CN109499088A - One kind being suitable for the pretreated Multifunctional absorption condenser of exhaust gas and exhaust gas preprocess method - Google Patents
One kind being suitable for the pretreated Multifunctional absorption condenser of exhaust gas and exhaust gas preprocess method Download PDFInfo
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- CN109499088A CN109499088A CN201811548219.XA CN201811548219A CN109499088A CN 109499088 A CN109499088 A CN 109499088A CN 201811548219 A CN201811548219 A CN 201811548219A CN 109499088 A CN109499088 A CN 109499088A
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- exhaust gas
- solution
- gas
- multifunctional absorption
- condenser
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 59
- 238000000034 method Methods 0.000 title claims abstract description 19
- 239000007789 gas Substances 0.000 claims abstract description 130
- 238000009833 condensation Methods 0.000 claims abstract description 34
- 230000005494 condensation Effects 0.000 claims abstract description 34
- 238000001816 cooling Methods 0.000 claims abstract description 24
- 238000009826 distribution Methods 0.000 claims abstract description 13
- 238000005406 washing Methods 0.000 claims abstract description 13
- 239000002912 waste gas Substances 0.000 claims abstract description 8
- 239000013589 supplement Substances 0.000 claims abstract description 7
- 230000008676 import Effects 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 14
- 238000002156 mixing Methods 0.000 claims description 10
- 239000003344 environmental pollutant Substances 0.000 claims description 9
- 231100000719 pollutant Toxicity 0.000 claims description 9
- 239000002253 acid Substances 0.000 claims description 8
- 239000000523 sample Substances 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 8
- 239000010865 sewage Substances 0.000 claims description 6
- 239000000945 filler Substances 0.000 claims description 5
- 239000003507 refrigerant Substances 0.000 claims description 5
- 238000005086 pumping Methods 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 230000008569 process Effects 0.000 abstract description 8
- 239000000126 substance Substances 0.000 abstract description 8
- 230000000694 effects Effects 0.000 description 10
- 239000002699 waste material Substances 0.000 description 7
- 239000012530 fluid Substances 0.000 description 6
- 239000004033 plastic Substances 0.000 description 6
- 229920003023 plastic Polymers 0.000 description 6
- 230000002378 acidificating effect Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 3
- 230000001133 acceleration Effects 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- -1 alkalinity Chemical compound 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
- B01D5/0006—Coils or serpentines
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0027—Condensation of vapours; Recovering volatile solvents by condensation by direct contact between vapours or gases and the cooling medium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0036—Multiple-effect condensation; Fractional condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0051—Regulation processes; Control systems, e.g. valves
-
- 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
- B01D53/002—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 condensation
Abstract
The invention discloses one kind to be suitable for the pretreated Multifunctional absorption condenser of exhaust gas and exhaust gas preprocess method, wherein, the Multifunctional absorption condenser includes Multifunctional absorption drainer, the inner cavity of the Multifunctional absorption drainer constitutes condensation chamber, the condensation chamber lower end is equipped with waste gas inlet and gas distribution pipe, and upper end is equipped with exhaust vent；The cooling coil of cooling is equipped in the condensation chamber, Multifunctional absorption drainer is equipped with solution supplement import and overflow port, condenses indoor solution and exhaust gas to be processed carries out contact condensation and carries out gas washing processing to exhaust gas.Of the invention can carry out condensation process to exhaust gas suitable for the pretreated Multifunctional absorption condenser of exhaust gas, go the part harmful substance in removing exhaust gas while reducing exhaust gas temperature.
Description
Technical field
The present invention relates to a kind of Multifunctional absorption condensers, and in particular to one kind is suitable for being rich in organic volatile and acid
The pretreated Multifunctional absorption condenser of the exhaust gas of the gases high-temperature water vapors such as (alkali) property and exhaust gas preprocess method.
Background technique
In some industrial processes, material needs to heat to remove moisture content and volatile substance, the exhaust gas of generation
By following characteristics: (1) temperature is about at 100 DEG C or so；(2) it is mixed with the steam of the volatile matters such as oil；(3) with acidic materials and organic
Exhaust gas etc..
Case therein:
1, in the regenerative process of waste plastics or waste plastics film, due in waste plastics or waste plastics film be rich in moisture,
The pollutants such as grease, therefore vapor, the oil of high temperature can be rich in the exhaust gas generated when heating (temperature≤300 DEG C) through melting
Steam and organic volatile etc.；Temperature when containing polyvinyl chloride composition in waste plastics or waste plastics film, when due to melting
>=200 DEG C of degree, therefore can also contain chlorine, plasticizer gas etc. in the exhaust gas generated.
2, during burning industrial residue using boiler, most of fire box temperatures are between 300-500 DEG C；It can generate a large amount of
High-temperature vapor and organic exhaust gas etc.；Industrial waste often mixes waste spinning fabric, rtificial leather, sawdust, the object for being stained with greasy dirt
Matter, moisture content etc.；More high-temperature acidic vapor, organic exhaust gas etc. or even dioxin poison gas can be generated during burning.
The processing method of the grade exhaust gas usually has: high temperature incineration method, biofilm, active carbon adsorption etc.；It is especially raw
Object membrane absorption method needs in advance to be located exhaust gas before handling the exhaust gas such as above-mentioned high-temperature vapor, oil vapour, sour gas
Reason, that is, be cooled to 15-30 DEG C；Existing condenser is only capable of reducing the effect of temperature, cannot remove the part nuisance in gas
Matter, and the effect to cool down is also to be improved.
Summary of the invention
Be suitable for it is an object of the invention to overcome the deficiencies of the prior art and provide one kind rich in organic volatile and acid or
The pretreated Multifunctional absorption condenser of the exhaust gas of the gases high-temperature water vapor such as alkalinity, the Multifunctional absorption condenser can be to useless
Gas carries out condensation process, goes the part harmful substance in removing exhaust gas while reducing exhaust gas temperature.
It is another object of the present invention to provide one kind to steam rich in organic volatile and the gases high-temperature water such as acid or alkalinity
The exhaust gas preprocess method of vapour.
The technical solution that the present invention solves above-mentioned technical problem is:
One kind being suitable for the pretreated Multifunctional absorption condenser of exhaust gas, including Multifunctional absorption drainer, this is multi-functional
The inner cavity of absorption condensation tank constitutes condensation chamber, which is equipped with waste gas inlet and gas distribution pipe, and upper end is arranged equipped with exhaust gas
Port；The cooling coil of cooling is equipped in the condensation chamber, Multifunctional absorption drainer is equipped with solution and supplements import, condensation
Indoor solution and exhaust gas to be processed carry out contact condensation and carry out gas washing processing to exhaust gas.
Preferably, the Multifunctional absorption drainer is equipped with overflow port, and solution is delivered to condensation chamber by pumping, solution it is defeated
Pipeline is sent to be equipped with the ejector for aspirating with mixing exhaust gas to be processed, the end of the transfer pipeline of solution and condensation are indoor
Gas distribution pipe connection, the air inlet of the gas distribution pipe constitute the solution and supplement import.When work, solution passes through the acceleration of pump, passes through
Ejector aspirates and mixes exhaust gas to be processed；And entered in condenser by the gas distribution pipe of condenser bottom.
A preferred embodiment of the invention, wherein the top of the condensation chamber is equipped with to be supplied for the solution of spray solution
Pipe, the solution sprayed out by solution supply pipe disperse in tank and with exhaust gas to be processed from bottom to top sufficiently directly contact into
Row cooling and gas washing.
Preferably, the filler or column plate for increasing gas-liquid contact chance are equipped in the condensation chamber, so as to reach
More efficient treatment effect.
Preferably, in balancing tank, which is equipped with for connecting with sewage disposal system the solution storage
Water outlet.
Preferably, concentration on-line checking mixing system, the concentration on-line checking mixing system are equipped in the balancing tank
Including concentration on-line checking probe, controller and dispensation apparatus, wherein the concentration on-line checking probe setting is adjusting water
It is connect in pond and with the signal input part of controller, the signal output end connection of the dispensation apparatus and controller.It is arranged in this way
Purpose be, due to containing acidic materials exhaust gas carry out contact processing when with treatment fluid neutralization reaction has occurred,
So that the basic ion in treatment fluid is constantly consumed, and after passing through the above-mentioned on-line checking mixing system of setting, concentration on-line checking
Probe by being transferred to controller for concentration data in real time, then concentration data is transferred to dispensation apparatus by controller, in this way,
The pH value that dispensation apparatus (being made of Scatula or dispensing slot) can be measured according to pH value detection device, on demand to adjusting water
Solution supplements the requirement of its concentration, absorbs treatment effect to reach ideal.
Preferably, the top of cooling chamber is arranged in the exhaust vent.
Preferably, the solution face in the Multifunctional absorption drainer and setting gas-liquid separation dress between exhaust vent
It sets.The gas-liquid separation device is made of demisting filler or group plate etc., by the way that gas-liquid separation device is arranged, can be reached more efficient
Treatment effect.
A kind of exhaust gas preprocess method realized suitable for the pretreated Multifunctional absorption condenser of exhaust gas, including following step
It is rapid:
The exhaust gas of high-temperature water vapor rich in organic volatile and acid or alkaline gas is drawn into multi-functional by power
In absorptive condenser；Refrigerant flows in the cooling coil of cooling in Multifunctional absorption condenser, by indirect with exhaust gas
The mode of contact takes away the heat that exhaust gas is brought into；Solution in Multifunctional absorption condenser is directly contacted with exhaust gas, by with to
The mode for handling exhaust gas progress contact condensation carries out gas washing processing to exhaust gas, so that solution passes through Multifunctional absorption condenser
When, on the one hand reaching reduces temperature, is on the one hand transferred to the pollutant of exhaust gas in solution by the washing of solution, allows through more function
Can the pollutant load of condenser treated exhaust gas reduce.
The working principle of the invention is:
When work, Multifunctional absorption condenser of the invention is by direct contact type to rich in organic volatile and acid or alkali
Property etc. gases high-temperature water vapor exhaust gas carry out condensation process；Specifically, high-temp waste gas directly contacts with cryogenic fluid, is sufficiently mixed
It closes, the heat of exhaust gas and the substance of entrainment are transferred in solution by gas-liquid interface in the process；And refrigerant coil pipe is by non-contact
Mode heat is taken away；The pollutant being transferred in solution by being purged into sewage disposal system, realize cooling and
The double action of detoxication.
The present invention have compared with prior art it is below the utility model has the advantages that
1, Multifunctional absorption condenser of the invention specifies the processing mode that solution is directly contacted with exhaust gas, is not only able to
The effect of cooling and condensation is improved, and solution can be chemically reacted directly with the harmful substance in exhaust gas, to remove
Part harmful substance in exhaust gas, reduces the load of subsequent treatment process.
2, Multifunctional absorption condenser of the invention can be configured when the high-temp waste gas for different characteristics is condensed
The solution of variety classes various concentration realizes dissolution and absorption to harmful substance in exhaust gas, realizes the pretreatment of exhaust gas, solves
Certainly exhaust gas is easily escaped difficult the problem of collecting.And sewage easily collecting；As long as suitable processing means is taken to handle, it can be ensured that environment
It does not pollute.
Detailed description of the invention
Fig. 1 is one kind of the invention corresponding knot of embodiment 1 suitable for the pretreated Multifunctional absorption condenser of exhaust gas
Structure schematic diagram.
Fig. 2 is one kind of the invention corresponding knot of embodiment 2 suitable for the pretreated Multifunctional absorption condenser of exhaust gas
Structure schematic diagram.
Multifunctional absorption drainer 1, waste gas inlet 2, gas distribution pipe 3, exhaust vent 4, cooling coil 5, overflow port 6,
Transfer pipeline 7, ejector 7-1, air inlet pipe 7-2, pump 7-3, balancing tank 8, water outlet 8-1, the concentration on-line checking of solution are visited
First 9, controller 10, medicine device 11, gas-liquid separation device 12, solution supply pipe 13.
Specific embodiment
Present invention will now be described in further detail with reference to the embodiments and the accompanying drawings, but embodiments of the present invention are unlimited
In this.
Embodiment 1
Referring to Fig. 1, it includes Multifunctional absorption that one kind of the invention, which is suitable for the pretreated Multifunctional absorption condenser of exhaust gas,
Drainer 1, the inner cavity of the Multifunctional absorption drainer 1 constitute condensation chamber, which is equipped with waste gas inlet 2 and gas distribution
Pipe 3, upper end are equipped with exhaust vent 4, which is arranged in the top of cooling chamber；Cooling is equipped in the condensation chamber
Cooling coil 5, Multifunctional absorption drainer 1 are equipped with solution and supplement import, condense indoor solution and exhaust gas to be processed
It carries out contact condensation and gas washing processing is carried out to exhaust gas.
The Multifunctional absorption drainer 1 is equipped with overflow port 6, and solution is delivered to condensation chamber, the conveying of solution by pumping 7-3
Pipeline 7 is equipped with the ejector 7-1 (exhaust gas is entered in ejector by air inlet pipe 7-2) for aspirating with mixing exhaust gas to be processed,
The end of the transfer pipeline 7 of solution is connect with indoor gas distribution pipe 3 is condensed, and the air inlet of the gas distribution pipe 3 constitutes the solution and mends
It is charged into mouth.When work, solution aspirates by the acceleration of pump 7-3, by ejector 7-1 and mixes exhaust gas to be processed；And pass through
The gas distribution pipe 3 of condenser bottom enters in condenser.Be equipped in the condensation chamber filler for increasing gas-liquid contact chance or
Column plate, so as to reach more efficient treatment effect.In balancing tank 8, which is equipped with uses the solution storage
In the water outlet 8-1 being connect with sewage disposal system.
Referring to Fig. 1, concentration on-line checking mixing system, concentration on-line checking allotment system are equipped in the balancing tank 8
System includes concentration on-line checking probe 9, controller 10 and dispensation apparatus 11, wherein 9 setting of concentration on-line checking probe
It is connect in balancing tank 8 and with the signal input part of controller 10, the signal of the dispensation apparatus 11 and controller 10 exports
End connection.The purpose being arranged in this way is, due to when carrying out contact processing to the exhaust gas containing acidic materials and treatment fluid
Neutralization reaction has occurred, so that the basic ion in treatment fluid is constantly consumed, and by the way that above-mentioned on-line checking mixing system is arranged
Afterwards, concentration data is by being transferred to controller 10 by concentration on-line checking probe 9 in real time, then by controller 10 by concentration data
It is transferred to dispensation apparatus 11, in this way, dispensation apparatus 11 (being made of Scatula or dispensing slot) can be according to pH value detection device
The pH value measured supplements the requirement of its concentration to the solution for adjusting water on demand, absorbs treatment effect to reach ideal.
Referring to Fig. 1, gas-liquid separation is set between the solution face and exhaust vent 4 in the Multifunctional absorption drainer 1
Device 12.The gas-liquid separation device 12 is made of demisting filler or group plate etc., by the way that gas-liquid separation device 12 is arranged, can be reached
More efficient treatment effect.
A kind of exhaust gas preprocess method realized suitable for the pretreated Multifunctional absorption condenser of exhaust gas, including following step
It is rapid:
The exhaust gas of high-temperature water vapor rich in organic volatile and acid or alkaline gas is drawn into multi-functional by power
In absorptive condenser；Refrigerant flows in the cooling coil of cooling in Multifunctional absorption condenser, by indirect with exhaust gas
The mode of contact takes away the heat that exhaust gas is brought into；Solution in Multifunctional absorption condenser is directly contacted with exhaust gas, by with to
The mode for handling exhaust gas progress contact condensation carries out gas washing processing to exhaust gas, so that solution passes through Multifunctional absorption condenser
When, on the one hand reaching reduces temperature, is on the one hand transferred to the pollutant of exhaust gas in solution by the washing of solution, allows through more function
Can the pollutant load of condenser treated exhaust gas reduce.
The working principle of the invention is:
When work, Multifunctional absorption condenser of the invention is by direct contact type to rich in organic volatile and acid or alkali
Property etc. gases high-temperature water vapor exhaust gas carry out condensation process；Specifically, high-temp waste gas directly contacts with cryogenic fluid, is sufficiently mixed
It closes, the heat of exhaust gas and the substance of entrainment are transferred in solution by gas-liquid interface in the process；And refrigerant coil pipe is by non-contact
Mode heat is taken away；The pollutant being transferred in solution by being purged into sewage disposal system, realize cooling and
The double action of detoxication.
Embodiment 2
Referring to fig. 2, the present embodiment and embodiment 1 the difference is that, the top of the condensation chamber is equipped with for spraying
The solution supply pipe 13 of leaching liquor, the solution sprayed out by solution supply pipe 13 disperse in tank and with from bottom to top to
Sufficiently directly contact carries out cooling and gas washing to reason exhaust gas.
Other embodiment other than the above of the invention is implemented referring to embodiment 1.
Above-mentioned is the preferable embodiment of the present invention, but embodiments of the present invention are not limited by the foregoing content,
His any changes, modifications, substitutions, combinations, simplifications made without departing from the spirit and principles of the present invention, should be
The substitute mode of effect, is included within the scope of the present invention.
Claims (9)
1. one kind is suitable for the pretreated Multifunctional absorption condenser of exhaust gas, which is characterized in that including Multifunctional absorption drainer,
The inner cavity of the Multifunctional absorption drainer constitutes condensation chamber, which is equipped with waste gas inlet and gas distribution pipe, and upper end is set
There is exhaust vent；The cooling coil of cooling is equipped in the condensation chamber, Multifunctional absorption drainer is supplemented equipped with solution
Import, condenses indoor solution and exhaust gas to be processed carries out contact condensation and carries out gas washing processing to exhaust gas.
2. according to claim 1 be suitable for the pretreated Multifunctional absorption condenser of exhaust gas, which is characterized in that described more
Function absorption condensation tank is equipped with overflow port, and solution is delivered to condensation chamber by pumping, and the transfer pipeline of solution is equipped with for aspirating
With the ejector for mixing exhaust gas to be processed, the end of the transfer pipeline of solution is connect with indoor gas distribution pipe is condensed, the gas distribution pipe
Air inlet constitute the solution and supplement import.
3. according to claim 1 be suitable for the pretreated Multifunctional absorption condenser of exhaust gas, which is characterized in that described cold
The top of solidifying room is equipped with the solution supply pipe for spray solution, is dispersed simultaneously in tank by the solution that solution supply pipe sprays out
It is sufficiently directly contacted with exhaust gas to be processed from bottom to top and carries out cooling and gas washing.
4. according to claim 3 be suitable for the pretreated Multifunctional absorption condenser of exhaust gas, which is characterized in that condensation chamber
The interior filler or column plate being equipped with for increasing gas-liquid contact chance.
5. according to claim 1 be suitable for the pretreated Multifunctional absorption condenser of exhaust gas, which is characterized in that described molten
Liquid is stored in balancing tank, which is equipped with the water outlet for connecting with sewage disposal system.
6. according to claim 5 be suitable for the pretreated Multifunctional absorption condenser of exhaust gas, which is characterized in that the tune
Be equipped with concentration on-line checking mixing system in economizing basin, the concentration on-line checking mixing system include concentration on-line checking probe,
Controller and dispensation apparatus, wherein the signal in balancing tank and with controller is arranged in the concentration on-line checking probe
The signal output end of input terminal connection, the dispensation apparatus and controller connects.
7. according to claim 1 be suitable for the pretreated Multifunctional absorption condenser of exhaust gas, which is characterized in that described useless
The top of cooling chamber is arranged in gas exhaust outlet.
8. according to claim 7 be suitable for the pretreated Multifunctional absorption condenser of exhaust gas, which is characterized in that described more
Gas-liquid separation device is set between solution face and exhaust vent in function absorption condensation tank.
9. a kind of using the described in any item exhaust gas suitable for the pretreated Multifunctional absorption condenser of exhaust gas of claim 1-8
Preprocess method, which comprises the following steps:
The exhaust gas of high-temperature water vapor rich in organic volatile and acid or alkaline gas is drawn into Multifunctional absorption by power
In condenser；Refrigerant flows in the cooling coil of cooling in Multifunctional absorption condenser, by with exhaust gas non-direct contact
Mode take away the heat that exhaust gas is brought into；Solution in Multifunctional absorption condenser is directly contacted with exhaust gas, by with it is to be processed
The mode that exhaust gas carries out contact condensation carries out gas washing processing to exhaust gas, so that when solution passes through Multifunctional absorption condenser,
On the one hand reaching reduces temperature, is on the one hand transferred to the pollutant of exhaust gas in solution by the washing of solution, allows through multi-functional
The pollutant load of condenser treated exhaust gas reduces.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811548219.XA CN109499088A (en) | 2018-12-17 | 2018-12-17 | One kind being suitable for the pretreated Multifunctional absorption condenser of exhaust gas and exhaust gas preprocess method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811548219.XA CN109499088A (en) | 2018-12-17 | 2018-12-17 | One kind being suitable for the pretreated Multifunctional absorption condenser of exhaust gas and exhaust gas preprocess method |
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| Publication Number | Publication Date |
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| CN109499088A true CN109499088A (en) | 2019-03-22 |
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| CN201811548219.XA Pending CN109499088A (en) | 2018-12-17 | 2018-12-17 | One kind being suitable for the pretreated Multifunctional absorption condenser of exhaust gas and exhaust gas preprocess method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113464842A (en) * | 2021-06-28 | 2021-10-01 | 江阴华西化工码头有限公司 | Overhead exhaust treatment device for pipeline |
| CN117030951A (en) * | 2023-10-08 | 2023-11-10 | 江苏熙天时环保科技有限责任公司 | Acid mist waste gas detection system and purifying tower with same |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2581055Y (en) * | 2002-12-03 | 2003-10-22 | 江西省国燕橡胶有限公司 | Circulation absorption separator |
| CN103007712A (en) * | 2012-12-12 | 2013-04-03 | 北京城市排水集团有限责任公司 | Low-consumption efficient separated wet type desulfurization system and control method |
| CN204865516U (en) * | 2015-09-02 | 2015-12-16 | 山东山大胶体材料有限责任公司 | Waste gas treating device |
| CN205007838U (en) * | 2015-09-16 | 2016-02-03 | 九江富达实业有限公司 | Waste gas absorbing device with cooling device |
| CN106268178A (en) * | 2016-08-16 | 2017-01-04 | 辽宁工程技术大学 | A kind of dust removal mist integrated apparatus for wet desulfurization system and method |
| CN207445889U (en) * | 2017-10-20 | 2018-06-05 | 宜昌人福药业有限责任公司 | A kind of condensing air-washer |
| CN209548749U (en) * | 2018-12-17 | 2019-10-29 | 广州市致顺科技有限公司 | One kind being suitable for the pretreated Multifunctional absorption condenser of exhaust gas |
-
2018
- 2018-12-17 CN CN201811548219.XA patent/CN109499088A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2581055Y (en) * | 2002-12-03 | 2003-10-22 | 江西省国燕橡胶有限公司 | Circulation absorption separator |
| CN103007712A (en) * | 2012-12-12 | 2013-04-03 | 北京城市排水集团有限责任公司 | Low-consumption efficient separated wet type desulfurization system and control method |
| CN204865516U (en) * | 2015-09-02 | 2015-12-16 | 山东山大胶体材料有限责任公司 | Waste gas treating device |
| CN205007838U (en) * | 2015-09-16 | 2016-02-03 | 九江富达实业有限公司 | Waste gas absorbing device with cooling device |
| CN106268178A (en) * | 2016-08-16 | 2017-01-04 | 辽宁工程技术大学 | A kind of dust removal mist integrated apparatus for wet desulfurization system and method |
| CN207445889U (en) * | 2017-10-20 | 2018-06-05 | 宜昌人福药业有限责任公司 | A kind of condensing air-washer |
| CN209548749U (en) * | 2018-12-17 | 2019-10-29 | 广州市致顺科技有限公司 | One kind being suitable for the pretreated Multifunctional absorption condenser of exhaust gas |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113464842A (en) * | 2021-06-28 | 2021-10-01 | 江阴华西化工码头有限公司 | Overhead exhaust treatment device for pipeline |
| CN113464842B (en) * | 2021-06-28 | 2022-03-22 | 江阴华西化工码头有限公司 | Overhead exhaust treatment device for pipeline |
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| CN117030951B (en) * | 2023-10-08 | 2024-01-16 | 江苏熙天时环保科技有限责任公司 | Acid mist waste gas detection system and purifying tower with same |
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