KR910012211A - 왁스의 하이드로이성화 방법 - Google Patents

왁스의 하이드로이성화 방법 Download PDF

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Publication number
KR910012211A
KR910012211A KR1019900021747A KR900021747A KR910012211A KR 910012211 A KR910012211 A KR 910012211A KR 1019900021747 A KR1019900021747 A KR 1019900021747A KR 900021747 A KR900021747 A KR 900021747A KR 910012211 A KR910012211 A KR 910012211A
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KR
South Korea
Prior art keywords
wax
binder
hydroisomerization
oxide
layered
Prior art date
Application number
KR1019900021747A
Other languages
English (en)
Inventor
쥬니어 토마스 프랜시스 데그난
오이겐 랜디스 미카엘
Original Assignee
알렉산더 제이. 맥킬로프
모빌오일 코퍼레이션
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 알렉산더 제이. 맥킬로프, 모빌오일 코퍼레이션 filed Critical 알렉산더 제이. 맥킬로프
Publication of KR910012211A publication Critical patent/KR910012211A/ko

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M1/00—Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/049—Pillared clays
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
    • C10G45/64—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves

Abstract

내용 없음

Description

왁스의 하이드로이성화 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 두 촉매를 가지고 석유왁스 공급액을 히이드로 이성화할때 사용할 경우 반응기 온도-윤활유 수율의 관계를 보여주는 그래프.

Claims (6)

  1. 석유왁스 또는 합성 파라핀 왁스를 그의 유동점을 줄이기 위해 인터스패틱 중합 산화물을 함유한 층상 티타네이트로 이루어져 있고 또한 Fe, Co, Ni, Ru, Rh, Pd, Os, Ir, 및 Pt중에서 선택한 수소화성분으로 추가로 이루어진 촉매와 충분한 하이드로 이성화 조건에서 접촉하여 하이드로 이성화하는 방법.
  2. 제1항에서, 하이드로 이성화조건이 1482-20790kPa의 수소분압, 232℃-454℃의 온도, 0.05hr-1-10hr-1의 LHSV 및 89-1780v/v의 수소순환속도인 방법.
  3. 제2항에서, 수소화성분이 Pt인 방법.
  4. 제3항에서, 중합 산화물이 실리카인 방법.
  5. 제1항에서, 촉매가 층상 티타네아트용 바인더로 추가로 이루어진 방법.
  6. 제5항에서, 바인더가 알루미나인 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019900021747A 1989-12-29 1990-12-26 왁스의 하이드로이성화 방법 KR910012211A (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US07/459,154 US4995962A (en) 1989-12-29 1989-12-29 Wax hydroisomerization process
US459154 1989-12-29

Publications (1)

Publication Number Publication Date
KR910012211A true KR910012211A (ko) 1991-08-07

Family

ID=23823633

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019900021747A KR910012211A (ko) 1989-12-29 1990-12-26 왁스의 하이드로이성화 방법

Country Status (6)

Country Link
US (1) US4995962A (ko)
EP (1) EP0435619A1 (ko)
JP (1) JPH04136092A (ko)
KR (1) KR910012211A (ko)
AU (1) AU627969B2 (ko)
CA (1) CA2032891A1 (ko)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5362378A (en) * 1992-12-17 1994-11-08 Mobil Oil Corporation Conversion of Fischer-Tropsch heavy end products with platinum/boron-zeolite beta catalyst having a low alpha value
US6695965B1 (en) 2000-04-04 2004-02-24 Exxonmobil Research And Engineering Company Process for adjusting the hardness of Fischer-Tropsch wax by blending
US6776898B1 (en) * 2000-04-04 2004-08-17 Exxonmobil Research And Engineering Company Process for softening fischer-tropsch wax with mild hydrotreating
DE10126516A1 (de) * 2001-05-30 2002-12-05 Schuemann Sasol Gmbh Verfahren zur Herstellung von mikrokristallinen Paraffinen
DE60214724T2 (de) * 2001-06-15 2007-09-06 Shell Internationale Research Maatschappij B.V. Verfahren zur herstellung eines mikrokristallinen wachses
DE10256431A1 (de) 2002-05-31 2004-01-15 SCHÜMANN SASOL GmbH Mikrokristallines Paraffin, Verfahren zur Herstellung von mikrokristallinen Paraffine und Verwendung der mikrokristallinen Paraffine
US20080260631A1 (en) 2007-04-18 2008-10-23 H2Gen Innovations, Inc. Hydrogen production process
JP5614533B2 (ja) * 2010-06-16 2014-10-29 Ｊｘ日鉱日石エネルギー株式会社 芳香族炭化水素の水素化触媒及びそれを用いた水素化方法
JP5730104B2 (ja) * 2011-03-31 2015-06-03 独立行政法人石油天然ガス・金属鉱物資源機構 担体の選別方法及び水素化処理用触媒の製造方法
CN105582987B (zh) * 2014-10-22 2018-01-16 中国石油化工股份有限公司大连石油化工研究院 一种石蜡烃择型异构化催化剂的预处理方法
CN105582985B (zh) * 2014-10-22 2018-01-16 中国石油化工股份有限公司大连石油化工研究院 一种石蜡烃择型异构化催化剂的原位预处理方法
WO2019189446A1 (ja) * 2018-03-27 2019-10-03 Ｊｘｔｇエネルギー株式会社 ワックス異性化油及びその製造方法

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3329480A (en) * 1963-10-18 1967-07-04 Union Oil Co Crystalline zircono-silicate zeolites
FR2553430B1 (fr) * 1983-10-14 1986-02-21 Shell Int Research Procede pour l'hydro-isomerisation de cires de petrole
DE3479429D1 (en) * 1983-10-14 1989-09-21 Shell Int Research Hydrocarbon conversion processes and modified refractory oxides which can be used in such processes
US4600503A (en) * 1984-12-28 1986-07-15 Mobil Oil Corporation Process for hydrotreating residual petroleum oil
US4724066A (en) * 1985-01-22 1988-02-09 Mobil Oil Corporation Composites of microporous aluminum phosphates and zeolites and conversions over these catalysts
US4612108A (en) * 1985-08-05 1986-09-16 Mobil Oil Corporation Hydrocracking process using zeolite beta

Also Published As

Publication number Publication date
AU6856590A (en) 1991-07-04
US4995962A (en) 1991-02-26
CA2032891A1 (en) 1991-06-30
JPH04136092A (ja) 1992-05-11
AU627969B2 (en) 1992-09-03
EP0435619A1 (en) 1991-07-03

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