Abstract: A process for the preparation of a gaseous mixture containing hydrogen and carbon monoxide by autothermal reforming, comprising(i) partial oxidation of a gaseous hydrocarbon feed in a partial oxidation zone,(ii) passing the effluent of the partial oxidation zone to a reforming zone; and(iii) reforming in the presence of a reforming catalyst in the reforming zone to form a reformed product stream, wherein the partial oxidation is carried out at a H.sub.2 C/C molar feed ratio of less than 0.2, and, preferably reformed product stream has a temperature in the range from 1000.degree. to 1350.degree. C., or wherein the reformed product stream has a temperature in the range from 1100.degree. to 1300.degree. C., and, preferably the partial oxidation is carried out at a H.sub.2 O/C molar feed ratio of less than 0.5.

Abstract: A process for the catalytic partial oxidation of a hydrocarbon feedstock comprises contacting a feed comprising a hydrocarbon feedstock and an oxygen-containing gas with a catalyst in a reaction zone, which catalyst is retained in the reaction zone in a fixed arrangement having a tortuosity of at least 1.1 and having at least 750 pores per square centimeter.

Abstract: The present invention provides a process for the preparation of carbon monoxide and/or hydrogen from a hydrocarbon feedstock. The hydrocarbon feedstock is subjected in a first stage to a catalytic partial oxidation process in which it is contacted, as a gaseous mixture comprising the hydrocarbon feedstock and an oxygen-containing gas, which gaseous mixture also comprises nitrogen, with a catalyst comprising as a catalytically active metal rhodium, iridium or platinum. At least a portion of the products of the first stage is subjected in a second stage to a process in which ammonia and/or hydrogen cyanide is removed.

Abstract: A process for the preparation of linear alternating copolymers of carbon monoxide and an ethylenically unsaturated compound by polymerizing the monomers in the presence of a suitable catalyst system, one or more components present in the reaction mixture being contaminated with alkali(ne earth) metal salt(s), which process involves a treatment by which at least part of the alkali(ne earth) metal salt is removed such that the total amount of alkali(ne earth) metals present in the copolymerization product is less than 1 part per million by weight; a copolymer composition comprising said copolymer, an alkali(ne earth) metal salt contaminant and a stabilizing quantity of a substance which is able to bind at least part of the alkali(ne earth) metal salt.

Abstract: This invention relates to a process for the preparation of Si.sub.2 N.sub.2 O-containing which comprises reacting an amorphous, non-porous silicon dioxide material with flowing, ammonia-containing gas at temperatures of 950.degree.-1300.degree. C. The expression "flowing, ammonia-containing gas" refers to a large number of different gas mixtures which may contain only ammonia or one or more other gases besides ammonia, such as nitrogen, hydrogen, carbon monoxide, carbon dioxide or oxygen. Preferably, pure ammonia or ammonia mixed with the customary unconverted reaction components of the ammonia synthesis, optionally mixed with traces of carbon dioxide, carbon monoxide or oxygen, is employed.

Abstract: This invention relates to a process for the preparation of Si.sub.2 N.sub.2 O-containing materials which comprises reacting an amorphous, non-porous silicon dioxide material with flowing, ammonia-containing gas at temperatures of 950.degree.-1300.degree. C. The expression "flowing, ammonia-containing gas" refers to a large number of different gas mixtures which may contain only ammonia or one or more other gases besides ammonia, such as nitrogen, hydrogen, carbon monoxide, carbon dioxide or oxygen. Preferably, pure ammonia or ammonia mixed with the customary uncoverted reaction components of the ammonia synthesis, optionally mixed with traces of carbon dioxide, carbon monoxide or oxygen, is employed.

Abstract: Process for the preparation of polycarbonates by reacting at least one epoxy compound with carbon dioxide at 40.degree. to 200.degree. C. and 2 to 40 bar in the presence of a catalytic amount of a double metal cyanide complex and(a) one or more salts composed of at least bivalent metal ions and metal-free anions having a solubility in water of at least 1 g/100 ml at 25.degree. C., and/or(b) one or more no-metal containing acids of which a 0.1 N solution in water at 25.degree. C. has a pH not exceeding 3.

Abstract: Process for the preparation of polycarbonates by reacting at least one epoxy compound with carbon dioxide at 40.degree. to 200.degree. C. and 2 to 40 bar in the presence of a catalytic amount of a double metal cyanide complex and (a) one or more salts composed of at least bivalent metal ions and metal-free anions having a solubility in water of at least 1 g/100 ml at 25.degree. C., and/or (b) one or more no-metal containing acids of which a 0.1 N solution in water at 25.degree. C. has a pH not exceeding 3.

Abstract: Process for the preparation of polycarbonates by reacting at least one epoxy compound with carbon dioxide at 40.degree. to 200.degree. C. and 2 to 40 bar in the presence of a catalytic amount of a double metal cyanide complex and(a) one or more salts composed of at least bivalent metal ions and metal-free anions having a solubility in water of at least 1 g/100 ml at 25.degree. C., and/or(b) one or more no-metal containing acids of which a 0.1N solution in water at 25.degree. C. has a pH not exceeding 3.

Abstract: A Fischer-Tropsch catalyst is prepared by impregnating a silica carrier with a solution of a zirconium or titanium compound, calcining the composition thus obtained, thereafter impregnating the carrier with a cobalt compound-containing solution and calcining and reducing the composition thus obtained. Catalysts so prepared and containing 5-40 pbw of cobalt and 2-150 pbw of zirconium or titanium per 100 pbw of silica, are used in the preparation of hydrocarbons from a H.sub.2 /CO mixture.