Nicholas A. Kotov - Ypsilanti MI, US Paul Podsiadlo - Easton PA, US Bong Sup Shim - Ann Arbor MI, US Ellen M. Arruda - Ann Arbor MI, US Anthony Waas - Ann Arbor MI, US
Assignee:
THE REGENTS OF THE UNIVERSITY OF MICHIGAN - Ann Arbor MI
A stiff layered polymer nanocomposite comprising a substrate adapted to receive a plurality of alternating layers of a first material and a second material; wherein the first material and second material are a polyelectrolyte, an organic polymer or an inorganic colloid and said first material and said second material have a chemical affinity for each other, said plurality of layers crosslinked using a chemical or physical crosslinking agent. Thin films that are consolidated and optionally crosslinked can be manufactured into hierarchical laminates with rigid and stress resistant properties.
Layer-By-Layer Assemblies Having Preferential Alignment Of Deposited Axially Anisotropic Species And Methods For Preparation And Use Thereof
Nicholas Kotov - Ypsilanti MI, US Bong Sup Shim - Ann Arbor MI, US Paul Podsiadlo - Westland MI, US
International Classification:
B32B 5/12 B05D 1/38
US Classification:
428105, 427470, 977742
Abstract:
Methods are provided for making layer-by-layer assemblies that comprise axial geometry nanoparticles. Such methods include forming a first layer on a substrate that comprises an axial nanoparticle, forming a second layer on the substrate that comprises an axial nanoparticle, where the first and second layers are aligned to respective first and second orientations. The disclosure also provides for multilayer materials having a first layer including a first polyelectrolyte and a first axial geometry nanoparticle which is substantially aligned along a first orientation. The multilayer material also includes a second layer including a second polyelectrolyte and a second axial geometry nanoparticle species having axial geometry, where the second nanoparticle species is substantially aligned along a second orientation which is distinct from the first orientation.
Processes For Isomerizing C8 Aromatic Hydrocarbons Using Serial Reactors
- Baytown TX, US Hari Nair - Spring TX, US Todd E. Detjen - Bellaire TX, US Paul Podsiadlo - Humble TX, US Travis D. Sparks - Deer Park TX, US
International Classification:
C07C 5/27
Abstract:
An changeable lead-lag configuration of two isomerization reactors can be used to achieve continuous isomerization operations in an aromatics production complex, even if the isomerization catalyst deactivates over time to require catalyst regeneration and/or replacement. The configuration can be particularly advantageous for two liquid phase isomerization reactors, especially those operated under a high WHSV≥5 hourwhere the isomerization catalyst can deactivate at a high rate.
Processes For Isomerizing C8 Aromatic Hydrocarbons
- Baytown TX, US Hari Nair - Spring TX, US Todd E. Detjen - Bellaire TX, US Paul Podsiadlo - Humble TX, US Travis D. Sparks - Deer Park TX, US
International Classification:
C07C 5/27 B01J 29/42
Abstract:
A liquid phase isomerization process comprising cofeeding molecular hydrogen at a feeding rate ≥100 ppm by weight can effectively convert a C8 aromatic hydrocarbon isomerization feed in the presence of an isomerization catalyst with a very low deactivation rate of the catalyst, even at high WHSV ≥5 hour.
Alkyl-Demethylation Processes And Catalyst Compositions Therefor
Catalyst compositions to perform selective alkyl-demethylation of C2+-hydrocarbyl-substituted aromatic hydrocarbon may exhibit a hydrogen chemisorption of at least 15% and comprise an oxide support material selected from the group consisting of an alkaline earth metal oxide, silica, a composite of an alkaline earth metal oxide and AlO, a composite of ZnO and AlO, a lanthanide oxide, a composite of a lanthanide oxide and AlO, and combinations and mixtures of two or more thereof; and a transition metal element dispersed upon the oxide support material. Alkyl-demethylation processes of a C6+ aromatic hydrocarbon-containing stream comprising C2+-hydrocarbyl-substituted aromatic hydrocarbons may comprise contacting the catalyst compositions in an alkyl-demethylation zone under alkyl-demethylation conditions to form an alkyl-demethylated aromatic hydrocarbon as an effluent exiting the alkyl-demethylation zone.
Transalkyation Processes In The Presence Of Sulfolane
- Bayrown TX, US Robert G. Tinger - Friendswood TX, US Paul Podsiadlo - Humble TX, US Todd E. Detjen - Houston TX, US Kathleen M. Keville - Beaumont TX, US
International Classification:
C07C 6/12
Abstract:
Co-feeding sulfolane into a transalkylation reactor along with the aromatic hydrocarbon feed(s) can improve benzene purity of the benzene product stream produced from the transalkylation product mixture, especially at the beginning phase of a catalyst cycle.
- Baytown TX, US Paul Podsiadlo - Humble TX, US Michel Molinier - Houston TX, US Scott J. Weigel - Allentown PA, US Travis D. Sparks - Deer Park TX, US Jocelyn A. Gilcrest - Mullica Hill NJ, US Joseph E. Gatt - Annandale NJ, US
Methods are provided for activation of catalysts comprising low amounts of a hydrogenation metal, such as low amounts of a Group 8-10 noble metal. The amount of hydrogenation metal on the catalyst can correspond to 0.5 wt % or less (with respect to the weight of the catalyst), or 0.1 wt % or less, or 0.05 wt % or less. Prior to loading a catalyst into a reactor, the corresponding catalyst precursor can be first activated in a hydrogen-containing atmosphere containing 1.0 vppm of CO or less. The thus first-activated catalyst can be transferred to a reactor with optional exposure to oxygen during the transfer, where it can be further activated using a hydrogen-containing atmosphere containing 3.0 vppm of CO or higher, to yield a twice-activated catalyst with high performance. The catalyst can be advantageously a transalkylation catalyst or an isomerization catalyst useful for converting aromatic hydrocarbons.
- Annandale NJ, US Paul Podsiadlo - Humble TX, US Chuansheng Bai - Phillipsburg NJ, US William W. Lonergan - Humble TX, US Louis F. Burns - Spring TX, US Stephen J. McCarthy - Center Valley PA, US Nicholas S. Rollman - Hamburg PA, US
A method for making catalyst materials is disclosed in which active metal ingredients of the final catalyst are added to a mixture for extruding the catalyst material that includes a binder, one or more precursors of one or more base metals and/or one or more noble metals, and a crystal of a zeolite. The extruded catalyst material is then pre-calcined and ion-exchanged and then a final calcining step is applied. The catalyst materials made by such a method are also disclosed as is a method for treating a hydrocarbon stream using the catalysts.
Exxonmobil Research & Engrg
Advanced Hydroprocessing Engineering Associate
Exxonmobil Apr 2019 - Aug 2019
Global Basestocks Optimization Advisor
Exxonmobil Chemical Feb 2019 - Apr 2019
Senior Staff Engineer
Exxonmobil Chemical May 2017 - Jan 2019
Staff Engineer
Exxonmobil Research & Engrg Feb 2014 - Apr 2017
Research Associate, Downstream Catalytic Technologies Development and Scale-Up
Education:
University of North Carolina at Chapel Hill 2018 - 2018
University of Michigan 2004 - 2008
Doctorates, Doctor of Philosophy, Chemical Engineering, Philosophy
University of Michigan 1999 - 2002
Bachelor of Science In Engineering, Bachelors, Chemical Engineering, Engineering
Lake Michigan Community College 1997 - 1999
Skills:
Characterization Spectroscopy Chemistry Nanomaterials Materials Science Chemical Engineering Research Nanotechnology Nanoparticles Laboratory Afm Energy Laboratory Skills
Languages:
English Polish Russian
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