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Kirk A Leissner

age ~67

from Galveston, TX

Also known as:
  • Alan Leissner Kirk
  • Nick Leis
Phone and address:
9352 Jamaica Bch, Galveston, TX 77554
409 996-1177

Kirk Leissner Phones & Addresses

  • 9352 Jamaica Bch, Galveston, TX 77554 • 409 996-1177
  • Jamaica Beach, TX
  • Angleton, TX
  • Dayton, OH
  • 9352 Jamaica Bch, Galveston, TX 77554

Us Patents

  • Turbulent Flow Process, Monoalkyl Aromatic Production Process And Reactor For Such Process

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  • US Patent:
    52275566, Jul 13, 1993
  • Filed:
    Apr 17, 1990
  • Appl. No.:
    7/511489
  • Inventors:
    James H. Benton - Surgar Land TX
    John B. Ivy - Lake Jackson TX
    Jack Broodo - Missouri City TX
    Kirk A. Leissner - Angleton TX
    Ellroy G. Fox - Clute TX
  • Assignee:
    The Dow Chemical Company - Midland MI
  • International Classification:
    C07C 270
    B01J 804
  • US Classification:
    585323
  • Abstract:
    A process for turbulently flowing together reactants in uniform proportions in a reactor vessel. A process for producing ethylbenzene by reacting ethylene and benzene in the presence of a catalyst in a reactor vessel from which useful heat generated by the reaction is transferred to a heat transfer medium flowing through the reactor and in which the reaction occurs in a relatively short time period. In one embodiment, polyethylbenzenes produced in the reactor vessel are not recycled into the vessel. A reactor for a reaction of reactant materials that are uniformly and turbulently mixed together.
  • Turbulent Flow Reactor

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  • US Patent:
    53343573, Aug 2, 1994
  • Filed:
    Dec 17, 1992
  • Appl. No.:
    7/992204
  • Inventors:
    James H. Benton - Sugar Land TX
    Jack Broodo - Missouri City TX
    John B. Ivy - Lake Jackson TX
    Kirk A. Leissner - Angleton TX
    Ellroy G. Fox - Clute TX
  • Assignee:
    The Dow Chemical Company - Midland MI
  • International Classification:
    B01J 1000
  • US Classification:
    422197
  • Abstract:
    A process for turbulently flowing together reactants in uniform proportions in a reactor vessel. A process for producing ethylbenzene by reacting ethylene and benzene in the presence of a catalyst in a reactor vessel from which useful heat generated by the reaction is transferred to a heat transfer medium flowing through the reactor and in which the reaction occurs in a relatively short time period. In one embodiment, polyethylbenzenes produced in the reactor vessel are not recycled into the vessel. A reactor for a reaction of reactant materials that are uniformly and turbulently mixed together.

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