John S. Buchanan - Lambertville NJ, US Paul F Keusenkothen - Houston TX, US Stephen H. Brown - Bernardsville NJ, US Julian A. Wolfenbarger - Houston TX, US James E. Graham - Baytown TX, US James N. McCoy - Houston TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C10G 69/04 C10G 69/06 C07C 4/04
US Classification:
208 61, 208 58, 585648, 585652
Abstract:
The invention concerns integration of hydroprocessing and steam cracking. A feed comprising crude or resid-containing fraction thereof is treated by hydroprocessing and visbreaking and then passed to a steam cracker to obtain a product comprising olefins.
John Scott Buchanan - Lambertville NJ, US Paul F. Keusenkothen - Houston TX, US Stephen Harold Brown - Pennington NJ, US Julian A. Wolfenbarger - Houston TX, US James Earl Graham - Baytown TX, US James N. McCoy - Houston TX, US
The invention is directed to a process comprising feeding high TAN feedstreams to a steam cracker, whereby naphthenic acids in the feedstreams are substantially converted to CO, CO, and low amounts of smaller acids (e. g. , formic, acetic, propionic, and butyric acids). The feedstream is preferably a high TAN feedstream comprising crude or high TAN feedstream which has previously been subjected to a refinery process to remove resid.
Paul Keusenkothen - Houston TX, US Megan Renstrom - Houston TX, US Julian Wolfenbarger - Houston TX, US Stephen Brown - Bernardsville NJ, US John Buchanan - Lambertville NJ, US
International Classification:
C10G 9/00 C07C 4/02 C10G 15/00
US Classification:
208106000, 585648000, 422189000
Abstract:
The invention concerns integration of hydroprocessing and steam cracking. A feed comprising crude or resid-containing fraction thereof is severely hydrotreated and passed to a steam cracker to obtain an olefins product.
Management Of Hydrogen In Hydorgen-Containing Streams From Hydrogen Sources
Bal K. Kaul - Fairfax VA, US John W. Viets - Fairfax VA, US Mohsen N. Harandi - Calgary, CA Julian A. Wolfenbarger - Friendswood TX, US John Di-Yi Ou - Houston TX, US David Stern - Asbury NJ, US
International Classification:
B01D 53/047
US Classification:
95 96
Abstract:
The use of rapid cycle pressure swing adsorption having a cycle time of less than 30 s for increasing the hydrogen concentration in hydrogen-containing steams, from a hydrogen source, such as a stream reforming unit.
Justin Dwight Edwards - Pacifica CA, US Julian Wolfenbarger - Landenberg PA, US Srinivas R. Vuddagiri - Davis CA, US Iraj Isaac Rahmim - San Francisco CA, US
Assignee:
SILURIA TECHNOLOGIES, INC. - San Francisco CA
International Classification:
C07C 2/84
US Classification:
585 16, 62619, 422187, 585658, 585330
Abstract:
Disclosed herein are processes for producing and separating ethane and ethylene. In some embodiments, an oxidative coupling of methane (OCM) product gas comprising ethane and ethylene is introduced to a separation unit comprising two separators. Within the separation unit, the OCM product gas is separated to provide a C-rich effluent, a methane-rich effluent, and a nitrogen-rich effluent. Advantageously, in some embodiments the separation is achieved with little or no external refrigeration requirement.
Two-Phase Distributor System For Downflow Reactors
Gregory P. Muldowney - Glen Mills PA Ronald A. Weiss - Flemington NJ Julian A. Wolfenbarger - Newtown PA
Assignee:
Mobil Oil Corporation - Fairfax VA
International Classification:
B01J 802 B01D 1102 B01D 4716
US Classification:
422220
Abstract:
A distributor system for uniformly directing vapor and liquid across the surface of a fixed bed of solids in a downflow reactor comprising a distributor tray, and a plurality of open-ended downpipes extending through the tray. A first array of the downpipes has a plurality of vertically spaced elevations of holes above the level of the tray. A second array of the downpipes has at least one elevation of holes at substantially the same height above the level of the tray as one of the upper elevations of holes in the first array of the downpipes. But, the second array has no elevation of holes corresponding to the lowermost elevation of holes, and possibly other lower elevations of holes, in the first array of downpipes. The absence of the lowermost holes in the second array of downpipes causes the liquid flow rate through the distributor tray at a given liquid height to be reduced when that liquid height falls below the elevation of the holes second from the bottom in the first array. This maximizes the liquid height above the lowermost holes, preserving good distribution even when the distributor is subject to variations in level from one point to another.
- The Woodlands TX, US Justin Dwight Edwards - League City TX, US Julian Wolfenbarger - Landenberg PA, US Srinivas R. Vuddagiri - Davis CA, US Iraj Isaac Rahmim - San Francisco CA, US
Disclosed herein are processes for producing and separating ethane and ethylene. In some embodiments, an oxidative coupling of methane (OCM) product gas comprising ethane and ethylene is introduced to a separation unit comprising two separators. Within the separation unit, the OCM product gas is separated to provide a C-rich effluent, a methane-rich effluent, and a nitrogen-rich effluent. Advantageously, in some embodiments the separation is achieved with little or no external refrigeration requirement.
- San Francisco CA, US Julian Wolfenbarger - Landenberg PA, US Milind Ajinkya - Oakton VA, US Jon McCarty - Menlo Park CA, US Joel M. Cizeron - Redwood City CA, US Sam Weinberger - San Francisco CA, US Justin Dwight Edwards - League City TX, US David Sheridan - Menlo Park CA, US Erik C. Scher - San Francisco CA, US Jarod McCormick - San Carlos CA, US
Systems and methods conducive to the formation of one or more alkene hydrocarbons using a methane source and an oxidant in an oxidative coupling of methane (OCM) reaction are provided. One or more vessels each containing one or more catalyst beds containing one or more catalysts each having similar or differing chemical composition or physical form may be used. The one or more catalyst beds may be operated under a variety of conditions. At least a portion of the catalyst beds may be operated under substantially adiabatic conditions. At least a portion of the catalyst beds may be operated under substantially isothermal conditions.