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Craig J Emett

from Swedesboro, NJ
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Also known as:
Craig Janzen Emett
Related to:
Vaughn C Emett, 78Scott A Emett, 39Rebecca Emett, 35Jane E Harris, 47Clark W Emett, 49
Connected to:
Jason S Emett, 45Steven D Emett, 54Constance T Emetti, 82Danny Emeyabbi, 39Deneisia D Emeziem, 35John M Emfinger, 48Troy A Emfinger, 60Amy C Emge, 54

Craig Emett Phones & Addresses

  • Swedesboro, NJ
  • 13619 Heath Spring Ct, Houston, TX 77044 (281) 458-5753

Resumes

Resumes

Craig Emett Photo 1

Synthetic Base Stock Application Development Lead

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Location:
Houston, TX
Industry:
Oil & Energy
Work:
ExxonMobil since Dec 2009
Engineer
Celanese May 2008 - Jan 2010
R&D Engineering Intern
Hexcel Feb 2007 - Feb 2008
Engineering Intern
Education:
University of Utah 2007 - 2010
B.Ch.E, Chemical Engineering
Skills:
Engineering
Process Engineering
Chemical Engineering
Process Simulation
Matlab
Microsoft Excel
Microsoft Office
Powerpoint
Microsoft Word
R&D
Aspen Plus
Languages:
English
Spanish
Craig Emett Photo 2

Craig Emett

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Publications

Us Patents

New Poly Alpha Olefin Compositions

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US Patent:
20130245343, Sep 19, 2013
Filed:
Sep 12, 2012
Appl. No.:
13/612246
Inventors:
Craig J. Emett - Houston TX, US
Mark P. Hagemeister - Houston TX, US
Wenning W. Han - Houston TX, US
Bruce A. Harrington - Houston TX, US
Phillip T. Matsunaga - Houston TX, US
Charles J. Ruff - Houston TX, US
Kevin B. Stavens - Houston TX, US
Margaret M. Wu - Skillman NJ, US
International Classification:
C07C 11/02
US Classification:
585 18, 585530
Abstract:
This invention is directed to a poly alpha olefin (PAO) composition formed in a first oligomerization, wherein at least portions of the PAO have properties that make them highly desirable for a subsequent oligomerization. A preferred process for producing this PAO uses a single site catalyst at high temperatures without adding hydrogen to produce a low viscosity PAO with excellent Noack volatility at high conversion rates. This PAO comprises a dimer product with at least 25 wt % tri-substituted vinylene olefins wherein said dimer product is highly desirable as a feedstock for a subsequent oligomerization. This PAO also comprises trimer and optionally higher oligomer products with outstanding properties that make these products useful as lubricant basestocks following hydrogenation.

Poly Alpha Olefin Compositions

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US Patent:
20130245344, Sep 19, 2013
Filed:
Sep 12, 2012
Appl. No.:
13/612450
Inventors:
Craig J. Emett - Houston TX, US
Mark P. Hagemeister - Houston TX, US
Bruce A. Harrington - Houston TX, US
Phillip T. Matsunga - Houston TX, US
Pramod J. Nandapurkar - Seabrook TX, US
Charles J. Ruff - Houston TX, US
Kevin B. Stavens - Houston TX, US
International Classification:
C10M 105/04
US Classification:
585 18, 585250
Abstract:
Poly alpha olefins (PAOs) are characterized by very low viscosity and excellent Noack volatility. A preferred process for synthesizing said PAOs involves first oligomerizing low molecular weight linear alpha olefins in the presence of a single site catalyst at high temperatures without adding hydrogen and then subsequently oligomerizing at least a portion of the product from the first step in the presence of an oligomerization catalyst.

Process To Produce Improved Poly Alpha Olefin Compositions

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US Patent:
20130253244, Sep 26, 2013
Filed:
Sep 12, 2012
Appl. No.:
13/612391
Inventors:
Craig J. Emett - Houston TX, US
Mark P. Hagemeister - Houston TX, US
Bruce A. Harrington - Houston TX, US
Chon Y. Lin - Houston TX, US
Phillip T. Matsunaga - Houston TX, US
Charles J. Ruff - Houston TX, US
Kevin B. Stavens - Houston TX, US
International Classification:
C10M 105/04
US Classification:
585326
Abstract:
This invention is directed to a two-step process for the preparation of improved poly alpha olefins wherein the first step involves oligomerizing low molecular weight linear alpha olefins in the presence of a single site catalyst and the second step involves oligomerization of at least a portion of the product from the first step in the presence of an oligomerization catalyst. The dimer product from the first oligomerization is characterized by a tri-substituted vinylene olefin content of at least 25 wt %.

Low Viscosity Engine Oil Compositions

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US Patent:
20130090273, Apr 11, 2013
Filed:
Sep 12, 2012
Appl. No.:
13/611500
Inventors:
Richard Wayne Martin - Woolwich Township NJ, US
Douglas Edward Deckman - Mullica Hill NJ, US
Kevin John Kelly - Mullica Hill NJ, US
Craig Janzen Emett - Houston TX, US
Mark Paul Hagemeister - Houston TX, US
Bruce Allan Harrington - Houston TX, US
Chon-Yie Lin - Houston TX, US
Phillip Thomas Matsunaga - Houston TX, US
Charles James Ruff - Houston TX, US
Kevin Bruce Stavens - Houston TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
ExxonMobil Research and Engineering Company - Annandale NJ
International Classification:
C10M 169/04
US Classification:
508150, 508389, 508371, 585 1
Abstract:
This invention is directed to ultra-low viscosity passenger car engine oil compositions with a kinematic viscosity at 100 C. of from 4 to 6 cSt, and comprising in admixture 60 wt % to 90 wt % of a first base oil component, based on the total weight of the composition, the first base oil component consisting of a polyalphaolefin base stock or combination of polyalphaolefin base stocks, each having a kinematic viscosity at 100 C. of from 3.2 cSt to 3.8 cSt; and 0.1 wt % to 20 wt % of a second base oil component, based on the total weight of the composition, the second base oil component consisting of a Group II, Group III or Group V base stock, or any combination thereof; wherein the composition comprises from 0 wt % to less than 0.25 wt % viscosity index improver, on a solid polymer basis.

High Efficiency Engine Oil Compositions

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US Patent:
20130090278, Apr 11, 2013
Filed:
Sep 12, 2012
Appl. No.:
13/611676
Inventors:
Richard Wayne Martin - Woolwich Township NJ, US
Douglas Edward Deckman - Mullica Hill NJ, US
Kevin John Kelly - Mullica Hill NJ, US
Craig Janzen Emett - Houston TX, US
Mark Paul Hagemeister - Houston TX, US
Bruce Allan Harrington - Houston TX, US
Chon-Yie Lin - Houston TX, US
Phillip Thomas Matsunaga - Houston TX, US
Charles James Ruff - Houston TX, US
Kevin Bruce Stavens - Houston TX, US
Assignee:
EXXONMOBIL CHEMICAL PATENTS INC. - Houston TX
EXXONMOBIL RESEARCH AND ENGINEERING COMPANY - Annandale NJ
International Classification:
C10M 169/02
US Classification:
508591
Abstract:
This invention is directed to passenger car engine oil compositions comprising in admixture wt % to wt % of a first base oil component, based on the total weight of the composition, the first base oil component consisting of a polyalphaolefin base stock or combination of polyalphaolefin base stocks, each having a kinematic viscosity at C. of from cSt to cSt; wt % to wt % of a second base oil component, based on the total weight of the composition, the second base oil component consisting of a Group II, Group III or Group V base stock, or any combination thereof; and at least wt % viscosity index improver, on a solid polymer basis.

Lubricating Compositions

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US Patent:
20130090277, Apr 11, 2013
Filed:
Sep 12, 2012
Appl. No.:
13/611629
Inventors:
Richard Wayne Martin - Woolwich Township NJ, US
Douglas Edward Deckman - Mullica Hill NJ, US
Kevin John Kelly - Mullica Hill NJ, US
Craig Janzen Emett - Houston TX, US
Mark Paul Hagemeister - Houston TX, US
Bruce Allan Harrington - Houston TX, US
Chon-Yie Lin - Houston TX, US
Phillip Thomas Matsunaga - Houston TX, US
Charles James Ruff - Houston TX, US
Kevin Bruce Stavens - Houston TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
ExxonMobil Research and Engineering Company - Annandale NJ
International Classification:
C10M 105/32
US Classification:
508459, 585 1
Abstract:
This invention is directed to lubricating compositions comprising a first base oil component consisting of a polyalphaolefin base stock or combination of polyalphaolefin base stocks, each having a kinematic viscosity at 100 C. of from 3.2 cSt to 3.8 cSt and obtained by a process comprising: (a) contacting a catalyst, an activator, and a monomer in a first reactor to obtain a first reactor effluent, the effluent comprising a dimer product, a trimer product, and optionally a higher oligomer product, (b) feeding at least a portion of the dimer product to a second reactor, (c) contacting said dimer product with a second catalyst, a second activator, and optionally a second monomer in the second reactor, (d) obtaining a second reactor effluent, the effluent comprising at least a trimer product, and (e) hydrogenating at least the trimer product of the second reactor effluent.

Metallocene Dimer Selective Catalysts And Processes To Produce Poly Alpha-Olefin Dimers

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US Patent:
20210347921, Nov 11, 2021
Filed:
May 3, 2021
Appl. No.:
17/239004
Inventors:
- Baytown TX, US
Jennifer L. Rapp - Houston TX, US
Jian Yang - Houston TX, US
Jo Ann M. Canich - Houston TX, US
Hua Zhou - Missouri City TX, US
Craig J. Emett - Houston TX, US
Kyle G. Lewis - Houston TX, US
International Classification:
C08F 10/14
C08F 4/659
C08F 4/6592
C08F 8/04
C07C 2/30
C07C 2/32
C08F 2/01
C10M 107/10
Abstract:
The present disclosure generally relates to processes to produce alpha-olefin oligomers and poly alpha-olefins. In an embodiment, the present disclosure provides a process to produce a poly alpha-olefin (PAO), the process including:

Processes To Produce Poly Alpha-Olefin Trimer And Apparatus Therefor

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US Patent:
20210284769, Sep 16, 2021
Filed:
May 3, 2021
Appl. No.:
17/240437
Inventors:
- Baytown TX, US
Mark H. Li - Sugar Land TX, US
Jennifer L. Rapp - Houston TX, US
Pramod J. Nandapurkar - Seabrook TX, US
Brian H. Wahn - Houston TX, US
Craig J. Emett - Houston TX, US
Najeeb M. Kuzhiyil - League City TX, US
Jian Yang - Houston TX, US
International Classification:
C08F 210/16
C08F 4/659
C08F 4/6592
C07C 2/30
C07C 2/32
Abstract:
In at least one embodiment, a process to produce a poly alpha-olefin (PAO) includes introducing a first alpha-olefin to a first catalyst system comprising activator and a metallocene compound into a continuous stirred tank reactor or a continuous tubular reactor under first reactor conditions to form a first reactor effluent. The first alpha-olefin is introduced to the reactor at a flow rate of about 100 g/hr or more. The first reactor effluent includes at least 60 wt % of PAO dimer and 40 wt % or less of higher oligomers, where the higher oligomers are oligomers that have a degree of polymerization of 3 or more. The process includes introducing the first reactor effluent and a second alpha-olefin to a second catalyst composition including an acid catalyst in a second reactor to form a second reactor effluent comprising PAO trimer.
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Craig J Emett from Swedesboro, NJ Get Report