Max M. Tirtowidjojo - Lake Jackson TX, US Barry B. Fish - Lake Jackson TX, US Hendrik L. Pelt - Terneuzen, NL Dennis W. Jewell - Angleton TX, US Mark D. Bearden - Richland WA, US Jon H. Siddall - Midland MI, US Brien A. Stears - League City TX, US Haivan D. Tran - Pearland TX, US Jan W. Verwijs - Hoek, NL Richard M. Wehmeyer - Lake Jackson TX, US
International Classification:
C07C 27/06
US Classification:
518705
Abstract:
The present invention provides a method for simplifying manufacture of a mixed alcohol or mixed oxygenate product from synthesis gas. The mixed alcohol or mixed oxygenate product contains ethanol and other oxygenates with two or more carbon atoms per molecule. The method includes stripping a portion of carbon dioxide and inert gases contained in a mixed alcohol synthesis reaction product using a methanol-containing stream, such as one produced as part of the method, as a medium to absorb said carbon dioxide and inert gases and recycling light products and heavy products to one or more of synthesis gas generation, mixed alcohol synthesis and separation of desired mixed alcohol or mixed oxygenate products from other components of a mixed alcohol synthesis stream. The present invention also provides downstream processing of the mixed alcohol or mixed oxygenate product by subjecting the product to a dehydration step in order to convert at least ethanol, preferably at least ethanol and propanol, to their corresponding olefins (e.g. ethylene and propylene).
Robert G. Bowman - Woodbury MN, US Eric E. Stangland - Midland MI, US Mark E. Jones - Midland MI, US Dean M. Millar - Midland MI, US Simon G. Podkolzin - Midland MI, US Brien A. Stears - League City TX, US Richard M. Wehmeyer - Lake Jackson TX, US
International Classification:
C07C 51/14 C07C 17/013
US Classification:
562520, 570243
Abstract:
Oxidatively halogenate methane by placing a feedstream that comprises methane, a source of halogen, a source of oxygen and, optionally, a source of diluent gas in contact with a first catalyst (e.g. a solid super acid or a solid super base) that has greater selectivity to methyl halide and carbon monoxide than to methylene halide, trihalomethane or carbon tetrahalide. Improve overall selectivity to methyl halide by using a second catalyst that converts at least part of the feedstream to a mixture of methyl halide, methylene halide, trihalomethane, carbon tetrahalide and unreacted oxygen, and placing that mixture in contact with the first catalyst which converts at least a portion of the methylene halide, trihalomethane and carbon tetrahalide to carbon monoxide, hydrogen halide and water.
Processes And Systems For Separating Carbon Dioxide In The Production Of Alkanes
- Midland MI, US Peter E. Groenendijk - Terneuzen, NL Andrzej Malek - Midland MI, US Davy L.S. Nieskens - Terneuzen, NL Brien A. Stears - Friendswood TX, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
C07C 7/08 B01D 3/14 B01D 3/40 B01D 53/14
Abstract:
A method for separating COfrom Cto Calkanes includes introducing a first stream including Cto Calkanes and COinto a first separation zone, the first separation zone including a hydrocarbon solvent, and separating the first stream into a recycle stream and a second stream in the first separation zone. The recycle stream including COand one or more of CO, H, and CH, and the second stream including Cto Calkanes. The method further includes introducing the second stream into a second separation zone, and separating the second stream into a third stream and a fourth stream, wherein the third stream includes Calkanes and the fourth stream includes Cto Calkanes.
- Midland MI, US Alexey Kirilin - Hoek, NL Andrzej Malek - Midland MI, US Victor Sussman - Midland MI, US Matthew T. Pretz - Freeport TX, US Brien A. Stears - League City TX, US Barry B. Fish - Lake Jackson TX, US Eric E. Stangland - Midland MI, US Brian W. Goodfellow - Sugarland TX, US Manish Sharma - Missouri City TX, US
According to one or more embodiments described herein, a method for dehydrogenating hydrocarbons may include passing a hydrocarbon feed comprising one or more alkanes or alkyl aromatics into a fluidized bed reactor, contacting the hydrocarbon feed with a dehydrogenation catalyst in the fluidized bed reactor to produce a dehydrogenated product and hydrogen, and contacting the hydrogen with an oxygen-rich oxygen carrier material in the fluidized bed reactor to combust the hydrogen and form an oxygen-diminished oxygen carrier material. In additional embodiments, a dual-purpose material may be utilized which has dehydrogenation catalyst and oxygen carrying functionality.
Processes And Systems For Separating Carbon Dioxide In The Production Of Alkanes
- Midland MI, US Peter E. Groenendijk - Terneuzen, NL Andrzej Malek - Midland MI, US Davy L.S. Nieskens - Terneuzen, NL Brien A. Stears - Friendswood TX, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
C07C 7/08 B01D 3/14 B01D 3/40 B01D 53/14
Abstract:
A method for separating COfrom Cto Calkanes includes introducing a first stream including Cto Calkanes and COinto a first separation zone, the first separation zone including a hydrocarbon solvent, and separating the first stream into a recycle stream and a second stream in the first separation zone. The recycle stream including COand one or more of CO, H, and CH, and the second stream including Cto Calkanes. The method further includes introducing the second stream into a second separation zone, and separating the second stream into a third stream and a fourth stream, wherein the third stream includes Calkanes and the fourth stream includes Cto Calkanes.
Methods For Designing Scaled-Up Fluid Catalytic Reactors
- Midland MI, US Ben J. Freireich - Midland MI, US Madhusudhan Kodam - Midland MI, US Brien A. Stears - Galveston TX, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
B01J 8/26
Abstract:
According to one or more embodiments of the present disclosure, a fluid catalytic reactor may be scaled-up by a method that includes one or more of constructing, operating, observing, or obtaining data related to a template fluid catalytic reactor comprising a template riser, a template lower reactor portion, and a template transition portion connecting the template riser and the template lower reactor portion. The method may further include one or more of constructing or operating a scaled-up fluid catalytic reactor based on the template fluid catalytic reactor.
Fluid Catalytic Reactors Which Include Flow Directors
- Midland MI, US Mark W. Stewart - Houston TX, US Ben J. Freireich - Midland MI, US Madhusudhan Kodam - Midland MI, US Brien A. Stears - Freeport TX, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
B01J 8/00 B01J 8/26 B01J 8/34 C10G 11/18
Abstract:
According to one or more embodiments, a fluid catalytic reactor may include a riser, a lower reactor portion, a transition portion, and a flow director. The riser may include a cross-sectional area, and the lower reactor portion may include a cross-sectional area. The transition portion may attach the riser to the lower reactor portion. The cross-sectional area of the riser may be less than the cross-sectional area of the lower reactor portion such that the transition portion is tapered inward from the lower reactor portion to the riser. The flow director may be positioned at least within an interior region of the transition portion. The flow director may include a body which affects the velocity profile of fluids moving from the lower reactor portion to the riser.
- Midland MI, US Lin Luo - Sugar Land TX, US Susan Domke - Midlothian VA, US Howard W. Clark - College Station TX, US Richard A. Pierce - Lake Jackson TX, US Andrzej M. Malek - Midland MI, US Mark W. Stewart - Pearland TX, US Brien A. Stears - Friendswood TX, US Guido Capone - San Giuliano Milanese, IT Duncan P. Coffey - Hockessin, DE Isa K. Mbaraka - Prospect KY, US
Increase propane dehydrogenation activity of a partially deactivated dehydrogenation catalyst by heating the partially deactivated catalyst to a temperature of at least 660 C., conditioning the heated catalyst in an oxygen-containing atmosphere and, optionally, stripping molecular oxygen from the conditioned catalyst.