CN107987563A - A kind of device and its production technology using tar slag production carbon black - Google Patents
A kind of device and its production technology using tar slag production carbon black Download PDFInfo
- Publication number
- CN107987563A CN107987563A CN201810082166.0A CN201810082166A CN107987563A CN 107987563 A CN107987563 A CN 107987563A CN 201810082166 A CN201810082166 A CN 201810082166A CN 107987563 A CN107987563 A CN 107987563A
- Authority
- CN
- China
- Prior art keywords
- carbon black
- connects
- cyclone separator
- pipeline
- tar slag
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/44—Carbon
- C09C1/48—Carbon black
- C09C1/50—Furnace black ; Preparation thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of device and its production technology using tar slag production carbon black, including heating tank, the heating tank connects reacting furnace by screw conveyor, the reative cell connects water tank by water pipe, the gas outlet of the reative cell connects circulating water pipe by pipeline, the outlet of the circulating water pipe connects main cyclone separator, the bag hose connects scummer by conveyance conduit, the scummer connects micropulverizer by pipeline, the micropulverizer connects the feed inlet for collecting cyclone separator by pipeline, the gas outlet for collecting cyclone separator connects the feed inlet of bag hose by pipeline, the slag-drip opening connection powdered carbon black basin for collecting cyclone separator, the powdered carbon black basin connects packing machine by feed conveyor.The present invention produces carbon black and carburant by using hazardous waste tar slag, solves tar slag environmental pollution problem, circular economy, waste utilization.
Description
Technical field
The invention belongs to tar slag production carbon black field, and more specifically, more particularly to one kind utilizes tar slag production charcoal
Black device.Meanwhile the invention further relates to a kind of production technology using tar slag production carbon black.
Background technology
As China's reform and opening-up deepens continuously, the development that domestic industrial enterprise also advances by leaps and bounds.Last decade, with me
State's national economy and highway develop rapidly, the also high speed development of the auto industry as one of China's pillar industry, so that
The fast development of tire industry is driven.Automobile tire yield and tire consumption increase sharply.Carbon black is as rubber
Reinforcing agent, demand is consequently increased, and carbon black industry is a kind of chemical industry of high energy consumption, these raw materials also can serve as
The raw material of industry, itself be also the energy, therefore production of carbon black it is energy-saving be it is very promising, it is energy saving also suitable to carbon black industry
It is important.
The processing of the existing factory focus dregs of fat is also very not in place, and arbitrarily discharge, easily pollutes environment, and tar slag can also be into
Row reprocessing, is processed into carbon black, therefore the present invention provides a kind of device and its production work using tar slag production carbon black
Skill
The content of the invention
It is an object of the invention to provide a kind of device and its production technology using tar slag production carbon black, with solution
State the problem of being proposed in background technology.
To achieve the above object, the present invention provides following technical solution:
A kind of device using tar slag production carbon black, including heating tank, the heating tank are connected by screw conveyor
Reacting furnace, the upper end of the reacting furnace connect air-introduced machine by pipeline, and the reacting furnace is internally provided with agitating device, described anti-
Stove is answered also to connect water tank by water pipe by pipeline coupled reaction room, the reative cell, the gas outlet of the reative cell passes through pipe
Road connects circulating water pipe, and the outlet of the circulating water pipe connects main cyclone separator, the main cyclone separator
Upper end connects digester, and the digester connects tail gas furnace, the lower end connection bag hose of the main cyclone separator, the bag filter
Device connects scummer by conveyance conduit, and the scummer connects micropulverizer by pipeline, and the micropulverizer passes through
The feed inlet of cyclone separator is collected in pipeline connection, and the gas outlet for collecting cyclone separator connects bag hose by pipeline
Feed inlet, the slag-drip opening connection powdered carbon black basin for collecting cyclone separator, the powdered carbon black basin are defeated by being fed
Device is sent to connect packing machine.
Preferably, the powdered carbon black basin is equipped with blender, for stirring the compactness of increase powdered carbon black.
A kind of production technology using tar slag production carbon black, includes the following steps:Tar slag and carbolineum are mixed, mixing
Ratio is 2:1, mixing is added in heating tank, and is heated to 80 DEG C, and reacting furnace is sent into by screw conveyor, in 1050 DEG C of temperature
In the case of, the mixed rapid gasification, and combustion of the dregs of fat, controls air inducing fan delivery, temperature sets 1050 DEG C, temperature liter by PC
High air-introduced machine revolution declines, and temperature declines the rise of air-introduced machine revolution, and gas enters reative cell, and temperature control exists after going out reative cell
1050-1100 DEG C, drip and crack rapidly and generate carbon black, drip and also cool down carbon black smoke, carbon black smoke is cooled to 700-900
DEG C enter circulating water pipe, when the temperature of carbon black smoke is 120 DEG C -200 DEG C, received by main cyclone separator and main bag hose
Collection, gas recovery pass through digester desulfurization, send tail gas furnace second-time burning through exhaust fan, the carbon black that main bag hose is collected enters defeated
Send pipeline, enter micropulverizer through scummer, by conveying fan send to collect cyclone separator, the carbon black tail gas isolated by
Reflux wind turbine returns to main bag hose, collects the carbon black to get off and enters powdered carbon black basin, after powdered carbon black blender density
Into feed conveyor, it is sent into packing machine and is packed.
Preferably, in order to react mixing dregs of fat homogeneous gasification, paddle controls mixing speed, temperature by PC in reacting furnace
Stirring is accelerated in degree rise, and temperature reduces mixing speed, so as to reach the homogeneous gasification reaction of the mixing dregs of fat.
Preferably, the dust produced in packaging process, is sent into reprocessing bag hose through reprocessing wind turbine, finally by again
Reason bag hose airtight valve enters blast system, is recycled, the gas discharge after separating off carbon black.
Preferably, remainder be carburant after reacting furnace reaction, and discharge is cut down from bottom top of rising, and discharge is whole to be closed,
Cool down 80 DEG C through circulating water leg, be sent into reserve pool.
Compared with prior art, the beneficial effects of the invention are as follows:The present invention produces charcoal by using hazardous waste tar slag
Black and carburant, solves tar slag environmental pollution problem, circular economy, waste utilization.
Brief description of the drawings
Fig. 1 is the structure diagram of the present invention.
In figure:1 heating tank, 2 screw conveyors, 3 reacting furnaces, 4 agitating devices, 5 air-introduced machines, 6 reative cells, 7 water tanks, 8 are followed
Ring water composite cooling pipe, 9 main cyclone separators, 10 digesters, 11 tail gas furnaces, 12 bag hoses, 13 scummers, 14 micropulverizers, 15
Cyclone separator, 18 blenders are collected in powdered carbon black basin, 16 packing machines, 17.
Embodiment
In order to make the purpose , technical scheme and advantage of the present invention be clearer, below in conjunction with specific embodiment, to this
Invention is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, not
For limiting the present invention.
A kind of device using tar slag production carbon black, including heating tank 1, the heating tank 1 are connected by screw conveyor 2
Logical reacting furnace 3, the upper end of the reacting furnace 3 connect air-introduced machine 5 by pipeline, and the reacting furnace 3 is internally provided with agitating device
4, the reacting furnace 3 also connects water tank 7 by pipeline coupled reaction room 6, the reative cell 6 by water pipe, the reative cell 6
Gas outlet connects circulating water pipe 8 by pipeline, and the outlet of the circulating water pipe 8 connects main cyclone separator 9, described
The upper end connection digester 10 of main cyclone separator 9, the digester 10 connect tail gas furnace 11, the main cyclone separator 9
Lower end connects bag hose 12, and the bag hose 12 connects scummer 13 by conveyance conduit, and the scummer 13 is connected by pipeline
Micropulverizer 14 is connect, the micropulverizer 14 connects the feed inlet for collecting cyclone separator 17, the collection by pipeline
The gas outlet of cyclone separator 17 connects the feed inlet of bag hose 12, the slag-drip opening for collecting cyclone separator 17 by pipeline
Powdered carbon black basin 15 is connected, the powdered carbon black basin 15 connects packing machine 16 by feed conveyor.
Specifically, the powdered carbon black basin 15 is equipped with blender 18, for stirring the compactness of increase powdered carbon black.
Present invention also offers a kind of production technology using tar slag production carbon black, include the following steps:By tar slag
Mixed with carbolineum, mixed proportion 2:1, mixing is added in heating tank, and is heated to 80 DEG C, is sent into and reacted by screw conveyor
Stove, in the case of 1050 DEG C of temperature, the mixed rapid gasification, and combustion of the dregs of fat, controls air inducing fan delivery, temperature is set by PC
1050 DEG C fixed, temperature rise air-introduced machine revolution declines, and temperature declines the rise of air-introduced machine revolution, and gas enters reative cell, goes out reaction
Temperature control drips at 1050-1100 DEG C and cracks rapidly and generate carbon black, drip and also cool down carbon black smoke behind room, carbon black smoke
It is cooled to 700-900 DEG C and enters circulating water pipe, when the temperature of carbon black smoke is 120 DEG C -200 DEG C, by main cyclonic separation
Device and main bag hose are collected, and gas recovery passes through digester desulfurization, send tail gas furnace second-time burning through exhaust fan, main bag hose is received
The carbon black of collection enters conveyance conduit, enters micropulverizer through scummer, is sent to cyclone separator is collected, separated by conveying fan
The carbon black tail gas gone out returns to main bag hose by reflux wind turbine, collects the carbon black to get off and enters powdered carbon black basin, through powdery carbon
Enter feed conveyor after black blender density, be sent into packing machine and packed.
Specifically, in order to react mixing dregs of fat homogeneous gasification, paddle controls mixing speed, temperature by PC in reacting furnace
Stirring is accelerated in degree rise, and temperature reduces mixing speed, so as to reach the homogeneous gasification reaction of the mixing dregs of fat.
Specifically, the dust produced in packaging process, is sent into reprocessing bag hose through reprocessing wind turbine, finally by again
Reason bag hose airtight valve enters blast system, is recycled, the gas discharge after separating off carbon black.
Specifically, remainder be carburant after reacting furnace reaction, discharge is cut down from bottom top of rising, discharge is whole to be closed,
Cool down 80 DEG C through circulating water leg, be sent into reserve pool.
The foregoing is only a preferred embodiment of the present invention, but protection scope of the present invention be not limited thereto,
Any one skilled in the art the invention discloses technical scope in, technique according to the invention scheme and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (6)
1. a kind of device using tar slag production carbon black, including heating tank (1), it is characterised in that:The heating tank (1) passes through
Screw conveyor (2) connection reacting furnace (3), the upper end of the reacting furnace (3) connect air-introduced machine (5), the reaction by pipeline
Stove (3) is internally provided with agitating device (4), and the reacting furnace (3) also passes through pipeline coupled reaction room (6), the reative cell (6)
Water tank (7) is connected by water pipe, the gas outlet of the reative cell (6) connects circulating water pipe (8), the circulation by pipeline
The outlet of water composite cooling pipe (8) connects main cyclone separator (9), and the upper end of the main cyclone separator (9) connects digester (10),
Digester (10) the connection tail gas furnace (11), the lower end connection bag hose (12) of the main cyclone separator (9), the bag filter
Device (12) connects scummer (13) by conveyance conduit, and the scummer (13) connects micropulverizer (14), institute by pipeline
State micropulverizer (14) and the feed inlet for collecting cyclone separator (17), the collection cyclone separator (17) are connected by pipeline
Gas outlet pass through pipeline connect bag hose (12) feed inlet, it is described collect cyclone separator (17) slag-drip opening connection powdery
Carbon black basin (15), the powdered carbon black basin (15) connect packing machine (16) by feed conveyor.
A kind of 2. device using tar slag production carbon black according to claim 1, it is characterised in that:The powdered carbon black
Basin (15) is equipped with blender (18), for stirring the compactness of increase powdered carbon black.
3. a kind of production technology using tar slag production carbon black according to claim 1, it is characterised in that including as follows
Step:Tar slag and carbolineum are mixed, mixed proportion 2:1, mixing is added in heating tank, and is heated to 80 DEG C, by spiral
Conveyer is sent into reacting furnace, and in the case of 1050 DEG C of temperature, the mixed rapid gasification, and combustion of the dregs of fat, air inducing is controlled by PC
Fan delivery, temperature set 1050 DEG C, and temperature rise air-introduced machine revolution declines, and temperature declines the rise of air-introduced machine revolution, and gas enters
Reative cell, temperature control drips at 1050-1100 DEG C and cracks rapidly and generate carbon black, drip and also cool down carbon black after going out reative cell
Flue gas, carbon black smoke is cooled to 700-900 DEG C and enters circulating water pipe, when the temperature of carbon black smoke is 120 DEG C -200 DEG C,
Collected by main cyclone separator and main bag hose, gas recovery passes through digester desulfurization, send tail gas furnace secondary combustion through exhaust fan
Burn, the carbon black that main bag hose is collected enters conveyance conduit, enters micropulverizer through scummer, is sent to collection and revolved by conveying fan
Wind separator, the carbon black tail gas isolated return to main bag hose by reflux wind turbine, collect the carbon black to get off and enter powdered carbon black
Basin, enters feed conveyor after powdered carbon black blender density, is sent into packing machine and is packed.
A kind of 4. production technology using tar slag production carbon black according to claim 3, it is characterised in that:In order to make to mix
The reaction of dregs of fat homogeneous gasification is closed, paddle controls mixing speed by PC in reacting furnace, and stirring is accelerated in temperature rise, and temperature reduces
Mixing speed is reduced, so as to reach the homogeneous gasification reaction of the mixing dregs of fat.
A kind of 5. production technology using tar slag production carbon black according to claim 3, it is characterised in that:Packaging process
The dust of middle generation, is sent into reprocessing bag hose through reprocessing wind turbine, is finally sent by reprocessing bag hose airtight valve into inlet air
System, is recycled, the gas discharge after separating off carbon black.
A kind of 6. production technology using tar slag production carbon black according to claim 3, it is characterised in that:Reacting furnace is anti-
Should after remainder be carburant, cut down discharge from bottom top of rising, discharge whole closing, through circulating 80 DEG C of water leg cooling, send
Enter reserve pool.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810082166.0A CN107987563A (en) | 2018-01-29 | 2018-01-29 | A kind of device and its production technology using tar slag production carbon black |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810082166.0A CN107987563A (en) | 2018-01-29 | 2018-01-29 | A kind of device and its production technology using tar slag production carbon black |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107987563A true CN107987563A (en) | 2018-05-04 |
Family
ID=62040334
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810082166.0A Pending CN107987563A (en) | 2018-01-29 | 2018-01-29 | A kind of device and its production technology using tar slag production carbon black |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107987563A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114032115A (en) * | 2021-02-03 | 2022-02-11 | 海通久卓环保科技有限公司 | Resource recovery method of waste coal tar |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202148275U (en) * | 2011-06-24 | 2012-02-22 | 龙星化工股份有限公司 | Energy conservation device for improving carbon black productivity |
CN104130599A (en) * | 2014-08-06 | 2014-11-05 | 新疆鑫凯高色素特种炭黑有限公司 | High-pigment carbon black furnace-process production device |
CN105086526A (en) * | 2014-05-09 | 2015-11-25 | 苏毅 | Method for producing spray carbon black by using waste oil residue |
CN206207422U (en) * | 2016-10-12 | 2017-05-31 | 深圳业高环保科技有限公司 | Heat scission reaction stove |
CN106947299A (en) * | 2017-05-03 | 2017-07-14 | 四川博蓝科新材料有限公司 | A kind of impurity content low colour carbon black production system and its production technology |
CN208022940U (en) * | 2018-01-29 | 2018-10-30 | 刁英健 | A kind of device producing carbon black using tar slag |
-
2018
- 2018-01-29 CN CN201810082166.0A patent/CN107987563A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202148275U (en) * | 2011-06-24 | 2012-02-22 | 龙星化工股份有限公司 | Energy conservation device for improving carbon black productivity |
CN105086526A (en) * | 2014-05-09 | 2015-11-25 | 苏毅 | Method for producing spray carbon black by using waste oil residue |
CN104130599A (en) * | 2014-08-06 | 2014-11-05 | 新疆鑫凯高色素特种炭黑有限公司 | High-pigment carbon black furnace-process production device |
CN206207422U (en) * | 2016-10-12 | 2017-05-31 | 深圳业高环保科技有限公司 | Heat scission reaction stove |
CN106947299A (en) * | 2017-05-03 | 2017-07-14 | 四川博蓝科新材料有限公司 | A kind of impurity content low colour carbon black production system and its production technology |
CN208022940U (en) * | 2018-01-29 | 2018-10-30 | 刁英健 | A kind of device producing carbon black using tar slag |
Non-Patent Citations (1)
Title |
---|
黄敬彬: "我国炭黑工业环境工程进展", 《橡胶工业》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114032115A (en) * | 2021-02-03 | 2022-02-11 | 海通久卓环保科技有限公司 | Resource recovery method of waste coal tar |
CN114032115B (en) * | 2021-02-03 | 2024-01-16 | 臧正军 | Recycling recovery method of waste coal tar |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101544781B (en) | Method for treating waste tire | |
CN105238432B (en) | Method and device for preparing high-quality bio-oil and white carbon black through self-heating acid pickling-pyrolysis-combustion integration | |
CN101307151B (en) | Apparatus for treating waste and old tyres | |
CN105753344B (en) | By the device and method that garbage flying ash disposition is cement raw material | |
CN103265964B (en) | Device for promoting reaction by direct contact between blast furnace slag particles and biomass particles | |
CN107011930A (en) | A kind of organic garbage treatment system | |
CN102277463B (en) | Reduction furnace and device for producing direct reduced iron | |
CN208776332U (en) | The production technology device of vanadic anhydride | |
CN209815990U (en) | Dry acetylene sludge acetylene gas and silicon iron recycling device | |
CN107987563A (en) | A kind of device and its production technology using tar slag production carbon black | |
CN109852428A (en) | Biomass feeding apparatus | |
CN202201915U (en) | Reduction furnace and directly reduced iron production device | |
CN101307152A (en) | Apparatus for treating waste and old tyres | |
CN105731840A (en) | Device and method for treating garbage fly ash into cement raw material | |
CN110180863A (en) | A kind of method and apparatus of kitchen garbage Quick Pretreatment | |
CN208022940U (en) | A kind of device producing carbon black using tar slag | |
CN201620039U (en) | Heating system of production process of potassium manganate | |
CN208332308U (en) | Coal-fired sludge coupled electricity-generation system | |
CN206751729U (en) | A kind of organic garbage treatment system | |
CN210131907U (en) | Industrial organic solid waste resource recovery processing device | |
WO2020108432A1 (en) | Vortex machine | |
CN208087436U (en) | A kind of device producing solid fuel using sludge | |
CN206751728U (en) | A kind of safe charging device of organic waste | |
CN207231245U (en) | Fluidized bed furnace cooling collection slag system | |
CN110822434A (en) | Pretreatment system for energy treatment of household garbage |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination |