Celanese International Corporation

Velocys Corp.

Celanese International Corporaton

Celanese International Corportation

Victor J Johnston

Heiko Weiner

R Jay Warner

Radmila Jevtic

Lincoln Sarager

David E Lee

Josefina T Chapman

Zhenhua Zhou

Trinity Horton

Adam Orosco

James H Zink

Radmila Wollrab

Laiyuan Chen

Barbara F Kimmich

Gerald Grusendorf

Emily Duff

Manuel Salado

John L Potts

Jan Cornelis Van Der Waal

Tianshu Pan

Trinity Horton Hale

Virginie Zuzaniuk

Nathan Kirk Powell

Mark O Scates

Robert Cunningham

Fred Ronald Olsson

Robert Alan Deck

Claudio Ribeiro

Nathan Bower

Deborah R Repman

Ronald David Shaver

Dheeraj Kumar

Xiaoyan Tu

Iva Franjkic

Al Amleh

Gerald Gruesendorf

Anna Lee Tonkovich

Terry Joseph Mazanec

Sean P Fitzgerald

Thomas D Yuschak

Bin Yang

Francis P Daly

Kai Jarosch

Leslie E Wade

Michael E Huckman

James A Foster

Tony Hammock

Wael Amleh

Samuel Roundy

Murray Viard

Cheng Zhang

Kenneth Balliet

Daniel Lindley

G Paull Torrence

Raymond J Zinobile

Ilias S Kotsianis

Qiang Yao

Kevin Clair Hanks

Andrew Shuff

Alfonso Javier Torres

Stephen Kerlegon

Radmilla Wollrab

Trinity Hale Horton

Barabra Kimmich

Jessica Freeman

Lauren Moore

Fred Ronaold Olsson

David Lee

Jay R Warner

Trinity Hale

Deborah H Repman

The present invention produces ethanol in a stacked bed reactor that comprises a first catalyst and a second catalyst, wherein the first and second catalysts comprise at least one group VIII metal, and wherein the second catalyst is substantially free of copper. The crude ethanol product may be separated and ethanol recovered.

Process for producing ethanol using multiple beds each having different catalysts

A process is disclosed for producing ethanol, comprising contacting acetic acid and hydrogen in a reactor in the presence of a catalyst comprising a binder, a mixed oxide, and at least two promoter metals comprising ruthenium and bismuth. The mixed oxide preferably also comprises cobalt and tin.

Ruthenium-bismuth mixed oxide hydrogenation catalysts and processes for producing ethanol

A process is disclosed for producing ethanol, comprising contacting acetic acid and hydrogen in a reactor in the presence of a catalyst comprising a binder and a mixed oxide comprising cobalt and preferably tin, wherein the mixed oxide is present in an amount from 60 to 90 wt. %, based on the total weight of the catalyst.

Hydrogenation catalysts comprising a mixed oxide and processes for producing ethanol

The present invention is to a process for producing a anhydrous ethanol composition comprising hydrogenating acetic acid in the presence of a catalyst to form a crude ethanol product; separating in a first column at least a portion of the crude ethanol product into a first distillate comprising ethanol, water and ethyl acetate, and a first residue comprising acetic acid; separating in a second column at least a portion of the first distillate into a second distillate comprising ethyl acetate and a second residue comprising ethanol and water; separating in a third column at least a portion of the second residue into a third distillate comprising ethanol and residual water and a third residue comprising separated water; and dehydrating at least a portion of the third distillate to form the anhydrous ethanol composition. The anhydrous ethanol composition, as formed, comprises less than 1 wt. % water.

Processes for producing anhydrous ethanol compositions

A process is disclosed for producing ethanol, comprising contacting hydrogen and a feed stream comprising acetic acid in a reactor in the presence of a catalyst comprising a binder and a mixed oxide comprising a promoter metal and tin, and preferably also comprising cobalt. The promoter metal is selected from the group consisting of rhenium, ruthenium, rhodium, palladium, osmium, iridium, platinum, and combinations thereof. The feed stream may comprises pure acetic acid or may comprise a mixture of 50 to 95 wt. % acetic acid and 5 to 50 wt. % ethyl acetate.

Hydrogenation catalysts comprising a mixed oxide comprising a promoter metal

The present invention relates to catalysts, to processes for making catalysts and to chemical processes employing such catalysts. The catalysts are preferably used for converting acetic acid to ethanol. The catalyst comprises a precious metal and one or more active metals on a modified support. The modified support may comprise cobalt tungstate.

Process for producing ethanol using hydrogenation catalysts

The present invention is directed to the separation of ethanol from a crude ethanol product obtained from the vaporization and hydrogenation of acetic acid using reduced residence time for the vapor phase reactants between exiting the vaporizer and entering the reactor. The crude ethanol product is separated in at least one column to recover an ethanol product.

Hydrogenation process with reduced residence time for vapor phase reactants

The present invention relates to a process for the formation of alcohols from alkanoic acids, the steps of the process comprising: contacting a feed stream containing the alkanoic acid and hydrogen at an elevated temperature with a hydrogenating catalyst comprising from 3 to 25 wt. % of active metals on a support, wherein the active metals comprise cobalt and tin.

Cobalt/tin catalyst for producing ethanol

In one embodiment, the invention is to a process for purifying a crude ethanol product. The process comprises the step of hydrogenating acetic acid in a reactor in the presence of a catalyst to form the crude ethanol product. The process further comprises the step of separating at least a portion of the crude ethanol product in a purification zone. The purification zone preferably comprises a first column, which yields a first distillate comprising ethanol, water and ethyl acetate, and a first residue comprising acetic acid. The at least a portion of the crude ethanol product has a residence time from the reactor to the purification zone from 5 minutes to 5 days.

Processes for maximizing ethanol formation in the hydrogenation of acetic acid

Recovery of ethanol from a crude ethanol product obtained from the hydrogenation of acetic acid and by reacting a portion of the crude ethanol product or one or more derivative streams containing ethyl acetate obtained therefrom in the presence of hydrogen, via hydrogenolyzis. The one or more derivative streams comprise ethyl acetate that are reacted via hydrogenolyzis to form additional ethanol that may be directly or indirectly fed to the separation zone or the hydrogenation reactor.

Hydrogenolysis of ethyl acetate in alcohol separation processes

The present invention relates to a catalyst having an amorphous support and one or more active metals. The amorphous support may comprise a support material and an amorphous support modifier, which adjusts the acidity of the support material. In preparing the amorphous catalyst, post-synthesis treatment, i.e. calcination, may be used to adjust the catalyst performance while converting acetic acid to ethanol.

Hydrogenation catalysts having an amorphous support

In one embodiment, the invention is to a method for producing a vinyl acetate composition. The method comprises the step of contacting acetic acid, oxygen, and ethylene under conditions effective to form a crude vinyl acetate composition comprising vinyl acetate, acetic acid, residual oxygen, and water. The method further comprises the step of contacting the crude vinyl acetate composition or a derivative thereof with at least one scavenger to form a treated crude vinyl acetate composition.

Methods for producing a vinyl acetate composition having a low impurity content

A process for recovering ethanol obtained from the hydrogenation of acetic acid. The crude ethanol product is separated in a column to produce a distillate stream comprising acetaldehyde and ethyl acetate and a residue stream comprising ethanol, acetic acid, ethyl acetate and water. The ethanol product is recovered from the residue stream.

Process to recover alcohol with reduced water from overhead of acid column

A process for produce ethanol by hydrogenation acetic acid and/or esters thereof is disclosed. The process involves reacting hydrogen feed stream with an acetic acid feed stream in a reactor operated in the presence of a catalyst to form an ethanol mixture and monitoring carbon monoxide concentration of the fresh hydrogen feed stream and adjusting temperature in the reactor in response to the carbon monoxide concentration of the fresh hydrogen feed stream.

Process for producing ethanol by hydrogenation with carbon monoxide controls

Recovery of ethanol from a crude ethanol product obtained from the hydrogenation of acetic acid using a low energy process. The crude ethanol product is separated in a column to produce a distillate stream comprising acetaldehyde and a residue stream comprising ethanol, acetic acid, ethyl acetate and water. The ethanol product is recovered from the residue stream.

Process to recover alcohol from an ethyl acetate residue stream

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Houston, TX, United States of America

Victor J Johnston