Patent classifications
B01J23/70
Alkane Dehydrogenation Catalyst and Methods of Converting Alkanes to Alkenes
Provided herein is an alkane dehydrogenation catalyst, a method of manufacturing an alkane dehydrogenation catalyst, and a method of converting alkanes to alkenes.
Alkane Dehydrogenation Catalyst and Methods of Converting Alkanes to Alkenes
Provided herein is an alkane dehydrogenation catalyst, a method of manufacturing an alkane dehydrogenation catalyst, and a method of converting alkanes to alkenes.
Catalytic decomposition of hydrocarbons for the production of hydrogen and carbon
A new process for the decomposition of hydrocarbon feed stream(s) that achieves the conversion of a hydrocarbon feed stream to hydrogen and filamentous carbon, with minimal resulting production of carbon oxides is described herein. In this invention it is proposed to achieve the hydrocarbon conversion by the use of dual fluidized bed reaction zones, fluidly connected, for (i). hydrocarbon reaction (the reactor) and (ii). catalyst regeneration and heating (the regenerator) and to use a transition metal supported catalyst to achieve high hydrocarbon conversion and to produce high quality filamentous carbon.
entitled METHOD FOR PREPARING A CATALYST FOR ENVIRONMENTAL DECONTAMINATION BY MEANS OF NON-SELECTIVE REDUCTIVE HETEROGENEOUS ELECTROCATALYSIS
A method consisting in depositing coating of a semiconductor such as TiO.sub.2 on the surface of a substrate of activated carbon in the form of grain or powder that acts by an advanced oxidation-reduction mechanism in environmental decontamination processes, by way of a heterogeneous electrocatalysis system applying an electrical potential having a magnitude equal to or greater than that of the bandgap energy of the semiconductor, which is 3.2 eV in the case of anatase TiO.sub.2, such that an electron rises from the valence band to the conduction band, leaving in its place holes, h+, with enough oxidative capacity to be able to oxidise H.sub.2O and form OH radicals.
FILTER CANDLE WITH MINERAL ADDITIVE
The present invention relates to a filter candle element for the dedusting of industrial gases having improved properties concerning stability and environmental sustainability. This filter candle element comprises a filter body which is composed of inorganic fibers, and a mineral additive which is accumulated to the inorganic fibers. The mineral additive preferably comprises zeolite. Another aspect of the invention relates to a method of manufacturing a filter candle element for dedusting industrial gases. The method comprises the following steps: production of a slurry comprising inorganic fibers and a mineral additive; sucking in the slurry onto a suction core to form the filter candle element; drying of the formed filter candle element.
FILTER CANDLE WITH MINERAL ADDITIVE
The present invention relates to a filter candle element for the dedusting of industrial gases having improved properties concerning stability and environmental sustainability. This filter candle element comprises a filter body which is composed of inorganic fibers, and a mineral additive which is accumulated to the inorganic fibers. The mineral additive preferably comprises zeolite. Another aspect of the invention relates to a method of manufacturing a filter candle element for dedusting industrial gases. The method comprises the following steps: production of a slurry comprising inorganic fibers and a mineral additive; sucking in the slurry onto a suction core to form the filter candle element; drying of the formed filter candle element.
Production of xylenes from syngas
This disclosure relates to the production of xylenes from syngas, in which the syngas is converted to an aromatic product by reaction with a Fischer-Tropsch catalyst and an aromatization catalyst. The Fischer-Tropsch catalyst and aromatization catalyst may be different catalysts or combined into a single catalyst. The aromatic product is then subjected to selective alkylation with methanol and/or carbon monoxide and hydrogen to increase its p-xylene content.
Production of xylenes from syngas
This disclosure relates to the production of xylenes from syngas, in which the syngas is converted to an aromatic product by reaction with a Fischer-Tropsch catalyst and an aromatization catalyst. The Fischer-Tropsch catalyst and aromatization catalyst may be different catalysts or combined into a single catalyst. The aromatic product is then subjected to selective alkylation with methanol and/or carbon monoxide and hydrogen to increase its p-xylene content.
METHODS OF SULFURIZING METAL CONTAINING PARTICLES
Methods of sulfurizing metal containing particles in the absence of hydrogen are described. One method includes contacting a bed of metal containing particles with a gaseous stream comprising hydrogen sulfide and inert gas under reaction conditions sufficient to produce sulfided metal containing particles. The gaseous stream is introduced into a vertical reactor at an inlet positioned at the bottom portion of the reactor and any unreacted hydrogen sulfide and inert gas is removed at an outlet positioned above the inlet. The sulfided metal containing particles can be removed from the reactor and stored.
METHOD FOR PRODUCING CATALYST FIBROUS STRUCTURE
A catalyst fibrous structure having a catalyst metal carried on a fibrous structure, wherein (a) a Log differential micropore volume distribution curve thereof obtained by measurement using a mercury intrusion technique has a peak having a maximum micropore diameter in the range of from 0.1 μm to 100 μm; (b) a Log differential micropore volume at the peak is 0.5 mL/g or more; and (c) an amount of a catalyst metal compound and a binder carried per unit volume is 0.05 g/mL or more. A production method for producing a catalyst fibrous structure having: (1) mixing a catalyst metal compound or a catalyst precursor, and an inorganic binder and a solvent; (2) grinding the mixture to obtain a coating material of the catalyst metal compound or the catalyst precursor having a median particle diameter of 2 μm or less and a viscosity of from 10 mPa.Math.s to 200 mPa.Math.s; (3) impregnating a fibrous structure with the coating material to fill up voids of the fibrous structure with the coating material of the catalyst metal compound or the catalyst precursor; (4) heating and drying the fibrous structure, directly as it is, at a temperature not lower than the boiling point of the solvent; and (5) heating and calcination the dried fibrous structure at a temperature not lower than the dehydration temperature of the inorganic binder to obtain a catalyst fibrous structure.