ES2139242T3 - Procedimiento para separar acidos esencialmente naftenicos de un aceite hidrocarbonado. - Google Patents

Procedimiento para separar acidos esencialmente naftenicos de un aceite hidrocarbonado.

Info

Publication number
ES2139242T3
ES2139242T3 ES95932243T ES95932243T ES2139242T3 ES 2139242 T3 ES2139242 T3 ES 2139242T3 ES 95932243 T ES95932243 T ES 95932243T ES 95932243 T ES95932243 T ES 95932243T ES 2139242 T3 ES2139242 T3 ES 2139242T3
Authority
ES
Spain
Prior art keywords
pct
procedure
hydrocarbon oil
acids
sec
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.)
Expired - Lifetime
Application number
ES95932243T
Other languages
English (en)
Inventor
Knut Grande
Carsten Sorlie
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Equinor ASA
Original Assignee
Den Norske Stats Oljeselskap AS
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 Den Norske Stats Oljeselskap AS filed Critical Den Norske Stats Oljeselskap AS
Application granted granted Critical
Publication of ES2139242T3 publication Critical patent/ES2139242T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C

Abstract

UN PROCEDIMIENTO PARA ELIMINAR ESENCIALMENTE ACIDOS NAFTENICOS DE UN ACEITE CRUDO QUE NO HA SIDO PREVIAMENTE FRACCIONADO MEDIANTE DESTILACION, O DEL QUE SE HA DESTILADO UNA FRACCION NAFTA. EL ACEITE CRUDO ES HIDROGENADO A 1-50 BARS Y 100-300 (GRADOS) C SOBRE UN CATALIZADOR DEL TIPO UTILIZADO PARA HIDROGENACION DE ACEITES RESIDUALES ATMOSFERICOS. COMO CATALIZADOR, SE UTILIZA ESPECIALMENTE NI-MO O NI-CO DEPOSITADO EN ALUMINA COMO UN MATERIAL PORTADOR.
ES95932243T 1994-08-29 1995-08-29 Procedimiento para separar acidos esencialmente naftenicos de un aceite hidrocarbonado. Expired - Lifetime ES2139242T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NO943188A NO303837B1 (no) 1994-08-29 1994-08-29 FremgangsmÕte for Õ fjerne hovedsakelig naftensyrer fra en hydrokarbonolje

Publications (1)

Publication Number Publication Date
ES2139242T3 true ES2139242T3 (es) 2000-02-01

Family

ID=19897347

Family Applications (1)

Application Number Title Priority Date Filing Date
ES95932243T Expired - Lifetime ES2139242T3 (es) 1994-08-29 1995-08-29 Procedimiento para separar acidos esencialmente naftenicos de un aceite hidrocarbonado.

Country Status (12)

Country Link
US (1) US6063266A (es)
EP (1) EP0778873B1 (es)
CN (1) CN1051569C (es)
AT (1) ATE187197T1 (es)
AU (1) AU3534695A (es)
BR (1) BR9508678A (es)
CA (1) CA2198623C (es)
DE (1) DE69513669T2 (es)
ES (1) ES2139242T3 (es)
MX (1) MX9701483A (es)
NO (1) NO303837B1 (es)
WO (1) WO1996006899A1 (es)

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CN1894372A (zh) * 2003-12-19 2007-01-10 国际壳牌研究有限公司 生产原油产品的系统,方法和催化剂
US7648625B2 (en) * 2003-12-19 2010-01-19 Shell Oil Company Systems, methods, and catalysts for producing a crude product
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US20070012595A1 (en) * 2003-12-19 2007-01-18 Brownscombe Thomas F Methods for producing a total product in the presence of sulfur
KR101162944B1 (ko) 2003-12-19 2012-07-06 쉘 인터내셔날 리써취 마트샤피지 비.브이. 원유 생성물을 제조하기 위한 시스템, 방법 및 촉매
CA2455011C (en) * 2004-01-09 2011-04-05 Suncor Energy Inc. Bituminous froth inline steam injection processing
CA2455149C (en) * 2004-01-22 2006-04-11 Suncor Energy Inc. In-line hydrotreatment process for low tan synthetic crude oil production from oil sand
TW200602591A (en) * 2004-07-08 2006-01-16 hong-yang Chen Gas supply device by gasifying burnable liquid
TWI415930B (zh) * 2005-04-06 2013-11-21 Shell Int Research 減少液態含烴原料總酸值（ｔａｎ）的方法
CA2604009A1 (en) * 2005-04-11 2006-10-19 Opinder Kishan Bhan Method and catalyst for producing a crude product having a reduced nitrogen content
KR20070120595A (ko) * 2005-04-11 2007-12-24 쉘 인터내셔날 리써취 마트샤피지 비.브이. 원유 생성물을 제조하기 위한 시스템, 방법 및 촉매
CA2604006A1 (en) 2005-04-11 2006-10-19 Shell International Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced nitroge content
BRPI0610670B1 (pt) * 2005-04-11 2016-01-19 Shell Int Research método para produzir um produto bruto, catalisador para produzir um produto bruto, e, método para fabricar um catalisador
WO2007149921A1 (en) * 2006-06-22 2007-12-27 Shell Oil Company Methods for producing a crude product from selected feed
US20070295646A1 (en) * 2006-06-22 2007-12-27 Bhan Opinder K Method for producing a crude product with a long-life catalyst
WO2007149917A1 (en) * 2006-06-22 2007-12-27 Shell Oil Company Methods for producing a total product with selective hydrocarbon production
US20080135449A1 (en) 2006-10-06 2008-06-12 Opinder Kishan Bhan Methods for producing a crude product
CN101240188B (zh) * 2007-02-09 2011-05-18 中国石油化工股份有限公司 一种含酸烃油的加工方法
US20090107925A1 (en) * 2007-10-31 2009-04-30 Chevron U.S.A. Inc. Apparatus and process for treating an aqueous solution containing biological contaminants
US20100155304A1 (en) * 2008-12-23 2010-06-24 Her Majesty The Queen In Right Of Canada As Represented Treatment of hydrocarbons containing acids
US20100206772A1 (en) * 2009-02-18 2010-08-19 Marathon Petroleum Company Llc Process for the fractionation of diluted bitumen for use in light sweet refinery
US8137565B2 (en) * 2009-05-27 2012-03-20 Conocophillips Company Naphthenic acid removal and conversion
NZ618202A (en) * 2009-07-06 2014-11-28 Halosource Inc Dual polymer system for water recovery and separation of suspended solids from aqueous media
CN102443417B (zh) * 2010-10-13 2014-03-05 中国石油化工股份有限公司 一种高酸烃油的加氢处理方法
KR101898289B1 (ko) * 2011-01-10 2018-09-13 에스케이이노베이션 주식회사 탄화수소류 유분 내의 유기산을 저감하는 방법
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KR101916207B1 (ko) 2011-07-29 2018-11-08 사우디 아라비안 오일 컴퍼니 정제 공급원료 내의 총 산가를 감소시키는 방법
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CN102492461A (zh) * 2011-11-14 2012-06-13 中国海洋石油总公司 一种馏分油加氢脱酸的方法
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Also Published As

Publication number Publication date
EP0778873A1 (en) 1997-06-18
US6063266A (en) 2000-05-16
CA2198623C (en) 2000-10-24
BR9508678A (pt) 1997-12-23
NO303837B1 (no) 1998-09-07
MX9701483A (es) 1998-02-28
CN1164867A (zh) 1997-11-12
ATE187197T1 (de) 1999-12-15
EP0778873B1 (en) 1999-12-01
CA2198623A1 (en) 1996-03-07
NO943188D0 (no) 1994-08-29
AU3534695A (en) 1996-03-22
DE69513669T2 (de) 2000-04-06
DE69513669D1 (de) 2000-01-05
WO1996006899A1 (en) 1996-03-07
CN1051569C (zh) 2000-04-19
NO943188L (no) 1996-03-01

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