CN206881453U - One kind mixing organic waste-gas purification and energy processing system - Google Patents

One kind mixing organic waste-gas purification and energy processing system Download PDF

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Publication number
CN206881453U
CN206881453U CN201720170290.3U CN201720170290U CN206881453U CN 206881453 U CN206881453 U CN 206881453U CN 201720170290 U CN201720170290 U CN 201720170290U CN 206881453 U CN206881453 U CN 206881453U
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tower
condensing
condensing tower
adsorption
absorption
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CN201720170290.3U
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Chinese (zh)
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刘会成
何云霞
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Wuxi Wisdom Environmental Protection Technology Monitoring Research Institute Co Ltd
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Wuxi Wisdom Environmental Protection Technology Monitoring Research Institute Co Ltd
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Abstract

The utility model discloses one kind mixing organic waste-gas purification and energy processing system,Including body,Absorption tower,Adsorption tower and recovery pond,The side of the body is fixedly installed air pump,The other end of the air pump connects the first condensing tower,The bottom of first condensing tower is provided with organic liquor collecting tank,The side of first condensing tower is communicated with the second condensing tower,The side connection absorption tower of second condensing tower,The bottom on the absorption tower is communicated with conversion pool,The opposite side of the body is provided with recovery pond,The liquid outlet passes through pipeline communication with recovery pond,The adsorption tower is internally provided with adsorption plate,The opposite side top of the body is provided with gas vent,By setting the first condensing tower and the second condensing tower,And it is set to different condensation temperatures,It is easy to the Direct Classification of waste gas to condense,Improve recovery utilization rate,Adsorption tower is set,It is easy to adsorb the VOCs in organic exhaust gas,Improve the clean-up effect of organic exhaust gas.

Description

One kind mixing organic waste-gas purification and energy processing system
Technical field
Organic waste gas treatment equipment technical field is the utility model is related to, is specially a kind of mixing organic waste-gas purification and energy Source processing system.
Background technology
With present industrial continuous development, the discharge of all kinds of organic exhaust gas is also increasingly severe, and organic exhaust gas mainly wraps Benzene class, various hydro carbons, alcohols, aldehydes etc. are included, the respiratory system and hematological system of people can be influenceed, serious is direct carcinogenic, and It is more serious to the damage ratio of atmospheric environment, it is therefore necessary to could to be discharged after being reclaimed to VOCs treatment.
Processing in the prior art to organic exhaust gas is relatively simple, it is impossible to can be reused in effective recovery organic exhaust gas Organic components, it is impossible to organic exhaust gas is reasonably utilized, and obtains in end-o f-pipe -control coarse, it is completely net not reach organic exhaust gas The purpose of change.
Utility model content
The purpose of this utility model is to provide a kind of mixing organic waste-gas purification and energy processing system, with solution State the problem of being proposed in background technology.
To achieve the above object, the utility model provides following technical scheme:One kind mixing organic waste-gas purification and the energy Change processing system, including body, absorption tower, adsorption tower and recovery pond, the side of the body are fixedly installed air pump, the gas One end of pump connects the first condensing tower by pipeline communication exhaust gas entrance, the other end of the air pump, first condensing tower Top is fixed on the upper end on the inside of body, and first condensing tower is internally provided with condenser pipe, the side of first condensing tower Condensing water inlet is provided with, the opposite side of first condensing tower is provided with condensation-water drain, the condensing water inlet and condensation Water out is respectively communicated with the both ends of condenser pipe, and the bottom of first condensing tower is provided with organic liquor collecting tank, described organic The bottom surface of liquid collecting tank is fixed on the inside of body, and the organic liquor collecting tank is connected with the first condensing tower by pipeline, institute The side bottom surface for stating organic liquor collecting tank is provided with organic liquor export mouth, and the side of first condensing tower is communicated with the second condensation Tower, second condensing tower is identical with the first condensation tower structure, and the side of second condensing tower is communicated with absorption tower, the suction The top of receipts tower is fixed on the upper end on the inside of body, and the top on the absorption tower is provided with shower nozzle, and the inside on the absorption tower is set Buffer board is equipped with, there is conversion pool the bottom on the absorption tower by pipeline communication, and the bottom surface of the conversion pool is fixed in body Side bottom surface, the bottom surface on the inside of the body are fixedly connected with support close to the position of conversion pool, and the upper surface of the support is set There is water pump, one end of the water pump connects with conversion pool, and its other end is connected with the top of absorption tower side, the conversion pool Side be provided with liquid outlet, the opposite side of the body is provided with recovery pond, and the liquid outlet is connected with recovery pond by pipeline Logical, the top of the adsorption tower is fixed on the upper end on the inside of body, the bottom of the adsorption tower side and the top of absorption tower side End is connected, and the adsorption tower is internally provided with adsorption plate, and the opposite side top of the body is provided with gas vent, described Gas vent is connected with adsorption tower, and the bottom surface corner of the body is respectively arranged with base.
Preferably, the condensate temperature of first condensing tower is arranged to 5 DEG C -20 DEG C, the condensation of second condensing tower Coolant-temperature gage is arranged to -5 DEG C -5 DEG C.
Preferably, the external aqueous solution of urea of the shower nozzle.
Preferably, some through holes are provided with the buffer board, and it is fiberglass resistant material.
Preferably, the adsorption plate is arranged with some pieces in parallel, and it is NACF.
Compared with prior art, the beneficial effects of the utility model are:By setting the first condensing tower and the second condensing tower, And different condensation temperatures is set to, it is easy to the Direct Classification of high-concentration waste gas to condense, improves recovery utilization rate, pass through Adsorption tower is set and is arranged to multi-stage absorption, is easy to adsorb the VOCs in organic exhaust gas, improves the clean-up effect of organic exhaust gas.
Brief description of the drawings
Fig. 1 is the utility model internal structure cut-away view;
Fig. 2 is buffer board structure schematic diagram of the present utility model.
In figure:1- bodies;The condensing towers of 2- first;The condensing towers of 3- second;4- absorption towers;5- adsorption towers;6- recovery ponds;7- gas Body exports;8- exhaust gas entrances;9- air pumps;10- condenser pipes;11- condensing water inlets;12- condensation-water drains;13- organic liquor liquid collectings Pond;14- buffer boards;15- shower nozzles;16- conversion pools;17- water pumps;18- supports;19- adsorption plates;20- pipelines;21- bases;22- Liquid outlet;23- organic liquor export mouths.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made The every other embodiment obtained, belong to the scope of the utility model protection.
Fig. 1 and Fig. 2 are referred to, the utility model provides a kind of technical scheme:One kind mixing organic waste-gas purification and the energy Change processing system, including body 1, absorption tower 4, adsorption tower 5 and recovery pond 6, the side of the body 1 are fixedly installed air pump 9, One end of the air pump 9 connects exhaust gas entrance 8 by pipeline 20, and the other end of the air pump 9 connects the first condensing tower 2, described The top of first condensing tower 2 is fixed on the upper end of the inner side of body 1, and first condensing tower 2 is internally provided with condenser pipe 10, described The side of first condensing tower 2 is provided with condensing water inlet 11, and the opposite side of first condensing tower 2 is provided with condensation-water drain 12, the condensing water inlet 11 and condensation-water drain 12 are respectively communicated with the both ends of condenser pipe 10, the bottom of first condensing tower 2 End is provided with organic liquor collecting tank 13, and the bottom surface of the organic liquor collecting tank 13 is fixed on the inside of body 1, the organic liquor collection Liquid pool 13 is connected with the first condensing tower 2 by pipeline 20, and the side bottom surface of the organic liquor collecting tank 13 is provided with organic liquor Export mouth 23, the side of first condensing tower 2 are communicated with the second condensing tower 3, the condensing tower 2 of the second condensing tower 3 and first Structure is identical, and the side of second condensing tower 3 is communicated with absorption tower 4, and the top on the absorption tower 4 is fixed on the inner side of body 1 Upper end, the top on the absorption tower 4 is provided with shower nozzle 15, and the absorption tower 4 is internally provided with buffer board 14, the absorption The bottom of tower 4 is communicated with conversion pool 16 by pipeline 20, and the bottom surface of the conversion pool 16 is fixed on the inside bottom surface of body 1, described The bottom surface of the inner side of body 1 is fixedly connected with support 18 close to the position of conversion pool 16, and the upper surface of the support 18 is provided with water Pump 17, one end of the water pump 17 connect with conversion pool 16, and its other end is connected with the top of the side of absorption tower 4, described turn The side for changing pond 16 is provided with liquid outlet 22, and the opposite side of the body 1 is provided with recovery pond 6, the liquid outlet 22 and recovery Pond 6 is connected by pipeline 20, and the top of the adsorption tower 5 is fixed on the upper end of the inner side of body 1, the bottom of the side of adsorption tower 5 End is connected with the top of the side of absorption tower 4, and the adsorption tower 5 is internally provided with adsorption plate 19, the opposite side of the body 1 Top is provided with gas vent 7, and the gas vent 7 is connected with adsorption tower 5, and the bottom surface corner of the body 1 is set respectively There is base 21.
The condensate temperature of first condensing tower 2 is arranged to 5 DEG C -20 DEG C, the condensate temperature of second condensing tower 3 It is arranged to -5 DEG C -5 DEG C, the 15 external aqueous solution of urea of shower nozzle, is provided with some through holes on the buffer board 14, and it is glass Glass steel resistant material, the adsorption plate 19 is arranged with some pieces in parallel, and it is NACF.
Operation principle:During use, organic exhaust gas enters the first condensing tower 2 in the presence of air pump 9 by pipeline 20, Condensate liquid is by entrance organic liquor collecting tank 13, then is directly exported by organic liquor export mouth 23 and carry out secondary use, Ran Houyou Machine waste gas enters the second condensing tower 3 and carries out time condensation, and time condensation liquid is again introduced into organic liquor collecting tank 13 for using, condensation Organic exhaust gas enters absorption tower 4 after end, and by nitrogen oxides of exhaust gas, chlorine, all oxidation is gone back in the presence of aqueous solution of urea Former, decomposition absorbs, and except denitrification and chlorine, solution Reusability in the presence of water pump 17, carries out more secondary responses, the liquid of high concentration Recovery pond 6 is entered by liquid outlet 22 in bottom, the gas after the completion of oxidation enters adsorption tower 5, gone out under the seat of activated carbon The VOCs gone in gas, air is discharged into by gas vent 7 after the completion of purification.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art, It is appreciated that these embodiments can be carried out with a variety of changes in the case where not departing from principle of the present utility model and spirit, repaiied Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.

Claims (5)

1. one kind mixing organic waste-gas purification and energy processing system, including body(1), absorption tower(4), adsorption tower(5)With Recovery pond(6), it is characterised in that:The body(1)Side be fixedly installed air pump(9), the air pump(9)One end pass through Pipeline(20)Connect exhaust gas entrance(8), the air pump(9)The other end connect the first condensing tower(2), first condensing tower (2)Top be fixed on body(1)The upper end of inner side, first condensing tower(2)It is internally provided with condenser pipe(10), described One condensing tower(2)Side be provided with condensing water inlet(11), first condensing tower(2)Opposite side be provided with condensed water and go out Mouthful(12), the condensing water inlet(11)And condensation-water drain(12)It is respectively communicated with condenser pipe(10)Both ends, described first Condensing tower(2)Bottom be provided with organic liquor collecting tank(13), the organic liquor collecting tank(13)Bottom surface be fixed on body(1) Inside, the organic liquor collecting tank(13)With the first condensing tower(2)Pass through pipeline(20)It is connected, the organic liquor collecting tank (13)Side bottom surface be provided with organic liquor export mouth(23), first condensing tower(2)Side be communicated with the second condensing tower (3), second condensing tower(3)With the first condensing tower(2)Structure is identical, second condensing tower(3)Side be communicated with suction Receive tower(4), the absorption tower(4)Top be fixed on body(1)The upper end of inner side, the absorption tower(4)Top be provided with Shower nozzle(15), the absorption tower(4)Be internally provided with buffer board(14), the absorption tower(4)Bottom pass through pipeline(20) It is communicated with conversion pool(16), the conversion pool(16)Bottom surface be fixed on body(1)Inside bottom surface, the body(1)Inner side Bottom surface is close to conversion pool(16)Position be fixedly connected with support(18), the support(18)Upper surface be provided with water pump (17), the water pump(17)One end and conversion pool(16)Connection, its other end and absorption tower(4)The top of side is connected, The conversion pool(16)Side be provided with liquid outlet(22), the body(1)Opposite side be provided with recovery pond(6), it is described Liquid outlet(22)With recovery pond(6)Pass through pipeline(20)Connection, the adsorption tower(5)Top be fixed on body(1)Inner side Upper end, the adsorption tower(5)The bottom and absorption tower of side(4)The top of side is connected, the adsorption tower(5)Inside set It is equipped with adsorption plate(19), the body(1)Opposite side top be provided with gas vent(7), the gas vent(7)With absorption Tower(5)It is connected, the body(1)Bottom surface corner be respectively arranged with base(21).
2. a kind of mixing organic waste-gas purification according to claim 1 and energy processing system, it is characterised in that:It is described First condensing tower(2)Condensate temperature be arranged to 5 DEG C -20 DEG C, second condensing tower(3)Condensate temperature be arranged to -5 ℃-5℃。
3. a kind of mixing organic waste-gas purification according to claim 1 and energy processing system, it is characterised in that:It is described Shower nozzle(15)External aqueous solution of urea.
4. a kind of mixing organic waste-gas purification according to claim 1 and energy processing system, it is characterised in that:It is described Buffer board(14)On be provided with some through holes, and it is fiberglass resistant material.
5. a kind of mixing organic waste-gas purification according to claim 1 and energy processing system, it is characterised in that:It is described Adsorption plate(19)It is arranged with some pieces in parallel, and it is NACF.
CN201720170290.3U 2017-02-24 2017-02-24 One kind mixing organic waste-gas purification and energy processing system Active CN206881453U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720170290.3U CN206881453U (en) 2017-02-24 2017-02-24 One kind mixing organic waste-gas purification and energy processing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720170290.3U CN206881453U (en) 2017-02-24 2017-02-24 One kind mixing organic waste-gas purification and energy processing system

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110215800A (en) * 2019-06-17 2019-09-10 世源科技工程有限公司 A kind of processing method and its processing equipment of high boiling point organic compound exhaust gas

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110215800A (en) * 2019-06-17 2019-09-10 世源科技工程有限公司 A kind of processing method and its processing equipment of high boiling point organic compound exhaust gas

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