Abstract: The present invention provides, in part, formulations comprising a beta-lactamase. Particularly, modified-release powder formulations comprising a beta-lactamase are provided which release a substantial amount of the beta-lactamase in the intestines. Therapeutic uses of the beta-lactamase formulations are also provided.

Abstract: The present invention relates, in part, to treatment of various diseases and disorders such as GI disorders through modulation of F420-dependent enzymes including specific enzymes involved in methanogenesis.

Abstract: Ferrocene dicarboxylic acid diesters have the general formula (I), in which X stands for an oligoethylene glycol radical with 2 to 20 ethoxyl units and/or an &agr;,&ohgr;-alkyldiol radical with 2 to 18 C atoms. Also disclosed are processes for preparing the same, their use, solid composite propellants containing the disclosed ferrocene dicarboxylic acid diesters and processes for preparing the same.

Abstract: The invention concerns a supported catalyst in the form of packing and constructed on an open-pore support material on whose external and internal surfaces a macro-porous ion exchange resin is mechanically and/or chemically affixed.

Abstract: Ferrocene compounds are produced from related intermediates, wherein the ferrocene compounds are represented by the general formula (I): ##STR1## wherein Z is one of the groups --CH.sub.2 --Y, --CO--(CH.sub.2).sub.n --CO--X or --CO--X, in which n is 1 to 6; X is an (oligo-)alkylene glycol residue with 1 to 10 alkoxy units or an alkanediol residue with 2 to 18 carbon atoms, and Y is X or OH, andR is an alkyl group with 2 to 18 carbon atoms, an aralkyl group with 7 to 20 carbon atoms, or H, when Y.noteq.OH.The related intermediates differ from the ferrocene compound in that Z is replaced by Z' which is --COOH or --CO--(CH.sub.2).sub.n --COOH. The ferrocene compounds of formula (I) are especially suitable as combustion moderators for solid fuels.

Abstract: Molded bodies in the form of packing bodies comprising a macroporous strongly acid or basic ion exchange resin having a voids fraction of 5-95 vol % of the macro shape without pores, a BET surface area of 0.1-1,000 sq m/g, and an ion exchange capacity of 0.05-10 meq/g.

Abstract: Metal oxide powders comprised of Cr(III) oxide, Ti(IV) oxide, V(V) oxide, or mixtures of these, or metal mixed oxides comprised of Cr(III) oxide and Ti(IV) oxide and V(V) oxide, or their mixtures. They have BET surfaces of 5-50m.sup.2 /g and mean particle diameters of 25-350 nm and are useful to increase conversion and selectivity in the manufacture of mono-olefins by catalytic dehydrogenation of saturated hydrocarbons. The metal oxide powders are produced from mixtures of the vaporized metal compounds chromyl chloride, titanium tetrachloride, and vanadyl chloride, in the presence of certain gases by laser pyrolysis.

Abstract: Metal oxide powders comprised of Cr(III) oxide, Ti(IV) oxide, V(V) oxide, or mixtures of these, or metal mixed oxides comprised of Cr(III) oxide and Ti(IV) oxide and V(V) oxide, or their mixtures. They have BET surfaces of 5-50 m.sup.2 /g and mean particle diameters of 25-350 nm and are useful to increase conversion and selectivity in the manufacture of mono-olefins by catalytic dehydrogenation of saturated hydrocarbons. The metal oxide powders are produced from mixtures of the vaporized metal compounds chromyl chloride, titanium tetrachloride, and vanadyl chloride, in the presence of certain gases by laser pyrolysis.

Abstract: A process for dehydrogenating saturated or unsaturated hydrocarbons wherein the flow direction of the oxygen-containing gas, employed for removing coke deposits on the catalyst surface, is opposite to that for the hydrocarbon feed undergoing dehydrogenation.

Abstract: Atomic hydrogen for chemical reaction is produced in relatively high concentrations by the combustion of molecular hydrogen with a substoichiometric quantity of oxygen. The chemical reactant is supplied at the point of the development of the atomic hydrogen. Combustion is effected at pressures between 10 mbar and 1.5 bar, with a mole ratio of molecular hydrogen to molecular oxygen of 2.3 to 5.0.

Abstract: A motor fuel comprising 35-98% hydrocarbon-containing base and 2-65% by volume of an additive which comprises a mixture containing(a) 5-35% by volume of methyl tert-butyl ether;(b) 5-40% by volume of isopropyl tert-butyl ether; and(c) 5-40% by volume of sec-butyl tert-butyl ether,has a high octane number and reduces exhaust pollutants.

Abstract: A process for producing sec-butanol and sec-butyl tert-butyl ether from butane comprises: (a) partially isomerizing n-butane to produce a mixture of n-butane and isobutane; (b) catalytically dehydrogenating said butanes to produce a mixture containing at least butene-1, isobutene and butadiene; (c) selectively hydrogenating butadiene and converting butene-1 to butene-2; (d) etherifying isobutene contained in the dehydrogenation reaction mixture with sec-butanol to form a mixture of sec-butyl tert-butyl ether and unreacted hydrocarbons; (e) converting butene-2 from the unreacted hydrocarbon mixture by hydration to produce sec-butanol; (f) recycling said sec-butanol to the etherification step; recovering said sec-butyl tert-butyl ether.

Abstract: A process for producing isopropyl alcohol and isopropyl tert-butyl ether from a mixture of light hydrocarbons containing propane and butane, comprises:(a) separating from the mixture of light hydrocarbons a propane fraction and a butane fraction containing at least n-butane;(b) isomerizing at least a portion of the n-butane in the butane fraction from step (a) whereby a hydrocarbon mixture containing at least n-butane and isobutane is formed;(c) catalytically dehydrogenating the isobutane in the hydrocarbon mixture from step (b) whereby a hydrocarbon mixture containing at least isobutene is produced;(d) catalytically dehydrogenating the propane in the propane fraction from step (a) whereby a hydrocarbon mixture containing at least propene is produced;(e) reacting the propene in the hydrocarbon mixture from step (d) with water, whereby a mixture containing hydrocarbons and isopropyl alcohol is formed;(f) reacting the isopropyl alcohol from step (e) with at least part of the isobutene in the hydrocarbon mixture