CN101935540A - Innocuous treatment technology for waste rubber by adding catalyst comprising steel wire - Google Patents
Innocuous treatment technology for waste rubber by adding catalyst comprising steel wire Download PDFInfo
- Publication number
- CN101935540A CN101935540A CN2009100542470A CN200910054247A CN101935540A CN 101935540 A CN101935540 A CN 101935540A CN 2009100542470 A CN2009100542470 A CN 2009100542470A CN 200910054247 A CN200910054247 A CN 200910054247A CN 101935540 A CN101935540 A CN 101935540A
- Authority
- CN
- China
- Prior art keywords
- steel wire
- oil
- waste
- old
- carbon black
- 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
Images
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to innocuous treatment technology for waste rubber by adding a catalyst comprising a steel wire, which comprises the following steps of: washing the waste rubber and crushing the rubber by using a crusher, and is characterized by comprising the following steps of: adding the catalyst comprising the steel wire into the crushed waste rubber granules, adding into a cracking furnace for cracking, and performing oil-gas separation and steel wire section and carbon black separation on the oil-gas mixed gas and solid produced by cracking; returning combustible gases subjected to oil-gas separation to the cracking furnace for combustion, and cooling and recovering fuel oil; cooling the oil-gas mixed gas, separating the combustible gases and the fuel oil, and cooling and separating the carbon black comprising the steel wire section; and cleaning and recovering the steel wire section, and grinding the carbon black into powder and recovering the powder by stirring and pelleting. The technology is characterized in that: the catalyst is a mixture of SiO2, Al2O3 and Fe2O3; the oil recovery rate is over 46 percent, the recovery rate of the combustible gases is 7 percent, and the sulfur accounts for over 3 percent of the carbon black. The innocuous treatment technology has the advantages of low energy consumption, safety, environmental protection, no pollutant emission and the like.
Description
Technical field
The present invention relates to a kind of treatment process of waste old, particularly a kind ofly add the harmless treatment process that catalyst pack contains the waste old of steel wire.
Background technology
Present economic develop rapidly along with the whole nation, increasing rubber enters into the every field of national economy, and therefore the rubber recoverable amount in the whole world increases rapidly, and the consequent is the problem that is treated as a needs solution of the waste old in every year.The processing of early stage waste old mainly is the harmless treatment to waste, but along with the notion of green economy proposes, waste old all can be recycled become a whether problem of Sustainable development, the consequent is that waste old is carried out cracking, reclaim carbon black, oil fuel and combustion gas in the waste old, but present treatment process is at first to need to send pyrolyzer to handle in the waste old fragment.Because do not have catalyzer as adding material, its cracking temperature is difficult to control, the carbon black quality is very low.And too high at oil product and fuel gas sulphur content, environment is produced pollution.Have plenty of and adopt the big fragment of the waste old after freezing method will cut to be refrigerated to end temperature, and then the particle of rubber is pulverized, but aforesaid method extremely wastes energy, the energy-conservation Sustainable development that can't realize with the method for bump.
Summary of the invention
The objective of the invention is to solve and handle the existing the problems referred to above of waste old in the prior art, a kind of harmless treatment process that catalyst pack contains the waste old of steel wire that adds is provided, the present invention designs a kind of harmless treatment process that catalyst pack contains the waste old of steel wire that adds, comprise washing waste old, crusher in crushing, it is characterized in that: the interpolation of the waste and old rubber particle after fragmentation catalyzer is contained steel wire send into the pyrolyzer cracking, fuel-air mixture body that produces after the cracking and solid carry out gas-oil separation respectively to be separated with sooty with the steel wire section; Inflammable gas after the gas-oil separation is recycled to the pyrolyzer burning, and fuel cools reclaims.Oil and gas separation method is the cooling fuel-air mixture, and fuel-air mixture is isolated inflammable gas and oil fuel after cooling.Steel wire separates with sooty, and the carbon black that contains the steel wire section is cooled off, and utilizes the separation screening auger that the steel wire section is separated with carbon black then.The steel wire section is cleaned the back and is reclaimed, and carbon black is reclaimed by stirring-granulating behind abrasive dust.With 390 ℃---temperature cracking 25 of 420 ℃---35 minutes, the footpath grain of the waste and old rubber particle of crusher in crushing is 20 to waste and old rubber particle in pyrolyzer---30 millimeters.It is characterized in that: described catalyzer is SiO
2, Al
2O
3, Fe
2O
3Mixture.It is characterized in that: SiO
2, Al
2O
3, Fe
2O
3Ratio of mixture be 1: 1: 3.Because the effect of catalyzer: the Oil Recovery rate is more than 46%, and combustible gas reclaims 7%, and the carbon black sulphur content is more than 3%.Advantage of the present invention is that a whole set of treatment process has advantages such as energy consumption is low, safety, environmental protection, non-pollutant discharge.
Description of drawings
Accompanying drawing is a process flow sheet of the present invention,
Below in conjunction with drawings and Examples the present invention is elaborated.
Embodiment
At first the waste old that reclaims is washed, be mingled in wherein rubbish to remove some, send crusher in crushing with waste old then, generally waste old need be broken into the footpath grain is 20---30 millimeter-sized particles, after fragmentation, note the bulk loopback crusher in crushing again of complete fragmentation at any time, waste and old rubber particle after will pulverizing then (adds catalyzer, for pressing 1: 1: 3 blended SiO
2, Al
2O
3, Fe
2O
3Powder) contains steel wire and send into the pyrolyzer cracking, pyrolyzer is heated by burning combustible gas, at 390 ℃---cracking under 420 ℃ the temperature condition, in pyrolyzer about 25---35 minutes, the fuel-air mixture body that produces from pyrolyzer after the cracking send oil gas separation equipment to carry out gas-oil separation, gas-oil separation is carried out in the refrigerated separation tower, with water coolant the fuel-air mixture body that enters in the refrigerated separation tower is cooled off, inflammable gas is overflowed from refrigerated separation tower top, and be transmitted back in the roasting kiln of pyrolyzer and burn, realize recycle, and gather condensed oil fuel, the direct canned recovery of oil fuel in refrigerated separation tower bottom.After the carbon black that contains the steel wire section is come out of the stove, at first cool off by the cooling auger, and utilize the separation screening auger that the steel wire section is separated with carbon black simultaneously, steel wire section after the separation is cleaned the back recycling, and after carbon black sends into the pulverizing mill abrasive dust, after water and carbon black dosage, carry out stirring-granulating, then dry packing.No any gas leak in the entire treatment technology carries out catalytic pyrolysis under condition of negative pressure, waste old can be converted into about 8% combustible gas, 50% oil fuel, 42% carbon black through above-mentioned treatment process process, realizes recycling fully.More than the catalytic pyrolysis efficient catalytic efficiency 1000g/g.cat, catalysis is long-acting stablized more than 1.5 hours.Has the dual-use function that cracking macromolecular chain and product molecule are reformed.Its basic physicochemical property is as follows:
Outward appearance: canescence, powdery, tap density: 0.6 ± 0.1g/ml,
Specific surface: 200～300m2/g, proterties: water-absorbent is strong, addition: 0.4～0.6% (to raw material).
Claims (7)
1. one kind is added the harmless treatment process that catalyst pack contains the waste old of steel wire, comprise washing waste old, crusher in crushing, it is characterized in that: the waste and old rubber particle after the fragmentation (interpolation catalyzer) steel wire is sent into the pyrolyzer cracking, and fuel-air mixture body that produces after the cracking and solid carry out gas-oil separation respectively to be separated with sooty with the steel wire section; Inflammable gas after the gas-oil separation is recycled to the pyrolyzer burning, and fuel cools reclaims.
2. by the described a kind of harmless treatment process that catalyst pack contains the waste old of steel wire that adds of claim 1, it is characterized in that: oil and gas separation method is the cooling fuel-air mixture, and fuel-air mixture is isolated inflammable gas and oil fuel after cooling.
3. by the described a kind of harmless treatment process that catalyst pack contains the waste old of steel wire that adds of claim 1; it is characterized in that: the carbon black that steel wire and sooty are separated into containing the steel wire section cools off; utilize the separation screening auger that the steel wire section is separated with carbon black then; the steel wire section is cleaned the back recycling; carbon black is reclaimed by the stirrer stirring-granulating behind abrasive dust, and reaches the use of off-colour industry product.
4. by the described a kind of harmless treatment process that catalyst pack contains the waste old of steel wire that adds of claim 1, it is characterized in that: waste and old rubber particle in pyrolyzer with 390 ℃---temperature cracking 25 of 420 ℃---35 minutes.
5. by the described a kind of harmless treatment process that catalyst pack contains the waste old of steel wire that adds of claim 1, it is characterized in that: the footpath grain of the waste and old rubber particle of crusher in crushing is 20---30 millimeters.
6. by the described a kind of harmless treatment process that catalyst pack contains the waste old of steel wire that adds of claim 1, it is characterized in that: described catalyzer is SiO
2, Al
2O
3, Fe
2O
3Mixture.
7. by the described a kind of harmless treatment process that catalyst pack contains the waste old of steel wire that adds of claim 6, it is characterized in that: SiO
2, Al
2O
3, Fe
2O
3Ratio of mixture be 1: 1: 3 thing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100542470A CN101935540A (en) | 2009-06-30 | 2009-06-30 | Innocuous treatment technology for waste rubber by adding catalyst comprising steel wire |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100542470A CN101935540A (en) | 2009-06-30 | 2009-06-30 | Innocuous treatment technology for waste rubber by adding catalyst comprising steel wire |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101935540A true CN101935540A (en) | 2011-01-05 |
Family
ID=43389114
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009100542470A Pending CN101935540A (en) | 2009-06-30 | 2009-06-30 | Innocuous treatment technology for waste rubber by adding catalyst comprising steel wire |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101935540A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104673351A (en) * | 2013-11-29 | 2015-06-03 | 招远市东晟橡胶制品有限公司 | Cracking process of waste rubber |
| CN105127100A (en) * | 2015-09-12 | 2015-12-09 | 商丘金蓬实业股份有限公司 | Carbon-black and steel-wire separating device |
| CN106185863A (en) * | 2016-07-06 | 2016-12-07 | 上海绿人生态经济环境保护研究所 | The technique that CNT prepared by the combustible gas utilizing junked tire thermal cracking to produce |
| CN107459996A (en) * | 2017-08-10 | 2017-12-12 | 无锡龙盈环保科技有限公司 | A kind of processing equipment of junked tire |
| CN107955419A (en) * | 2017-11-30 | 2018-04-24 | 绵阳安立特环境能源科技有限公司 | A kind of method that waste tire prepares industrial carbon black |
| CN111286219A (en) * | 2020-03-19 | 2020-06-16 | 福建华峰运动用品科技有限公司 | Method for recovering carbon black from shoe material and application |
| CN113563743A (en) * | 2021-07-09 | 2021-10-29 | 中国化学工业桂林工程有限公司 | Catalytic regeneration method of pyrolysis carbon black |
| CN116042250A (en) * | 2023-03-31 | 2023-05-02 | 新疆轮匠碳中和产业园有限公司 | Steel wire peeling-free production system and method based on pyrolysis treatment of junked tires |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5233109A (en) * | 1989-11-06 | 1993-08-03 | National University Of Singapore | Production of synthetic crude petroleum |
| CN1117517A (en) * | 1994-08-24 | 1996-02-28 | 中国长江动力公司(集团) | Method and equipment for catalytic cracking waste rubber |
| CN1388880A (en) * | 2000-08-10 | 2003-01-01 | Rj利格鲁普公司 | Low energy method of pyrolysis of hydrocarbon materials such as rbber |
| CN101402745A (en) * | 2007-04-25 | 2009-04-08 | 陈汇宏 | Method and apparatus for combination regeneration, or coproduction with hydrocarbon black of waste and old macromolecule material |
-
2009
- 2009-06-30 CN CN2009100542470A patent/CN101935540A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5233109A (en) * | 1989-11-06 | 1993-08-03 | National University Of Singapore | Production of synthetic crude petroleum |
| CN1117517A (en) * | 1994-08-24 | 1996-02-28 | 中国长江动力公司(集团) | Method and equipment for catalytic cracking waste rubber |
| CN1388880A (en) * | 2000-08-10 | 2003-01-01 | Rj利格鲁普公司 | Low energy method of pyrolysis of hydrocarbon materials such as rbber |
| CN101402745A (en) * | 2007-04-25 | 2009-04-08 | 陈汇宏 | Method and apparatus for combination regeneration, or coproduction with hydrocarbon black of waste and old macromolecule material |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104673351A (en) * | 2013-11-29 | 2015-06-03 | 招远市东晟橡胶制品有限公司 | Cracking process of waste rubber |
| CN105127100A (en) * | 2015-09-12 | 2015-12-09 | 商丘金蓬实业股份有限公司 | Carbon-black and steel-wire separating device |
| CN105127100B (en) * | 2015-09-12 | 2017-07-21 | 商丘金蓬实业股份有限公司 | Carbon black, steel wire separator |
| CN106185863A (en) * | 2016-07-06 | 2016-12-07 | 上海绿人生态经济环境保护研究所 | The technique that CNT prepared by the combustible gas utilizing junked tire thermal cracking to produce |
| CN107459996A (en) * | 2017-08-10 | 2017-12-12 | 无锡龙盈环保科技有限公司 | A kind of processing equipment of junked tire |
| CN107955419A (en) * | 2017-11-30 | 2018-04-24 | 绵阳安立特环境能源科技有限公司 | A kind of method that waste tire prepares industrial carbon black |
| CN111286219A (en) * | 2020-03-19 | 2020-06-16 | 福建华峰运动用品科技有限公司 | Method for recovering carbon black from shoe material and application |
| CN113563743A (en) * | 2021-07-09 | 2021-10-29 | 中国化学工业桂林工程有限公司 | Catalytic regeneration method of pyrolysis carbon black |
| CN113563743B (en) * | 2021-07-09 | 2022-04-22 | 中国化学工业桂林工程有限公司 | Catalytic regeneration method of pyrolysis carbon black |
| CN116042250A (en) * | 2023-03-31 | 2023-05-02 | 新疆轮匠碳中和产业园有限公司 | Steel wire peeling-free production system and method based on pyrolysis treatment of junked tires |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101935540A (en) | Innocuous treatment technology for waste rubber by adding catalyst comprising steel wire | |
| CN101812314B (en) | Low-temperature catalytic cracking method with high-value utilization of waste tire | |
| Sharma et al. | Disposal of waste tyres for energy recovery and safe environment | |
| CN103977529B (en) | Chromium slag pyrolysis treatment method with low tar emission | |
| CN102757803B (en) | Steam low-temperature carbonization system and method of waste tire fluidized bed | |
| CN109517612B (en) | Continuous, efficient and green waste tire superheated steam energy conversion method | |
| CN103693805A (en) | Device and method for recycling coal pyrolysis waste | |
| CN112707610B (en) | Process for resource utilization of oily sludge | |
| CN106544050A (en) | The cyclic utilization system and its method of damaged tire | |
| CN104845649A (en) | Method using coke powder and tar slag for substitution of part of coal for production of coke | |
| CN111234858A (en) | System and process for recycling waste tires | |
| US12012334B2 (en) | Method for removing ash from solid carbonaceous material | |
| JP2012087222A (en) | Treatment method and treatment apparatus for carbonaceous material | |
| CN104059681A (en) | Regenerative type combustion gas radiant tube revolving bed oil shale dry distillation method and shale slag utilization technology | |
| CN101307152B (en) | Apparatus for treating waste and old tyres | |
| CN107964411B (en) | Method for recycling coking coal from dry quenching coke breeze | |
| CN210030584U (en) | Waste tire recycling system | |
| CN115448623B (en) | Method for preparing cementing material by sintering and activating coal gangue | |
| CN102899093A (en) | High-efficiency and clean coal gasification process | |
| CN113604239B (en) | Waste tire treatment and recovery method | |
| CN208454889U (en) | A kind of device preparing clean coal using pyrolysis of waste gasification partial carbonization | |
| CN207789460U (en) | The environmentally friendly cracking system of waste tire recycling | |
| CN110358581B (en) | Device and method for granulating, pyrolyzing and gasifying water-containing oil residues | |
| JPS62221484A (en) | Method for treating shredder dust | |
| CN106318430A (en) | System and method utilizing low-rank coal |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20110105 |