Vice President Human Resources - Zaza Energy Corporation
Position:
Vice President Human Resources at ZaZa Enengy Corporation
Location:
Houston, Texas Area
Industry:
Oil & Energy
Work:
ZaZa Enengy Corporation
since Jun 2011
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Vice President Human ResourcesThe Hanover Company
Oct 1993 - May 2011
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Vice President Human ResourcesBaker Hughes
1980 - 1993
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Executive Assistant/Fleet Coordinator
Education:
University of Phoenix Bachelor of Science, Business Management
Training Director/System Analyst At Thomas Consulting Services
Position:
AMSI Consultant/Training Director at Thomas Consulting Services
Location:
Houston, Texas Area
Industry:
Computer Software
Work:
Thomas Consulting Services
since Jun 2004
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AMSI Consultant/Training DirectorKaplan Management - Houston, Texas Area Jun 2010 - Dec 2011
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Training Director/System AnalystMG Properties
2004 - 2008
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AMSI ConsultantAMSI
Jan 2003 - Jun 2004
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Senior Trainer/Implementation AnalystAMSI
Jan 2001 - Jan 2004
-
TrainerAMSI
Oct 2000 - Jan 2001
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Support RepresentativeBMS Management
May 1998 - May 2000
-
Accounting Clerk
Education:
The University of Texas at El Paso 1995 - 2000
B.A., Marketing
Assistant Director, Glasscock School Of Continuing Studies At Rice University
Position:
Asst CEO, CFO, and Travel Consultant at Thomas Retirement Center
Location:
Houston, Texas Area
Industry:
Higher Education
Work:
Thomas Retirement Center
since May 2010
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Asst CEO, CFO, and Travel ConsultantRice University
Oct 2001 - May 2011
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Assistant Director, Glasscock School of Continuing StudiesOklahoma Department of Career Tech - Stillwater, OK 1965 - 1997
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Administrative Assistant to State Director
Karen A. Thomas - Houston TX Kyle L. Preston - Port Neches TX
Assignee:
Texaco Chemical Inc. - White Plains NY
International Classification:
C07C40904, C07C 2710
US Classification:
568571
Abstract:
Tertiary butyl hydroperoxide and tertiary butyl alcohol are prepared from isobutane and oxygen in a vertical reactor by sparging a mixture of isobutane with oxygen to the bottom of the reactor, by charging a reaction mixture recycle stream to the reactor above the sparge point, by centrally charging a downwardly flowing stream of cooled fresh isobutane to the top of the reactor to induce central downflow of the fresh isobutane annular and upflow of the sparged mixture and the recycle stream, by withdrawing a liquid product stream adjacent the top of the reactor, by withdrawing a vapor product stream from the top of the reactor, by condensing entrained liquids in the vapor product, by recycling the condensed liquids and by recovering the liquid product stream.