And Rare Earth Metal (sc, Y Or Lanthanide)containing Patents (Class 502/65)
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Patent number: 7776775Abstract: The present invention provides a cracking catalyst, containing a rare-earth Y-zeolite and a support, which is characterized in that the rare-earth content in crystal lattice of the rare-earth Y-zeolite is 4-15 wt % of RE2O3; the original unit cell size is 2.440-2.465 nm; the equilibrium unit cell size of the catalyst after 100% steam-aging treatment at 800° C. for 17 hours is larger than 2.435 nm; the rare-earth atom content in the support is 1.0-8.0 wt % of the support. The present invention also relates to a preparation process for the same catalyst.Type: GrantFiled: March 31, 2006Date of Patent: August 17, 2010Assignees: China Petroleum & Chemical Corporation, Research Institute of Petroleum Processing, SinopecInventors: Jun Du, Zheng Li, Jun Long, Mingde Xu, Zhijian Da, Huiping Tian, Mingyuan He
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Publication number: 20100190634Abstract: Disclosed is a NOx purifying catalyst which is capable of removing NOx sufficiently efficiently even during operations at low temperatures such as operations in diesel cars. Specifically disclosed is a NOx purifying catalyst for processing NOx in an exhaust gas by performing lean/rich control of air/fuel ratio of the exhaust gas. This NOx purifying catalyst comprises at least a first catalyst layer containing a ? zeolite containing iron element and a cerium oxide material and a second catalyst layer containing a noble metal, a cerium oxide material and a heat-resistant inorganic oxide. The second catalyst layer and the first catalyst layer are sequentially arranged on a carrier in such a manner that the first catalyst layer forms the uppermost layer.Type: ApplicationFiled: July 4, 2008Publication date: July 29, 2010Applicant: Honda Motor Co., Ltd.Inventors: Naohiro Sato, Osami Yamamoto, Koichi Inaba
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Publication number: 20100190635Abstract: A metal-modified alkylation catalyst including a metal/zeolite is provided where the metal is one or two selected from the group consisting of yttrium and a rare earth of the lanthanide series other than cerium. Where two metals are used, one may be Ce or La. The metal-promoted zeolite is useful as a molecular sieve aromatic alkylation catalyst for the production of ethylbenzene by the ethylation of benzene in the liquid phase or critical phase. An alkylation product is produced containing ethylbenzene as a primary product with the attendant production of heavier alkylated by-products of no more than 10-60 wt % of the ethylbenzene.Type: ApplicationFiled: March 31, 2010Publication date: July 29, 2010Applicant: Fina Technology, Inc.Inventors: Kevin P. Kelly, James R. Butler
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Patent number: 7763560Abstract: A catalyst which purges a diesel engine exhaust gas of HC, CO, and SOF and reduces the emission of particulates as well and a method for the production thereof are provided. The catalyst for purifying a diesel engine exhaust gas has deposited on a refractory three-dimensional structure a catalyst component comprising silica-alumina supporting at least one noble metal selected from the group consisting of platinum, palladium, and rhodium and zeolite. This catalyst is produced by adding a noble metal component into a slurry of silica-alumina thereby inducing chemical adsorption, then adding zeolite to the resultant mixture thereby obtaining a mixed slurry of a noble metal-supporting silica-alumina and zeolite, dipping a refractory three-dimensional structure in the slurry thereby inducing deposition of the catalyst component, and subsequently calcining the resultant composite.Type: GrantFiled: May 4, 2004Date of Patent: July 27, 2010Assignees: ICT Co., Ltd, International Catalyst Technology, Inc.Inventors: Makoto Horiuchi, Masao Hori, Tatsuya Yoshikawa, Atsushi Fukumoto, Takuji Nakane
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Publication number: 20100183490Abstract: An oxidation catalyst composite, methods and systems for the treatment of exhaust gas emissions from an advanced combustion engine, such as the oxidation of unburned hydrocarbons (HC), and carbon monoxide (CO) and the reduction of nitrogen oxides (NOx) from a diesel engine and an advanced combustion diesel engine are disclosed. More particularly, washcoat compositions are disclosed comprising at least two washcoat layers, a first washcoat comprising a palladium component and a first support containing cerium and a second washcoat containing platinum and one or more molecular sieves.Type: ApplicationFiled: January 14, 2010Publication date: July 22, 2010Applicant: BASF Catalystic LLCInventors: Jeffrey B. Hoke, Joseph C. Dettling
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Publication number: 20100166629Abstract: An oxidation catalyst for the treatment of exhaust gas emissions, such as the oxidation of unburned hydrocarbons (HC), and carbon monoxide (CO) and the reduction of nitrogen oxides (NOx) from a diesel engine and methods of exhaust gas treatment are disclosed. More particularly, a washcoat composition is disclosed comprising at least two washcoat layers, a first washcoat comprising palladium supported on ceria-zirconia and ceria-zirconia-alumina and a second washcoat containing one or more of platinum and palladium and one or more hydrocarbon storage components. An undercoat may also be included in the catalyst. Also disclosed are method of exhaust gas treatment and diesel exhaust gas treatment systems that include the oxidation catalyst and a downstream soot filter.Type: ApplicationFiled: December 21, 2009Publication date: July 1, 2010Applicant: BASF Catalysts LLCInventor: Michel Deeba
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Publication number: 20100160581Abstract: The present invention relates to a supported catalyst composition for polymerization of olefins comprising at least two catalytic components; and a polymerization process using that catalyst composition; and a method for its preparation.Type: ApplicationFiled: August 11, 2006Publication date: June 24, 2010Inventors: Wei Xu, Syriac J. Palackal, Atieh Abu-Ruqabah, Maneet Muktibodh, Bing Wang, Nicolaas Hendrika Friederichs
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Publication number: 20100145127Abstract: A catalyst composition comprising on weight basis the following components: a) 30 to 99.5% of at least one intergrowth molecular sieve; b) 0 to 20% of a rare earth element or oxides thereof; c) 0 to 10% of at least one element from Group VA of the Periodic Table or oxides thereof; d) 0 to 10% of at least one element from Group IIIA of the Periodic Table or oxides thereof; e) 0 to 20% of at least one element from Group IB or IIB of the Periodic Table or oxides thereof; f) 0 to 20% of at least one element from Group IA or IIA of the Periodic Table or oxides thereof; and g) 0 to 65% of a binder, wherein the components b), c), d), e) and f) are supported on the component a), and contents of at least two of the components b), c), d), e) and f) are larger than zero, is described. A process for preparing said catalyst composition and a process for the production of olefins via catalytic cracking by using said catalyst composition are also described.Type: ApplicationFiled: April 3, 2008Publication date: June 10, 2010Inventors: Zaiku Xie, Ma Guangwei, Yang Weimin, Yao Hui, Yang Xiaqin
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Publication number: 20100133145Abstract: A catalytic cracking catalyst composition is disclosed that is suitable for reducing the sulfur content of catalytically cracking liquid products, in particularly gasoline products, produced during a catalytic cracking process. Preferably, the catalytic cracking process is a fluidized catalytic cracking (FCC) process. The composition comprises zeolite, zinc and at least one rare earth element having an ionic radii of less than 0.95 ? at a coordination number of 6. Preferably, zinc and the rare earth element are present as cations that have been exchanged on the zeolite. The zeolite is preferably a Y-type zeolite.Type: ApplicationFiled: January 28, 2008Publication date: June 3, 2010Applicant: W. R. GRACE & CO.-CONN.Inventors: Richard Franklin Wormsbecher, Ruizhong Hu
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Patent number: 7709407Abstract: A supported palladium-gold catalyst is produced under mild conditions using a commonly available base, such as sodium hydroxide (NaOH) or sodium carbonate (Na2CO3). In this method, support materials and a base solution are mixed together and the temperature of the mixture is increased to a temperature above room temperature. Then, palladium salt and gold salt are added to the mixture while maintaining the pH of the mixture to be greater than 7.0 and keeping the mixture at a temperature above room temperature. This is followed by filtering out the supported palladium-gold particles, washing with warm de-ionized water and calcining.Type: GrantFiled: January 21, 2009Date of Patent: May 4, 2010Assignee: Nanostellar, Inc.Inventor: Xianghong Hao
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Patent number: 7691767Abstract: Provided are a catalyst which inhibits light paraffins form being produced in catalytic cracking of heavy hydrocarbons and which effectively produces olefins and a process in which the above catalyst is used to produce olefins from heavy hydrocarbons at a high yield. The catalyst is a catalytic cracking catalyst for catalytically cracking a hydrocarbon raw material, comprising (A) pentasil type zeolite modified with a rare earth element and zirconium and (B) faujasite type zeolite, and the process is a production process for olefin and a fuel oil, comprising bringing a heavy oil containing 50 mass % or more of a hydrocarbon fraction having a boiling point of 180° C. or higher into contact with the catalyst described above to crack it.Type: GrantFiled: January 17, 2007Date of Patent: April 6, 2010Assignees: Research Association of Refinery Integration for Group-Operation, Idemitsu Kosan Co., Ltd.Inventors: Kenichi Wakui, Kinsho Furusawa, Akio Suwa, Toshio Itoh, Hisao Nagashima
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Patent number: 7686949Abstract: An improved hydrotreating process for use with lube oil boiling range feedstreams utilizing a catalyst comprising a hydrogenation-dehydrogenation component selected from the Group VIII noble metals and mixtures thereof, a mesoporous support, and a binder.Type: GrantFiled: August 17, 2005Date of Patent: March 30, 2010Assignee: ExxonMobil Research and Engineering CompanyInventors: Stephen J. McCarthy, Jean W. Beeckman, Sylvain S. Hantzer, Geoffrey L. Woolery, Glenn R. Sweeten
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Publication number: 20100048383Abstract: A close coupled three-way catalyst for purification of exhaust gas of motor vehicle and the preparation thereof. The support is selected from cordierite honeycomb ceramic materials having a pore volume of 0.25-0.35 ml/g. The coating layer is the mixture of hexaaluminate and perovskite-type composite oxide, cerium-zirconium solid solution, rare-earth oxide and alumina, alkali-earth oxide and zeolite having a high Si/Al ratio. The active components are palladium-rhodium, rare-earth oxide and transition metal in the hexaaluminate and perovskite-type composite oxide. The catalyst has not only the function of low-temperature catalytic oxidation of hydrocarbons, but also the function of reduction of nitrogen oxides, and can be used for purifying the exhaust gas of motor vehicles using gasoline, liquid gas, or CNG as fuel.Type: ApplicationFiled: February 14, 2007Publication date: February 25, 2010Applicant: East China University of Science & TechnologyInventors: Guanzhong Lu, Yun Guo, Zhigang Zhang
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Patent number: 7662273Abstract: A process for producing lube oil basestocks wherein a wax containing lube oil boiling range feedstream is converted into a basestock suitable for use in motor oil applications by contacting it with a hydrodewaxing catalyst containing a medium pore molecular sieve having deposited thereon an active metal oxide and at least one hydrogenation metal selected from the Group VIII and Group VIB metals.Type: GrantFiled: August 17, 2005Date of Patent: February 16, 2010Assignee: ExxonMobil Research and Engineering CompanyInventors: William J. Murphy, Stuart L. Soled, Ian A. Cody, David W. Larkin, Terry E. Helton, Gary B. McVicker
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Patent number: 7662213Abstract: The present invention relates generally to zeolites having a silica/alumina ratio of less than or equal to 10 (Si/Al?10) that are exchanged with Ag+ and thermally treated in such a way to favor adsorption over alternative catalytic and chemically reactive functionalities. The adsorbents of the present invention and the method of producing such adsorbents maximize the working adsorption capacity through ?-complexation. Applications for such adsorbents include any process in which contaminants from gas streams can form ?-complexes with the Ag in the zeolite, particularly the removal of CO, ethylene, propylene and the like from air and CO/H2 from air in prepurifier adsorbers in the production of ultra high purity (UHP) N2.Type: GrantFiled: October 21, 2008Date of Patent: February 16, 2010Assignee: Praxair Technology, Inc.Inventors: Mark William Ackley, Philip A. Barrett
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Publication number: 20100010279Abstract: A catalyst composition comprising metal phosphate binder and zeolite can be used to enhance olefin yields during hydrocarbon cracking processes. The composition typically further comprises aluminum phosphate, and the metal of the metal phosphate is a metal other than aluminum. Depending on the metal chosen, enhanced propylene and isobutylene yields in fluid catalytic cracking processes can be obtained compared to catalysts that do not contain such metal phosphate binders. The catalyst can also comprise non-zeolitic molecular sieves, thereby making the composition suitable for use in areas outside of catalytic cracking, e.g., purification and adsorbent applications.Type: ApplicationFiled: July 14, 2009Publication date: January 14, 2010Inventor: Ranjit Kumar
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Patent number: 7641787Abstract: Compositions for reduction of NOx generated during a catalytic cracking process, preferably, a fluid catalytic cracking process, are disclosed. The compositions comprise a fluid catalytic cracking catalyst composition, preferably containing a Y-type zeolite, and a particulate NOx composition containing particles of a zeolite having a pore size ranging from about 3 to about 7.2 Angstroms and a SiO2 to Al2O3 molar ratio of less than about 500. Preferably, the NOx reduction composition contains NOx reduction zeolite particles bound with an inorganic binder. In the alternative, the NOx reduction zeolite particles are incorporated into the cracking catalyst as an integral component of the catalyst. Compositions in accordance with the invention are very effective for the reduction of NOx emissions released from the regenerator of a fluid catalytic cracking unit operating under FCC process conditions without a substantial change in conversion or yield of cracked products.Type: GrantFiled: November 7, 2008Date of Patent: January 5, 2010Assignee: W.R. Grace & Co.-Conn.Inventors: George Yaluris, Michael Scott Ziebarth, Xinjin Zhao
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Publication number: 20090326299Abstract: The invention relates to the use of a catalyst based on crystalline aluminosilicates for the conversion of oxygenates to lower olefins, the catalyst having an SiO2/Al2O3 molar ratio of 20 to 200 and being modified with 0.1% to 10% by weight of readily oxidant metal (calculated as the corresponding metal oxide) and/or with 0.05% to 5% by weight of cerium (calculated as Ce2O3), and also to an associated method.Type: ApplicationFiled: May 31, 2007Publication date: December 31, 2009Applicant: SUD-CHEMIE AGInventors: Arno Tissler, Rainer Rakoczy, Roderik Althoff
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Patent number: 7638453Abstract: A catalyst composition containing a medium pore molecular sieve having deposited thereon an active metal oxide and at least one hydrogenation metal selected from the Group VIII and Group VIB metals for use in hydrodewaxing lube oil boiling range feedstreams.Type: GrantFiled: August 17, 2005Date of Patent: December 29, 2009Assignee: ExxonMobile Research and Engineering CompanyInventors: William J. Murphy, Stuart L. Soled, Ian A. Cody, David W. Larkin, Terry E. Helton, Gary B. McVicker
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Publication number: 20090305873Abstract: A honeycomb structure includes at least one honeycomb unit having a longitudinal direction and including zeolite, an inorganic binder, and walls. The zeolite includes a first zeolite ion-exchanged with at least one of Cu, Mn, Ag, and V and a second zeolite ion-exchanged with at least one of Fe, Ti, and Co. Each wall has first and second surfaces which extend along the longitudinal direction and define a thickness of each wall. A ratio of the first zeolite by weight to a total weight of the first and second zeolites at a center of the thickness of each wall is larger than the ratio of the first zeolite at the first or second surface. A ratio of the second zeolite by weight to the total weight at the first or second surface is larger than the ratio of the second zeolite at the center of the thickness of each wall.Type: ApplicationFiled: July 29, 2009Publication date: December 10, 2009Applicant: IBIDEN CO., LTD.Inventors: Kazushige OHNO, Masafumi Kunieda, Takahiko Ido
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Publication number: 20090298673Abstract: An exhaust gas purification catalyst includes a catalyst layer formed on a support. The catalyst layer contains Ce-containing oxide particles having an oxygen storage/release capacity and a catalytic metal. The catalyst layer further contains a large number of iron oxide particles of 300 nm diameter or less that are dispersed therein and are in contact with the Ce-containing oxide particles. When observed by electron microscopy, the proportion of the area of iron oxide particles of 300 nm diameter or less to the total area of all of iron oxide particles in the catalyst layer is 30% or more.Type: ApplicationFiled: May 28, 2009Publication date: December 3, 2009Applicant: MAZDA MOTOR CORPORATIONInventors: Masaaki AKAMINE, Masahiko SHIGETSU, Hirosuke SUMIDA, Tatsuto FUKUSHIMA, Seiji MIYOSHI, Hiroshi YAMADA, Hideharu IWAKUNI, Koichiro HARADA
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Publication number: 20090297419Abstract: A catalyst and a method for selectively reducing nitrogen oxides with ammonia are provided. The catalyst includes a first component of copper, chromium, cobalt, nickel, manganese, iron, niobium, or mixtures thereof, a second component of cerium, a lanthanide, a mixture of lanthanides, or mixtures thereof, and a zeolite. The catalyst may also include strontium as an additional second component. The catalyst selectively reduces nitrogen oxides to nitrogen with ammonia at low temperatures. The catalyst has high hydrothermal stability. The catalyst has high activity for conversion of nitrogen oxides in exhaust streams, and are not significantly influenced by the NO/NO2 ratio. The catalyst and the method may have special application to selective reduction of nitrogen oxides in exhaust gas from diesel vehicles, although the catalyst and the method have broad application to a wide range of gas streams that contain nitrogen oxides.Type: ApplicationFiled: August 7, 2009Publication date: December 3, 2009Inventors: Stephen J. Golden, Svetlana Iretskaya
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Publication number: 20090291034Abstract: A honeycomb structure includes at least one honeycomb unit including zeolite, an inorganic binder, and cell walls. The cell walls extend from a first end face to a second end face to define cells along a longitudinal direction of the at least one honeycomb unit. Each of the cell walls includes a center part in the longitudinal direction and a first end part adjacent to the first end face. The first end part has a thickness larger than a thickness of the center part, and/or the first end part has a porosity smaller than a porosity of the center part.Type: ApplicationFiled: May 26, 2009Publication date: November 26, 2009Applicant: IBIDEN CO., LTD.Inventors: Kazushige OHNO, Masafumi Kunieda, Takahiko Ido
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Publication number: 20090291831Abstract: A honeycomb structure includes at least one honeycomb unit. The honeycomb unit includes plural cell walls to define plural cells, about 61 to about 70 mass % of zeolite, about 15 to about 25 mass % of an inorganic fiber, and about 10 to about 20 mass % of alumina other than alumina included in the zeolite and the inorganic fiber. The honeycomb unit has an opening ratio (%) of about 57% or more. The opening ratio is equal to or less than y shown in a formula of y=0.55x+30 when a content x (mass %) of the zeolite included in the honeycomb unit is less than about 66 mass %. The opening ratio is equal to or less than y shown in a formula of y 32 ?0.25x+82.8 when the content x (mass %) is about 66 mass % or more.Type: ApplicationFiled: January 26, 2009Publication date: November 26, 2009Applicant: IBIDEN CO., LTD.Inventors: Kazushige OHNO, Masafumi Kunieda, Takahiko Ido
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Publication number: 20090291832Abstract: A honeycomb structure includes a first end face, a second end face, and at least one honeycomb unit. The second end face is disposed opposite the first end face along a longitudinal direction of the honeycomb structure. The at least one honeycomb unit has plural cell walls extending along the longitudinal direction from the first end face toward the second end face to define plural cells. The at least one honeycomb unit includes about 50 mass % to about 60 mass % of zeolite, about 15 mass % to about 25 mass % of inorganic fibers, about 20 mass % to about 32 mass % of alumina that is not contained in the zeolite or the inorganic fibers, and an opening ratio Y(%). The opening ratio Y(%) satisfies an expression about 57?Y?0.7X+25, where X (mass %) is a zeolite content of the at least one honeycomb unit.Type: ApplicationFiled: February 11, 2009Publication date: November 26, 2009Applicant: IBIDEN CO., LTD.Inventors: Kazushige OHNO, Masafumi Kunieda, Takahiko Ido
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Publication number: 20090291833Abstract: A honeycomb structure includes center and peripheral regions. The center region has a smaller similarity shape in relation to a peripheral shape of the honeycomb structure in a cross section perpendicular to the longitudinal direction. The peripheral region is located outside the smaller similarity shape. Zeolite ion-exchanged with at least one of Cu, Mn, Ag, and V is present at a first weight ratio and a second weight ratio in the center region and the peripheral region, respectively, relative to a total weight of the zeolite. The second weight ratio is larger than the first weight ratio. Zeolite ion-exchanged with at least one of Fe, Ti, and Co is present at a third weight ratio and a fourth weight ratio in the center region and the peripheral region, respectively, relative to a total weight of the zeolite. The third weight ratio is larger than the fourth weight ratio.Type: ApplicationFiled: June 30, 2009Publication date: November 26, 2009Applicant: IBIDEN CO., LTD.Inventors: Kazushige OHNO, Masafumi KUNIEDA, Takahiko IDO
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Patent number: 7622413Abstract: A multifunctional additive for maximizing yield of light olefins and LPG, with a tolerance to contaminant metals. Maximization of the referenced properties is accomplished through the use of a zeolite treated with a phosphorus source, calcined and impregnated with a rare earth salt. The process for preparation of the referenced catalyst includes the following steps: preparation of a precursor containing a zeolite that is selective of olefins with a source of phosphorus; placement of a source of phosphorus in this precursor through calcination; deposition of rare earth salts on the surface of the additive for maximizing the yield of light olefins and LPG that forms; and drying the multifunctional additive formed.Type: GrantFiled: August 2, 2006Date of Patent: November 24, 2009Assignee: Petroleo Brasileiro S.A. - PetrobrasInventors: Lam Yiu Lau, Eliane Bernad Castro Mattos, Joao Eduardo Cerutti Karam, Ricardo Drolhe Montaury Pimenta, Rodolfo Eugênio Roncolatto
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Publication number: 20090272675Abstract: A method for producing a substantially desulfurized a hydrocarbon fuel stream at temperatures less than 100° C. The method includes providing a nondesulfurized fuel cell hydrocarbon fuel stream that may include water and passing the fuel stream sequentially through a zeolite Y adsorbent and a selective sulfur adsorbent. The zeolite Y adsorbent may be exchanged with copper ions. The method produces a substantially desulfurized hydrocarbon fuel stream containing less than 50 ppb sulfur.Type: ApplicationFiled: June 5, 2009Publication date: November 5, 2009Applicant: SUD-CHEMIE INC.Inventors: Chandra C Ratnasamy, Jon P. Wagner, R. Steve Spivey, Hans-Georg Anfang
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Patent number: 7601254Abstract: A process for the conversion of a hydrocarbon feedstock to produce olefins, aromatic compounds and ultra low sulfur diesel wherein the hydrocarbon feedstock is reacted in a fluid catalytic cracking (FCC) zone to produce olefins and light cycle oil. The effluent from the FCC is preferably separated to produce a stream comprising ethylene and propylene, a stream comprising higher boiling olefins and light cycle oil (LCO). The stream containing the higher boiling olefins is cracked to provide additional ethylene and propylene. The LCO is selectively hydrocracked to produce aromatic compounds and ultra low sulfur diesel.Type: GrantFiled: May 19, 2005Date of Patent: October 13, 2009Assignee: UOP LLCInventor: Christopher D. Gosling
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Publication number: 20090230023Abstract: The present invention 1, 2 or 3 provides a desulfurization function-added FCC catalyst which can efficiently reduce the sulfur content of FCC gasoline while maintaining the yield of FCC gasoline in a process of producing FCC gasoline by cracking of heavy oil.Type: ApplicationFiled: June 25, 2007Publication date: September 17, 2009Applicants: IDEMITSU KOSAN CO., LTD., PETROLEUM ENERGY CENTER, A JURIDICAL INC. FOUND.Inventors: Akira Iino, Toshio Itoh, Shinji Akashi
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Patent number: 7585812Abstract: A catalyst for use in the Fischer-Tropsch process, and a method to prepare the catalyst is disclosed. The catalyst of the present invention has a higher surface area, more uniform metal distribution, and smaller metal crystallite size than Fischer-Tropsch catalysts of the prior art.Type: GrantFiled: June 20, 2008Date of Patent: September 8, 2009Assignee: Sud-Chemie Inc.Inventors: X. D. Hu, Patrick J. Loi, Robert J. O'Brien
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Patent number: 7582202Abstract: A Composition comprising one or more metal hydroxy salts and a matrix, binder or carrier material, wherein the metal hydroxy salt is a compound comprising (a) as metal either (i) one or more divalent metals, at least one of them being selected from the group consisting of Ni, Co, Ca, Zn, Mg, Fe, and Mn, or (ii) one or more trivalent metal(s), (b) framework hydroxide, and (c) a replaceable anion. This composition has various catalytic applications.Type: GrantFiled: February 10, 2004Date of Patent: September 1, 2009Assignees: Akzo Nobel N.V., Albemarle Netherlands B.V.Inventors: William Jones, Paul O'Connor, Dennis Stamires
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Publication number: 20090211944Abstract: Oxidic composition consisting essentially of oxidic forms of a first metal, a second metal, and optionally a third metal, the first metal being either Ca or Ba and being present in the composition in an amount of from about 5 to about 80 wt %, the second metal being Al and being present in the composition in an amount of from about 5 to about 80 wt %, the third metal being selected from the group consisting of La, Ti, and Zr, and being present in an amount of from 0 to about 17 wt %—all weight percentages calculated as oxides and based on the weight of the oxidic composition, the oxidic composition being obtainable by (a) preparing a physical mixture comprising solid compounds of the first, the second, and the optional third metal, (b) optionally aging the physical mixture, without anionic clay being formed, and (c) calcining the mixture. This composition is suitable for use in FCC processes for the passivation of metals with only minimal influence on the zeolite's hydrothermal stability.Type: ApplicationFiled: June 2, 2006Publication date: August 27, 2009Applicant: Albemarle Netherlands B.V.Inventors: Dennis Stamires, Paul O'Connor, William Jones
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Patent number: 7576025Abstract: A composition comprising FCC catalyst particles and additive particles suitable for the reduction of NOx emissions from a FCC regenerator, said additive particles comprising a Mg and Al-containing anionic clay or solid solution, a rare earth metal oxide, alumina and/or silica-alumina, and Y-type zeolite. The invention further relates to a process for preparing such a composition and its use for reducing NOx emissions.Type: GrantFiled: October 12, 2004Date of Patent: August 18, 2009Assignee: Albemarle Netherlands B.V.Inventors: Christopher W. Kuehler, Paul O'Connor, Dennis Stamires
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Publication number: 20090196811Abstract: A NOx reduction catalyst is provided which reduces NOx in processing gas. The NOx reduction catalyst includes a catalyst substrate containing an oxide, a NOx absorption component, and a NOx purification component.Type: ApplicationFiled: May 17, 2007Publication date: August 6, 2009Applicant: CATALER CORPORATIONInventors: Yoshinori Yamashita, Norihiko Aono, Toshimi Murai
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Patent number: 7569511Abstract: An alcohol steam reforming catalyst for generating hydrogen contains palladium, yttrium, and at least one of cerium and a metal oxide. The catalyst displays both an improved alcohol conversion rate and improved carbon dioxide selectivity. Methods of making and using the alcohol steam reforming catalyst are described.Type: GrantFiled: May 5, 2006Date of Patent: August 4, 2009Assignee: BASF Catalysts LLCInventors: Christopher R. Castellano, Ye Liu, Ahmad Moini, Gerald Stephen Koermer, Robert Joseph Farrauto
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Publication number: 20090192338Abstract: Systems and methods for producing and using one or more doped catalysts are provided. One or more coked-catalyst particles can be fluidized in the presence of one or more oxidants to provide a fluidized mixture. The coke from the one or more coked-catalyst particles can be removed to provide regenerated catalyst particles within the fluidized mixture. One or more doping agents can be distributed to the fluidized mixture, and the one or more doping agents can be deposited onto the surface of the regenerated catalyst particles to provide a regenerated, doped catalyst particle.Type: ApplicationFiled: January 29, 2008Publication date: July 30, 2009Inventor: PRITHAM RAMAMURTHY
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Publication number: 20090163353Abstract: The invention is directed to an isomerization catalyst containing an intermediate pore size molecular sieve, a metal or metals selected from the group consisting of Ca, Cr, Mg, La, Ba, Pr, Sr, K and Nd which are effective in raising the isomerization selectivity, and additionally loaded with a Group VIII metal or metals for hydrogenation purposes.Type: ApplicationFiled: February 25, 2009Publication date: June 25, 2009Inventors: Joseph A. Biscardi, Darren P. Fong, Paul Marcantonio
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Publication number: 20090139898Abstract: The present invention provides a hydrogenation catalyst, containing a carrier, metal components of nickel, molybdenum and tungsten supported thereon, and an adjuvant component selected from the group consisting of fluorine and phosphor and combination thereof. In another embodiment, the present invention provides a hydrogenation catalyst, containing a carrier and metal components of nickel, molybdenum and tungsten supported thereon, wherein said carrier contains a molecular sieve. The present invention provides further use of said catalyst in the process for hydrogenating hydrocarbon oil. In comparison with a hydrogenation catalyst according to the prior art, the catalyst according to the present invention has a much higher activity.Type: ApplicationFiled: April 20, 2006Publication date: June 4, 2009Inventors: Xiangyun Long, Xuefen Liu, Hong Nie, Kui Wang, Jing Xin, Qinghe Liu, Xiaodong Gao, Zhihai Hu, Yahua Shi, Dadong Li
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Patent number: 7531706Abstract: A process for producing olefin by catalytic cracking of hydrocarbon material characterized in employing zeolite of penta-sil type comprising rare earth elements and at least one of manganese or zirconium as a catalyst. It enables to produce light olefin such as ethylene, propylene, and so on with selectively high yield and with long term stability, by catalytic cracking of gaseous or liquid hydrocarbon as ingredients under lower temperature than the conventional method and suppressing by-product such as aromatic hydrocarbon or heavy substances.Type: GrantFiled: October 21, 2003Date of Patent: May 12, 2009Assignee: Idemitsu Kosan Co., Ltd.Inventors: Kenichi Wakui, Yoshihiro Nakamura, Mitsuaki Hayashi
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Publication number: 20090118559Abstract: Oxidic composition consisting essentially of oxidic forms of a first metal, a second metal, and optionally a third metal, the first metal being either Fe or Zn and being present in the composition in an amount of from about 5 to about 80 wt %, the second metal being Al and being present in the composition in an amount of from about 5 to about 80 wt %, the third metal being selected from the group consisting of Mo, W, Ce, and V, and being present in an amount of from 0 to about 17 wt %—all weight percentages calculated as oxides and based on the weight of the oxidic composition, the oxidic composition being obtainable by (a) preparing a physical mixture comprising solid compounds of the first, the second, and the optional third metal, (b) optionally aging the physical mixture, without anionic clay being formed, and (c) calcining the mixture.Type: ApplicationFiled: June 2, 2006Publication date: May 7, 2009Applicant: ALBEMARLE NETHERLANDS B.V.Inventors: Dennis Stamires, Paul O'Connor, William Jones
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Patent number: 7524788Abstract: Process for preparing alkylated aromatic compounds which comprises reacting an aromatic compound with a ketone and hydrogen in the presence of a catalytic composition comprising a solid acid material and copper. A preferred aspect is to use a catalytic composition also containing one or more elements selected from elements of groups IIIA, IVA, IIIB, IVB, VB, VIB, VIIB, group VIII limited to Fe, Ru and Os, and of the series of lanthanides. A particularly preferred aspect is to use a catalytic composition containing one or more elements selected from elements of groups IIIA and VIB.Type: GrantFiled: December 18, 2002Date of Patent: April 28, 2009Assignee: Polimeri Europa S.p.A.Inventors: Gianni Girotti, Franco Rivetti, Stefano Ramello
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Publication number: 20090081098Abstract: A catalyst and a method for selectively reducing nitrogen oxides with ammonia are provided. The catalyst includes a first component of copper, chromium, cobalt, nickel, manganese, iron, niobium, or mixtures thereof, a second component of cerium, a lanthanide, a mixture of lanthanides, or mixtures thereof, and a zeolite. The catalyst may also include strontium as an additional second component. The catalyst selectively reduces nitrogen oxides to nitrogen with ammonia at low temperatures. The catalyst has high hydrothermal stability. The catalyst has high activity for conversion of nitrogen oxides in exhaust streams, and are not significantly influenced by the NO/NO2 ratio. The catalyst and the method may have special application to selective reduction of nitrogen oxides in exhaust gas from diesel vehicles, although the catalyst and the method have broad application to a wide range of gas streams that contain nitrogen oxides.Type: ApplicationFiled: November 20, 2008Publication date: March 26, 2009Inventors: Stephen J. Golden, Svetlana Iretskaya
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Patent number: 7507684Abstract: The invention relates to an extruded solid catalyst body for breaking down nitrogen oxides in the presence of a reducing agent as well as to a process for manufacture of said body. The solid catalyst body has an active material that contains 60 to 87% by weight of an ion-exchanged zeolite containing at least one metal from the group containing Cu, Hf, La, Au, In, V, lanthanoids and transition metals of group VIII of the periodic system, more than 10 to 37% by weight of aluminum oxide and 2 to 10% by weight of inorganic fibers. The solid catalyst body, the active material of which contains a zeolite can be manufactured by extrusion and has a high degree of mechanical stability at a high catalytic activity.Type: GrantFiled: December 29, 2006Date of Patent: March 24, 2009Assignee: Argillon GmbHInventors: Lothar Hofmann, Jörg Münch, Ralf Dotzel
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Patent number: 7507686Abstract: The sulfur content of liquid cracking products, especially the cracked gasoline, of the catalytic cracking process is reduced by the use of a sulfur reduction catalyst composition comprising a porous molecular sieve which contains a metal in an oxidation state above zero within the interior of the pore structure of the sieve as well as a cerium component which enhances the stability and sulfur reduction activity of the catalyst. The molecular sieve is normally a faujasite such as USY. The primary sulfur reduction component is normally a metal of Period 3 of the Periodic Table, preferably vanadium. The sulfur reduction catalyst may be used in the form of a separate particle additive or as a component of an integrated cracking/sulfur reduction catalyst.Type: GrantFiled: April 29, 2005Date of Patent: March 24, 2009Assignee: W. R. Grace & Co. - Conn.Inventors: Arthur W. Chester, Hye Kyung Cho Timken, Terry G. Roberie, Michael S. Ziebarth
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Patent number: 7485595Abstract: A molecular sieve-containing catalyst for cracking hydrocarbons, comprising molecular sieve, refractory inorganic oxide, clay and a metal component, wherein the amount of said molecular sieve is from 1 to 90% by weight, the refractory inorganic oxide is from 2 to 80% by weight, the clay is from 2 to 80% by weight, and the metal component is from 0.1 to 30% by weight, calculated as the oxide of said metal having its maximum valence state, based on the total amount of the catalyst, wherein said metal component exists essentially in a reduction state and is one or more metals selected from the group consisting of metals of Group IIIA (other than aluminum), and metals of Group IVA, VA, IB, IIB, VB, VIB and VIIB, and non-noble metals of Group VIII of the periodic table. The catalyst has higher cracking activity and higher sulfur reduction activity.Type: GrantFiled: May 28, 2004Date of Patent: February 3, 2009Assignees: China Petroleum & Chemical Corporation, Research Institute of Petroleum Processing, SinopecInventors: Jun Long, Yuxia Zhu, Huiping Tian, Yujian Liu, Zhenyu Chen, Yaoqing Guo, Zhijian Da, Jiushun Zhang, Mingyuan He
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Patent number: 7476638Abstract: The sulfur content of liquid cracking products, especially the cracked gasoline, of the catalytic cracking process is reduced by the use of a sulfur reduction additive comprising a porous molecular sieve which contains a metal in an oxidation state above zero within the interior of the pore structure of the sieve. The molecular sieve is normally a large pore size zeolite such as USY or zeolite beta or an intermediate pore size zeolite such as ZSM-5. The metal is normally a metal of Period 3 of the Periodic Table, preferably zinc or vanadium. The sulfur reduction catalyst may be used in the form of a separate particle additive or as a component of an integrated cracking/sulfur reduction catalyst.Type: GrantFiled: December 16, 2004Date of Patent: January 13, 2009Assignee: W. R. Grace & Co. - Conn.Inventors: Arthur W. Chester, Hye Kyung Cho Timken, Terry G. Roberie, Michael S. Ziebarth
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Patent number: 7459413Abstract: The present invention provides a catalyst and a process for its preparation and its use in cracking heavy feedstocks. The catalyst comprises one or more zeolites having a controlled silica to alumina ratio and preferably treated with alkali in the presence of a matrix component selected from the group consisting of clays, synthetic matrix other than pillared clay, and mixtures thereof. The catalyst are particularly useful in treating heavy feedstock such as residues from oil sands processing.Type: GrantFiled: February 21, 2007Date of Patent: December 2, 2008Assignee: State Key Laboratory of Heavy Oil ProcessingInventors: Baojian Shen, Jinsen Gao, Chunming Xu, Liang Zhao, Xianfeng Li, Pei Wu
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Publication number: 20080293561Abstract: A cracking catalyst, which contains alumina, phosphorus and molecular sieve, with or without clay, wherein said alumina is ?-alumina or a mixture of ?-alumina and ?-alumina and/or ?-alumina, and wherein the catalyst contains, on the basis of the total amount of the catalyst, 0.5-50 wt % of ?-alumina, 0-50 wt % of ?-alumina and/or ?-alumina, 10-70 wt % of molecular sieve, 0-75 wt % of clay, and 0.1-8 wt % of phosphorus, measured as P2O5. The catalyst not only has higher cracking activity and higher cracking ability for cracking heavy oil, but also improves significantly quality and yield of gasoline, LCO and LPG in cracking products.Type: ApplicationFiled: July 14, 2005Publication date: November 27, 2008Applicants: CHINA PETROLEUM & CHEMICAL CORPORATION, RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPECInventors: Jun Long, Zhonghong Qiu, Youbao Lu, Jiushun Zhang, Zhijian Da, Huiping Tian, Yuxia Zhu, Wanhong Zhang, Zhenbo Wang
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Patent number: 7456128Abstract: Disclosed herein are cracking catalysts useful in the thermo-catalytic cracking (TCC)—formerly called selective deep catalytic cracking (SDCC)—of petroleum naphthas, gas oils and other heavy hydrocarbon distillates to selectively produce light olefins, said catalyst comprising mesoporous mixed oxides modified by the presence of inorganic compounds containing chemical elements selected from phosphorus, sulfur, chlorine and mixtures thereof, said catalyst being supported on yttria stabilized zirconium oxide and/or aluminum oxide. Preferably, the catalyst will have the the following formula: (a) MoO3 and/or WO3; (b) La2O3; (c) CeO2; (d) P, S or Cl; (e) ZrO2; (f) Y2O3. Also preferably, the catalyst will be combined with a material selected from an acidic crystalline (modified or not) zeolite, an acidic silica molecular sieve and an acidic alumina. Also disclosed are methods of making said cracking catalysts. The cracking catalysts can be used in both mono- and dual reactor configurations.Type: GrantFiled: April 29, 2005Date of Patent: November 25, 2008Assignee: Valorbec, S.E.C., Represented by The Gestion Valeo, S.E.C.Inventor: Raymond Le Van Mao