HERBERT E BARNER
Engineering in Kinnelon, NJ
License number
Massachusetts 25804
Issued Date
Dec 17, 1971
Expiration Date
Jun 30, 2004
Type
Chemical Engineer
Address
Address
Kinnelon, NJ 07405
Professional information
Selective Oxidation Process And Catalyst Therefor
US Patent:
6417376, Jul 9, 2002
Filed:
Sep 29, 1999
Appl. No.:
09/407436
Inventors:
Chuen Y. Yeh - Edison NJ
Lawrence L. Murrell - South Plainfield NJ
Robert E. Trubac - Ridgewood NJ
Rudolf A. Overbeek - Chatham Township NJ
Chiung Y. Huang - Glen Ridge NJ
Cemal Ercan - Bloomfield NJ
Nelleke Vander Puil - Hoboken NJ
Herbert E. Barner - Kinnelon NJ
Lawrence L. Murrell - South Plainfield NJ
Robert E. Trubac - Ridgewood NJ
Rudolf A. Overbeek - Chatham Township NJ
Chiung Y. Huang - Glen Ridge NJ
Cemal Ercan - Bloomfield NJ
Nelleke Vander Puil - Hoboken NJ
Herbert E. Barner - Kinnelon NJ
Assignee:
ABB Lummus Global Inc. - Bloomfield NJ
International Classification:
B01J 27198
US Classification:
549248, 549534, 549259, 562532, 568472, 568475, 568479, 502209, 502305, 502348, 502350
Abstract:
A process for selectively oxidizing an organic molecule by reacting said organic molecule and oxygen in the presence of a selective oxidation catalyst supported on a mesh-like structure.
Supercritical Water Oxidation With Overhead Effluent Quenching
US Patent:
5200093, Apr 6, 1993
Filed:
Jun 3, 1991
Appl. No.:
7/709264
Inventors:
Herbert E. Barner - Kinnelon NJ
Chiung-Yuan Huang - Glen Ridge NJ
William R. Killilea - West Chelmsford MA
Glenn T. Hong - Tewksbury MA
Chiung-Yuan Huang - Glen Ridge NJ
William R. Killilea - West Chelmsford MA
Glenn T. Hong - Tewksbury MA
Assignee:
ABB Lummus Crest Inc. - Bloomfield NJ
International Classification:
C02F 174, C02F 1108
US Classification:
210761
Abstract:
In a supercritical oxidation process, the oxidized supercritical fluid effluent (46) discharged from the upper region of the reactor vessel (10) is contacted with a cold quench liquid (66) so as to produce a relatively solids free vapor stream (53) and a liquid stream (51) containing the bulk of the precipitates and other solids carried over in the oxidized supercritical fluid effluent (46). The temperature of the resultant liquid stream (51) is maintained at a temperature below the solids solubility inversion temperature, typically below 600. degree. F. , so as to dissolve a substantial portion of the precipitates and other solids collected therein.