Celanese International Corporation

Virent, Inc.

Sabic Global Technologies B.v.

Dick Alan Nagaki

Josefina T Chapman

Craig J Peterson

Sean G Mueller

Heiko Weiner

Mark O Scates

Tianshu Pan

Alexandra S Locke

Randy Douglas Cortright

Ming Qiao

Elizabeth Bowden

Ilias S Kotsianis

Elizabeth Woods

Zhun Zhao

Himanshu Lodha

Zhenhua Zhou

David H West

Wugeng Liang

Raul Velasco Pelaez

Dustin Fickel

Aghaddin Mamedov

Istvan Lengyel

Paulette N Hazin

Krishnan Sankaranarayanan

Travis Conant

Yu-Lun Fang

C William Gundlach, Iv

Derek Falcone

Ashwin Patel

Jason Loiland

Lisa Kamke

Myat Noe Zin Myint

Craig T Peterson

Sean Mueller

Craig J Petersen

C William Gundlach Iv

The invention relates to a composition containing a catalyst having high catalytic stability for conducting oxidative coupling of methane (OCM) at high carbon efficiency, while improving both methane and oxygen conversion. Particularly, the inventive catalyst is a metal oxide supported catalyst, which contains an alkali metal promoter and a mixed metal oxide component having at least one alkali earth metal and at least one rare earth metal. The metal oxide support is selected in a manner, such that at least a portion of the metal oxide support is capable of reacting with at least a part or whole of the alkali metal promoter under conditions of calcination during catalyst preparation. The invention further provides a method for preparing such a metal oxide supported catalyst composition, using a calcination process. Additionally, the invention further describes a process for producing Chydrocarbons, using such a catalyst composition.

OCM catalyst composition having improved stability and carbon efficiency

Provided are systems and methods for obtaining ethylene and propylene products from, for example, shale gas and shale gas condensate feedstocks. These systems and method operate by utilizing a hydrocracker train to crack C4 and C5 hydrocarbons to a product stream of propane and ethane or using a hydrogenolysis train to process C4 and C5 hydrocarbons to a product stream of propane and ethane that is provided to a cracker for an efficient conversion to ethylene and propylene. The disclosed systems are configured to reduce the amount of offsite hydrogen needed and also provide product streams that include a well-defined set of products as compared to existing approaches.

Shale gas and condensate to chemicals

The present invention provides processes for catalytically converting biomass to oxygenated compounds suitable for use in bioreforming processes.

Catalytic biomass deconstruction

Disclosed is a catalyst comprising: a composition having a formula BNMOwherein B represents boron, N represents nitrogen, M comprises a metal or metalloid, and O represents oxygen, x ranges from 0 to 1, y ranges from 0.01 to 5.5; and z ranges from 0 to 16.5. The catalyst may be suitable for converting alkanes to olefins.

Functionalized boron nitride catalysts for the production of light olefins from alkane feeds via oxidative dehydrogenation

A method for producing Chydrocarbons and Hcomprising (a) introducing to a reactor a reactant mixture comprising methane, (b) heating the reactant mixture to a preheating temperature to yield a heated mixture, (c) generating free radicals in the heated mixture to form a primary effluent mixture comprising free radicals, Chydrocarbons, H, and unreacted methane, (d) reacting the primary effluent mixture in a secondary reaction zone to form a secondary effluent mixture comprising Chydrocarbons, H, free radicals, and unreacted methane, at a secondary reaction zone temperature that is greater than the preheating temperature, wherein a free radicals amount in the primary effluent mixture is greater than a free radicals amount in the secondary effluent mixture, (e) cooling the secondary effluent mixture to a quench temperature lower than the secondary reaction zone temperature to yield a product mixture comprising Chydrocarbons and H, and (f) recovering the product mixture.

Method for producing hydrocarbons by non-oxidative coupling of methane

The present invention provides processes for deconstructing biomass using a solvent produced in a bioreforming reaction.

Solvolysis of biomass using solvent from a bioreforming process

A process for selective formation of ethanol from acetic acid by hydrogenating acetic acid in the presence of a catalyst comprising a modified support having cobalt and an alkaline earth support modifier. The active metals may include a first metal of palladium, platinum, and combinations thereof and a second metal of copper, iron, nickel, zinc, silver, chromium, tin, and combinations thereof.

Hydrogenation catalysts with cobalt and alkaline-earth metal modified supports

In one embodiment, the invention is to a process for producing an acrylate product. The process comprises the step of dehydrating a crude alkylenating agent stream to form a dehydrated alkylenating agent stream and a water stream. The process further comprises reacting acetic acid with at least a portion of the dehydrated alkylenating agent stream to form a crude acrylate product stream comprising acrylate product and alkylenating agent stream. The dehydrating of the crude alkylenating stream is accomplished using at least one evaporator or at least one distillation column.

Processes for the production of acrylic acids and acrylates

In one embodiment, the invention is to a process for producing an acrylate product. The process comprises the step of providing a crude product stream comprising the acrylate product and an alkylenating agent. The process further comprises the step of separating at least a portion of the crude product stream to form an alkylenating agent stream and an intermediate product stream. The alkylenating agent stream comprises at least 1 wt % alkylenating agent and the intermediate product stream comprises acrylate product.

Processes for producing acrylic acids and acrylates

The invention relates to a process for producing an acrylate product comprising the step of reacting a reaction gas mixture A comprising methanol and oxygen to form a product gas mixture A. The process may further comprise the step of combining at least a portion of the product gas mixture A and acetic acid to form a reaction gas mixture B. The process may further comprise the step of reacting at least a portion of the acetic acid in the reaction gas input mixture B with at least a portion of the formaldehyde in the reaction gas input mixture B to form a product gas mixture B. The process may further comprise the step of separating at least a portion of the product gas mixture B to form an alkylenating agent stream comprising at least 1 wt % alkylenating agent and an intermediate acrylate product stream comprising acrylate product.

Integrated process for the production of acrylic acids and acrylates

The invention is to a process for producing an acrylate product. The process includes the steps of contacting an alkanoic acid and an alkylenating agent over a catalyst composition under conditions effective to produce the acrylate product. The catalyst composition comprises vanadium, bismuth and titanium. Preferably, the catalyst comprises 0.3 wt % to 30 wt % vanadium, 0.1 wt % to 69 wt % bismuth and 0.1 wt % to 61 wt % tungsten, in an active phase.

Catalyst for producing acrylic acids and acrylates

A process for producing a crude product stream including an acrylate product and an alkylenating agent and separating at least a portion of the crude product stream to form alkylenating agent and intermediate product streams. The alkylenating agent stream comprises at least 1 wt % alkylenating agent and the intermediate product stream comprises acrylate products in high concentration. The crude product stream is formed by contacting acetic acid and formaldehyde in the presence of at least one aldol condensation catalyst under conditions effective to form the stream. Catalysts which are particularly useful are multielement oxide active materials of the general formulaVPFeXXO.

In one embodiment, the invention is to a process for producing an acrylate product. The process includes the steps of contacting an alkanoic acid and an alkylenating agent over a catalyst composition under conditions effective to produce the acrylate product. The catalyst composition comprises a metal phosphate matrix containing vanadium and bismuth. Preferably, the catalyst comprises, in an active phase, vanadium to bismuth at a molar ratio of at least 0.02:1. Preferably, the catalyst composition is substantially free of titanium.

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The Woodlands, TX, United States of America

Dick Alan Nagaki