CN207056268U - Volatile organic waste gas treatment improvement system with double treatment structures - Google Patents

Volatile organic waste gas treatment improvement system with double treatment structures Download PDF

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Publication number
CN207056268U
CN207056268U CN201720795163.2U CN201720795163U CN207056268U CN 207056268 U CN207056268 U CN 207056268U CN 201720795163 U CN201720795163 U CN 201720795163U CN 207056268 U CN207056268 U CN 207056268U
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pipeline
waste gas
adsorption
desorption
adsorption material
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郑石治
扶亚民
陈伦庆
吕权训
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Shanghai Huamao Environmental Protection Energy Saving Equipment Co ltd
Desiccant Technology Corp
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Shanghai Huamao Environmental Protection Energy Saving Equipment Co ltd
Desiccant Technology Corp
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Abstract

The utility model relates to a volatile organic waste gas treatment improvement system with double treatment structures, which comprises a waste gas inlet pipeline, a zeolite rotating wheel, a purified gas discharge pipeline, a cooling gas inlet pipeline, an incinerator, the combined design of a concentrated waste gas pipeline and a chimney, and is mainly characterized in that an absorption and desorption structure is assembled on the purified gas discharge pipeline, 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 concentrated waste gas pipeline, and the heat source pipeline is connected to the incinerator, therefore, the gas output by the purified gas discharge pipeline can be treated by the absorption and desorption structure to carry out the concentrated waste gas treatment, and the concentrated waste gas treated by the absorption and desorption structure is conveyed to the concentrated waste gas pipeline through the waste gas output pipeline again, so that the waste gas is treated by a double structure, then the concentrated waste gas is conveyed to the incinerator through the concentrated waste gas pipeline for uniform combustion and cracking, the treatment efficiency can reach 97 percent or even more than 99 percent, and the incinerator has the environmental protection effects of energy saving and carbon reduction.

Description

The volatile organic waste gas processing improvement system of the double processing structures of tool
Technical field
The utility model relates to a kind of volatile organic waste gas processing improvement system for having double processing structures, and espespecially one Kind can will be delivered to the concentration flue gas leading by the exhaust output tube road again by the concentration waste gas handled by adsorption desorption structure In road, 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 Processing structure volatile organic waste gas processing improvement system, make user can easy operation assembling, be to grind think of, design group with great concentration System, 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 improvement for having double processing structures System, it is to include a gas inlet pipeline, a zeolite runner, a net gas discharge pipe, a cooling gas air inlet pipeline, an incineration The Combination Design of stove, a concentration exhaust pipe and a chimney, it is that group is de- provided with a suction that it, which is essentially consisted on the net gas discharge pipe, Attached structure, and the adsorption desorption structure is provided with an exhaust output tube road and a thermal source pipeline, and the thermal source pipeline is to be connected to this Incinerator, the another exhaust output tube road is to be connected to the concentration exhaust pipe, thus, allows what is exported by the net gas discharge pipe Gas by the adsorption desorption structure can concentrate the processing of waste gas again, and again by by the concentration handled by adsorption desorption structure Waste gas is delivered in the concentration exhaust pipe by the exhaust output tube road again so that waste gas is handled by dual structure Under, then via the concentration exhaust pipe carry out that burning cracking is uniform, and its treatment effeciency can reach to be delivered in the incinerator 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 improvement for having double processing structures System, and by being provided with a runner in the adsorption desorption structure, the runner is wherein appointed for rotary type tower, horizontal or tubular etc. One 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 handles Improved lines for a kind of volatile organic waste gas for having double processing structures System, it is to include a gas inlet pipeline, a zeolite runner, a net gas discharge pipe, a cooling gas air inlet pipeline, an incineration Stove, a concentration exhaust pipe and a chimney, wherein the zeolite runner are provided with adsorption zone, cooling zone and are desorbed area, and the waste gas Air inlet pipeline is 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 with Between the chimney, and the cooling gas air inlet pipeline is the cooling zone for connecting the zeolite runner, and the another concentration exhaust pipe is provided at Between the desorption area of the zeolite runner and the incinerator, it is characterised in that:It is that group is provided with an adsorption desorption 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 thermal source pipeline is to be connected to this to burn Change stove, the another exhaust output tube road is to be connected to the concentration exhaust pipe.
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 delivered in the concentration exhaust pipe so that waste gas is under by dual structure processing, then via the concentration waste gas Pipeline carries out burning cracking uniformly to be delivered in the incinerator, and its treatment effeciency can reach 97% or even more than 99%, and have There is the environmental protection efficacy of 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 volatile organic waste gas processing improvement system of structure are to apply to semiconductor industry, opto-electronics or chemical industry The exhaust-gas treatment of the factory building of related industry so that for waste gas under by dual structure processing, its treatment effeciency can reach 97% very To more than 99%, and the environmental protection efficacy with carbon reduction, make that there is its practicality.
And the Major Systems of the volatile organic waste gas processing improvement system of the double processing structures of tool of the present utility model are bags A gas inlet pipeline 10, a zeolite runner 20, a net gas discharge pipe 30, one has been included to cool down gas air inlet pipeline 40, one and incinerate Stove 50, one concentrates the chimney 70 (as shown in Figures 1 and 2) of exhaust pipe 60 and one, and the wherein zeolite runner 20 also can be to use it He adsorbs the concentration runner of material, and the zeolite runner 20 is provided with adsorption zone 21, cooling zone 22 and desorption area 23, that can carry out The absorption of waste gas and by waste gas desorption into concentration waste gas, the another incinerator 50 can be heat accumulating type incinerator (RTO) or direct combustion Any of which such as stove (TO).
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 thermal source pipeline 120 is connection To the incinerator 50, the another exhaust output tube road 110 is to be connected to the concentration exhaust pipe 60 (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 The concentration exhaust pipe 60 is delivered to by the exhaust output tube road 110, clean gas is separately passed through into net gas discharge pipe again 30, which are delivered to chimney 70, discharges so that waste gas conveys under by dual structure processing, then via the concentration exhaust pipe 60 It is uniform that burning cracking is carried out in the incinerator 50, its treatment effeciency can reach 97% or even more than 99%, and with energy-conservation Subtract the environmental protection efficacy of carbon.
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 thermal source pipeline 220 is to be connected to the incinerator 50, the another exhaust output tube road 210 is to be connected to The concentration exhaust pipe 60.
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 delivered to again The concentration exhaust pipe 60 so that waste gas is delivered under by dual structure processing, then via the concentration exhaust pipe 60 It is uniform that burning cracking is carried out in the incinerator 50, its treatment effeciency is reached 97% or even more than 99%, and subtract with energy-conservation The environmental protection efficacy of carbon.The incinerator 50 of another the present embodiment can be heat accumulating type incinerator (RTO) or direct-combustion furnace (TO) etc. wherein It is any.
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 thermal source pipeline 320 is to be connected to the incinerator 50, the another exhaust output tube road 310 is to be connected to The concentration exhaust pipe 60.
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 delivered to the concentration exhaust pipe 60 again so that waste gas is passing through Under dual structure processing, then via the concentration exhaust pipe 60, to carry out burning cracking uniform being delivered in the incinerator 50, makes Its treatment effeciency can reach 97% or even more than 99%, and the environmental protection efficacy with carbon reduction.The incinerator of another the present embodiment It 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 volatile organic waste gas processing improvement system for having double processing structures, includes a gas inlet pipeline, a boiling Stone runner, a net gas discharge pipe, a cooling gas air inlet pipeline, an incinerator, a concentration exhaust pipe and a chimney, wherein should 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 The 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 The cooling zone of runner, the another concentration exhaust pipe is between the desorption area of the zeolite runner and the incinerator, it is characterised in that: Group is provided with an adsorption desorption structure on the net gas discharge pipe, and the adsorption desorption structure is provided with an exhaust output tube road and a heat source tube Road, and the exhaust output tube road is connected to the concentration exhaust pipe, the another thermal source pipeline is connected to the incinerator.
2. the volatile organic waste gas processing improvement system of the double processing structures of tool as claimed in claim 1, it is characterised in that its In the incinerator be further any of which of heat accumulating type incinerator or direct-combustion furnace, and be further provided with the thermal source pipeline One auxiliary heater.
3. the volatile organic waste gas processing improvement system of the double processing structures of tool as claimed in claim 1, it is characterised in that its In be further provided with a runner in the adsorption desorption structure, the runner is any of which of rotary type tower, horizontal or tubular, and The runner 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 volatile organic waste gas processing improvement system of the double processing structures of tool as claimed in claim 3, it is characterised in that its In 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 volatile organic waste gas processing improvement system of the double processing structures of tool as claimed in claim 1, it is characterised in that its In two adsorption material buckets are further provided with the adsorption desorption structure, 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 when the adsorption material Bucket be set to be desorbed the used time be provided with air inlet pipeline and desorption gas pipeline.
6. the volatile organic waste gas processing improvement system of the double processing structures of tool as claimed in claim 5, it is characterised in that its In the adsorption desorption structure adsorption material bucket in be further provided with adsorption material, and the adsorption material is further activated carbon, zeolite, silicon Glue, activated alumina, molecular sieve, manganese oxide, calcium hydroxide, any of which of graphene or doughnut.
7. the volatile organic waste gas processing improvement system of the double processing structures of tool as claimed in claim 1, it is characterised in that its In multiple adsorption material buckets are further provided with the adsorption desorption structure, and the plurality of adsorption material bucket is used respectively as absorption, desorption is used And cooling is used, 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, and work as The adsorption 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 set There are air inlet pipeline and cooling gas pipeline.
8. the volatile organic waste gas processing improvement system of the double processing structures of tool as claimed in claim 7, it is characterised in that its In the adsorption desorption structure adsorption material bucket in be further respectively provided with adsorption material, and the adsorption material is further activated carbon, zeolite, silicon Glue, activated alumina, molecular sieve, calcium hydroxide, any of which of graphene or doughnut.
9. the volatile organic waste gas processing improvement system of the double processing structures of tool as described in claim 5 or 7, its feature exist In wherein the adsorption material bucket is further set to the hollow long cylinder bodily form, hollow cuboid or the hollow ball bodily form.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110772927A (en) * 2019-06-28 2020-02-11 上海深城环保设备工程有限公司 Parallel pipe type gas adsorption concentration device
CN111203068A (en) * 2018-04-23 2020-05-29 李君� High-efficient environmental protection's organic waste gas adsorbs concentrator
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
CN115445387A (en) * 2022-08-23 2022-12-09 江苏中电创新环境科技有限公司 Treatment system and method for high-air-volume low-concentration organic waste gas

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111203068A (en) * 2018-04-23 2020-05-29 李君� High-efficient environmental protection's organic waste gas adsorbs concentrator
CN111203068B (en) * 2018-04-23 2021-10-12 张景峰 High-efficient environmental protection's organic waste gas adsorbs concentrator
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
CN110772927A (en) * 2019-06-28 2020-02-11 上海深城环保设备工程有限公司 Parallel pipe type gas adsorption concentration device
CN110772927B (en) * 2019-06-28 2021-01-29 上海深城环保设备工程有限公司 Parallel pipe type gas adsorption concentration device
US11850544B2 (en) 2019-06-28 2023-12-26 Shanghai Shencheng Environmental Protection Equipment & Engineering Co., Ltd. Parallel pipe type gas adsorption and concentration apparatus
CN115445387A (en) * 2022-08-23 2022-12-09 江苏中电创新环境科技有限公司 Treatment system and method for high-air-volume low-concentration organic waste gas

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