CN1696210A - Method for preparing acetylene black from waste plastics, tire - Google Patents
Method for preparing acetylene black from waste plastics, tire Download PDFInfo
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- CN1696210A CN1696210A CN 200510012531 CN200510012531A CN1696210A CN 1696210 A CN1696210 A CN 1696210A CN 200510012531 CN200510012531 CN 200510012531 CN 200510012531 A CN200510012531 A CN 200510012531A CN 1696210 A CN1696210 A CN 1696210A
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- damaged tire
- plastic waste
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Abstract
A process for preparing the acetylene carbon black from used and rejected plastics and tyre includes thermodecomposing at 400-600 deg.C, thermodecomposing again in the optimally designed reactor with DC arc plasma generator, and collecting the product by cyclone separator.
Description
One, technical field
The present invention utilizes plastic waste, damaged tire to prepare the method for Shawinigan black and the category that technology belongs to chemical production technical field.
Two, technical background
Plastic waste, damaged tire are the environmentally harmful wastes of a class of following the human modern life to produce.Because human lives and social civilization are more and more serious to the degree of dependence of plastics, as disposable plastic bag, agricultural mulching, disposable transfusion device, various casing, medical needle tubing etc., thereby the quantity of demand is in quick increase.Yet in a single day these materials become waste and enter environment and can cause " white pollution ", and entering soil can influence crop yield, and revealing to put in the external world to influence environmental beauty.If the waste plastic after medical such as also can diseases inducedly propagate at problem; Damaged tire is the another kind of waste of modern civilization life.The swift and violent increase of various Motor vehicles causes the rapid rising of damaged tire quantity, thereby environment is caused having a strong impact on of what is called " black pollution ".This two class " white " and " black " waste are carried out harmlessness disposing and can recycling be the human very urgent problem of feeling in the recent period.The fuel that pyrolysis liquefaction produced of plastic waste, damaged tire is said to a certain extent at present, can promote its utility value, but be to be solved, thereby only liquid do not utilized institute's potential useful matter in the liquefaction process is farthest developed by simple combustion system because of directly still having many problems to have as the fuel of Motor vehicles.Therefore, understand in this sense, directly use as conventional fuel its potential value is not made full use of, belong to extensive style and utilize mode.The present invention is based on this situation, develop two-stage method technology and handle, these refuses can be changed into a kind of important substance---the Shawinigan black of chemical field widespread demand through special device.
At present the operational path of Shawinigan black be earlier with coal by being transformed into carbide of calcium with lime calcining, hydrolysis becomes acetylene then, carries out pyrolysis again.Its production process route comparative maturity, but since environmental pollution is serious and coal resource be difficult to regeneration, can be exhausted, seek alternative materials and new production route and seem very necessary.The present invention is to be raw material with plastic waste, damaged tire, at first obtains higher liquid or the gas of productive rate by conventional fast pyrogenation, then the product reactor through optimization design under plasma condition that obtains is carried out pyrolysis once more, can obtain Shawinigan black.
Three, summary of the invention:
The present invention is difficult to digest, be difficult to a kind of method and technology that promotes its utility value that the efficient situation of utilizing is researched and developed in view of a large amount of waste or used plastics, the damaged tire that produce in the environment.Can obtain carbon dust, and the widely used Shawinigan black in fields such as manufacturing of electronic component by this technology and technology in battery, high-carbon black pigment, printing, duplicating and Laser Printing.Advantage is to greatest extent these refuses to have been carried out recycling; solved in the protection environmental process stubborn problem has been compared in these waste treatment; overcome the limited coal resource that causes by coal system Shawinigan black and reduced problem, and obtained the high value-added product Shawinigan black.
The present invention utilizes plastic waste, damaged tire prepares the method for Shawinigan black, it is characterized in that it being with various waste or used plastics, damaged tire is a raw material, adopt the two-stage method processing treatment, its technological process is: with various waste or used plastics, damaged tire, in temperature is 400-600 ℃, rare gas element is to send into fluidized-bed reactor under the condition of carrier gas, carry out first section fast pyrogenation, gas-phase product in reactor the residence time less than 0.6 minute, then the gas-phase product that pyrolysis is obtained is directly sent into the direct current-arc plasma producer by carrier gas, second section graphiote reactor through optimization design carries out pyrolysis again, the solid material that the collection pyrolysis obtains is a Shawinigan black, its processing parameter is: working current is 110~190A, and voltage is 240~340V, and the flow of argon gas is 0.5~2m
3/ h, main hydrogen flow is 0.5~2.0m
3/ h, secondary hydrogen flow is 0.2~2.0m
3/ h, input speed is 0.6~4kg/h, and reactor inside diameter is 40~70mm, and length is 1500~1800mm.
Above-mentioned a kind of method of utilizing plastic waste, damaged tire to prepare Shawinigan black, it is characterized in that described raw material is the mixture of damaged tire and plastic waste or the single thing of damaged tire or plastic waste, the gas-phase product that described pyrolysis obtains also can put together after cooling becomes liquid collecting and carry out second section pyrolysis again.
Above-mentioned a kind of method of utilizing plastic waste, damaged tire to prepare Shawinigan black is characterized in that described damaged tire and plastic waste size range are greater than 40 orders or less than 0.44mm.
The advantage that the present invention utilizes plastic waste, damaged tire to prepare the method for Shawinigan black is: the generation and the decomposition of acetylene are carried out synchronously; shortened traditional operational path; technical scheme is advanced unique; raw material is a large amount of damaged tire, plastic waste waste; the source is abundant; acquisition cost is cheap, belong to the project that field of environment protection is encouraged and supported, thereby this technology has wide market application prospect.
Embodiment
With the internal diameter is 50mm, highly is 1200mm, and the bed material is an example for the fluidized-bed of quartz sand.
Embodiment 1.
Fluidized-bed is heated to 500 ℃ with the temperature rise rate of 30K/min, and feeding flow is the nitrogen of 3.0L/min, then damaged tire is sent into fluidized-bed with 1.8 kilograms speed per hour, and its pyrolysis product is directly sent into plasma generator.Its processing parameter is: working current is 140A, and voltage is 305V, and the flow of argon gas is 2.0m
3/ h, main hydrogen flow is 0.9m
3/ h, secondary hydrogen flow is 0.2m
3/ h; Reactor inside diameter is 45mm, and length is 1500mm, can obtain the product Shawinigan black by cyclone separator.
Embodiment 2.
Fluidized-bed is heated to 550 ℃ with the temperature rise rate of 30K/min, feeding flow is the nitrogen of 3.0L/min, then with damaged tire and plastic waste with the mixed material of 2: 1 mode, with per hour 1.8 kilograms speed charging, the pyrolysis product cooling gets liquid (1); Mix with same speed charging in 1: 2 mode with plastic waste by damaged tire, pyrolysis product through cool off liquid (2).Liquid (1) and (2) are merged the back send into second section anti-device of giving birth to 1.8 kilograms input speed per hour, promptly plasma is instead given birth to device, and the processing parameter of its producer is: working current is 140A, and voltage is 310V, and the flow of argon gas is 2.0m
3/ h, main hydrogen flow is 0.6m
3/ h, secondary hydrogen flow is 0.2m
3/ h; Reactor inside diameter is 50mm, and length is 1600mm, separates to obtain Shawinigan black by cyclone separator.
Embodiment 3.
Fluidized-bed is heated to 600 ℃ with the temperature rise rate of 30K/min, and feeding flow is the nitrogen of 3.0L/min, then plastic waste is sent into fluidized-bed with 1.8 kilograms speed per hour, and its pyrolysis product is through the cold liquid that obtains.Liquid is sent into plasma generator with the feeding speed of 2.5kg/h, and the processing parameter of its producer is: working current is 160A, and voltage is 320V, and argon flow amount is 1.5m
3/ h, main hydrogen flow is 0.8m
3/ h, secondary hydrogen flow is 0.3m
3/ h; Reactor inside diameter is 55mm, and length is 1550mm, separates to obtain Shawinigan black by cyclone separator.
Embodiment 4.
Fluidized-bed is heated to 450 ℃ with the temperature rise rate of 30K/min, feeding flow is the nitrogen of 3.0L/min, then with damaged tire and plastic waste with the mixed material of 2: 1 mode, send into fluidized-bed with 1.8 kilograms speed per hour, the pyrolysis product that obtains is directly sent into plasma generator, the processing parameter of its producer is: working current is 160A, and voltage is 320V, and the flow of argon gas is 1.8m
3/ h, main hydrogen flow is 0.6m
3/ h, secondary hydrogen flow is 0.3m
3/ h; Reactor inside diameter is 60mm, and length is 1800mm, separates to obtain Shawinigan black by cyclone separator.
Claims (3)
1. one kind is utilized plastic waste, damaged tire prepares the method for Shawinigan black, it is characterized in that it being with various waste or used plastics, damaged tire is a raw material, adopt the two-stage method processing treatment, its technological process is: with various waste or used plastics, damaged tire, in temperature is 400-600 ℃, rare gas element is to send into fluidized-bed reactor under the condition of carrier gas, carry out first section fast pyrogenation, gas-phase product in reactor the residence time less than 0.6 minute, then the gas-phase product that pyrolysis is obtained is directly sent into the direct current-arc plasma producer by carrier gas, second section graphiote reactor through optimization design carries out pyrolysis again, the solid material that the collection pyrolysis obtains is a Shawinigan black, its processing parameter is: working current is 110~190A, and voltage is 240~340V, and the flow of argon gas is 0.5~2m
3/ h, main hydrogen flow is 0.5~2.0m
3/ h, secondary hydrogen flow is 0.2~2.0m
3/ h, input speed is 0.6~4kg/h, and reactor inside diameter is 40~70mm, and length is 1500~1800mm.
2. according to the described a kind of method of utilizing plastic waste, damaged tire to prepare Shawinigan black of claim 1, it is characterized in that described raw material is the mixture of damaged tire and plastic waste or the single thing of damaged tire or plastic waste, the gas-phase product that described pyrolysis obtains also can put together after cooling becomes liquid collecting and carry out second section pyrolysis again.
3. according to the described a kind of method of utilizing plastic waste, damaged tire to prepare Shawinigan black of claim 1, it is characterized in that described damaged tire and plastic waste size range are greater than 40 orders or less than 0.44mm.
Priority Applications (1)
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CN 200510012531 CN1696210A (en) | 2005-05-24 | 2005-05-24 | Method for preparing acetylene black from waste plastics, tire |
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CN 200510012531 CN1696210A (en) | 2005-05-24 | 2005-05-24 | Method for preparing acetylene black from waste plastics, tire |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101298522B (en) * | 2008-07-02 | 2011-07-27 | 欧阳林 | Environment-friendly type technology for waste plastic cracking black carbon |
CN103708461A (en) * | 2013-12-25 | 2014-04-09 | 北京神雾环境能源科技集团股份有限公司 | Method for preparing calcium carbide |
CN105331378A (en) * | 2015-10-28 | 2016-02-17 | 贵州安泰再生资源科技有限公司 | Method of comprehensively utilizing junked tire subjected to pyrolysis |
CN107488455A (en) * | 2017-08-17 | 2017-12-19 | 太原理工大学 | A kind of method that thermal decomposing waste tire residue is upgraded to tire carbon black |
WO2024198035A1 (en) * | 2023-03-29 | 2024-10-03 | 上海菲利科思新材料有限公司 | Method and device system for producing ethylene-device steam cracking raw oil and nano charcoal material from waste plastics |
-
2005
- 2005-05-24 CN CN 200510012531 patent/CN1696210A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101298522B (en) * | 2008-07-02 | 2011-07-27 | 欧阳林 | Environment-friendly type technology for waste plastic cracking black carbon |
CN103708461A (en) * | 2013-12-25 | 2014-04-09 | 北京神雾环境能源科技集团股份有限公司 | Method for preparing calcium carbide |
CN103708461B (en) * | 2013-12-25 | 2016-08-24 | 神雾环保技术股份有限公司 | The method preparing calcium carbide |
CN105331378A (en) * | 2015-10-28 | 2016-02-17 | 贵州安泰再生资源科技有限公司 | Method of comprehensively utilizing junked tire subjected to pyrolysis |
CN105331378B (en) * | 2015-10-28 | 2017-10-03 | 贵州安泰再生资源科技有限公司 | A kind of junked tire is pyrolyzed method of comprehensive utilization |
CN107488455A (en) * | 2017-08-17 | 2017-12-19 | 太原理工大学 | A kind of method that thermal decomposing waste tire residue is upgraded to tire carbon black |
WO2024198035A1 (en) * | 2023-03-29 | 2024-10-03 | 上海菲利科思新材料有限公司 | Method and device system for producing ethylene-device steam cracking raw oil and nano charcoal material from waste plastics |
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