CA2093412A1 - Novel hydroconversion process employing catalyst with specified pore size distribution - Google Patents
Novel hydroconversion process employing catalyst with specified pore size distributionInfo
- Publication number
- CA2093412A1 CA2093412A1 CA002093412A CA2093412A CA2093412A1 CA 2093412 A1 CA2093412 A1 CA 2093412A1 CA 002093412 A CA002093412 A CA 002093412A CA 2093412 A CA2093412 A CA 2093412A CA 2093412 A1 CA2093412 A1 CA 2093412A1
- Authority
- CA
- Canada
- Prior art keywords
- tpv
- ang
- novel
- size distribution
- pore size
- 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.)
- Granted
Links
- 239000011148 porous material Substances 0.000 title abstract 3
- 239000003054 catalyst Substances 0.000 title 1
- 150000004706 metal oxides Chemical class 0.000 abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 238000009835 boiling Methods 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 229910044991 metal oxide Inorganic materials 0.000 abstract 1
- 229910000510 noble metal Inorganic materials 0.000 abstract 1
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
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/185—Phosphorus; Compounds thereof with iron group metals or platinum group metals
- B01J27/1853—Phosphorus; Compounds thereof with iron group metals or platinum group metals with iron, cobalt or nickel
-
- B01J35/615—
-
- B01J35/635—
-
- B01J35/66—
-
- B01J35/69—
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
Abstract
Heavy hydrocarbons are hydrotreated to increase content of components boiling below 1000°F by contact with Group VIII non-noble metal oxide and Group VI-B metal oxide on alumina having a Total Surface Area of 150-240 m2/g, a Total Pore Volume, (TPV) of 0.7-0.98, and a Pore Diameter Distribution whereby <= 20 0 of the TPV is present as primary micropores of diameter <= 100.ANG., at least about 34% of TPV is present as secondary micropores of diameter of about 100.ANG.-200.ANG., and about 26%-46% of the TPV is present as mesopores of diameter >= 200.ANG..
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/870,970 US5399259A (en) | 1992-04-20 | 1992-04-20 | Hydroconversion process employing catalyst with specified pore size distribution |
US870,970 | 1992-04-20 | ||
US95317692A | 1992-09-29 | 1992-09-29 | |
US07/953,176 | 1992-09-29 |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2093412A1 true CA2093412A1 (en) | 1993-10-21 |
CA2093412C CA2093412C (en) | 2002-12-31 |
Family
ID=27128179
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA 2093412 Expired - Lifetime CA2093412C (en) | 1992-04-20 | 1993-04-05 | Novel hydroconversion process employing catalyst with specified pore size distribution |
Country Status (2)
Country | Link |
---|---|
US (2) | US5435908A (en) |
CA (1) | CA2093412C (en) |
Families Citing this family (65)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5868923A (en) * | 1991-05-02 | 1999-02-09 | Texaco Inc | Hydroconversion process |
US5827421A (en) * | 1992-04-20 | 1998-10-27 | Texaco Inc | Hydroconversion process employing catalyst with specified pore size distribution and no added silica |
US5928499A (en) * | 1993-10-01 | 1999-07-27 | Texaco Inc | Hydroconversion process employing catalyst with specified pore size distribution, median pore diameter by surface area, and pore mode by volume |
US6015485A (en) * | 1994-05-13 | 2000-01-18 | Cytec Technology Corporation | High activity catalysts having a bimodal mesopore structure |
US5968348A (en) * | 1994-05-16 | 1999-10-19 | Texaco Inc. | Hydroconversion process employing a phosphorus loaded NiMo catalyst with specified pore size distribution |
US5817594A (en) * | 1994-11-03 | 1998-10-06 | Shell Oil Company | Catalyst and hydrotreating process |
AU1959997A (en) * | 1996-02-14 | 1997-09-02 | Texaco Development Corporation | Low pressure process for the hydroconversion of heavy hydrocarbo ns |
US6387248B2 (en) * | 1997-11-06 | 2002-05-14 | Texaco Inc. | Method of preparing a catalyst for use in the hydrotreating of high boiling hydrocarbon feedstocks |
GC0000065A (en) | 1998-09-01 | 2004-06-30 | Japan Energy Corp | Hydrocracking catalyst, producing method threof, and hydrocracking method. |
CA2320485C (en) † | 1998-12-08 | 2005-02-08 | Japan Energy Corporation | Catalyst for hydrofining and method for preparation thereof |
JP4303820B2 (en) * | 1999-01-26 | 2009-07-29 | 日本ケッチェン株式会社 | Hydrotreating catalyst and hydrotreating method |
US6933409B1 (en) | 1999-05-13 | 2005-08-23 | Symyx Technologies, Inc. | Amination of aromatic hydrocarbons and heterocyclic analogs thereof |
US6417135B1 (en) * | 1999-08-27 | 2002-07-09 | Huntsman Petrochemical Corporation | Advances in dehydrogenation catalysis |
WO2001026805A1 (en) * | 1999-10-14 | 2001-04-19 | China Petrochemical Corporation | Catalyst for hydrorefining distillate oil, its carrier and preparation thereof |
US6239066B1 (en) * | 1999-11-04 | 2001-05-29 | Shell Oil Company | Process for forming high activity catalysts |
IT1317868B1 (en) | 2000-03-02 | 2003-07-15 | Eni Spa | SUPPORTED COBALT CATALYST, PARTICULARLY USEFUL IN THE REACTION OF FISCHER-TROPSCH. |
DE60120692T2 (en) * | 2000-05-19 | 2006-10-19 | Johnson Matthey Plc | CATALYSTS WITH HIGH COBAL SURFACE |
US6508999B1 (en) | 2000-11-21 | 2003-01-21 | Shell Oil Company | Aluminum trihydroxide phase |
US6589908B1 (en) | 2000-11-28 | 2003-07-08 | Shell Oil Company | Method of making alumina having bimodal pore structure, and catalysts made therefrom |
JP4638610B2 (en) * | 2001-01-05 | 2011-02-23 | 日本ケッチェン株式会社 | Hydrotreating catalyst and hydrotreating method |
KR100398058B1 (en) * | 2001-05-18 | 2003-09-19 | 주식회사 경동도시가스 | Modified θ-alumina-supported nickel reforming catalysts and its use for producing synthesis gas from natural gas |
JP3786007B2 (en) * | 2001-05-29 | 2006-06-14 | 住友金属鉱山株式会社 | Catalyst for hydrotreating aromatic compounds in hydrocarbon oils |
JP4612229B2 (en) * | 2001-06-08 | 2011-01-12 | 日本ケッチェン株式会社 | Catalyst for hydrotreating heavy hydrocarbon oil and hydrotreating method |
US6897175B2 (en) * | 2001-10-09 | 2005-05-24 | General Electric | Catalyst and method for the alkylation of hydroxyaromatic compounds |
US6799615B2 (en) * | 2002-02-26 | 2004-10-05 | Leslie G. Smith | Tenon maker |
FR2839902B1 (en) * | 2002-05-24 | 2007-06-29 | Inst Francais Du Petrole | HYDROREFINING AND / OR HYDROCONVERSION CATALYST AND USE THEREOF IN HYDROCARBON CHARGING HYDROCARBON PROCESSES |
US6676606B2 (en) * | 2002-06-11 | 2004-01-13 | Koninklijke Philips Electronics N.V. | Ultrasonic diagnostic micro-vascular imaging |
US7074740B2 (en) * | 2002-07-02 | 2006-07-11 | Chevron U.S.A. Inc. | Catalyst for conversion processes |
US6958309B2 (en) * | 2002-08-01 | 2005-10-25 | Conocophillips Company | Hydrothermal pretreatment for increasing average pore size in a catalyst support |
US7390766B1 (en) * | 2003-11-20 | 2008-06-24 | Klein Darryl P | Hydroconversion catalysts and methods of making and using same |
US20050109674A1 (en) * | 2003-11-20 | 2005-05-26 | Advanced Refining Technologies Llc | Hydroconversion catalysts and methods of making and using same |
EP1753844B1 (en) * | 2004-04-28 | 2016-06-08 | Headwaters Heavy Oil, LLC | Hydroprocessing method and system for upgrading heavy oil |
US10941353B2 (en) | 2004-04-28 | 2021-03-09 | Hydrocarbon Technology & Innovation, Llc | Methods and mixing systems for introducing catalyst precursor into heavy oil feedstock |
BRPI0510346A (en) * | 2004-04-28 | 2007-10-30 | Headwaters Heavy Oil Llc | fixed bed hydroprocessing methods and systems for upgrading an existing fixed bed system |
MXPA06012528A (en) | 2004-04-28 | 2007-08-02 | Headwaters Heavy Oil Llc | Ebullated bed hydroprocessing methods and systems and methods of upgrading an existing ebullated bed system. |
FR2887557B1 (en) * | 2005-06-23 | 2012-11-02 | Inst Francais Du Petrole | INTEGRATED ENCHARING OF EXTRACTION AND TREATMENT PROCESSES OF EXTRA HEAVY OR BITUMINOUS BRUT |
MXPA05012893A (en) * | 2005-11-29 | 2007-11-23 | Mexicano Inst Petrol | Catalyst for the hydrodesulfurization of residues and heavy crudes. |
PL1960101T3 (en) | 2005-12-14 | 2015-02-27 | Advanced Refining Technologies Llc | Method of making hydroprocessing catalyst |
DE102007011471B4 (en) * | 2006-03-09 | 2021-09-30 | Shell Internationale Research Maatschappij B.V. | Catalyst combination for the hydrogenating processing of vacuum gas oils and / or visbreaker gas oils |
CN101332433B (en) * | 2007-06-27 | 2011-07-20 | 中国石油化工股份有限公司 | Catalytic cracking catalyst, preparation method and use thereof |
MX2007009504A (en) * | 2007-08-07 | 2009-02-06 | Mexicano Inst Petrol | Catalyst for the first stage of hydro demetallization in a hydro processing system with multiple reactors for the improvement of heavy and extra-heavy crudes. |
US8034232B2 (en) | 2007-10-31 | 2011-10-11 | Headwaters Technology Innovation, Llc | Methods for increasing catalyst concentration in heavy oil and/or coal resid hydrocracker |
US8142645B2 (en) * | 2008-01-03 | 2012-03-27 | Headwaters Technology Innovation, Llc | Process for increasing the mono-aromatic content of polynuclear-aromatic-containing feedstocks |
US8575063B2 (en) * | 2008-10-27 | 2013-11-05 | Hongying He | Nickel-based reforming catalysts |
US8372268B2 (en) * | 2009-03-24 | 2013-02-12 | Shell Oil Company | High surface area composition for use in the catalytic hydroconversion of a heavy hydrocarbon feedstock, a method making such composition and its use |
KR101841689B1 (en) * | 2009-10-30 | 2018-03-29 | 삼성전자주식회사 | Mesoporous complex catalyst and process for preparing the same |
JP5805761B2 (en) * | 2010-08-13 | 2015-11-04 | シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー | Hydrotreating catalyst produced from waste catalyst fine powder and use thereof |
CN103052445B (en) * | 2010-08-13 | 2015-09-16 | 国际壳牌研究有限公司 | Can be used for composition containing chelating agent and polar additive in hydrocarbon feed hydrotreatment and production and preparation method thereof |
KR101917198B1 (en) | 2010-12-20 | 2019-01-24 | 셰브런 유.에스.에이.인크. | Hydroprocessing catalysts and methods for making thereof |
PL2750792T3 (en) | 2011-09-01 | 2022-01-31 | Advanced Refining Technologies, Llc | Catalyst support and catalysts prepared therefrom |
US9790440B2 (en) | 2011-09-23 | 2017-10-17 | Headwaters Technology Innovation Group, Inc. | Methods for increasing catalyst concentration in heavy oil and/or coal resid hydrocracker |
TWI579043B (en) * | 2012-02-17 | 2017-04-21 | 先進精鍊科技有限公司 | Spheroidal catalyst support and preparation method thereof |
TWI611836B (en) * | 2012-02-17 | 2018-01-21 | Advanced Refining Technologies Llc. | Catalyst support and preparation method thereof |
TWI594795B (en) | 2012-05-21 | 2017-08-11 | 蜆殼國際研究所 | Improved catalyst and process for hydroconversion of a heavy feedstock |
TWI632235B (en) | 2012-06-20 | 2018-08-11 | 美商先進精鍊科技有限公司 | Catalyst for hydrodesulfurization of residuum hydrocarbon feedstocks and preparaton method thereof |
US9644157B2 (en) | 2012-07-30 | 2017-05-09 | Headwaters Heavy Oil, Llc | Methods and systems for upgrading heavy oil using catalytic hydrocracking and thermal coking |
US10220379B2 (en) * | 2014-05-01 | 2019-03-05 | Shell Oil Company | Catalyst and its use for the selective hydrodesulfurization of an olefin containing hydrocarbon feedstock |
US11414608B2 (en) | 2015-09-22 | 2022-08-16 | Hydrocarbon Technology & Innovation, Llc | Upgraded ebullated bed reactor used with opportunity feedstocks |
US11414607B2 (en) | 2015-09-22 | 2022-08-16 | Hydrocarbon Technology & Innovation, Llc | Upgraded ebullated bed reactor with increased production rate of converted products |
US11421164B2 (en) | 2016-06-08 | 2022-08-23 | Hydrocarbon Technology & Innovation, Llc | Dual catalyst system for ebullated bed upgrading to produce improved quality vacuum residue product |
US9956553B2 (en) | 2016-06-28 | 2018-05-01 | Chevron U.S.A. Inc. | Regeneration of an ionic liquid catalyst by hydrogenation using a macroporous noble metal catalyst |
US11118119B2 (en) | 2017-03-02 | 2021-09-14 | Hydrocarbon Technology & Innovation, Llc | Upgraded ebullated bed reactor with less fouling sediment |
US11732203B2 (en) | 2017-03-02 | 2023-08-22 | Hydrocarbon Technology & Innovation, Llc | Ebullated bed reactor upgraded to produce sediment that causes less equipment fouling |
US11318448B2 (en) | 2018-01-31 | 2022-05-03 | Advanced Refining Technologies Llc | Hydroprocessing catalyst for the reduction of metals and sulfur in heavy feeds |
CA3057131A1 (en) | 2018-10-17 | 2020-04-17 | Hydrocarbon Technology And Innovation, Llc | Upgraded ebullated bed reactor with no recycle buildup of asphaltenes in vacuum bottoms |
Family Cites Families (20)
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---|---|---|---|---|
US3993598A (en) * | 1974-02-07 | 1976-11-23 | Exxon Research And Engineering Company | Process for preparing a heavy crude conversion catalyst |
US3993599A (en) * | 1974-02-07 | 1976-11-23 | Exxon Research And Engineering Company | Process for preparing a heavy crude conversion catalyst |
US3989645A (en) * | 1974-02-07 | 1976-11-02 | Exxon Research And Engineering Company | Process for preparing a heavy crude conversion catalyst |
US4082695A (en) * | 1975-01-20 | 1978-04-04 | Mobil Oil Corporation | Catalyst for residua demetalation and desulfurization |
US4069139A (en) * | 1975-12-29 | 1978-01-17 | Exxon Research & Engineering Co. | Hydrodesulfurization of oil utilizing a narrow pore size distribution catalyst |
US4066572A (en) * | 1976-10-12 | 1978-01-03 | Nalco Chemical Company | Phospha-alumina gel and method of preparation |
US4225421A (en) * | 1979-03-13 | 1980-09-30 | Standard Oil Company (Indiana) | Process for hydrotreating heavy hydrocarbons |
US4357263A (en) * | 1979-10-22 | 1982-11-02 | Mobil Oil Corporation | Catalyst for the upgrading of aromatic liquids |
FR2486094B1 (en) * | 1980-07-02 | 1985-03-22 | Catalyse Soc Prod Francais | |
US4549957A (en) * | 1981-06-17 | 1985-10-29 | Amoco Corporation | Hydrotreating catalyst and process |
US4548709A (en) * | 1983-04-29 | 1985-10-22 | Mobil Oil Corporation | Hydrotreating petroleum heavy ends in aromatic solvents with dual pore size distribution alumina catalyst |
US4588709A (en) * | 1983-12-19 | 1986-05-13 | Intevep, S.A. | Catalyst for removing sulfur and metal contaminants from heavy crudes and residues |
US4642179A (en) * | 1983-12-19 | 1987-02-10 | Intevep, S.A. | Catalyst for removing sulfur and metal contaminants from heavy crudes and residues |
FR2570385B1 (en) * | 1984-09-14 | 1987-08-21 | Raffinage Cie Francaise | PROCESS FOR HYDROPROCESSING HYDROCARBON CHARGES AND CATALYST FOR CARRYING OUT SAID METHOD |
US4941964A (en) * | 1988-03-14 | 1990-07-17 | Texaco Inc. | Hydrotreatment process employing catalyst with specified pore size distribution |
US5094994A (en) * | 1988-05-13 | 1992-03-10 | Texaco Inc. | Catalyst composition for hydroprocessing petroleum feedstocks |
US5047142A (en) * | 1988-05-13 | 1991-09-10 | Texaco Inc. | Catalyst composition and method for hydroprocessing petroleum feedstocks |
JP2631712B2 (en) * | 1988-08-18 | 1997-07-16 | コスモ石油株式会社 | Catalyst composition for hydrotreating heavy hydrocarbon oil and hydrotreating method using the same |
US5266300A (en) * | 1989-08-02 | 1993-11-30 | Texaco Inc. | Method of making porous alumina |
US5215955A (en) * | 1991-10-02 | 1993-06-01 | Chevron Research And Technology Company | Resid catalyst with high metals capacity |
-
1993
- 1993-04-05 CA CA 2093412 patent/CA2093412C/en not_active Expired - Lifetime
-
1994
- 1994-05-16 US US08/242,995 patent/US5435908A/en not_active Expired - Lifetime
-
1995
- 1995-04-20 US US08/425,971 patent/US5545602A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
US5545602A (en) | 1996-08-13 |
US5435908A (en) | 1995-07-25 |
CA2093412C (en) | 2002-12-31 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request |