The present application generally relates to the introduction of a renewable fuel oil as a feedstock into refinery systems or field upgrading equipment. For example, the present application is directed to methods of introducing a liquid thermally produced from biomass into a petroleum conversion uni
The present application generally relates to the introduction of a renewable fuel oil as a feedstock into refinery systems or field upgrading equipment. For example, the present application is directed to methods of introducing a liquid thermally produced from biomass into a petroleum conversion unit; for example, a refinery fluid catalytic cracker (FCC), a coker, a field upgrader system, a hydrocracker, and/or hydrotreating unit; for co-processing with petroleum fractions, petroleum fraction reactants, and/or petroleum fraction feedstocks and the products, e.g., fuels, and uses and value of the products resulting therefrom.
대표청구항▼
1. A method for preparing liquid fuel products, comprising: co-processing a plurality of reactants in a catalytic cracker, said plurality of reactants comprising: i) 93-99.95 wt. % of a petroleum fraction; andii) 0.05-7 wt. % of a renewable fuel oil blended with a conditioning additive, said renewab
1. A method for preparing liquid fuel products, comprising: co-processing a plurality of reactants in a catalytic cracker, said plurality of reactants comprising: i) 93-99.95 wt. % of a petroleum fraction; andii) 0.05-7 wt. % of a renewable fuel oil blended with a conditioning additive, said renewable fuel oil derived from rapid thermal processing of a cellulosic biomass,wherein the renewable fuel oil has: a) carbon content of at least 40 wt. % on a moisture-free basis;b) an oxygen content in the range of between 20-50 wt. % on a moisture-free basis; andc) a water content in the range of between 10-40 wt. %. 2. The method of claim 1, wherein: a) the catalytic cracker is present in a refinery; andb) the blended renewable fuel oil is introduced to the refinery. 3. The method of claim 1, wherein the rapid thermal processing comprises non-catalytic rapid thermal processing. 4. The method of claim 1, wherein the alcohol additive comprises ethanol. 5. The method of claim 1, wherein the renewable fuel oil has a water content of less than 20 wt. %. 6. The method of claim 1, wherein the alcohol additive comprises methanol. 7. The method of claim 1, wherein the alcohol additive comprises propanol. 8. The method of claim 1, wherein the alcohol additive comprises isopropyl alcohol. 9. The method of claim 1, wherein the alcohol additive comprises glycerol. 10. The method of claim 1, wherein the alcohol additive comprises butanol. 11. The method of claim 1, wherein: a) the renewable fuel oil is further blended with a petroleum material; andb) the further blended renewable fuel oil is introduced to the catalytic cracker. 12. The method of claim 11, wherein the further blending is in the presence of a surfactant. 13. The method of claim 11, wherein the further blending is in the absence of a surfactant. 14. The method of claim 1, wherein: a) the renewable fuel oil is the product of grinding and non-catalytic rapid thermal processing of the cellulosic biomass. 15. The method of claim 14, wherein at least 70 wt. % of the cellulosic biomass is converted to the renewable fuel oil. 16. The method of claim 1, wherein the renewable fuel oil has: a) a solids content of less than 0.01 wt. %; andb) an ash content of less than 0.05 wt. %. 17. The method of claim 15, wherein the alcohol additive is ethanol. 18. A method for preparing liquid fuel products, comprising: co-processing a plurality of reactants in a catalytic cracker, said plurality of reactants comprising: i) 93-99.95 wt. % of a petroleum fraction; andii) 0.05-7 wt. % of renewable fuel oil blended with ethanol, said renewable fuel oil comprising a product of grinding and non-catalytic rapid thermal processing to convert at least 60 wt. % of the cellulosic biomass to the unenriched renewable fuel oil,wherein the renewable fuel oil has: a) carbon content of at least 40 wt. % on a moisture-free basis;b) an oxygen content in the range of between 20-50 wt. % on a moisture-free basis; andc) a water content in the range of between 10-40 wt. %. 19. The method of claim 18, wherein: a) the renewable fuel oil is further blended with a petroleum material; andb) the further blended renewable fuel oil is introduced to the catalytic cracker. 20. The method of claim 19, wherein the further blending is in the absence of a surfactant.
연구과제 타임라인
LOADING...
LOADING...
LOADING...
LOADING...
LOADING...
이 특허에 인용된 특허 (236)
Rehmat Amirali G. (Darien IL) Dorfman Lev (Skokie IL), Advanced staged combustion system for power generation from coal.
Hedrick,Brian W.; Palmas,Paolo; Myers,Daniel N.; Newman,Michael C.; Ziolkiewicz Dydak,Agnieszka; Broerman,Andrew W., Apparatus and process for minimizing catalyst residence time in a reactor vessel.
Johnson,Warren L.; Yavari,Gholam H.; Radelin,Desmond St. A. G., Apparatus for separating fouling contaminants from non-condensable gases at the end of a pyrolysis/thermolysis of biomass process.
Hohmann Carl W. ; Harrington Douglas W. ; Dutton Maureen L. ; Tipton ; Jr. Billy Charles ; Bacak James W. ; Salazar Frank, Automated propellant blending.
Huber, George W.; Cheng, Yu-Ting; Carlson, Torren; Vispute, Tushar; Jae, Jungho; Tompsett, Geoff, Catalytic pyrolysis of solid biomass and related biofuels, aromatic, and olefin compounds.
Palmas, Paolo; Sechrist, Paul Alvin; Myers, Daniel N.; Kulprathipanja, Sid; Frey, Stanley Joseph; Freel, Barry, Char-handling processes in a pyrolysis system.
Ciais Andr (Mornant FRX) Variot Gilles (Villeurbanne FRX), Device and installations for the distillation by thin layer evaporation particularly of hydrocarbons, and process for op.
Jukkola Walfred W. (Westport CT) Leon Albert M. (Mamaroneck NY) Van Dyk ; Jr. Garritt C. (Bethel CT) McCoy Daniel E. (Williamsport PA) Fisher Barry L. (Montgomery PA) Saiers Timothy L. (Williamsport , Fluidized bed heat exchanger with water cooled air distributor and dust hopper.
Beech, Jr., James H.; Coute, Nicolas P.; Smith, Jeffrey S.; Nicoletti, Michael Peter, Fluidizing a population of catalyst particles having a low catalyst fines content.
McIntyre Glover C. (Pickering CAX) Lacombe Robert J. (Saint John WI CAX) Forbess Russell G. (Weston WI), Furnace combustion zone temperature control method.
Best Donald F. (Mahopac NY) Long Gary N. (Putnam Valley NY) Pellet Regis J. (Cronton-on-Hudson NY) Rabo Jule A. (Armonk NY) Wolynic Edward T. (Scarsdale NY) Gortsema Frank P. (Pleasantville NY) Sprin, Hydrocracking catalyst and hydrocracking process.
Chen Nai Y. (Titusville NJ) LaPierre Rene B. (Medford NJ) Partridge Randall D. (Trenton NJ) Wong Stephen S. (Medford NJ), Integrated hydroprocessing scheme for production of premium quality distillates and lubricants.
Pandey Ramesh C. (Highland Park NJ) Yankov Luben K. (Edison NJ), Isolation and purification of paclitaxel from organic matter containing paclitaxel, cephalomannine and other related tax.
Kocal, Joseph A.; Marinangeli, Richard; Lupton, Francis Stephen; King, Lisa, Low oxygen biomass-derived pyrolysis oils and methods for producing the same.
Busch Lloyd E. (Ashland KY) Palmeter Charles W. (Ashland KY) Henderson Gerald O. (Ashland KY) Rice William M. (Ashland KY), Method and apparatus for converting oil feeds.
Horizoe Hirotoshi,JPX ; Shimizu Yoshihito,JPX ; Sato Jun,JPX ; Yasuda Shizuo,JPX ; Kaihara Yuji,JPX ; Kawami Yoshimasa,JPX, Method and apparatus for producing superheated steam using heat from the incineration of waste material.
Brioni Osvaldo,ITX ; Buizza Dario,ITX, Method and apparatus for producing wood charcoal by pyrolysis of wood-like products or vegetable biomasses in general.
Dinjus, Eckhard; Henrich, Edmund; Raffelt, Klaus; Weirich, Friedhelm, Method for producing and preparing fast pyrolysis products from biomass for an entrained-flow pressure gasification.
Kwon Sook-hyung (Seoul KRX) Min Wha-sik (Seoul KRX) Lee Yun-kil (Seoul KRX), Method for producing feedstocks of high quality lube base oil from unconverted oil of fuels hydrocracker operating in re.
Hypp?nen,Timo; Kauppinen,Kari V. O.; Lehtonen,Pekka; Vilokki,Harri; V?liaho,Kimmo, Method of and an apparatus for recovering heat in a fluidized bed reactor.
Burger Edward D. (Plano TX) Curtin Daniel J. (Plano TX) Edison Robert R. (Olympia Fields IL), Method of removing contaminant from a hydrocarbonaceous fluid.
Carver David R. (Boulder CO) Prout Timothy R. (Boulder CO) Workman Christopher T. (Boulder CO) Henderson Donia L. (Boulder CO) Hughes Charles L. (Boulder CO), Method of using ion exchange media to increase taxane yields.
Gartside, Robert J.; Haines, Robert I.; Skourlis, Thomas; Sumner, Charles, Olefin plant recovery system employing a combination of catalytic distillation and fixed bed catalytic steps.
Cabrera Carlos A. (Northbrook IL) Myers Daniel N. (Arlington Heights IL) Hammershaimb Harold U. (Western Springs IL), Partial CO combustion with staged regeneration of catalyst.
Reh Lothar (Bergen-Enkheim DE) Hirsch Martin (Frankfurt am Main DE) Collin Per H. (Falun SE) Flink Sune N. (Vaesteraas SE), Process for burning carbonaceous materials.
Hogendoorn, Johannes Antonius; Kersten, Sascha Reinier Aldegonda; Meesala, Lavanya; Mercader, Ferran De Miguel; Moppi, Argi Joachim Antonio; Schaverien, Colin John, Process for catalytic hydrotreatment of a pyrolysis oil.
Angelo ; II James F. (949 Eagle Fayetteville AR 72701) Kephart Wilbur L. (324 Sugarwood Dr. Knoxville TN 27922), Process for chemical/thermal treatment without toxic emissions.
Owen Hartley (Belle Mead NJ) Schipper Paul H. (Wilmington DE), Process for control of multistage catalyst regeneration with full then partial CO combustion.
Mansour Momtaz Nosshi ; Durai-Swamy Kanda-Swamy ; Warren David Walter, Process for detoxifying waste materials by steam reformation through endothermic gasification reactions.
Koppenhoefer Ralph,DEX ; Weimer Siegfried,DEX, Process for intermediately quenching light-metal castings coming from a solution heat treatment furnance.
Agrawal, Rakesh; Agrawal, Manju; Singh, Navneet R., Process for producing liquid hydrocarbon by pyrolysis of biomass in presence of hydrogen from a carbon-free energy source.
Solbakken Age (Montgomery TX) Apffel Fred P. (Houston TX) Robinson Sam P. (Houston TX) Hayes Bobby L. (Houston TX), Process for recovering carbon black and hydrocarbons from used tires.
Keckler,Kenneth Paul; Corma,Avelino; Knox,Thomas; Greenough,Paul; Hodges,Michael G., Process for removal of sulfur from components for blending of transportation fuels.
Kowalczyk Dennis C. (Pittsburgh PA) Bricklemyer Bruce A. (Avonmore PA) Svoboda Joseph J. (Pittsburgh PA), Process for removing polymer-forming impurities from naphtha fraction.
Scott Donald S. (Waterloo CAX) Piskorz Jan (Waterloo CAX) Radlein Desmond (Waterloo CAX) Majerski Piotr (Waterloo CAX), Process for the production of anhydrosugars from lignin and cellulose containing biomass by pyrolysis.
van de Beld,Lambertus; Boerefijn,Ferry Ronald; Bos,Gijsbert Maurits; Goudriaan,Frans; Naber,Jaap Erik; Zeevalkink,Jan Anton, Process for the production of liquid fuels from biomass.
Gouman, Rudolf Robert; Herold, Rudolf Henri Max; Last, Thijme; Manshande, Bernardus Josephus Maria; Smit, Cornelis Jacobus, Process for the removal of contaminants.
Kalnes Tom N. ; James ; Jr. Robert B., Process for the simultaneous conversion of waste lubricating oil and pyrolysis oil derived from organic waste to produce.
Scott Donald S. (Waterloo CAX) Piskorz Jan (Waterloo CAX) Radlein Desmond (Waterloo CAX) Majerski Piotr (Waterloo CAX), Process for the thermal conversion of biomass to liquids.
Galiasso, Roberto; Palmisano, Eusebio; Arreaza, Gerardo; Quenza, Samuel; Ramnarine, Sandra, Process scheme for sequentially treating diesel and vacuum gas oil.
Marker, Terry L.; Kokayeff, Peter; Abdo, Suheil F.; Baldiraghi, Franco; Sabatino, Luigina M. F., Production of diesel fuel from biorenewable feedstocks with lower hydrogen consumption.
Marker, Terry L.; Kokayeff, Peter; Faraci, Giovanni; Baldiraghi, Franco, Production of diesel fuel from renewable feedstocks with reduced hydrogen consumption.
Craig Wayne K. (126 Auld Crescent Saskatoon ; Saskatchewan CAX S7H 4W9) Soveran Douglas W. (7309 5th Avenue Regina ; Saskatchewan CAX S4T 0N2), Production of hydrocarbons with a relatively high cetane rating.
Green ; Norman W. ; Duraiswamy ; Kandaswamy ; Lumpkin ; Robert E. ; Kne ll ; Everett W. ; Mirza ; Zia I. ; Winter ; Bruce L., Pyrolysis of carbonaceous materials with solvent quench recovery.
Green Norman W. (Upland CA) Duraiswamy Kandaswamy (Sterling VA) Lumpkin Robert E. (Claremont CA) Winter Bruce L. (Claremont CA), Pyrolysis with staged recovery.
Spars Byron G. (Mill Valley CA) Tamm Paul W. (Oakland CA) Wallman P. Henrik (Berkeley CA), Reactor vessel and process for thermally treating a granular solid.
Mirza Zia I. (La Verne CA) Knell Everett W. (Los Alamitos CA) Winter Bruce L. (Danville CA), Recovering hydrocarbons from hydrocarbon-containing vapors.
Spilker, Kerry K.; Vogel, Roger; Stevens, James F.; Ricci, Peter C., Selective, integrated processing of bio-derived ester species to yield low molecular weight hydrocarbons and hydrogen for the production of biofuels.
Spilker, Kerry K.; Vogel, Roger; Stevens, James F.; Ricci, Peter C., Selective, integrated processing of bio-derived ester species to yield low molecular weight hydrocarbons and hydrogen for the production of biofuels.
Pinault,Mathieu; Gauthier,Thierry; Kressmann,Stéphane; Selmen,Arnault, Series of hydroconversion and steam reforming processes to optimize hydrogen production on production fields.
Sechrist Paul A. (Des Plaines IL) Lomas David A. (Arlington Heights IL) Myers Daniel N. (Arlington Heights IL), Supplying FCC lift gas directly from product vapors.
Trojani Benito L. (Via Polar ; 8 Lugano ; Breganzona CHX), Tube provided with inner fins and outer fins or pins, particularly for heat exchangers, and method therefor.
※ AI-Helper는 부적절한 답변을 할 수 있습니다.