CN207056259U - Volatile organic waste gas treatment system with double treatment structures - Google Patents
Volatile organic waste gas treatment system with double treatment structures Download PDFInfo
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- CN207056259U CN207056259U CN201720795165.1U CN201720795165U CN207056259U CN 207056259 U CN207056259 U CN 207056259U CN 201720795165 U CN201720795165 U CN 201720795165U CN 207056259 U CN207056259 U CN 207056259U
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- waste gas
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- 239000007789 gas Substances 0.000 title claims abstract description 133
- 239000010815 organic waste Substances 0.000 title claims abstract description 21
- 238000003795 desorption Methods 0.000 claims abstract description 63
- 239000002912 waste gas Substances 0.000 claims abstract description 49
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 46
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000010457 zeolite Substances 0.000 claims abstract description 46
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 32
- 238000010521 absorption reaction Methods 0.000 claims abstract description 27
- 239000000112 cooling gas Substances 0.000 claims abstract description 14
- 238000001179 sorption measurement Methods 0.000 claims description 122
- 239000000463 material Substances 0.000 claims description 106
- 238000002336 sorption--desorption measurement Methods 0.000 claims description 45
- 238000001816 cooling Methods 0.000 claims description 24
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 claims description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 9
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 9
- 239000000920 calcium hydroxide Substances 0.000 claims description 9
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 9
- 235000012489 doughnuts Nutrition 0.000 claims description 9
- 239000002808 molecular sieve Substances 0.000 claims description 9
- 239000000741 silica gel Substances 0.000 claims description 9
- 229910002027 silica gel Inorganic materials 0.000 claims description 9
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 9
- 229910021389 graphene Inorganic materials 0.000 claims description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 7
- 238000002485 combustion reaction Methods 0.000 claims description 5
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 10
- 230000007613 environmental effect Effects 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 7
- 230000009977 dual effect Effects 0.000 description 6
- 239000004065 semiconductor Substances 0.000 description 3
- 241000208340 Araliaceae Species 0.000 description 2
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 2
- 235000003140 Panax quinquefolius Nutrition 0.000 description 2
- 210000001015 abdomen Anatomy 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 235000008434 ginseng Nutrition 0.000 description 2
- 230000005693 optoelectronics Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
Abstract
A volatile organic waste gas treatment system with double treatment structures comprises a waste gas inlet pipeline, a zeolite rotating wheel, a clean gas discharge pipeline, a cooling gas inlet pipeline, an incinerator, a concentrated waste gas pipeline and a chimney, and is characterized in that the clean gas discharge pipeline is provided with an absorption and desorption structure, the absorption and desorption structure is provided with a waste gas output pipeline and a heat source pipeline, the waste gas output pipeline is connected to the waste gas inlet pipeline, the heat source pipeline is connected to the incinerator, therefore, gas output by the clean gas discharge pipeline can be treated by the absorption and desorption structure to carry out concentrated waste gas, and concentrated waste gas treated by the absorption and desorption structure is conveyed back to the waste gas inlet pipeline by the waste gas output pipeline, so that the treatment efficiency of the waste gas can reach 97 percent or even more than 99 percent under the double-structure treatment, and has the environmental protection effects of energy saving and carbon reduction.
Description
Technical field
The utility model relates to a kind of volatide organic waste gas treating system for having double processing structures, espespecially a kind of energy
It will be transmitted back to again by the exhaust output tube road in the gas inlet pipeline by the concentration waste gas handled by adsorption desorption structure,
And the exhaust-gas treatment of the factory building suitable for semiconductor industry, opto-electronics or chemical industry related industry.
Background technology
As environmental consciousness comes back, in order to reduce the pollution to air, the discharge that government starts for chimney is stipulated more
Strict standard, its reduction rate, which should be greater than, especially to be Qiang Zhiyaoqiud to volatile organic waste gas caused by semiconductor related industry
90% or total release be less than 0.6kg/hr.
Mostly it is that adsorption desorption is carried out with a zeolite runner and industry is handling its volatile organic waste gas at present, and will
Concentration volatile organic contaminant matter is burnt through incinerator again, and the clean gas by burning is emitted into air again afterwards.
It is about between 95%-97% by the effect that is reached of gas of the adsorption desorption of zeolite runner at present so, because
Waste gas will pass through zeolite runner to be adsorbed, so the adsorption effect that the flow of waste gas easily causes greatly runner reduces very much,
And the discharge standard for the gas for making to be discharged by chimney can not be lifted.
Therefore, for this creator in view of disadvantages mentioned above, the phase can propose that a kind of tool of the environmental protection efficacy with carbon reduction is double
The volatide organic waste gas treating system of processing structure, make user can easy operation assembling, be to grind think of, design group system with great concentration, with
User's convenience is provided, for the motives in writing of this creator wound to be ground.
Utility model content
Main purpose of the present utility model, it is to provide a kind of volatile organic waste gas processing system for having double processing structures
System, include a gas inlet pipeline, a zeolite runner, a net gas discharge pipe, a cooling gas air inlet pipeline, an incinerator,
The Combination Design of one concentration exhaust pipe and a chimney, it is that group is provided with an adsorption desorption knot that it, which is essentially consisted on the net gas discharge pipe,
Structure, and the adsorption desorption structure is provided with an exhaust output tube road and a thermal source pipeline, and the exhaust output tube road is to be connected to this
Gas inlet pipeline, the another thermal source pipeline is to be connected to the incinerator, thus, allows the gas exported by the net gas discharge pipe
By the adsorption desorption structure can concentrate the processing of waste gas again, and again by by the concentration waste gas handled by adsorption desorption structure
Be transmitted back to again by the exhaust output tube road in the gas inlet pipeline so that waste gas by dual structure processing under, its
Treatment effeciency can reach 97% or even more than 99%, and the environmental protection efficacy with carbon reduction, and then increase overall practicality.
Another object of the present utility model, it is to provide a kind of volatile organic waste gas processing system for having double processing structures
System, and by being provided with a runner in the adsorption desorption structure, the runner is for any of which such as rotary type tower, horizontal or tubulars
Kind, and the runner is provided with adsorption zone, cooling zone and desorption area, and the net gas discharge pipe is the absorption for being connected to the runner
Area, the another desorption area one end is to connect the exhaust output tube road, and the desorption area other end is to connect the thermal source pipeline, makes this de-
Attached area can be desorbed by the heat energy of the incinerator, and in being that can set up an auxiliary heater on the thermal source pipeline to have
The efficiency of the hot blast in the thermal source pipeline is lifted, treatment effeciency can be improved, and then increases overall usability.
For the above-mentioned purpose, the utility model is a kind of volatide organic waste gas treating system for having double processing structures, is
Include an a gas inlet pipeline, zeolite runner, a net gas discharge pipe, a cooling gas air inlet pipeline, an incinerator, one dense
Contracting exhaust pipe and a chimney, wherein the zeolite runner are provided with adsorption zone, cooling zone and are desorbed area, and the gas inlet pipeline
The adsorption zone for being connected to the zeolite runner, and the net gas discharge pipe be provided at the adsorption zone of the zeolite runner and the chimney it
Between, and the cooling gas air inlet pipeline is the cooling zone for connecting the zeolite runner, the another concentration exhaust pipe is provided at the zeolite and turned
Between the desorption area of wheel and the incinerator, it is characterised in that：It is that group is provided with an adsorption desorption structure on the net gas discharge pipe, and is somebody's turn to do
Adsorption desorption structure is provided with an exhaust output tube road and a thermal source pipeline, and the exhaust output tube road is to be connected to the gas inlet
Pipeline, the another thermal source pipeline is to be connected to the incinerator.
Wherein the incinerator is further any of which of heat accumulating type incinerator or direct-combustion furnace, and on the thermal source pipeline
It is further provided with an auxiliary heater.
A runner wherein is further provided with the adsorption desorption structure, the runner is its of rotary type tower, horizontal or tubular
In it is any, and the runner is provided with adsorption zone, cooling zone and desorption area, and the net gas discharge pipe is connected to the absorption of the runner
Area, the another desorption area one end connects the exhaust output tube road, and the desorption area other end connects the thermal source pipeline.
Adsorption material is wherein further provided with the runner, and the adsorption material is further activated carbon, zeolite, silica gel, activity
Aluminum oxide, molecular sieve, manganese oxide, calcium hydroxide, any of which of graphene or doughnut.
Wherein be further provided with two adsorption material buckets in the adsorption desorption structure, and the two adsorption materials bucket is used respectively as absorption and
Desorption is used, and is provided with air inlet pipeline, waste gas outlet pipe and clean gas pipeline when the adsorption material bucket is set to the absorption used time, is separately worked as
The adsorption material bucket be set to be desorbed the used time be provided with air inlet pipeline and desorption gas pipeline.
Adsorption material is wherein further provided with the adsorption material bucket of the adsorption desorption structure, and the adsorption material is further activity
Carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, calcium hydroxide, any of which of graphene or doughnut.
Multiple adsorption material buckets are wherein further provided with the adsorption desorption structure, and the plurality of adsorption material bucket is respectively as absorption
With, desorption use and cooling use, when the adsorption material bucket be set to adsorb the used time be provided with air inlet pipeline, waste gas outlet pipe and clean gas
Pipeline, and air inlet pipeline and desorption gas pipeline are provided with when the adsorption material bucket is set to the desorption used time, separately when the adsorption material bucket is set to
The cooling used time is provided with air inlet pipeline and cooling gas pipeline.
Adsorption material is wherein further respectively provided with the adsorption material bucket of the adsorption desorption structure, and the adsorption material is further activity
Carbon, zeolite, silica gel, activated alumina, molecular sieve, calcium hydroxide, any of which of graphene or doughnut.
Wherein the adsorption material bucket is further set to the hollow long cylinder bodily form, hollow cuboid or the hollow ball bodily form.
The beneficial effects of the utility model are that it can be taken off by the suction again by the gas that the net gas discharge pipe is exported
Attached structure concentrate the processing of waste gas, and again will be defeated by the waste gas again by the concentration waste gas handled by adsorption desorption structure
Go out pipeline to be transmitted back in the gas inlet pipeline so that under by dual structure processing, its treatment effeciency can reach waste gas
97% or even more than 99%, and the environmental protection efficacy with carbon reduction, and then increase overall practicality.
Brief description of the drawings
In order to be further understood that feature, feature and technology contents of the present utility model, refer to below in connection with this
The detailed description of utility model and accompanying drawing, only appended accompanying drawing only provides uses with reference to explanation, is not used to limit the utility model, its
In：
Fig. 1 is the structural representation of the utility model Major Systems.
Fig. 2 is that the adsorption desorption structure of the utility model Major Systems is the structural representation of runner.
Fig. 3 is that the adsorption desorption structure of the utility model Major Systems has the structural representation of two adsorption material buckets.
Fig. 4 is that the adsorption desorption structure of the utility model Major Systems has the structural representation of multiple adsorption material buckets.
Fig. 5 is that the adsorption desorption structure of the utility model Major Systems has another structural representation of multiple adsorption material buckets.
Embodiment
Fig. 1 to Fig. 5 is referred to, is the schematic diagram for the utility model embodiment, and the double processing knots of tool of the present utility model
The preferred forms of the volatide organic waste gas treating system of structure are to apply to semiconductor industry, opto-electronics or chemical industry correlation
The exhaust-gas treatment of the factory building of industry so that for waste gas under by dual structure processing, its treatment effeciency can reach 97% even
More than 99%, and the environmental protection efficacy with carbon reduction, make that there is its practicality.
And the Major Systems of the volatide organic waste gas treating system of the double processing structures of tool of the present utility model are to include
One gas inlet pipeline 10, a zeolite runner 20, a net gas discharge pipe 30, one cool down gas air inlet pipeline 40, an incinerator 50,
The one concentration chimney 70 (as shown in Figures 1 and 2) of exhaust pipe 60 and one, wherein the zeolite runner 20 also can be using other absorption
The concentration runner of material, and the zeolite runner 20 is provided with adsorption zone 21, cooling zone 22 and desorption area 23, so that waste gas can be carried out
Adsorb and by waste gas desorption into concentration waste gas, the another incinerator 50 can be heat accumulating type incinerator (RTO) or direct-combustion furnace (TO)
Etc. any of which.
And the gas inlet pipeline 10 is the adsorption zone 21 for connecting the zeolite runner 20, so that the absorption of the zeolite runner 20
The waste gas in the gas inlet pipeline 10 can be adsorbed in area 21, and the other end of the adsorption zone 21 of the zeolite runner 20 is then connected with net gas
Discharge pipe 30, the net gas discharge pipe 30 are to be then connected to the chimney 70, by by the adsorption zone 21 of the zeolite runner 20
The gas (gas reaches discharge standard because concentration reduces) less than standard value adsorbed can be via the net gas delivery pipe
Road 30 is discharged to be delivered to the chimney 70, and wherein the gas inlet pipeline 10 is connected to the adsorption zone 21 of the zeolite runner 20
Between be that can be pumped the waste gas in the gas inlet pipeline 10 to the zeolite runner 20 by a blower fan (not shown)
Adsorption zone 21 in, and the net gas discharge pipe 30 between the adsorption zone 21 of the zeolite runner 20 and the chimney 70 can also be provided with
One blower fan (not shown), arranged being pumped the gas in the net gas discharge pipe 30 to chimney 70 by the air exhauster
Put.
The another cooling gas air inlet pipeline 40 is the cooling zone 22 for connecting the zeolite runner 20, and the cooling gas air inlet pipeline 40
It is inside to convey fresh air, is used by the fresh air to provide the cooling of the cooling zone 22 of the zeolite runner 20, and the cooling
Gas air inlet pipeline 40 is to be then connected to a heater 80, the fresh air in the cooling gas air inlet pipeline 40 is turned by the zeolite
It can be delivered in heater 80 and be heated behind the cooling zone 22 of wheel 20, and the heater 80 is then connected to the zeolite runner 20
The one end in area 23 is desorbed, so that hot gas that the heater 80 is burnt can work as to the thermal source for being desorbed area 23 of the zeolite runner 20,
Waste gas in the desorption area 23 of the zeolite runner 20 is set to be desorbed after the hot gas into concentration waste gas, and the zeolite runner 20
The other end for being desorbed area 23 is to be connected to again by the concentration exhaust pipe 60 in incinerator 50, will pass through the zeolite runner
The concentration waste gas being desorbed in 20 desorption area 23 can be delivered in incinerator 50 to carry out via the concentration exhaust pipe 60
Burning cracking is uniform.
And primary structure of the present utility model is on the net gas discharge pipe 30 it is that group is provided with an adsorption desorption structure 100,
And the adsorption desorption structure 100 is provided with an exhaust output tube road 110 and a thermal source pipeline 120, and the exhaust output tube road 110 is
The gas inlet pipeline 10 is connected to, the another thermal source pipeline 120 is to be connected to the incinerator 50 (as shown in Figures 1 and 2), by
This, the adsorption desorption structure that can be passed through again on the net gas discharge pipe 30 with the gas for allowing the net gas discharge pipe 30 to be exported
100 are handled to carry out the adsorption treatment of waste gas and desorption, and can be again by the concentration waste gas passed through handled by the adsorption desorption structure 100
It is transmitted back to by the exhaust output tube road 110 in the gas inlet pipeline 10, clean gas is separately passed through into net gas delivery pipe again
Road 30 is delivered to chimney 70 and discharged so that for waste gas under by dual structure processing, its treatment effeciency can reach 97% even
More than 99%, and the environmental protection efficacy with carbon reduction.
And above-mentioned adsorption desorption structure 100 is provided with a runner 130, the runner 130 is for rotary type tower (not shown), level
Any of which such as formula or tubular, the wherein runner 130 are provided with adsorption zone 1301, cooling zone 1302 and desorption area 1303
(as shown in Figure 2), and the net gas discharge pipe 30 is the adsorption zone 1301 for being connected to the runner 130, the desorption of the another runner 130
The one end of area 1303 is to connect the exhaust output tube road 110, and the other end of desorption area 1303 is to connect the thermal source pipeline 120, is made
The desorption area 1303 of the runner 130 can be desorbed by the heat energy for the incinerator 50 that the thermal source pipeline 120 is connected.Separately should
An auxiliary heater 121 is provided with thermal source pipeline 120, when the hot blast that the incinerator 50 is transmitted is not enough to supply the runner 130
Desorption area 1303 when being desorbed, the hot blast lifted in the thermal source pipeline 120 can be lifted by the auxiliary heater 121,
Enable to reach and the temperature that the desorption area 1303 of the runner 130 is desorbed is provided.Wherein adsorption material is provided with the runner 130
(not shown), and the adsorption material is for activated carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, calcium hydroxide, stone
Any of which such as black alkene or doughnut.
And above-mentioned thermal source pipeline 120 is in addition to for connecting the incinerator 50 and the adsorption desorption structure 100, the heat source tube
Road 120 is provided with a difference pipeline 140, with for being connected at the chimney 70, when the wind for the hot blast that the incinerator 50 is transmitted
When power is too big, the wind model of the hot blast of part can be discharged to the chimney 70 by the difference pipeline 140.
And another embodiment aspect of the present utility model is identical with the main design for implementing system is also provided with a gas inlet
Pipeline 10, a zeolite runner 20, a net gas discharge pipe 30, one cool down gas air inlet pipeline 40, an incinerator 50, one concentration waste gas
The grade key facility of 60 and one chimney of pipeline 70 (the main content for implementing system of ginseng), it is mainly the net gas discharge pipe 30
On be that group is provided with an adsorption desorption structure 200 (as shown in Figure 3), and the adsorption desorption structure 200 is provided with an exhaust output tube road 210
And a thermal source pipeline 220, and the exhaust output tube road 210 is to be connected to the gas inlet pipeline 10, the another thermal source pipeline 220 is
It is connected to the incinerator 50.
And two adsorption material buckets 2000 are provided with adsorption desorption structure 200 set on the net gas discharge pipe 30, and this two
Adsorption material bucket 2000 be respectively as absorption use and desorption with (such as at interval of one hour switch, by the suction of script absorption
Attached material bucket 2000 switches to the adsorption material bucket 2000 of desorption, and the adsorption material bucket 2000 of script desorption then switches to absorption to use
Adsorption material bucket 2000), and the adsorption material bucket 2000 is designed as the hollow long cylinder bodily form, hollow cuboid or hollow sphere
The bodies such as shape, separately when the adsorption material bucket 2000 be set to adsorb the used time be provided with air inlet pipeline 2011, waste gas outlet pipe 2012 and
Clean gas pipeline 2013, and it is set to air inlet pipeline 2021 and desorption gas pipe when the adsorption material bucket 2000 is set to the desorption used time
Road 2022.
Furthermore it is that belly shirt is provided with adsorption material 2100 in the adsorption material bucket 2000 of the adsorption desorption structure 200, and the adsorption material
2100 be for activated carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, calcium hydroxide, graphene or doughnut etc.
Any of which, and discharged the net gas by the set adsorption material bucket 2000 for being used for adsorbing in the adsorption desorption structure 200
The gas that pipeline 30 is exported is adsorbed, then by can be through by being used for gas that the adsorption material bucket 2000 that adsorbs adsorbed
It is delivered in the net gas discharge pipe 30, then is conveyed by clean gas pipeline 2013 of the adsorption material bucket 2000 for the absorption used time
Discharged to the chimney 70, can separately be passed through via for the highly enriched waste gas after the adsorption material bucket 2000 that adsorbs adsorbs
The adsorption material bucket 2000 be adsorb the used time waste gas outlet pipe 2012 come be delivered to the adsorption material bucket 2000 be desorption the used time
Air inlet pipeline 2021, and the adsorption material bucket 2000 is to connect the thermal source pipeline 220 for the air inlet pipeline 2021 of desorption, makes the suction
Attached material bucket 2000 can be desorbed for the desorption used time by the heat energy for the incinerator 50 that the thermal source pipeline 220 is connected.Separately should
An auxiliary heater 221 is provided with thermal source pipeline 220, when the hot blast that the incinerator 50 is transmitted is not enough to supply the adsorption material bucket
2000 be the desorption used time, can lift the hot blast lifted in the thermal source pipeline 220 by the auxiliary heater 221, enabled to reach
Temperature of the adsorption material bucket 2000 to be desorbed needed for the desorption used time is provided.
And above-mentioned thermal source pipeline 220 is in addition to for connecting the incinerator 50 and the adsorption desorption structure 200, the heat source tube
Road 220 is provided with a difference pipeline 230, with for being connected at the chimney 70, when the wind for the hot blast that the incinerator 50 is transmitted
When power is too big, the wind model of the hot blast of part can be discharged to the chimney 70 by the difference pipeline 230.
The waste gas of the another high concentration being desorbed by the adsorption material bucket 2000 of desorption is de- with the adsorption material bucket 2000
The desorption gas pipeline 2022 of attached used time is delivered to the exhaust output tube road 210, and the exhaust output tube road 210 is transmitted back to again
In the gas inlet pipeline 10 so that for waste gas under by dual structure processing, its treatment effeciency can reach 97% or even 99%
More than, and the environmental protection efficacy with carbon reduction.The incinerator 50 of another the present embodiment can be heat accumulating type incinerator (RTO) or
Any of which such as direct-combustion furnace (TO).
And another embodiment aspect of the present utility model is identical with the design of main implementation system is also provided with a gas inlet
Pipeline 10, a zeolite runner 20, a net gas discharge pipe 30, one cool down gas air inlet pipeline 40, an incinerator 50, one concentration waste gas
The grade key facility of 60 and one chimney of pipeline 70 (the main content for implementing system of ginseng), it is mainly the net gas discharge pipe 30
On be that group is provided with an adsorption desorption structure 300 (as shown in Figure 4), and the adsorption desorption structure 300 is provided with an exhaust output tube road 310
And a thermal source pipeline 320, and the exhaust output tube road 310 is to be connected to the gas inlet pipeline 10, the another thermal source pipeline 320 is
It is connected to the incinerator 50.
And multiple adsorption material buckets 3000 are provided with adsorption desorption structure 300 set on the net gas discharge pipe 30, and this is more
Individual adsorption material bucket 3000 be respectively as absorption use, desorption use and cooling with (such as at interval of one hour by 3 kinds effect absorption
Material bucket 3000 is switched over, and the adsorption material bucket 300 of script absorption is switched to the adsorption material bucket 3000 of desorption, and originally
The adsorption material bucket 3000 of desorption then switches to the adsorption material bucket 3000 of absorption, or the adsorption material bucket by wherein absorption
3000 switch to the adsorption material bucket 3000 of cooling), and the adsorption material bucket 3000 is set to the hollow long cylinder bodily form, hollow rectangular
The body such as the bodily form or the hollow ball bodily form, and it is provided with air inlet pipeline 3011, waste gas when the adsorption material bucket 3000 is set to the absorption used time
Outlet pipe 3012 and clean gas pipeline 3013, and it is provided with air inlet pipeline when the adsorption material bucket 3000 is set to the desorption used time
3021 and desorption gas pipeline 3022, separately it is provided with air inlet pipeline 3031 and cooling when the adsorption material bucket 3000 is set to cool down the used time
Gas piping 3032.
Therefore, when the air inlet pipeline 3011 that the adsorption material bucket 3000 is the absorption used time is connected with the net gas discharge pipe 30
Connect, and the adsorption material bucket 3000 be adsorb the used time waste gas outlet pipe 3012 be with the adsorption material bucket 3000 be desorption the used time
Air inlet pipeline 3021 connects, and the another adsorption material bucket 3000 is and the net gas delivery pipe for the clean gas pipeline 3013 of absorption used time
Road 30 is connected, and the adsorption material bucket 3000 is and the exhaust output tube road 310 for the desorption gas pipeline 3022 of desorption used time
It is connected, the another adsorption material bucket 3000 be that to cool down the air inlet pipeline 3031 of used time be for connection outer gas (or gas discharge pipe only
30), the adsorption material bucket 3000 as cooling is cooled down, then by the adsorption material bucket 3000 for cooling the used time it is cold
But gas piping 3032 is connected to the clean gas pipeline 3013.
Furthermore it is that belly shirt is provided with adsorption material 3100 in the adsorption material bucket 3000 of the adsorption desorption structure 300, and the adsorption material
3100 be for activated carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, calcium hydroxide graphene or doughnut etc.
Any of which, and discharged the net gas by the set adsorption material bucket 3000 for being used for adsorbing in the adsorption desorption structure 300
The gas that pipeline 30 is exported is adsorbed, then by can be through by being used for gas that the adsorption material bucket 3000 that adsorbs adsorbed
It is delivered in the net gas discharge pipe 30, then is conveyed by clean gas pipeline 3013 of the adsorption material bucket 3000 for the absorption used time
Discharged to the chimney 70.
Separately can be by the adsorption material bucket via the highly enriched waste gas after being adsorbed for the adsorption material bucket 3000 that adsorbs
3000 be adsorb the used time waste gas outlet pipe 3012 come be delivered to the adsorption material bucket 3000 be desorbed the used time air inlet pipeline
3021, and the adsorption material bucket 3000 is to connect the thermal source pipeline 320 for the air inlet pipeline 3021 of desorption, makes the adsorption material bucket
3000 can be desorbed for the desorption used time by the heat energy for the incinerator 50 that the thermal source pipeline 320 is connected.The another heat source tube
An auxiliary heater 321 is provided with road 320, when the hot blast that the incinerator 50 is transmitted be not enough to be for the adsorption material bucket 3000
The used time is desorbed, can be enabled to reach to provide and be somebody's turn to do by the auxiliary heater 321 to lift the hot blast lifted in the thermal source pipeline 320
Adsorption material bucket 3000 is the temperature being desorbed needed for the desorption used time.
And above-mentioned thermal source pipeline 320 is in addition to for connecting the incinerator 50 and the adsorption desorption structure 300, the heat source tube
Road 320 is provided with a difference pipeline 330, with for being connected at the chimney 70, when the wind for the hot blast that the incinerator 50 is transmitted
When power is too big, the wind model of the hot blast of part can be discharged to the chimney 70 by the difference pipeline 330.
The another adsorption material bucket 3000 is to supply connection outer gas (as shown in Figure 5) for the air inlet pipeline 3031 of cooling used time, or
The clean gas pipeline 3013 (as shown in Figure 4) is connected, the adsorption material bucket 3000 as cooling is cooled down, then leads to
The adsorption material bucket 3000 is crossed to cool down the cooling gas pipeline 3032 of used time to be connected to the clean gas pipeline 3013, should
Adsorption material bucket 3000 is the gas discharge in the cooling gas pipeline 3032 of cooling used time.The separately adsorption material bucket for passing through desorption
Desorption gas pipeline 3022 of the waste gas of 3000 high concentrations being desorbed with the adsorption material bucket 3000 for the desorption used time is delivered to
The exhaust output tube road 310, and the exhaust output tube road 310 is transmitted back in the gas inlet pipeline 10 again so that waste gas is passing through
Cross under dual structure processing, its treatment effeciency can reach 97% or even more than 99%, and the environmental protection efficacy with carbon reduction.Separately
The incinerator of the present embodiment can be any of which such as heat accumulating type incinerator (RTO) or direct-combustion furnace (TO).
By detailed description above, those familiar with this technology can be made to understand that the utility model may achieve object defined above really,
The real regulation for having met Patent Law, therefore propose patent application.
It is only above-described, preferred embodiment only of the present utility model, when the utility model can not be limited with this
The scope of implementation；Therefore all simple equivalence changes made according to present utility model application the scope of the claims and creation description
With modification, all should still belong in the range of the utility model claims cover.
Claims (9)
1. a kind of volatide organic waste gas treating system for having double processing structures, include a gas inlet pipeline, a zeolite turns
Wheel, a net gas discharge pipe, a cooling gas air inlet pipeline, an incinerator, a concentration exhaust pipe and a chimney, the wherein zeolite
Runner is provided with adsorption zone, cooling zone and desorption area, and the gas inlet pipeline is connected to the adsorption zone of the zeolite runner, and this is net
Gas discharge pipe is between the adsorption zone and the chimney of the zeolite runner, and the cooling gas air inlet pipeline connects the zeolite runner
Cooling zone, the another concentration exhaust pipe is between the desorption area of the zeolite runner and the incinerator, it is characterised in that：This is net
Group is provided with an adsorption desorption structure on gas discharge pipe, and the adsorption desorption structure is provided with an exhaust output tube road and a thermal source pipeline,
And the exhaust output tube road is connected to the gas inlet pipeline, the another thermal source pipeline is connected to the incinerator.
2. the volatide organic waste gas treating system of the double processing structures of tool as claimed in claim 1, it is characterised in that wherein should
Incinerator is further any of which of heat accumulating type incinerator or direct-combustion furnace, and it is auxiliary that one is further provided with the thermal source pipeline
Help heater.
3. the volatide organic waste gas treating system of the double processing structures of tool as claimed in claim 1, it is characterised in that wherein should
A runner is further provided with adsorption desorption structure, the runner is any of which of rotary type tower, horizontal or tubular, and this turn
Wheel is provided with adsorption zone, cooling zone and desorption area, and the net gas discharge pipe is connected to the adsorption zone of the runner, the another desorption area one
End connects the exhaust output tube road, and the desorption area other end connects the thermal source pipeline.
4. the volatide organic waste gas treating system of the double processing structures of tool as claimed in claim 3, it is characterised in that wherein should
Be further provided with adsorption material in runner, and the adsorption material is further activated carbon, zeolite, silica gel, activated alumina, molecular sieve,
Manganese oxide, calcium hydroxide, any of which of graphene or doughnut.
5. the volatide organic waste gas treating system of the double processing structures of tool as claimed in claim 1, it is characterised in that wherein should
It is further provided with two adsorption material buckets in adsorption desorption structure, and the two adsorption materials bucket is used respectively as absorption and desorption is used, and when should
Adsorption material bucket be set to adsorb the used time be provided with air inlet pipeline, waste gas outlet pipe and clean gas pipeline, separately when the adsorption material bucket is set
Air inlet pipeline and desorption gas pipeline are provided with for the desorption used time.
6. the volatide organic waste gas treating system of the double processing structures of tool as claimed in claim 5, it is characterised in that wherein should
Adsorption material is further provided with the adsorption material bucket of adsorption desorption structure, and the adsorption material is further activated carbon, zeolite, silica gel, work
Property aluminum oxide, molecular sieve, manganese oxide, calcium hydroxide, any of which of graphene or doughnut.
7. the volatide organic waste gas treating system of the double processing structures of tool as claimed in claim 1, it is characterised in that wherein should
Multiple adsorption material buckets are further provided with adsorption desorption structure, and the plurality of adsorption material bucket is used respectively as absorption, desorption is used and cold
But use, be provided with air inlet pipeline, waste gas outlet pipe and clean gas pipeline when the adsorption material bucket is set to the absorption used time, and work as the suction
Attached material bucket be set to be desorbed the used time be provided with air inlet pipeline and desorption gas pipeline, separately when the adsorption material bucket be set to cooling the used time be provided with into
Air pipe and cooling gas pipeline.
8. the volatide organic waste gas treating system of the double processing structures of tool as claimed in claim 7, it is characterised in that wherein should
Further be respectively provided with adsorption material in the adsorption material bucket of adsorption desorption structure, and the adsorption material is further activated carbon, zeolite, silica gel,
Activated alumina, molecular sieve, calcium hydroxide, any of which of graphene or doughnut.
9. the volatide organic waste gas treating system of the double processing structures of tool as described in claim 5 or 7, it is characterised in that its
In the adsorption material bucket be further set to the hollow long cylinder bodily form, hollow cuboid or the hollow ball bodily form.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW106206741 | 2017-05-12 | ||
| TW106206741U TWM549655U (en) | 2017-05-12 | 2017-05-12 | Volatile organic exhaust gas treatment system with dual treatment structures |
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| Publication Number | Publication Date |
|---|---|
| CN207056259U true CN207056259U (en) | 2018-03-02 |
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ID=61012737
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720795165.1U Active CN207056259U (en) | 2017-05-12 | 2017-07-03 | Volatile organic waste gas treatment system with double treatment structures |
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| CN (1) | CN207056259U (en) |
| TW (1) | TWM549655U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111520731A (en) * | 2019-02-01 | 2020-08-11 | 华懋科技股份有限公司 | Direct-combustion backflow heat recovery high-efficiency organic waste gas treatment system and method |
| CN111804122A (en) * | 2019-04-12 | 2020-10-23 | 华懋科技股份有限公司 | High-efficiency organic waste gas treatment system and method for reflux heat recovery |
| TWI722522B (en) * | 2019-08-07 | 2021-03-21 | 華懋科技股份有限公司 | Heat storage reflux high-efficiency organic waste gas treatment system and method |
| TWI740186B (en) * | 2019-08-07 | 2021-09-21 | 華懋科技股份有限公司 | Organic waste gas concentrated heat storage combustion reflux cooling system and method |
| TWI741341B (en) * | 2019-08-07 | 2021-10-01 | 華懋科技股份有限公司 | Organic waste gas concentrated heat storage combustion backflow system and method |
-
2017
- 2017-05-12 TW TW106206741U patent/TWM549655U/en unknown
- 2017-07-03 CN CN201720795165.1U patent/CN207056259U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111520731A (en) * | 2019-02-01 | 2020-08-11 | 华懋科技股份有限公司 | Direct-combustion backflow heat recovery high-efficiency organic waste gas treatment system and method |
| CN111520731B (en) * | 2019-02-01 | 2023-03-03 | 华懋科技股份有限公司 | Direct-combustion backflow heat recovery organic waste gas treatment system and method |
| CN111804122A (en) * | 2019-04-12 | 2020-10-23 | 华懋科技股份有限公司 | High-efficiency organic waste gas treatment system and method for reflux heat recovery |
| TWI722522B (en) * | 2019-08-07 | 2021-03-21 | 華懋科技股份有限公司 | Heat storage reflux high-efficiency organic waste gas treatment system and method |
| TWI740186B (en) * | 2019-08-07 | 2021-09-21 | 華懋科技股份有限公司 | Organic waste gas concentrated heat storage combustion reflux cooling system and method |
| TWI741341B (en) * | 2019-08-07 | 2021-10-01 | 華懋科技股份有限公司 | Organic waste gas concentrated heat storage combustion backflow system and method |
Also Published As
| Publication number | Publication date |
|---|---|
| TWM549655U (en) | 2017-10-01 |
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