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45results about How to "Maximizing conversion" patented technology

Production of liquid fuels by a concatenation of processes for treatment of a hydrocarbon feedstock

ActiveUS20050250862A1Maximize conversion of carbonLimit costly adjustmentThermal non-catalytic crackingCatalytic crackingSyngasChemistry
The invention relates to an installation and a process for the production of liquid fuels starting from a solid feedstock that contains the organic material in which: a) the solid feedstock is subjected to a gasification stage so as to convert said feedstock into synthesis gas, b) the synthesis gas is subjected to a purification treatment, c) the purified synthesis gas is subjected to a conversion stage that comprises the implementation of a Fischer-Tropsch-type synthesis so as to convert said synthesis gas into a liquid effluent and a gaseous effluent, d) the liquid effluent is fractionated so as to obtain a gaseous fraction, a naphtha fraction, a kerosene fraction and a gas oil fraction, and e) at least a portion of the naphtha fraction is recycled in gasification stage a).
Owner:INST FR DU PETROLE +1

Regenerative autothermal catalytic steam reformer

A compact steam reformer produces hydrogen to power a fuel cell, such as can be used in a vehicle. The steam reformer includes a first channel, at least partly coated with a steam reforming catalyst, and a second channel, at least partly coated with a combustion catalyst, the channels being in thermal contact with each other. Heat from the combustion is used in the steam reforming reaction. In another embodiment, the gas streams feeding the reforming and combustion channels pass through a valve which reverses the gas streams periodically. The combustion channel becomes the reforming channel, and vice versa, so that carbon deposits in the former reforming channel are burned off. This arrangement enables the reforming reaction to continue indefinitely at peak efficiency.
Owner:JOHNSON MATTHEY PLC

High temperature reforming process and catalyst for use therein

A process for generating aromatics from a hydrocarbon feedstream is disclosed. The process includes the steps of (a) passing the hydrocarbon feedstream to a reformer, wherein the reformer is operated at a temperature greater than 540° C.; and (b) reforming the hydrocarbon feedstream to aromatics in the presence of a catalyst, wherein the catalyst comprises (i) a refractory inorganic oxide support, (ii) a platinum group metal, (iii) a Group IVA metal, (iv) a third metal selected from alkali metals and alkaline earth metals, and (v) a halogen.
Owner:UOP LLC
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