Patents by Inventor Michael D. Briscoe
Michael D. Briscoe has filed for patents to protect the following inventions. This listing includes patent applications that are pending as well as patents that have already been granted by the United States Patent and Trademark Office (USPTO).
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Patent number: 9453165Abstract: A process for converting a reactant composition comprising H2 and CO to a product comprising at least one aliphatic hydrocarbon having at least about 5 carbon atoms comprises: flowing the reactant composition through a microchannel reactor in contact with a Fischer-Tropsch catalyst to convert the reactant composition to the product, the microchannel reactor comprising a plurality of process microchannels containing the catalyst; transferring heat from the process microchannels to a heat exchanger; and removing the product from the microchannel reactor; the process producing at least about 0.5 gram of aliphatic hydrocarbon having at least about 5 carbon atoms per gram of catalyst per hour; the selectivity to methane in the product being less than about 25%. A supported catalyst comprises Co, and a microchannel reactor comprises at least one process microchannel and at least one adjacent heat exchange zone.Type: GrantFiled: April 30, 2015Date of Patent: September 27, 2016Assignee: Velocys, Inc.Inventors: Yong Wang, Anna Lee Tonkovich, Terry Mazanec, Francis P. Daly, Dave VanderWiel, Jianli Hu, Chunshe Cao, Charles Kibby, Xiaohong Li, Michael D. Briscoe, Nathan Gano, Ya-Huei Chin
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Publication number: 20150259609Abstract: The disclosed invention relates to a process for converting a reactant composition comprising H2 and CO to a product comprising at least one aliphatic hydrocarbon having at least about 5 carbon atoms, the process comprising: flowing the reactant composition through a microchannel reactor in contact with a Fischer-Tropsch catalyst to convert the reactant composition to the product, the microchannel reactor comprising a plurality of process microchannels containing the catalyst; transferring heat from the process microchannels to a heat exchanger; and removing the product from the microchannel reactor; the process producing at least about 0.5 gram of aliphatic hydrocarbon having at least about 5 carbon atoms per gram of catalyst per hour; the selectivity to methane in the product being less than about 25%. The disclosed invention also relates to a supported catalyst comprising Co, and a microchannel reactor comprising at least one process microchannel and at least one adjacent heat exchange zone.Type: ApplicationFiled: April 30, 2015Publication date: September 17, 2015Inventors: Yong Wang, Anna Lee Tonkovich, Terry Mazanec, Francis P. Daly, Dave VanderWiel, Jianli Hu, Chunshe Cao, Charles Kibby, Xiaohong Li, Michael D. Briscoe, Nathan Gano, Ya-Huei Chin
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Patent number: 9023900Abstract: Disclosed is a process for converting a reactant composition comprising H2 and CO to a product comprising at least one aliphatic hydrocarbon having at least about 5 carbon atoms, the process comprising: flowing the reactant composition through a microchannel reactor in contact with a Fischer-Tropsch catalyst to convert the reactant composition to the product, the microchannel reactor comprising a plurality of process microchannels containing the catalyst; transferring heat from the process microchannels to a heat exchanger; and removing the product from the microchannel reactor; the process producing at least about 0.5 gram of aliphatic hydrocarbon having at least about 5 carbon atoms per gram of catalyst per hour; the selectivity to methane in the product being less than about 25%. Also disclosed is a supported catalyst comprising Co, and a microchannel reactor comprising at least one process microchannel and at least one adjacent heat exchange zone.Type: GrantFiled: February 16, 2012Date of Patent: May 5, 2015Assignee: Velocys, Inc.Inventors: Yong Wang, Anna Lee Tonkovich, Terry Mazanec, Francis P. Daly, Dave VanderWiel, Jianli Hu, Chunshe Cao, Charles Kibby, Xiaohong Li, Michael D. Briscoe, Nathan Gano, Ya-Huei Chin
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Publication number: 20130217793Abstract: The disclosed invention relates to a process for converting a reactant composition comprising H2 and CO to a product comprising at least one aliphatic hydrocarbon having at least about 5 carbon atoms, the process comprising: flowing the reactant composition through a microchannel reactor in contact with a Fischer-Tropsch catalyst to convert the reactant composition to the product, the microchannel reactor comprising a plurality of process microchannels containing the catalyst; transferring heat from the process microchannels to a heat exchanger; and removing the product from the microchannel reactor; the process producing at least about 0.5 gram of aliphatic hydrocarbon having at least about 5 carbon atoms per gram of catalyst per hour; the selectivity to methane in the product being less than about 25%. The disclosed invention also relates to a supported catalyst comprising Co, and a microchannel reactor comprising at least one process microchannel and at least one adjacent heat exchange zone.Type: ApplicationFiled: February 16, 2012Publication date: August 22, 2013Inventors: Yong Wang, Anna Lee Tonkovich, Terry Mazanec, Francis P. Daly, Dave VanderWiel, Jianli Hu, Chunshe Cao, Charles Kibby, Xiaohong Li, Michael D. Briscoe, Nathan Gano, Ya-Huei Chin
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Patent number: 8188153Abstract: The disclosed invention relates to a process for converting a reactant composition comprising H2 and CO to a product comprising at least one aliphatic hydrocarbon having at least about 5 carbon atoms, the process comprising: flowing the reactant composition through a microchannel reactor in contact with a Fischer-Tropsch catalyst to convert the reactant composition to the product, the microchannel reactor comprising a plurality of process microchannels containing the catalyst; transferring heat from the process microchannels to a heat exchanger; and removing the product from the microchannel reactor; the process producing at least about 0.5 gram of aliphatic hydrocarbon having at least about 5 carbon atoms per gram of catalyst per hour; the selectivity to methane in the product being less than about 25%. The disclosed invention also relates to a supported catalyst comprising Co, and a microchannel reactor comprising at least one process microchannel and at least one adjacent heat exchange zone.Type: GrantFiled: March 5, 2010Date of Patent: May 29, 2012Assignee: Velocys, Inc.Inventors: Yong Wang, Anna Lee Tonkovich, Terry Mazanec, Francis P. Daly, Dave VanderWiel, Jianli Hu, Chunshe Cao, Charles Kibby, Xiaohong Shari Li, Michael D. Briscoe, Nathan Gano, Ya-Huei Chin
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Publication number: 20100160463Abstract: The disclosed invention relates to a process for converting a reactant composition comprising H2 and CO to a product comprising at least one aliphatic hydrocarbon having at least about 5 carbon atoms, the process comprising: flowing the reactant composition through a microchannel reactor in contact with a Fischer-Tropsch catalyst to convert the reactant composition to the product, the microchannel reactor comprising a plurality of process microchannels containing the catalyst; transferring heat from the process microchannels to a heat exchanger; and removing the product from the microchannel reactor; the process producing at least about 0.5 gram of aliphatic hydrocarbon having at least about 5 carbon atoms per gram of catalyst per hour; the selectivity to methane in the product being less than about 25%. The disclosed invention also relates to a supported catalyst comprising Co, and a microchannel reactor comprising at least one process microchannel and at least one adjacent heat exchange zone.Type: ApplicationFiled: March 5, 2010Publication date: June 24, 2010Inventors: Yong Wang, Anna Lee Tonkovich, Terry Mazanec, Francis P. Daly, Dave VanderWiel, Jianli Hu, Chunshe Cao, Charles Kibby, Xiaohong Shari Li, Michael D. Briscoe, Nathan Gano, Ya-Huei Chin
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Patent number: 7722833Abstract: A microchannel reactor is described which has at least one process microchannel and at least one heat exchange zone. The microchannel reactor may be used for conducting a Fischer-Tropsch synthesis reaction.Type: GrantFiled: July 11, 2006Date of Patent: May 25, 2010Assignee: Velocys, Inc.Inventors: Yong Wang, Anna Lee Tonkovich, Terry Mazanec, Francis P. Daly, Dave VanderWiel, Jianli Hu, Chunshe Cao, Charles Kibby, Xiaohong Shari Li, Michael D. Briscoe, Nathan Gano, Ya-Huei Chin
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Patent number: 7686855Abstract: Disclosed are methods for transporting one or more synthetic products produced from a carbonaceous source, such as coal, natural gas, or biomass, which may be located in a location that is remote from markets for such products. The synthetic products may include lower molecular weight alcohols such as methanol, lower molecular weight ethers such as dimethyl ether, olefins and/or the products of a Fischer-Tropsch or other hydrocarbon synthesis. The methods include transport of such synthetic products via a pipeline in the dense phase state, either neat or blended with light hydrocarbons, such as natural gas.Type: GrantFiled: September 6, 2005Date of Patent: March 30, 2010Assignee: BP Corporation North America Inc.Inventors: Ronald Sills, Theo H. Fleisch, Taras Y. Makogon, Michael D. Briscoe
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Patent number: 7168265Abstract: An integrated process for producing LNG and GTL products is provided, wherein a CO2-containing natural gas feed to an LNG production zone is first pre-treated to separate at least a portion of the CO2 therefrom, and the resulting CO2 stream obtained thereby is then directed to a GTL production zone and utilized to make GTL products that include methanol and/or methanol derivatives.Type: GrantFiled: March 22, 2004Date of Patent: January 30, 2007Assignee: BP Corporation North America Inc.Inventors: Michael D. Briscoe, Theo H. Fleisch, Michael J. Gradassi, Jeffrey H. Sawchuk, Pedro Ernesto Fischer-Calderon
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Patent number: 7084180Abstract: The disclosed invention relates to a process for converting a reactant composition comprising H2 and CO to a product comprising at least one aliphatic hydrocarbon having at least about 5 carbon atoms, the process comprising: flowing the reactant composition through a microchannel reactor in contact with a Fischer-Tropsch catalyst to convert the reactant composition to the product, the microchannel reactor comprising a plurality of process microchannels containing the catalyst; transferring heat from the process microchannels to a heat exchanger; and removing the product from the microchannel reactor; the process producing at least about 0.5 gram of aliphatic hydrocarbon having at least about 5 carbon atoms per gram of catalyst per hour; the selectivity to methane in the product being less than about 25%. The disclosed invention also relates to a supported catalyst comprising Co, and a microchannel reactor comprising at least one process microchannel and at least one adjacent heat exchange zone.Type: GrantFiled: January 28, 2004Date of Patent: August 1, 2006Assignee: Velocys, Inc.Inventors: Yong Wang, Anna Lee Tonkovich, Terry Mazanec, Francis P. Daly, Dave VanderWiel, Jianli Hu, Chunshe Cao, Charles Kibby, Xiaohong Shari Li, Michael D. Briscoe, Nathan Gano, Ya-Huei Chin
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Publication number: 20040248999Abstract: An integrated process for producing LNG and GTL products is provided, wherein a CO2-containing natural gas feed to an LNG production zone is first pre-treated to separate at least a portion of the CO2 therefrom, and the resulting CO2 stream obtained thereby is then directed to a GTL production zone and utilized to make GTL products that include methanol and/or methanol derivatives.Type: ApplicationFiled: March 22, 2004Publication date: December 9, 2004Inventors: Michael D. Briscoe, Theo H. Fleisch, Michael J. Gradassi, Jeffrey H. Sawchuk, Pedro Ernesto Fischer-Calderon
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Publication number: 20040244279Abstract: The invention is directed to compositions comprising mixtures of natural gas and dimethyl ether suitable for use as fuel compositions, and particularly to blends of dimethyl ether and a natural gas derived from LNG produced in an LNG process. The dimethyl ether can be added, for example, to a lean natural gas to improve the heat value thereof, and in embodiments, the dimethyl ether is conveniently derived from low value CO2 contaminants present in a raw natural gas stream used to prepare LNG. Also disclosed are methods to prepare the mixtures.Type: ApplicationFiled: March 22, 2004Publication date: December 9, 2004Inventors: Michael D. Briscoe, Theo H. Fleisch
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Patent number: 6749829Abstract: The present invention is directed to a process for producing synthesis gas comprising the steps of reacting a hydrogen-containing stream with an oxygen-containing stream and producing an oxidized stream comprising water; contacting a feedstream comprising hydrocarbon or hydrocarbon comprising at least one atom of oxygen with the oxidized stream comprising water and forming a reforming feedstream; and passing the reforming feedstream into a reforming reaction zone at reforming reaction conditions and producing a synthesis gas product.Type: GrantFiled: July 23, 2002Date of Patent: June 15, 2004Assignee: BP Corporation North America Inc.Inventor: Michael D. Briscoe
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Patent number: 6743829Abstract: An integrated process for producing LNG and GTL products is provided comprising cooling natural gas in at least one cooling step so as to provide a cooled natural gas stream; processing the cooled natural gas stream in at least two expansion/separation cycles, each expansion/separation cycle comprising the Substeps of (a) isentropically or isenthalpically expanding at least a portion of the cooled natural gas steam for producing a natural gas vapor component and a LNG component, (b) separating at least a portion of the natural gas vapor component from the LNG component, and (c) repeating substeps (a) through (b) wherein at least a portion of the LNG component from the previous expansion/separation cycle is directed to each successive Substep (a) and wherein the final LNG product is the LNG component after the final separating step and is substantially liquid at substantially atmospheric pressure; and converting at least a portion of one or more of the expansion/separation cycle natural gas vapor components inType: GrantFiled: January 18, 2002Date of Patent: June 1, 2004Assignee: BP Corporation North America Inc.Inventors: Ernesto Fischer-Calderon, Michael D. Briscoe, Michael J. Gradassi, Jeffrey H. Sawchuk
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Publication number: 20040018144Abstract: The present invention is directed to a process for producing synthesis gas comprising the steps of reacting a hydrogen-containing stream with an oxygen-containing stream and producing an oxidized stream comprising water; contacting a feedstream comprising hydrocarbon or hydrocarbon comprising at least one atom of oxygen with the oxidized stream comprising water and forming a reforming feedstream; and passing the reforming feedstream into a reforming reaction zone at reforming reaction conditions and producing a synthesis gas product.Type: ApplicationFiled: July 23, 2002Publication date: January 29, 2004Inventor: Michael D. Briscoe
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Publication number: 20030136146Abstract: An integrated process for producing LNG and GTL products is provided comprising cooling natural gas in at least one cooling step so as to provide a cooled natural gas stream; processing the cooled natural gas stream in at least two expansion/separation cycles, each expansion/separation cycle comprising the Substeps of (a) isentropically or isenthalpically expanding at least a portion of the cooled natural gas steam for producing a natural gas vapor component and a LNG component, (b) separating at least a portion of the natural gas vapor component from the LNG component, and (c) repeating substeps (a) through (b) wherein at least a portion of the LNG component from the previous expansion/separation cycle is directed to each successive Substep (a) and wherein the final LNG product is the LNG component after the final separating step and is substantially liquid at substantially atmospheric pressure; and converting at least a portion of one or more of the expansion/separation cycle natural gas vapor components inType: ApplicationFiled: January 18, 2002Publication date: July 24, 2003Inventors: Ernesto Fischer-Calderon, Michael D. Briscoe, Michael J. Gradassi, Jeffrey H. Sawchuk
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Patent number: 6344491Abstract: A method for producing a synthesis gas from a light hydrocarbon stream using air or oxygen-enriched air as an oxidant in a high pressure autothermal reactor and converting the synthesis gas in a Fischer-Tropsch process using a supported cobalt catalyst to produce heavy paraffins wherein the required process pressure is supplied by charging the reactant streams to the autothermal reactor at a high pressure.Type: GrantFiled: September 16, 1999Date of Patent: February 5, 2002Assignee: Syntroleum CorporationInventors: Gary L. Beer, Michael D. Briscoe
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Patent number: 6239184Abstract: A process for extending the life of a Fisher-Tropsch catalyst in a process for converting synthesis gas produced in an autothermal reactor by the substoichiometric oxidation of a light hydrocarbon gas by removing ammonia from the synthesis gas prior to passing the synthesis gas to a Fischer-Tropsch reactor.Type: GrantFiled: September 22, 1999Date of Patent: May 29, 2001Assignee: Syntroleum CorporationInventors: Gary L. Beer, James F. Leahy, Greg A. Lisewsky, Kernan J. McHugh, Michael D. Briscoe
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Patent number: 6156234Abstract: An improved process for the compression and heating of air or oxygen-enriched air for charging to an autothermal reactor by using a single high compression ratio compressor to produce a high-pressure, high-temperature air or oxygen-enriched air stream for mixture with a hydrocarbon gas stream to produce a charge stream to an autothermal reactor at an elevated pressure above about 350 psig and at an elevated temperature from about 700 to about 900.degree. F.Type: GrantFiled: September 23, 1999Date of Patent: December 5, 2000Assignee: Atlantic Richfield CompanyInventors: Michael D. Briscoe, Kernan J. McHugh, John R. Wolflick