[go: up one dir, main page]

KR890013163A - 잔류 탄화수소유의 열 분해 방법 및 이에 의해 생산된 탄화수소유 - Google Patents

잔류 탄화수소유의 열 분해 방법 및 이에 의해 생산된 탄화수소유 Download PDF

Info

Publication number
KR890013163A
KR890013163A KR1019890001594A KR890001594A KR890013163A KR 890013163 A KR890013163 A KR 890013163A KR 1019890001594 A KR1019890001594 A KR 1019890001594A KR 890001594 A KR890001594 A KR 890001594A KR 890013163 A KR890013163 A KR 890013163A
Authority
KR
South Korea
Prior art keywords
hydrocarbon oil
asphaltenes
synthesis gas
thermal decomposition
heavy hydrocarbon
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.)
Granted
Application number
KR1019890001594A
Other languages
English (en)
Other versions
KR970010860B1 (ko
Inventor
비써 디이드리크
마리아 게라르두스 센덴 마티예스
앙리 에마누엘 델 아미꼬 자끄
Original Assignee
오노 알버어스
셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이
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.)
Filing date
Publication date
Application filed by 오노 알버어스, 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 filed Critical 오노 알버어스
Publication of KR890013163A publication Critical patent/KR890013163A/ko
Application granted granted Critical
Publication of KR970010860B1 publication Critical patent/KR970010860B1/ko
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/34—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
    • C10G9/36—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
    • C10G9/38—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours produced by partial combustion of the material to be cracked or by combustion of another hydrocarbon
    • 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
    • C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/007—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 in the presence of hydrogen from a special source or of a special composition or having been purified by a special treatment
    • 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
    • C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
    • C10G67/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
    • C10G67/0454—Solvent desasphalting
    • C10G67/049—The hydrotreatment being a hydrocracking
    • 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
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S208/00—Mineral oils: processes and products
    • Y10S208/95—Processing of "fischer-tropsch" crude

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Industrial Gases (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

내용 없음.

Description

잔류 탄화수소유의 열 분해 방법 및 이에 의해 생산된 탄화수소유
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 감압에서 분해된 잔류물을 증류시키는 실시양태를 나타낸다.
제2도는 분해된 잔류물을 탈아스팔트화 시키는 실시양태를 나타낸다.

Claims (12)

  1. 단계 1 : 열 분해 지역내의 온도를 직접적인 열 교환 수단에 의해 420℃-850℃로 유지시키기 위해, 충분히 높은 온도의 합성기체 및 잔류 탄화수소유를 열 분해 지역에 공급하고 ; 단계 2 : 단계 1로부터의 분해 된 생성물을 (a) 합성 기체를 함유하는 기체성 분류물, (b) 하나 또는 그 이상의 탄화수소 증류 분류물 및 (c) 분해된 잔류물로 분리하고 ; 단계 3 : 단계 2로부터의 분해된 잔류물을 아스팔텐이 비교적 적은 하나 또는 그 이상의 중탄화수소유와 아스팔텐이 비교적 많은 하나 또는 그 이상의 탄화수소유로 분리하고 ; 단계 4 : 합성 기체 생산과 더불어 증기 및 산소 존재하에서 단계 3으로부터의 아스팔텐이 비교적 많은 하나 또는 그 이상의 중탄화 수소유를 기체화하고 ; 단계 5 : 단계 4로부터의 합성 기체를 단계 1의 합성 기체로 적용하는 단계들로 구성된 잔류 탄화수소유의 열 분해 방법.
  2. 제1항에 있어서, 단계 1의 열 분해가 420℃-645℃범위의 온도에서 수행되는 방법.
  3. 제2항에 있어서, 단계 1의 열 분해가 460℃-550℃범위의 온도에서 수행되는 방법.
  4. 제1항 내지 제3항중 어느 한 항에 있어서, 단계 1이 3-10바아 범위의 압력에서 수행되는 방법.
  5. 제1항 내지 제4항중 어느 한 항에 있어서, 단계 1의 열 분해가 1초-10분 범위의 평균 잔류 시간에서 수행되는 방법.
  6. 제5항에 있어서, 단계 1의 열 분해가 10초-10분 범위의 평균 잔류 시간에서 수행되는 방법.
  7. 제1항 내지 제6항중 어느 한 항에 있어서, 단계 4로부터의 합성 기체내에 존재하는 열이 기체가 단계 5에서 적용되기 전에 냉각 매체를 사용하여 간접적인 열 교환 수단에 의해 그로부터 회수되는 방법.
  8. 제1항 내지 제7항중 어느 한 항에 있어서, 단계 4로부터의 합성 기체내에 존재하는 금속 입자 및 회분이 기체가 단계 5에서 적용되기전에 탄소질 생성물 입자들에 대해 선택적으로 제거되는 방법.
  9. 제1항 내지 제8항중 어느 한 항에 있어서, 단계 2로 부터의 분해된 잔류물이 단계 3에서 부대기압에서의 증류 수단에 의해 아스팔텐이 비교적 적은 하나 또는 그 이상의 중탄화수소유 중류물과 아스팔텐이 비교적 많은 중 잔류 탄화수소유로 분리되는 방법.
  10. 제1항 내지 제8항중 어느 한 항에 있어서, 단계 2로 부터의 분해된 잔류물이 단계 3에서 추출제와 접촉되어 아스팔텐이 비교적 적은 중탄화수소유를 함유하는 추출상과 아스팔텐이 비교적 많은 중탄화수소유를 포함하는 추출 잔류물을 형성하는 방법.
  11. 제10항에 있어서, 추출제가 프로판, 부탄, 이소부탄 및/또는 펜탄인 방법.
  12. 제1항 내지 제11항의 공정에 의해 얻어진 탄화수소유.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019890001594A 1988-02-11 1989-02-09 잔류 탄화수소유의 열 분해 방법 및 이에 의해 생산된 탄화수소유 Expired - Fee Related KR970010860B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB8803156 1988-02-11
GB888803156A GB8803156D0 (en) 1988-02-11 1988-02-11 Process for thermal cracking of residual hydrocarbon oils
NL8803156 1988-12-23

Publications (2)

Publication Number Publication Date
KR890013163A true KR890013163A (ko) 1989-09-21
KR970010860B1 KR970010860B1 (ko) 1997-07-01

Family

ID=10631518

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019890001594A Expired - Fee Related KR970010860B1 (ko) 1988-02-11 1989-02-09 잔류 탄화수소유의 열 분해 방법 및 이에 의해 생산된 탄화수소유

Country Status (12)

Country Link
US (1) US4938862A (ko)
EP (1) EP0328216B1 (ko)
JP (1) JP2588772B2 (ko)
KR (1) KR970010860B1 (ko)
CN (1) CN1020626C (ko)
AT (1) ATE69256T1 (ko)
AU (1) AU606779B2 (ko)
CA (1) CA1320467C (ko)
DE (1) DE68900393D1 (ko)
ES (1) ES2025838T3 (ko)
GB (1) GB8803156D0 (ko)
GR (1) GR3003193T3 (ko)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8828335D0 (en) * 1988-12-05 1989-01-05 Shell Int Research Process for conversion of heavy hydrocarbonaceous feedstock
EP0779916B1 (en) * 1994-09-05 1998-12-09 Shell Internationale Researchmaatschappij B.V. Process for the thermal cracking of a residual hydrocarbon oil
FR2764300B1 (fr) * 1997-06-10 1999-07-23 Inst Francais Du Petrole Procede de conversion de fractions lourdes petrolieres comprenant une etape d'hydrodesulfuration et une etape de conversion en lit bouillonnant
CN1163572C (zh) * 1998-07-29 2004-08-25 德士古发展公司 溶剂脱沥青和气化的联合工艺
AR021966A1 (es) * 1998-12-22 2002-09-04 Texaco Development Corp Utilizacion de membranas y expansores/compresores en gasificacion
US6171473B1 (en) * 1999-04-08 2001-01-09 Abb Lummus Global Inc. Integrated residue thermal cracking and partial oxidation process
AU2001249765A1 (en) * 2000-03-30 2001-10-15 Align Technology, Inc. System and method for separating three-dimensional models
CN1333044C (zh) * 2003-09-28 2007-08-22 中国石油化工股份有限公司 一种烃油裂化方法
EP1747255A1 (en) 2004-02-02 2007-01-31 Boris Nikolaevich Ulko Process and installation for high temperature processing of heavy petroleum residues
US7964090B2 (en) * 2008-05-28 2011-06-21 Kellogg Brown & Root Llc Integrated solvent deasphalting and gasification
US8690977B2 (en) 2009-06-25 2014-04-08 Sustainable Waste Power Systems, Inc. Garbage in power out (GIPO) thermal conversion process
US9056771B2 (en) * 2011-09-20 2015-06-16 Saudi Arabian Oil Company Gasification of heavy residue with solid catalyst from slurry hydrocracking process
ES2441691B1 (es) 2013-10-21 2014-08-11 Eqtec Iberia S.L. Procedimiento para el acondicionamiento de una corriente de gas proveniente de un gasificador, craqueo termico de alquitranes y reformado con vapor y reactor empleado
KR102778733B1 (ko) * 2021-01-29 2025-03-07 주식회사 엘지화학 합성가스의 제조방법
KR102777486B1 (ko) * 2021-01-29 2025-03-10 주식회사 엘지화학 합성가스의 제조방법
KR102778727B1 (ko) * 2021-06-24 2025-03-07 주식회사 엘지화학 합성가스 및 방향족 탄화수소의 제조방법
KR102778736B1 (ko) * 2021-06-24 2025-03-07 주식회사 엘지화학 합성가스 및 방향족 탄화수소의 제조방법

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2539434A (en) * 1947-02-25 1951-01-30 Hydrocarbon Research Inc Synthesis of hydrocarbons
US2605215A (en) * 1949-01-15 1952-07-29 Texas Co Conversion of heavy carbonaceous oils to motor fuels, fuel gas, and synthesis gas
US2917532A (en) * 1957-08-13 1959-12-15 Universal Oil Prod Co Combination process for hydrotreating and synthesizing hydrocarbons
US3928170A (en) * 1971-04-01 1975-12-23 Kureha Chemical Ind Co Ltd Method for manufacturing petroleum pitch having high aromaticity
JPS5230283B2 (ko) * 1973-12-17 1977-08-06
GB1518085A (en) * 1974-08-19 1978-07-19 Shell Int Research Process for the production of hydrogen carbon monoxide and light hydrocarbon-containing gases
JPS59152992A (ja) * 1983-02-18 1984-08-31 Mitsubishi Heavy Ind Ltd 炭化水素からオレフインを製造するための熱分解法
JPS59159887A (ja) * 1983-03-03 1984-09-10 Mitsubishi Heavy Ind Ltd 炭化水素からオレフインを製造するための熱分解法
JPS6011585A (ja) * 1983-06-30 1985-01-21 Mitsubishi Heavy Ind Ltd 炭化水素から石油化学製品を製造するための熱分解法
JPS61163992A (ja) * 1985-01-16 1986-07-24 Fuji Standard Res Kk 炭素繊維用原料として好適なピツチの連続的製造方法
JPH06296589A (ja) * 1992-09-22 1994-10-25 Olympus Optical Co Ltd 医療システム

Also Published As

Publication number Publication date
GB8803156D0 (en) 1988-03-09
EP0328216B1 (en) 1991-11-06
ES2025838T3 (es) 1992-04-01
US4938862A (en) 1990-07-03
EP0328216A1 (en) 1989-08-16
KR970010860B1 (ko) 1997-07-01
JPH01252696A (ja) 1989-10-09
CN1020626C (zh) 1993-05-12
ATE69256T1 (de) 1991-11-15
CN1036787A (zh) 1989-11-01
DE68900393D1 (de) 1991-12-12
AU606779B2 (en) 1991-02-14
CA1320467C (en) 1993-07-20
GR3003193T3 (en) 1993-02-17
JP2588772B2 (ja) 1997-03-12
AU2979889A (en) 1989-08-17

Similar Documents

Publication Publication Date Title
KR890013163A (ko) 잔류 탄화수소유의 열 분해 방법 및 이에 의해 생산된 탄화수소유
US3676519A (en) Quench process
US3594304A (en) Thermal liquefaction of coal
US4778585A (en) Two-stage pyrolysis of coal for producing liquid hydrocarbon fuels
CA2081773A1 (en) Method using hydrogen donor diluent for upgrading steam cracker tars
US3850738A (en) Bituminous coal liquefaction process
KR960701970A (ko) 고물 또는 폐 플라스틱 재료를 처리하기 위한 방법
US4216074A (en) Dual delayed coking of coal liquefaction product
US4161442A (en) Processing of tar sands
US4003821A (en) Process for production of hydrocarbon liquid from oil shale
US4427526A (en) Process for the production of hydrogenated aromatic compounds and their use
US4552649A (en) Fluid coking with quench elutriation using industrial sludge
US4325803A (en) Process for hydrogenation/extraction of organics contained in rock
US4057487A (en) Fluid coking process
US2763701A (en) Production of indene
US4405437A (en) Process for coal liquefaction employing a superior coal liquefaction process solvent
Sinag et al. Comparison of retorting and supercritical extraction techniques on gaining liquid products from Goynuk oil shale (Turkey)
KR870008995A (ko) 디이젤 연료 제조방법
KR880000552A (ko) 중금속 및 황이 많은 원유 잔사로부터 종래의 연료유와 경질제품을 제조하는 방법
US4244805A (en) Liquid yield from pyrolysis of coal liquefaction products
KR850006226A (ko) 지연 코우크스화법에 있어 생성물의 수율을 증가시키는 방법
US1863670A (en) Production of viscous oils and hydrocarbon products of low boiling point
EP0414483B1 (en) Molecular restructuring catalyst
JPS60163996A (ja) 重質炭化水素の熱分解方法
MX2022014654A (es) Procesos para mejorar el rendimiento de la conversión posterior de aceites.

Legal Events

Date Code Title Description
PA0109 Patent application

Patent event code: PA01091R01D

Comment text: Patent Application

Patent event date: 19890209

PG1501 Laying open of application
A201 Request for examination
PA0201 Request for examination

Patent event code: PA02012R01D

Patent event date: 19940128

Comment text: Request for Examination of Application

Patent event code: PA02011R01I

Patent event date: 19890209

Comment text: Patent Application

E902 Notification of reason for refusal
PE0902 Notice of grounds for rejection

Comment text: Notification of reason for refusal

Patent event date: 19970130

Patent event code: PE09021S01D

G160 Decision to publish patent application
PG1601 Publication of registration
E701 Decision to grant or registration of patent right
PE0701 Decision of registration

Patent event code: PE07011S01D

Comment text: Decision to Grant Registration

Patent event date: 19970911

GRNT Written decision to grant
PR0701 Registration of establishment

Comment text: Registration of Establishment

Patent event date: 19971211

Patent event code: PR07011E01D

PR1002 Payment of registration fee

Payment date: 19971211

End annual number: 3

Start annual number: 1

PR1001 Payment of annual fee

Payment date: 20000602

Start annual number: 4

End annual number: 4

PR1001 Payment of annual fee

Payment date: 20010526

Start annual number: 5

End annual number: 5

PR1001 Payment of annual fee

Payment date: 20020522

Start annual number: 6

End annual number: 6

PR1001 Payment of annual fee

Payment date: 20030528

Start annual number: 7

End annual number: 7

PR1001 Payment of annual fee

Payment date: 20040726

Start annual number: 8

End annual number: 8

PR1001 Payment of annual fee

Payment date: 20050812

Start annual number: 9

End annual number: 9

PR1001 Payment of annual fee

Payment date: 20060814

Start annual number: 10

End annual number: 10

PR1001 Payment of annual fee

Payment date: 20071128

Start annual number: 11

End annual number: 11

FPAY Annual fee payment

Payment date: 20081124

Year of fee payment: 12

PR1001 Payment of annual fee

Payment date: 20081124

Start annual number: 12

End annual number: 12

LAPS Lapse due to unpaid annual fee
PC1903 Unpaid annual fee

Termination category: Default of registration fee

Termination date: 20101110