Systems and methods of producing a crude product
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
C10L-001/00
C10G-045/00
출원번호
UP-0013904
(2004-12-16)
등록번호
US-7811445
(2010-11-01)
발명자
/ 주소
Wellington, Scott Lee
Milam, Stanley Nemec
출원인 / 주소
Shell Oil Company
대리인 / 주소
Taylor, Richard B.
인용정보
피인용 횟수 :
22인용 특허 :
117
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 c
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. The crude product may include, hydrocarbon gas that is non-condensable at 25° C. and 0.101 MPa, naphtha, kerosene, residue, or mixtures thereof.
대표청구항▼
What is claimed is: 1. A crude product comprising, per gram of crude product: at most 0.15 grams of hydrocarbon gas that is non-condensable at 25° C. and 0.101 MPa; from 0.001 to 0.2 grams of naphtha, the naphtha containing at least 0.001 grams of paraffins per gram of naphtha, where the paraf
What is claimed is: 1. A crude product comprising, per gram of crude product: at most 0.15 grams of hydrocarbon gas that is non-condensable at 25° C. and 0.101 MPa; from 0.001 to 0.2 grams of naphtha, the naphtha containing at least 0.001 grams of paraffins per gram of naphtha, where the paraffins are comprised of iso-paraffins and n-paraffins, where the weight ratio of iso-paraffins to n-paraffins is at most 1.4; from 0.001 to 0.5 grams of kerosene, the kerosene having a freezing point at a temperature of at most −30° C., as determined by ASTM Method D2386, and the kerosene having at least 0.2 grams of aromatics per gram of kerosene, as determined by ASTM Method D5186; and from 0.00001 to 0.05 grams of residue, as determined by ASTM Method 5307. 2. The crude product of claim 1, wherein the non-condensable hydrocarbon gas and the naphtha, when combined, have at most 0.15 grams of olefins per gram of the combined non-condensable hydrocarbon gases and naphtha, as determined by ASTM D6730. 3. The crude product of claim 1, wherein the crude product also has at least 0.001 grams of diesel per gram of crude product, and the diesel has at least 0.3 grams of aromatics per gram of diesel, as determined by ASTM Method D5186. 4. The crude product of claim 1, wherein the crude product also has at least 0.001 grams of VGO per gram of crude product, and the VGO has at least 0.3 grams of aromatics per gram of VGO, as determined by IP Method 368/90. 5. The crude product of claim 1, wherein the naphtha has at most 0.01 grams of benzene per gram of naphtha, as determined by ASTM Method D6730. 6. The crude product of claim 1, wherein the naphtha and the non-condensable hydrocarbon gases, when combined, comprise iso-paraffins and n-paraffins with a weight ratio of the iso-paraffins to the n-paraffins in the combined naphtha and non-condensable hydrocarbon gases of at most 1.4, as determined by ASTM Method D6730. 7. The crude product of claim 1, wherein the non-condensable hydrocarbon gas contains hydrocarbons with a carbon number from 1 to 3, where the hydrocarbons with a carbon number from 1 to 3 comprise olefins and paraffins with carbon numbers of 2 (C2) and 3 (C3), and a weight ratio of the combined C2 and C3 olefins to the combined C2 and C3 paraffins is at most 0.3, as determined by ASTM Method D6730. 8. The crude product of claim 1, wherein the non-condensable hydrocarbon gas contains hydrocarbons with a carbon number from 1 to 3, where the hydrocarbons with a carbon number from 1 to 3 comprise olefins and paraffins with a carbon number of 2 (C2), wherein a weight ratio of the C2 olefins to the C2 paraffins is at most 0.2, as determined by ASTM Method D6730. 9. The crude product of claim 1, wherein the non-condensable hydrocarbon gas contains hydrocarbons with a carbon number from 1 to 3, where the hydrocarbons with a carbon number from 1 to 3 comprise olefins and paraffins with a carbon number of 3 (C3), wherein a weight ratio of the C3 olefins to the C3 paraffins is at most 0.3, as determined by ASTM Method D6730. 10. The crude product of claim 1, wherein the crude product has from about 0.09 to about 0.13 grams of atomic hydrogen per gram of crude product. 11. The crude product of claim 1, wherein the crude product has a weight ratio of atomic hydrogen to atomic carbon of at most 1.75. 12. A method of producing transportation fuel, comprising: processing a crude product, wherein the material crude product has, per gram of crude product: at most 0.15 grams of hydrocarbon gas that is non-condensable at 25° C. and 0.101 MPa; from 0.001 to 0.2 grams of naphtha containing at least 0.001 grams of paraffins per gram of naphtha, where the paraffins are comprised of iso-paraffins and n-paraffins, where the weight ratio of iso-paraffins to n-paraffins is at most 1.4; from 0.001 to 0.5 grams of kerosene, the kerosene having a freezing point at a temperature of at most −30° C., as determined by ASTM Method D2386, and the kerosene having at least 0.2 grams of aromatics per gram of kerosene, as determined by ASTM Method D5186; and from 0.00001 to 0.05 grams of residue, as determined by ASTM Method D5307. 13. The method of claim 12, wherein the processing comprises distilling the crude product into one or more distillate fractions. 14. The method of claim 12, wherein the processing comprises hydrotreating.
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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.
de Agudelo M. M. Ramirez (Los Teques VEX) Galarraga C. E. (Los Teques VEX), Catalyst for the simultaneous hydrodemetallization and hydroconversion of heavy hydrocarbon feedstocks.
Ramirez de Agudelo M. M. (Los Teques VEX) Galarraga C. E. (Los Teques VEX), Catalyst for the simultaneous hydrodemetallization and hydroconversion of heavy hydrocarbon feedstocks and process for p.
Patel Kundanbhai M. (Landing NJ) Murthy Andiappan K. S. (Lake Hiawatha NJ) Bekker Alex Y. (Teaneck NJ), Catalytic process for production of light hydrocarbons by treatment of heavy hydrocarbons with water.
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.
Milam, Stanley Nemec; Reynolds, Michael Anthony; Wellington, Scott Lee; Ranganathan, Easwar Santhosh; Chan, Win Sim, Process for treating a hydrocarbon-containing feed.
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