The Hershey Company 2013 - 2017
Director and Senior Mgr, Open Innovation
Sc Johnson 2004 - 2012
Technology Acquisition Manager, Home Cleaning
Sc Johnson 2000 - 2004
Research Associate, Furniture and Floor
Johnson Polymer 1996 - 1999
Commercial Development Manager
1996 - 1999
Massachusetts Institute of Technology
Education:
University of Chicago
Master of Business Administration, Masters, Marketing, Business
Massachusetts Institute of Technology
Doctorates, Doctor of Philosophy, Materials Science, Engineering
Skills:
Consumer Products Commercialization Product Innovation Open Innovation Product Development Negotiation Technology Licensing Codevelopment Licensing Strategy R&D Polymers Coatings Ip Competitive Analysis Technology Transfer Business Development Competitive Intelligence Cross Functional Team Leadership Fast Moving Consumer Goods Fmcg Innovation Management Leadership Management Marketing Mergers and Acquisitions Research and Development
Michael C. Fryan - Racine WI, US Douglas A. Soller - Racine WI, US Rakesh K. Popli - Franksville WI, US Frank J. Steer - Racine WI, US Evan A. Sparks - Madison WI, US
Portable wipe dispensers are provided. In one form the wipe dispenser can be used to spray a cleaning liquid onto a wipe being dispensed from the device. Alternatively the outlet may be directed against a surface external to the dispenser.
Continuous Production Of Reduced Gel Content Hydroxylated Addition Polymers
Kevin M. Andrist - Racine WI J. David Campbell - Racine WI Richard W. Chylla - Racine WI Rakesh K. Popli - Racine WI
Assignee:
S. C. Johnson & Son, Inc. - Racine WI
International Classification:
C08F 2026
US Classification:
526320
Abstract:
A process is disclosed for the continuous production, with reduced gel formation, of free radical addition polymers from ethylenically unsaturated monomers containing at least one free hydroxyl group such as 2-hydroxyethyl methacrylate, from about 0 to about 5% by weight of an alpha-beta unsaturated carboxylic acid such as acrylic acid or methacrylic acid, and the remainder of the monomers used are free radical addition copolymerizable compounds such as styrene, methyl methacrylate and butyl acrylate. The free radical addition polymerization is conducted at from about 150. degree. C. to about 310. degree. C. under superatmospheric pressure in the presence of one or more solvents. The solvent or the volume average of the solvent mixture has an overall calculated root mean square value of the hydrogen bonding and polar contributions of each solvent's solubility parameters in the range of from about 6 to about 15. The solvent or solvents in total have sufficient volatility under the conditions being used to conduct the polymerization such that any liquid condensate of vapor mixture forming on interior surfaces of the reactor equipment located above the surface of the monomer reactants contains at least 50 mole percent of the solvent to reduce gel formation on such interior surfaces. The process permits the continuous polymerization of the polymers over extended periods of time with reduced formation of gel particles and gel deposits.
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JAGDISH TYTLER (EX. CENTRAL MINISTER, MP, SENIOR CONGRESSMAN) ENJOYED ...