Process for preparing a catalyst support which process comprises a) mixing pentasil zeolite having a bulk silica to alumina molar ratio in the range of from 20 to 150 with water, a silica source and an alkali metal salt, b) extruding the mixture obtained in step (a), c) drying and calcining the extrudates obtained in step (b), d) subjecting the calcined extrudates obtained in step (c) to ion exchange to reduce the alkali metal content, and e) drying the extrudates obtained in step (d); process for preparing a catalyst by furthermore impregnating such support with platinum in an amount in the range of from 0.001 to 0.1 wt % and tin in an amount in the range of from 0.01 to 0.5 wt %, each on the basis of total catalyst; ethylbenzene dealkylation catalyst obtainable thereby and a process for dealkylation of ethylbenzene which process comprises contacting feedstock containing ethylbenzene with such catalyst.

Disclosed are a catalyst composition for oxidative dehydrogenation and a method of preparing the same. More particularly, disclosed is a catalyst composition comprising a multi-ingredient-based metal oxide catalyst and a mixed metal hydroxide. The catalyst composition and the method of preparing the same according to the present disclosure may prevent loss occurring in a filling process due to superior mechanical durability and wear according to long-term use, may inhibit polymer formation and carbon deposition during reaction, and may provide a superior conversion rate and superior selectivity.

A TiO.sub.2-based catalyst precursor material in powder form includes TiO.sub.2 particles with the formula TiO.sub.(2-x)(OH).sub.2x (x=0-1). The particles are coated with one or more auxiliary shaping agents and after coating and drying have a specific surface area of at least 150 m.sup.2/g. The material has a content of 1) 50-99.5% by weight of the titanium-oxygen compound with the general formula TiO.sub.(2-x)(OH).sub.2x, wherein x=0 to 1, or mixtures thereof, wherein the crystalline phases of the titanium-oxygen compound are in the anatase form, and 2) 0.5-50% by weight of an auxiliary shaping agent or mixtures thereof, which evaporates, sublimates and/or decomposes upon heating to temperatures below the transformation temperature from anatase to rutile, wherein the % by weight are relative to the total weight of the dried catalyst precursor material.

The present invention relates to a calcined shaped alumina and to a method of preparing a calcined shaped alumina. The method comprises that the alumina in the alumina suspension is hydrothermally aged to have a specific crystallite size. This in turn produces a highly stable alumina in the form of a calcined shaped alumina particularly at temperatures of 1200 C. and above.

A Fischer-Tropsch catalyst includes a substantially homogeneous blend of cobalt and alumina, wherein the catalyst includes a pore volume (PV) ranging from 0.3 cc/g to 0.5 cc/g and an average pore diameter (PD) ranging from 18 nm to 30 nm. Methods of preparing the Fischer-Tropsch catalyst are also included in the present disclosure.

A Fischer-Tropsch catalyst includes a substantially homogeneous blend of cobalt and alumina, wherein the catalyst includes a pore volume (PV) ranging from 0.3 cc/g to 0.5 cc/g and an average pore diameter (PD) ranging from 18 nm to 30 nm. Methods of preparing the Fischer-Tropsch catalyst are also included in the present disclosure.

The invention is in the field of modified carbon products. More in particular, the invention is in the field of graphitized activated carbon bodies. The invention is directed to carbon bodies and ferromagnetic carbon bodies, the production of these bodies from activated carbon, and the applications of the carbon bodies and ferromagnetic carbon bodies, for instance in water treatment and in electrochemical applications.

The invention relates to a process for preparing molecular sieves, such as ZSM-57, using one or more structure directing agents selected from the group consisting of N.sup.1,N.sup.1,N.sup.5,N.sup.5-tetraethyl-N.sup.1,N.sup.5-dimethylpentane-1,5-diaminium, 1-ethyl-1-(5-(1-methylpiperidin-1-ium-1-yl)pentyl)piperidin-1-ium, 1,1-(hexane-1,6-diyl)bis(1-ethylpiperidin-1-ium), and 1,1-diethylpyrrolidin-1-ium.

A method for using a molecular sieve shaped by rice husks as a template is provided. A method using a molecular sieve shaped by rice husks as a catalyst for a thermal cracking reaction for stearic acid is provided. A method for manufacturing a molecular sieve incorporating rice husks, the method includes the following steps. (1) mixing molecular sieve powder containing rice husks, a binder, and an extrusion aid to be homogeneous, then adding a peptizer, and mixing to be homogeneous to obtain a uniform mixture; (2) introducing water to the uniform mixture, mixing to be homogeneous, and performing a kneading process to shape a sticky conglomerate; (3) extruding the sticky conglomerate obtained in the step (2) with an extrusion device to obtain moist strips; and (4) drying, calcining, and shaping the moist strips obtained in the step (3) to obtain the molecular sieve incorporating the rice husks.

A method for using a molecular sieve shaped by rice husks as a template is provided. A method using a molecular sieve shaped by rice husks as a catalyst for a thermal cracking reaction for stearic acid is provided. A method for manufacturing a molecular sieve incorporating rice husks, the method includes the following steps. (1) mixing molecular sieve powder containing rice husks, a binder, and an extrusion aid to be homogeneous, then adding a peptizer, and mixing to be homogeneous to obtain a uniform mixture; (2) introducing water to the uniform mixture, mixing to be homogeneous, and performing a kneading process to shape a sticky conglomerate; (3) extruding the sticky conglomerate obtained in the step (2) with an extrusion device to obtain moist strips; and (4) drying, calcining, and shaping the moist strips obtained in the step (3) to obtain the molecular sieve incorporating the rice husks.