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Method for recycling rubber-containing wastes

a technology of rubber-containing wastes and wastes, which is applied in the field of recycling rubber-containing wastes, can solve the problems of high energy intensity, very actual polymer wastes, and use of wastes from synthetic rubber production, and achieve the effects of improving process productivity, simplifying technology, and speeding up process

Inactive Publication Date: 2006-12-14
OBSCHESTVO S OGRANICHENNOY OTVETSTVENNOSTYU N T D TAMANNO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

"The invention is a method for recycling rubber-containing wastes by thermal liquefaction and catalytic reforming, which improves the process efficiency and simplifies the technology. The method can accelerate the recycling process, increase the yield of high-octane gasoline fraction, and produce technical carbon as a commercial product. The method also reduces power intensity, expands the functional capabilities, and lowers the operating costs. The technical effects of the invention include improved process efficiency, simplified technology, increased yield of high-octane gasoline fraction, and reduced power intensity."

Problems solved by technology

The problem of chemical processing of various organic industrial and household polymeric wastes is very actual due to continuous increase in their quantities and pollution of the environment.
A limitation of the said method is the use of wastes from the synthetic rubber production, since such wastes are not always available in the required quantity.
A limitation of the said method is its high energy intensity due to using, as a part of the solvent, the liquid fraction with the boiling temperature not less than 210° C., and high operation pressures exceeding 6.1 MPa.
Some limitations of the said method are:
for efficient thermal liquefaction (thermolysis) the process is carried out in the presence of a rare-earth metal or intermetallics based on rare-earth metals or in the presence which are taken in the amount of 0.5% to 10% of the reaction mixture weight, which complicates the production process, and, moreover, removal of these additional catalysts and additives from the resulting valuable target product, namely, technical carbon, is very complicated;
low quality of technical carbon due to big amounts of ash materials, which is a consequence of using additives together with a solvent;
a high consumption rate of a solvent when producing a high-quality gasoline fraction.

Method used

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Examples

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Embodiment Construction

[0041]FIG. 1 schematically shows: a thermolysis reactor 1, a unit 2 for preparation and feeding of rubber-containing wastes, a reforming reactor 3, a cooler-condenser 4, a gas-liquid separator 5, a pump 6, a pipe furnace 7, a distributive device 9, a rectifying column 10.

[0042] The production process of thermal liquefaction (thermolysis) of rubber-containing wastes begins with waste preparation, e.g., worn tires. Rubber-containing wastes are washed, milled and separated from the slime I (steel cord, textile, dirt) in the unit 2 and afterwards are fed into the reactor 1 (conical) with a fluidized bed of rubber crumb and technical carbon in a solvent, which are is a state close to pseudo-critical.

[0043] Thermolysis of rubber and its conversion to the thermolysis products is carried out in the pseudo-fluidized bed of the solvent:

[0044] II—liquid heavy hydrocarbons having a boiling temperature above 220° C.;

[0045] III—powder technical carbon removed from the reactor 1 with the use o...

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Abstract

The inventive method includes thermal liquefaction of wastes in an organic solvent at a temperature above 270° C. and a pressure up to 6 MPa. The liquid fraction is separated from the undissolved product. The liquid fraction is distilled into the fraction with the boiling temperature below 220° C. and the fraction with the boiling temperature above 220° C. Alkyl benzene or the gasoline fraction with a boiling temperature below 220° C. is used as an organic solvent at the start-up of the process. Thermal liquefaction of a batch of wastes is carried out in an organic solvent at a temperature from 280° C. to 435° C. and a pressure at least 2.9 MPa, the organic solvent-waste weight ratio being more than 1.0. The liquid fraction with the boiling temperature below 220° C. is subjected to catalytic reforming. A part of the liquid fraction, as subjected to catalytic reforming, with the boiling temperature below 220° C. is used as the target product, and the remaining part of the liquid fraction, as subjected to catalytic reforming, with the boiling temperature below 220° C. is used as a solvent and returned for thermal liquefaction of a new batch of wastes at a temperature from 280° C. to 435° C. and a pressure at least 2.9 MPa, the solvent-waste weight ratio being more than 1.0. The process of thermal liquefaction is continued in the said conditions of thermal liquefaction and catalytic reforming for the next and subsequent batches of wastes, while a part of the liquid fraction, as subjected to catalytic reforming, with the boiling temperature below 220° C. being returned for thermal liquefaction.

Description

FIELD OF THE INVENTION [0001] This invention relates to disposal in the chemical industry of organic industrial and household rubber wastes and their processing into motor fuel and chemical stock to be further used as a boiler fuel, a bituminous-like binder or stock for production thereof, technical carbon or stock for production thereof, for electric arc furnaces, electrolysis baths, carbon-carbonic materials (CCM) for metallurgy, etc, as well as a small quantity of hydrocarbon gas which may be used as a fuel. PRIOR ART [0002] The problem of chemical processing of various organic industrial and household polymeric wastes is very actual due to continuous increase in their quantities and pollution of the environment. [0003] Removal of this problem will enable to solve the ecological task of complex and harmless disposal of rubber-containing industrial and household wastes, expand the base of hydrocarbon stock produced from oil, coals, shale coals, natural bitumen. [0004] A method for...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10G1/10C08J11/04C08J11/20C08L21/00C10G1/00C10G31/06C10G35/04C10G55/02
CPCC08J11/20C10G1/002C10G55/02C10G35/04C10G31/06Y02W30/62
Inventor BOCHAVER, KIRILL ZYSKOVICH
Owner OBSCHESTVO S OGRANICHENNOY OTVETSTVENNOSTYU N T D TAMANNO
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