KR970027273A - 윤활 기재 오일의 제조 방법 - Google Patents

윤활 기재 오일의 제조 방법 Download PDF

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Publication number
KR970027273A
KR970027273A KR1019960059633A KR19960059633A KR970027273A KR 970027273 A KR970027273 A KR 970027273A KR 1019960059633 A KR1019960059633 A KR 1019960059633A KR 19960059633 A KR19960059633 A KR 19960059633A KR 970027273 A KR970027273 A KR 970027273A
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South Korea
Prior art keywords
dewaxing
hydroconversion
process according
base oil
fischer
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KR1019960059633A
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English (en)
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KR100457182B1 (ko
Inventor
데이비드 브루스 세루티
제임스 에이 애드킨스
삐에르 그랑발레
로랑 조르쥬 우브
알렉상드르 베르토 장-마리
로베르 베르나르드 게르망 길버트
회크 아렌드
마리아 페트루스 얀센 마르티누스
Original Assignee
채스킨 제이 엘
제네랄 일렉트릭 캄파니
알베르투스 빌헬무스 요아네스 쩨스트라텐
셀 인터나쵸나아레 레사아치 마아츠샤피 비이.브이.
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Publication of KR970027273A publication Critical patent/KR970027273A/ko
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Publication of KR100457182B1 publication Critical patent/KR100457182B1/ko

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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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/043—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a change in the structural skeleton
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/10—Lubricating oil
    • 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

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  • 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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Lubricants (AREA)

Abstract

(a) Fischer-Tropsch 왁스 공급물을 하이드로전환 조건하에서 하이드로전환 촉매와 접촉시키고, (b) 단계 (a)에서 수득된 하이드로전환 유출물을 적어도 하나의 경량성 분획과 중량성 분획을 분리시킨 다음, (c) 중량성 분획을 탈랍하여 기재 오일을 수득하는 단계를 포함하는 적어도 50℃의 응고점 및 90wt%의 비점과 10wt% 비점사이의 차이(T90-T10)가 40 내지 150℃범위인 비점을 갖는 Fischer-Tropsch 왁스 공급물로부터 적어도 150의 VI를 갖는 윤활 기재 오일의 제조 방법.

Description

윤활 기재 오일의 제조 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (10)

  1. (a) Fischer-Tropsch 왁스 공급물을 하이드로전환 조건하에서 하이드로전환 촉매와 접촉시키고, (b) 단계 (a)에서 수득된 하이드로전환 유출물을 적어도 하나의 경량성 분획과 중량성 분획을 분리시킨 다음, (c) 중량성 분획을 탈랍하여 기재 오일을 수득하는 단계를 포함하는 적어도 50℃의 응고점 및 90wt%의 비점과 10wt% 비점사이의 차이(T90-T10)가 40 내지 150℃범위인 비점을 갖는 Fischer-Tropsch 왁스 공급물로부터 적어도 150의 VI를 갖는 윤활 기재 오일의 제조 방법.
  2. 제1항에 있어서, T90-T10이 50 내지 130℃ 범위인 방법.
  3. 제1항 또는 2항에 있어서, Fischer-Tropsch 왁스 공급물이 55 내지 150℃, 바람직하게는 60 내지 120℃ 범위의 응고점을 갖는 방법.
  4. 제1항 내지 3항 중 어느 한 항에 있어서, 하이드로전환 촉매가 내화성 산화물 담체상에 지지된 수소화 성분을 포함하는 방법.
  5. 제4항에 있어서, 하이드로전환 촉매가 수소화 성분으로서 백금 및/또는 팔라듐을 포함하는 방법.
  6. 제5항에 있어서, 하이드로전환 촉매가 무정형 실리카-알루미나 담체상에 지지된 백금 및 팔라듐을 포함하는 방법.
  7. 제4항에 있어서, 하이드로전환 촉매가 수소화 성분으로서 적어도 하나의 ⅥB족 금속, 바람직하게는 텅스텐 및 적어도 하나의 Ⅷ족 비귀금속, 바람직하게는 니켈을 포함하는 방법.
  8. 제1항 내지 7항 중 어느 한 항에 있어서, 중량성 분획이 단계 (b)에서 350 내지 420℃의 유효 절단점에서 수득되는 방법.
  9. 제1항 내지 8항 중 어느 한 항에 있어서, 단계 (c)에서의 탈랍이 용매 탈랍에 의해 수행되는 방법.
  10. 제1항 내지 8항 중 어느 한 항에 있어서, 단계 (c)에서의 탈랍이 촉매적 탈랍에 의해 수행되는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019960059633A 1995-11-28 1996-11-26 윤활 기재 오일의 제조 방법 KR100457182B1 (ko)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
EP95402515.1 1995-11-09
US08/555,672 1995-11-13
EP95402713 1995-11-28
EP95402713.2 1995-11-28

Publications (2)

Publication Number Publication Date
KR970027273A true KR970027273A (ko) 1997-06-24
KR100457182B1 KR100457182B1 (ko) 2005-04-19

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KR1019960059633A KR100457182B1 (ko) 1995-11-28 1996-11-26 윤활 기재 오일의 제조 방법

Country Status (11)

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JP (1) JP3986107B2 (ko)
KR (1) KR100457182B1 (ko)
CN (1) CN1089794C (ko)
AU (1) AU705415B2 (ko)
CA (1) CA2191290C (ko)
DE (2) DE69633549T2 (ko)
DZ (1) DZ2129A1 (ko)
MY (1) MY114570A (ko)
SG (1) SG74001A1 (ko)
TW (1) TW416981B (ko)
ZA (1) ZA969906B (ko)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6103099A (en) * 1998-09-04 2000-08-15 Exxon Research And Engineering Company Production of synthetic lubricant and lubricant base stock without dewaxing
NL1015036C2 (nl) * 1999-04-29 2001-02-12 Inst Francais Du Petrole Flexibel proces voor de productie van basisoliÙn en gemiddelde destillatieproducten met een omzetting-hydro-isomerisatie gevolgd door een katalytische ontparaffinering.
AR032930A1 (es) * 2001-03-05 2003-12-03 Shell Int Research Procedimiento para preparar un aceite de base lubricante y gas oil
AR032941A1 (es) * 2001-03-05 2003-12-03 Shell Int Research Un procedimiento para preparar un aceite base lubricante y aceite base obtenido, con sus diversas utilizaciones
JP4674342B2 (ja) * 2002-06-26 2011-04-20 昭和シェル石油株式会社 潤滑油組成物
JP4808962B2 (ja) * 2002-07-19 2011-11-02 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ エキステンダー油含有シリコンゴム組成物及び該エキステンダー油の製造方法
US6703353B1 (en) * 2002-09-04 2004-03-09 Chevron U.S.A. Inc. Blending of low viscosity Fischer-Tropsch base oils to produce high quality lubricating base oils
US7125818B2 (en) * 2002-10-08 2006-10-24 Exxonmobil Research & Engineering Co. Catalyst for wax isomerate yield enhancement by oxygenate pretreatment
US20040129603A1 (en) * 2002-10-08 2004-07-08 Fyfe Kim Elizabeth High viscosity-index base stocks, base oils and lubricant compositions and methods for their production and use
US7132042B2 (en) * 2002-10-08 2006-11-07 Exxonmobil Research And Engineering Company Production of fuels and lube oils from fischer-tropsch wax
US7704379B2 (en) * 2002-10-08 2010-04-27 Exxonmobil Research And Engineering Company Dual catalyst system for hydroisomerization of Fischer-Tropsch wax and waxy raffinate
US20040154958A1 (en) * 2002-12-11 2004-08-12 Alexander Albert Gordon Functional fluids having low brookfield viscosity using high viscosity-index base stocks, base oils and lubricant compositions, and methods for their production and use
US6962651B2 (en) * 2003-03-10 2005-11-08 Chevron U.S.A. Inc. Method for producing a plurality of lubricant base oils from paraffinic feedstock
US20050077208A1 (en) * 2003-10-14 2005-04-14 Miller Stephen J. Lubricant base oils with optimized branching
US8137531B2 (en) * 2003-11-05 2012-03-20 Chevron U.S.A. Inc. Integrated process for the production of lubricating base oils and liquid fuels from Fischer-Tropsch materials using split feed hydroprocessing
JP6080489B2 (ja) * 2005-01-07 2017-02-15 Ｊｘエネルギー株式会社 潤滑油基油
CN102911726B (zh) * 2011-08-01 2015-04-15 中国石油化工股份有限公司 高粘度指数润滑油基础油的生产方法
CN103102946B (zh) * 2011-11-10 2015-07-22 中国石油化工股份有限公司 一种生产轻质润滑油基础油和重质润滑油基础油的方法
CN103773476B (zh) * 2012-10-24 2015-06-17 中国石油化工股份有限公司 一种加氢裂化-异构脱蜡生产高粘度指数润滑油基础油方法
CN103773465B (zh) * 2012-10-24 2015-04-15 中国石油化工股份有限公司 一种组合工艺生产高粘度指数润滑油基础油的方法
CN103773466B (zh) * 2012-10-24 2015-06-17 中国石油化工股份有限公司 加氢裂化-异构脱蜡组合生产润滑油基础油方法

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US4943672A (en) * 1987-12-18 1990-07-24 Exxon Research And Engineering Company Process for the hydroisomerization of Fischer-Tropsch wax to produce lubricating oil (OP-3403)
NO885605L (no) * 1987-12-18 1989-06-19 Exxon Research Engineering Co Fremgangsmaate for fremstilling av smoereolje.
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Also Published As

Publication number Publication date
JP3986107B2 (ja) 2007-10-03
DE69633549T2 (de) 2005-11-17
JPH09221685A (ja) 1997-08-26
DZ2129A1 (fr) 2002-07-23
CN1167811A (zh) 1997-12-17
MY114570A (en) 2002-11-30
TW416981B (en) 2001-01-01
KR100457182B1 (ko) 2005-04-19
ZA969906B (en) 1997-05-28
AU7198896A (en) 1997-06-05
DE69635320D1 (de) 2005-11-24
CA2191290A1 (en) 1997-05-29
CN1089794C (zh) 2002-08-28
CA2191290C (en) 2006-09-26
DE69633549D1 (de) 2004-11-11
AU705415B2 (en) 1999-05-20
SG74001A1 (en) 2000-07-18
DE69635320T2 (de) 2006-04-20

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