Peter J Moore
Architects in Philadelphia, PA
License number
New Jersey 21AI00684200
Issued Date
Jan 7, 1976
Expiration Date
Jul 31, 1997
Category
Architecture
Type
Registered Architect
Address
Address
Philadelphia, PA
Professional information
National Sales Director, Graphics At Xpedx
Position:
National Sales Director, Graphics at xpedx
Location:
Greater Philadelphia Area
Industry:
Printing
Work:
xpedx
since Oct 2010
-
National Sales Director, Graphics
xpedx
Mar 2010 - Oct 2010
-
Graphics Business Unit Manager
Pitman Company
Oct 2008 - Apr 2010
-
President
Pitman Company
Jan 2004 - Jan 2008
-
Executive VP of Sales
Pitman Company
2002 - 2004
-
Senior VP of Sales and Operations
Education:
Villanova University 1977 - 1980
BA, Bachelor of Arts Malvern Prep
BA, Bachelor of Arts Malvern Prep
Interests:
Private Pilot, Certified Scuba Diver, Golfer
Pastor Of English And Youth Ministries At China Grace Christian Church
Position:
Pastor of English and Youth Ministries at China Grace Christian Church
Location:
Greater Philadelphia Area
Industry:
Religious Institutions
Work:
China Grace Christian Church
-
Pastor of English and Youth Ministries
Education:
Westminster Theological Seminary
M.Div.
M.Div.
Grant Manager At O'connell &Amp; Associates
Position:
Grant Manager at O'Connell & Associates
Location:
Greater Philadelphia Area
Industry:
Government Relations
Work:
O'Connell & Associates
-
Grant Manager
Process For Preparing Continuously Variable-Composition Copolymers
US Patent:
2009004, Feb 19, 2009
Filed:
Jul 14, 2008
Appl. No.:
12/172382
Inventors:
Nadine Iroff - Perkiomenville PA, US
Peter Moore - Philadelphia PA, US
Peter Moore - Philadelphia PA, US
Assignee:
EVONIK ROHMAX ADDITIVES GMBH - Darmstadt
International Classification:
C08F 2/01, C08F 2/06
US Classification:
526 60, 526 65, 526 66, 526 61
Abstract:
A continuously variable composition copolymer is prepared in a reaction system, by (a) providing a reaction vessel comprising a first monomer composition; (b) providing a feed vessel comprising a second monomer composition; (c) initiating a polymerization reaction in the reaction vessel; (d) continuing the polymerization reaction during the gradual addition of the second monomer composition from the feed vessel to the reaction vessel, wherein the gradual addition of the second monomer composition is performed such that the continuously variable composition copolymer is obtained; (e) maintaining the polymerization until at least 90% of the total monomer composition has been converted to the copolymer; wherein the copolymer has a weight average molecular weight from 10,000 to 1,000,000; wherein the copolymer is soluble in lubricating oil, wherein the monomers of the first monomer composition provided in the reaction vessel comprise at least 50% by weight of all the monomers used to prepare the copolymer.