Abstract: The invention relates to a process for the continuous production of one or more olefins from an aqueous solution of corresponding alcohol(s) including: Providing a solid-free aqueous solution of the alcohol(s); putting the solution through a reactor, which is filled with a fixed-bed catalyst such that the solution comes into contact with the catalyst when flowing through the reactor at a temperature of at least 300° C. and a pressure of at least 220 bar in such a temperature/pressure combination that the alcohol(s) are reacted under supercritical conditions; and transferring a resulting two-stage mixture to a separator, in which the mixture is separated in a raw olefin gas phase and an aqueous liquid phase; wherein the catalyst is selected from among metal oxides having the properties of a Bronstedt acid, insoluble metallic or semi-metallic phosphates as well as porous materials selected from among pumice and carbon, the surface area of which is coated with inorganic acid groups.

Abstract: Method for the manufacture of furan compounds by using a heterogeneous catalyst in aqueous solution.

Abstract: The invention relates to a process for the continuous production of one or more olefins from an aqueous solution of corresponding alcohol(s) comprising the following steps: Providing a solid-free aqueous solution of the alcohol(s), Putting said solution through a reactor, which is filled with a fixed-bed catalyst such that said solution comes into contact with the catalyst when flowing through said reactor at a temperature of at least 300° C. and a pressure of at least 220 bar in such a temperature/pressure combination that said alcohol(s) are reacted under supercritical conditions, and Transferring a resulting two-stage mixture to a separator, in which said mixture is separated in a raw olefin gas phase and an aqueous liquid phase, Wherein said catalyst is selected from among metal oxides having the properties of a Brønstedt acid, insoluble metallic or semi-metallic phosphates as well as porous materials selected from among pumice and carbon, the surface area of which is coated with inorganic acid groups.

Abstract: Disclosed is a method for producing polyalcohols in the form of sugar alcohols from the group comprising sorbitol and mannitol and other optional C2 to C6 polyols. According to said method, a monosaccharide, disaccharide, oligosaccharide, or polysaccharide containing at least one glucose unit and/or at least one fructose unit is continuously reacted with hydrogen at an elevated temperature and at a great pressure in an aqueous phase in the presence of a hydrogenating catalyst based on ruthenium or ruthenium oxide so as to obtain the inventive polyalcohols. The minimum temperature is set at 100° C. while the minimum pressure is set at 150 bar and the maximum dwell time of the reactants during catalytic hydrogenation is set at 600 s.

Abstract: Disclosed is a method for producing polyalcohols in the form of sugar alcohols from the group comprising sorbitol and mannitol and other optional C2 to C6 polyols. According to said method, a monosccharide, disaccharide, oligosaccharide, or polysaccharide containing at least one glucose unit and/or at least one fructose unit is continously reacted with hydrogen at an elevated temperature and at a great pressure in an aqueous phase in the presence of a hydrogenating catlyst based on ruthenium or ruthenium oxide so as to obtain the inventive polyalcohols. The minimum temperature is set at 100° C. while the minimum pressure is set at 150 bar and the maximum dwell time of the reactants during catalytic hydrogenation is set at 600 s.

Abstract: A process for utilizing the material of ammonium-containing effluent which contains further soluble constituents and, possible additional solids, comprising: a) optionally separating off the solids, b) concentrating the substantially solids-free ammonium-containing effluent to give an aqueous concentrate having an increased content of ammonium and additional soluble constituents, with simultaneous recovery of substantially ammonium-free pure water, c) precipitating ammonium as magnesium ammonium phosphate from the ammonium-containing aqueous concentrate, and d) separating off precipitated magnesium ammonium phosphate with recovery of substantially ammonium-free residual concentrate which at least partially contains the additional soluble constituents.

Abstract: A process for utilizing the material of ammonium-containing effluent which contains further soluble constituents and, possible additional solids, comprising: