97
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 48
- 238000003795 desorption Methods 0.000 claims abstract description 35
- 238000001179 sorption measurement Methods 0.000 claims abstract description 31
- 239000002912 waste gas Substances 0.000 claims abstract description 30
- 230000008676 import Effects 0.000 claims abstract description 22
- 239000007789 gas Substances 0.000 claims abstract description 20
- 239000003463 adsorbent Substances 0.000 claims abstract description 11
- 238000006073 displacement reaction Methods 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 238000010521 absorption reaction Methods 0.000 claims description 8
- 239000008235 industrial water Substances 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000003610 charcoal Substances 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 238000001514 detection method Methods 0.000 claims description 6
- 239000007792 gaseous phase Substances 0.000 claims description 3
- 239000007791 liquid phase Substances 0.000 claims description 3
- 239000012071 phase Substances 0.000 claims description 3
- 239000008400 supply water Substances 0.000 claims description 2
- 229910001873 dinitrogen Inorganic materials 0.000 claims 1
- 230000009975 flexible effect Effects 0.000 claims 1
- 238000010025 steaming Methods 0.000 claims 1
- 238000000034 method Methods 0.000 description 14
- 230000008569 process Effects 0.000 description 9
- 230000000694 effects Effects 0.000 description 5
- 239000007921 spray Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 206010000369 Accident Diseases 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000037396 body weight Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000003137 locomotive effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40086—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by using a purge gas
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
This application discloses a kind of adjustable activated carbon adsorption/desorption complexes of Wet-dry.The adjustable activated carbon adsorption/desorption complexes of the Wet-dry, including adsorbent equipment, desorption apparatus, control device and some pipelines and valve, the adsorbent equipment includes pneumatic filter, adsorption tanks, main fan and aiutage, the adsorption tanks are provided with exhaust gas inlet, waste gas outlet, nitrogen inlet and nitrogen outlet, the pneumatic filter outlet is connected to exhaust gas inlet by pipeline, the aiutage import is connected to waste gas outlet by pipeline, the main fan is connected between aiutage and waste gas outlet, the nitrogen inlet and nitrogen outlet are connected to desorption apparatus, the desorption apparatus not only can be desorbed but also can be desorbed with steam with nitrogen, each segment pipe is respectively equipped with valve, the valve passes through the control device centralized Control.The adjustable activated carbon adsorption/desorption complexes of the Wet-dry are used using steam and nitrogen as desorption medium.
Description
Technical field
The application is related to exhaust-gas treatment field, and more particularly to a kind of adjustable activated carbon adsorption/desorption of Wet-dry is into suit
Put.
Background technology
Activated carbon has preferable specific surface area and very strong absorption, decolourized and the performance that eliminates the unusual smell, therefore usually by conduct
The adsorbing medium of circulating purification system, to absorb poisonous, the polluter in waste gas, waste water, activated carbon can be with after desorption
It is used for multiple times, is adsorbed and two processes of desorption so existing, adsorption process is as follows：Waste gas removes small outstanding by air cleaner
After floating particles, into the top of adsorption tanks, after charcoal absorption in tank, harmful components are removed, meet the net of discharge standard
Change gas, be discharged into through blower fan in air；Desorption and regeneration process is as follows：After activated carbon has used a period of time, its surface is inhaled
Attached a certain amount of solvent (use time length, depending on the content of body weight and production time length) is, it is necessary to be desorbed
Regeneration, existing desorption apparatus is generally simple dry method desorption or wet method desorption, when desorption apparatus breaks down, do not have it is standby can
Choosing, can only stop being desorbed work.So needing to propose to improve.
The content of the invention
It is existing to overcome it is an object of the invention to provide a kind of adjustable activated carbon adsorption/desorption complexes of Wet-dry
There is the deficiency in technology.
To achieve the above object, the present invention provides following technical scheme：
The embodiment of the present application discloses a kind of adjustable activated carbon adsorption/desorption complexes of Wet-dry,
Including adsorbent equipment, desorption apparatus, control device and some pipelines and valve, the adsorbent equipment includes gas mistake
Filter, adsorption tanks, main fan and aiutage, the adsorption tanks go out provided with exhaust gas inlet, waste gas outlet, nitrogen inlet and nitrogen
Mouthful, the pneumatic filter outlet is connected to exhaust gas inlet by pipeline, and the aiutage import is connected to waste gas by pipeline
Outlet, the main fan is connected between aiutage and waste gas outlet, and the nitrogen inlet and nitrogen outlet are connected to
Desorption apparatus；
The desorption apparatus includes displacement blower fan, circulating fan, First Heat Exchanger, the second heat exchanger, the 3rd heat exchanger, the
Four heat exchangers, drainer, condenser pump, incinerator, nitrogen device and steam unit, the displacement blower fan two ends pass through pipeline respectively
The gaseous phase outlet of nitrogen inlet and drainer is connected to, the liquid-phase outlet of the drainer is connected to the burning by pipeline
Stove, the condenser pump is arranged between the drainer and incinerator, and the circulating fan two ends are connected to by pipeline respectively
Nitrogen outlet and First Heat Exchanger import, the nitrogen device and the 4th heat exchanger import are parallel to the circulated air by pipeline
Between machine and First Heat Exchanger, the outlet of the First Heat Exchanger and the 4th heat exchanger is connected to nitrogen by pipeline respectively and entered
Mouthful, the second heat exchanger import is connected to waste gas outlet by pipeline, and second heat exchanger exit is connected to by pipeline
3rd heat exchanger import, the 3rd heat exchanger exit is connected to drainer gas phase import, second heat exchanger, the 3rd heat exchange
Device and the 4th heat exchanger are by the use of external source as heat transferring medium, and the steam unit is connected to suction by First Heat Exchanger
Attached tank and steam unit；
Each segment pipe is respectively equipped with valve, and the valve passes through the control device centralized Control.
It is preferred that, in the above-mentioned adjustable activated carbon adsorption/desorption complexes of Wet-dry, in the adsorption tanks
Adsorbent is activated carbon.
It is preferred that, in the above-mentioned adjustable activated carbon adsorption/desorption complexes of Wet-dry, at the main fan
In explosion-proof closed environment.
It is preferred that, in the above-mentioned adjustable activated carbon adsorption/desorption complexes of Wet-dry, the nitrogen outlet connects
It is connected to containing oxygen detection.
It is preferred that, in the above-mentioned adjustable activated carbon adsorption/desorption complexes of Wet-dry, pass through the test number
According to also including some Shower taps in the adsorption tanks.
It is preferred that, in the above-mentioned adjustable activated carbon adsorption/desorption complexes of Wet-dry, the locomotive is provided with
Camera, the Shower tap is connected to fire water supply and industrial water source simultaneously.
It is preferred that, in the above-mentioned adjustable activated carbon adsorption/desorption complexes of Wet-dry, the First Heat Exchanger
From the adjustable heat exchanger of temperature.
Compared with prior art, the advantage of the invention is that：The adjustable activated carbon adsorption/desorption of the Wet-dry is into suit
Putting realizes the high efficiency desorption parsing after charcoal absorption.Steam and two kinds of desorption mediums of nitrogen are mutually standby, and system can
It is stronger by property stability, meanwhile, designed by the use of industrial water source and fire water supply as the spray of double-safety, it can be ensured that system
Safety is perfectly safe, and not only treatment effeciency is high for this device, the organic substance that can efficiently go in removing exhaust gas, and the effect of the device is not only
National waste gas emission standard can be reached and operation and maintenance cost is low, security highest.
Brief description of the drawings
, below will be to embodiment or existing in order to illustrate more clearly of the embodiment of the present application or technical scheme of the prior art
There is the accompanying drawing used required in technology description to be briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments described in application, for those of ordinary skill in the art, on the premise of not paying creative work,
Other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 show the operation principle schematic diagram of desorption apparatus in the specific embodiment of the invention.
Fig. 2 show the operation principle schematic diagram that adsorption device is adsorbed in the specific embodiment of the invention.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, detailed retouch is carried out to the technical scheme in the embodiment of the present invention
State, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.Based on the present invention
In embodiment, the every other implementation that those of ordinary skill in the art are obtained on the premise of creative work is not made
Example, belongs to the scope of protection of the invention.
Join shown in Fig. 1 and Fig. 2, the adjustable activated carbon adsorption/desorption complexes of Wet-dry in the present embodiment, including
Adsorbent equipment 1000, desorption apparatus 2000, control device (being not drawn into figure) and some pipelines (non-label in figure) and valve (figure
In non-label), the adsorbent equipment 1000 include pneumatic filter 1010, adsorption tanks 1020, main fan 1030 and aiutage
1040, adsorption tanks 1020 are provided with exhaust gas inlet 1021, waste gas outlet 1022, nitrogen inlet 1023 and nitrogen outlet 1024, gas
The outlet of filter 1010 is connected to exhaust gas inlet 1021 by pipeline, and the import of aiutage 1040 is connected to waste gas outlet by pipeline
1022, main fan 1030 is connected between aiutage 1040 and waste gas outlet 1022, nitrogen inlet 1023 and nitrogen outlet
1024 are connected to desorption apparatus 2000；
The desorption apparatus 2000 includes displacement blower fan 2010, circulating fan 2020, First Heat Exchanger 2030, second and exchanged heat
Device 2040, the 3rd heat exchanger 2050, the 4th heat exchanger 2060, drainer 2070, condenser pump 2080, incinerator 2090, nitrogen dress
2100 and steam unit 2110 are put, displacement blower fan 2010 two ends are connected to nitrogen inlet 1023 and drainer by pipeline respectively
2070 gaseous phase outlet, the liquid-phase outlet of drainer 2070 is connected to incinerator 2090 by pipeline, and condenser pump 2080 is arranged at
Between drainer 2070 and incinerator 2090, the two ends of circulating fan 2020 are connected to nitrogen outlet 1024 and by pipeline respectively
The import of one heat exchanger 2030, nitrogen device 2100 and the import of the 4th heat exchanger 2060 are parallel to the He of circulating fan 2020 by pipeline
Between First Heat Exchanger 2030, the outlet of the heat exchanger 2060 of First Heat Exchanger 2030 and the 4th is connected to nitrogen by pipeline respectively
Import 1023, the import of the second heat exchanger 2040 is connected to waste gas outlet 1022 by pipeline, and the outlet of the second heat exchanger 2040 passes through
Pipeline is connected to the import of the 3rd heat exchanger 2050, and the outlet of the 3rd heat exchanger 2050 is connected to the gas phase import of drainer 2070, second
Heat exchanger 2040, the 3rd heat exchanger 2050 and the 4th heat exchanger 2060 are used as heat transferring medium, steam unit by the use of external source
2110 are connected to adsorption tanks 1020 and steam unit 2110 by First Heat Exchanger 2030；
Each segment pipe is respectively equipped with valve, and valve passes through control device centralized Control.
In the technical scheme, how control device controls a valve to belong to prior art, does not just repeat one by one, the dry and wet two
The high efficiency desorption parsing after charcoal absorption is realized with adjustable activated carbon adsorption/desorption complexes.Steam and nitrogen
Two kinds of desorption mediums are mutually standby, and system reliability stability is stronger, meanwhile, protected by the use of industrial water source and fire water supply as double
The spray design of dangerous formula, it can be ensured that system is perfectly safe safely, not only treatment effeciency is high for this device, can efficiently go in removing exhaust gas
Organic substance, the effect of the device can not only reach national waste gas emission standard and operation and maintenance cost is low, and security is most
It is high.
Further, the adsorbent in adsorption tanks 1020 is activated carbon.
In the technical scheme, adsorbent in adsorption tanks 1020 is that can enter after activated carbon, charcoal absorption harmful substance
Row desorption, i.e., activated carbon can be utilized repeatedly, save the energy.
Further, main fan 1030 is in explosion-proof closed environment.
In the technical scheme, main fan 1030 is in explosion-proof closed environment, and main fan 1030 is directly contacted with waste gas.
Further, nitrogen outlet is connected with containing oxygen detection 1050.
In the technical scheme, nitrogen outlet is connected with containing oxygen detection 1050, useless in using nitrogen displacement adsorption tanks
During gas, by carrying out on-line checking containing oxygen detection, it is ensured that waste gas is completely displaced in adsorption tanks.
Further, some Shower taps 1025 are also included in adsorption tanks 1020.
In the technical scheme, some Shower taps 1025 are also included in adsorption tanks 1020, when occurring unexpected fire accidents,
Can directly it be put out a fire in the very first time, it is to avoid fire expands.
Further, Shower tap 1025 is connected to fire water supply 5000 and industrial water source 6000 simultaneously.
In the technical scheme, Shower tap is connected to fire water supply 5000 and industrial water source 6000, fire water supply simultaneously
5000 design with industrial water source 6000 as the spray of double-safety, it can be ensured that perfectly safe safely during fire extinguishing.
Further, First Heat Exchanger 2030 selects the adjustable heat exchanger of temperature.
In the technical scheme, First Heat Exchanger selects the adjustable heat exchanger of temperature, according to the different waste gas of processing, can adjust
The different temperature of section, accelerates the efficiency of desorption.
Adsorption process：Waste gas is after the pretreatment of pneumatic filter 1010, and adsorption tanks 1020 are in explosion-proof closed main ventilation
The lower negative pressure operation of the effect of machine 1030, activated carbon trapping that organic solvent is adsorbed in tank 1020, adsorbs and concentrates, it is purified after
Waste gas is discharged into air through aiutage 1040.
Desorption process：Charcoal absorption organic matter in adsorption tanks 1020 is reached after saturation state, stops waste gas input.Examine
Consider the device for treating desorption with dry clean nitrogen before the factors such as control desorption process hydrolysis generation, device desorption to be purged
Displacement, displacement blower fan 2010 is opened.The waste gas gone out using nitrogen displacement in the tank body of adsorption tanks 1020, by containing oxygen detection 1050
On-line checking is carried out, when oxygen content is less than setting value 0.1%, ON cycle blower fan 2020, nitrogen is through being connected with high-temperature vapor
First Heat Exchanger 2030 be desorbed by circulating-heating (temperature is adjustable, is individually set according to different VOCS compositions), will be organic
Thing is desorbed from activated carbon, and activated carbon recovers its activity in adsorption tanks, and the high-temp waste gas for during which being desorbed out, which enters, is connected with industry
The second heat exchanger 2040 and the second heat exchanger 2050 of water and chilled water are constantly condensed, organic gas condensing in waste gas extremely
In lime set tank 2070, condensate liquid is delivered in incinerator 2090 by lime set pump 2080, adsorption tanks and pipe after waste gas has been condensed
High temperature nitrogen containing high concentration in road, in the presence of circulating fan 2020, by the 4th heat exchanger 2060 high temperature nitrogen
Closed to be cooled to normal temperature, adsorption tanks desorption is just completed, the input of correspondence nitrogen and output.If there is event in nitrogen device 2010
Barrier, closes nitrogen device.Close the import and export of nitrogen valve of First Heat Exchanger 2030.The steam of steam unit 2100 is through direct
Enter after the heating of one heat exchanger 2030 and steam desorption is carried out in adsorption tanks, blowdown is carried out by unified drainage.
In summary, after the adjustable activated carbon adsorption/desorption complexes of the Wet-dry realize charcoal absorption
High efficiency desorption parsing.Steam and two kinds of desorption mediums of nitrogen are mutually standby, and system reliability stability is stronger, meanwhile, utilize
Industrial water source and fire water supply are designed as the spray of double-safety, it can be ensured that system is perfectly safe safely, and this device is not only
Treatment effeciency is high, and the organic substance that can efficiently go in removing exhaust gas, the effect of the device can not only reach national waste gas emission standard
And operation and maintenance cost is low, security highest.
It should be noted that herein, such as first and second or the like relational terms are used merely to a reality
Body or operation make a distinction with another entity or operation, and not necessarily require or imply these entities or deposited between operating
In any this actual relation or order.Moreover, term " comprising ", "comprising" or its any other variant are intended to
Nonexcludability is included, so that process, method, article or equipment including a series of key elements not only will including those
Element, but also other key elements including being not expressly set out, or also include being this process, method, article or equipment
Intrinsic key element.In the absence of more restrictions, the key element limited by sentence "including a ...", it is not excluded that
Also there is other identical element in process, method, article or equipment including the key element.
Described above is only the embodiment of the application, it is noted that for the ordinary skill people of the art
For member, on the premise of the application principle is not departed from, some improvements and modifications can also be made, these improvements and modifications also should
It is considered as the protection domain of the application.
Claims (7)
1. a kind of adjustable activated carbon adsorption/desorption complexes of Wet-dry, it is characterised in that the Wet-dry adjusting flexible
Property charcoal adsorption/desorption complexes, including adsorbent equipment, desorption apparatus, control device and some pipelines and valve, the absorption
Device includes pneumatic filter, adsorption tanks, main fan and aiutage, and the adsorption tanks are provided with exhaust gas inlet, waste gas outlet, nitrogen
Gas import and nitrogen outlet, the pneumatic filter outlet are connected to exhaust gas inlet by pipeline, and the aiutage import passes through
Pipeline is connected to waste gas outlet, and the main fan is connected between aiutage and waste gas outlet, the nitrogen inlet and nitrogen
Outlet is connected to desorption apparatus；
The desorption apparatus is changed including displacement blower fan, circulating fan, First Heat Exchanger, the second heat exchanger, the 3rd heat exchanger, the 4th
Hot device, drainer, condenser pump, incinerator, nitrogen device and steam unit, the displacement blower fan two ends are connected by pipeline respectively
In nitrogen inlet and the gaseous phase outlet of drainer, the liquid-phase outlet of the drainer is connected to the incinerator, institute by pipeline
State condenser pump to be arranged between the drainer and incinerator, the circulating fan two ends are connected to nitrogen by pipeline respectively and gone out
Mouthful and First Heat Exchanger import, the nitrogen device and the 4th heat exchanger import are parallel to the circulating fan and the by pipeline
Between one heat exchanger, the outlet of the First Heat Exchanger and the 4th heat exchanger is connected to nitrogen inlet by pipeline respectively, described
Second heat exchanger import is connected to waste gas outlet by pipeline, and second heat exchanger exit is connected to the 3rd heat exchange by pipeline
Device import, the 3rd heat exchanger exit is connected to drainer gas phase import, second heat exchanger, the 3rd heat exchanger and the 4th
Heat exchanger is by the use of external source as heat transferring medium, and the steam unit is connected to adsorption tanks and steaming by First Heat Exchanger
Vapour device；
Each segment pipe is respectively equipped with valve, and the valve passes through the control device centralized Control.
2. the adjustable activated carbon adsorption/desorption complexes of Wet-dry according to claim 1, it is characterised in that：It is described
Adsorbent in adsorption tanks is activated carbon.
3. the adjustable activated carbon adsorption/desorption complexes of Wet-dry according to claim 1, it is characterised in that：It is described
Main fan is in explosion-proof closed environment.
4. the adjustable activated carbon adsorption/desorption complexes of Wet-dry according to claim 1, it is characterised in that：It is described
Nitrogen outlet is connected with containing oxygen detection.
5. the adjustable activated carbon adsorption/desorption complexes of Wet-dry according to claim 1, it is characterised in that：It is described
Also include some Shower taps in adsorption tanks.
6. the adjustable activated carbon adsorption/desorption complexes of Wet-dry according to claim 5, it is characterised in that：It is described
Shower tap is connected to fire water supply and industrial water source simultaneously.
7. the adjustable activated carbon adsorption/desorption complexes of Wet-dry according to claim 1, it is characterised in that：It is described
First Heat Exchanger selects the adjustable heat exchanger of temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710409055.1A CN107158879A (en) | 2017-06-02 | 2017-06-02 | The adjustable activated carbon adsorption/desorption complexes of Wet-dry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710409055.1A CN107158879A (en) | 2017-06-02 | 2017-06-02 | The adjustable activated carbon adsorption/desorption complexes of Wet-dry |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107158879A true CN107158879A (en) | 2017-09-15 |
Family
ID=59824516
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710409055.1A Pending CN107158879A (en) | 2017-06-02 | 2017-06-02 | The adjustable activated carbon adsorption/desorption complexes of Wet-dry |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107158879A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109046251A (en) * | 2018-10-09 | 2018-12-21 | 上海汉磊环保科技有限公司 | A kind of activated carbon adsorption detachment assays device |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202169134U (en) * | 2011-07-27 | 2012-03-21 | 山东电力工程咨询院有限公司 | Novel desulphurization accident flue gas spray cooling system |
| CN202724967U (en) * | 2012-05-14 | 2013-02-13 | 武汉旭日华科技发展有限公司 | Tail gas adsorbing device of mixed bed layer |
| CN103585854A (en) * | 2013-10-29 | 2014-02-19 | 嘉园环保股份有限公司 | Technology for recovering and processing organic exhaust gas by activated carbon adsorption and N2 desorption |
| CN203577580U (en) * | 2013-11-20 | 2014-05-07 | 苏州巨联科技有限公司 | Activated carbon adsorption recovery device taking nitrogen as desorption medium |
| JP2015000381A (en) * | 2013-06-17 | 2015-01-05 | 東洋紡株式会社 | Organic solvent recovery system |
| CN206094118U (en) * | 2016-09-19 | 2017-04-12 | 南通海阳节能环保科技有限公司 | An organic waste gas purifier |
| CN206778138U (en) * | 2017-06-02 | 2017-12-22 | 张家港市艾尔环保工程有限公司 | The adjustable activated carbon adsorption/desorption complexes of Wet-dry |
-
2017
- 2017-06-02 CN CN201710409055.1A patent/CN107158879A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202169134U (en) * | 2011-07-27 | 2012-03-21 | 山东电力工程咨询院有限公司 | Novel desulphurization accident flue gas spray cooling system |
| CN202724967U (en) * | 2012-05-14 | 2013-02-13 | 武汉旭日华科技发展有限公司 | Tail gas adsorbing device of mixed bed layer |
| JP2015000381A (en) * | 2013-06-17 | 2015-01-05 | 東洋紡株式会社 | Organic solvent recovery system |
| CN103585854A (en) * | 2013-10-29 | 2014-02-19 | 嘉园环保股份有限公司 | Technology for recovering and processing organic exhaust gas by activated carbon adsorption and N2 desorption |
| CN203577580U (en) * | 2013-11-20 | 2014-05-07 | 苏州巨联科技有限公司 | Activated carbon adsorption recovery device taking nitrogen as desorption medium |
| CN206094118U (en) * | 2016-09-19 | 2017-04-12 | 南通海阳节能环保科技有限公司 | An organic waste gas purifier |
| CN206778138U (en) * | 2017-06-02 | 2017-12-22 | 张家港市艾尔环保工程有限公司 | The adjustable activated carbon adsorption/desorption complexes of Wet-dry |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109046251A (en) * | 2018-10-09 | 2018-12-21 | 上海汉磊环保科技有限公司 | A kind of activated carbon adsorption detachment assays device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN111249857B (en) | VOC exhaust-gas treatment purifier and have its baking finish room | |
| CN107511019B (en) | Volatile organic pollutant's processing apparatus | |
| CN105597490B (en) | Organic waste gas adsorption, desorption, concentration and purification system and method thereof | |
| CN205760441U (en) | A kind of scattered adsorption, the organic exhaust gas purifying system of concentration desorption and regeneration | |
| TW201617125A (en) | Organic exhaust adsorption concentration purification system and method thereof | |
| KR101926171B1 (en) | Apparatus for recovering volatile organic solvent | |
| CN105013288A (en) | Vacuum drying active carbon waste gas management process and vacuum drying active carbon waste gas management apparatus | |
| CN107990334A (en) | A kind of absorption vacuum desorption condensation recycling of new VOCs exhaust gas or burning processing system | |
| CN206778138U (en) | The adjustable activated carbon adsorption/desorption complexes of Wet-dry | |
| CN205517124U (en) | Organic waste gas processing apparatus based on fixed molecular sieve adsorption bed | |
| TWM574661U (en) | Single wheel system with high-temperature desorption | |
| CN205925337U (en) | Second grade sorption recovery system | |
| CN208465546U (en) | A kind of waste gas purification apparatus | |
| CN109731433A (en) | The ethyl acetate recovery method combined is adsorbed with runner using activated carbon adsorption | |
| CN107158879A (en) | The adjustable activated carbon adsorption/desorption complexes of Wet-dry | |
| CN209423276U (en) | A kind of lacquer spraying waste gas processing unit | |
| CN209317364U (en) | A kind of pretreatment of exhaust gas and concentration condensing recovery governing system | |
| CN208959584U (en) | Adsoption catalysis integrated treatment unit | |
| CN208694613U (en) | A kind of nitrogen desorption condensate recycling device | |
| CN209093023U (en) | For handling the adsorption activation device of industrial waste gas | |
| CN215939474U (en) | Treatment device for sulfur-containing organic waste gas in phosphorization industry | |
| CN206444407U (en) | Organic exhaust gas adsorption concentration catalytic combustion system with nitrogen defencive function | |
| CN205084581U (en) | Organic waste gas's device is handled to multiregion | |
| CN208553605U (en) | A kind of waste gas condensation recovery system | |
| CN108204599B (en) | DMF waste gas treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170915 |