Mitchell E Odinak

age ~65

from Pittsford, NY

Also known as:
  • Mitchell Patricia Odinak
  • Mitchell P Odinak
  • Mitchell Odimak
Phone and address:
1 Durham Way, Pittsford, NY 14534

Mitchell Odinak Phones & Addresses

  • 1 Durham Way, Pittsford, NY 14534
  • 1650 Vail Valley Dr, Vail, CO 81657 • 9704761632
  • Corning, NY
  • 208 Lincoln Rd, Horseheads, NY 14845 • 6077391872
  • Somerville, MA
  • Watertown, MA
  • 1 Durham Way, Pittsford, NY 14534 • 6077316522

Work

  • Position:
    Service Occupations

Education

  • Degree:
    Graduate or professional degree

Us Patents

  • Flow Distributor For Monolith Reactors

    view source
  • US Patent:
    7032894, Apr 25, 2006
  • Filed:
    Nov 5, 2001
  • Appl. No.:
    10/013008
  • Inventors:
    George Y. Adusei - Branchburg NJ, US
    Stephen A. Campbell - Corning NY, US
    Wei Liu - Painted Post NY, US
    Mitchell E. Odinak - Horseheads NY, US
    Shantanu Roy - Painted Post NY, US
  • Assignee:
    Corning Incorporated - Corning NY
  • International Classification:
    B01F 3/04
  • US Classification:
    261 97, 261103, 422190, 422220, 422222
  • Abstract:
    A device for distributing fluid into a monolith bed includes a plurality of flow channels stacked in order of decreasing diameter. The flow channels successively split a flow stream into a multiple flow streams prior to the flow stream entering the monolith bed.
  • Monolithic Catalyst Dehydrogenation Reactor

    view source
  • US Patent:
    6623707, Sep 23, 2003
  • Filed:
    Jun 19, 2000
  • Appl. No.:
    09/597888
  • Inventors:
    William P. Addiego - Big Flats NY
    Stephen A. Campbell - Corning NY
    Wei Liu - Painted Post NY
    Mitchell E. Odinak - Horseheads NY
  • Assignee:
    Corning Incorporated - Corning NY
  • International Classification:
    C07C 532
  • US Classification:
    422190, 422188, 422191, 422192, 422198, 422199, 422211, 422218, 422222, 585440
  • Abstract:
    Axial flow dehydrogenation reactors comprising multiple catalyst beds formed of honeycomb monoliths, the beds being separated from each other by heating stages to maintain reactant stream temperature, provide low pressure drop and improved conversion efficiency when used alone or in combination with other reactors, e. g. , as reactor upgrades for series reactor systems incorporating radial flow reactor stages.

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