Search

Sandy C Hinds

from Bozeman, MT
Age ~67
Get Report
Also known as:
Sandy Clay Hinds, Sc Hinds, Hinds Sandy Clay
Phone and address:
2352 W Beall St APT 1, Bozeman, MT 59718
Related to:
Krista Custer, 40Murni HindsWilliam O Crawford, 55Deborah C Hinds, 67Trisha L Hinds, 63Gustav A Hinds, 66Jim S Hinds, 91Kay F Hinds, 86
Connected to:
Andrea Hinds, 42Annika E Hinds, 57Arianne T Hinds, 60Arlis Hinds, 47Becky Hinds, 62Cecil O Hinds, 61Chelsea Hinds, 32Claudette Hinds, 77Clayton D Hinds, 46Damion J Hinds, 38

Sandy Hinds Phones & Addresses

  • 2352 W Beall St APT 1, Bozeman, MT 59718
  • Albuquerque, NM
  • Spring, TX
  • Bunker Hill Village, TX
  • Silver City, NM
  • Baytown, TX
  • Crosby, TX
  • Galveston, TX
  • Pensacola, FL
  • Plano, TX

Resumes

Resumes

Sandy Hinds Photo 1

Senior Business Travel Consultant

View page
Work:

Senior Business Travel Consultant
Education:
Strayer University
Sandy Hinds Photo 2

Sandy Hinds

View page
Sandy Hinds Photo 3

Sandy Hinds

View page
Sandy Hinds Photo 4

Sandy Hinds

View page
Location:
United States

Publications

Us Patents

Low Molecular Weight Induced Condensing Agents

View page
US Patent:
7696289, Apr 13, 2010
Filed:
May 12, 2006
Appl. No.:
11/433682
Inventors:
D. Brett Fischbuch - Kingwood TX, US
Robert O. Hagerty - La Porte TX, US
Sandy C. Hinds - Crosby TX, US
Douglas R. Holroyd - Al-Jubail Industrial, SA
Ai Vey Ng - Singapore, SG
Diwaker Singh - Singapore, SG
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C08F 2/34
C08F 6/00
C08F 210/08
US Classification:
526 68, 526 70, 526901, 528482
Abstract:
The present invention relates to a continuous gas phase process comprising passing a recycle stream through a fluidized bed in a gas phase fluidized bed reactor, wherein the recycle stream comprises a low molecular weight dew point increasing component and a high molecular weight component, polymerizing an alpha-olefin monomer in the presence of a catalyst, and controlling an amount of the low molecular weight dew point increasing component in the recycle stream such that a dew point approach temperature of the recycle stream is less than the dew point approach temperature when operating with the higher molecular weight dew point increasing component alone.

Method For Transitioning From A Catalyst To An Incompatible Catalyst In A Gas-Phase Reactor

View page
US Patent:
20040127655, Jul 1, 2004
Filed:
Oct 10, 2003
Appl. No.:
10/683711
Inventors:
Thomas Veariel - Houston TX, US
George Yenetchi - Baytown TX, US
Sandy Hinds - Crosby TX, US
Diwaker Singh - Singapore, SG
Thierry Polchlopek - Bolbec, FR
International Classification:
C08F002/00
US Classification:
526/082000, 526/088000, 526/090000, 526/170000, 526/943000
Abstract:
The present invention is a process for transitioning from a first polymerization catalyst system to a second polymerization catalyst system incompatible with the first polymerization catalyst system in a gas-phase reactor. The novel process comprises conducting a first polymerization reaction using a first polymerization catalyst system; stopping the first polymerization reaction; removing the contents of the first polymerization reaction from the reactor while maintaining a substantially closed system; then, in the substantially closed system, introducing a substantially contaminant free seedbed into the reactor; introducing a second feed system and a second catalyst system into the reactor; and conducting a second polymerization reaction.

Gas-Phase Process

View page
US Patent:
20050182207, Aug 18, 2005
Filed:
Dec 22, 2004
Appl. No.:
11/021918
Inventors:
Diwaker Singh - Singapore, SG
Sandy Hinds - Crosby TX, US
Brett Fischbuch - Kingwood TX, US
Ng Ai Vey - Singapore, SG
International Classification:
C08F002/00
US Classification:
526068000, 526069000, 526070000, 526088000, 526901000
Abstract:
A continuous gas fluidized bed polymerization process for the production of a polymer from a monomer including continuously passing a gaseous stream comprising the monomer through a fluidized bed reactor in the presence of a catalyst under reactive conditions; withdrawing a polymeric product and a stream comprising unreacted monomer gases; cooling said stream comprising unreacted monomer gases to form a mixture comprising a gas phase and a liquid phase and reintroducing said mixture into said reactor with sufficient additional monomer to replace that monomer polymerized and withdrawn as the product, wherein said liquid phase is vaporized, and wherein the stream comprises at least two inert condensing agents selected from the group consisting of alkanes, cycloalkanes, and mixtures thereof, each of the inert condensing agents having a normal boiling point less than 40 C.
Control profile
Sandy C Hinds from Bozeman, MT, age ~67 Get Report