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Mark A Liepa

age ~65

from Charlottesville, VA

Mark Liepa Phones & Addresses

  • Charlottesville, VA
  • 112 Seiberling Dr, Northfield, OH 44067 • (610)8120388
  • Sagamore Hills, OH
  • 303 Colonial Dr, Exton, PA 19341 • (610)3637675
  • Humble, TX
  • West Chester, PA
  • Philadelphia, PA
  • Cambridge, MA
  • Sagamore Hls, OH
  • 112 Seiberling Dr, Northfield, OH 44067 • (610)3637675

Work

  • Company:
    Bridgestone
    2012
  • Address:
    Akron, Ohio
  • Position:
    Synthesis processes engineer

Education

  • Degree:
    ScD
  • School / High School:
    Massachusetts Institute of Technology
    1982 to 1988
  • Specialities:
    Chemical Engineering

Skills

What If and Hazop Process Hazard Analysis • Root Cause Incident Analysis • Aspen Plus Engineering Software • Data Regression and Statistical Analysis • Process Analysis • Chemical Engineering • Process Optimization • Catalysis • Chemistry • R&D • Process Safety • Engineering • Pilot Plant • Process Improvement

Languages

English • Latvian

Industries

Research

Resumes

Mark Liepa Photo 1

Mark Albert Liepa

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Location:
303 Colonial Dr, Exton, PA 19341
Industry:
Research
Work:
Bridgestone - Akron, Ohio since 2012
Synthesis Processes Engineer

AIChE Delaware Valley Section 2009 - 2012
Secretary

LyondellBasell 1988 - 2011
Senior Principal Researcher

Design Institute for Physical Properties 2002 - 2008
Chair, Project 851 Critical Properties of Pure Compounds

Exxon Research & Engineering Company - Baytown, Texas Feb 1982 - Jul 1982
Research Engineer
Education:
Massachusetts Institute of Technology 1982 - 1988
ScD, Chemical Engineering
Massachusetts Institute of Technology 1982 - 1983
SM, Chemical Engineering Practice
University of Michigan 1977 - 1981
BSE, Chemical Engineering
University of Michigan 1977 - 1981
BSE, Engineering Science
Skills:
What If and Hazop Process Hazard Analysis
Root Cause Incident Analysis
Aspen Plus Engineering Software
Data Regression and Statistical Analysis
Process Analysis
Chemical Engineering
Process Optimization
Catalysis
Chemistry
R&D
Process Safety
Engineering
Pilot Plant
Process Improvement
Languages:
English
Latvian

Us Patents

  • Adsorbent Bed Loading And Regeneration

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  • US Patent:
    6563010, May 13, 2003
  • Filed:
    Jun 3, 2002
  • Appl. No.:
    10/161004
  • Inventors:
    Mark A. Liepa - Exton PA
  • Assignee:
    ARCO Chemical Technology, L.P. - Greenville DE
  • International Classification:
    C07C 2734
  • US Classification:
    568917, 210673, 210670, 210676
  • Abstract:
    The process for removing impurities from a liquid by contact with a solid adsorbent using parallel contact adsorbent beds such that when one bed is contacting the liquid the parallel bed is being regenerated by contact with heated inert gas, wherein during changeover of the beds inert gas is transferred from the regenerated bed to the spent bed during the period that liquid is being drained from the spent bed.
  • Epoxidation Process

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  • US Patent:
    6710194, Mar 23, 2004
  • Filed:
    Jan 23, 2003
  • Appl. No.:
    10/349655
  • Inventors:
    Robert N. Cochran - West Chester PA
    Prakash G. Balan - Wilmington DE
    Mark A. Liepa - Exton PA
    Bernard Cooker - Malvern PA
  • Assignee:
    ARCO Chemical Technology, L.P. - Greenville DE
  • International Classification:
    C07D30106
  • US Classification:
    549533, 549532
  • Abstract:
    Propylene oxide is produced by liquid phase reaction of propylene oxygen and hydrogen in contact with a solid epoxidation catalyst at elevated temperature and pressure, the reaction conditions being regulated to provide a weight ratio of dissolved oxygen to dissolved hydrogen in the liquid reaction mixture of at least 16.
  • Drycleaning Method

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  • US Patent:
    7575604, Aug 18, 2009
  • Filed:
    Oct 6, 2006
  • Appl. No.:
    11/544326
  • Inventors:
    Paul E. Galick - West Chester PA, US
    Mark A. Liepa - Exton PA, US
  • Assignee:
    Lyondell Chemical Technology, L.P. - Wilmington DE
  • International Classification:
    D06L 1/00
    D06L 1/02
    D06L 1/20
  • US Classification:
    8142, 8137, 8141, 134 34, 134 11, 134 12
  • Abstract:
    A drycleaning method is disclosed. The method uses a composition comprising 30 to 90 wt. % of a dipropylene glycol C-Calkyl ether, 5 to 65 wt. % of one or more C-Chydrocarbons, and 1 to 10 wt. % of water. The method combines acceptable stain removal with faster-than-expected evaporability, particularly at the elevated temperatures used in commercial drycleaning.
  • In Situ Filtration Draught Tube Reactor System

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  • US Patent:
    20040124140, Jul 1, 2004
  • Filed:
    Dec 30, 2002
  • Appl. No.:
    10/331703
  • Inventors:
    Gary Sawyer - Media PA, US
    Mark Liepa - Exton PA, US
    Prakash Balan - Wilmington DE, US
  • International Classification:
    B01D011/00
  • US Classification:
    210/634000, 210/323200, 210/484000, 210/497010
  • Abstract:
    Reduced attrition of catalyst and extended operation of heterogenous catalyzed slurry reactions in draught tube reactors is facilitated by locating vertically oriented filter media within the draught tube reactor annular space to provide a product outlet stream substantially free of catalyst.
  • Production Of Propylene Glycol Monoalkyl Ether

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  • US Patent:
    20090187049, Jul 23, 2009
  • Filed:
    Jan 17, 2008
  • Appl. No.:
    12/009212
  • Inventors:
    Xiangmin Li - Glen Mills PA, US
    Lawrence M. Candela - Havertown PA, US
    Mark A. Liepa - Exton PA, US
  • International Classification:
    C07C 43/10
  • US Classification:
    568678
  • Abstract:
    The invention is a process for producing a propylene glycol monoalkyl ether which comprises first reacting propylene oxide and an alcohol in the presence of an alkali or alkaline earth metal alkoxide catalyst to produce an alkoxylation mixture comprising propylene glycol monoalkyl ether; distilling the alkoxylation mixture to produce a first overhead stream comprising propylene oxide and alcohol and a first bottoms stream comprising propylene glycol monoalkyl ether; and then distilling the first bottoms stream to produce purified propylene glycol monoalkyl ether as a second overhead stream. The reaction and/or one or more of the distillation steps occur in the presence of an alkali metal borohydride. The process produces propylene glycol monoalkyl ether with low UV absorbance and reduced carbonyl impurities.
  • Epoxidation Of Olefins

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  • US Patent:
    55655815, Oct 15, 1996
  • Filed:
    Oct 18, 1990
  • Appl. No.:
    7/599763
  • Inventors:
    Mark A. Liepa - West Chester PA
  • Assignee:
    ARCO Chemical Technology, L.P. - Greenville DE
  • International Classification:
    C07D31300
  • US Classification:
    549346
  • Abstract:
    The present invention relates to the epoxidation of olefins using cyclohexyl hydroperoxide as reactant, the improvement being using a secondary or tertiary alcohol such as cyclohexanol or tertiary butyl alcohol as a stabilizing agent during the epoxidation, the alcohol stabilizer being fed to the epoxidation reaction zone in an amount greater than 3 moles per mole of hydroperoxide fed to the epoxidation reaction zone.
  • Propylene Oxide Production

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  • US Patent:
    59731710, Oct 26, 1999
  • Filed:
    Oct 7, 1998
  • Appl. No.:
    9/167329
  • Inventors:
    Robert N. Cochran - West Chester PA
    John C. Jubin - West Chester PA
    Mark A. Liepa - Exton PA
    Robert Nedwick - Broomall PA
    Rangasamy Pitchai - West Chester PA
    W. Wayne Wentzheimer - Grand Rapids MI
  • Assignee:
    ARCO Chemical Technology, LP - Greenville DE
  • International Classification:
    C07D30106
  • US Classification:
    549533
  • Abstract:
    An integrated process is provided for the production of propylene oxide from propane wherein propane is dehydrogenated to propylene and hydrogen and the resulting propylene, propane, and hydrogen mixture together with added oxygen is reacted over a palladium on titanium silicilite catalyst to form propylene oxide, the molar ratio of oxygen to hydrogen in the reaction feed being at least about 2/1.

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