GB1232173A - - Google Patents
Info
- Publication number
- GB1232173A GB1232173A GB1232173DA GB1232173A GB 1232173 A GB1232173 A GB 1232173A GB 1232173D A GB1232173D A GB 1232173DA GB 1232173 A GB1232173 A GB 1232173A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- feed
- support
- bed
- central tube
- 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
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
- B01J8/0207—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 flow within the bed being predominantly horizontal
-
- 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
- C10G45/22—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 hydrogen dissolved or suspended in the 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/002—Apparatus for fixed bed hydrotreatment processes
Abstract
1,232,173. Hydrodesulphurization. SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V. 18 Nov., 1969, No. 56356/69. Heading C5E. Residual oils are hydrodesulphurized while substantially in the liquid phase and containing dissolved hydrogen by radial flow through a fixed bed of catalyst. The reaction is carried out at 350-475‹ C. and 50-350 kg./cm.<SP>2</SP> using a catalyst such as Ni and/or Co together with W or Mo as the metals, oxides or sulphides on an oxidic support, e.g. alumina which can contain boron phosphate, phosphorus, F or Cl, or on a support of zeolite Y. Suitable feeds are atmospheric or vacuum residues which can have been deasphalted or catalytically hydrofined, black oils, visbreaker effluents and tar sand oil. 5-30 volumes of the desulphurized product containing 0À05-2À5 wt. per cent H 2 S can be recycled per volume of fresh feed. The cylindrical radial flow reactor 35 comprises a perforated catalyst support 45 through which the liquid feed from the inlet 36a passes into the catalyst bed 47. The feed passes from the catalyst bed into the perforated central tube 39 and out of the exit 37a. The spaces 53 and 54 can be filled with ceramic or aluminium balls, glass beads and/or marble chips and space 53 serves to dissolve the hydrogen in the liquid feed. Alternatively the feed can be passed through the bed from the central tube 39 and out through the catalyst support 45 and the passage 36a.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB5635669 | 1969-11-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1232173A true GB1232173A (en) | 1971-05-19 |
Family
ID=10476415
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1232173D Expired GB1232173A (en) | 1969-11-18 | 1969-11-18 |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1232173A (en) |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998059019A1 (en) * | 1997-06-24 | 1998-12-30 | Process Dynamics, Inc. | Two phase hydroprocessing |
WO2000018854A1 (en) * | 1998-09-29 | 2000-04-06 | Canadian Environmental Equipment & Engineering Technologies, Inc. | Process for treating crude oil using hydrogen in a special unit |
WO2003091363A1 (en) * | 2002-04-23 | 2003-11-06 | Bp Oil International Limited | Purification process |
EP1394237A1 (en) * | 1997-06-24 | 2004-03-03 | Process Dynamics, Inc. | Two phase hydroprocessing |
WO2005061669A3 (en) * | 2003-12-19 | 2006-01-05 | Shell Oil Co | Systems, methods, and catalysts for producing a crude product |
WO2006021822A1 (en) * | 2004-08-23 | 2006-03-02 | Thalesnano Zrt. | A cartridge reactor for a flow-type laboratory hydrogenation apparatus |
US7291257B2 (en) | 1997-06-24 | 2007-11-06 | Process Dynamics, Inc. | Two phase hydroprocessing |
WO2009013971A1 (en) * | 2007-07-24 | 2009-01-29 | Idemitsu Kosan Co., Ltd. | Hydrorefining method for hydrocarbon oil |
US7569136B2 (en) | 1997-06-24 | 2009-08-04 | Ackerson Michael D | Control system method and apparatus for two phase hydroprocessing |
US7648625B2 (en) | 2003-12-19 | 2010-01-19 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7678264B2 (en) | 2005-04-11 | 2010-03-16 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7745369B2 (en) | 2003-12-19 | 2010-06-29 | Shell Oil Company | Method and catalyst for producing a crude product with minimal hydrogen uptake |
US7749374B2 (en) | 2006-10-06 | 2010-07-06 | Shell Oil Company | Methods for producing a crude product |
US7918992B2 (en) | 2005-04-11 | 2011-04-05 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US8137536B2 (en) | 2003-12-19 | 2012-03-20 | Shell Oil Company | Method for producing a crude product |
US20120103868A1 (en) * | 2010-10-28 | 2012-05-03 | E. I. Du Pont De Nemours And Company | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
US8608938B2 (en) | 2003-12-19 | 2013-12-17 | Shell Oil Company | Crude product composition |
US9096804B2 (en) | 2011-01-19 | 2015-08-04 | P.D. Technology Development, Llc | Process for hydroprocessing of non-petroleum feedstocks |
US9139782B2 (en) | 2011-02-11 | 2015-09-22 | E I Du Pont De Nemours And Company | Targeted pretreatment and selective ring opening in liquid-full reactors |
RU2575120C2 (en) * | 2010-10-28 | 2016-02-10 | Е.И. Дюпон Де Немур Энд Компани | Hydraulic treatment of heavy raw hydrocarbon deposits in liquid-filled reactors |
-
1969
- 1969-11-18 GB GB1232173D patent/GB1232173A/en not_active Expired
Cited By (48)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7291257B2 (en) | 1997-06-24 | 2007-11-06 | Process Dynamics, Inc. | Two phase hydroprocessing |
US6123835A (en) * | 1997-06-24 | 2000-09-26 | Process Dynamics, Inc. | Two phase hydroprocessing |
EP1394237A1 (en) * | 1997-06-24 | 2004-03-03 | Process Dynamics, Inc. | Two phase hydroprocessing |
US6881326B2 (en) | 1997-06-24 | 2005-04-19 | Process Dynamics, Inc. | Two phase hydroprocessing |
WO1998059019A1 (en) * | 1997-06-24 | 1998-12-30 | Process Dynamics, Inc. | Two phase hydroprocessing |
US7569136B2 (en) | 1997-06-24 | 2009-08-04 | Ackerson Michael D | Control system method and apparatus for two phase hydroprocessing |
WO2000018854A1 (en) * | 1998-09-29 | 2000-04-06 | Canadian Environmental Equipment & Engineering Technologies, Inc. | Process for treating crude oil using hydrogen in a special unit |
WO2003091363A1 (en) * | 2002-04-23 | 2003-11-06 | Bp Oil International Limited | Purification process |
US8025794B2 (en) | 2003-12-19 | 2011-09-27 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US8613851B2 (en) | 2003-12-19 | 2013-12-24 | Shell Oil Company | Crude product composition |
US8764972B2 (en) | 2003-12-19 | 2014-07-01 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7648625B2 (en) | 2003-12-19 | 2010-01-19 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7674368B2 (en) | 2003-12-19 | 2010-03-09 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7674370B2 (en) | 2003-12-19 | 2010-03-09 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US8663453B2 (en) | 2003-12-19 | 2014-03-04 | Shell Oil Company | Crude product composition |
US7736490B2 (en) | 2003-12-19 | 2010-06-15 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7745369B2 (en) | 2003-12-19 | 2010-06-29 | Shell Oil Company | Method and catalyst for producing a crude product with minimal hydrogen uptake |
US8608946B2 (en) | 2003-12-19 | 2013-12-17 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7780844B2 (en) | 2003-12-19 | 2010-08-24 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7807046B2 (en) | 2003-12-19 | 2010-10-05 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7837863B2 (en) | 2003-12-19 | 2010-11-23 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US8608938B2 (en) | 2003-12-19 | 2013-12-17 | Shell Oil Company | Crude product composition |
US7955499B2 (en) | 2003-12-19 | 2011-06-07 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7959796B2 (en) | 2003-12-19 | 2011-06-14 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
WO2005061669A3 (en) * | 2003-12-19 | 2006-01-05 | Shell Oil Co | Systems, methods, and catalysts for producing a crude product |
US8070937B2 (en) | 2003-12-19 | 2011-12-06 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US8137536B2 (en) | 2003-12-19 | 2012-03-20 | Shell Oil Company | Method for producing a crude product |
US8506794B2 (en) | 2003-12-19 | 2013-08-13 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US8241489B2 (en) | 2003-12-19 | 2012-08-14 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US8475651B2 (en) | 2003-12-19 | 2013-07-02 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
WO2006021822A1 (en) * | 2004-08-23 | 2006-03-02 | Thalesnano Zrt. | A cartridge reactor for a flow-type laboratory hydrogenation apparatus |
US7678264B2 (en) | 2005-04-11 | 2010-03-16 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US8481450B2 (en) | 2005-04-11 | 2013-07-09 | Shell Oil Company | Catalysts for producing a crude product |
US7918992B2 (en) | 2005-04-11 | 2011-04-05 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7749374B2 (en) | 2006-10-06 | 2010-07-06 | Shell Oil Company | Methods for producing a crude product |
WO2009013971A1 (en) * | 2007-07-24 | 2009-01-29 | Idemitsu Kosan Co., Ltd. | Hydrorefining method for hydrocarbon oil |
KR20140000255A (en) * | 2010-10-28 | 2014-01-02 | 이 아이 듀폰 디 네모아 앤드 캄파니 | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
US20120103868A1 (en) * | 2010-10-28 | 2012-05-03 | E. I. Du Pont De Nemours And Company | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
CN103189476A (en) * | 2010-10-28 | 2013-07-03 | 纳幕尔杜邦公司 | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
WO2012058396A3 (en) * | 2010-10-28 | 2012-10-11 | E. I. Du Pont De Nemours And Company | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
RU2575120C2 (en) * | 2010-10-28 | 2016-02-10 | Е.И. Дюпон Де Немур Энд Компани | Hydraulic treatment of heavy raw hydrocarbon deposits in liquid-filled reactors |
CN103189476B (en) * | 2010-10-28 | 2016-12-07 | 纳幕尔杜邦公司 | The hydrotreating of heavy hydrocarbon feedstocks in full liquid reactor |
US10144882B2 (en) | 2010-10-28 | 2018-12-04 | E I Du Pont De Nemours And Company | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
KR101939854B1 (en) | 2010-10-28 | 2019-01-17 | 이 아이 듀폰 디 네모아 앤드 캄파니 | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
US9096804B2 (en) | 2011-01-19 | 2015-08-04 | P.D. Technology Development, Llc | Process for hydroprocessing of non-petroleum feedstocks |
US9828552B1 (en) | 2011-01-19 | 2017-11-28 | Duke Technologies, Llc | Process for hydroprocessing of non-petroleum feedstocks |
US10961463B2 (en) | 2011-01-19 | 2021-03-30 | Duke Technologies, Llc | Process for hydroprocessing of non-petroleum feedstocks |
US9139782B2 (en) | 2011-02-11 | 2015-09-22 | E I Du Pont De Nemours And Company | Targeted pretreatment and selective ring opening in liquid-full reactors |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
CSNS | Application of which complete specification have been accepted and published, but patent is not sealed |