KR970001511A - Oiling apparatus and its method by complex pyrolysis of waste tire / waste oil - Google Patents

Oiling apparatus and its method by complex pyrolysis of waste tire / waste oil Download PDF

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Publication number
KR970001511A
KR970001511A KR1019950014824A KR19950014824A KR970001511A KR 970001511 A KR970001511 A KR 970001511A KR 1019950014824 A KR1019950014824 A KR 1019950014824A KR 19950014824 A KR19950014824 A KR 19950014824A KR 970001511 A KR970001511 A KR 970001511A
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KR
South Korea
Prior art keywords
waste
oil
pyrolysis
tires
pyrolysis reactor
Prior art date
Application number
KR1019950014824A
Other languages
Korean (ko)
Other versions
KR0148205B1 (en
Inventor
김동찬
신대현
정수현
김상국
강계식
우제경
손성근
김정덕
노남선
김광호
Original Assignee
손영목
한국에너지기술연구소
Priority date (The priority date 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 date listed.)
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Publication date
Application filed by 손영목, 한국에너지기술연구소 filed Critical 손영목
Priority to KR1019950014824A priority Critical patent/KR0148205B1/en
Publication of KR970001511A publication Critical patent/KR970001511A/en
Application granted granted Critical
Publication of KR0148205B1 publication Critical patent/KR0148205B1/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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C2201/00—Codes relating to disintegrating devices adapted for specific materials
    • B02C2201/06—Codes relating to disintegrating devices adapted for specific materials for garbage, waste or sewage
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/46—Constructional details of screens in general; Cleaning or heating of screens
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4006—Temperature
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B15/00—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form
    • F26B15/10—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions
    • F26B15/105—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the articles, e.g. can lids, discs, being conveyed by means of rotating screw spindles
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics

Abstract

본 발명은 가열된 폐유내에서 폐타이어를 열분해 반응시켜 오일화하기 위한 열분해 반응조건과 장치 및 그 방법에 관한 것으로 열분해 반응시 온도를 380℃로 낮추고 폐타이어와 폐유의 공급비를 2:1하여 분해시킴으로서 폐유에 대한 폐타이어의 처리량을 높이고 열효율을 증대시켰으며 반응기내에 첨가제 수산화 칼슘[Ca(OH)2]을 첨가하여 열분해 생성오일 중의 유황분과 염소등의 유해물질의 함유량을 최소화하였고, 열분해 장치의 기계적 결함을 해소하기 위해 폐유가열장치, 폐타이어의 연속공급장치, 열분해 반응기 및 잔유물 건조기의 장치상의 문제점을 개선한 폐타이어/폐유의 복합열분해에 의한 오일화 장치.The present invention relates to a pyrolysis reaction condition, an apparatus, and a method for pyrolyzing waste tires in a heated waste oil and to oil them, thereby lowering the temperature of the pyrolysis reaction to 380 ° C. and providing a 2: 1 feed ratio between waste tires and waste oil. By decomposing, the waste tire was increased for waste oil, thermal efficiency was increased, and additive calcium hydroxide [Ca (OH) 2 ] was added to the reactor to minimize the content of harmful substances such as sulfur and chlorine in the pyrolysis generating oil. An oilification apparatus by waste pyrolysis of waste tires / waste oil which improves the problems of waste oil heating device, continuous supply of waste tires, pyrolysis reactor and residue dryer to solve the mechanical defect of

Description

폐타이어/폐유의 복합열분해에 의한 오일화 장치와 그 방법Oiling apparatus and its method by complex pyrolysis of waste tire / waste oil

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

제1도는 본 발명의 오일화공정을 나타낸 장치의 개념도.1 is a conceptual diagram of an apparatus showing the oilification process of the present invention.

Claims (2)

가열된 폐유내에서 폐타이어를 열분해 반응시켜 오일화하는 열분해 반응조건으로서 폐타이어/폐유의 공급비율을 2:1로 하고, 열분해 반응기(6)내의 온도를 380℃로 하며 첨가제로 수산화 칼슘[Ca(OH)2]을 폐타이어량의 5% 이내를 첨가하는 것을 특징으로 하는 폐타이어/폐유의 복합열분해에 의한 오일화 방법.Pyrolysis reaction conditions in which the waste tires are pyrolyzed and oilified in the heated waste oil. The feed ratio of waste tire / waste oil is 2: 1, the temperature in the pyrolysis reactor 6 is 380 ° C., and calcium hydroxide [Ca] is added as an additive. (OH) 2 ] is an oilification method by complex pyrolysis of waste tires / waste oil, characterized in that the addition of less than 5% of the amount of waste tires. 파쇄된 폐타이어를 2중댐퍼(3)에 의해 열분해 반응기(6)에 공급하고 동시에 폐유를 가열로(4)에서 예열하여 증발탑(5)에서 저비점분을 제거 후 고비점분의 유분만을 열분해 반응기(6)에 공급하며 폐타이어는 열분해 반응기(6)내에서 스크류에 의해 하부로부터 상부로 이송되면서 열분해되어 가스상으로 되며 이를 급냉조 (8)에 도입하여 중질유분과 가스상으로 분리시키고 중질유분에 함유된 입자들과 타르성분은 슬럿지 분리조(9)에서 분리되며 급냉조(8)에서 응축되지 않은 가스상은 응축기(10)를 거친후 가스-오일분리기(11)로 보내져 경질유와 비응축성 가스로 분리하는 오일화 장치이며 열분해 반응기(6)에서 슬럿지 상태로 배출된 잔류물은 스크류 건조기(7)에서 건조하여 2중댐퍼로 구성된 잔류물 배출기(14)를 통해 배출되면서 냉각되고 철심분리기(15), 파쇄기(16) 및 체 분리기(17)의 과정을 거쳐 제품의 잔류물 상태를 얻는 것을 특징으로 하는 폐타이어/폐유의 복합열분해에 의한 오일화 장치.The crushed waste tires are supplied to the pyrolysis reactor 6 by the double damper 3 and at the same time, the waste oil is preheated in the heating furnace 4 to remove the low boiling point from the evaporation tower 5 and then only the high boiling point oil is pyrolysis reactor. (6), the waste tire is thermally decomposed into the gas phase by being transferred from the bottom to the top by a screw in the pyrolysis reactor (6) and introduced into the quench tank (8) to separate the heavy oil and gas phase and contained in the heavy oil. Particles and tar components are separated in the sludge separation tank (9), and the non-condensed gas phase in the quench tank (8) is passed through the condenser (10) and sent to the gas-oil separator (11) to separate light oil and non-condensable gas. Residue discharged in the sludge state from the pyrolysis reactor (6) is dried in the screw dryer (7) and cooled while being discharged through the residue ejector (14) consisting of a double damper, iron core separator (15), Wedges five days screen device according to the composite thermal decomposition of the waste tire / waste oil, characterized in that over the course of 16 and the separator body 17 to obtain a residue of the products. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019950014824A 1995-06-05 1995-06-05 Apparatus and method for manufacture of oil by combination thermal decomposition used waste ires/oils KR0148205B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019950014824A KR0148205B1 (en) 1995-06-05 1995-06-05 Apparatus and method for manufacture of oil by combination thermal decomposition used waste ires/oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019950014824A KR0148205B1 (en) 1995-06-05 1995-06-05 Apparatus and method for manufacture of oil by combination thermal decomposition used waste ires/oils

Publications (2)

Publication Number Publication Date
KR970001511A true KR970001511A (en) 1997-01-24
KR0148205B1 KR0148205B1 (en) 1998-08-01

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100473763B1 (en) * 2002-09-28 2005-03-10 천지득 Recycling machine of waste tire for oil, carbon and wire core by auto continuous process

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100864904B1 (en) * 2005-07-20 2008-10-22 (주)기경아이이앤드씨 Apparatus for making oil and generating electricity with used hot gas
US8066785B2 (en) 2007-07-30 2011-11-29 Recarbon Corp. Process for recycling waste materials
US7842106B2 (en) 2007-07-30 2010-11-30 Recarbon Corp. Process for using polymeric waste materials to produce fuel
US7846225B2 (en) * 2007-07-30 2010-12-07 Recarbon Corp. Process for recycling polymeric waste materials
KR102558884B1 (en) * 2021-10-14 2023-07-24 김남용 Eco-friendly hybrid waste resource treatment system with Emulsification line and heat source sharing and filtration recovery circulation line

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100473763B1 (en) * 2002-09-28 2005-03-10 천지득 Recycling machine of waste tire for oil, carbon and wire core by auto continuous process

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Publication number Publication date
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