CN204730228U - The smoke processing system that a kind of living beings class solid waste and danger are given up in processing procedure - Google Patents
The smoke processing system that a kind of living beings class solid waste and danger are given up in processing procedure Download PDFInfo
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- CN204730228U CN204730228U CN201520343715.7U CN201520343715U CN204730228U CN 204730228 U CN204730228 U CN 204730228U CN 201520343715 U CN201520343715 U CN 201520343715U CN 204730228 U CN204730228 U CN 204730228U
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Abstract
The utility model discloses the smoke processing system in a kind of living beings class solid waste and the useless processing procedure of danger, SNCR process, chilling depickling process, neutralisation treatment, absorption process, dust removal process and carrying out washing treatment are carried out successively to flue gas, thus effectively reduce the discharge of harmful substances from flue gases, ensure that the flue gas of above-mentioned process can qualified discharge; As preferably, chilling depickling process adopts NaOH solution, and neutralisation treatment adopts NaOH powder, absorbs process and adopts charcoal absorption, the form that dust removal process adopts bag-type dust to be combined with ceramic capillary dedusting, water film dedusting, and the active carbon that will adsorb dioxin traps.
Description
Technical field
The utility model relates to the living beings class resource utilization system technical field being applicable to pyrolysis gasification system, particularly a kind of living beings class solid waste and the smoke processing system given up in processing procedure of endangering.
Background technology
Biomass waste is mankind's discarded objects that production and consumption produces in the process utilizing living beings.Its traditional processing mode comprises landfill and burning, but there are needs takies a large amount of soil, and easily brings the problem of secondary pollution, more especially has the refuse of harmfulness.
Current, the biomass waste of China has the advantages that generation is large, labile organic compound content is high, if effectively can utilize it, not only can decreasing pollution, and also will contribute to alleviating China's energy starved present situation.
At present, the flue gas produced after biomass waste burns directly discharges often, or just through simple process, harmful substance wherein very easily causes air pollution, does not meet the theory of environmental protection instantly.
Utility model content
In view of this, the utility model provides the smoke processing system in a kind of living beings class solid waste and the useless processing procedure of danger, for the living beings class recycling of pyrolysis gasification system, effectively can reduce the discharge of harmful substances from flue gases.
For achieving the above object, the utility model provides following technical scheme:
A smoke processing system in living beings class solid waste and the useless processing procedure of danger, comprise connect successively SNCR tower, quench deacidification tower, neutralizing tower, absorption tower, deduster and scrubbing tower.
Preferably, NaOH solution is adopted to carry out chilling depickling process in described quench deacidification tower.
Preferably, NaOH powder is adopted to carry out neutralisation treatment in described neutralizing tower.
Preferably, caustic soda dry powder gathering-device is provided with in described neutralizing tower, described caustic soda dry powder gathering-device comprises filler recovery device, its entrance is arranged lower than outlet, and be provided with filter mechanism in its path, described filter mechanism offers the micropore that can stop solid matter, the outlet of described filler recovery device is in the entrance on described absorption tower.
Preferably, described filler recovery device is rotary type.
Preferably, active carbon is adopted to carry out absorption process in described absorption tower.
Preferably, described deduster adopts the form that bag-type dust, ceramic capillary dedusting and/or water film dedusting combine.
Preferably, the gas outlet of described quench deacidification tower is communicated in the air inlet of described neutralizing tower bottom, and the gas outlet on described neutralizing tower top is communicated in the air inlet on described absorption tower; The flow-disturbing mechanism for hindering flue gas to rise is provided with in described neutralizing tower.
Preferably, the gas outlet on described neutralizing tower top is communicated in the air inlet of bottom, described absorption tower, and the gas outlet on top, described absorption tower is communicated in the air inlet of described deduster; The flow-disturbing mechanism for hindering flue gas to rise is provided with in described absorption tower.
Preferably, the air-introduced machine be connected between described deduster and described scrubbing tower is also comprised.
As can be seen from above-mentioned technical scheme, the living beings class solid waste that the utility model provides and the smoke processing system that danger is given up in processing procedure, SNCR process, chilling depickling process, neutralisation treatment, absorption process, dust removal process and carrying out washing treatment are carried out successively to flue gas, thus effectively reduce the discharge of harmful substances from flue gases, ensure that the flue gas of above-mentioned process can qualified discharge.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, 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.
The structural representation of the smoke processing system that Fig. 1 provides for the utility model embodiment;
The structural representation of the caustic soda dry powder gathering-device that Fig. 2 provides for the utility model embodiment.
Detailed description of the invention
The utility model discloses the smoke processing system in a kind of living beings class solid waste and the useless processing procedure of danger, for the living beings class recycling of pyrolysis gasification system, effectively can reduce the discharge of harmful substances from flue gases.
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, the structural representation of the smoke processing system that Fig. 1 provides for the utility model embodiment.
The living beings class solid waste that the utility model embodiment provides and the smoke processing system that danger is given up in processing procedure, its core improvement is, comprise connect successively SNCR (SNCR) tower (not shown), quench deacidification tower, neutralizing tower, absorption tower, deduster and scrubbing tower; The flying dust through deduster collection is wherein discharged and focuses on, and the sewage after scrubbing tower wet scrubbing is dealt carefully with through discharging.
As can be seen from above-mentioned technical scheme, the living beings class solid waste that the utility model provides and the smoke processing system that danger is given up in processing procedure, SNCR process, chilling depickling process, neutralisation treatment, absorption process, dust removal process and carrying out washing treatment are carried out successively to flue gas, thus effectively reduce the discharge of harmful substances from flue gases, ensure that the flue gas of above-mentioned process can qualified discharge.
As preferably, ammoniacal liquor or urea in SNCR tower, is adopted to spray in fume high-temperature district as reducing agent, to suppress NO_x formation, the concentration of control NOx.Concrete, the concentration of ammoniacal liquor or urea is 40%, to reach best effect.
Chilling depickling process can be passed through alkali lye (calcium alkali or soda) and realize, i.e. wet method depickling, the liquid of atomization and the moment of smoke contacts produce physical change and chemical reaction, reach the object removing acid and suppression harmful substance generation (as dioxin) in flue gas.As preferably, adopt NaOH solution to carry out chilling depickling process in quench deacidification tower, concentration can be specially 5%, and now water is all evaporated to water vapour.
In the specific embodiment that this programme provides, through the flue-gas temperature of waste heat boiler at 500-550 degree, after over-quenching depickling process, be reduced to 150-200 degree, carry out neutralisation treatment afterwards.As preferably, NaOH powder in neutralizing tower, is adopted to carry out dry method neutralisation treatment.Be specially and utilize nitrogen to be sprayed in neutralizing tower by the NaOH powder (caustic soda) through heating to react with flue gas.Can first utilize grinder to pulverize caustic soda, as preferably, before NaOH powder sprays into, first be warmed up to more than 100.If adopt calcium hydroxide in neutralisation treatment, the product that itself and flue gas obtain is Powdered, is not easy to reclaim, meeting and subsequent technique mixing of materials, is difficult to be separated, causes its consumption larger; And this programme adopts NaOH powder (caustic soda) in neutralisation treatment, the sulfide that itself and flue gas obtain is graininess, and can carry out recycling easily, consumption is very little, thus effectively reduces the cost of fume treatment.
In order to optimize above-mentioned technical scheme further, also comprise in neutralisation treatment: Transformatin and recycling are carried out to the flue gas after NaOH powder dry process, Transformatin refers to filter the sulfide grain in flue gas, and recycling refers to collect sulfide grain and chemical treatment obtains NaOH.
The concrete mode of Transformatin can with reference to shown in the caustic soda dry powder gathering-device in Fig. 2, the entrance of the filler recovery device in it is arranged lower than outlet, be provided with filter mechanism in its path, the micropore that it is offered effectively can stop solid matter (particle).Operationally, flue gas is entered by the entrance of filler recovery device low level, and in the process that within it chamber path rises, granular sulfide cannot pass through filter mechanism, finally leaves from the outlet of a high position, enter follow-up treating apparatus through the flue gas be separated.
In order to optimize above-mentioned technical scheme further, filler recovery device is rotary type, is specially in the present embodiment and rotates around the vertical axis of caustic soda dry powder gathering-device, thus produce centrifugal force, helps the falling of granular sulfide to the collecting mechanism of below.
The living beings class solid waste that the utility model embodiment provides and the smoke processing system that danger is given up in processing procedure, adopt active carbon to carry out absorption process, the dioxin in absorption flue gas and heavy metal in absorption tower.
Neutralisation treatment of the prior art and absorption process are often carried out in same reaction tower, and neutralisation treatment, at low level, absorbs process in a high position, causes the material of two processing procedures to mix, be difficult to separation and recovery, cause the consumption of material larger.In order to address this problem, in scheme, neutralisation treatment and absorption process are carried out in different reaction towers, and namely the layout respectively on neutralizing tower and absorption tower, avoids the mixing of two kinds of reaction masses, is convenient to recycle and reuse, thus effectively cuts operating costs.
As preferably, the form that deduster adopts bag-type dust, ceramic capillary dedusting and/or water film dedusting to combine, will the active carbon trapping of absorption dioxin.
In the specific embodiment that this programme provides, the gas outlet of quench deacidification tower is communicated in the air inlet of neutralizing tower bottom, and the gas outlet on neutralizing tower top is communicated in the air inlet on absorption tower; And the flow-disturbing mechanism be provided with in neutralizing tower for hindering flue gas to rise, flue gas is detained in neutralizing tower, carries out the time of neutralisation treatment with prolong smoke, ensure that neutralization reaction is abundant.
In order to optimize above-mentioned technical scheme further, the gas outlet on neutralizing tower top is communicated in the air inlet of bottom, absorption tower, and the gas outlet on top, absorption tower is communicated in the air inlet of deduster; Be provided with the flow-disturbing mechanism for hindering flue gas to rise in absorption tower, flue gas is detained in absorption tower, carry out with prolong smoke the time absorbing process, ensure fully to absorb the dioxin in flue gas and heavy metal.
As preferably, the structure of the flow-disturbing mechanism in neutralizing tower and absorption tower can be specially: first end is fixedly connected on the inwall of tower, and the second end points to the inside of tower; Further, the height of the second end lower than the height of first end, to play better obstruction flow-disturbing effect to flue gas.
Often containing liquid (as aqueous vapor) in flue gas, produce white cigarette when discharging, the limited height that such flue gas rises, and be unfavorable for diffusion.In the specific embodiment that this programme provides, after scrubbing tower, being also connected with flue gas reheater, for adding heat smoke, by liquid (as aqueous vapor) vaporization wherein, flue gas diffusion can being beneficial to, avoiding affecting surrounding enviroment.
The living beings class solid waste that the utility model embodiment provides and the smoke processing system that danger is given up in processing procedure, also comprise the air-introduced machine be connected between deduster and scrubbing tower.
Flue gas through repeatedly washing out from scrubbing tower is discharged through chimney, in order to optimize above-mentioned technical scheme further, chimney arranges smoke on-line monitoring system, the exhaust gas constituents that can discharge in air at Real-Time Monitoring, when the index of harmful substance transfinites, send warning, with timely correcting process system; Or directly feed back to the functional realiey module of each treatment process, such as increase the consumption of NaOH solution in quench deacidification tower, the consumption of NaOH powder in neutralizing tower, the consumption of active carbon in absorption tower, improve the dust collection capacity of deduster, increase the washing times in scrubbing tower.
The basic technology of this programme: SNCR+ quench tower+dry method+active carbon injection+sack cleaner+wet scrubber tower+flue gas reheater.Certainly, according to ecological requirements, smoke processing system is not quite similar, and can carry out suitable adjustment according to actual conditions to the concrete system in above steps.
In sum, the living beings class solid waste that the utility model embodiment provides and the smoke processing system that danger is given up in processing procedure, SNCR process, chilling depickling process, neutralisation treatment, absorption process, dust removal process and carrying out washing treatment are carried out successively to flue gas, thus effectively reduce the discharge of harmful substances from flue gases, ensure that the flue gas of above-mentioned process can qualified discharge; As preferably, chilling depickling process adopts NaOH solution, and neutralisation treatment adopts NaOH powder, absorbs process and adopts charcoal absorption, the form that dust removal process adopts bag-type dust to be combined with ceramic capillary dedusting, water film dedusting, and the active carbon that will adsorb dioxin traps.
In this description, each embodiment adopts the mode of going forward one by one to describe, and what each embodiment stressed is the difference with other embodiments, between each embodiment identical similar portion mutually see.
To the above-mentioned explanation of the disclosed embodiments, professional and technical personnel in the field are realized or uses the utility model.To be apparent for those skilled in the art to the multiple amendment of these embodiments, General Principle as defined herein when not departing from spirit or scope of the present utility model, can realize in other embodiments.Therefore, the utility model can not be restricted to these embodiments shown in this article, but will meet the widest scope consistent with principle disclosed herein and features of novelty.
Claims (10)
1. the smoke processing system in living beings class solid waste and the useless processing procedure of danger, is characterized in that, comprise connect successively SNCR tower, quench deacidification tower, neutralizing tower, absorption tower, deduster and scrubbing tower.
2. living beings class solid waste according to claim 1 and the smoke processing system given up in processing procedure of endangering, is characterized in that, adopt NaOH solution to carry out chilling depickling process in described quench deacidification tower.
3. living beings class solid waste according to claim 2 and the smoke processing system given up in processing procedure of endangering, is characterized in that, adopt NaOH powder to carry out neutralisation treatment in described neutralizing tower.
4. living beings class solid waste according to claim 3 and the smoke processing system given up in processing procedure of endangering, it is characterized in that, caustic soda dry powder gathering-device is provided with in described neutralizing tower, described caustic soda dry powder gathering-device comprises filler recovery device, its entrance is arranged lower than outlet, and being provided with filter mechanism in its path, described filter mechanism offers the micropore that can stop solid matter, the outlet of described filler recovery device is in the entrance on described absorption tower.
5. living beings class solid waste according to claim 4 and the smoke processing system given up in processing procedure of endangering, it is characterized in that, described filler recovery device is rotary type.
6. living beings class solid waste according to claim 5 and the smoke processing system given up in processing procedure of endangering, is characterized in that, adopts active carbon to carry out absorption process in described absorption tower.
7. living beings class solid waste according to claim 6 and the smoke processing system given up in processing procedure of endangering, is characterized in that, the form that described deduster adopts bag-type dust, ceramic capillary dedusting and/or water film dedusting to combine.
8. the smoke processing system that the living beings class solid waste according to claim 1-7 any one and danger are given up in processing procedure, it is characterized in that, the gas outlet of described quench deacidification tower is communicated in the air inlet of described neutralizing tower bottom, and the gas outlet on described neutralizing tower top is communicated in the air inlet on described absorption tower; The flow-disturbing mechanism for hindering flue gas to rise is provided with in described neutralizing tower.
9. living beings class solid waste according to claim 8 and the smoke processing system given up in processing procedure of endangering, it is characterized in that, the gas outlet on described neutralizing tower top is communicated in the air inlet of bottom, described absorption tower, and the gas outlet on top, described absorption tower is communicated in the air inlet of described deduster; The flow-disturbing mechanism for hindering flue gas to rise is provided with in described absorption tower.
10. living beings class solid waste according to claim 9 and the smoke processing system given up in processing procedure of endangering, is characterized in that, also comprise the air-introduced machine be connected between described deduster and described scrubbing tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520343715.7U CN204730228U (en) | 2015-05-25 | 2015-05-25 | The smoke processing system that a kind of living beings class solid waste and danger are given up in processing procedure |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520343715.7U CN204730228U (en) | 2015-05-25 | 2015-05-25 | The smoke processing system that a kind of living beings class solid waste and danger are given up in processing procedure |
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| CN204730228U true CN204730228U (en) | 2015-10-28 |
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| CN201520343715.7U Withdrawn - After Issue CN204730228U (en) | 2015-05-25 | 2015-05-25 | The smoke processing system that a kind of living beings class solid waste and danger are given up in processing procedure |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104819479A (en) * | 2015-05-25 | 2015-08-05 | 山东百川同创能源有限公司 | Biomass solid waste and hazardous waste treatment process flue gas treatment system |
-
2015
- 2015-05-25 CN CN201520343715.7U patent/CN204730228U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104819479A (en) * | 2015-05-25 | 2015-08-05 | 山东百川同创能源有限公司 | Biomass solid waste and hazardous waste treatment process flue gas treatment system |
| CN104819479B (en) * | 2015-05-25 | 2018-01-09 | 山东百川同创能源有限公司 | A kind of smoke processing system in biomass class solid waste and dangerous waste processing procedure |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20151028 Effective date of abandoning: 20180109 |
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| AV01 | Patent right actively abandoned |