CN207056267U - Volatile organic waste gas treatment system with bypass treatment structure - Google Patents
Volatile organic waste gas treatment system with bypass treatment structure Download PDFInfo
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- CN207056267U CN207056267U CN201720790421.8U CN201720790421U CN207056267U CN 207056267 U CN207056267 U CN 207056267U CN 201720790421 U CN201720790421 U CN 201720790421U CN 207056267 U CN207056267 U CN 207056267U
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- 239000007789 gas Substances 0.000 title claims abstract description 205
- 239000010815 organic waste Substances 0.000 title claims abstract description 22
- 238000003795 desorption Methods 0.000 claims abstract description 92
- 239000002912 waste gas Substances 0.000 claims abstract description 73
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 50
- 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 50
- 239000010457 zeolite Substances 0.000 claims abstract description 50
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 34
- 238000001179 sorption measurement Methods 0.000 claims description 186
- 239000000463 material Substances 0.000 claims description 170
- 238000002336 sorption--desorption measurement Methods 0.000 claims description 61
- 238000010521 absorption reaction Methods 0.000 claims description 39
- 238000001816 cooling Methods 0.000 claims description 33
- 239000000112 cooling gas Substances 0.000 claims description 18
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 claims description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 9
- 235000012489 doughnuts Nutrition 0.000 claims description 9
- 229910002027 silica gel Inorganic materials 0.000 claims description 9
- 239000000741 silica gel Substances 0.000 claims description 9
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 8
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 8
- 239000000920 calcium hydroxide Substances 0.000 claims description 8
- 229910021389 graphene Inorganic materials 0.000 claims description 8
- 239000002808 molecular sieve Substances 0.000 claims description 8
- 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 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 6
- 238000009835 boiling Methods 0.000 claims 1
- 235000019504 cigarettes Nutrition 0.000 claims 1
- 239000004575 stone Substances 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 9
- 230000007613 environmental effect Effects 0.000 abstract description 9
- 239000012141 concentrate Substances 0.000 description 4
- 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
- 238000005336 cracking Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 235000008434 ginseng Nutrition 0.000 description 2
- 230000005693 optoelectronics Effects 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Treating Waste Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The utility model relates to a volatile organic waste gas treatment system with bypass treatment structure, which mainly comprises a suction and desorption structure arranged on the clean gas discharge pipeline, a waste gas output pipeline and a heat source pipeline arranged on the suction and desorption structure of the clean gas discharge pipeline, the waste gas output pipeline is connected to the waste gas inlet pipeline, and the heat source pipeline is connected to the incinerator, therefore, the waste gas of the waste gas inlet pipeline can be treated by concentrated waste gas through the zeolite runner, the concentrated waste gas can also be treated by the suction and desorption structure of the bypass pipeline, the gas output by the clean gas discharge pipeline can be treated by concentrated waste gas through the suction and desorption structure of the clean gas discharge pipeline, and the concentrated waste gas treated by the suction and desorption structure of the clean gas discharge pipeline is conveyed back to the waste gas inlet pipeline through the waste gas output pipeline, the treatment efficiency of the waste gas can reach 97 percent or even more than 99 percent under the treatment of multiple structures, thereby having 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 bypass processing structure, espespecially a kind of
Waste gas concentrate outside the processing of waste gas via the adsorption desorption structure of the zeolite runner and the bypass line, can also be via this
The adsorption desorption structure of net gas discharge pipe concentrate the processing of waste gas, and is applied to semiconductor industry, opto-electronics or change
The exhaust-gas treatment of the factory building of work 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, in view of disadvantages mentioned above, the phase can propose by a kind of tool of the environmental protection efficacy with carbon reduction this creator
The volatide organic waste gas treating system of logical processing structure, make user can easy operation assembling, be to grind think of, design group system with great concentration,
To provide user's convenience, 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 bypass processing structure
System, it is to include a gas inlet pipeline, a zeolite runner, a net gas discharge pipe, bypass conduit, a cooling gas air inlet pipe
Road, an incinerator, one concentration exhaust pipe and a chimney Combination Design, it is that group is set that it, which is essentially consisted on the net gas discharge pipe,
There is an adsorption desorption structure, and the adsorption desorption structure of the net gas discharge pipe 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, thus, allows this
The waste gas of gas inlet pipeline, can also be via the bypass pipe in addition to concentrate the processing of waste gas via the zeolite runner
The adsorption desorption structure on road concentrate the processing of waste gas, and the gas exported by the net gas discharge pipe can pass through to this is net
The adsorption desorption structure of gas discharge pipe, and again will be by the suction of the net gas discharge pipe once to be concentrated the processing of waste gas again
Concentration waste gas handled by desorption structure is transmitted back in the gas inlet pipeline by the exhaust output tube road again so that waste gas
Under by multiplet processing, its treatment effeciency can reach 97% or even more than 99%, be imitated with the environmental protection with carbon reduction
Can, 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 bypass processing structure
System, and a runner is provided with the adsorption desorption structure by the net gas discharge pipe, the runner is for rotary type tower, horizontal or cylinder
Any of which such as shape formula, and the runner is provided with adsorption zone, cooling zone and desorption area, and the net gas discharge pipe is to be connected to
The adsorption zone of the runner, the another desorption area one end is to connect the exhaust output tube road, and the desorption area other end is to connect the heat
Source capsule road, the desorption area is set to be desorbed by the heat energy of the incinerator, and in being that to set up one auxiliary on the thermal source pipeline
Heater is helped to have the efficiency for lifting the hot blast in the thermal source pipeline, treatment effeciency can be improved, and then increases overall make
The property used.
For the above-mentioned purpose, the utility model has the volatide organic waste gas treating system for bypassing processing structure to be a kind of,
Be include a gas inlet pipeline, a zeolite runner, a net gas discharge pipe, bypass conduit, a cooling gas air inlet pipeline,
One incinerator, a concentration exhaust pipe and a chimney, wherein the zeolite runner are provided with adsorption zone, cooling zone and desorption area, and
The gas inlet pipeline is the adsorption zone for being connected to the zeolite runner, and the net gas discharge pipe is provided at the suction of the zeolite runner
Between attached area and the chimney, and the cooling gas air inlet pipeline is the cooling zone for connecting the zeolite runner, the another concentration exhaust pipe
It is provided between the desorption area of the zeolite runner and the incinerator, and the bypass line one end is to connect the gas inlet pipeline,
And the other end of the bypass line is to connect the net gas discharge pipe, and in being provided with an adsorption desorption structure on the bypass line,
The adsorption desorption structure of the another bypass line is provided with a concentrated gas pipeline, and the concentrated gas pipeline is to be connected to the thickened waste
Air pipe, it is characterised in that：Also group is provided with an adsorption desorption structure on the net gas discharge pipe, and the suction of the net gas discharge pipe takes off
Attached 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 exhaust inlet pipe
Road, 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 of the net gas discharge pipe, the runner is rotary type tower, level
Any of which of formula or tubular, and the runner is provided with adsorption zone, cooling zone and desorption area, and the net gas discharge pipe connection
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.
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.
Two adsorption material buckets are wherein further provided with the adsorption desorption structure of the net gas discharge pipe, and the two adsorption materials bucket divides
It Zuo Wei not adsorb to use and be desorbed and use, and when the adsorption material bucket is set to adsorb the used time provided with air inlet pipeline, waste gas outlet pipe and does
Net gas piping, separately it is provided with air inlet pipeline and desorption gas pipeline when the adsorption material bucket is set to the desorption used time.
Two adsorption material buckets are wherein further provided with the adsorption desorption structure of the bypass line, and the two adsorption materials bucket is made respectively
Used for absorption and desorption is used, and air inlet pipeline, waste gas outlet pipe and clean gas are provided with when the adsorption material bucket is set to the absorption used time
Body pipeline, separately it is provided with air inlet pipeline and desorption gas pipeline when the adsorption material bucket is set to the desorption used time.
Wherein it is further provided with multiple adsorption material buckets in the adsorption desorption structure of the net gas discharge pipe, and the plurality of adsorption material
Bucket is used respectively as absorption use, desorption and cooling is used, and air inlet pipeline, waste gas outlet are provided with when the adsorption material bucket is set to the absorption used time
Pipeline 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 work as
The adsorption material bucket be set to cool down the used time be provided with air inlet pipeline and cooling gas pipeline.
Multiple adsorption material buckets are wherein further provided with the adsorption desorption structure of the bypass line, and the plurality of adsorption material bucket divides
Use Zuo Wei not be adsorbed, desorption is used and cools down use, air inlet pipeline, waste gas outlet pipe are provided with when the adsorption material bucket is set to the absorption used time
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 suction
Attached material bucket be set to cool down the used time be 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 its treatment effeciency can reach 97% or even more than 99%, to subtract with energy-conservation
The environmental protection efficacy of carbon.
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 that the multiplet of the utility model Major Systems handles schematic diagram.
Fig. 2 is that the adsorption desorption structure of the bypass line of the utility model Major Systems is with two adsorption material buckets and net gas
The adsorption desorption structure of discharge pipe is the structural representation of runner.
Fig. 3 is that the adsorption desorption structure of the bypass line of the utility model Major Systems is with multiple adsorption material buckets and net gas
The adsorption desorption structure of discharge pipe has the structural representation of two adsorption material buckets.
Fig. 4 is that the adsorption desorption structure of the bypass line of the utility model Major Systems is with multiple adsorption material buckets and net gas
The adsorption desorption structure of discharge pipe has the structural representation of multiple adsorption material buckets.
Fig. 5 is that the adsorption desorption structure of the bypass line of the utility model Major Systems is with multiple adsorption material buckets and net gas
The adsorption desorption structure of discharge pipe 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 tool bypass processing 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 phase
The exhaust-gas treatment of the factory building of pass industry so that for waste gas under by multiplet processing, its treatment effeciency can reach 97% even
More than 99%, with 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 tool bypass processing structure of the present utility model are to include
There are a gas inlet pipeline 10, a zeolite runner 20, a net gas discharge pipe 30, bypass conduit 40, one to cool down gas air inlet pipe
Road 50, wherein an incinerator 60, the one concentration chimney 80 (as shown in Figures 1 to 5) of exhaust pipe 70 and one, the zeolite runner 20 are also
Can be the concentration runner that materials are adsorbed using other, and the zeolite runner 20 is provided with adsorption zone 21, cooling zone 22 and desorption area
23, can carry out the absorption of waste gas and by waste gas desorption into concentration waste gas, the another incinerator 60 can be heat accumulating type incinerator
Or any of which such as direct-combustion furnace (TO) (RTO).
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 80, 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 80, 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 80 can also be provided with
One blower fan (not shown), arranged being pumped the gas in the net gas discharge pipe 30 to chimney 80 by the air exhauster
Put.
The another cooling gas air inlet pipeline 50 is the cooling zone 22 for connecting the zeolite runner 20, and the cooling gas air inlet pipeline 50
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 50 is to be then connected to a heater 90, the fresh air in the cooling gas air inlet pipeline 50 is turned by the zeolite
It can be delivered in heater 90 and be heated behind the cooling zone 22 of wheel 20, and the heater 90 is then connected to the zeolite runner 20
The one end in area 23 is desorbed, so that hot gas that the heater 90 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 22 is to be connected to again by the concentration exhaust pipe 70 in incinerator 60, will pass through the zeolite runner
The concentration waste gas being desorbed in 20 desorption area 23 can be delivered in incinerator 60 to carry out via the concentration exhaust pipe 70
Burning cracking is uniform.
Furthermore the one end of bypass line 40 is to connect the gas inlet pipeline 10, and the other end of the bypass line 40 is
The net gas discharge pipe 30 is connected, by the bypass line 40 waste gas in the gas inlet pipeline 10 can be enable to be divided into two,
And the exhaust gas flow of the adsorption zone 21 for the zeolite runner 20 that the gas inlet pipeline 10 connected is diminished, to improve the zeolite
The adsorption effect of the adsorption zone 21 of runner 20 can reach more than 95% efficiency (assuming that the zeolite runner 20 is in the situation not shunted
Under can be to 95% efficiency).
The adsorption desorption knot of at least an adsorption desorption structure 100, the wherein bypass line 40 is provided with the another bypass line 40
Adsorption material 110 (as shown in Figure 1) is provided with structure 100, and the adsorption material 110 is for activated carbon, zeolite, silica gel, active oxidation
Any of which such as aluminium, molecular sieve, manganese oxide, calcium hydroxide, graphene or doughnut, taken off by the suction of the bypass line 40
Attached structure 100 is adsorbed the waste gas entered in bypass line 40, then by by the adsorption desorption knot of the bypass line 40
(gas reaches more than 99% efficiency to the gas that structure 100 adsorbed because concentration reduces, in this way, passing through a certain proportion of side
Reduction of fractions to a common denominator stream, total treatment effeciency is set to be lifted to more than more than 96%, or even 97%) can be defeated via the net gas discharge pipe 30
The chimney 80 is delivered to be discharged.
Furthermore the adsorption desorption structure 100 of the bypass line 40 is provided with a concentrated gas pipeline 120, and the concentrated gas
Pipeline 120 is to be connected to the concentration exhaust pipe 70, quilt after the adsorption desorption structure 100 via the bypass line 40 is adsorbed
The highly enriched waste gas of desorption can be delivered in the concentration exhaust pipe 70 before the incinerator 60, then passes through the concentration exhaust pipe
70 convey into the incinerator 60, allow the incinerator 60 to carry out the burning operation of highly enriched waste gas, enable treatment effeciency
Improve, the another incinerator 60 can be any of which such as heat accumulating type incinerator (RTO) or direct-combustion furnace (TO).
It is that can be provided with two adsorption material buckets 130 in the adsorption desorption structure 100 of the another above-mentioned bypass line 40, and two adsorption material
Bucket 130 be respectively as absorption use and desorption with (such as at interval of one hour switch, by the adsorption material bucket of script absorption
130 switch to the adsorption material bucket 130 of desorption, and the adsorption material bucket 130 of script desorption then switches to the adsorption material of absorption
130) (as shown in Figure 2), and the adsorption material bucket 130 is designed as the hollow long cylinder bodily form, hollow cuboid or hollow ball to bucket
The bodies such as the bodily form, separately when the adsorption material bucket 130 be set to adsorb the used time be provided with air inlet pipeline 1311, waste gas outlet pipe 1312 and
Clean gas pipeline 1313, and it is set to air inlet pipeline 1321 and desorption gas pipe when the adsorption material bucket 130 is set to the desorption used time
Road 1322.
Separately can be by the adsorption material bucket via the highly enriched waste gas after being adsorbed for the adsorption material bucket 130 that adsorbs
130 be adsorb the used time waste gas outlet pipe 1312 come be delivered to the adsorption material bucket 130 be desorbed the used time air inlet pipeline 1321,
And the adsorption material bucket 130 is the waste gas outlet pipe 1312 for adsorbing the used time and the air inlet pipeline that the adsorption material bucket 130 is desorption
A heater 150 is provided between 1321, and the highly enriched waste gas enters waste gas after the heater 150 heating
For being desorbed in the adsorption material bucket 130 that is desorbed, then the high concentration that the adsorption material bucket 130 by desorption is desorbed
Desorption gas pipeline 1322 of the waste gas with the adsorption material bucket 130 for the desorption used time is delivered to the concentrated gas pipeline 120, and is somebody's turn to do
Concentrated gas pipeline 120 is delivered in the concentration exhaust pipe 70 before the incinerator 60 again, then passes through the concentration exhaust pipe 70
To convey into the incinerator 60, the incinerator 60 is allowed to carry out the burning operation of highly enriched waste gas with by highly enriched waste gas
The cracking that can burn is uniform.
It is that can be provided with multiple adsorption material buckets 140 in the adsorption desorption structure 100 of the another above-mentioned bypass line 40, and the plurality of suction
Attached material bucket 140 be respectively as absorption use, desorption use and cooling with (such as at interval of one hour by 3 kinds effect adsorption material bucket
140 are switched over, and the adsorption material bucket 140 of script absorption is switched to the adsorption material bucket 140 of desorption, and are desorbed use originally
Adsorption material bucket 140 then switch to the adsorption material bucket 140 of absorption, or the adsorption material bucket 140 of wherein absorption is switched to
The adsorption material bucket 140 of cooling) (as shown in Figure 3 to Figure 4), and the adsorption material bucket 140 is set to the hollow long cylinder bodily form, hollow
The body such as cuboid or the hollow ball bodily form, and be provided with air inlet pipeline 1411 when the adsorption material bucket 140 is set to the absorption used time, give up
Gas outlet pipe 1412 and clean gas pipeline 1413, and it is provided with air inlet pipeline when the adsorption material bucket 140 is set to the desorption used time
1421 and desorption gas pipeline 1422, separately it is provided with air inlet pipeline 1431 and cooling when the adsorption material bucket 140 is set to cool down the used time
Gas piping 1432.
Therefore, when the air inlet pipeline 1411 that the adsorption material bucket 140 is the absorption used time is connected with the gas inlet pipeline 10
Connect, and the adsorption material bucket 140 be adsorb the used time waste gas outlet pipe 1412 be with the adsorption material bucket 140 be to be desorbed the used time to enter
Air pipe 1421 connects, and the adsorption material bucket 140 is the waste gas outlet pipe 1412 of absorption used time and the adsorption material bucket 140 is de-
A heater 150 is provided between attached air inlet pipeline 1421, the another adsorption material bucket 140 is the clean gas pipe of absorption used time
Road 1413 is connected with the net gas discharge pipe 30, and the adsorption material bucket 140 is the desorption gas pipeline 1422 of desorption used time
It is to be connected with the concentrated gas pipeline 120, the another adsorption material bucket 140 is outer for connection for the air inlet pipeline 1431 of cooling used time
Gas (or gas inlet pipeline 10), the adsorption material bucket 140 as cooling is cooled down, then passes through the adsorption material bucket
140 are connected to the waste gas outlet pipe 1412 for the cooling gas pipeline 1432 of cooling used time.
And adsorption material bucket 130,140 set in the adsorption desorption structure 100 of the above-mentioned bypass line 40 is hollow installing
There is adsorption material 110, and the adsorption material 110 is for activated carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, hydroxide
Any of which such as calcium, graphene or doughnut, and be used for inhaling set by the adsorption desorption structure 100 for passing through the bypass line 40
Attached adsorption material bucket 130,140 is adsorbed the waste gas entered in bypass line 40, then will be passed through and be used for adsorbing use
Adsorption material bucket 130,140 adsorbed gas (gas because concentration reduces reach more than 99% efficiency, in this way, logical
A certain proportion of bypass shunt is crossed, total treatment effeciency is lifted to more than more than 96%, or even 97%) can be via the absorption
Material bucket 130,140 is delivered in the net gas discharge pipe 30 for the clean gas pipeline 1313,1413 of absorption used time, then is conveyed
Discharged to the chimney 80.
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 200,
And the adsorption desorption structure 200 of the net gas discharge pipe 30 is provided with an exhaust output tube road 210 and a thermal source pipeline 220, and should
Exhaust output tube road 210 is to be connected to the gas inlet pipeline 10 (as shown in Figure 1), and the another thermal source pipeline 220 is to be connected to this
Incinerator 60, thus, it 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
Adsorption desorption structure 200 carry out the adsorption treatment of waste gas and desorption processing, and will be taken off by the suction of the net gas discharge pipe 30
Concentration waste gas handled by attached structure 200 can be transmitted back in the gas inlet pipeline 10 by the exhaust output tube road 210 again,
Clean gas separately is delivered into chimney 80 by net gas discharge pipe 30 again to discharge so that waste gas is handled by multiplet
Under, its treatment effeciency can reach 97% or even more than 99%, and the environmental protection efficacy with carbon reduction.
And the adsorption desorption structure 200 of the above-mentioned net gas discharge pipe 30 is provided with a runner 230 (as shown in Figure 2), this turn
Wheel 230 is to be provided with adsorption zone for any of which such as rotary type tower (not shown), horizontal or tubular, the wherein runner 230
2301st, cooling zone 2302 and desorption area 2303, and the net gas discharge pipe 30 is the adsorption zone 2301 for being connected to the runner 230,
One end of desorption area 2303 of the another runner 230 is to connect the exhaust output tube road 210, and the other end of desorption area 2303 is connection
The thermal source pipeline 220, enable the heat for the incinerator 60 that the desorption area 2303 of the runner 230 connected by the thermal source pipeline 220
It can be desorbed.An auxiliary heater 221 is provided with the another thermal source pipeline 220, when the hot blast that the incinerator 60 is transmitted
When being not enough to be desorbed for the desorption area 2303 of the runner 230, the thermal source can be lifted to be lifted by the auxiliary heater 221
Hot blast in pipeline 220, it is enabled reach the temperature that the desorption area 2303 of the runner 230 is desorbed is provided.The wherein runner 230
Adsorption material (not shown) is inside provided with, and the adsorption material is for activated carbon, zeolite, silica gel, activated alumina, molecular sieve, oxidation
Any of which such as manganese, calcium hydroxide, graphene or doughnut.
And above-mentioned thermal source pipeline 220 is except for connecting the adsorption desorption knot of the incinerator 60 and the net gas discharge pipe 30
Outside structure 200, the thermal source pipeline 220 is provided with a difference pipeline 222, with for being connected at the chimney 80, when the incinerator 60
, can be by the difference pipeline 222 by the wind model of the hot blast of part to the chimney when wind-force of the hot blast transmitted is too big
80 are discharged.
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, bypass conduit 40, one cool down gas air inlet pipeline 50, an incinerator
60th, the key facility such as concentration chimney 80 of exhaust pipe 70 and one (the main content for implementing system of ginseng), it is mainly this
It is that group is provided with an adsorption desorption structure 200 on net gas discharge pipe 30, and the adsorption desorption structure 200 of the net gas discharge pipe 30 is to set
There are 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 to be connected to the incinerator 60.
And two adsorption material buckets 240 are provided with adsorption desorption structure 200 set on the net gas discharge pipe 30, and two suction
Attached material bucket 240 be respectively as absorption use and desorption with (such as at interval of one hour switch, by the adsorption material of script absorption
Bucket 240 switches to the adsorption material bucket 240 of desorption, and the adsorption material bucket 240 of script desorption then switches to the absorption of absorption
Material bucket 240) (as shown in Figure 3), and the adsorption material bucket 240 is designed as the hollow long cylinder bodily form, hollow cuboid or hollow
The bodies such as spherical, separately it is provided with air inlet pipeline 2411, waste gas outlet pipe 2412 when the adsorption material bucket 240 is set to the absorption used time
And clean gas pipeline 2413, and it is set to air inlet pipeline 2421 and desorption gas when the adsorption material bucket 240 is set to the desorption used time
Pipeline 2422.
Furthermore it is that belly shirt is provided with adsorption material in the adsorption material bucket 240 of the adsorption desorption structure 200 of the net gas discharge pipe 30
241, and the adsorption material 241 is for activated carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, calcium hydroxide, graphite
Any of which such as alkene or doughnut, and be used for adsorbing set by the adsorption desorption structure 200 for passing through the net gas discharge pipe 30
Adsorption material bucket 240 is adsorbed the gas that the net gas discharge pipe 30 is exported, then by by being used for what is adsorbed
The gas that adsorption material bucket 240 adsorbed can be defeated for the clean gas pipeline 2413 of absorption used time via the adsorption material bucket 240
Deliver in the net gas discharge pipe 30, then be delivered to the chimney 80 and discharged, separately via the adsorption material bucket 240 for adsorbing
Highly enriched waste gas after adsorbing can adsorb the waste gas outlet pipe 2412 of used time to be delivered to by the adsorption material bucket 240
The adsorption material bucket 240 is is desorbed the air inlet pipeline 2421 of used time, and the adsorption material bucket 240 is for the air inlet pipeline 2421 of desorption
The thermal source pipeline 220 is connected, the incinerator for enabling the adsorption material bucket 240 to be connected for the desorption used time by the thermal source pipeline 220
60 heat energy is desorbed.An auxiliary heater 221 is provided with the another thermal source pipeline 220, when the incinerator 60 is transmitted
Hot blast be not enough to for the adsorption material bucket 240 for desorption the used time, can by the auxiliary heater 221 come lifted lifted the heat source tube
Hot blast in road 220, it is enabled to reach the temperature for providing the adsorption material bucket 240 to be desorbed needed for the desorption used time.
And above-mentioned thermal source pipeline 220 is except for connecting the adsorption desorption knot of the incinerator 60 and the net gas discharge pipe 30
Outside structure 200, the thermal source pipeline 220 is provided with a difference pipeline 222, with for being connected at the chimney 80, when the incinerator 60
, can be by the difference pipeline 222 by the wind model of the hot blast of part to the chimney when wind-force of the hot blast transmitted is too big
80 are discharged.
The waste gas of the another high concentration being desorbed by the adsorption material bucket 240 of desorption is desorption with the adsorption material bucket 240
The desorption gas pipeline 2422 of used time is delivered to the exhaust output tube road 210, and the exhaust output tube road 210 is transmitted back to this again
In gas inlet pipeline 10 (as shown in Figure 3) so that for waste gas under by multiplet processing, its treatment effeciency can reach 97%
Even more than 99%, and the environmental protection efficacy with carbon reduction.The incinerator 60 of another the present embodiment can be heat accumulating type incinerator
Or any of which such as direct-combustion furnace (TO) (RT0).
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, bypass conduit 40, one cool down gas air inlet pipeline 50, an incinerator
60th, the key facility such as concentration chimney 80 of exhaust pipe 70 and one (the main content for implementing system of ginseng), it is mainly this
It is that group is provided with an adsorption desorption structure 200 on net gas discharge pipe 30, and the adsorption desorption structure 200 of the net gas discharge pipe 30 is to set
There are 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 to be connected to the incinerator 60.
And multiple adsorption material buckets 250 are provided with adsorption desorption structure 200 set on the net gas discharge pipe 30, and it is the plurality of
Adsorption material bucket 250 be respectively as absorption use, desorption use and cooling with (such as at interval of one hour by 3 kinds effect adsorption material
Bucket 250 is switched over, and the adsorption material bucket 250 of script absorption is switched to the adsorption material bucket 250 of desorption, and is desorbed originally
Adsorption material bucket 250 then switches to the adsorption material bucket 250 of absorption, or the adsorption material bucket 250 of wherein absorption is switched
Into the adsorption material bucket 250 of cooling), and the adsorption material bucket 250 is set to the hollow long cylinder bodily form, hollow cuboid or hollow
The bodies such as spherical, and it is provided with air inlet pipeline 2511, waste gas outlet pipe 2512 when the adsorption material bucket 250 is set to the absorption used time
And clean gas pipeline 2513, and it is provided with air inlet pipeline 2521 and desorption gas when the adsorption material bucket 250 is set to the desorption used time
Pipeline 2522, separately it is provided with air inlet pipeline 2531 and cooling gas pipeline 2532 when the adsorption material bucket 250 is set to the cooling used time.
Therefore, when the air inlet pipeline 2511 that the adsorption material bucket 250 is the absorption used time is connected with the net gas discharge pipe 30
Connect, and the adsorption material bucket 250 be adsorb the used time waste gas outlet pipe 2512 be with the adsorption material bucket 250 be to be desorbed the used time to enter
Air pipe 2521 connects, and the another adsorption material bucket 250 is and the net gas discharge pipe for the clean gas pipeline 2513 of absorption used time
30 are connected, and the adsorption material bucket 250 for the desorption gas pipeline 2522 of desorption used time is connected with the exhaust output tube road 210
Connecing, the another adsorption material bucket 250 is that the air inlet pipeline 2531 of cooling used time is to supply connection outer gas (or clean gas pipeline 2513),
So that the adsorption material bucket 250 as cooling to be cooled down, then the cooling gas by the adsorption material bucket 250 for the cooling used time
Pipeline 2532 is connected to the clean gas pipeline 2513.
Furthermore it is that belly shirt is provided with adsorption material in the adsorption material bucket 250 of the adsorption desorption structure 200 of the net gas discharge pipe 30
251, and the adsorption material 251 is for activated carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, calcium hydroxide graphene
Or any of which such as doughnut, and be used for adsorbing use set by the adsorption desorption structure 200 for passing through the net gas discharge pipe 30
Adsorption material bucket 250 gas that the net gas discharge pipe 30 is exported is adsorbed, then by by being used for the suction adsorbed
The gas that attached material bucket 250 adsorbed can adsorb the clean gas pipeline 2513 of used time to convey via the adsorption material bucket 250
To the net gas discharge pipe 30, then it is delivered to the chimney 80 and is discharged.
Separately can be by the adsorption material bucket via the highly enriched waste gas after being adsorbed for the adsorption material bucket 250 that adsorbs
250 be adsorb the used time waste gas outlet pipe 2512 come be delivered to the adsorption material bucket 250 be desorbed the used time air inlet pipeline 2521,
And the adsorption material bucket 250 is to connect the thermal source pipeline 220 for the air inlet pipeline 2521 of desorption, it is de- to make the adsorption material bucket 250
The attached used time can be desorbed by the heat energy for the incinerator 60 that the thermal source pipeline 220 is connected.It is on the another thermal source pipeline 220
Provided with an auxiliary heater 221, it is the desorption used time to be not enough to when the hot blast that the incinerator 60 is transmitted for the adsorption material bucket 250,
The hot blast lifted in the thermal source pipeline 220 can be lifted by the auxiliary heater 221, it is enabled reach the adsorption material bucket is provided
250 temperature to be desorbed needed for the desorption used time.
And above-mentioned thermal source pipeline 220 is except for connecting the adsorption desorption knot of the incinerator 60 and the net gas discharge pipe 30
Outside structure 200, the thermal source pipeline 220 is provided with a difference pipeline 222, with for being connected at the chimney 80, when the incinerator 60
, can be by the difference pipeline 222 by the wind model of the hot blast of part to the chimney when wind-force of the hot blast transmitted is too big
80 are discharged.
The another adsorption material bucket 250 is to supply connection outer gas (as shown in Figure 5) for the air inlet pipeline 2531 of cooling used time, or even
The clean gas pipeline 2513 (as shown in Figure 4) is connect, the adsorption material bucket 250 as cooling is cooled down, then passes through
The adsorption material bucket 250 inhales this to cool down the cooling gas pipeline 2532 of used time to be connected to the clean gas pipeline 2513
Attached material bucket 250 is the gas discharge in the cooling gas pipeline 2532 of cooling used time.The separately adsorption material bucket 250 for passing through desorption
Desorption gas pipeline 2522 of the waste gas for the high concentration being desorbed with the adsorption material bucket 250 for the desorption used time is delivered to the waste gas
Output pipe 210, and the exhaust output tube road 210 is transmitted back in the gas inlet pipeline 10 (as shown in Figure 4) again so that waste gas
Under by multiplet processing, its treatment effeciency can reach 97% or even more than 99%, and the environmental protection effect with carbon reduction
Energy.The incinerator 60 of another the present embodiment can be any of which such as heat accumulating type incinerator (RTO) or direct-combustion furnace (TO).
By detailed description above, known art person 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 (10)
1. a kind of volatide organic waste gas treating system for having bypass processing structure, includes a gas inlet pipeline, a zeolite
Runner, a net gas discharge pipe, bypass conduit, a cooling gas air inlet pipeline, an incinerator, a concentration exhaust pipe and a cigarette
Chimney, wherein the zeolite runner are provided with adsorption zone, cooling zone and desorption area, and the gas inlet pipeline is connected to the zeolite runner
Adsorption zone, and the net gas discharge pipe is located between the adsorption zone and the chimney of the zeolite runner, and the cooling gas air inlet pipeline
The cooling zone of the zeolite runner is connected, the another concentration exhaust pipe is located between desorption area and the incinerator of the zeolite runner,
And the bypass line one end connects the gas inlet pipeline, and the other end of the bypass line connects the net gas discharge pipe, and
An adsorption desorption structure is provided with the bypass line, the adsorption desorption structure of the another bypass line is provided with a concentrated gas pipeline, and
The concentrated gas pipeline is connected to the concentration exhaust pipe, it is characterised in that also group is de- provided with a suction on the net gas discharge pipe
Attached structure, and the adsorption desorption structure of the net gas discharge pipe is provided with an exhaust output tube road and a thermal source pipeline, and the waste gas is defeated
Go out pipeline and be 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 tool bypass processing structure as claimed in claim 1, it is characterised in that wherein
The incinerator is further any of which of heat accumulating type incinerator or direct-combustion furnace, and one is further provided with the thermal source pipeline
Auxiliary heater.
3. the volatide organic waste gas treating system of tool bypass processing structure as claimed in claim 1, it is characterised in that wherein
A runner is further provided with the adsorption desorption structure of the net gas discharge pipe, the runner is rotary type tower, horizontal or tubular
Any of which, and the runner is provided with adsorption zone, cooling zone and desorption area, and the net gas discharge pipe is connected to the suction of the runner
Attached area, 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 tool bypass processing structure as claimed in claim 3, it is characterised in that wherein
Adsorption material is further provided with the runner, and the adsorption material is further activated carbon, zeolite, silica gel, activated alumina, molecule
Sieve, manganese oxide, calcium hydroxide, any of which of graphene or doughnut.
5. the volatide organic waste gas treating system of tool bypass processing structure as claimed in claim 1, it is characterised in that wherein
Two adsorption material buckets are further provided with the adsorption desorption structure of the net gas discharge pipe, and the two adsorption materials bucket is used respectively as absorption
And desorption is used, and air inlet pipeline, waste gas outlet pipe and clean gas pipeline are provided with when the adsorption material bucket is set to the absorption used time, separately
Air inlet pipeline and desorption gas pipeline are provided with when the adsorption material bucket is set to the desorption used time.
6. the volatide organic waste gas treating system of tool bypass processing structure as claimed in claim 1, it is characterised in that wherein
Two adsorption material buckets are further provided with the adsorption desorption structure of the bypass line, and the two adsorption materials bucket is used respectively as absorption and de-
Attached use, and air inlet pipeline, waste gas outlet pipe and clean gas pipeline are provided with when the adsorption material bucket is set to the absorption used time, separately working as should
Adsorption material bucket be set to be desorbed the used time be provided with air inlet pipeline and desorption gas pipeline.
7. the volatide organic waste gas treating system of tool bypass processing structure as claimed in claim 1, it is characterised in that wherein
Multiple adsorption material buckets are further provided with the adsorption desorption structure of the net gas discharge pipe, and the plurality of adsorption material bucket is respectively as suction
Attached use, desorption are used and cooling is used, and air inlet pipeline, waste gas outlet pipe and clean gas are provided with when the adsorption material bucket is set to the absorption used time
Body 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
Air inlet pipeline and cooling gas pipeline are provided with for the cooling used time.
8. the volatide organic waste gas treating system of tool bypass processing structure as claimed in claim 1, it is characterised in that wherein
Multiple adsorption material buckets are further provided with the adsorption desorption structure of the bypass line, 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.
9. the volatide organic waste gas treating system of the tool bypass processing structure as described in claim 5,6,7 or 8, its feature exist
In, adsorption material is wherein further respectively provided with the adsorption material bucket of the adsorption desorption structure, and the adsorption material is further activated carbon, boiling
Stone, silica gel, activated alumina, molecular sieve, calcium hydroxide, any of which of graphene or doughnut.
10. the volatide organic waste gas treating system of the tool bypass processing structure as described in claim 5,6,7 or 8, its feature
It is, wherein the adsorption material bucket is 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 |
|---|---|---|---|
| TW106207155 | 2017-05-19 | ||
| TW106207155U TWM549656U (en) | 2017-05-19 | 2017-05-19 | Volatile organic exhaust gas treatment system with bypass treatment structure |
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| CN207056267U true CN207056267U (en) | 2018-03-02 |
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| CN110038499B (en) * | 2019-04-23 | 2021-03-16 | 宁波巨化化工科技有限公司 | Hydroformylation reactor |
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