CN204865478U - Integrated form stench clean system - Google Patents
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- CN204865478U CN204865478U CN201520243558.2U CN201520243558U CN204865478U CN 204865478 U CN204865478 U CN 204865478U CN 201520243558 U CN201520243558 U CN 201520243558U CN 204865478 U CN204865478 U CN 204865478U
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Abstract
The utility model provides an integrated form stench clean system. The device mainly includes: include: dominant reaction tower, draught fan and the tower of absorb the remnant air, the one end of draught fan is continuous with the top of dominant reaction tower through the pipeline, and it is continuous with the tower of absorb the remnant air's bottom that the other end passes through the pipeline, and the foul gas passes through dominant reaction tower, draught fan and the tower of absorb the remnant air in proper order. Set up absorbing device, defroster and low temperature foul smell purifier in advance from bottom to top in the dominant reaction tower, set up back absorbing device, collecting tank, swirler, degree of depth absorbing device and second defroster from bottom to top in the tower of absorb the remnant air. The utility model discloses a plasma technique body and the mode that the SOx/NOx control technique combined together utilize the plasma technique to turn into the odorant small molecule substance such as odorless carbon dioxide and nitrogen oxide in the dominant reaction tower, realize the deodorization function, the tower of absorb the remnant air then absorbs the small molecule substance of foul gas to it reaches corresponding emission standard to do degree of depth absorption to the macromolecule of some difficult degradations.
Description
Technical field
The utility model relates to gas purification technique field, particularly relates to a kind of integrated form stench cleaning system.
Background technology
Stench, also claims vicious gas, refers to that all stimulate olfactory organ to cause the gaseous matter of people's unhappiness and damage living environment, i.e. offensive gases.Stench can poison respiratory tract, cardiovascular and nervous system, insulting sense of smell, is one of the reason making human body produce distortion, canceration.The comparison of ingredients of stench is complicated, and wherein endangering larger has hydrogen sulfide, ammonia, thio-alcohol (as: methyl mercaptan), thioether class (as: dimethyl disulfide), toluene, phenol, indoles (as: nitrogen (mixing) indenes), fatty acid, aldehydes, amine and halogen-containing organic matter etc. tens kinds.In life, some foul gas directly discharges air, pollutes to air, is directly detrimental to health, and causes unnecessary puzzlement to people's life; Some foul gas, with water and waste sludge discharge water body, not only affects water quality, and threatens to hydrobiological life.Stench influence degree is large, and impact scope is wide, and public response is stronger.Along with the raising of people's living standard, foul gas process is subject to extensive concern.
The foul gas of monosodium glutamate manufactory and refuse depot mainly contains ammonia, methyl sulfide, hydrogen sulfide, methane, methyl mercaptan aldehydes, propionic acid, nitrogen (mixing) indenes and thiol class substance etc., in view of stench has above-mentioned harm, be necessary to take appropriate measures to the stench controlled and process produces in glutamate production processing and refuse collection, storage, transport and processing procedure.
Traditional Deodor method comprises: WATER-WASHING METHOD, combustion method, cooling method, absorption method, air dilution method, soda acid absorption process, biomembrance process, oxidizing process and catforming etc., these methods exist that operating cost is high, secondary pollution, treatment effect is not good and control the defects such as difficulty is large, especially for low concentration, large discharge and the process of the lower foul waste gas of concentration requirement after administering, deodorizing effect is not good.
The lower temperature plasma technology of rising in recent years is as the novel the methods of odour control of one, there is the environmental protection treatment new technology that purification efficiency is high, energy consumption is low, secondary pollution is few, applied widely, treating capacity is large, simple to operate, especially be applicable to process low concentration, atm number gaseous contaminant, the method utilizes a large amount of active particles in plasma directly to remove substance decomposition that is poisonous, harmful and difficult degradation.
Current plasma technique controls the main Problems existing of foul gas to be had: plasma technique is difficult to degraded to a part of larger molecular organics, and gas flow is comparatively large, when pollutant levels are higher, is difficult to accomplish harmless odorless process; In addition, the odorant after plasma reaction is converted into the small-molecule substance of the foul smells such as sulfide (as sulfur trioxide) and nitrogen oxide, and these small-molecule substances are also main atmosphere pollutions, thus cause secondary pollution, and energy consumption is high.And due to the existence of the small-molecule substance of odorless in advanced treatment process, the effective rate of utilization of medicament reduces greatly.
Utility model content
Embodiment of the present utility model provides a kind of integrated form stench cleaning system, to realize carrying out effective purified treatment to foul gas.
To achieve these goals, the utility model takes following technical scheme.
A kind of integrated form stench cleaning system, comprise: main reaction tower (100), air-introduced machine (6) and tail gas absorber (200), one end of described air-introduced machine (6) is connected through the top of piping with described main reaction tower (100), the other end of described air-introduced machine (6) is connected by the bottom of pipeline with described tail gas absorber (200), and foul gas is successively through described main reaction tower (100), air-introduced machine (6) and tail gas absorber (200).
Preferably, in described main reaction tower (100), pre-absorption device is set from bottom to top, first demister (4) and low temperature odor purification (5), foul gas is entered in described main reaction tower (100) by the air inlet (1) of described main reaction tower (100) bottom, and successively through the pre-receiving apparatus of described suction, low temperature odor purification (5) and the first demister (4).
Preferably, between described main reaction tower (100) and tail gas absorber (200), water tank (15) is set, pre-absorption device in described main reaction tower (100) comprises the first packing layer (2), first spray equipment (3) and circulating pump (14), described first demister (4) is arranged between described first spray equipment (3) and described low temperature odor purification (5), in described first packing layer (2) part, the first peep hole (13) is set, described circulating pump (14) is connected with described first spray equipment (3) and described water tank (15), water in described water tank (15) is drawn in described first spray equipment (3).
Preferably, at the bottom of the tower of described main reaction tower (100), store absorbing liquid, one end of described circulating pump (14) connects at the bottom of tower washes receipts liquid, and the other end connects described first spray equipment (3), realizes absorbing liquid circulation.
Preferably, rear absorption plant, collecting tank (17), cyclone (9), degree of depth absorption plant and the second demister (12) are set from bottom to top in described tail gas absorber (200), flue gas enters in described tail gas absorber (200) by the air inlet of described tail gas absorber (200) bottom, and absorption plant, described collecting tank (17), described cyclone (9), described degree of depth absorption plant and described second demister (12) after described successively, finally by the top discharge air of described tail gas absorber (200).
Preferably, described rear absorption plant comprises the second packing layer (7), the second spray equipment (8) and circulating pump (19), in described second packing layer (7) part, the second peep hole (16) is set, described circulating pump (19) is connected with described second spray equipment (8), water tank (15), is drawn in described second spray equipment (8) by the water in described water tank (15).
Preferably, arrange wash receipts liquid in the bottom of described tail gas absorber (200), one end of described circulating pump (19) connects at the bottom of tower washes receipts liquid, and the other end connects described second spray equipment (8), realizes absorbing liquid circulation.
Preferably, described degree of depth absorption plant comprises the 3rd packing layer (10), the 3rd spray equipment (11), cyclone (9), chemical tank (20), collecting tank (17) and circulating pump (21), described collecting tank (17) is arranged between described 3rd spray equipment (11) and described cyclone (9), be made up of inner tank wall and baffle plate obliquely, the bottom of described collecting tank (17) is connected with described chemical tank (20) by pipeline.
Preferably, one end of described circulating pump (21) connects chemical tank (20), and the other end connects described 3rd spray equipment (11), realizes absorbing liquid circulation.
Preferably, described cyclone (9) is arranged between described collecting tank (17) and described degree of depth absorption plant, absorbing liquid flows down along tube wall after described cyclone (9), is collected and flow to described chemical tank (20) by back of pipeline by described collecting tank (17).
The technical scheme provided as can be seen from above-mentioned embodiment of the present utility model, the utility model embodiment is by constructing the integrated form stench cleaning system be made up of main reaction tower, air-introduced machine and tail gas absorber, adopt the mode that plasma technology body combines with desulphurization denitration technology, adopt the structure that double tower three circulates, achieve foul gas efficiently to remove thoroughly, utilize plasma technique odorant to be converted into the small-molecule substance such as sulfide and nitrogen oxide of odorless in main reaction tower, realize deodorization functions; Tail gas absorber then absorbs the small-molecule substance of such atmosphere pollution, and does degree of depth absorption to the large molecule of part difficult degradation.The integrated form stench cleaning system of the utility model embodiment is applicable to foul gas process, and particularly relate to the foul gas process of high concentration, have odor removal efficient high, operating cost is low, simple to operate, the advantage of non-secondary pollution.
The aspect that the utility model is additional and advantage will part provide in the following description, and these will become obvious from the following description, or be recognized by practice of the present utility model.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme of the utility model embodiment, below the accompanying drawing used required in describing embodiment is briefly described, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of a kind of integrated form stench cleaning system that the utility model embodiment provides,
In figure: main reaction tower 100, tail gas absorber 200,1: air inlet, 2: the first packing layers, 3: the first spray equipments, 4: the first demisters, 5: low temperature odor purification, 6: air-introduced machine, 7: the second packing layers, 8: the second spray equipments, 9: hydrocyclone, 10: the three packing layers, 11: the three spray equipments, 12: the second demisters, 13: the first peep holes, 14: circulating pump 1,15: water tank, 16: the second peep holes, 17: baffle plate, 18: the three peep holes, 19: circulating pump 2,20: chemical tank, 21: circulating pump 3 and 22: valve.
Detailed description of the invention
Be described below in detail embodiment of the present utility model, the example of described embodiment is shown in the drawings, and wherein same or similar label represents same or similar element or has element that is identical or similar functions from start to finish.Being exemplary below by the embodiment be described with reference to the drawings, only for explaining the utility model, and can not being interpreted as restriction of the present utility model.
Those skilled in the art of the present technique are appreciated that unless expressly stated, and singulative used herein " ", " one ", " described " and " being somebody's turn to do " also can comprise plural form.Should be further understood that, the wording used in description of the present utility model " comprises " and refers to there is described feature, integer, step, operation, element and/or assembly, but does not get rid of and exist or add other features one or more, integer, step, operation, element, assembly and/or their group.Should be appreciated that, when we claim element to be " connected " or " coupling " to another element time, it can be directly connected or coupled to other elements, or also can there is intermediary element.In addition, " connection " used herein or " coupling " can comprise wireless connections or couple.Wording "and/or" used herein comprises one or more arbitrary unit listing item be associated and all combinations.
Those skilled in the art of the present technique are appreciated that unless otherwise defined, and all terms used herein (comprising technical term and scientific terminology) have the meaning identical with the general understanding of the those of ordinary skill in field belonging to the utility model.Should also be understood that those terms defined in such as general dictionary should be understood to have the meaning consistent with the meaning in the context of prior art, unless and define as here, can not explain by idealized or too formal implication.
For ease of the understanding to the utility model embodiment, be further explained explanation below in conjunction with accompanying drawing for several specific embodiment, and each embodiment does not form the restriction to the utility model embodiment.
The utility model embodiment is on the basis of eliminating stink, odorant is transformed to the sulfide generated, nitrogen oxide has done further absorption, and advanced treating has been done to the odorant of difficult degradation, also sulfide can be achieved while guarantee stink is up to standard, the qualified discharge of nitrogen oxide, while guarantee efficient deodorizing, also solves secondary pollution problem.
Plasma is known as the 4th kind of thing form except solid, liquid, gas tri-state, it by electronics, ion, free radical and neutral particle form in electroneutral conducting fluid.Plasma is generally divided into hot plasma (equilibrium plasma) and low temperature plasma (nonequilibrium plasma), lower temperature plasma technology is widely used in fields such as semi-conductor industry, thin polymer film, material antiseptic erosion, plasma electronics, plasma synthesis, plasma metallurgy, plasma Coal Chemical Industry, plasma three-protection design, lower temperature plasma technology is under making whole plasma system keep the prerequisite of low temperature, produce the electronics with sufficiently high energy, gas molecule is excited by collision, dissociates and ionize; Thus realize effective utilization of chemical reaction and energy, make it have a wide range of applications at field of Environment Protection.
The generation of plasma mainly contains gaseous discharge method, radiation exposure method, photo-ionisation method, thermal ionization method etc.Comprehensive various discharge type, wherein gas discharge is the most general and conventional.Usually breakdown for gas under electric field action and conduction physical phenomenon call gas discharge, the plasma produced by this kind of mode is called gas discharge plasma.
The structural representation of a kind of integrated form stench cleaning system that the utility model embodiment provides as shown in Figure 1, comprise: main reaction tower 100, tail gas absorber 200, air inlet 1, first packing layer 2, first spray equipment 3, first demister 4, low temperature odor purification 5, air-introduced machine 6, second packing layer 7, second spray equipment 8, hydrocyclone 9, 3rd packing layer 10, 3rd spray equipment 11, second demister 12, first peep hole 13, circulating pump 1-14, water tank 15, second peep hole 16, baffle plate 17, 3rd peep hole 18, circulating pump 2-19, chemical tank 20, circulating pump 3-21 and valve 22.
As shown in Figure 1, the utility model embodiment comprises main reaction tower 100, air-introduced machine 6 and tail gas absorber 200, one end of air-introduced machine 6 is connected through the top of piping with main reaction tower 100, the other end is connected by the bottom of pipeline with tail gas absorber 200, and waste gas is successively through main reaction tower 100, air-introduced machine 6 and tail gas absorber 200.
Arrange from bottom to top in described main reaction tower 100 and inhale pre-receiving apparatus, first demister 4 and low temperature odor purification 5, foul gas is entered in main reaction tower 100 by the air inlet 1 bottom main reaction tower 100, and successively through pre-absorption device, low temperature odor purification 5 and the first demister 4.
Between described main reaction tower (100) and tail gas absorber (200), water tank (15) is set, pre-absorption device in described main reaction tower 100 comprises the first packing layer 2, first spray equipment 3 and circulating pump 14, arranges peep hole 13 in the first packing layer 2 part.Circulating pump 14 is connected with the first spray equipment 3 and water tank 15, is drawn into by the water in water tank 15 in first spray equipment 3.Absorbing liquid is stored at the bottom of the tower of main reaction tower 100, circulating pump 14 one end connects at the bottom of tower washes receipts liquid, one end connects the first spray equipment 3, realize absorbing liquid circulation, above-mentioned pre-absorption device mainly plays dedusting and pre-absorption effect, first demister 4 is arranged between the first spray equipment 3 and low temperature odor purification 5, can remove the drop be mingled with in foul gas.Both above-mentioned pre-absorption device and the first demister 4 are combined, and can play dedusting and pre-absorption effect, ensure that the operation of the efficient stable of follow-up low temperature odor purification 5.
Low temperature odor purification 5 is entered through the pretreated foul smell of above-mentioned pre-absorption device, under the effect of high electric field, on the one hand, the high energy electron produced in electrode space goes to clash into gas with foreign flavor molecule with the speed of 3,000,000 times to 3,000 ten thousand times each second, odorant is directly broken down into simple substance or is converted into odorless material, on the other hand, odorant under the effect such as a large amount of high energy electron, ion, excited state particle, oxygen radical and hydroperoxyl radical the oxidized odorless Small molecular that is decomposed into (as SO
2, SO
3, NO
x, CO
2deng), the power supply of this low temperature odor purification 5 is high-voltage discharger.After low temperature odor purification 5 processes, foul gas originally is mainly converted into the Small molecular of some odorless and the material frowzy of some difficult degradations, the Small molecular of these odorless and material frowzy are discharged at main reaction tower 100 top, arrive the air inlet of the bottom of tail gas absorber 200 along pipeline through air-introduced machine 6, enter tail gas absorber 200 by this air inlet.
Rear absorption plant, collecting tank 17, cyclone 9, degree of depth absorption plant and the second demister 12 are set in described tail gas absorber 200 from bottom to top, flue gas enters in tail gas absorber 200 by the air inlet bottom tail gas absorber 200, and successively through absorption plant, collecting tank 17, cyclone 9, degree of depth absorption plant and the second demister 12 later, finally by the top discharge air of tail gas absorber 200.
Flue gas first will through absorption plant later in tail gas absorber, and this rear absorption plant comprises the second packing layer 7, second spray equipment 8 and circulating pump 19, arranges the second peep hole 16 in the second packing layer 7 part.Absorbing fluid is stored at the bottom of the tower of tail gas absorber 200, and circulating pump 19 one end connects at the bottom of tower washes receipts liquid, and the other end connects the second spray equipment 8, realizes absorbing liquid circulation.Circulating pump 19 is connected with the second spray equipment 8 and water tank 15, is drawn into by the water in water tank 15 in second spray equipment 8.The sulfide that this rear absorption plant dominant absorption produces after plasma reaction, the atmosphere pollutions such as nitrogen oxide, while elimination secondary pollution, also alleviate the degree of depth absorb load, the effective rate of utilization of medicament is improved, thus reduce the dosage of medicament, reduce operating cost, flue gas penetration depth absorption plant after absorption plant after this.
Degree of depth absorption plant is in the first half of tail gas absorber 200, and it comprises the 3rd packing layer 10, the 3rd spray equipment 11, cyclone 9, chemical tank 20, collecting tank 17 and circulating pump 21.Collecting tank 17 is arranged between the 3rd spray equipment 11 and cyclone 9, by inner tank wall with become the baffle plate of 45 degree obliquely and form, the bottom of collecting tank 17 by through the pipeline of tank body be connected with chemical tank, the effect of collecting tank 17 is the spray liquid of collection degree of depth absorption and flows to chemical tank 20 by back of pipeline, realizes degree of depth absorbing liquid and recycles.
Described cyclone 9 is arranged between collecting tank 17 and degree of depth absorption plant, its effect be realize aqueous vapor abundant mixing and absorbing liquid is stayed, so that collecting tank 17 can effectively be collected along inner tank wall.Absorbing liquid flows down along tube wall after cyclone 9, is collected and flow to chemical tank by back of pipeline by collecting tank 17.Circulating pump 21 1 termination chemical tank, a termination the 3rd spray equipment 11, realizes absorbing liquid circulation.
The Main Function of degree of depth absorption plant does further process to the odorant of difficult degradation, ensures foul smell qualified discharge, and the waste gas after the purification of this degree of depth absorption plant is gone out by the tower top discharge of tail gas absorber 200 by the second demister 12.
Plasma deodorizing has two approach: one is in plasma production, and odorant can directly be broken down into simple substance by high energy electron bombardment or be converted into harmless odorless material.Under the effect of extra electric field, accelerated motion after electrons gain energy in electrode space, go to clash into gas with foreign flavor molecule with the speed of 3,000,000 times to 3,000 ten thousand times each second, when the energy of electronics identical with a certain Chemical bond energy of gas with foreign flavor molecule or bigger time, there is inelastic collision, most of kinetic transformation is can in contaminant molecule by electronics, thus caused make it excite, physics, the chemical reaction of the series of complex such as dissociation or ionization, make the group chemical bond fission producing stink, then reach deodorizing object through multistage purification.Another is odorant oxidation Decomposition under the effects such as a large amount of high energy electron, ion, excited state particle, oxygen radical and hydroperoxyl radical is harmless products.
Its main process is expressed by following reaction equation: (AB-contaminant molecule, e-electronics)
Excite: e+AB → AB
*+ e
Neutral dissociation: e+AB → A+B+e
Direct ion: e+AB → AB
++ 2e
Ionization dissociation: e+AB → A+B
++ 2e, A
++ B+2e
Form anion: e+AB → AB
-(electron adsorption)
E+AB → A+B
-(electronics is from attached)
Neutral dissociation and ionization dissociation produce the neutral group of the promising paired electrons of a large amount of band, make plasma have active chemical property, can to odorant oxidation removal, and key reaction is as follows:
H
2S+O
2,O
2-,O
2+→SO
3+H
2O
NH
3+O
2,O
2-,O
2+→NO
X+H
2O
VOCs+O
2,O
2-,O
2+→SO
3+CO
2+H
2O
The low-temperature plasma body deodorizing device of the utility model embodiment not only has plasma, also has a large amount of ozone.Ozone has very strong oxidation susceptibility, and can produce the organic or inorganic material of stink and other smell by fast decoupled very much, the main component of stink is amine R
3n, hydrogen sulfide H
2s, methyl mercaptan CH
3sH etc.Ozone is to its oxidation Decomposition, and product is not or have less smell.
R
3N+O
3→R
3N-O+O
2
H
2S+O
3→S+H
2O+O
2
CH
3SH+O
3→[CH
3-S-S-CH
3]→CH
3-SO
3H+O
2
In sum, the utility model embodiment is by constructing the integrated form stench cleaning system be made up of main reaction tower, air-introduced machine and tail gas absorber, adopt the mode that plasma technology body combines with desulphurization denitration technology, by the structure that double tower three circulates, achieve foul gas efficiently to remove thoroughly, utilize plasma technique odorant to be converted into the small-molecule substance such as sulfide and nitrogen oxide of odorless in main reaction tower, realize deodorization functions; Tail gas absorber then absorbs the small-molecule substance of such atmosphere pollution, and does degree of depth absorption to the large molecule of part difficult degradation, reaches corresponding discharge standard.The integrated form stench cleaning system of the utility model embodiment is applicable to foul gas process, and particularly relate to the foul gas process of high concentration, have odor removal efficient high, operating cost is low, simple to operate, the advantage of non-secondary pollution.
The device of the utility model embodiment all arranges absorption plant before and after plasma reactor, front absorption plant plays the effect of dedusting and pre-absorption odorant soluble in water, the load of plasma reactor can be alleviated, ensure the efficient stable of plasma reaction.Rear absorption plant and degree of depth absorb set are formed in a tail gas absorber, but each own separate circulatory system.The sulfide that rear absorption plant dominant absorption produces after plasma reaction, the atmosphere pollutions such as nitrogen oxide, also alleviate the degree of depth and absorb load, the effective rate of utilization of medicament is improved while elimination secondary pollution, thus reduce the dosage of medicament, reduce operating cost.
One of ordinary skill in the art will appreciate that: accompanying drawing is the schematic diagram of an embodiment, the module in accompanying drawing or flow process might not be that enforcement the utility model is necessary.
One of ordinary skill in the art will appreciate that: the parts in the device in embodiment can describe according to embodiment and be distributed in the device of embodiment, also can carry out respective change and be arranged in the one or more devices being different from the present embodiment.The parts of above-described embodiment can merge into parts, also can split into multiple subassembly further.
Each embodiment in this description all adopts the mode of going forward one by one to describe, between each embodiment identical similar part mutually see, what each embodiment stressed is the difference with other embodiments.Especially, for device or system embodiment, because it is substantially similar to embodiment of the method, so describe fairly simple, relevant part illustrates see the part of embodiment of the method.Apparatus and system embodiment described above is only schematic, the wherein said unit illustrated as separating component or can may not be and physically separates, parts as unit display can be or may not be physical location, namely can be positioned at a place, or also can be distributed on multiple NE.Some or all of module wherein can be selected according to the actual needs to realize the object of the present embodiment scheme.Those of ordinary skill in the art, when not paying creative work, are namely appreciated that and implement.
The above; be only the utility model preferably detailed description of the invention; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; the change that can expect easily or replacement, all should be encompassed within protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of claim.
Claims (10)
1. an integrated form stench cleaning system, it is characterized in that, comprise: main reaction tower (100), air-introduced machine (6) and tail gas absorber (200), one end of described air-introduced machine (6) is connected through the top of piping with described main reaction tower (100), the other end of described air-introduced machine (6) is connected by the bottom of pipeline with described tail gas absorber (200), and foul gas is successively through described main reaction tower (100), air-introduced machine (6) and tail gas absorber (200).
2. integrated form stench cleaning system according to claim 1, it is characterized in that, in described main reaction tower (100), pre-absorption device is set from bottom to top, first demister (4) and low temperature odor purification (5), foul gas is entered in described main reaction tower (100) by the air inlet (1) of described main reaction tower (100) bottom, and successively through described pre-absorption device, low temperature odor purification (5) and the first demister (4).
3. integrated form stench cleaning system according to claim 2, it is characterized in that, between described main reaction tower (100) and tail gas absorber (200), water tank (15) is set, pre-absorption device in described main reaction tower (100) comprises the first packing layer (2), first spray equipment (3) and circulating pump (14), described first demister (4) is arranged between described first spray equipment (3) and described low temperature odor purification (5), in described first packing layer (2) part, the first peep hole (13) is set, described circulating pump (14) is connected with described first spray equipment (3) and described water tank (15), water in described water tank (15) is drawn in described first spray equipment (3).
4. integrated form stench cleaning system according to claim 3, it is characterized in that, absorbing liquid is stored at the bottom of the tower of described main reaction tower (100), one end of described circulating pump (14) connects at the bottom of tower washes receipts liquid, the other end connects described first spray equipment (3), realizes absorbing liquid circulation.
5. the integrated form stench cleaning system according to claim 3 or 4, it is characterized in that, in described tail gas absorber (200), rear absorption plant is set from bottom to top, collecting tank (17), cyclone (9), degree of depth absorption plant and the second demister (12), flue gas enters in described tail gas absorber (200) by the air inlet of described tail gas absorber (200) bottom, and absorption plant after described successively, described collecting tank (17), described cyclone (9), described degree of depth absorption plant and described second demister (12), finally by the top discharge air of described tail gas absorber (200).
6. integrated form stench cleaning system according to claim 5, it is characterized in that, described rear absorption plant comprises the second packing layer (7), the second spray equipment (8) and circulating pump (19), in described second packing layer (7) part, the second peep hole (16) is set, described circulating pump (19) is connected with described second spray equipment (8) and described water tank (15), is drawn in described second spray equipment (8) by the water in described water tank (15).
7. integrated form stench cleaning system according to claim 6, it is characterized in that, arrange in the bottom of described tail gas absorber (200) and wash receipts liquid, one end of described circulating pump (19) connects at the bottom of tower washes receipts liquid, the other end connects described second spray equipment (8), realizes absorbing liquid circulation.
8. integrated form stench cleaning system according to claim 7, it is characterized in that, described degree of depth absorption plant comprises the 3rd packing layer (10), the 3rd spray equipment (11), cyclone (9), chemical tank (20), collecting tank (17) and circulating pump (21), described collecting tank (17) is arranged between described 3rd spray equipment (11) and described cyclone (9), be made up of inner tank wall and baffle plate obliquely, the bottom of described collecting tank (17) is connected with described chemical tank (20) by pipeline.
9. integrated form stench cleaning system according to claim 8, it is characterized in that, one end of described circulating pump (21) connects chemical tank (20), and the other end connects described 3rd spray equipment (11), realizes absorbing liquid circulation.
10. integrated form stench cleaning system according to claim 9, it is characterized in that, described cyclone (9) is arranged between described collecting tank (17) and described degree of depth absorption plant, absorbing liquid flows down along tube wall after described cyclone (9), is collected and flow to described chemical tank (20) by back of pipeline by described collecting tank (17).
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104941409A (en) * | 2015-04-21 | 2015-09-30 | 北京源生恒通环保科技有限公司 | Integrated type stink purification system |
| CN105771569A (en) * | 2016-03-16 | 2016-07-20 | 南京工业大学 | Method for treating methionine production process waste gas |
| CN108554142A (en) * | 2018-04-20 | 2018-09-21 | 浙江大学 | A kind of removing arc tunnel ultrahigh concentration NOxSystem and method |
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2015
- 2015-04-21 CN CN201520243558.2U patent/CN204865478U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104941409A (en) * | 2015-04-21 | 2015-09-30 | 北京源生恒通环保科技有限公司 | Integrated type stink purification system |
| CN105771569A (en) * | 2016-03-16 | 2016-07-20 | 南京工业大学 | Method for treating methionine production process waste gas |
| CN108554142A (en) * | 2018-04-20 | 2018-09-21 | 浙江大学 | A kind of removing arc tunnel ultrahigh concentration NOxSystem and method |
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