CN107913551A - For removing the commutative adsorption/desorption device of particulate pollutant or gas pollutant - Google Patents
For removing the commutative adsorption/desorption device of particulate pollutant or gas pollutant Download PDFInfo
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- CN107913551A CN107913551A CN201710673975.4A CN201710673975A CN107913551A CN 107913551 A CN107913551 A CN 107913551A CN 201710673975 A CN201710673975 A CN 201710673975A CN 107913551 A CN107913551 A CN 107913551A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B14/00—Arrangements for collecting, re-using or eliminating excess spraying material
- B05B14/40—Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths
- B05B14/43—Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths by filtering the air charged with excess material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0036—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
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- 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
-
- 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
- B01D53/0407—Constructional details of adsorbing systems
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- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/96—Regeneration, reactivation or recycling of reactants
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/345—Regenerating or reactivating using a particular desorbing compound or mixture
- B01J20/3458—Regenerating or reactivating using a particular desorbing compound or mixture in the gas phase
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3483—Regenerating or reactivating by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0258—Other waste gases from painting equipments or paint drying installations
-
- 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
- B01D2259/40011—Methods relating to the process cycle in pressure or temperature swing adsorption
- B01D2259/40058—Number of sequence steps, including sub-steps, per cycle
- B01D2259/40062—Four
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- 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
- B01D2259/40088—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
- B01D2259/4009—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating using hot gas
-
- 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
- B01D2259/404—Further details for adsorption processes and devices using four beds
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Oil, Petroleum & Natural Gas (AREA)
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Abstract
A kind of commutative adsorption/desorption device for removing particulate pollutant or gas pollutant includes adsorption module, desorption module and supplying module.Adsorption module includes adsorption chamber, the filter for being used to remove particulate pollutant accommodated by adsorption chamber, and the absorbing unit for being used to adsorb and remove gas pollutant accommodated by adsorption chamber.Desorption module is connected with adsorption module, and the absorbing unit of gas pollutant has been adsorbed for accommodating and has been desorbed the gas pollutant for being adsorbed onto absorbing unit.Supplying module is connected with adsorption module, for providing other absorbing unit.
Description
Technical field
The disclosure of invention is related to a kind of commutative adsorption/desorption device, more specifically, the disclosure of invention is related to
One kind is used to removing particulate pollutant and (such as is produced in spraying process in the spray booth of shipyard or vehicle assembling factory
Adhesive coating particle or dust) or removal gas pollutant (such as VOC (Volatile Organic Compounds, volatilization
Property organic compound), HAP (Hazardous Air Pollutant, hazardous air pollutants) etc.) commutative adsorption/desorption
Device.
Background technology
In the case of being sprayed in the spray booth of shipyard or vehicle assembling factory, such as adhesive coating can be produced
The particulate pollutant such as particle or dust or the gas pollutant such as VOC, HAP, and developed and removed the more of pollutant
Kind technology.
For example, traditional commerce technology is the adsorption technology using activated carbon, regeneration/reduction hot oxidant (RTO) etc..So
And the cost price of equipment is very high, equipment land used is limited, difficult in maintenance and expensive, and also produces secondary pollution.
In traditional adsorption technology using activated carbon, understood in selective removal harmful components due to active carbon dust
Secondary pollution is produced, the replacement cycle is very short, and equipment is excessive, and possibility of catching fire when handling VOC or HAP is very high.
RTO (Regenerative Thermal are being carried out at about 600 DEG C~800 DEG C using gas burner
Oxidizer, heat accumulating type oxidator) heating for burning pollutant when, the initial investment for equipment is expensive, with relatively low
Energy expenditure is high during concentration drive or during intermittent driving, is regarding during fuel combustion gas/oil as generation secondary pollution for example
Dioxin or nitrogen compound, maintenance cost is high, and equipment is excessive.
In order to solve the above problem as caused by above-mentioned VOC or HAP removal devices, it is 10-0966481 to disclose registration number
Korean Patent, the Korean Patent that registration number is 10-1108096, the Korean Patent of registration number 10-0966481 etc..However, go
It is restricted during except the particulate pollutant produced by spray booth, and contaminant remaining is fixed on adsorbent, reduces absorption
The removal rate of agent and the pressure for adding equipment.
The content of the invention
The present invention is developed for solving the above problem of association area.The present invention provides a kind of for removing particulate matter
The commutative adsorption/desorption device of pollutant or gas pollutant, it can simultaneously effective remove particulate pollutant and gas is dirty
Thing is contaminated, and absorbing unit can be made to be desorbed and be recycled by using commutative structure.
According to illustrative embodiments, for removing the commutative adsorption/desorption device of particulate pollutant or gas pollutant
Including adsorption module, desorption module and supplying module.Adsorption module includes adsorption chamber, is contained in adsorption chamber and is used to remove particle
The filter of pollutant, and it is contained in the absorbing unit for being used for adsorbing and remove gas pollutant in adsorption chamber.It is desorbed module
It is connected with adsorption module, the absorbing unit of gas pollutant has been adsorbed for accommodating and the gaseous contamination of absorbing unit will be adsorbed onto
Thing is desorbed.Supplying module is connected with adsorption module, for providing other absorbing unit.
In the exemplary embodiment, adsorption module can include：First connector, it is arranged in the first of adsorption chamber
Side, for absorbing unit to be supplied to desorption module；Second connector, it is arranged in the second side of adsorption chamber, for from supply
Module receives absorbing unit.
In the exemplary embodiment, the first connector may be coupled to the front side of adsorption chamber, and the second connector can connect
It is connected to the rear side of adsorption chamber.
In the exemplary embodiment, multiple absorbing units can be stacked on adsorption chamber along the direction of advance of gas pollutant
In, and be desorbed module and can accommodate the absorbing unit of foremost.
In the exemplary embodiment, when the absorbing unit of foremost is provided to desorption module, absorbing unit can be with
Moved forward along the direction opposite with the direction of advance of gas pollutant.
In the exemplary embodiment, adsorption module can also include mobile unit, it is arranged in the rear side of adsorption chamber, use
Moved forward in making absorbing unit along the direction opposite with the direction of advance of gas pollutant.
In the exemplary embodiment, multiple other absorbing units can be stacked in supplying module, and other
One of absorbing unit can be provided to adsorption chamber.
In the exemplary embodiment, desorption module can include：Desorption chamber, it is connected to the first connector；It is and logical
Road unit, it is connected to the front side of desorption chamber and is used to provide heating wind or cooling wind to desorption chamber.
In the exemplary embodiment, channel unit can include：First passage, it is with heating unit, for providing
Heat wind；Second channel, it is separated with first passage, and wind is cooled down for providing；And valve, it selectively opens or closes first
Passage and second channel.
In the exemplary embodiment, the direction of advance of the particulate pollutant inside adsorption module or gas pollutant can be with
It is opposite with the heating wind of desorption inside modules or the direction of cooling wind.
In the exemplary embodiment, multiple absorbing units can be stacked and be contained in inside desorption chamber.
In the exemplary embodiment, filter is arranged in before adsorption chamber so that can remove particle contamination first
Thing.
According to this illustrative embodiment, adsorption module includes the filter for removing particulate pollutant and removes gaseous contamination
The absorbing unit of thing, therefore particulate pollutant and gas pollutant are removed at the same time.Therefore, it can effectively remove and be produced from spraying
The VOC and HAP of room.
In addition, the desorption module being connected with adsorption module periodically can be desorbed absorbing unit, and through desorption
Absorbing unit can be recycled later, therefore can reduce the cost of absorbing unit.
In addition, multiple absorbing units are stacked so as to increase adsorption efficiency, and adsorb the suction of the most foremost of pollutant
Coupon member is desorbed first, so as to improve desorption efficiency by identical desorption process.
In addition, the other absorption that the vacant space for being moved to desorption module by absorbing unit to be formed is supplied to module is single
Member filling, therefore adsorption process can be kept in desorption process.Therefore, it is possible to reduce processing time.
In addition, desorption module accommodates multiple absorbing units, and supplying module accommodates multiple other absorbing units, therefore
How in office absorbing unit can be effectively replaced if necessary, therefore add process efficiency.
In addition, heating wind and cooling wind are selectively provided to desorption module so as to improve desorption efficiency, and de-
Attached absorbing unit is supplied to adsorption chamber in time.
Brief description of the drawings
Fig. 1 is the plan for the commutative adsorption/desorption device for showing an illustrative embodiments according to the present invention；
Fig. 2A to Fig. 2 G is to show to be desorbed absorbing unit and supply step in the commutative adsorption/desorption device of Fig. 1
Rapid plan；With
Fig. 3 is the plane for the commutative adsorption/desorption device for showing another illustrative embodiments according to the present invention
Figure.
Embodiment
The present invention is described more fully with hereinafter with reference to attached drawing, embodiment the invention is shown in the accompanying drawings.So
And the present invention can be implemented with many different forms, and it should not be construed as limited to embodiment described in this paper.And
These embodiments are to provide so that disclosure is fully and complete, and this will be fully passed on to those skilled in the art
The scope of invention.In the accompanying drawings, for the sake of clarity, the size and relative size in each layer and region may be exaggerated.It should manage
Solution, although term first, second, third, etc. can be used for describing multiple element, component, region, layer and/or part, these
Element, component, region, layer and/or part should not be limited by these terms.These terms are only used to by an element, component,
Region, layer or part are distinguished with another region, layer or part.Therefore, without departing from the teachings of the present invention, below
The first element, component, region, layer or the part discussed can be referred to as the second element, component, region, layer or part.
Term used herein is only used for description particular implementation, and is not intended to the limitation present invention.As made herein
As, not yet explicitly show during number and be also intended to when using " described " including plural form, it is bright unless the context otherwise
Really point out.
It will also be understood that in this specification using term " comprising " and/or "comprising" when refer to there are the feature, entirety,
Step, operation, element and/or component, but do not preclude the presence or addition of other one or more features, entirety, step, operation,
Element, component and/or its combination.
Unless otherwise defined, otherwise all terms (including technical term and scientific terminology) used herein and institute of the present invention
The those of ordinary skill in category field normally understood there is identical implication.It is also understood that term is (in such as common dictionary
Those terms of definition) it should be interpreted as having the implication consistent with its implication in association area background, and should not be with
Idealization or the meaning that excessively formalizes are explained, unless being clearly so defined herein.
Hereinafter, the illustrative embodiments of the present invention will be described in detail with reference to the accompanying drawings.
Fig. 1 is the plan for the commutative adsorption/desorption device for showing an illustrative embodiments according to the present invention.
With reference to figure 1, the commutative adsorption/desorption device 10 of this illustrative embodiment includes adsorption module 100, desorption mould
Block 200 and supplying module 300.
Adsorption module 100 removes the particulate pollutant and gas pollutant in input pollutant.Desorption module 200 makes absorption
The pollutant desorption of unit, for removing the pollutant of adsorption module 100.Absorbing unit is supplied to absorption by supplying module 300
Module 100.
Adsorption module 100 includes adsorption chamber 110, filter 120, absorbing unit 130,140 and first fan of mobile unit
150, desorption module 200 includes the second fan 210, channel unit 220 and desorption chamber 230, and supplying module 300 includes supply
Room 310 and other absorbing unit 320.
Adsorption module 100 removes the gas pollutant and particulate pollutant entered by first entrance 101, and passes through the
The removed pollutant of one outlet, 102 discharge.Gas pollutant and particulate pollutant are moved to first outlet from first entrance 101
102。
Adsorption chamber 110 is arranged between first entrance 101 and first outlet 102.Filter 120 is arranged in adsorption chamber 110
Front portion (towards the position of the foremost of first entrance 101).
Here, filter 120 can include electret filter (to its apply electrostatic), therefore particulate pollutant first by
Filter 120 removes.
In adsorption chamber 110, adsorption space 111 is formed behind filter 120, absorbing unit 130 is accommodated in absorption
In space 111.
Here, absorbing unit 130 includes multiple first absorbing units to the 4th absorbing unit 131,132,133 and 134, and
And absorbing unit can be stacked along the direction of advance of pollutant.Therefore, pollutant passes through the absorbing unit of series connection, gas pollutant
Removed.
Absorbing unit adsorbs and removes gas pollutant, and can include adsorbent such as activated carbon, zeolite.
Here, the quantity of absorbing unit can change, and be not limited to 4 as depicted.
If desired, the gas pollutant adsorbed in absorbing unit can be desorbed by being desorbed module 200.
Therefore, in order to be desorbed absorbing unit, each in absorbing unit 131,132,133 and 134 is moved to desorption
Module 200, and in this illustrative embodiments, in the side of adsorption chamber 110 formed with the first connector 112.
Among absorbing unit 131,132,133 and 134, the absorbing unit (such as first in Fig. 1 of position up front
Absorbing unit 131) adsorbed gas pollutant is most, therefore is firstly moved to desorption module 200 and carries out the first desorption.
Adsorption chamber 110, be disposed with absorbing unit (the first absorbing unit 131 in Fig. 1) positioned at foremost one
Side, the first connector 112 are connected with adsorption chamber 110, therefore the absorbing unit positioned at foremost moves to desorption module 200 and taken off
It is attached.
In this illustrative embodiments, the first absorbing unit 131 moves to desorption module 200, therefore adsorption space 111 has
Vacancy.Therefore, the other absorbing unit 320 of supplying module 300 is provided to adsorption space 111.
Here, supplying module 300 is connected to adsorption module 100, and the second connector 113 via the second connector 113
In adsorption chamber 110, the absorbing unit (the 4th absorbing unit 134 in Fig. 1) that is disposed with position most rearward side and absorption
Room 110 connects.
In addition, the second connector 113 and the first connector 112 are oppositely extending, and it is desorbed module 200 and supplying module
300 are connected to adsorption module 100 with different directions from each other.
As described below, there is provided the other absorbing unit 320 to adsorption chamber 110 can be provided to the absorbing unit of stacking
131st, 132,133 and 134 most position (the 4th absorbing unit 134 in Fig. 1), therefore the second connector 113 and absorption rearward
Room 110, positioned at absorbing unit most rearward at position side connection.
Connect in addition, first switch unit 114 and second switch unit 115 are separately positioned on the first connector 112 and second
Connect at device 113, to open the first connector 112 and the second connector 113 in absorbing unit or the movement of other absorbing unit,
And the first connector 112 and the second connector 113 are closed when not moving.
In this illustrative embodiments, absorbing unit 130 and other absorbing unit 320 are named differently, but
It is substantially identical unit (component).For example, absorbing unit is 131,132,133 and of the first absorbing unit to the 4th absorbing unit
One of 134, absorbing unit in addition is one of the 5th absorbing unit to the 8th absorbing unit 321,322,323 and 324.
Here, the quantity of absorbing unit and the quantity of other absorbing unit can change, and be not limited to as depicted 4
It is a.
Mobile unit 140 is arranged in the rear side of adsorption chamber 110, and along the direction opposite with the direction of advance of pollutant
Mobile absorbing unit 131,132,133 and 134.
As described above, when the first absorbing unit 131 is provided to desorption module 200, the space of the first absorbing unit 131
Vacate, and mobile unit 140 along the direction opposite with pollutant direction of advance move the second to the 4th absorbing unit 132,133 and
134。
Therefore, the second absorbing unit 132 occupies the space where the first absorbing unit 131, and 134 institute of the 4th absorbing unit
Vacated in space.
Then, as described above, the 5th absorbing unit 321 provided from supplying module 300 is moved to occupy the 4th absorption list
Space where member 134.
Here, the adsorption and desorption the following detailed description of absorbing unit and the processing step exchanged.
First fan 150 is arranged at first outlet 102, and pollutant is moved to first outlet from first entrance 101
102。
As described above, desorption module 200 is connected to the side of adsorption module 100, and will be adsorbed onto on absorbing unit 130
Gas pollutant be desorbed so that absorbing unit 130 recycles.
Desorption module 200 includes：Second entrance 201, for the air entrance for desorption；Second outlet 202, after desorption
Air outflow.As shown in the figure, the desorption air-flow in desorption module 200 and the contaminant stream in adsorption module 100 are reverse.
Therefore it provides the air of the absorbing unit 130 filtered to the pollutant to being moved along a fixed-direction with
Therefore the moving direction of pollutant is on the contrary, more easily can be desorbed the pollutant in absorbing unit 130.
Second fan 210 forces air to flow to second outlet 202 from second entrance 201.
Channel unit 220 is connected with the second fan 210.Channel unit 220 becomes the air supplied by second entrance 201
For heating wind or cooling wind, the air after changing then optionally is provided.
Channel unit 220 includes first passage 221, the second channel 222 separated with first passage 221 and is arranged in the
Valve 224 between one passage 221 and second channel 222.
Therefore, can be selectively provided to by the air for switching the valve 224 to enter via second entrance 201
One passage 221 or second channel 222.
Here, heating unit 223 is arranged at first passage 221, therefore is heated by the air of first passage 221,
In being to provide heating wind.
When the air by second entrance 201 is cold, it can not arrange that any cooling is single in second channel 222
Member.Alternatively, be disposed with cooling unit in second channel 222, therefore air is cooled, in being to provide cooling wind.
Therefore, heating wind and cooling wind are optionally provided by channel unit 220.Therefore, it is arranged in channel unit 220
The absorbing unit 130 in desorption chamber 230 below is heated wind heating, and therefore, the pollutant in absorbing unit 130 is desorbed.
Then, absorbing unit 130 is cooled air cooling, and is provided to adsorption module 100.
Desorption chamber 230 forms accommodation space, and absorbing unit 130 is accommodated in accommodation space.
Each absorbing unit is provided to desorption chamber 230 by the first connector 112, and pollutant is in desorption chamber 230
In be desorbed, therefore absorbing unit is recycled.
In this illustrative embodiments, desorption chamber 230 forms the predetermined space for accommodating the multiple absorbing unit 130.
Therefore, accommodate the multiple absorbing unit 130 and make its desorption, therefore can be more efficiently desorbed.
In addition, although it is not shown in the figure, the absorbing unit being desorbed in desorption chamber 230 is provided to predetermined storage
Space, or it is immediately supplied to supplying module 300.
Fig. 2A to Fig. 2 G is to show to be desorbed absorbing unit and supply step in the commutative adsorption/desorption device of Fig. 1
Rapid plan.
With reference to figure 2A, in commutative adsorption/desorption device 10, the first absorbing unit to the 4th absorbing unit 131,132,
133 and 134 are stacked in adsorption space 111, and adsorb the pollutant entered by first entrance 101.
Then, after the scheduled time is adsorbed, with reference to figure 2B, the first absorbing unit to the 4th absorbing unit 131,132,
The first most absorbing unit 131 of absorption pollutant is moved to the desorption chamber 230 of desorption module 200 among 133 and 134.
To carry out the movement, first switch unit 114 is opened, and the first absorbing unit 131 is via the first connector 112
It is moved to desorption chamber 230.
Then, with reference to figure 2C, during being recycled in desorption chamber 230 to the first absorbing unit 131, mobile unit
140 along the direction opposite with the direction of advance of pollutant move the second absorbing unit to the 4th absorbing unit 132,133 and
134。
First absorbing unit 131 is moved along the direction opposite with the direction of advance of pollutant in desorption chamber 230, and is taken off
It is attached.
Then, absorbing unit is moved with reference to figure 2D, mobile unit 140, then returnes to initial position, and open second
Switch element 115.
Then, it is empty that the 5th absorbing unit 321 among other absorbing unit being contained in supply chamber 310 is moved to absorption
Between 111.
Then, with reference to figure 2E, the 5th absorbing unit 321 in supply chamber 310 is moved to adsorption space 111, and then second
Absorbing unit is stacked in adsorption space 111 to the 5th absorbing unit 132,133,134 and 321 and adsorbs pollutant.
Then, with reference to figure 2F, the 6th absorbing unit in supply chamber 310 is retained in the 8th absorbing unit 322,323 and
324 move forward to prepare in addition to be moved to the second connector 113.
Therefore, after the first absorbing unit 131 is desorbed and is exchanged with the 5th absorbing unit 321, the second absorbing unit
Exchanged successively with the 6th absorbing unit to the 8th absorbing unit 322,323,324 to the 4th absorbing unit 132,133,134, as above
It is described.
Then, with reference to figure 2G, the first absorbing unit to the 4th absorbing unit 131,132,133 and 134 series stacks de-
In alcove 230, and the 5th to the 8th absorbing unit 321,322,323 and 324 series stacks are in adsorption chamber 111.Then, pollute
Thing is adsorbed.
In addition, the first absorbing unit being recycled to the 4th absorbing unit 131,132,133 and 134 via other shifting
Moving cell is provided to supply chamber 310, then can constantly repeat above-mentioned circulation.
Fig. 3 is the plane for the commutative adsorption/desorption device for showing another illustrative embodiments according to the present invention
Figure.
According in the tradable absorption of this illustrative embodiment and desorption apparatus 20 and foregoing exemplary embodiment
Device 10 it is essentially identical, difference is the shape of desorption chamber, therefore uses identical reference numeral, and appoints omitting
What repeat specification.
With reference to figure 3, in commutative adsorption/desorption device 20, single absorbing unit can be accommodated in desorption chamber 240, because
This is desorbed single absorbing unit.
Therefore, after being completed to single absorbing unit desorption, absorbing unit is moved to other holder or supply
In module 300.
Therefore, when single absorbing unit is desorbed, heat wind or cooling wind be forced to be applied on single absorbing unit,
Therefore can be more efficiently desorbed.
According to this illustrative embodiment, adsorption module includes the filter for removing particulate pollutant and removes gaseous contamination
The absorbing unit of thing, so as to remove particulate pollutant and gas pollutant at the same time.Therefore, it can effectively remove and be produced from spray booth
Raw VOC and HAP.
In addition, the desorption module being connected with adsorption module periodically can be desorbed absorbing unit, and the suction being desorbed
Coupon member can be recycled afterwards, therefore can reduce the cost of absorbing unit.
In addition, multiple absorbing units are stacked so as to increase adsorption efficiency, and adsorb the suction of the most foremost of pollutant
Coupon member is desorbed first, so as to improve desorption efficiency by identical desorption process.
In addition, the vacant space for being moved to desorption module by absorbing unit to be formed is supplied to the other absorption of module
Unit is filled, therefore adsorption process can be kept in desorption process.Therefore, it is possible to reduce processing time.
In addition, accommodating multiple absorbing units in desorption module, and multiple other absorbing units are accommodated in supplying module,
Therefore how in office absorbing unit can be effectively replaced if necessary, therefore add process efficiency.
In addition, heating wind and cooling wind are selectively provided to desorption module so as to improve desorption efficiency, and de-
Attached absorbing unit is supplied to adsorption chamber in time.
The illustrative embodiments and its advantage of the present invention have been described, it should be noted that will by appended right not departing from
Under the spirit and scope of the present invention for asking restriction, various changes, substitutions and modifications can be carried out herein.
Claims (12)
1. a kind of commutative adsorption/desorption device, including：
Adsorption module, the adsorption module include adsorption chamber, are contained in the mistake for removing particulate pollutant in the adsorption chamber
Filter and the absorbing unit being contained in the adsorption chamber for adsorbing and removing gas pollutant；
Module is desorbed, the desorption module is connected with the adsorption module, for accommodating the absorption of adsorbed gas pollutant
The gas pollutant being adsorbed onto on the absorbing unit is simultaneously desorbed by unit；With
Supplying module, the supplying module are connected with the adsorption module, for providing other absorbing unit.
2. commutative adsorption/desorption device according to claim 1, wherein the adsorption module includes：
First connector, first connector are arranged in the first side of the adsorption chamber, for the absorbing unit to be provided
To the desorption module；With
Second connector, second connector are arranged in the second side of the adsorption chamber, for being received from the supplying module
The absorbing unit.
3. commutative adsorption/desorption device according to claim 2, wherein first connector is connected to the absorption
The front side of room, and second connector is connected to the rear side of the adsorption chamber.
4. commutative adsorption/desorption device according to claim 3, wherein, multiple absorbing units are along the gas pollutant
Direction of advance be stacked in the adsorption chamber,
Wherein described desorption module receives the absorbing unit of foremost.
5. commutative adsorption/desorption device according to claim 4, wherein when the absorbing unit of the foremost is provided
During to the desorption module, the absorbing unit is moved forward along the direction opposite with the direction of advance of the gas pollutant.
6. commutative adsorption/desorption device according to claim 5, wherein the adsorption module further includes mobile unit, institute
The rear side that mobile unit is arranged in the adsorption chamber is stated, for making the absorbing unit along the advance side with the gas pollutant
Move forward in the opposite direction.
7. commutative adsorption/desorption device according to claim 3, plurality of other absorbing unit is stacked on described
In supplying module, and one of described other absorbing unit is provided to the adsorption chamber.
8. commutative adsorption/desorption device according to claim 2, wherein the desorption module includes：
Desorption chamber, the desorption chamber are connected with first connector；With
Channel unit, the channel unit are connected to the front side of the desorption chamber, for the desorption chamber provide heating wind or
Cool down wind.
9. commutative adsorption/desorption device according to claim 8, wherein the channel unit includes：
First passage, the first passage have heating unit, and wind is heated for providing；
Second channel, the second channel are separated with the first passage, and wind is cooled down for providing；With
Valve, the valve selectively open or close the first passage and the second channel.
10. commutative adsorption/desorption device according to claim 9, wherein the particle inside the adsorption module is dirty
Contaminate thing or the direction of advance of gas pollutant and the direction phase of the heating wind of the desorption inside modules or the cooling wind
Instead.
11. commutative adsorption/desorption device according to claim 8, wherein the multiple absorbing unit is stacked and accommodates
Inside the desorption chamber.
12. commutative adsorption/desorption device according to claim 1, wherein the filter is arranged in the adsorption chamber
Above so that remove the particulate pollutant first.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2016-0128228 | 2016-10-05 | ||
| KR1020160128228A KR101749177B1 (en) | 2016-10-05 | 2016-10-05 | Exchangeable adsorption and desorption apparatus |
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| Publication Number | Publication Date |
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| CN107913551A true CN107913551A (en) | 2018-04-17 |
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| CN201710673975.4A Pending CN107913551A (en) | 2016-10-05 | 2017-08-09 | For removing the commutative adsorption/desorption device of particulate pollutant or gas pollutant |
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| WO2020074479A1 (en) * | 2018-10-13 | 2020-04-16 | Oerlikon Textile Gmbh & Co. Kg | Method and device for filtering contaminated air |
| EP3892353A3 (en) * | 2020-04-09 | 2021-11-10 | Luftechnik Gransee GmbH | Filter changing device |
| US11549704B2 (en) | 2020-04-09 | 2023-01-10 | Lufttechnik Gransee GmbH | Filter device and method for changing a filter element |
| FR3127911A1 (en) * | 2021-10-12 | 2023-04-14 | Speedinnov | Ventilation device for transport vehicle, transport vehicle and associated maintenance method |
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| KR101893497B1 (en) * | 2018-02-07 | 2018-08-30 | (주)씨앤지테크 | EXCHANGEABLE ADSORPTION AND DESORPTION APPARATUS FOR THE REMOVAL OF VOCs |
| KR20240052167A (en) | 2022-10-13 | 2024-04-23 | 한국생산기술연구원 | Composite filter capable of simultaneously reducing particulate and gaseous substances and manufacturing method of the same |
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| KR20130104486A (en) * | 2012-03-14 | 2013-09-25 | 에스코 주식회사 | A smoke reduction apparatus of a exhaust gas |
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| US20050150382A1 (en) * | 2004-01-08 | 2005-07-14 | Sheehan Darren S. | Filter system with automatic media refresh |
| KR20090130320A (en) * | 2007-04-23 | 2009-12-22 | 주식회사 엔바이온 | Air cleaner having regenerative filter, and method for regenerative of air cleaner filter |
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| WO2020074479A1 (en) * | 2018-10-13 | 2020-04-16 | Oerlikon Textile Gmbh & Co. Kg | Method and device for filtering contaminated air |
| US11938438B2 (en) | 2018-10-13 | 2024-03-26 | Oerlikon Textile Gmbh & Co. Kg | Method and device for filtering contaminated air |
| EP3892353A3 (en) * | 2020-04-09 | 2021-11-10 | Luftechnik Gransee GmbH | Filter changing device |
| US11549704B2 (en) | 2020-04-09 | 2023-01-10 | Lufttechnik Gransee GmbH | Filter device and method for changing a filter element |
| US11731070B2 (en) | 2020-04-09 | 2023-08-22 | Oerlikon Textile Gmbh & Co Kg | Filter device |
| FR3127911A1 (en) * | 2021-10-12 | 2023-04-14 | Speedinnov | Ventilation device for transport vehicle, transport vehicle and associated maintenance method |
| EP4166412A1 (en) * | 2021-10-12 | 2023-04-19 | SpeedInnov | Ventilation device for transport vehicle, associated transport vehicle and maintenance method |
Also Published As
| Publication number | Publication date |
|---|---|
| KR101749177B1 (en) | 2017-06-21 |
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