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Phillip Paul Savage

from Port Huron, MI
Age ~58
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Also known as:
Phillip P Savage, Phillip M Savage, Phillip Savage Leagel, Phil P Savage, Philip P Savage, Phillip P Sovage, Phillip Savage S, Phillp Savage
Related to:
Nicholas J Savage, 31Elizabeth A Savage, 56Melissa D Savage, 54Andrea Savage, 52Sarah Wisniewski, 59
Connected to:
Adina D Savage, 43Alycia R Savage, 57Alyson J Savage, 58Betsey P Savage, 78Brittani R Savage, 28Buster Savage, 72Cara P Savage, 52Cindy Savage, 60Clarence W Savage, 50Dayle A Savage, 68

Phillip Savage Phones & Addresses

  • Port Huron, MI
  • 568 Saint Paul St, Marysville, MI 48040
  • 808 Virginia Ave, Marysville, MI 48040 (810) 388-1407 (810) 388-0091
  • 266 Sundown Dr, Dawsonville, GA 30534 (706) 265-6752
  • Waterford, MI
  • Murrayville, GA
  • Warren, MI
  • Kimball, MI
  • Stratford, NY
  • Johnstown, NY

Work

Company: Forsyth county family haven Jan 2013 Position: Driver/clerk

Education

School / High School: Ashford University in their BA of Social Science Mar 2014 Specialities: program

Resumes

Resumes

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Phillip Savage

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Phillip Savage

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Phillip Savage

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Location:
United States
Phillip Savage Photo 4

Phillip Savage Dawsonville, GA

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Work:
Forsyth County Family Haven

Jan 2013 to 2000
Driver/clerk
The Home Depot
Dahlonega, GA
May 2011 to Nov 2012
Receiving Associate
Chuck Latham Associates

Jan 2005 to Dec 2011
Team Lead/New
Little Caesars Pizza
Dawsonville, GA
Nov 2010 to May 2011
Store manager
Education:
Ashford University in their BA of Social Science
Mar 2014
program

Business Records

Name / Title
Company / Classification
Phones & Addresses
Phillip Savage
PHILLIP SAVAGE LLC

Publications

Us Patents

Method For Reducing Microcontaminants During Synthesis Of Pentachlorophenol

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US Patent:
7446235, Nov 4, 2008
Filed:
Mar 24, 2006
Appl. No.:
11/388816
Inventors:
Phillip E. Savage - Ann Arbor MI, US
Jianli Yu - Plymouth MI, US
Assignee:
The Regents of The University of Michigan - Ann Arbor MI
International Classification:
C07C 39/00
C07C 37/68
US Classification:
568776, 568755
Abstract:
A method for reducing contaminants during synthesis of pentachlorophenol includes providing a phenol-based starting material and a catalyst, which form a reaction mixture. A chlorine flow is introduced so that it is in contact with the reaction mixture, and the starting material and chlorine are reacted via a temperature-programmed reaction. The chlorine flow is terminated at a predetermined temperature prior to an end of the temperature-programmed reaction and/or at a point where the yield of pentachlorophenol is less than about 95%.

Method For Reducing Microcontaminants During Synthesis Of Pentachlorophenol

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US Patent:
7696389, Apr 13, 2010
Filed:
Oct 31, 2008
Appl. No.:
12/263275
Inventors:
Phillip E. Savage - Ann Arbor MI, US
Jianli Yu - Plymouth MI, US
Assignee:
The Regents of The University of Michigan - Ann Arbor MI
International Classification:
C07C 39/00
C07C 37/68
US Classification:
568776, 568755
Abstract:
A method for reducing contaminants during synthesis of pentachlorophenol includes providing a phenol-based starting material and a catalyst, which form a reaction mixture. A chlorine flow is introduced so that it is in contact with the reaction mixture, and the starting material and chlorine are reacted via a temperature-programmed reaction. The chlorine flow is terminated at a predetermined temperature prior to an end of the temperature-programmed reaction and/or at a point where the yield of pentachlorophenol is less than about 95%.

Method Of Producing An Upgraded Bio-Oil

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US Patent:
20120055077, Mar 8, 2012
Filed:
Sep 2, 2011
Appl. No.:
13/224451
Inventors:
Phillip E. Savage - Ann Arbor MI, US
Peigao Duan - Jiaozuo, CN
International Classification:
C10L 1/00
C10L 1/188
US Classification:
44307, 44385
Abstract:
A method of producing an upgraded bio-oil from a wet biomass that includes heating the wet biomass at a first temperature and a first pressure for a time period ranging from 10 to 200 minutes to form a crude bio-oil. The first temperature ranges from 200 to 400 C. and the first pressure ranges from 0.1 to 25 MPa, with the proviso that at least a portion of the water present in the wet biomass remains in a liquid phase throughout the step of heating to form the crude bio-oil, and the first temperature and pressure are below super-critical conditions for water. The method also includes heating the crude bio-oil and the water at a second temperature and a second pressure to form the upgraded bio-oil. Some water remains in the liquid phase or in a super-critical fluid phase throughout the step of heating to form the upgraded bio-oil.
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Phillip Paul Savage from Port Huron, MI, age ~58 Get Report