KR930006141A - Pyrolysis Process for Oil Recovery from Waste Tires Using Waste Oil as Fruit - Google Patents

Pyrolysis Process for Oil Recovery from Waste Tires Using Waste Oil as Fruit Download PDF

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Publication number
KR930006141A
KR930006141A KR1019910016020A KR910016020A KR930006141A KR 930006141 A KR930006141 A KR 930006141A KR 1019910016020 A KR1019910016020 A KR 1019910016020A KR 910016020 A KR910016020 A KR 910016020A KR 930006141 A KR930006141 A KR 930006141A
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KR
South Korea
Prior art keywords
oil
waste
generated
fruit
pyrolyzed
Prior art date
Application number
KR1019910016020A
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Korean (ko)
Other versions
KR930011919B1 (en
Inventor
정수현
신대현
김동찬
Original Assignee
오정무
재단법인 한국동력자원연구소
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Application filed by 오정무, 재단법인 한국동력자원연구소 filed Critical 오정무
Priority to KR1019910016020A priority Critical patent/KR930011919B1/en
Publication of KR930006141A publication Critical patent/KR930006141A/en
Application granted granted Critical
Publication of KR930011919B1 publication Critical patent/KR930011919B1/en

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste

Abstract

파쇄된 폐타이어(T)를 이동층 반응기(3)에 투입하면서 폐타이어에 대하여 1:1∼2의 무게비율로 폐유(4)를 공급하여 400-600℃로 가열함으로써 발생된 생성오일(0)과 생성가스(G)를 급냉조(5)와 응축기(6)에 의하여 분리회수하고 일부는 가열로(8)용에 순환한다. 이동층 반응기(3)에서 열분해되지 않은 폐유 및 폐타이어는 나선식 반응기(9)에서 열분해하여 생성오일(0)과 생성가스(G)를 회수 및 순환하는 공정이며 또 잔류물은 자석식 분리기(10)에 의하여 스틸(S)과 카본블랙(C)으로 분리하여 아스팔트에 대해 8-10% 첨가한 아스팔트 혼합재 또는 보강재로 활용하는 공정을 포함하는 것을 특징으로 하는 폐유를 열매로 하여 폐타이어로부터 오일 회수를 위한 열분해 공정.Generated oil (0) generated by supplying the waste oil (4) at a weight ratio of 1: 1 to 2 with respect to the waste tire while inputting the crushed waste tire (T) to the moving bed reactor (0) (0) ) And the generated gas (G) are separated and recovered by the quench tank (5) and the condenser (6), and some of them are circulated for the furnace (8). Waste oil and waste tire not pyrolyzed in the moving bed reactor (3) are pyrolyzed in the spiral reactor (9) to recover and circulate the product oil (0) and the product gas (G), and the residue is a magnetic separator (10). Separation into steel (S) and carbon black (C) by using) as an asphalt mixture or reinforcing material added to the asphalt mixed with 8-10%, recovering oil from waste tires as a fruit Pyrolysis process for

Description

폐유를 열매로 하여 폐타이어로부터 오일 회수를 위한 열분해공정Pyrolysis Process for Oil Recovery from Waste Tires Using Waste Oil as Fruit

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제1도는 폐유를 열매로 하는 폐타이어의 열분해 장치도,1 is a pyrolysis device of waste tires using waste oil as a fruit.

제3도는 생성오일의 증류곡선,3 shows the distillation curve of the produced oil,

제5도는 잔류물 평균입경과 아스팔트 점도와의 관계.5 is the relationship between the average particle diameter of residue and the viscosity of asphalt.

Claims (1)

파쇄된 폐타이어(T)를 이동층 반응기(3)에 투입하면서 폐타이어에 대하여 1:1∼2의 무게비율로 폐유(4)를 공급하여 400-600℃로 가열함으로써 발생된 생성오일(0)과 생성가스(G)를 급냉조(5)와 응축기(6)에 의하여 분리회수하고 일부는 가열로(8)용에 순환한다. 이동층 반응기(3)에서 열분해되지 않은 폐유 및 폐타이어는 나선식 반응기(9)에서 열분해하여 생성오일(0)과 생성가스(G)를 회수 및 순환하는 공정이며 또 잔류물은 자석식 분리기(10)에 의하여 스틸(S)과 카본 블랙(C)으로 분리하여 아스팔트에 대해 8-10% 첨가한 아스팔트 혼합재 또는 보강재로 활용하는 공정을 포함하는 것을 특징으로 하는 폐유를 열매로 하여 폐타이어로부터 오일회수를 위한 열분해 공정.Generated oil (0) generated by supplying the waste oil (4) at a weight ratio of 1: 1 to 2 with respect to the waste tire while inputting the crushed waste tire (T) to the moving bed reactor (0) (0) ) And the generated gas (G) are separated and recovered by the quench tank (5) and the condenser (6), and some of them are circulated for the furnace (8). Waste oil and waste tire not pyrolyzed in the moving bed reactor (3) are pyrolyzed in the spiral reactor (9) to recover and circulate the product oil (0) and the product gas (G), and the residue is a magnetic separator (10). To recover the oil from the waste tires as a fruit, comprising the step of separating the steel (S) and the carbon black (C) into 8-10% of the asphalt mixture or as a reinforcing material. Pyrolysis process for ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019910016020A 1991-09-13 1991-09-13 Thermal cracking process for production of liquid hydrocarbon mixtures from waste tires KR930011919B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019910016020A KR930011919B1 (en) 1991-09-13 1991-09-13 Thermal cracking process for production of liquid hydrocarbon mixtures from waste tires

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019910016020A KR930011919B1 (en) 1991-09-13 1991-09-13 Thermal cracking process for production of liquid hydrocarbon mixtures from waste tires

Publications (2)

Publication Number Publication Date
KR930006141A true KR930006141A (en) 1993-04-20
KR930011919B1 KR930011919B1 (en) 1993-12-22

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Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019910016020A KR930011919B1 (en) 1991-09-13 1991-09-13 Thermal cracking process for production of liquid hydrocarbon mixtures from waste tires

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KR (1) KR930011919B1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100847512B1 (en) * 2007-05-16 2008-07-22 천명원 Manufacturing method for liquid fuel
KR101356910B1 (en) * 2012-02-17 2014-01-29 박희원 Device and method for organic synthesis gas generating device of automotive waste

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100593725B1 (en) * 2005-12-05 2006-06-30 (주)에티스 Waste tires of pyroiysis and oil paint system
CN108949269A (en) * 2018-08-22 2018-12-07 湖南文理学院 A kind of chemical industry synthesis liquefied gas production capacity optimal control method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100847512B1 (en) * 2007-05-16 2008-07-22 천명원 Manufacturing method for liquid fuel
KR101356910B1 (en) * 2012-02-17 2014-01-29 박희원 Device and method for organic synthesis gas generating device of automotive waste

Also Published As

Publication number Publication date
KR930011919B1 (en) 1993-12-22

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