CN208295935U - Slurry factory stench processing system - Google Patents

Slurry factory stench processing system Download PDF

Info

Publication number
CN208295935U
CN208295935U CN201820954012.1U CN201820954012U CN208295935U CN 208295935 U CN208295935 U CN 208295935U CN 201820954012 U CN201820954012 U CN 201820954012U CN 208295935 U CN208295935 U CN 208295935U
Authority
CN
China
Prior art keywords
line
foul smell
processing system
pipeline
slurry factory
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201820954012.1U
Other languages
Chinese (zh)
Inventor
郝健
赵会山
张良辉
贾永现
郑高峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mori Hiroshi Asia Pacific (shandong) Pulp And Paper Co
Original Assignee
Mori Hiroshi Asia Pacific (shandong) Pulp And Paper Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mori Hiroshi Asia Pacific (shandong) Pulp And Paper Co filed Critical Mori Hiroshi Asia Pacific (shandong) Pulp And Paper Co
Priority to CN201820954012.1U priority Critical patent/CN208295935U/en
Application granted granted Critical
Publication of CN208295935U publication Critical patent/CN208295935U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Incineration Of Waste (AREA)

Abstract

The utility model discloses a kind of slurry factory stench processing systems, including incinerator and flue gas scrubber, wherein, setting combuster and the integrated burner above combustion chamber, integrated burner are connected to burning line, air feed pipeline and foul smell pipeline in incinerator;Flue gas scrubber includes tower and spray system, the entrance of tower and the outlet of combustion chamber;When in use, fuel first in burning line is lighted a fire after integrated burner sprays, it lights a fire successfully with after flameholding, begin through air feed pipeline and the top-down air feed into combustion chamber of foul smell pipeline and foul smell, foul smell burn in the combustion chamber generation flue gas enter in flue gas scrubber carry out carrying out washing treatment after be discharged;Above-mentioned slurry factory stench processing system can as it is spare replenish slurry factory maintenance down, alkali recovery furnace stop jumping or cancel closedown when; guarantee that stench gas system can be still effectively treated; smell diffusion is reduced to the maximum extent, so that the normal operation for entire slurry line provides safeguard.

Description

Slurry factory stench processing system
Technical field
The utility model relates to slurry factory Odor control technical field, in particular to a kind of slurry factory stench processing system.
Background technique
Modern Pulping Technology mostly uses sulfate pulping, and foul gas can be generated in pulping process, these gases It is unprocessed to be discharged to the smell that will form unique kraft pulp mills in atmosphere.
Currently, the stench that slurry factory foul smell is collected and processing system will successfully can generate in sulfate production process Gas collection simultaneously carries out chemical conversion.All foul smell source streams can be collected in factory and by them controllable by designing perfect system Gas treatment point is transported under temperature and pressure.Since many pollutants for being collected into have combustibility, using burn as The main means of Odor control.In the prior art, using alkali recovery furnace as the primary combustion of foul smell point, with limekiln or coal-fired pot Furnace etc. is as spare.But how to guarantee the foul smell collected when slurry factory maintenance down, alkali recovery furnace stop jumping or cancel closedown still It can be effectively treated, reduce smell diffusion to the maximum extent, become those skilled in the art's technical problem urgently to be resolved.
Utility model content
In view of this, the purpose of this utility model is to provide a kind of slurry factory stench processing system, to starch as spare When factory's maintenance down, alkali recovery furnace stop jumping or cancel closedown, guarantee that the foul smell collected can be still effectively treated, to the maximum extent Reduce smell diffusion.
To achieve the above object, the utility model provides the following technical solutions:
A kind of slurry factory stench processing system, comprising:
Incinerator, the interior setting combuster of the incinerator and the integrated burner above the combustion chamber, The integrated burner is connected to burning line, air feed pipeline and foul smell pipeline;
Flue gas scrubber, including tower and spray system, the outlet of the entrance of the tower and the combustion chamber.
Preferably, the burning line includes in natural gas line, Liquefied petroleum gas pipe, methanol line and diesel oil pipe At least one.
Preferably, the natural gas line or Liquefied petroleum gas pipe include main line and branch line, the integrated burner with The branch line of the natural gas line or the Liquefied petroleum gas pipe is igniter gas supply line, with the natural gas line or the liquid Change the main line of gas pipeline as starting fluid supply line and auxiliary fuel supply line.
Preferably, the air feed pipeline is three-level parallel connection air feed pipeline.
Preferably, the foul smell pipeline includes the highly concentrated foul smell pipe being successively connected to from top to bottom with the integrated burner Line, chip bin foul smell pipeline and low dense foul smell pipeline.
Preferably, flame detecting instrument is provided on the integrated burner.
Preferably, it is additionally provided with below the combustion chamber in the incinerator for being carried out at cooling to combustion product The cold quenching room of reason.
Preferably, the spray system includes detergent circulator and first spray head, and the detergent circulator enters Mouth is connected to the bottom of the tower, is exported and is connected to the spray head being set to inside the tower.
Preferably, the first spray head is provided with multiple, multiple first spray heads in the tower from top to bottom between Every arrangement.
Preferably, second spray head, the outlet of the detergent circulator and second spray are provided in the cold quenching room Head connection.
In order to achieve the above object, slurry factory stench processing system provided by the utility model, including incinerator and flue gas Scrubbing tower, wherein setting combuster and the integrated burner above combustion chamber, integrated burner in incinerator It is connected to burning line, air feed pipeline and foul smell pipeline, integrated burner jet flames and fuel into combustion chamber make Foul smell burns in the combustion chamber;Flue gas scrubber includes tower and spray system, and the entrance of tower and the outlet of combustion chamber connect It is logical;
When in use, the fuel first in burning line is lighted a fire after integrated burner sprays, successfully band burning of lighting a fire After stabilization, air feed pipeline and the top-down air feed into combustion chamber of foul smell pipeline and foul smell are begun through, foul smell is in combustion chamber The flue gas that interior burning generates enters in flue gas scrubber to be discharged after progress carrying out washing treatment;Above-mentioned slurry factory stench processing system can be made For it is spare replenish slurry factory maintenance down, alkali recovery furnace stop jumping or cancel closedown when, guarantee stench gas system effective place still can be obtained Reason reduces smell diffusion to the maximum extent, so that the normal operation for entire slurry line provides safeguard.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of slurry factory stench processing system provided by the embodiment of the utility model.
In figure:
1 is combustion chamber;2 be integrated burner;3 be chip bin foul smell pipeline;4 be highly concentrated foul smell pipeline;5 be natural gas Pipeline;6 be flame detecting instrument;7 be burning torch;8 be methanol line;9 be air feed pipeline;10 be low dense foul smell pipeline;11 be Two spray heads;12 be cold quenching room;13 be detergent circulator;14 be tower;15 be first spray head.
Specific embodiment
The purpose of this utility model is to provide a kind of slurry factory stench processing system, the structures of the slurry factory stench processing system Design can be spare as supplementing in slurry factory maintenance down, alkali recovery furnace stop jumping or cancel closedown, guarantees the foul smell collected still It can be effectively treated, reduce smell diffusion to the maximum extent.
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work Every other embodiment obtained, fall within the protection scope of the utility model.
Referring to Fig. 1, Fig. 1 is the structural schematic diagram of slurry factory stench processing system provided by the embodiment of the utility model.
The utility model embodiment provides a kind of slurry factory stench processing system, including incinerator and flue gas scrubber.
Wherein, incinerator is the main member of Odor control, and combuster 1 is arranged inside and is located at 1 top of combustion chamber Integrated burner 2, integrated burner 2 is connected to burning line, air feed pipeline 9 and foul smell pipeline, Integrated Combustion Device 2 jet flames and fuel into combustion chamber 1, make foul smell burn in combustion chamber 1;Flue gas scrubber include tower 14 and Spray system, the entrance of tower 14 and the outlet of combustion chamber 1;
Compared with prior art, slurry factory stench processing system provided by the utility model, when in use, burning line first Interior fuel is lighted a fire after the ejection of integrated burner 2, light a fire successfully with after flameholding, begin through air feed pipeline 9 with it is smelly Gas pipeline top-down air feed and foul smell into combustion chamber 1, burn in combustion chamber 1 flue gas of generation of foul smell enter flue gas and wash It washs and is discharged after carrying out carrying out washing treatment in tower;Above-mentioned slurry factory stench processing system can as it is spare replenish slurry factory maintenance down, When alkali recovery furnace stop jumping or cancel closedown, guarantee that stench gas system can be still effectively treated, reduce smell diffusion to the maximum extent, To be provided safeguard for the normal operation of entire slurry line.
In the utility model embodiment, slurry factory stench processing system can be carried out at foul smell burning using pluralities of fuel Reason, for example, fuel can for one of natural gas, liquefied gas, methanol and diesel oil or it is a variety of be used cooperatively, be corresponding to it , above-mentioned burning line includes at least one of natural gas line 5, Liquefied petroleum gas pipe, methanol line 8 and diesel oil pipe.
It will be appreciated by persons skilled in the art that methanol is one of the product of slurry factory production, using methanol as fuel, no Foul smell can only be handled, slurry factory discharge can also be reduced, therefore, in the utility model embodiment, above-mentioned slurry factory is smelly The burning line of gas processing system includes at least methanol line 8.
It is well known that gas is easier to burn than liquid, and methanol is liquid under normal temperature state, therefore, if using Methanol is igniter fuel, then the success rate lighted a fire is undesirable, for this purpose, in the utility model embodiment, burning pipeline further includes Natural gas line 5 or Liquefied petroleum gas pipe, natural gas line 5 provides natural gas or Liquefied petroleum gas pipe provides liquefied gas conduct The igniter fuel of integrated burner 2, to improve the success rate of igniting.
Above-mentioned technical proposal is advanced optimized, natural gas line 5 or Liquefied petroleum gas pipe include main line and branch line, integration Burner 2 is using the branch line of natural gas line 5 or Liquefied petroleum gas pipe as igniter gas supply line, with natural gas line 5 or liquefied gas The main line of pipeline is as starting fluid supply line and auxiliary fuel supply line.
Starting fluid supply line refer to after integrated burner 2 is lighted a fire successfully in the case that furnace temperature is high not enough to Integrated burner 2 supplies the pipeline of fuel, and in the utility model embodiment, natural gas, liquefied gas can be used as starting Fuel, it is of course also possible to use other fuel, such as diesel oil.
The source of above-mentioned natural gas, liquefied gas and diesel oil is not particularly limited, and can use commercial goods.
When the temperature of combustion chamber 1 is increased to 800 DEG C~900 DEG C, can be burnt using methanol as fuel, bavin Oil, natural gas, liquefied gas etc. are used as auxiliary fuel, are supplemented in methanol deficiency.
Above-mentioned technical proposal is advanced optimized, in the utility model embodiment, combustion chamber 1 is cylinder, including shell And liner, wherein shell uses composite stainless steel material, and liner uses refractory ceramic fibre material.
Foul smell caused by slurry factory is generally made of highly concentrated foul smell, low dense foul smell and chip bin foul smell, wherein chip bin The concentration of foul smell is identical as low dense foul smell under normal circumstances, but in some special cases, the concentration of chip bin foul smell can be anxious Increase severely and add, more than the least concentration of explosion, therefore, in the utility model embodiment, foul smell pipeline includes highly concentrated foul smell pipeline 4, chip bin foul smell pipeline 3 and low dense foul smell pipeline 10, and above-mentioned three kinds of foul smell pipelines according to concentration size from top to bottom Primary access integrated burner 2, i.e., highly concentrated foul smell pipeline 4, chip bin foul smell pipeline 3 and low dense foul smell pipeline 10 on to Under be successively connected to integrated burner 2, in this way, when highly concentrated foul smell is passed through in integrated burner 2 with integrated burner 2 Burning torch 7 is closest, using the characteristic of its high heating value, can play the role of combustion-supporting, and improve furnace temperature rapidly, and is located at height The low dense foul smell that the low dense foul smell pipeline 10 of dense 4 lower section of foul smell pipeline is passed through can play supplement air, adjust since concentration is lower The effect for saving furnace temperature facilitates the workload for reducing air feed pipeline 9.
And to make various foul smell that can be fully burned, in the utility model embodiment convenient for controlling furnace temperature In, air feed pipeline 9 is three-level parallel connection air feed pipeline 9, i.e. air feed pipeline 9 is made of three air feed tap lines in parallel, and Volume damper can be set on every pipeline, to realize by the aperture for adjusting volume damper to every air feed tap line Volume of air supply control.
Specifically, the level-one air feed tap line A in three-level parallel connection air feed pipeline 9 is located at the center of integrated burner 2 Position is embedded in the cylindrical central sleeve of integrated burner 2, close to methanol line 8 or diesel oil pipe and integrated burner 2 Burning torch 7 provides turbulent flow appropriate;Second level air feed tap line B passes through in the distribution plate entrance in an integrated burner 2 Heart sleeve periphery, provides combustion air for natural gas and highly concentrated foul smell, and collectively form second layer sleeve;Three-level air feed bypass duct Line C is located at second layer sleeve periphery, provides secondary combustion air.
Above-mentioned technical proposal is advanced optimized, deflector, low dense foul smell and chip bin foul smell are additionally provided in combustion chamber 1 Enter combustion chamber 1 from top to bottom in the form of being vortexed deflector, improves efficiency of combustion.
To ensure that incinerator works normally, in the utility model embodiment, flame spy is provided on integrated burner 2 Instrument 6 is surveyed, whether normal is worked by the 6 monitoring integration burner 2 of flame detecting instrument, if the work of integrated burner 2 occurs Abnormal, then flame detecting instrument 6 is alarmed.Specifically, in the utility model embodiment, flame detecting instrument 6 is infrared ray and ultraviolet The double selection types of line.
In the utility model embodiment, the spray system of flue gas scrubber includes detergent circulator 13 and the first spray First 15, the entrance of detergent circulator 13 is connected to the bottom of tower 14, is exported and is connected to the spray head being set to inside tower 14, By above structure, cleaning solution can be recycled, improve the utilization rate of cleaning solution, reduce cost.Specifically, above-mentioned washing The main component of liquid is sodium hydroxide.Sulfur dioxide reflection in sodium hydroxide and flue gas generates sodium sulfite and bisulfite Sodium.
It is understood that flue gas should be led to from the bottom of flue gas scrubber tower 14 to improve flue gas washing effect Enter, flows up flue gas inversely spraying across sodium hydroxide, tower 14 is discharged from top, to avoid the formation of white cigarette, tower 14 Tower top be also equipped with demister arrangements.
Advanced optimize above-mentioned technical proposal, in the utility model embodiment, first spray head 15 be provided with it is multiple, it is multiple The arranged for interval from top to bottom in tower 14 of first spray head 15.
Due to usually containing element sulphur in foul smell and fuel methanol, usually there is sulfur-bearing chemical combination in combustion product Object should for safety make its temperature be maintained at 100 DEG C once in subsequent process of wet desulphurization, but combustion product Temperature is often higher than this numerical value, for this purpose, also setting up in incinerator in the lower section of combustion chamber 1 in the utility model embodiment There is the cold quenching room 12 for carrying out cooling processing to combustion product, which drops combustion product in a manner of heat exchange Temperature processing, the heat of recycling can be used for the production of slurry factory other processes.
Preferably, in the utility model embodiment, second spray head 11, detergent circulator 13 are provided in cold quenching room 12 Outlet be connected to second spray head 11, cooling processing is carried out to flue gas in this way, not only can use cleaning solution, can also be to flue gas It is pre-washed, further increases fume treatment effect.
Specifically, in the utility model embodiment, cold quenching room 12 includes that venturi connects throat and equipped with multiple second The cylindrical body portion of spray head 11.
Each embodiment in this specification is described in a progressive manner, the highlights of each of the examples are with other The difference of embodiment, the same or similar parts in each embodiment may refer to each other.
The foregoing description of the disclosed embodiments can be realized professional and technical personnel in the field or using originally practical new Type.Various modifications to these embodiments will be readily apparent to those skilled in the art, and determine herein The General Principle of justice can be realized in other embodiments without departing from the spirit or scope of the present utility model.Cause This, the present invention will not be limited to the embodiments shown herein, and is to fit to and principles disclosed herein The widest scope consistent with features of novelty.

Claims (10)

1. a kind of slurry factory stench processing system characterized by comprising
Incinerator, the interior setting combuster of the incinerator and the integrated burner above the combustion chamber, it is described Integrated burner is connected to burning line, air feed pipeline and foul smell pipeline;
Flue gas scrubber, including tower and spray system, the outlet of the entrance of the tower and the combustion chamber.
2. slurry factory stench processing system according to claim 1, which is characterized in that the burning line includes natural gas tube At least one of line, Liquefied petroleum gas pipe, methanol line and diesel oil pipe.
3. slurry factory stench processing system according to claim 2, which is characterized in that the natural gas line or liquefaction tracheae Line includes main line and branch line, and the integrated burner is using the branch line of the natural gas line or the Liquefied petroleum gas pipe as point Internal heat supply line, it is using the main line of the natural gas line or the Liquefied petroleum gas pipe as starting fluid supply line and auxiliary Help fuel supply lines.
4. slurry factory stench processing system according to claim 1 to 3, which is characterized in that the air feed pipeline is Three-level parallel connection air feed pipeline.
5. slurry factory stench processing system according to claim 1 to 3, which is characterized in that the foul smell pipeline packet Include the highly concentrated foul smell pipeline, chip bin foul smell pipeline and low dense foul smell being successively connected to from top to bottom with the integrated burner Pipeline.
6. slurry factory stench processing system according to claim 1 to 3, which is characterized in that the Integrated Combustion Flame detecting instrument is provided on device.
7. slurry factory stench processing system according to claim 1 to 3, which is characterized in that in the incinerator The cold quenching room for carrying out cooling processing to combustion product is additionally provided with below the combustion chamber.
8. slurry factory stench processing system according to claim 7, which is characterized in that the spray system includes that cleaning solution follows Ring pump and first spray head, the entrance of the detergent circulator are connected to the bottom of the tower, are exported and are set to and is described Spray head connection inside tower.
9. slurry factory stench processing system according to claim 8, which is characterized in that the first spray head be provided with it is multiple, Multiple first spray heads arranged for interval from top to bottom in the tower.
10. slurry factory stench processing system according to claim 8, which is characterized in that be provided with second in the cold quenching room Spray head, the outlet of the detergent circulator are connected to the second spray head.
CN201820954012.1U 2018-06-20 2018-06-20 Slurry factory stench processing system Active CN208295935U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820954012.1U CN208295935U (en) 2018-06-20 2018-06-20 Slurry factory stench processing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820954012.1U CN208295935U (en) 2018-06-20 2018-06-20 Slurry factory stench processing system

Publications (1)

Publication Number Publication Date
CN208295935U true CN208295935U (en) 2018-12-28

Family

ID=64702207

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820954012.1U Active CN208295935U (en) 2018-06-20 2018-06-20 Slurry factory stench processing system

Country Status (1)

Country Link
CN (1) CN208295935U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111270031A (en) * 2019-04-28 2020-06-12 北京中北欧瑞智工程技术有限公司 Blast furnace diffuses raw coke oven gas purifier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111270031A (en) * 2019-04-28 2020-06-12 北京中北欧瑞智工程技术有限公司 Blast furnace diffuses raw coke oven gas purifier

Similar Documents

Publication Publication Date Title
CN100422434C (en) System for producing energy at a pulp mill
CN104154519B (en) A kind of alcohol-group fuel steam boiler
CN102168857B (en) High-concentration saliferous organic waste liquid incinerator and incineration technique
CN101813320B (en) Built-in integrated smoke exhaust-heat boiler burner for catalysis device
CN2864378Y (en) Multistage multi-room gas boiler for coal gasification
CN103591591B (en) Saponification waste liquid burning and alkali recovery boiler
CN103471109A (en) Incinerator for treating waste gases and waste liquid in methionine production process
CN106215664A (en) Danger waste burning system flue gas combination method of denitration and device
CN208295935U (en) Slurry factory stench processing system
CN102182996A (en) Top spraying type fuel oil and waste gas combined boiler
CN105910115B (en) A kind of incinerator for waste liquid
CN203464291U (en) Burning device for processing waste gas and waste liquid in methionine process production
CN207893756U (en) A kind of flue gas is interior to recycle ultra-low NOx emission gas burner
CN211625237U (en) Burner with high-low pressure, high-low heat value double fuel gas
CN202074532U (en) High concentration salt bearing organic waste liquid incinerator
CN204042838U (en) A kind of alcohol-group fuel steam boiler
CN114110612A (en) Incineration pretreatment process for high-sulfur solid waste
CN107504502A (en) A kind of waste fluid burning plant and technique
CN208750738U (en) A kind of processing system for burning combined steam overheat
CN204042921U (en) Layering is adopted to spray the organic liquid waste burning boiler of waste liquid structure
CN209196867U (en) A kind of external-burning exhaust gas ground flare burner
CN214009238U (en) Odor incineration system for pulp mill
CN102072654A (en) External combustion regenerative heater
CN220149229U (en) Sulfur production combustion furnace of sulfur recovery Claus reaction system capable of burning waste acid
CN209431898U (en) A kind of equipment reducing sulphur emissions

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant