Patent classifications
C07C5/00
Methods for dehydrogenating reactant hydrocarbons
According to one or more embodiments presently disclosed, one or more reactant hydrocarbons may be dehydrogenated by a method that includes contacting the one or more reactant hydrocarbons with a catalyst system to dehydrogenate at least a portion of the reactant hydrocarbons. The catalyst system may include a zincosilicate support material that includes an MFI framework type structure incorporating at least silicon and zinc. The catalyst system may further include one or more alkali or alkaline earth metals, and one or more platinum group metals.
Branched products
A process for producing isomerized olefins, branched aldehydes, branched alcohols, branched surfactants and other branched derivatives through isomerization, hydroformylation, hydrogenation, surfactant forming reactions and other derivative forming reactions.
Selective poisoning of aromatization catalysts to increase catalyst activity and selectivity
Spent aromatization catalysts containing a transition metal and a catalyst support are selectively poisoned in the disclosed reforming methods, resulting in improvements in overall aromatics yield and selectivity.
DEHYDROGENATION CATALYSTS
This disclosure relates to catalyst compositions including gallium and a zirconium-based mixed oxide support, to methods for making such catalysts, and to methods for dehydrogenating hydrocarbons with such catalysts. For example, in one embodiment, a catalyst composition includes a mixed oxide support comprising at least about 50 wt. % of zirconium oxide, the mixed oxide support being present in the composition in an amount within the range of about 40 wt. % to about 99.9 wt. %; and disposed on the support, gallium, present in the composition in an amount within the range of about 0.1 wt. % to about 30 wt. %, calculated as Ga.sub.2O.sub.3 on a calcined basis.
SITE-SPECIFIC ISOTOPIC LABELING OF 1,4-DIENE SYSTEMS
Methods for preparing isotopically modified 1,4-diene systems from non-isotopically modified 1,4-dienes involve selective oxidation of one or more bis-allylic position(s), or the preparation of isotopically modified 1,4-diene systems via trapping pi-allylic complexes with a source of deuterium or tritium. Such methods are useful for preparing isotopically modified polyunsaturated lipid including polyunsaturated fatty acids and polyunsaturated fatty acid derivatives.
SITE-SPECIFIC ISOTOPIC LABELING OF 1,4-DIENE SYSTEMS
Methods for preparing isotopically modified 1,4-diene systems from non-isotopically modified 1,4-dienes involve selective oxidation of one or more bis-allylic position(s), or the preparation of isotopically modified 1,4-diene systems via trapping pi-allylic complexes with a source of deuterium or tritium. Such methods are useful for preparing isotopically modified polyunsaturated lipid including polyunsaturated fatty acids and polyunsaturated fatty acid derivatives.
SITE-SPECIFIC ISOTOPIC LABELING OF 1,4-DIENE SYSTEMS
Methods for preparing isotopically modified 1,4-diene systems from non-isotopically modified 1,4-dienes involve selective oxidation of one or more bis-allylic position(s), or the preparation of isotopically modified 1,4-diene systems via trapping pi-allylic complexes with a source of deuterium or tritium. Such methods are useful for preparing isotopically modified polyunsaturated lipid including polyunsaturated fatty acids and polyunsaturated fatty acid derivatives.
Dehydrogenation of LPG or NGL and flexible utilization of the olefins thus obtained
The object of the invention is to specify a process with which both C.sub.5 and C.sub.9 aldehydes can be produced economically. Here, the process should be able to to be supplied with the lowest possible dependence on raw material suppliers and also should be able to react flexibly to fluctuations in demand with respect to C.sub.5 and C.sub.9 aldehydes. The use of resources should also be optimized. The process proposed uses LPG or NGL as raw material. The process according to the invention essentially differs from known LPG-based processes in that the intermediate obtained, after dehydrogenation and removal of by-products, is divided into two portions. C9 aldehyde is produced from the first portion by oligomerization and hydroformylation while C5 aldehyde is obtained by hydroformylation of the second portion. This has the critical advantage that it is possible to divide the intermediate flexibly into the two portions so that either more C.sub.5 or more C.sub.9 aldehydes can be produced depending on the respective demand.
Process for the production of white oils from waste oils
The present invention describes a process for the production of technical white oils or edible or medicinal oils from waste oils originating from industrial use or engine use, said process using a deep hydrotreatment.
Service improvement by better incoming diagnosis data, problem specific training and technician feedback
A method for failure analysis and technician assessment, the method may include sensing sensed vehicle parameters by multiple vehicle sensors that comprise multiple types of sensors; calculating, by a vehicle monitor, based on the sensed vehicle parameters, parameters of multiple vehicle components; wherein the vehicle monitor is mechanically coupled to the vehicle or installed in the vehicle; searching, by the vehicle monitor and based on the parameters of the multiple vehicle components, for a vehicle failure that is either a current vehicle failure or an impeding vehicle failure; receiving, by the vehicle monitor, a notification that the vehicle failure was repaired; and estimating an impact of the repair by the vehicle monitor and based on at least parameters of multiple vehicle components that are calculated from sensed vehicle parameters that are sensed after the repair.