Transformation of LPG into aromatic hydrocarbons and hydrogen over zeolite catalysts, Steam dehydrogenation and oxidative reheat process using only one catalyst system, Catalyst for the dehydrogenation of C6-C15 paraffins, Palladium containing hydrogenation catalysts, Process for the preparation of botadiene from N-butene, Recent topics of research and development of catalysis by niobium and tantalum oxides, Autothermal process for the production of olefins, Factors affecting the selectivity of the aromatization of light alkanes on modified ZSM-5 catalysts, Boron-promoted reducible metal oxides and methods for their use, Process for converting olefins having 4 to 12 carbon atoms into propylene, Alkane dehydrogenation over supported chromium oxide catalysts, The effect of potassium in the preparation of magnesium orthovanadate and pyrovanadate on the oxidative dehydrogenation of propane and butane, Conversion of light alkanes to aromatic hydrocarbons: II. However, the effective reactor performance and process reliability largely depends upon the heat requirement for endothermic reaction. Aspect 30: The method according to any preceding aspect, wherein the catalytic reactor comprises a fluidized bed reactor. In still further aspects, the pressure can be in a range derived from any of the two above listed exemplary pressures. Aspect 59: The method according to any preceding aspect, wherein the heat generating material comprises at least 25 wt % of the catalyst bed. No. For this exemplary example, the selected hydrogen co-injection sites on the FBR reactor are depicted in FIG. Aspect 66: The method according to any preceding aspect, wherein the hydrogen feed stream and hydrocarbon feed stream is contacted with a catalyst or a catalyst bed in a radial flow direction. In further aspects, the hydrogen feed stream is contacted with the hydrocarbon stream after preheating of the hydrocarbon feed stream. The CAM system uses a highly efficient alkane dehydrogenation catalyst, the molecular pincer-type iridium complex, to dehydrogenate the PE and the light alkane. Runs 6 to 10 inclusive show that barium peroxide doped with 1% iron gave good selectivity for coupling of isobutane, in contrast to the results for the undoped barium peroxide, as well as substantial activity for dehydrogenation of isobutane. Role of gallium species in propane transformation on GaZSM5 catalysts, Dehydrogenation and oxydehydrogenation of paraffins to olefins, Process for the catalytic dehydrogenation of alkanes to alkenes with simultaneous combustion of hydrogen, Catalytic oxidative dehydrogenation of n-butane, Catalytic hydration of olefins to produce ketones, Conversion of butane over the solid superacid ZrO2/SO42â in the presence of hydrogen, Catalytic dehydrogenation of organic compounds, Lapse for failure to pay maintenance fees, Information on status: patent discontinuation, Expired due to failure to pay maintenance fee. The base metal is selected from the group containing Group IB-VIIB metals, Group IIIA-VA metals, Lanthanide metals, iron, cobalt, and nickel. This regioselectivity holds great promise with respect to the formation of valuable a-olefins and products derived from them in tandem catalytic systems. Barium peroxide is a stable article of commerce and readily available. Aspect 69: The method according to any preceding aspect, wherein the method produces an improved hydrocarbon feed conversion. ), but some errors and deviations should be accounted for. 16. The temperature will vary depending on the processing arrangement and the feedstock, but the minimum temperature necessary is easily determined. While aspects of the present invention can be described and claimed in a particular statutory class, such as the system statutory class, this is for convenience only and one of skill in the art will understand that each aspect of the present invention can be described and claimed in any statutory class. ", Regeneration of catalysts for the dehydrogenation of alkanes, Regeneration of catalysts for dehydrating alkanes, Regeneration method of C10-C13 long-chain n-alkanes dehydrogenation deactivated catalyst, Continuous method for carrying out autothermal gas phase dehydrogenations, A kind of method that dehydrogenation of isobutane prepares isobutene, A kind of successive reaction regenerating unit utilizing sulphurized catalyst to carry out dehydrating alkanes, The renovation process of platiniferous catalyst for dehydrogenation of low-carbon paraffin, Process and catalyst for dehydrogenation of organic compounds, Process for the catalytic dehydrogenation of alkanes to alkenes with simultaneous combustion of hydrogen, Catalyst having a bimodal pore radius distribution, Method for catalytically dehydrating hydrocarbons, Continuous heterogeneous catalyzed partial dehydrogenation of hydrocarbon involves feeding hydrocarbon to reaction chamber enclosed by shell made of specific steel, passing hydrocarbon through catalyst bed and dehydrogenating feed, Unsaturated hydrocarbon manufacturing process.