JEFFREY A JONES, M.D.
Urology at Taub Loop, Houston, TX

2011025, Oct 20, 2011

Apr 19, 2010

12/762910

David B. Spicer - Houston TX, US
Jeffrey P. Jones - Houston TX, US

C07C 4/04, B01J 19/00, B21D 53/02, F28F 1/00, F28F 21/08

585648, 165177, 165180, 2989003, 422198

In one aspect, the present techniques include a heat exchange apparatus including: a) a body comprising an interior cavity, the body including: a first surface and a second surface defining at least a portion of the body and the first surface positioned exterior with respect to the second surface and the interior cavity, and the second surface positioned exterior with respect to the interior cavity and interior with respect to the first surface; b) a first conduit for conveying a fluid to the body; c) a second conduit in fluid communication with the first conduit wherein the second conduit is positioned at least partially within the interior cavity of the body; and d) a joint between the first conduit and the second conduit, wherein the joint moves between a first location and a second location based on the temperature within the interior cavity, wherein at least one of said first location and said second location is positioned intermediate the first surface and the second surface.

2012009, Apr 26, 2012

Oct 12, 2011

13/271808

ChangMin Chun - Annandale NJ, US
D. Samuel Deutsch - Flemington NJ, US
James E. Feather - Fairfax VA, US
Jeffrey P. Jones - Houston TX, US
David B. Spicer - Houston TX, US

EXXONMOBIL RESEARCH AND ENGINEERING COMPANY - Annandale NJ

F16L 9/147, B05D 3/06, C23C 26/00, B05D 3/10, B05D 3/14, H05H 1/24, B05D 3/12

138177, 427576, 427554, 427532

Provided is a bimetallic tube for transport of hydrocarbon feedstocks in a petrochemical process unit and/or refinery process unit, including: i) an outer tube layer being formed from a steam cracker alloy including at least 18.0 wt. % Cr and at least 10.0 wt. % Ni; ii) an inner tube layer being formed from an alumina forming bulk alloy including 5.0 to 10.0 wt. % of Al, 18.0 wt. % to 25.0 wt. % Cr, less than 0.5 wt. % Si, and at least 35.0 wt. % Fe with the balance being Ni, wherein the inner tube layer is formed plasma powder welding the alumina forming bulk alloy on the inner surface of the outer tube layer; and iii) an oxide layer formed on the surface of the inner tube layer, wherein the oxide layer is substantially comprised of alumina, chromia, silica, mullite, spinels, or mixtures thereof.

7338645, Mar 4, 2008

Jan 21, 2004

10/761745

Jeffrey P. Jones - Houston TX, US
Kenneth Ray Clem - Humble TX, US
Stephen N. Vaughn - Kingwood TX, US
Teng Xu - Houston TX, US
Jeffrey L. White - Cary NC, US

ExxonMobil Chemical Patents Inc. - Houston TX

B01J 19/26, B01J 8/00, C07C 1/20

422240, 422198, 422139, 422220, 422108, 585639

Disclosed is a method and system for reducing the formation of metal catalyzed side-reaction byproducts formed in the feed vaporization and introduction system of a methanol to olefin reactor system by forming and/or coating one or more of the heating devices, feed lines or feed introduction nozzles of/with a material that is resistant to the formation of metal catalyzed side reaction byproducts. The invention also may include monitoring and/or maintaining the temperature of at least a portion of the feed vaporization and introduction system and/or of the feedstock contained therein below about 400° C. , 350° C. , 300° C. , 250° C. , 200° C. or below about 150° C. The temperature can be maintained in the desired range by jacketing at least a portion of the feed vaporization and introduction system, such as at least a portion of the feed introduction nozzle, with a thermally insulating material or by implementing a cooling system.

7951985, May 31, 2011

Jan 6, 2011

12/985789

Neeraj Sangar - League City TX, US
Larry L. Iaccino - Seabrook TX, US
Jeffrey P. Jones - Houston TX, US

ExxonMobil Chemical Patents Inc. - Houston TX

C07C 2/52

585403, 585407, 585420, 585418

In a process for converting methane to aromatic hydrocarbons, a feed containing methane is contacted with a dehydrocyclization catalyst in a reaction zone under conditions effective to convert the methane to aromatic hydrocarbons. The reaction zone is contained within a reactor and the reactor or an internal component of the reactor has at least one surface that is chemically exposed to the feed and is formed from a refractory material that exhibits a carbon uptake (mass of carbon absorbed per unit of exposed metal surface area) of less than 25 g/mwhen exposed to mixture of 50 vol % methane and 50 vol % Hat 900° C. for 168 hours.

2012001, Jan 26, 2012

Jul 21, 2011

13/188330

Calvin W. Crossley - Houston TX, US
Jeffrey W. Jones - Houston TX, US
Allen P. Allegra - Houston TX, US
Jonathan Bowman - Houston TX, US
Lloyd Brown - Houston TX, US
John Dagleish - Houston TX, US
Brian J. Fielding - Houston TX, US
Mitch Guinn - Houston TX, US
Joe Q. Jin - Houston TX, US
Wan Cai Kan - Houston TX, US
Roald T. Lokken - Houston TX, US
Mario R. Lugo - Houston TX, US
Peter G. Noble - Houston TX, US
Matthew J. Obernuefemann - Houston TX, US
Murray Smith - Houston TX, US
Paul M. Sommerfield - Houston TX, US
Charlie Tyrell - Houston TX, US
Richard Weser - Houston TX, US
Stephen Wetch - Houston TX, US

E21B 43/01, E21B 33/00

166344, 166364

A system and method for rapidly responding to and regaining control of uncontrolled flow from offshore hydrocarbon wells, comprising a subsea containment assembly, optionally including a capture caisson assembly installed around the assembly, riser systems for production of hydrocarbons to capture vessels on the surface of the sea, and modularized subsystems facilitating communication between and fluid flow from the subsea containment assembly through the riser to the capture vessel.