Drg Holdings
Retired
Lake County Schools
Science Teacher and Petroleum Consultant
Mcat Services May 2005 - Sep 2008
Vice President Engineering and Plant Manager
Kbr, Inc. Dec 1997 - Dec 2002
Manager Magnacat Technology
Ashland Petroleum Company Aug 1980 - Dec 1997
Senior Research Scientist
Education:
Western Kentucky University
Bachelors, Bachelor of Science, Biology, Chemistry
Marshall University
Master of Science, Masters, Organic Chemistry
Skills:
Chemical Engineering Chemistry Process Engineering Catalysis Engineering Laboratory Science Energy Teaching Process Optimization Petroleum Project Management Classroom Educational Technology Management Process Control Chemical Processing Inventor Petroleum Refining Petroleum Systems Petroleum Products Technology Integration Secondary Education Instructional Technology Teacher Training
William P. Hettinger - Deerfield Beach FL Howard F. Moore - Catlettsburg KY Terry L. Goolsby - Ashland KY A. V. Peppard - Catlettsburg KY
Assignee:
Ashland Inc. - Ashland KY
International Classification:
B03C 100
US Classification:
209213
Abstract:
Optimized utilization of combinations of fluid catalyst magnetic separator, classifier, and/or attriter can be used to achieve lower catalyst cost, and better catalyst activity and selectivity through control of metal-on-catalyst, particle size and particle size distribution. This process is especially useful when processing high metal-containing feedstocks. This provides a catalyst recovery unit (RCU. TM. ) ancillary to an FCC or similar unit.
Hydrocarbon Conversion Catalyst Additives And Processes
Terry L. Goolsby - Ashland KY Maurice M. Mitchell - Ashland KY
Assignee:
Marathon Ashland Petroleum LLC
International Classification:
C10G 900 C10G 2904 C10B 5500 B01J 2390
US Classification:
208106
Abstract:
Magnetic separation of fluid cracking catalyst and magnetic hooks can be improved by adding antimony, in the feed or during catalyst manufacture, to enhance the magnetic susceptibility, thus increasing the separation efficiency of the older less active fluid cracking catalyst from the more desirable fraction for recycle. Antimony can also be used as a tag for determination of age distribution of said catalyst. Concentration levels of 0. 005-15 wt. % antimony (Sb) on the catalyst or sorbent are preferred. The invention is particularly preferred on catalyst and sorbents which comprise at least about 0. 001 wt. %, more preferably above about 0. 01 wt. % iron, because the antimony has been found to enhance the magnetic susceptibility of iron-containing particulates.
Combination Magnetic Separation, Classification And Attrition Process For Renewing And Recovering Particulates
William P. Hettinger - Deerfield Beach FL Howard F. Moore - Catlettsburg KY Terry L. Goolsby - Ashland KY A. V. Peppard - Catlettsburg KY
Assignee:
Ashland Inc. - Ashland KY
International Classification:
B07B 100 C10G 1100
US Classification:
209233
Abstract:
Optimized utilization of combinations of fluid catalyst magnetic separator, classifier, and/or attriter can be used to achieve lower catalyst cost, and better catalyst activity and selectivity through control of metal-on-catalyst, particle size and particle size distribution. This process is especially useful when processing high metal-containing feedstocks. This provides a catalyst recovery unit (RCU. TM. ) ancillary to an FCC or similar unit.
Cracking Catalyst With High Magnetic Susceptibility
Terry L. Goolsby - Ashland KY Maurice M. Mitchell - Ashland KY
Assignee:
Marathon Ashland Petroleum, LLC - Findlay OH
International Classification:
B01J 2904 B01J 2987 B01J 2906 B01J 2100 B01J 2900
US Classification:
502 60
Abstract:
A catalytic cracking catalyst comprising zeolite, kaolin, alumina and/or silica, antimony and 100-5,000 wt. ppm Ni is disclosed. The Ni-antimony interact in the environment of a fluidized catalytic cracking reactor to increase the magnetic susceptibility of the catalyst, permitting removal of nickel contaminated catalyst by magnetic separation.