DK135175B - Fremgangsmåde til hydroafsvovling af råolie eller reduceret råolie. - Google Patents

Fremgangsmåde til hydroafsvovling af råolie eller reduceret råolie.

Info

Publication number
DK135175B
DK135175B DK565169AA DK565169A DK135175B DK 135175 B DK135175 B DK 135175B DK 565169A A DK565169A A DK 565169AA DK 565169 A DK565169 A DK 565169A DK 135175 B DK135175 B DK 135175B
Authority
DK
Denmark
Prior art keywords
crude oil
hydrodesulfurization
reduced
reduced crude
oil
Prior art date
Application number
DK565169AA
Other languages
Danish (da)
English (en)
Other versions
DK135175C (de
Inventor
Edgar Carlson
Alfred Mathias Henke
William Richard Lehrian
Joel Drexler Mckinney
Kirk Joseph Metzger
Original Assignee
Gulf Research Development 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 Gulf Research Development Co filed Critical Gulf Research Development Co
Publication of DK135175B publication Critical patent/DK135175B/da
Application granted granted Critical
Publication of DK135175C publication Critical patent/DK135175C/da

Links

Classifications

    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
    • B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/023—Details
    • B01J2208/024—Particulate material
    • B01J2208/025—Two or more types of catalyst
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Catalysts (AREA)
DK565169AA 1968-10-25 1969-10-24 Fremgangsmåde til hydroafsvovling af råolie eller reduceret råolie. DK135175B (da)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US77062568A 1968-10-25 1968-10-25

Publications (2)

Publication Number Publication Date
DK135175B true DK135175B (da) 1977-03-14
DK135175C DK135175C (de) 1977-08-22

Family

ID=25089199

Family Applications (1)

Application Number Title Priority Date Filing Date
DK565169AA DK135175B (da) 1968-10-25 1969-10-24 Fremgangsmåde til hydroafsvovling af råolie eller reduceret råolie.

Country Status (6)

Country Link
US (1) US3562800A (de)
JP (2) JPS495202B1 (de)
DE (1) DE1953398A1 (de)
DK (1) DK135175B (de)
GB (1) GB1274920A (de)
NL (1) NL162125B (de)

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4113661A (en) * 1973-08-09 1978-09-12 Chevron Research Company Method for preparing a hydrodesulfurization catalyst
US4341625A (en) * 1973-08-09 1982-07-27 Chevron Research Company Method for preparing a catalyst carrier, a catalyst containing the carrier, and a hydrocarbon hydrodesulfurization process using the catalyst
US3859203A (en) * 1974-01-22 1975-01-07 Gulf Research Development Co Removal of sulfur from residual oil with downstream ammonia addition
US3860511A (en) * 1974-01-22 1975-01-14 Gulf Research Development Co Two-stage residual oil hydrodesulfurication process with ammonia addition
US3859204A (en) * 1974-01-22 1975-01-07 Gulf Research Development Co Residual oil hydrodesulfurization process by catalyst pretreatment and ammonia addition
US3859202A (en) * 1974-01-22 1975-01-07 Gulf Research Development Co First stage residual oil hydrodesulfurization with ammonia addition
US4179357A (en) * 1978-07-27 1979-12-18 Uop Inc. Selective hydrocracking process for middle distillate
US4615796A (en) * 1981-10-29 1986-10-07 Chevron Research Company Method for contacting solids-containing feeds in a layered bed reactor
US4431526A (en) * 1982-07-06 1984-02-14 Union Oil Company Of California Multiple-stage hydroprocessing of hydrocarbon oil
NL8901239A (nl) * 1989-05-18 1990-12-17 Meern Bv Engelhard De Katalysator voor hydrogenering en/of dehydrogenering.
US5039396A (en) * 1990-07-30 1991-08-13 Texaco Inc. Hydrotreater feed/effluent heat exchange
US8062521B2 (en) * 1998-05-29 2011-11-22 Crystaphase Products, Inc. Filtering medium and method for contacting solids-containing feeds for chemical reactors
US7722832B2 (en) 2003-03-25 2010-05-25 Crystaphase International, Inc. Separation method and assembly for process streams in component separation units
US10744426B2 (en) 2015-12-31 2020-08-18 Crystaphase Products, Inc. Structured elements and methods of use
US10054140B2 (en) 2016-02-12 2018-08-21 Crystaphase Products, Inc. Use of treating elements to facilitate flow in vessels
US12071592B2 (en) 2017-02-12 2024-08-27 Magēmā Technology LLC Multi-stage process and device utilizing structured catalyst beds and reactive distillation for the production of a low sulfur heavy marine fuel oil
US12025435B2 (en) 2017-02-12 2024-07-02 Magēmã Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil
US10604709B2 (en) 2017-02-12 2020-03-31 Magēmā Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials
US10655074B2 (en) 2017-02-12 2020-05-19 Mag{hacek over (e)}m{hacek over (a)} Technology LLC Multi-stage process and device for reducing environmental contaminates in heavy marine fuel oil
US11788017B2 (en) 2017-02-12 2023-10-17 Magëmã Technology LLC Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil
EP4076719A1 (de) 2019-12-20 2022-10-26 Crystaphase Products Inc. Rücksättigung von gas in einen flüssigkeitszufuhrstrom
CA3192003A1 (en) 2020-09-09 2022-03-17 Crystaphase Products, Inc. Process vessel entry zones

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS495202A (de) * 1972-04-29 1974-01-17

Also Published As

Publication number Publication date
NL162125B (nl) 1979-11-15
GB1274920A (en) 1972-05-17
NL6916016A (de) 1970-04-28
DE1953398A1 (de) 1970-05-06
DK135175C (de) 1977-08-22
JPS5615755B1 (de) 1981-04-11
US3562800A (en) 1971-02-09
JPS495202B1 (de) 1974-02-06

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