ES8601292A1 - Un procedimiento de hidrorrefino de una corriente de alimentacion que contiene hidrocarburos - Google Patents

Un procedimiento de hidrorrefino de una corriente de alimentacion que contiene hidrocarburos

Info

Publication number
ES8601292A1
ES8601292A1 ES536660A ES536660A ES8601292A1 ES 8601292 A1 ES8601292 A1 ES 8601292A1 ES 536660 A ES536660 A ES 536660A ES 536660 A ES536660 A ES 536660A ES 8601292 A1 ES8601292 A1 ES 8601292A1
Authority
ES
Spain
Prior art keywords
containing feed
group
molybdenum dithiocarbamate
hydrofining process
dithiocarbamate compound
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
Application number
ES536660A
Other languages
English (en)
Other versions
ES536660A0 (es
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.)
Phillips Petroleum Co
Original Assignee
Phillips Petroleum Co
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 Phillips Petroleum Co filed Critical Phillips Petroleum Co
Publication of ES8601292A1 publication Critical patent/ES8601292A1/es
Publication of ES536660A0 publication Critical patent/ES536660A0/es
Granted 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
    • 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
    • C10G45/14—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 with moving solid particles
    • C10G45/16—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 with moving solid particles suspended in the oil, e.g. slurries

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

Abstract

PROCEDIMIENTO DE HIDRORREFINO DE UNA CORRIENTE DE ALIMENTACION QUE CONTIENE HIDROCARBUROS. COMPRENDE: A) INTRODUCIR UN COMPUESTO DE DITIOCARBONATO DE MOLIBDENO SUSCEPTIBLE DE DESCOMPOSICION EN LA CORRIENTE DE ALIMENTACION DE HIDROCARBUROS PARA REDUCIR EL CONTENIDO DE MOLIBDENO ENTRE 1 Y 30 PPM; Y B) PONER EN CONTACTO A LA CORRIENTE DE ALIMENTACION DE HIDROCARBUROS QUE TIENE UN CONTENIDO DE MO ENTRE 1 Y 30 PPM CON HIDROGENO Y CON UNA COMPOSICION DE CATALIZADOR FORMADO POR UN SOPORTE Y UN PROMOTOR A UNA TEMPERATURA ENTRE 150 A 550JC BAJO UNA PRESION DE 704 KG/CM Y DURANTE 01 A 10 HORAS. EL COMPUESTO DE DITIOCARBONATO DE MOLIBDENO SE ELIGE ENTRE MO(S-SC-NRR2)NM Y MOOPSQ(S-SC-NRR2). SIENDO: R1 Y R2 H GRUPOS ALQUILO DE C 1 A 20 Y OTROS; M 1 O 2; N 3 4 5 O 6; P 0 1 O 2; Q 0 1 O 2 Y R 1 2 3 O 4 EL SOPORTE AL2O3 O SIO2 Y EL PROMOTOR UN METAL DEL GRUPO VIB O VIIB.
ES536660A 1983-10-11 1984-10-10 Un procedimiento de hidrorrefino de una corriente de alimentacion que contiene hidrocarburos Granted ES536660A0 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US54059783A 1983-10-11 1983-10-11
US06/589,362 US4612110A (en) 1983-10-11 1984-03-14 Hydrofining process for hydrocarbon containing feed streams

Publications (2)

Publication Number Publication Date
ES8601292A1 true ES8601292A1 (es) 1985-10-16
ES536660A0 ES536660A0 (es) 1985-10-16

Family

ID=27066480

Family Applications (1)

Application Number Title Priority Date Filing Date
ES536660A Granted ES536660A0 (es) 1983-10-11 1984-10-10 Un procedimiento de hidrorrefino de una corriente de alimentacion que contiene hidrocarburos

Country Status (6)

Country Link
US (1) US4612110A (es)
EP (1) EP0142033B1 (es)
AU (1) AU546943B2 (es)
CA (1) CA1245592A (es)
DE (1) DE3472416D1 (es)
ES (1) ES536660A0 (es)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2555192B1 (fr) * 1983-11-21 1987-06-12 Elf France Procede de traitement thermique de charges hydrocarbonees en presence d'additifs qui diminuent la formation de coke
US5064527A (en) * 1984-05-08 1991-11-12 Exxon Research & Engineering Company Catalytic process for hydroconversion of carbonaceous materials
US5055174A (en) * 1984-06-27 1991-10-08 Phillips Petroleum Company Hydrovisbreaking process for hydrocarbon containing feed streams
US4596654A (en) * 1985-06-24 1986-06-24 Phillips Petroleum Company Hydrofining catalysts
US4728417A (en) * 1986-07-21 1988-03-01 Phillips Petroleum Company Hydrofining process for hydrocarbon containing feed streams
US4775652A (en) * 1986-07-21 1988-10-04 Phillips Petroleum Company Hydrofining composition
US4695369A (en) * 1986-08-11 1987-09-22 Air Products And Chemicals, Inc. Catalytic hydroconversion of heavy oil using two metal catalyst
US4708784A (en) * 1986-10-10 1987-11-24 Phillips Petroleum Company Hydrovisbreaking of oils
US4853110A (en) * 1986-10-31 1989-08-01 Exxon Research And Engineering Company Method for separating arsenic and/or selenium from shale oil
US5152885A (en) * 1990-12-18 1992-10-06 Exxon Research And Engineering Company Hydrotreating process using noble metal supported catalysts
JP2010527397A (ja) * 2007-05-15 2010-08-12 ダウ グローバル テクノロジーズ インコーポレイティド コポリマー混合物
CN106459819B (zh) 2015-03-31 2021-11-09 出光兴产株式会社 润滑油组合物和降低内燃机摩擦的方法

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4243553A (en) * 1979-06-11 1981-01-06 Union Carbide Corporation Production of improved molybdenum disulfide catalysts
WO1982003226A1 (en) * 1981-03-19 1982-09-30 Beck Wayne H Immobilization of vanadia deposited on sorbent materials during treatment of carbo-metallic oils
US4430207A (en) * 1983-05-17 1984-02-07 Phillips Petroleum Company Demetallization of hydrocarbon containing feed streams

Also Published As

Publication number Publication date
CA1245592A (en) 1988-11-29
AU3386184A (en) 1985-04-18
EP0142033B1 (en) 1988-06-29
EP0142033A1 (en) 1985-05-22
AU546943B2 (en) 1985-09-26
US4612110A (en) 1986-09-16
DE3472416D1 (en) 1988-08-04
ES536660A0 (es) 1985-10-16

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Legal Events

Date Code Title Description
MM4A Patent lapsed

Effective date: 19960506