CN107198888A - VOC removal device and VOC minimizing technology - Google Patents
VOC removal device and VOC minimizing technology Download PDFInfo
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- CN107198888A CN107198888A CN201710003454.8A CN201710003454A CN107198888A CN 107198888 A CN107198888 A CN 107198888A CN 201710003454 A CN201710003454 A CN 201710003454A CN 107198888 A CN107198888 A CN 107198888A
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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
- B01D53/002—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
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- 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
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- 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
- B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
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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
- 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
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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
- B01D53/38—Removing components of undefined structure
- B01D53/44—Organic components
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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
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/81—Solid phase processes
- B01D53/82—Solid phase processes with stationary reactants
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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
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8678—Removing components of undefined structure
- B01D53/8687—Organic components
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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
- B01D2258/06—Polluted air
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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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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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- Chemical & Material Sciences (AREA)
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- Chemical Kinetics & Catalysis (AREA)
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- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
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- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
There is provided VOC removal device and VOC minimizing technology.VOC removal device according to an embodiment of the present invention includes：Polluting air supply unit, there is provided the pollution air comprising VOC；Cooling end, enters above-mentioned contaminated and cools down above-mentioned pollution air；And filter house, make to enter and adsorb the above-mentioned VOC included in above-mentioned pollution air by the contaminated of above-mentioned cooling end.
Description
Technical field
The present invention relates to VOC removal device and VOC minimizing technology.
Background technology
VOC (VOC, Volatile Organic Compound) is to easy due to high-vapor-pressure
The liquid phase or the general designation of the organic compound of gas phase being evaporated in air.VOC is inhaled as by expiration organ
Enter and cause the carcinogen of adverse effect, it may trigger leukaemia, central nervous disorders, chromosome abnormality etc. to human body.
In addition, VOC may trigger depletion of the ozone layer, greenhouse effects of the earth and chain anti-because of photochemical oxidation thing
The environmental problem of the photochemical fog answered generated photochemical oxidation thing and occurred etc..Moreover, due to most of volatilization
Property organic compound containing irritant and make us foreign odor, therefore may produce pole to living environment when flowing out in air
Big harm.Most of VOC is artificially produced because of the commecial activity of the mankind mostly, and it occurs original
Because being also various, mainly such as petrochemical plant, application factory and motor-vehicle tail-gas.This VOC institute
The harmfulness having is even more serious in densely populated metropolitan area, and reality is that each field is all being ground
Study carefully with making great efforts to reduce this harmfulness.
The content of the invention
The problem to be solved in the present invention, which is to provide, can remove waving for the VOC that produces in process
Hair property organic compound removal device.
The invention solves the problems that another problem is that providing prevents because of have hot of the pollution air of high temperature to air
The VOC removal device of the thermal pollution of generation.
Of the invention the problem of, is not limited to technical problem mentioned hereinabove, and those skilled in the art can be by following
Record is expressly understood that NM other technical problems.
VOC removal device according to an embodiment of the present invention includes：Air supply unit is polluted,
The pollution air for including VOC is provided；Cooling end, enters above-mentioned contaminated and cools down above-mentioned pollution sky
Gas；And filter house, make to enter and adsorb above-mentioned included in above-mentioned pollution air by the contaminated of above-mentioned cooling end
VOC.
In addition, above-mentioned cooling end may also include the heat exchanger for making extraneous air carry out heat exchange with above-mentioned pollution air.
In addition, above-mentioned cooling end may include the cooling worm cooled down to above-mentioned pollution air.
In addition, at least a portion in above-mentioned pollution air can be liquefied by above-mentioned cooling end, and above-mentioned volatility is organic
Compound removal device may also include the discharger for handling liquefied above-mentioned pollution air.
In addition, above-mentioned filter house may include at least one filter, above-mentioned filter may include to be selected to be inhaled by applied chemistry
Attached dose of filter, the filter of Applied Physics adsorbent, the mistake of the filter being made up of porous material and applications catalyst
More than one filter in the group that filter is constituted.
Included according to the VOC removal device of another embodiment of the present invention：There is provided comprising waving for stove
The pollution air of hair property organic compound；Cooling end, enters above-mentioned contaminated and cools down above-mentioned pollution air；First filtering
Device, makes to enter and adsorb the volatile organic included in above-mentioned pollution air by the above-mentioned contaminated of above-mentioned cooling end
Compound；First pipeline, is connected to above-mentioned stove to transmit the above-mentioned pollution air that is provided by above-mentioned stove and via above-mentioned cooling
Portion and the above-mentioned externally connected gas of first filter；And second pipe, it is connected to said external gas and by extraneous air
Transmit to above-mentioned cooling end.
In addition, above-mentioned cooling end may include the heat exchange for making said external air carry out heat exchange with above-mentioned pollution air
Device.
In addition, above-mentioned first pipeline can directly be contacted with above-mentioned second pipe in above-mentioned heat exchanger.
In addition, above-mentioned first pipeline can be wrapped around one another with above-mentioned second pipe, or can in the state of adjacent to each other with
Mode with least one bending section extends.
In addition, one end of above-mentioned second pipe may be connected to said external gas, and the other end of above-mentioned second pipe
It may be connected to above-mentioned stove.
In addition, above-mentioned first filter may include selected from filter, the Applied Physics adsorbent by applied chemistry adsorbent
Filter, a filter in the group that constitutes of the filter of the filter that is made up of porous material and applications catalyst.
In addition, at least a portion in above-mentioned pollution air can be liquefied by above-mentioned cooling end, and above-mentioned volatility is organic
Compound removal device may also include the discharger for handling liquefied above-mentioned pollution air.
In addition, above-mentioned VOC removal device may also include the accumulator tank that is connected with above-mentioned discharger with
And the 3rd pipeline of the above-mentioned heat exchanger of connection, above-mentioned discharger and above-mentioned accumulator tank, and one end of above-mentioned 3rd pipeline
Above-mentioned heat exchanger is may be connected to, and the other end of above-mentioned 3rd pipeline may be connected to above-mentioned first pipeline.
In addition, above-mentioned cooling end may include at least one cooling worm.
In addition, above-mentioned VOC removal device may also include second mistake adjacent with above-mentioned first filter
Filter, and above-mentioned cooling worm may include the first cooling worm and the second cooling worm, wherein above-mentioned first cooling worm, on
Stating the first filter, above-mentioned second filter and above-mentioned second cooling worm can sequentially arrange along above-mentioned first pipeline.
In addition, above-mentioned cooling end may include heat exchanger and cooling worm, and above-mentioned heat exchanger and above-mentioned cooling rotation
Pipe can be along above-mentioned first pipe arrangement.
In addition, above-mentioned VOC removal device may also include front end filter, the front end filter along
Above-mentioned first pipe arrangement and it is arranged between above-mentioned stove and above-mentioned cooling end.
VOC minimizing technology according to an embodiment of the present invention may include following steps：Bag is provided
Pollution air containing VOC；The above-mentioned pollution air being provided is cooled down；And make the above-mentioned of cooling
Contaminated enters filter house and adsorbs the VOC being included in above-mentioned pollution air.
In addition, the step of being cooled down to the above-mentioned pollution air being provided may include to make extraneous air using heat exchanger
The step of heat exchange being carried out with above-mentioned pollution air.
In addition, at least a portion in above-mentioned pollution air is liquefied by cooling down above-mentioned pollution air, and it is above-mentioned
The step of method may also include processing and store above-mentioned liquefied pollution air.
According to the embodiment of the present invention, it can adsorb and remove from the pollution air comprising VOC and wave
Hair property organic compound.
Air thermal pollution caused by the heat that the pollution air because of high temperature has can be prevented.
Above illustrated content is not limited to according to the effect of embodiment of the present invention, and is included in this specification
More various effect.
Brief description of the drawings
Fig. 1 is the block diagram of VOC removal device according to an embodiment of the present invention.
Fig. 2 is the process chart of VOC removal device according to an embodiment of the present invention.
Fig. 3 is the part of the heat exchanger of VOC removal device according to an embodiment of the present invention
Enlarged drawing.
Fig. 4 is the magnified partial view of the heat exchanger of the VOC removal device according to Fig. 3 modified example.
Fig. 5 is the process chart of the VOC removal device according to another embodiment of the present invention.
Fig. 6 is the process chart of the VOC removal device according to another embodiment of the present invention.
Fig. 7 is the process chart of the VOC removal device according to another embodiment of the present invention.
Fig. 8 is the process chart of the VOC removal device according to another embodiment of the present invention.
Fig. 9 is the process chart of the VOC removal device according to another embodiment of the present invention.
Figure 10 is the process chart of the VOC removal device according to another embodiment of the present invention.
Figure 11 is the process chart of the VOC removal device according to another embodiment of the present invention.
Embodiment
With reference to the embodiment being described in detail below in association with accompanying drawing, advantages and features of the invention and realize described excellent
The method of point and feature will become clear and definite.But, the present invention is not limited to embodiment as disclosed hereinafter, but can realize
For variform different from each other.These embodiments are intended merely to make disclosure of the invention complete and in order to by the model of invention
Enclose and intactly inform and provided to those skilled in the art, and the present invention is only by claims
Scope is defined.
It should be appreciated that although first, second grade is used to describe a variety of inscapes, these inscapes are not arranged by these
Diction limitation.These wording are only used for distinguishing an inscape and other inscapes.Therefore, it should be appreciated that without departing substantially from
In the case of the technological thought of the present invention, the first inscape hereinafter referred to is alternatively referred to as the second inscape.
Hereinafter, refer to the attached drawing is illustrated to embodiments of the present invention.Although in this manual with according to the present invention
Display device be illustrated for the example of liquid crystal display device, but be not restricted to that this, and it has been equally applicable to
The situation of machine luminous display unit.
Fig. 1 is the block diagram of VOC removal device according to an embodiment of the present invention.
Reference picture 1, VOC removal device according to an embodiment of the present invention is included including offer
The pollution air supply unit OV of the pollution air of VOC, make contaminated enter and cool down pollution air it is cold
But portion RE and make by cooling end RE contaminated to enter and adsorb the volatile organic compound included in pollution air
The filter house FI of thing.
Pollution air supply unit OV can be generated comprising VOC (VOC, Volatile Oxide
Compound pollution air).In this manual, VOC (VOC, Volatile Oxide
Compound) it is understood to be the general designation of the organic compound for holding evaporable liquid phase or gas phase because of high-vapor-pressure.Example
Such as, VOC (VOC, Volatile Oxide Compound) may include to be selected from by benzene (Benzene, C6H6)、
Formaldehyde (Formaldehyde, HCHO), toluene (Toluene, C7H8), dimethylbenzene (Xylene, C6H4(CH3)), ethene
(Ethylene, CH2=CH2), styrene (Styrene, C8H8) and acetaldehyde (Acetaldehyde, CH3CHO) in the group constituted
Material more than any one.In addition, VOC (VOC, Volatile Oxide Compound) may include
Trigger the stench releaser of stench in air.
Pollution air supply unit OV can discharge the pollution air of high temperature.In the exemplary embodiment, the temperature of air is polluted
Degree can be in the range of 100 DEG C to 600 DEG C.However, the temperature of pollution air is not limited to this, and in this manual,
" the pollution air of high temperature " refer to due to include heating process in special process and it is issuable, with normal temperature more than
The general name of the gas of temperature.
Pollution air supply unit OV may include the stove with heating function.In this manual, stove refers to include to object
The device for all means that the temperature of body is heated, and it is not only restricted to its specific heating means.
It can be flowed into cooling end RE by the pollution air supply unit OV pollution air provided.Cooling end RE plays reduction pollution
The effect of the temperature of air.Exemplarily, the temperature for polluting air can be down to less than 40 DEG C by cooling end RE.In this process
In, the part in pollution air can be by condensing and liquefy.VOC according to an embodiment of the present invention
Removal device may also include the discharger for handling the above-mentioned pollution air being liquefied.Will be hereinafter detailed to this progress
Explanation.
Cooling end RE is as reducing the means of the temperature from the pollution air supply unit OV pollution air flowed into, and it can
Including heat exchanger.Heat exchanger can be the air cooling heat exchanger cooled down using extraneous air to pollution air.More
In detail, heat exchanger can trigger both thermal equilibrium states by making extraneous air and pollution air carry out heat exchange, from
And reduce the temperature of pollution air.In other words, the inside of heat exchanger can be disposed with the pipeline for entering contaminated and make
The pipeline that extraneous air is flowed into, at this moment, can be by will connect the contaminated pipeline entered and the pipeline for flowing into extraneous air
Touch to trigger both heat exchanges.In this case, two kinds of air will not be mixed, and can pass through the heat transfer via pipeline
And trigger thermal balance.That is, the temperature of pollution air can relatively be declined by extraneous air, and the temperature of extraneous air can lead to
Cross the temperature of pollution air and relatively rise.
In a heat exchanger, the pollution air of cooling can be flowed into the filter house FI that will be described hereinafter.In heat exchange
The extraneous air heated up in device can be expelled to outside again, or can flow into pollution air supply unit to reuse.Will be
Hereinafter this is described in detail.
In another exemplary embodiment, cooling end RE may include cooling worm to reduce from pollution air supply unit OV
The temperature of the pollution air of inflow.Polluting air can be cooled when by cooling worm.Specifically, such as freon refrigerant
Transmitted via cooling worm, and the pollution air of high temperature gradually cools when by cooling worm.It is therein a part or
All can be condensing, and may also include discharger to handle liquefied pollution air.Hereinafter discharger will be carried out
Describe in detail.
In certain embodiments of the present invention, cooling end RE may include more than one heat exchanger and/or one with
On cooling worm.That is, cooling end RE may be configured as including one or more heat exchangers, or may be configured as including one
Or multiple cooling worms.In addition, cooling end RE can also include more than one heat exchanger and more than one cooling simultaneously
Coil.
It can be flowed into by cooling end RE pollution air along pipeline in filter house FI.
Filter house FI purifying contaminated air.Therefore, filter house FI may filter that the volatility included in pollution air is organic
Compound (VOC) and/or the stench releaser for triggering stench.Filter house FI may include to adsorb VOC
(VOC) and/or trigger stench stench releaser filter with filter VOC (VOC) and/or initiation
The stench releaser of stench.
Filter house FI can have one or more filters.Drawn according to VOC (VOC) or stench
The species of stimulating food matter, filter may include physical absorbent or chemosorbent.Physical absorbent or chemosorbent can
It is selectively applied or is together applied.In other words, filter may include to be selected from by physical absorbent and chemisorbed
Adsorbent more than any one in the group that agent is constituted.
Above-mentioned physical absorbent or chemosorbent also may be configured as including moisture.In physical absorbent or chemistry
Adsorbent is configured in the case of including moisture, may be such that the removal of water miscible VOC (VOC) becomes to hold
Easily.
The filter in filter house FI is applied to may include porous material with capturing volatile organic compound (VOC)
And/or trigger the stench releaser of stench.Exemplarily, filter may be configured as including being selected from macromolecule, zeolite, activity
Material more than any one in charcoal, metal oxide and ceramics.It is configured to include porous as described above in filter
In the case of material, the stench releaser of VOC (VOC) and/or initiation stench included in pollution air
Matter can be trapped on the porous material of filter with molecular forms.
Filter may include to contribute to capturing volatile organic compound (VOC) and/or trigger the stench releaser of stench
The catalyst of matter, to lift the strainability of filter.Exemplarily, catalyst can be platinum system oxidation catalyst.Platinum
Be oxidation catalyst as low temperature system oxidation catalyst, it can mixed aluminium oxides (Al2O3) and platinum (Pt) and constitute.It is this to urge
Agent can be used in 200 DEG C to 300 DEG C of temperature range.As another example, catalyst can be nickel cobalt system oxidation catalysis
Agent.Nickel cobalt system oxidation catalyst is as high temperature system oxidation catalyst, and it is by mixed aluminium oxides (Al2O3) and nickel cobalt material structure
Into.This catalyst can be used in more than 300 DEG C temperature ranges.
Filter house FI can be used alone above-mentioned various ways filter or multiple filterings of aforesaid way are applied in combination
Device.That is, filter house FI may be configured as the multiple filters for including performing function different from each other.That is, filter house FI may include choosing
The filter of free applied chemistry adsorbent, the filter of Applied Physics adsorbent, the filter being made up of porous material and
More than one filter in the group that the filter of applications catalyst is constituted.That is, filter house FI may include with different from each other
Function filter combination.
The filter of multiple species included by filter house FI can have proper temperature.In other words, filter can be
The strainability of lifting has been given play under specified temp.That is, pollution air is not directly transferred to filter house as above
Transmit in FI but via cooling end RE, so as to lift filter house FI detergent power.
Hereinafter, the more specific embodiment to the present invention is illustrated.
Fig. 2 is the process chart of VOC removal device according to an embodiment of the present invention.
Reference picture 2, VOC removal device according to an embodiment of the present invention is included including offer
The stove OV1 of the pollution air of VOC, make contaminated enter and cool down pollution air heat exchanger EX1,
The contaminated through over-heat-exchanger EX1 is set to enter and adsorb first of the VOC included in pollution air
Filter F I1, be connected with stove OV1 and transmit from stove OV1 provide pollution air and via heat exchanger EX1 and first filter
First pipeline L1 of the externally connected gases of device FI1 and externally connected gas and the outside sky of heat exchanger EX1 transmission
The second pipe L2 of gas.
It is empty that stove OV1 can generate the pollution comprising VOC (VOC, Volatile Oxide Compound)
Gas.
Stove OV1 can discharge the pollution air of high temperature.In the exemplary embodiment, the temperature of pollution air can be 100
DEG C to 600 DEG C.However, the temperature not limited to this of pollution air, and in this manual, the pollution air of high temperature is understood that
For because including heating process in special process and the general name of gas issuable, with temperature more than normal temperature.
Stove OV1 may include the means for making subject heat up, and its concrete mode is unrestricted.Exemplarily, stove OV1 can
To be the stove used in the baking process of liquid crystal display device.In this case, the temperature of pollution air can be 150 DEG C
To 230 DEG C.However, what this was merely exemplary, and the scope of the present invention is not limited by above-mentioned flow-route and temperature.
The pollution air generated in stove OV1 can be via the first pipeline L1 inflow heat exchangers that will be described hereinafter
In EX1.Heat exchanger EX1 may be arranged inside closed first chamber CH1.First chamber CH1 can provide with extraneous air every
Exhausted space.Because first chamber CH1 provides the space completely cut off with extraneous air as described above, therefore, it is possible to prevent anticipation not
The inflow of the extraneous air arrived and due to pollute air outflow caused by outside air pollution.
Heat exchanger EX1 can reduce the temperature from the stove OV1 pollution air flowed into.That is, heat exchanger EX1 can be utilized
The air cooling heat exchanger of the temperature of extraneous air reduction pollution air.Specifically, heat exchanger EX1 can be by making extraneous air
Carry out heat exchange to trigger both thermal equilibrium states with pollution air, so as to reduce the temperature of pollution air.To this in other words,
The extraneous air of normal temperature can be via in the second pipe L2 inflow heat exchangers EX1 that will be described hereinafter.Move pollution air
The first dynamic pipeline L1 and the second pipe L2 for moving extraneous air can be contacted in heat exchanger EX1 internal physicals.The
One pipeline L1 and second pipe L2 heat exchange can occur by both physical contacts.That is, the pipes of the first pipeline L1 and second
Road L2 thermal balance can be triggered by the heat transfer according to the first pipeline L1 and second pipe L2 contact.That is, due to first
Pipeline L1 and second pipe L2 contacts, the temperature of the first pipeline L1 with relatively-high temperature can decline, and with relative low temperature
Second pipe L2 temperature can rise.Thus, it can decline by the temperature of the first pipeline L1 pollution air, and pass through
The temperature of two pipeline L2 extraneous air can rise.That is, by taking this mode, it can not mixed in pollution air and extraneous air
Heat exchange is carried out in the case of conjunction.
Reference picture 3 and Fig. 4 are said to the first pipeline L1 and second pipe the L2 mode contacted in heat exchanger EX1
It is bright.
Fig. 3 is the part of the heat exchanger of VOC removal device according to an embodiment of the present invention
Enlarged drawing.
Reference picture 3, the first pipeline L1 and second pipe L2 can be in direct contact with one another in heat exchanger EX1.
As described above, the first pipeline L1 and second pipe L2 can carry out heat exchange by conduction pattern.Thus, the first pipeline
L1 and second pipe L2 contact area are bigger, and heat exchange can carry out easier.For the first pipeline L1 of increase and second pipe
L2 contact area, the first pipeline L1 and second pipe L2 can be connected to each other with predetermined length.In other words, can be with wrapped around one another
(twist)。
Fig. 4 is the magnified partial view of the heat exchanger of the VOC removal device according to Fig. 3 modified example.
Reference picture 4, the first pipeline L1 and second pipe L2 can be in the state of adjacent to each other with more than one curved
The mode of pars convoluta extends.As described above, the first pipeline L1 and second pipe L2 contact area can be increased using various ways.
Exemplarily, the mode that the first pipeline L1 and second pipe L2 can have more than one bending section extends.In other words,
One pipeline L1 and second pipe L2 predetermined lengths adjacent to each other, wherein adjacent part can include bent portion at least in part.
That is, the first pipeline L1 and second pipe L2 can have the mode of the form of fold each other adjacent.
By referring again to Fig. 2 to the other of VOC removal device according to an embodiment of the present invention
Structure is illustrated.
Pollution air through over-heat-exchanger EX1 can be flowed into the first filter F I1 via the first pipeline L1.First filtering
Device FI1 may be arranged in closed second chamber CH2.Second chamber CH2 can provide the space completely cut off with extraneous air.Because the
Two cavity C H2 provide the space completely cut off with extraneous air as described above, therefore, it is possible to prevent unexpected extraneous air
Flow into and due to air pollution caused by the outflow of pollution air.
Second chamber CH2 can be connected with first chamber CH1.That is, first chamber CH1 and second chamber CH2 can share closed
Space.But be not restricted to that this, the space with external environment can be also provided independently in second chamber CH2 and first chamber CH1.
The effect for the pollution air that the executable purifications of first filter F I1 are flowed into.Therefore, according to VOC
(VOC) or stench releaser species, the first filter F I1 may include physical absorbent or chemosorbent.Physics
Adsorbent or chemosorbent can be selectively applied or together be applied.In other words, the first filter F I1 can be wrapped
Include adsorbent more than any one in the group being made up of physical absorbent and chemosorbent.
Above-mentioned physical absorbent or chemosorbent may be configured as including moisture.Inhaled in physical absorbent or chemistry
Attached dose is configured in the case of including moisture, and may be such that the removal of water miscible VOC (VOC) becomes easy.
First filter F I1 may include porous material with capturing volatile organic compound (VOC) and/or trigger stench
Stench releaser.
Exemplarily, the first filter F I1 may be configured as including selected from macromolecule, zeolite, activated carbon, metal oxide and
Material more than any one in ceramics.In the case where filter is configured to include porous material as described above, bag
The VOC (VOC) and/or the stench releaser of initiation stench being contained in pollution air can be with molecule shapes
Formula is trapped on porous material included in the first filter F I1.
First filter F I1 may include to contribute to capturing volatile organic compound (VOC) and/or trigger the stench of stench
The catalyst of releaser is to lift the first filter F I1 strainability.Exemplarily, catalyst can be the oxidation of platinum system
Catalyst.Platinum system oxidation catalyst is as low temperature system oxidation catalyst, and it can mix aluminum oxide (Al2O3) and platinum (Pt) and
Constitute.This catalyst can be used in 200 DEG C to 300 DEG C of temperature range.As it is another illustrate, catalyst can be nickel/
Cobalt system oxidation catalyst.Nickel cobalt system oxidation catalyst is as high temperature system oxidation catalyst, and it is by having mixed aluminum oxide (Al2O3) and
The material of nickel cobalt is constituted.This catalyst can be used in more than 300 DEG C temperature ranges.
That is, the first filter F I1 can be selected from the filter by applied chemistry adsorbent, the mistake of Applied Physics adsorbent
A filter in the group that the filter of filter, the filter being made up of porous material and applications catalyst is constituted.
VOC removal device according to an embodiment of the present invention may include the first pipeline L1 and
Two pipeline L2.
First pipeline L1 one end can be connected with stove OV1, and can transmit the pollution air generated by stove OV1.That is, first
Pipeline L1 provides the passage for moving pollution air.First pipeline L1 is connected with heat exchanger EX1, and will can be given birth to by stove OV1
Into pollution air transmit to heat exchanger EX1.Because arrangements of the first pipeline L1 inside heat exchanger EX1 and above institute
The arrangement of elaboration is identical, therefore will omit detailed description thereof.Then, the first pipeline L1 can will be cold in heat exchanger EX1
But pollution air is transmitted to the first filter F I1.That is, the first pipeline L1 can be connected with the first filter F I1.By the first filtering
Device FI1 filtered airs can be expelled to outside via the first pipeline L1.To make the discharge of pollution air smooth, the first pipeline L1's
The other end can be disposed with first exhaust fan Fan o 1.First exhaust fan Fan o 1 can will by the first filter F I1 and it is net
The pollution air of change is expelled to outside.
That is, the first pipeline L1 one end can be connected with stove OV1, and the first pipeline L1 other end can be with first exhaust fan
Fan o 1 are connected.In other words, the first pipeline L1 can be connected with stove OV1, and can be filtered via heat exchanger EX1 and first
Device FI1 and first exhaust fan Fan o 1 and ft connection.
More than any one in second pipe L2 one end and the other end it can be connected with extraneous gas.Therefore, the second pipe
Road L2 one end can be disposed with inflow fan Fan i.The work for making extraneous air flow into second pipe L2 can be played by flowing into fan Fan i
With.As described above, the extraneous air flowed into via second pipe L2 can be in inflow heat exchanger EX1.It is complete by heat exchanger EX1
Extraneous air into the heat exchange of the pollution air with being moved in the first pipeline L1 can be expelled to outside via second pipe L2
Gas.The second pipe L2 other end can be disposed with second exhaust fan Fan o 2, be become with causing second pipe L2 outer machine to discharge
Obtain easily.That is, second pipe L2 one end can be connected by flowing into fan Fan i with extraneous gas, and second pipe L2's is another
One end can be connected by second exhaust fan Fan o 2 with extraneous gas.In other words, extraneous air can be via being arranged in the second pipe
The inflow fan Fan i of road L2 end flow into and through heat exchanger EX1, via being arranged at the second pipe L2 other end
Second exhaust fan Fan o2 be expelled to outside.
Triggered by the heat exchanger EX1 volatile contaminant materials and/or stench being cooled to close to the pollution air of normal temperature
Material is filtered by the first filter F I1, therefore it can be the air close to the cleaning of normal temperature to be expelled to the air of outside.Thus,
The thermal pollution of the extraneous air occurred because discharging the hot air with high temperature can be prevented and because discharge includes volatility
Organic compound and/or the air of stench releaser and the pollution of extraneous air occurred.
The VOC removal device according to another embodiment of the present invention will hereinafter be illustrated.
In the following embodiments, the structure identical structure with having illustrated will be referred to identical reference, and will
Omit or simplify repeat specification.
Fig. 5 is the process chart of the VOC removal device according to another embodiment of the present invention.
Reference picture 5, the difference with Fig. 2 embodiment is, in the volatility according to another embodiment of the present invention
In organic compound removal device, the second pipe L2 other end is connected with stove OV1.
The second pipe L2 other end can be connected with stove OV1.When constituting heat exchange as described above in heat exchanger EX1
When, the temperature by the first pipeline L1 pollution air can decline, and pass through second pipe L2 extraneous air temperature can on
Rise., can be through the over-heat-exchanger EX1 extraneous airs heated up in the case that the second pipe L2 other end is connected with stove OV1
It is used again in stove OV1.Thereby, it is possible to prevent to be expelled to thermal pollution problem outside and occurring because of the air of high temperature,
And the energy required for being saved by recycling used heat in technique.
Fig. 6 is the process chart of the VOC removal device according to another embodiment of the present invention.
Reference picture 6, discharger DR is may also include according to the VOC removal device of another embodiment of the present invention.
As described above, pollution some or all of air moved in the first pipeline L1 can be by heat exchanger
EX1 is condensing and liquefies.In this case, liquefied pollution air can be stored in accumulator tank 100 by discharger DR.For
This, may also include according to the VOC removal device of another embodiment of the present invention and connect with heat exchanger EX1
Connect and transmit liquefied pollution air to discharger DR the 3rd pipeline L3.
Discharger DR may include first row ejecting plate DR_1 and second row ejecting plate DR_2.By cold in heat exchanger EX1
Condensing pollution air can be transmitted to discharger DR via the 3rd pipeline L3.In this process, liquefied pollution is empty
Gas can be stored in first row ejecting plate DR_1.The liquefaction pollution air being stored in first row ejecting plate DR_1 can be via the 3rd pipeline
L3 is moved to second row ejecting plate DR_2.Although not shown in figures, measurement storage can be disposed with second row ejecting plate DR_2
There is the first water level regulation sensor S1 that the water level of air is polluted in the liquefaction in second row ejecting plate DR_2.It is arranged in the second discharge
The liquefaction that the first water level regulation sensor S1 in plate DR_2 can store more than certain water level in second row ejecting plate DR_2 pollutes empty
The water level of sensing liquefaction pollution air during gas.The liquefaction pollution air being stored in second row ejecting plate DR_2 can be continued on through by the 3rd
Pipeline L3 is stored into accumulator tank 100.The liquefaction pollution sky that sensing is stored in accumulator tank 100 can be disposed with accumulator tank 100
Second water level regulation sensor S2 of the water level of gas.Second water level regulation sensor S2, which can be monitored, to be stored in accumulator tank 100
The amount of liquefaction pollution air, and informed this to user when air is polluted in the liquefaction for storing more than certain water level to lead back to
Receive the replacing of groove 100.
When liquefaction pollution air is stored in accumulator tank 100, the part in liquefaction pollution air can be gasified again
Into VOC.In this case, the VOC of gasification can be moved via the 3rd pipeline L3, from
And in the first pipeline L1 before back flowing back into inflow heat exchanger EX1.That is, the 3rd pipeline L3 one end can be with heat exchanger
EX1 connections, and the 3rd pipeline L3 other end can be connected with the first pipeline L1 before inflow heat exchanger EX1.In addition, the 3rd
Check-valves V can be disposed with pipeline L3 to prevent that vaporized VOC flows back again.Specifically, check-valves V
It can be arranged in the 3rd pipeline L3 between the pipeline L1 of accumulator tank 100 and first.
Fig. 7 is the process chart of the VOC removal device according to another embodiment of the present invention.
Reference picture 7, the difference with Fig. 2 embodiment is, in the volatility according to another embodiment of the present invention
In organic compound removal device, front end filter sFI is disposed with the first pipeline L1.
Front end filter sFI can be disposed with first pipeline L1.Specifically, front end filter sFI may be arranged at stove OV1 with
Between heat exchanger EX1.Front end filter sFI can perform is entering heat exchanger EX1 by the first pipeline L1 contaminated
Filter the effect of primary pollution air in advance before.
Front end filter sFI may include to remove mist resistant filter (Demister Filter) and/or carbon filter (Carbon
Filter).Front end filter sFI is being included according to the VOC removal device of another embodiment of the present invention
In the case of, because filtering the fine unwanted particles or stench releaser of pollution air once by the first pipeline L1 in advance
Matter, therefore, it is possible to alleviate the first filter F I1 burden, and can lift VOC removal device entirety
Strainability.
Fig. 8 is the process chart of the VOC removal device according to another embodiment of the present invention.
The difference of Fig. 8 and Fig. 2 embodiment is that cooling end RE includes the first cooling worm C1, without including heat friendship
Parallel operation EX1.
It can be flowed into the first cooling worm C1 by the first pipeline L1 pollution air.First cooling worm C1 passes through fluorine profit
Gas etc. is held high to receive cold air, and thus, it is possible to reduce the temperature of the gas by the first cooling worm C1.That is, pollution air exists
Flowed into the state of being cooled down by the first cooling worm C1 via the first pipeline L1 in the first filter F I1.It is cold by first
But coil C1 and the first filter F I1 pollution air can be expelled to outside via the first pipeline L1 again, therefore, as above institute
State, first exhaust fan Fan o 1 can be disposed with the first pipeline L1 other end.Pollution is being cooled down using the first cooling worm C1
In the case of air, pollution air can be rapidly cooled down than heat exchanger EX1, and pollution air can be cooled to than logical
Cross the situation lower temperature that extraneous gas is cooled down.
Fig. 9 is the process chart of the VOC removal device according to another embodiment of the present invention.
Reference picture 9, the difference with Fig. 8 embodiment is, according to the VOC of another embodiment of the present invention
Removal device also include the second cooling worm C2 and the second filter F I2.
Second cooling worm C2 can have the structure substantially the same with the first cooling worm C1.In illustrative embodiments
In, the first cooling worm C1, the first filter F I1, the second filter F I2 and the second cooling worm C2 can be along the first pipeline L1
Sequentially arrange.
The effect for the pollution air that the executable purifications of second filter F I2 are flowed into.Therefore, according to VOC
(VOC) or stench releaser species, the second filter F I2 may include physical absorbent or chemosorbent.Physics
Adsorbent or chemosorbent can be selectively applied or together be applied.In other words, the second filter F I2 can be wrapped
Include adsorbent more than any one in the group being made up of physical absorbent and chemosorbent.
Above-mentioned physical absorbent or chemosorbent may be configured as including moisture.In physical absorbent or chemisorbed
Agent is configured in the case of including moisture, and the removal of water miscible VOC (VOC) can become easy.
Second filter F I2 may include porous material with capturing volatile organic compound (VOC) and/or trigger stench
Stench releaser.
Exemplarily, the second filter F I2 may be configured as including selected from macromolecule, zeolite, activated carbon, metal oxide and
Material more than any one in ceramics.In the case where filter is configured to include porous material as described above, bag
The VOC (VOC) and/or the stench releaser of initiation stench being contained in pollution air can be with molecule shapes
Formula is trapped on porous material included in the second filter F I2.
Second filter F I2 may include to contribute to capturing volatile organic compound (VOC) and/or trigger the stench of stench
The catalyst of releaser, to lift the second filter F I2 strainability.Exemplarily, catalyst can be platinum system oxygen
Change catalyst.Platinum system oxidation catalyst is as low temperature system oxidation catalyst, and it can mix aluminum oxide (Al2O3) and platinum (Pt)
And constitute.This catalyst can be used in 200 DEG C to 300 DEG C of temperature range.Illustrated as another, catalyst can be
Nickel cobalt system oxidation catalyst.Nickel cobalt system oxidation catalyst is as high temperature system oxidation catalyst, and it is by having mixed aluminum oxide
(Al2O3) and nickel cobalt material constitute.This catalyst can be used in more than 300 DEG C temperature ranges.
That is, the second filter F I2 can be selected from the filter by applied chemistry adsorbent, the mistake of Applied Physics adsorbent
A filter in the group that the filter of filter, the filter being made up of porous material and applications catalyst is constituted.
First filter F I1 and the second filter F I2 can be substantially the same filter or can not be each other not
Same filter.That is, the first filter F I1 and the second filter F I2 can be identical filter, or can be selected from by
Filter, the filter of Applied Physics adsorbent, the filter being made up of porous material and the application of applied chemistry adsorbent
The combination of two filters in the group that the filter of catalyst is constituted.
Also include as described above according to the VOC removal device of another embodiment of the present invention
In the case of second filter F I2, filter house FI strainability can be further lifted.
In addition, passing through the second cooling worm C2 in the pollution air by the second filter F I2 and being discharged to outside
In the case of, can more positively it prevent because of the thermal pollution of extraneous air caused by the heat that pollution air has.
Figure 10 is the process chart of the VOC removal device according to another embodiment of the present invention.
Reference picture 10, the difference with Fig. 2 embodiment is have according to the volatility of another embodiment of the present invention
Machine compound removal device includes both heat exchanger EX1 and the first cooling worm C1.
VOC removal device according to certain embodiments of the present invention may include heat exchanger EX1 and
Any one in first cooling worm C1, but can also include both simultaneously.In this case, pollution air can be via
First pipeline L1 flows serially through heat exchanger EX1 and the first cooling worm C1.Pass through repeated application heat exchanger EX1 and first
Cooling worm C1, so as to lift cooling end RE1 cooling performance to greatest extent, and may be because thus, it is possible to completely cut off in advance
Pollution air have heat and occur extraneous air thermal pollution.
Figure 11 is the process chart of the VOC removal device according to another embodiment of the present invention.
Reference picture 11, the difference with Figure 10 embodiment is, according to the volatility of another embodiment of the present invention
Organic compound removal device also includes the second filter F I2 and the second cooling worm C2.
As described above, VOC removal device according to certain embodiments of the present invention can include simultaneously
Heat exchanger EX1 and cooling worm.
Second cooling worm C2 can have the structure substantially the same with the first cooling worm C1.In illustrative embodiments
In, heat exchanger EX1, the first cooling worm C1, the first filter F I1, the second filter F I2 and the second cooling worm C2 can edges
The first pipeline L1 sequentially to arrange.
Also include as described above according to the VOC removal device of another embodiment of the present invention
In the case of second filter F I2, filter house FI strainability can be further lifted.
In addition, passing through the second cooling worm C2 in the pollution air by the second filter F I2 and being discharged to outside
In the case of, it can positively prevent the thermal pollution of the extraneous air caused by the heat that pollution air has.
Hereinafter, VOC minimizing technology according to an embodiment of the present invention will be said
It is bright.VOC minimizing technology according to an embodiment of the present invention can be using above-mentioned according to some of the invention
The removal device of the VOC of embodiment, but be not restricted to that this.One of the structure being described below
Dividing can be identical with the structure of VOC removal device above according to certain embodiments of the present invention, therefore
To avoid repeat specification, the explanation to part-structure will be omitted.
VOC minimizing technology according to an embodiment of the present invention comprises the following steps：There is provided to include and wave
The pollution air of hair property organic compound；The pollution air being provided is cooled down；And enter the contaminated of cooling
In first filter and adsorb be included in pollution air in VOC.
First, the step of can carrying out providing the pollution air comprising VOC.VOC
It can be provided by pollution air supply unit.Exemplarily, pollution air supply unit may include stove, and can generate and provide in stove
The pollution air of high temperature.Pollute air supply unit and stove can be with volatility hereinbefore according to certain embodiments of the present invention
Illustrated pollution air supply unit and stove are substantially the same in organic compound removal device.Therefore, it can directly be used
Explanation in Fig. 1 and Fig. 2.
Next, the step of cooled down to the pollution air of offer.The pollution air of offer is cooled down
Step may include via heat exchanger EX1 by the heat exchange with extraneous air come to pollution air cool down the step of or
The step of person is cooled down using cooling worm to pollution air.Heat exchanger EX1 and cooling worm can be with hereinbefore bases
Illustrated heat exchanger EX1 and cooling worm in the VOC removal device of some embodiments of the present invention
It is substantially the same.Therefore, the explanation for Fig. 2 and Fig. 9 can directly be used to it, so detailed description thereof will be omitted.
Next, the contaminated that can enter to exercise cooling enters filter house and adsorbed to be included in waving in above-mentioned pollution air
The step of hair property organic compound.The adsorbable VOC being included in pollution air of filter house.Filter house can
It is substantial with filter house illustrated in VOC removal device according to certain embodiments of the present invention
It is identical.Therefore detailed description thereof will be omitted.
According to the VOC minimizing technology of another embodiment of the present invention may also include recovery by pair
The step of liquefaction pollution air that the step of pollution air being provided is cooled down produces.Pollute at least a portion in air
It can be liquefied by cooling down pollution air.The recovery of liquefied pollution air can be performed by discharger DR.Discharger DR
Can be substantially the same with the discharger DR of VOC removal device according to certain embodiments of the present invention.
Therefore, can be directly using explanation above to Fig. 6 to it.
Although embodiment of the present invention is illustrated above with reference to accompanying drawing, the technical field of the invention
Technical staff be appreciated that the present invention can not change the present invention technological thought or essential feature in the case of be embodied as it
Its concrete form.It will be understood, therefore, that above described embodiment is exemplary, and non-limiting in all respects
Property.
The explanation of reference
OV：Pollute air supply unit
RE：Cooling end
FI：Filter house
OV1：Stove
CH1、CH2：Chamber
EX1：Heat exchanger
L1：First pipeline
L2：Second pipe
Fan i：Flow into fan
Fan o 1、Fan o 2：Exhaust fan
FI1：First filter
DR：Discharger
DR_1：First row ejecting plate
DR_2：Second row ejecting plate
S1、S2：Water level regulation sensor
V：Check-valves
100：Accumulator tank
C1、C2：Cooling worm
Claims (20)
1. a kind of VOC removal device, including：
Polluting air supply unit, there is provided the pollution air comprising VOC；
Cooling end, enters the contaminated and cools down the pollution air；And
Filter house, makes by the contaminated of the cooling end to enter and adsorb described in included in the pollution air
VOC.
2. VOC removal device according to claim 1, wherein, the cooling end includes：
Heat exchanger, makes extraneous air carry out heat exchange with the pollution air.
3. VOC removal device according to claim 1, wherein, the cooling end includes：
Cooling worm, is cooled down to the pollution air.
4. VOC removal device according to claim 1, wherein, at least one in the pollution air
Part is liquefied by the cooling end,
Wherein, the VOC removal device also includes：
Discharger, handles the liquefied pollution air.
5. VOC removal device according to claim 1, wherein,
The filter house include at least one filter, the filter include be selected from by applied chemistry adsorbent filter,
In the group that the filter of the filter of Applied Physics adsorbent, the filter being made up of porous material and applications catalyst is constituted
More than one filter.
6. a kind of VOC removal device, including：
There is provided the pollution air comprising VOC for stove；
Cooling end, enters the contaminated and cools down the pollution air；
First filter, makes by the contaminated of the cooling end to enter and adsorb included in the pollution air
The VOC；
First pipeline, is connected to the stove to transmit the pollution air that is provided by the stove and via the cooling end
With the externally connected gas of the first filter；And
Second pipe, is connected to the extraneous gas and transmits extraneous air to the cooling end.
7. VOC removal device according to claim 6, wherein, the cooling end includes：
Heat exchanger, makes the extraneous air carry out heat exchange with the pollution air.
8. VOC removal device according to claim 7, wherein,
First pipeline is directly contacted with the second pipe in the heat exchanger.
9. VOC removal device according to claim 8, wherein,
First pipeline can be wrapped around one another with the second pipe, or with least one in the state of adjacent to each other
The mode of bending section extends.
10. VOC removal device according to claim 6, wherein,
One end of the second pipe is connected to the extraneous gas, and the second pipe the other end be connected to it is described
Stove.
11. VOC removal device according to claim 6, wherein,
First filter include be selected from by the filter of applied chemistry adsorbent, the filter of Applied Physics adsorbent, by
A filter in the group that the filter and the filter of applications catalyst that porous material is constituted are constituted.
12. VOC removal device according to claim 6, wherein, in the pollution air at least
A part is liquefied by the cooling end,
Wherein, the VOC removal device also includes：
Discharger, handles the liquefied pollution air.
13. VOC removal device according to claim 12, in addition to：
Accumulator tank, is connected with the discharger；And
3rd pipeline, connects the heat exchanger, the discharger and the accumulator tank,
Wherein, one end of the 3rd pipeline is connected to the heat exchanger, and the other end of the 3rd pipeline is connected to
First pipeline.
14. VOC removal device according to claim 6, wherein,
The cooling end includes at least one cooling worm.
15. VOC removal device according to claim 14, in addition to：
Second filter, it is adjacent with first filter,
Wherein, the cooling worm includes the first cooling worm and the second cooling worm, wherein first cooling worm, described
First filter, second filter and second cooling worm are sequentially arranged along first pipeline.
16. VOC removal device according to claim 6, wherein,
The cooling end includes heat exchanger and cooling worm, wherein the heat exchanger and the cooling worm are along described the
One pipe arrangement.
17. VOC removal device according to claim 6, in addition to：
Front end filter, along first pipe arrangement and is arranged between the stove and the cooling end.
18. a kind of VOC minimizing technology, comprises the following steps：
The pollution air for including VOC is provided；
The pollution air being provided is cooled down；And
The volatility for making the contaminated of cooling enter filter house and adsorb included in the pollution air is organic
Compound.
19. VOC minimizing technology according to claim 18, wherein, to the pollution sky being provided
The step of gas is cooled down includes：
Make the step of extraneous air carries out heat exchange with the pollution air using heat exchanger.
20. VOC minimizing technology according to claim 18, wherein, in the pollution air at least
A part is liquefied by cooling down the pollution air,
Wherein, the VOC minimizing technology also includes：
The step of handling and store the liquefied pollution air.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2016-0032969 | 2016-03-18 | ||
| KR1020160032969A KR102701361B1 (en) | 2016-03-18 | 2016-03-18 | Apparatus for filtering volatile organic compounds and method for filtering volatile organic compounds |
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| CN107198888A true CN107198888A (en) | 2017-09-26 |
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| CN201710003454.8A Pending CN107198888A (en) | 2016-03-18 | 2017-01-04 | VOC removal device and VOC minimizing technology |
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|---|---|
| JP (1) | JP7017854B2 (en) |
| KR (1) | KR102701361B1 (en) |
| CN (1) | CN107198888A (en) |
| TW (1) | TWI790995B (en) |
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| CN110523268B (en) * | 2019-07-30 | 2020-05-19 | 南京易德高臭氧有限公司 | Flue gas oxidizer for air purification |
| KR102099599B1 (en) * | 2019-09-26 | 2020-04-14 | (주)상원기계 | INDUSTRIAL HYBRID MODULE TYPE VOCs TREATING APPARATUS |
| CN110824846B (en) * | 2019-10-16 | 2022-11-08 | 武汉华星光电半导体显示技术有限公司 | Baking device and manufacturing method of display panel |
| KR102083264B1 (en) * | 2019-10-21 | 2020-03-02 | 권정선 | Hume treating apparatus and chiller for semiconductor process equipment having the same |
| JP7434891B2 (en) | 2019-12-26 | 2024-02-21 | 東洋紡エムシー株式会社 | Organic solvent recovery system |
| CN114867543B (en) * | 2019-12-26 | 2024-03-29 | 东洋纺Mc株式会社 | Organic solvent recovery system |
| KR102264527B1 (en) * | 2021-01-29 | 2021-06-14 | 주식회사 누리플랜 | Toxic gas removing system |
| TWI782670B (en) * | 2021-08-20 | 2022-11-01 | 志聖工業股份有限公司 | Drying equipment and gas drying unit |
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| CN1127993A (en) * | 1993-07-26 | 1996-07-31 | 西罗斯国际公司 | Arrangement for reducing the humidity content of a gaseous medium |
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| Publication number | Publication date |
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| TWI790995B (en) | 2023-02-01 |
| KR20170109187A (en) | 2017-09-28 |
| JP7017854B2 (en) | 2022-02-09 |
| KR102701361B1 (en) | 2024-09-02 |
| TW201733660A (en) | 2017-10-01 |
| JP2017170427A (en) | 2017-09-28 |
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