Gerald Charles Tustin - Kingsport TN Joseph Robert Zoeller - Kingsport TN Leslie Sharon Depew - Kingsport TN
Assignee:
Eastman Chemical Company - Kingsport TN
International Classification:
C07C 6700
US Classification:
560238
Abstract:
This invention pertains to the preparation of vinyl acetate by contacting within a contact zone a mixture of ketene and acetaldehyde with an acid catalyst at about one bar pressure and between about 85. degree. and 200. degree. C. and removing the reaction products from the contact zone.
Method For Producing Acetaldehyde From Acetic Acid
Gerald C. Tustin - Kingsport TN Leslie S. Depew - Kingsport TN Nick A. Collins - Fall Branch TN
Assignee:
Eastman Chemical Company - Kingsport TN
International Classification:
C07C 4700 C07C 4500 B01J 2300 B01J 2342
US Classification:
568420
Abstract:
A method of producing acetaldehyde hydrogenates acetic acid in the presence of an iron oxide catalyst containing between 2. 5 and 90 wt % Pd, more preferably 10 and 80 wt % Pd and most preferably 20 and 60 wt % Pd. The catalyst has a specific surface area of less than 150 m. sup. 2 /g. Hydrogen and acetic acid are fed to a reactor in a hydrogen to acetic acid ratio of 2:1 to 25:1, more preferably in a hydrogen to acetic acid ratio of 3:1 to 15:1 and most preferably in a hydrogen to acetic acid ratio of 4:1 to 12:1. The hydrogenation is performed at a temperature of about 250. degree. C. to 400. degree. C. , more preferably about 270. degree. C. to 350. degree. C. and most preferably about 280. degree. C. to 325. degree. C. The hydrogenation of acetic acid produces a partially gaseous product, and acetaldehyde is absorbed from the partially gaseous product with a solvent containing acetic acid. The gas remaining after the absorption step contains hydrogen, and this gas is recycled for the hydrogenation of acetic acid.
Disclosed is a process for the preparation of acetaldehyde by the hydrogenation of ketene in the presence of a transition metal hydrogenation catalyst.
Gerald Charles Tustin - Kingsport TN Joseph Robert Zoeller - Kingsport TN Leslie Sharon Depew - Kingsport TN
Assignee:
Eastman Chemical Company - Kingsport TN
International Classification:
C07C 6700
US Classification:
560238
Abstract:
This invention pertains to the preparation of vinyl acetate by contacting a mixture of hydrogen and ketene with a heterogeneous catalyst containing a transition metal to produce acetaldehyde, which is then reacted with ketene in the presence of an acid catalyst to produce vinyl acetate.
Ester Synthesis Using Heterogeneous Au/Tio2 Catalyst
- Kingsport TN, US Sumit Chakraborty - Johnson City TN, US Leslie Sharon Depew - Kingsport TN, US
Assignee:
Eastman Chemical Company - Kingsport TN
International Classification:
C07C 67/44 B01J 23/52
Abstract:
A process for direct esterification of an alkyl aldehyde with an alkyl alcohol to produce an alkyl ester is disclosed. The process comprises reacting an alkyl aldehyde with an alkyl alcohol in the presence of an Au/TiOa catalyst, a base and an enal or oxygen to form an ester and an aldehyde. The process avoids liberation of water and avoids the step of oxidation of the alkyl aldehyde to an alkyl acid.
Surface Coating Incorporating Phase Change Material
- Kingsport TN, US Pruthesh Hariharrao Vargantwar - Kingsport TN, US Leslie Sharon Depew - Kingsport TN, US Glen Dennis Shields - Kingsport TN, US Jennifer Lynn Cogar - Unicoi TN, US
Assignee:
Eastman Chemical Company - Kingsport TN
International Classification:
E04B 1/76 C09D 105/16 C09K 5/06 C09D 5/26
Abstract:
A stable emulsion having a fluid medium; a phase change material (PCM) comprising a straight, branched and/or cyclic aliphatic moiety having from 3 to 18 carbon atoms, polymers, and copolymers having residues of the straight, branched and/or cyclic aliphatic moiety; and a modified cyclodextrin having at least one functional moiety capable of forming a stable emulsion with the PCM in the fluid medium. The invention further includes a modified paint or surface coating having from 10 to 99 weight % of a base coating and from 1 to 90 weight % of the stable emulsion admixed therein.