Systems and methods of producing a crude product
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
C10G-047/02
C10G-047/00
출원번호
US-0014297
(2004-12-16)
등록번호
US-7416653
(2008-08-26)
발명자
/ 주소
Wellington,Scott Lee
Brownscombe,Thomas Fairchild
Milam,Stanley Nemec
출원인 / 주소
Shell Oil Company
대리인 / 주소
Taylor,Richard B.
인용정보
피인용 횟수 :
64인용 특허 :
105
초록▼
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixture at 25�� C. and 0.101 MPa. One or more properties of the crud
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixture at 25�� C. and 0.101 MPa. One or more properties of the crude product may be changed by at least 10% relative to the respective properties of the crude feed. In some embodiments, gas is produced during contact with one or more catalysts and the crude feed.
대표청구항▼
What is claimed is: 1. A method of producing a crude product, comprising contacting a crude feed with a hydrogen source in the presence of one or more catalysts comprising a transition metal sulfide catalyst to produce a total product that includes the crude product, wherein the crude product is a
What is claimed is: 1. A method of producing a crude product, comprising contacting a crude feed with a hydrogen source in the presence of one or more catalysts comprising a transition metal sulfide catalyst to produce a total product that includes the crude product, wherein the crude product is a liquid mixture at 25�� C. and 0.101 MPa, and the transition metal sulfide catalyst comprises K3Fe10S14. 2. The method of claim 1, wherein the transition metal sulfide catalyst comprises a mixture of one or more transition metal sulfides, one or more alkali metals, one or more compounds of one or more alkali metals, or mixtures thereof, and during contacting a portion of the transition metal sulfides are convert to K3Fe10S14. 3. The method of claim 1, wherein the transition metal sulfide catalyst has a total of at least 0.4 grams of one or more additional transition metal sulfides per gram of transition metal sulfide catalyst. 4. The method of claim 3, wherein an atomic ratio of transition metal to sulfur in at least one of the additional transition metals sulfides is in a range from about 0.5 to about 10. 5. The method of claim 1, wherein the transition metal sulfide catalyst comprises one or more additional transition metal sulfides, one or more alkali metals, one or more compounds of one or more alkali metals, or a mixture thereof. 6. The method of claim 1, wherein the transition metal sulfide catalyst comprises one or more additional transition metal sulfides, one or more alkaline-earth metals, one or more compounds of one or more alkaline-earth metals, or a mixture thereof. 7. The method of claim 1, wherein the transition metal sulfide catalyst comprises one or more additional transition metal sulfides and zinc. 8. The method of claim 1, wherein the transition metal sulfide catalyst comprises one or more additional transition metal sulfides, one or more alkali metals, one or more compounds of one or more alkali metals, or a mixture thereof and an atomic ratio of transition metal to sulfur in at least one additional transition metal sulfide is in a range from about 0.5 to about 2.5, and an atomic ratio of the alkali metal to the transition metal in the at least one additional transition metal sulfide is in a range from above 0 to about 1. 9. The method of claim 1, wherein the transition metal sulfide catalyst comprises one or more additional transition metal sulfides, one or more alkaline-earth metals, one or more compounds of one or more alkaline-earth metals, or a mixture thereof and an atomic ratio of transition metal to sulfur in at least one additional transition metal sulfide is in a range from about 0.5 to about 2.5, and an atomic ratio of the alkaline-earth metal to transition metal in at least one additional transition metal sulfide is in a range from above 0 to about 1. 10. The method of claim 1, wherein the crude feed has at least 0.2 grams of residue per gram of crude feed. 11. The method of claim 1, wherein the crude feed has at least 0.2 grams of residue per gram of crude feed, and the method further comprises controlling contacting conditions such that the crude product has a residue content of at most 30% of a residue content of the crude feed. 12. The method of claim 1, wherein the crude product has at least 0.8 grams of hydrocarbons that are a liquid mixture at 25�� C. and 0.101 MPa per gram of crude product. 13. The method of claim 1, wherein the crude feed has a total Ni/V/Fe content, expressed in total grams of Ni/V/Fe per gram of crude feed, and the method further comprises controlling contacting conditions such that the crude product has a total Ni/V/Fe content of at most 90% of the Ni/V/Fe content of the crude feed, wherein Ni/V/Fe content is as determined by ASTM Method D5863. 14. The method of claim 1, wherein the crude feed has a sulfur content, expressed in grams of sulfur per gram of crude feed, and further comprising controlling contacting conditions such that the crude product has a sulfur content of at most 90% of the sulfur content of the crude feed, wherein sulfur content is as determined by ASTM Method D4294. 15. The method of claim 1, wherein the crude product has from about 0.1 to about 0.99 grams of vacuum gas oil per gram of crude product. 16. The method of claim 1, wherein the crude product has from about 0.1 to about 0.5 grams of distillate per gram of crude product. 17. The method of claim 1, wherein contacting comprises producing a total product that includes the crude product and at least a portion of the total product is produced as a vapor, and the method further comprises condensing at least a portion of the vapor to form the crude product. 18. The method of claim 1, wherein the method further comprises combining the crude product with a crude that is the same as or different from the crude feed to form a blend suitable for transportation and/or treatment facilities. 19. The method of claim 1, wherein the method further comprises processing the crude product to produce transportation fuel. 20. A crude product obtainable by a method, comprising contacting a crude feed with a hydrogen source in the presence of one or more catalysts comprising a transition metal sulfide catalyst to produce a total product that includes the crude product, wherein the crude product is a liquid mixture at 25�� C. and 0.101 MPa, and the transition metal sulfide catalyst comprises K3Fe10S14. 21. A method of producing transportation fuel, comprising: processing a crude product, wherein the crude product is obtainable by: contacting a crude feed with a hydrogen source in the presence of one or more catalysts comprising a transition metal sulfide catalyst to produce a total product that includes the crude product, wherein the crude product is a liquid mixture at 25�� C. and 0.101 MPa, and the transition metal sulfide catalyst comprises K3Fe10S14. 22. The method of claim 21, wherein the processing comprises distilling the crude product into one or more distillate fractions. 23. The method of claim 21, wherein the processing comprises hydrotreating.
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이 특허에 인용된 특허 (105)
Jacobson Allan J. (Princeton NJ) Ho Teh C. (Bridgewater NJ) Chianelli Russel R. (Somerville NJ) Pecoraro Theresa A. (Danville CA), Amorphous, iron promoted Mo and W sulfide hydroprocessing catalysts and uses thereof.
Raybaud Pascal,FRX ; Toulhoat Herve,FRX ; Kasztelan Slavik,FRX, Catalyst compromising a mixed sulphide and its use for hydrorefining and hydroconverting hydrocarbons.
Boorman Philip M. (Calgary CAX) Chivers Tristram (Calgary CAX) Tavares Donald F. (Calgary CAX) Mahadev Kalabeerappa N. (Calgary CAX), Catalyst for sulphur removal from hydrocarbons.
Kretschmar Klaus (Dorsten DEX) Merz Ludwig (Recklinghausen DEX) Niemann Klaus (Oberhausen DEX) Guitian Jos (Dorsten DEX) Krasuk Julio (Duesseldorf DEX) Marruffo Franzo (Duesseldorf DEX) Kurzeja Klaus, Catalyst for the hydrogenation of hydrocarbon material.
Baird ; Jr. William C. (Baton Rouge LA) Bearden ; Jr. Roby (Baton Rouge LA), Combined desulfurization and hydroconversion with alkali metal hydroxides.
Baird ; Jr. William C. (Baton Rouge LA) Beardon ; Jr. Roby (Baton Rouge LA), Desulfurization and hydroconversion of residua with sodium hydride and hydrogen.
Aldridge Clyde L. (Baton Rouge LA) Bearden ; Jr. Roby (Baton Rouge LA) Lewis William E. (Baton Rouge LA), Hydroconversion of heavy feeds by use of both supported and unsupported catalysts.
Tamalis George R. (Houston TX) Chess David D. (Houston TX) Patel Mahendra S. (Hopewell Junction NY) Bhattacharya Ajit K. (Beacon NY) Gipson Robert M. (Port Arthur TX), Hydroconversion process containing a molybdenum complex recovered from epoxidation of olefinic hydrocarbons.
Varghese Philip (Voorhees NJ) Whitehurst Darrell D. (Titusville NJ), Hydrocracking of heavy feeds plus light fractions with dispersed dual function catalyst.
Sears Paul L. (Dunrobin CAX) de Bruijn Theo J. W. (Constance Bay CAX) Dawson William H. (Edmonton CAX) Pruden Barry B. (Calgary CAX) Jain Anil K. (Calgary CAX), Hydrocracking of heavy hydrocarbon oils with heavy hydrocarbon recycle.
Belinko Keith (Nepean CAX) Khulbe Chandra P. (Oakville CAX) Jain Anil K. (Oakville CAX), Hydrocracking of heavy oil in presence of ultrafine iron sulphate.
Ranganathan Ramaswami (Ottawa CAX) Denis Jean-Marie D. (Munster CAX) Pruden Barry B. (Ottawa CAX), Hydrocracking of heavy oils using iron coal catalyst.
Sudhakar Chakka (Wappingers Falls NY) Dolfinger ; Jr. Frank (Poughkeepsie NY) Cesar Max R. (Newburgh NY) Patel Mahendra S. (Hopewell Junction NY) Fritz Paul O. (Newburgh NY), Hydrodearomatization of hydrocarbon oils using novel “phophorus treated carbon”supported metal sulfide catalysts.
Eberly ; Jr. Paul E. (Baton Rouge LA), Hydrodesulfurization process with conversion of heavy hydrocarbons utilizing a catalyst containing a group IIA metal com.
Dohler Werner (Marl-Polsum DEX) Holighaus Rolf (Haltern DEX) Niemann Klaus (Oberhausen DEX), Hydrogenation of mineral oils contaminated with chlorinated hydrocarbons.
Dahlberg Arthur J. (Rodeo CA) Shinn John H. (Richmond CA) Rosenthal Joel W. (El Cerrito CA) Chu Tim T. (Oakland CA), Hydroprocessing of heavy hydrocarbonaceous oils.
Ebner Jerry R. (St. Louis MO) Gleaves John T. (St. Louis MO), Method and apparatus for carrying out catalyzed chemical reactions and for studying catalysis.
Ebner Jerry R. (St. Charles MO) Gleaves John T. (St. Charles MO), Method and apparatus for carrying out catalyzed chemical reactions and for studying catalysts.
Seamans James Dallas (Woodlands TX) Adams Charles Terrell (Houston TX) Dominguez Wendy Beth (Rosenberg TX) Chen Andrew An-Ju (Houston TX), Method of presulfurizing a hydrotreating, hydrocracking or tail gas treating catalyst.
Erekson Erek J. (LaGrange IL) Lee Anthony L. (Glen Ellyn IL) Barone S. Peter (Hoffman Estates IL) Solomon Irvine J. (Highland Park IL), Mixed basic metal oxide/sulfide catalyst.
Erekson Erek J. (LaGrange IL) Lee Anthony L. (Glen Ellyn IL) Barone S. Peter (Hoffman Estates IL) Solomon Irvine J. (Highland Park IL), Mixed basic metal sulfide catalyst.
Eijsbouts, Sonja; Oogjen, Bob Gerardus; Homan Free, Hermannus Willem; Cerfontain, Marinus Bruce; Riley, Kenneth Lloyd; Soled, Stuart Leon; Miseo, Sabato, Mixed metal catalyst, its preparation by co-precipitation, and its use.
Erekson Erek J. (LaGrange IL) Lee Anthony L. (Glen Ellyn IL), Mixed-solid solution tri-metallic oxide/sulfide catalyst and process for its preparation.
Deschamps Andr (Noisy le Roi FRX) Dezael Claude (Maisons Laffitte FRX) Franckowiak Sigismond (Rueil-Malmaison FRX), Process for converting heavy petroleum residues to hydrogen and gaseous distillable hydrocarbons.
Oleck Stephen M. (Moorestown NJ) Sherry Howard S. (Cherry Hill NJ) Fischer Ronald H. (Oakton VA) Milstein Donald (Cherry Hill NJ), Process for demetalation and desulfurization of petroleum oils.
Brons Glen ; Myers Ronald Damian,CAX ; Bearden ; Jr. Roby ; MacLeod John Brenton,CAX, Process for desulfurization of petroleum feeds utilizing sodium metal.
Krasuk Julio H. (Caracas VEX) Silva Fernando J. (Miranda VEX) Galiasso Roberto E. (Miranda VEX) Souto Alfredo (Miranda VEX), Process for hydroconversion and upgrading of heavy crudes of high metal and asphaltene content.
Boon Andries Qirin Maria,NLX ; Den Ouden Constantinus Johannes Jacobus,NLX ; Bhan Opinder Kishen, Process for hydrotreating metal-contaminated hydrocarbonaceous feedstock.
Eijsbouts, Sonja; Oogjen, Bob Gerardus; Homan Free, Harmannus Willem; Cerfontain, Marinus Bruce; Riley, Kenneth Lloyd; Soled, Stuart Leon; Miseo, Sabato, Process for preparing a mixed metal catalyst composition.
Kretschmar Klaus (Dorsten DEX) Merz Ludwig (Recklinghausen DEX) Niemann Klaus (Oberhausen DEX), Process for the hydrogenative conversion of heavy oils and residual oils, used oils and waste oils, mixed with sewage sl.
Seamans James D. (Woodlands TX) Adams Charles T. (Houston TX) Dominguez Wendy B. (Rosenberg TX) Chen Andrew A.-J. (Houston TX), Process of hydrotreating and/or hydrocracking hydrocarbon streams or tail gas treating sulfur-containing gas streams.
Colombet Pierre (Nantes FRX) Molinie Philippe (Saint Herblain FRX) Spiesser Michel (Nantes FRX), Production of binary rare earth/sulfur or transition metal/sulfur compounds.
Nongbri Govanon (Newtown PA) Brandt Susan M. (Oakford PA) Chervenak Michael C. (Pennington NJ), Selective operating conditions for high conversion of special petroleum feedstocks.
Dahlberg Arthur J. (Rodeo CA) Shinn John H. (Richmond CA) Rosenthal Joel W. (El Cerrito CA) Chu Tim T. (Oakland CA), Two-step hydroprocessing of heavy hydrocarbonaceous oils.
King Laurence F. (Mooretown CA) Gaspar Noel J. (Sarnia CA) Pasternak Israel S. (Sarnia CA), Visbreaking a heavy hydrocarbon feedstock in a regenerable molten medium in the presence of hydrogen.
Jiao, Ling; Chabot, Julie; Nguyen, Joseph V.; Dunckley, Christopher Paul; Yang, Shuwu; Maris, Erin P.; Mironov, Oleg; Reynolds, Bruce Edward; Kuperman, Alexander E., Hydroprocessing catalysts and methods for making thereof.
Mironov, Oleg; Kuperman, Alexander E.; Bhaduri, Rahul Shankar; Chabot, Julie; Yang, Shuwu; Jiao, Ling; Nguyen, Joseph V.; Reynolds, Bruce Edward, Hydroprocessing catalysts and methods for making thereof.
Mironov, Oleg; Kuperman, Alexander E.; Chabot, Julie; Yang, Shuwu; Nguyen, Joseph V.; Jiao, Ling; Reynolds, Bruce Edward; Brait, Axel; Kwik, Kenneth; Kotun, Modinat, Hydroprocessing catalysts and methods for making thereof.
Nguyen, Joseph V.; Chabot, Julie; Jiao, Ling; Dunckley, Christopher Paul; Yang, Shuwu; Maris, Erin P.; Mironov, Oleg; Reynolds, Bruce Edward; Kuperman, Alexander E., Hydroprocessing catalysts and methods for making thereof.
Milam, Stanley Nemec; Reynolds, Michael Anthony; Wellington, Scott Lee; Ranganathan, Easwar Santhosh; Chan, Win Sim, Process for treating a hydrocarbon-containing feed.
Nguyen, Joseph V; Brait, Axel; Chabot, Julie; Kou, Bo; Maris, Erin; Bhaduri, Rahul S.; Kuperman, Alexander E., Systems and methods for producing a crude product.
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