2014 to 2000 Visiting Adjunct Professor of Black Studies and TheatreRap Arts Youth Fellowship Program - The Center for Families and Children
2008 to 2000Cleveland School of the Arts
Mar 2013 to 2014Randolph-Macon College
2008 to 2014 Lecture/Demo Acting WorkshopsNeighborhood Leadership Association
2013 to 2013Silent Voices
2013 to 2013I Too Sing America
2012 to 2012Denison University
2006 to 2012 Visiting Assistant Professor/Vail Guest ArtistCleveland Public Theatre Lecture
2008 to 2008 Demo Acting WorkshopMacalester College Saint Paul, MN 2007 to 2007Macalester College
2003 to 2003Macalester College
2000 to 2003 Assistant Professor of Dramatic ArtsLaughter on the Twenty Third Floor Wooster, OH 2002 to 2002Quatermainie's Terms
2000 to 2000Three Ways Home
2000 to 2000The College of Wooster
1995 to 2000 Assistant Professor of TheatreYoungstown Early Intervention Program
1995 to 2000The Man of La Mancha Athens, OH 1995 to 1995Ohio University
1993 to 1995 Graduate Assistantship, Stage Management and ActingWayne State University Detroit, MI 1994 to 1994Upward Bound College Prep Academy
1993 to 1994Three Ways Home
1993 to 1993Quartermaine's Terms
1993 to 1993 STAGE MANAGEMENT (Academic)Wayne State University
1992 to 1992 Graduate Assistantship, ActingThe Joseph Papp Public Theatre New York, NY 1987 to 1992 Acting and PlaywritingThe Joseph Papp Public Theatre London 1988 to 1988The South Bronx Community Action Theatre
1986 to 1987 Theatre DirectorMind Builders
1986 to 1986 ActingAmerican Folk Theatre
1983 to 1983 ActingGifted and Talented Program
1981 to 1981 Playwrights Horizons, Acting
Education:
Ohio University 1995 M.F.A.Wayne State University 1992 to 1993Ohio University 1975 B.F.A.
Us Patents
Solid Catalyst Alkylation Process With Regeneration Section And Hydrogen Fractionation Zone
Dale J. Shields - Buffalo Grove IL Paul A. Sechrist - Des Plaines IL
Assignee:
UOP LLC - Des Plaines IL
International Classification:
C07C 260
US Classification:
585719, 585712, 585713, 585727
Abstract:
An alkylating agent alkylates an alkylation substrate in a solid catalyst alkylation process in which an alkylation reactor produces a reaction effluent and a catalyst regeneration zone produces a hydrogen-containing regeneration effluent. The alkylation effluent passes to an alkylate fractionation zone, while the regeneration effluent passes to a hydrogen fractionation zone to remove hydrogen and produce a hydrogen-depleted stream that passes to the alkylate fractionation zone. The process recycles hydrogen, and can recycle halogen-containing species as well, within the process while preventing admixture of hydrogen with the alkylating agent. This invention is particularly applicable to alkylation processes that use an olefinic alkylating agent.
Alkylation Process With Efficient Effluent Refrigeration
Lynn H. Rice - Arlington Heights IL, US Dale J. Shields - Grayslake IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
C07C 2/56 C07C 5/27
US Classification:
585332, 585331, 585734, 585709
Abstract:
An integrated isomerization-alkylation process is disclosed that uses a common distillation zone. The process can comprise halogen removal. The process is suitable for the production of motor fuels from isoparaffins and olefins using solid alkylation and isomerization catalysts.
Processes For The Isomerization Of Normal Butane To Isobutane
David J. Shecterle - Des Plaines IL, US Dale J. Shields - Des Plaines IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
C07C 5/27 C07C 7/144
US Classification:
585738, 585818
Abstract:
In a normal butane isomerization process where the isomerization effluent () is fractionated in a deisobutanizer () operated such that a lower boiling fraction () is provided containing at least 80 mass-% isobutane and a higher boiling fraction () containing normal butane and at least 10 mass-% isobutane. The higher boiling fraction () is contacted with a selectively permeable membrane () to provide a permeate () containing normal butane-containing and a retentate () containing at least 80 mass-% isobutane. The preferred membranes are sieving membranes having a CPermeate Flow Index of at least 0. 01 and a CPermeate Flow Ratio of at least 1. 25:1.
Process And Apparatus For Oligomerization In Multiple Stages With Single Fractionation Column
Bipin V. Vora - Naperville IL, US Charles P. Luebke - Mount Prospect IL, US Jill M. Meister - Elk Grove Village IL, US Michael A. Schultz - Chicago IL, US Dale J. Shields - Buffalo Grove IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
C07C 2/08
US Classification:
585517, 585510, 585520
Abstract:
In an oligomerization process comprising at least two oligomerization reactors, at least portions of product streams from two reactors are separated in the same separator vessel. In an embodiment, a liquid product stream from the first oligomerization reactor is fed to a fractionation column and a side cut from the fractionation column feeds the second oligomerization reactor.
Processes For The Isomerization Of Normal Butane To Isobutane
In a normal butane isomerization process where the isomerization effluent () is fractionated in a deisobutanizer () operated such that a lower boiling fraction () is provided containing at least 80 mass-% isobutane and a higher boiling fraction () containing normal butane and at least 10 mass-% isobutane. The higher boiling fraction () is contacted with a selectively permeable membrane () to provide a permeate () containing normal butane-containing and a retentate () containing at least 80 mass-% isobutane. The preferred membranes are sieving membranes having a CPermeate Flow Index of at least 0. 01 and a CPermeate Flow Ratio of at least 1. 25:1.
Apparatus For Oligomerization In Multiple Stages With Single Fractionation Column
Bipin V. Vora - Naperville IL, US Charles P. Luebke - Mount Prospect IL, US Jill M. Meister - Elk Grove Village IL, US Michael A. Schultz - Kuala Lumpur, MY Dale J. Shields - Grayslake IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
B01J 8/00 B01D 3/00 C10C 21/00
US Classification:
422610, 422614, 422618, 422620, 422632, 196 46
Abstract:
In an oligomerization apparatus comprising at least two oligomerization reactors, at least portions of product streams from two reactors are separated in the same separator vessel; a liquid product stream from the first oligomerization reactor is fed to a fractionation column and a side cut from the fractionation column feeds the second oligomerization reactor.
Ballman Elementary School Ft. Smith AR 1984-1988, Hederick Elementary School Booneville AR 1988-1991
Community:
Jeffrey Benton, Lynn Wilkins, Dalton Gray, Kevin Thompson, Sarah Basham, Joseph Linker, Tanya Mullen, Denise Cooper, Anthony Dickason, Tracie Ashley, Jennifer Swaim