Acute Upper Respiratory Tract Infections Fractures, Dislocations, Derangement, and Sprains Migraine Headache Otitis Media Skin and Subcutaneous Infections
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English
Description:
Dr. Driver graduated from the Oregon Health & Science University School of Medicine in 1980. He works in Clarkston, WA and specializes in Emergency Medicine. Dr. Driver is affiliated with Tri-State Memorial Hospital.
Name / Title
Company / Classification
Phones & Addresses
Michael Driver Treasurer
NANEUM LIMITED
Isbn (Books And Publications)
The Dynamic Decision Maker: Five Decision Styles for Executive and Business Success
A process for preparing fatty amines by the cross-metathesis of normal alpha olefins and acrylonitrile to form an intermediate fatty acid nitrile which is hydrogenated to the corresponding fatty amine.
Process For Increasing The Yield Of Lubricating Base Oil From A Fischer-Tropsch Plant
David R. Johnson - Petaluma CA Christopher A. Simmons - El Cerrito CA Donald H. Mohr - Orinda CA Stephen J. Miller - San Francisco CA Stephen K. Lee - Oakland CA William L. Schinski - San Rafael CA Michael S. Driver - San Francisco CA
Assignee:
Chevron U.S.A. Inc. - San Ramon CA
International Classification:
C10G 6717
US Classification:
208 80, 208 78, 208950, 585304, 585327
Abstract:
A process for increasing the yield of C plus hydrocarbon products from a Fischer-Tropsch plant which comprises the steps of (a) separating a Fischer-Tropsch product into a wax fraction and a condensate fraction; (b) dewaxing the wax fraction to produce a high boiling intermediate; (c) hydrofinishing the high boiling intermediate; (d) dehydrating the alcohols in the condensate fraction to convert them into olefins; (e) oligomerizing the olefins to form higher molecular weight hydrocarbons; (f) hydrofinishing the oligomerization mixture; and (g) and recovering a C plus hydrocarbon product from the hydrofinishing zone.
Process For Upgrading Fischer-Tropsch Syncrude Using Thermal Cracking And Oligomerization
David R. Johnson - Petaluma CA Christopher A. Simmons - El Cerrito CA Donald H. Mohr - Orinda CA Stephen J. Miller - San Francisco CA Stephen K. Lee - Oakland CA William L. Schinski - San Rafael CA Michael S. Driver - San Francisco CA William J. Cannella - Hercules CA
Assignee:
Chevron U.S.A. Inc. - San Ramon CA
International Classification:
C07C 204
US Classification:
585303, 585302, 585304, 585329, 585330, 208950
Abstract:
A process for upgrading a Fischer-Tropsch feedstock which comprises (a) recovering from a Fischer-Tropsch reactor a Fischer-Tropsch wax fraction and a Fischer-Tropsch condensate fraction, wherein the Fischer-Tropsch condensate fraction contains alcohols boiling below about 370Â C. ; (b) contacting the Fischer-Tropsch condensate fraction with a dehydration catalyst in a dehydration zone under dehydration conditions pre-selected to convert at least some of the alcohols present in said fraction into olefins and recovering a first intermediate effluent from said dehydration zone; (c) pyrolyzing the paraffins in the Fischer-Tropsch wax fraction in a thermal cracking zone under thermal cracking conditions pre-selected to crack the Fischer-Tropsch wax molecules to form olefins and collecting a second intermediate effluent from the thermal cracking zone; (d) passing the first and second intermediate effluents recovered from steps (b) and (c) to an oligomerization zone containing an oligomerization catalyst under oligomerization conditions to form an oligomerization mixture having a higher molecular weight than either of said first and second intermediate effluent; (e) hydrofinishing the oligomerization mixture in a hydrofinishing zone; and (f) recovering from the hydrofinishing zone a C plus hydrocarbon product, most preferably a lubricating base oil.
Process For Upgrading Fischer-Tropsch Syncrude Using Thermal Cracking And Oligomerization
David Johnson - Petaluma CA, US Christopher Simmons - El Cerrito CA, US Donald Mohr - Orinda CA, US Stephen Miller - San Francisco CA, US Stephen Lee - Oakland CA, US William Schinski - San Rafael CA, US Michael Driver - San Francisco CA, US William Cannella - Hercules CA, US
Assignee:
Chevron U.S.A. Inc.
International Classification:
C07C001/00
US Classification:
585/324000, 585/327000
Abstract:
A process for upgrading a Fischer-Tropsch feedstock which comprises (a) recovering from a Fischer-Tropsch reactor a Fischer-Tropsch wax fraction and a Fischer-Tropsch condensate fraction, wherein the Fischer-Tropsch condensate fraction contains alcohols boiling below about 370 C.; (b) contacting the Fischer-Tropsch condensate fraction with a dehydration catalyst in a dehydration zone under dehydration conditions pre-selected to convert at least some of the alcohols present in said fraction into olefins and recovering a first intermediate effluent from said dehydration zone; (c) pyrolyzing the paraffins in the Fischer-Tropsch wax fraction in a thermal cracking zone under thermal cracking conditions pre-selected to crack the Fischer-Tropsch wax molecules to form olefins and collecting a second intermediate effluent from the thermal cracking zone; (d) passing the first and second intermediate effluents recovered from steps (b) and (c) to an oligomerization zone containing an oligomerization catalyst under oligomerization conditions to form an oligomerization mixture having a higher molecular weight than either of said first and second intermediate effluent; (e) hydrofinishing the oligomerization mixture in a hydrofinishing zone; and (f) recovering from the hydrofinishing zone a Cplus hydrocarbon product, most preferably a lubricating base oil.
Hydrotreating Of Fischer-Tropsch Derived Feeds Prior To Oligomerization Using An Ionic Liquid Catalyst
David Johnson - Petaluma CA, US Thomas Harris - Benicia CA, US Michael Driver - San Francisco CA, US
Assignee:
Chevron U.S.A. Inc.
International Classification:
C07C002/00
US Classification:
585/329000
Abstract:
A process for oligomerizing a Fischer-Tropsch derived feed containing oxygenates which comprises (a) reducing significantly the oxygenates present in the Fischer-Tropsch derived feed by contacting said feed with a hydrotreating catalyst under hydrotreating conditions in a hydrotreating zone and recovering from the hydrotreating zone a Fischer-Tropsch derived hydrotreated feed which contains a significantly reduced amount of oxygenates as compared to the Fischer-Tropsch derived feed and also a significant amount of paraffins; (b) pyrolyzing the Fischer-Tropsch derived hydrotreated feed in a thermal cracking zone under thermal cracking conditions pre-selected to crack the paraffin molecules to form olefins and collecting an olefin-enriched Fischer-Tropsch feed from the thermal cracking zone; (c) contacting the olefin-enriched Fischer-Tropsch feed with a Lewis acid ionic liquid catalyst in an oligomerization zone under oligomerization reaction conditions; and (d) recovering from the oligomerization zone a Fischer-Tropsch derived product having molecules characterized by a higher average molecular weight and increased branching as compared to the Fischer-Tropsch derived feed.
Hydrotreating Of Fischer-Tropsch Derived Feeds Prior To Oligomerization Using An Ionic Liquid Catalyst
David Johnson - Petaluma CA, US Thomas Harris - Benicia CA, US Michael Driver - San Francisco CA, US
International Classification:
C10G057/02
US Classification:
585330000, 585329000
Abstract:
A process for oligomerizing a Fischer-Tropsch derived feed containing oxygenates which comprises (a) reducing significantly the oxygenates present in the Fischer-Tropsch derived feed by contacting said feed with a hydrotreating catalyst under hydrotreating conditions in a hydrotreating zone and recovering from the hydrotreating zone a Fischer-Tropsch derived hydrotreated feed which contains a significantly reduced amount of oxygenates as compared to the Fischer-Tropsch derived feed and also a significant amount of paraffins; (b) pyrolyzing the Fischer-Tropsch derived hydrotreated feed in a thermal cracking zone under thermal cracking conditions pre-selected to crack the paraffin molecules to form olefins and collecting an olefin-enriched Fischer-Tropsch feed from the thermal cracking zone; (c) contacting the olefin-enriched Fischer-Tropsch feed with a Lewis acid ionic liquid catalyst in an oligomerization zone under oligomerization reaction conditions; and (d) recovering from the oligomerization zone a Fischer-Tropsch derived product having molecules characterized by a higher average molecular weight and increased branching as compared to the Fischer-Tropsch derived feed.
Aqueous Solutions Of Amine Functionalized Ionic Compounds For Carbon Capture Processes
- San Ramon CA, US - Mobile AL, US Zunqing He - San Rafael CA, US Kevin N. West - Mobil AL, US Hye Kyung Timken - Albany CA, US Michael S. Driver - San Francisco CA, US
International Classification:
B01D 53/62 B01D 53/14 B01D 53/78
Abstract:
An aqueous ionic absorbent solution is disclosed containing (a) about 15 wt. % to about 80 wt. % of one or more diluents, based on the total weight of the aqueous ionic absorbent solution; and (b) an ionic absorbent containing a cation and an anion comprising an amine moiety.
Process For The Separation Of Carbon Dioxide From Flue Gas
- San Ramon CA, US - Mobile AL, US Zunqing He - San Rafael CA, US Kevin N. West - Mobil AL, US Hye Kyung Timken - Albany CA, US Michael S. Driver - San Francisco CA, US
International Classification:
B01D 53/14
US Classification:
95156, 95236, 95235, 95232
Abstract:
A process and system for separating COfrom a flue gas stream is disclosed. The process involves (a) contacting a flue gas stream containing water vapor and COwith an ionic absorbent under absorption conditions to absorb at least a portion of the COfrom the flue gas stream and form a CO-absorbent complex; wherein the ionic absorbent comprises a cation and an anion comprising an amine moiety; and (b) recovering a gaseous product having a reduced COcontent.
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