Mark Schott resumes & CV records
Resumes
Mark Schott
Mark Schott
Mark Schott
Mark Schott
Mark Schott
Location:
United States
Mark D Schott, 491754 Winston St, Alliance, OH 44601
Mark Schott Phones & Addresses
1754 Winston St, Alliance, OH 44601 330-8233419
Elgin, IL
Work
Position:
Homemaker
Education
Degree:
High school graduate or higher
Emails
Mentions for Mark D Schott
Publications & IP owners
Us Patents
Metal Organic FrameworkâPolymer Mixed Matrix Membranes
US Patent:
7637983, Dec 29, 2009
Filed:
Jun 30, 2006
Appl. No.:
11/427834
Inventors:
Chunqing Liu - Schaumburg IL, US
Beth McCulloch - Clarendon Hills IL, US
Stephen T. Wilson - Libertyville IL, US
Annabelle I. Benin - Oak Forest IL, US
Mark E. Schott - Palatine IL, US
Beth McCulloch - Clarendon Hills IL, US
Stephen T. Wilson - Libertyville IL, US
Annabelle I. Benin - Oak Forest IL, US
Mark E. Schott - Palatine IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
B01D 53/22
US Classification:
95 45, 95 50, 95 51, 95 54, 95 55, 96 4, 96 12, 96 13, 96 14, 210640, 21050021, 21050027
Abstract:
Metal-organic framework (MOF)-polymer mixed matrix membranes (MOF-MMMs) have been prepared by dispersing high surface area MOFs (e. g. IRMOF-1) into a polymer matrix (e. g. Matrimid 5218). The MOFs allow the polymer to infiltrate the pores of the MOFs, which improves the interfacial and mechanical properties of the polymer and in turn affects permeability. Pure gas permeation tests show the incorporation of 20 wt-% of IRMOF-1 in Matrimid 5218 polyimide matrix results in 280% improvement in COpermeability without a loss of CO/CHselectivity compared to those of the pure Matrimid 5218 membrane. This type of MOF-MMMs has significantly improved gas separation performance with dramatically high COpermeability (>35 barrer) and higher than 29 CO/CHselectivity at 50 C. under 100 psig pressure, which are attractive candidates for practical gas separation applications such as COremoval from natural gas.
Adsorber For Pretreatment Of Natural Gas Containing Bulk Hydrogen Sulfide
US Patent:
7803215, Sep 28, 2010
Filed:
Dec 12, 2007
Appl. No.:
11/954437
Inventors:
Bradley P. Russell - Wheaton IL, US
Mark E. Schott - Palatine IL, US
Gordon T. Cartwright - Tyler TX, US
Mark E. Schott - Palatine IL, US
Gordon T. Cartwright - Tyler TX, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
B01D 53/04
US Classification:
95136, 95143, 423230, 208208 R, 208310 R, 585822
Abstract:
The invention relates to a process for removing heavy hydrocarbons and hydrogen sulfide from natural gas. The combination of a silica-gel and an activated carbon adsorber allow for a significant reduction in the overall bed volume required for removal of hydrocarbons.
Ionic Liquid-Solid-Polymer Mixed Matrix Membranes For Gas Separations
US Patent:
7943543, May 17, 2011
Filed:
Sep 29, 2006
Appl. No.:
11/537294
Inventors:
Chunqing Liu - Schaumburg IL, US
Santi Kulprathipanja - Inverness IL, US
Mark E. Schott - Palatine IL, US
Stephen T. Wilson - Libertyville IL, US
Santi Kulprathipanja - Inverness IL, US
Mark E. Schott - Palatine IL, US
Stephen T. Wilson - Libertyville IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
B01J 20/28
B01D 53/22
B01D 53/22
US Classification:
502 4, 96 4, 95 45, 95 51
Abstract:
New ionic liquid-solid-polymer mixed matrix membranes were proposed for gas separations such as COremoval from natural gas or N. For the new mixed matrix membranes, the solids such as carbon molecular sieves, microporous molecular sieves, MCM-41 type of mesoporous molecular sieves, or polymer of intrinsic microporosity (PIM) are coated (or impregnated) with ionic liquids such as 1-butyl-3-methyl imidazolium bis[trifluoromethylsulfonyl]amide. The ionic liquids coated or impregnated solids are then dispersed in the continuous polymer matrix to form mixed matrix membranes. These hybrid mixed matrix membranes will combine the properties of the continuous polymer phase, the ionic liquids, and the dispersed ionic liquids coated or impregnated solids phase, which will possibly open up new opportunities for gas separation processes such as COseparation from natural gas or flue gas.
Natural Gas Purification System
US Patent:
8282707, Oct 9, 2012
Filed:
May 19, 2011
Appl. No.:
13/111458
Inventors:
Leonid Bresler - Northbrook IL, US
John M. Foresman - Homer Glen IL, US
William I. Echt - Highwood IL, US
Mark E. Schott - Palatine IL, US
John M. Foresman - Homer Glen IL, US
William I. Echt - Highwood IL, US
Mark E. Schott - Palatine IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
B01D 53/22
US Classification:
95 51, 95 45, 95 49, 95 90, 95114
Abstract:
The present invention relates to an integrated membrane/absorbent/adsorbent process and system for removal of mercury and sulfur compounds from natural gas on a ship that houses natural gas purification equipment. First mercury and most of the sulfur compounds are removed by an adsorbent bed and then the natural gas stream passes through a membrane unit to produce a partially purified natural gas residue stream to be dried and then liquefied and a carbon dioxide permeate stream that can be used as a fuel gas.
Integrated Membrane And Adsorption System For Carbon Dioxide Removal From Natural Gas
US Patent:
8388732, Mar 5, 2013
Filed:
May 11, 2011
Appl. No.:
13/105462
Inventors:
Shain-Jer Doong - Kildeer IL, US
Lubo Zhou - Inverness IL, US
Dennis J. Bellville - Deer Park IL, US
Mark E. Schott - Palatine IL, US
Leonid Bresler - Northbrook IL, US
John M. Foresman - Homer Glen IL, US
Lubo Zhou - Inverness IL, US
Dennis J. Bellville - Deer Park IL, US
Mark E. Schott - Palatine IL, US
Leonid Bresler - Northbrook IL, US
John M. Foresman - Homer Glen IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
B01D 53/22
US Classification:
95 45, 95 49, 95 51, 95 90, 95114
Abstract:
The present invention relates to an integrated membrane/adsorbent process and system for removal of carbon dioxide from natural gas on a ship that houses natural gas purification equipment. Additional membrane units or adsorbent beds are used to reduce the amount of product gas that is lost in gas streams that are used to regenerate the adsorbent beds. These systems produce a product stream that meets the specifications of less than 50 parts per million carbon dioxide in natural gas for liquefaction.
Permeate Adapter For Multi-Tube Pressure Vessel
US Patent:
8540876, Sep 24, 2013
Filed:
Oct 1, 2007
Appl. No.:
11/906262
Inventors:
Steven M. Poklop - Palatine IL, US
Christopher Naunheimer - Arlington Heights IL, US
Mark E. Schott - Palatine IL, US
Christopher Naunheimer - Arlington Heights IL, US
Mark E. Schott - Palatine IL, US
Assignee:
UOP LLC - Des Plaines IL
International Classification:
B01D 63/06
B01D 69/04
B01D 25/00
B01D 69/04
B01D 25/00
US Classification:
2103218, 21032189, 2103232, 210439
Abstract:
A permeate adapter is provided. The permeate adapter may be used within a pressure vessel. The permeate adapter includes a front portion and an oppositely disposed back portion. The front portion includes a permeate opening for receiving an end of a permeate passage tube of a membrane cartridge and for being in fluid communication with a permeate reservoir. The front portion and the back portion each include one or more fluid openings. Fluid passageways are connected between the one or more front portion fluid openings and the back portion fluid openings. The fluid passageways receive an end of a membrane cartridge at the front portion. At the back portion, the fluid passageways are in fluid communication with a fluid reservoir adjacent the back portion of the permeate adapter.
Membrane Separation Assemblies
US Patent:
2006012, Jun 15, 2006
Filed:
Dec 10, 2004
Appl. No.:
11/009682
Inventors:
Mark Schott - Palatine IL, US
A. Schwartz - Upland CA, US
A. Schwartz - Upland CA, US
International Classification:
B01D 63/00
US Classification:
210321600, 210321720, 096004000, 096009000
Abstract:
Assemblies for use in separation of a fluid feed. Assemblies typically include an elongated housing having a fluid feed stream inlet, a residual stream outlet and a permeate stream outlet. The housing contains at least one membrane separation element to form a membrane separation element linear string that at least in part defines a linear permeate passage tube. A permeate adapter is joined with an end of the linear permeate passage tube. The permeate adapter includes a receiving opening for receiving an end of the linear permeate passage tube. The adapter defines a permeate passageway extending therethrough and includes a plurality of permeate discharge openings disposed such as to place the receiving opening and the permeate discharge openings in fluid flow communication.
Process To Maximize Methane Content In Natural Gas Stream
US Patent:
2009015, Jun 25, 2009
Filed:
Feb 25, 2009
Appl. No.:
12/392554
Inventors:
Kurt M. Vanden Bussche - Lake in the Hills IL, US
Paul T. Barger - Arlington Heights IL, US
David W. Penner - Lake Zurich IL, US
Mark E. Schott - Palatine IL, US
Frank S. Modica - Naperville IL, US
Paul T. Barger - Arlington Heights IL, US
David W. Penner - Lake Zurich IL, US
Mark E. Schott - Palatine IL, US
Frank S. Modica - Naperville IL, US
International Classification:
C10L 3/00
US Classification:
481277
Abstract:
The present invention relates to a hydrogenolysis process and catalyst for conversion of ethane to methane in a natural gas stream when such streams contain large quantities of ethane. Such natural gas streams include the product of the in situ treatment of oil shale to produce oil and gas. Hydrogenolysis catalysts have been identified that produce high yields of ethane at low light-off temperatures.
NOTICE: You may not use BackgroundCheck or the information it provides to make decisions about employment, credit, housing or any other purpose that would require Fair Credit Reporting Act (FCRA) compliance. BackgroundCheck is not a Consumer Reporting Agency (CRA) as defined by the FCRA and does not provide consumer reports.