Celanese International Corporation

Exxonmobil Chemical Patents Inc.

Other

Dow Global Technolgoies LLC

University of Michigan

Jeremy J Patt

Larry Lee Iaccino

Neeraj Sangar

Teng Xu

Kenneth Ray Clem

J Scott Buchanan

Elizabeth L Stavens

Levi T Thompson

Mark O Scates

Ronald David Shaver

James H Zink

Mobae Afeworki

Cory Bernard Phillips

Barbara F M Kimmich

James R Ogle

Mark A Nierode

Chang Hwan Kim

Shyamal K Bej

Dong Ju Moon

A carbonylation process for producing acetic acid including: (a) carbonylating methanol or its reactive derivatives in the presence of a Group VIII metal catalyst and methyl iodide promoter to produce a liquid reaction mixture including acetic acid, water, methyl acetate and methyl iodide; (b) feeding the liquid reaction mixture at a feed temperature to a flash vessel which is maintained at a reduced pressure; (c) flashing the reaction mixture to produce a crude product vapor stream.

Method and apparatus for carbonylating methanol with acetic acid enriched flash stream

A carbonylation process for producing acetic acid including: (a) carbonylating methanol or its reactive derivatives in the presence of a Group VIII metal catalyst and methyl iodide promoter to produce a liquid reaction mixture including acetic acid, water, methyl acetate and methyl iodide; and (b) feeding the liquid reaction mixture at a feed temperature to a flash vessel which is maintained at a reduced pressure.

A method comprising: a) contacting an article comprising one or more blades (), the one or more blades () having a leading edge () curved upward and separated into prongs () by one or more notches () in the one or more blades (), with two or more substrates () joined by a pasty material overflowing at one or more seams (), where the one or more notches () of the article straddle the one or more seams (); and b) moving the article or the substrates () such that the pasty material overflowing at the one or more seams () is removed.

Process for removing excess pasty material joining a plurality of substrates

A carbonylation process for producing acetic acid including: (a) carbonylating methanol or its reactive derivatives in the presence of a Group VIII metal catalyst and methyl iodide promoter to produce a liquid reaction mixture including acetic acid, water, methyl acetate and methyl iodide; (b) feeding the liquid reaction mixture to a flash vessel; (c) flashing the reaction mixture to produce a crude product vapor stream.

A method comprising; a) assembling a plurality of ceramic filters, into an array wherein two or more of the outer surfaces of each filter are located adjacent to outer surfaces of other ceramic filters with removable spacers located between the adjacent surfaces of ceramic filters such that the spaces between, the adjacent surfaces are uniform m a work surface; b) removing sequentially one or more of the ceramic filters or horizontal rows of the ceramic filters and removing the spacers between adjacent surfaces until a single ceramic fitter or horizontal row remains; c) applying a cement layer to the outer surface of the single ceramic filter or horizontal row on the work surface; d) replacing the next adjacent ceramic filter or horizontal row of ceramic filters in the location the ceramic filler or horizontal row of ceramic filters were removed from; e) sequentially applying layers of cement to the outer surface of a ceramic filter or outer surfaces of a horizontal row of ceramic filters and replacing the next adjacent ceramic filter or horizontal, row of ceramic filters in the location or locations the ceramic filter or horizontal rows of ceramic filters were removed from, until all of the ceramic filters are replaced in the same position on the work surface with uniform cement layers located between all adjacent surfaces of rise ceramic filters.

Process for bonding arrays of ceramic filters

A carbonylation process for producing acetic acid including: (a) carbonylating methanol or its reactive derivatives in the presence of a Group VIII metal catalyst and methyl iodide promoter to produce a liquid reaction mixture including acetic acid, water, methyl acetate and methyl iodide; (b) feeding the liquid reaction mixture at a feed temperature to a flash vessel which is maintained at a reduced pressure; (c) heating the flash vessel while concurrently flashing the reaction mixture to produce a crude product vapor stream, wherein the reaction mixture is selected and the flow rate of the reaction mixture fed to the flash vessel as well as the amount of heat supplied to the flash vessel is controlled such that the temperature of the crude product vapor stream is maintained at a temperature less than 90&#xb0; F. cooler than the feed temperature of the liquid reaction mixture to the flasher and the concentration of acetic acid in the crude product vapor stream is greater than 70% by weight of the crude product vapor stream.

A watch comprises a case, an electronic movement module inside the case, a piece of closed-cell foam inside the case, and a dielectric liquid filling the remaining voids of the interior of the case. The closed-cell foam compensates for thermal expansion of the dielectric liquid over a wide range of operating temperatures. Upon heating, the liquid expands and the foam is compressed. Upon cooling, the liquid contracts and the foam is decompressed.

Thermal expansion compensator for liquid-filled watches

A process for reducing the aldehyde concentration in a target stream of a carbonylation process is disclosed. More specifically, a process for reducing the aldehyde concentration in an internal process stream or feed stream of a carbonylation process is disclosed. In particular, a process in which a target stream comprising a carbonylatable reactant and a first aldehyde concentration is subjected to a reaction comprising a supported catalyst that comprises at least one Group 8 to Group 11 metal at conditions sufficient to reduce the first aldehyde concentration to a second aldehyde concentration is disclosed.

Process for the reduction of aldehyde concentration in a target stream

In a process for converting a low carbon number aliphatic hydrocarbon to higher hydrocarbons including aromatic hydrocarbons, a feed containing the aliphatic hydrocarbon is contacted with a dehydrocyclization catalyst under conditions effective to convert the aliphatic hydrocarbon to aromatic hydrocarbons and produce an effluent stream comprising aromatic hydrocarbons and hydrogen. The dehydrocyclization catalyst comprises a metal or metal compound and a molecular sieve wherein the ratio of the amount of any Bronsted acid sites in the catalyst to the amount of said metal in the catalyst is less than 0.4 mol/mol of said metal.

Production of aromatics from aliphatics

In a process for converting methane to aromatic hydrocarbons, a feed containing methane is supplied to one or more reaction zone(s) containing catalytic material operating under reaction conditions effective to convert at least a portion of the methane to aromatic hydrocarbons; the reaction zone(s) being operated with an inverse temperature profile.

Production of aromatics from methane

In a process for converting methane to aromatic hydrocarbons, a feed containing methane and a particulate catalytic material are supplied to a reaction zone operating under reaction conditions effective to convert at least a portion of the methane to aromatic hydrocarbons and to deposit carbonaceous material on the particulate catalytic material causing catalyst deactivation. At least a portion of the deactivated particulate catalytic material is removed from the reaction zone and is heated to a temperature of about 700&#xb0; C. to about 1200&#xb0; C. by direct and/or indirect contact with combustion gases produced by combustion of a supplemental fuel. The heated particulate catalytic material is then regenerated with a hydrogen-containing gas under conditions effective to convert at least a portion of the carbonaceous material thereon to methane and the regenerated catalytic particulate material is recycled back to the reaction zone.

Growing community of inventors

Lake Jackson, TX, United States of America

Jeremy J Patt