초록 ▼

are useful for the preparation of chlorine from hydrogen chloride in a non-steady-state Deacon process, for the reaction of ethylbenzene to give styrene in a non-steady-state oxydehydrogenation, for preparing aziridine from ethanolamine, in reductions, hydrogenations, oxidations, dehydrogenations, a

are useful for the preparation of chlorine from hydrogen chloride in a non-steady-state Deacon process, for the reaction of ethylbenzene to give styrene in a non-steady-state oxydehydrogenation, for preparing aziridine from ethanolamine, in reductions, hydrogenations, oxidations, dehydrogenations, acid- or base-catalyzed reactions or reactions in a fluidized bed, for removing combustion residues from diesel exhaust gases and for removing NO.sub.x from waste gases, in bioreactors together with bacteria and as biocatalyst supports with immobilized enzymes or microbes, and a process for producing said monomodal or polymodal catalyst support or catalyst.

대표청구항 ▼

[ We claim:] [1.] A monomodal or polymodal catalyst support or catalyst having a BET specific surface area of from 0.01 to 250 m.sup.2 /g and a monomodal or polymodal pore size distribution having a mean pore diameter of from 50 to 300,000 nm measured by the mercury pressure porosimetry method, wher

[ We claim:] [1.] A monomodal or polymodal catalyst support or catalyst having a BET specific surface area of from 0.01 to 250 m.sup.2 /g and a monomodal or polymodal pore size distribution having a mean pore diameter of from 50 to 300,000 nm measured by the mercury pressure porosimetry method, wherein the pore size distribution fulfills at least one of the following conditions a) to d)a) from 10 to 95% of the pore volume is from about 0.2 to 100 times the mean pore diameter,b) from 10 to 80% of the pore volume is from about 0.8 to 100 times the mean pore diameter,c) from 50 to 95% of the pore volume is from about 0.2 to 1 times the mean pore diameter,d) from 50 to 80% of the pore volume is from about 0.8 to 1 times the mean pore diameter, the conditione) the width at half height of the pore size distribution is less than 0.6 times the mean pore diameter. [2.] A process for producing a monomodal or polymodal catalyst support or catalyst as defined in claim 1, comprising the steps of shaping a mixture ofA) from 15 to 70% by volume of at least one ofI) an inorganic powder selected from the group of oxides, nitrides, carbides, silicates, aluminosilicates of the elements beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium, indium, thallium, silicon, germanium, tin, lead, antimony, selenium, tellurium, polonium, astatine, iron, cobalt, nickel, ruthenium, rhodium, palladium, osmium, iridium, platinum, copper, silver, gold, zinc, cadmium, mercury, scandium, yttrium, lanthanum, actinium, titanium, zirconium, hafnium, vanadinium, niobium, tantalum, chromium, molybdenum, tungsten, manganese, technetium, rhenium, cerium, praseodymium and mixtures thereof,II) a metallic powder selected from compounds metals and alloys of the elements boron, aluminum, gallium, indium, thallium, silicon, germanium, tin, lead, antimony, selenium, tellurium, polonium, neodymium, samarium, dysprosium, astatine, iron, cobalt, Raney cobalt, nickel, Raney nickel, ruthenium, rhodium, palladium, osmium, iridium, platinum, copper, silver, gold, zinc, cadmium, mercury, scandium, yttrium, lanthanum, actinium, titanium, zirconium, hafnium, vanadinium, niobium, tantalum, chromium, molybdenum, tungsten, manganese, technetium, rhenium, cerium, praseodymium, WC, TiC, TaC, VC and mixtures thereof, WC-cobalt, TiC-cobalt, TaC-cobalt, VC-cobalt and mixtures thereof and also carbon,III) an active component selected from the group of the inorganic acids, the metals lithium, sodium, potassium, rubidium, cesium, francium, beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium, indium, thallium, silicon, germanium, tin, lead, arsenic, antimony, bismuth, selenium, tellurium, polonium, astatine, iron, cobalt, Raney cobalt, nickel, Raney nickel, ruthenium, rhodium, palladium, osmium, iridium, platinum, copper, silver, gold, zinc, cadmium, mercury, scandium, yttrium, lanthanum, actinium, titanium, zirconium, hafnium, vanadinium, niobium, tantalum, chromium, molybdenum, tungsten, manganese, technetium, rhenium, cerium, praseodymium, mixtures thereof, and their borates, carbonates, silicates, nitrates, phosphates, arsenates, antimonates, bismuthates, sulfates, selenates, tellurates, vanadates, molybdates, niobates, chromates, oxides, hydroxides, halides, sulfides, selenides, tellurides, nitrides, phosphides, arsenides, acetates, acetylacetonates, palladates, platinates, cyanides, thiocyanates, manganates, rhenates, osmates, carbides, suicides, borides, and ammonium compounds and all component mixtures thereof andIV) an organic powder selected from the group of Teflon and polyimideB) from 30 to 85% by volume of a binder selected from the group of a polyethylene polymer, a polypropylene polymer, a copolymer of one selected from ethylene, propylene, 1-butene and isobutene, a polystyrene copolymer, a polymethyl methacrylate copolymer, a polyethylene oxide copolymer, an ethylene-vinyl acetate copolymer, and a mixture ofB.sub.1) from 50 to 100% by weight of a polyoxymethylene homopolymer or copolymer andB.sub.2) from 0 to 50% by weight of a polymer homogeneously dissolved in B.sub.1) or dispersed in B.sub.1) at a mean particle size of less than 1 .mu.m andC) from 0 to 15% by volume of a dispersant,removing the binder by pyrolysis at from 300 to 600.degree. C. andsubsequent presintering at from 600 to 1400.degree. C. and,optionally, applying active components III to the component A) or to the presintered composition by single or multiple steeping, impregnating, spray impregnating, precipitating on, hicoating, washcoating or spray drying,wherein the catalyst support or catalyst after the pyrolytic removal of the binder has a BET specific surface area of from 0.01 to 250 m.sup.2 /g and a pore size distribution of from 50 to 300,000 nm measured by the mercury pressure porosimetry method.