Abstract: The invention relates to an apparatus for analyzing heterogeneously catalyzed reactions comprising at least one reactor (3) through which a particulate catalyst flows and at least one reactant feed, wherein arranged downstream of each reactor (3) is a separation apparatus (17) for separating the particulate catalyst from a reaction product comprising condensable gases and arranged downstream of the separation apparatus (17) is a liquid separator (31) for separating liquid constituents from the reaction product, wherein the liquid separator (31) comprises a metallic tube (103) and a deflection body (119), wherein the metallic tube (103) is closed at its ends and the deflection body (119) is accommodated in the metallic tube (103) and the metallic tube (103) comprises a side feed (135) at a first end (105) and a gas outlet (113) at a second end (107) and the gas outlet (113) is connected to at least one sample vessel (37).

Abstract: The invention relates to a separation unit for separating off liquid components from a gas stream comprising liquid components, the separation unit (1) comprising a metallic tube (3) and a baffler (19), the metallic tube (3) having a first end (5) and a second end (7) and being closed at the first and second ends (5, 7), the baffler (19) being placed inside the metallic tube (3), the metallic tube (3) having a side feed (35) at the first end (5) and a gas outlet (13) at the second end (7). The invention further relates to the use of the separation unit and a process for determining the amount of liquid components in a two phase stream comprising a gaseous phase and liquid components.

Abstract: Disclosed herein is an apparatus and a method for catalytic conversion of chemical substances in the presence of pulverulent catalysts in a trickle bed reactor with residence times in the range of 0.1-10 seconds, wherein the apparatus includes a trickle bed reactor (2), the inlet side of which is functionally connected to a catalyst reservoir vessel (1) and a reactant feed, and the outlet side of which is functionally connected to a separator (3). The separator (3) has an exit conduit for leading off product stream, wherein the apparatus has the characteristic feature that the exit conduit disposed on the separator (3) for leading off product stream has a continuously acting valve connected via a controller to a pressure measurement sensor, wherein the continuously acting valve and the pressure measurement sensor form a pressure control circuit with a controller.

Abstract: The invention relates to an apparatus for analyzing reactions, comprising at least one reactor (1) and at least two sample vessels (13), wherein, in the case of an apparatus having one reactor (1), the reactor (1) is connected to at least two sample vessels (13), and, in the case of an apparatus having more than one reactor (1), each reactor (1) is connected to at least one sample vessel (13). The invention further relates to a method of analyzing reactions in such an apparatus.

Abstract: Disclosed herein is an apparatus and a method for catalytic conversion of chemical substances in the presence of pulverulent catalysts in a trickle bed reactor with residence times in the range of 0.1-10 seconds, wherein the apparatus includes a trickle bed reactor (2), the inlet side of which is functionally connected to a catalyst reservoir vessel (1) and a reactant feed, and the outlet side of which is functionally connected to a separator (3). The separator (3) has an exit conduit for leading off product stream, wherein the apparatus has the characteristic feature that the exit conduit disposed on the separator (3) for leading off product stream has a continuously acting valve connected via a controller to a pressure measurement sensor, wherein the continuously acting valve and the pressure measurement sensor form a pressure control circuit with a controller.

Abstract: An apparatus and process for spraying liquids and producing very fine mist with the apparatus, the apparatus including: a needle injector that includes a capillary line (1) and an outer tube (8); a liquid supply (5); and a gas supply (4), where: the capillary line (1) is arranged in the interior space of the outer tube (2); the internal diameter of the capillary line in the needle injector is in the range of 2-1000 ?m; the capillary line is in active communication with a gas supply (4); and the outer tube (2) is in active communication with a liquid supply (5).

Abstract: The invention relates to an apparatus and a process for spraying liquids and producing very fine mist, where the apparatus comprises a needle injector, a liquid supply (5) and a gas supply (4). The needle injector comprises at least one capillary line (1) and at least one outer tube (8), where the capillary line (1) is arranged in the interior space of the outer tube (2) and the internal diameter of the capillary line in the needle injector is in the range of 2-1000 ?m, preferably in the range of 4-300 ?m, more preferably in the range of 5-250 ?m. The capillary line is in active communication with a gas supply (4) and the outer tube (2) is in active communication with a liquid supply (5). A spray mist which comprises the liquid in the form of very finely dispersed droplets of 10-20 ?m and has a low flow velocity is produced by means of the process of the invention. The properties of the spray mist can be controlled very well via the configuration of the apparatus and the experimental parameters.

Abstract: The present invention provides a material library which comprises a plurality of different materials in spatial distribution in a three-dimensional substrate, in which the material composition continuously changes along a hypothetical spatial axis of the substrate and in this manner provides a three-dimensional material library. In addition, the present invention provides a process for producing continuous three-dimensional material libraries which comprise a plurality of different materials in a substrate, in which firstly a first substance is applied to a first surface of a substrate, then a second substance is applied to a second surface region of the substrate which is identical or different to the first surface region, in which then the substances are distributed in the interior of the substrate according to a predefined concentration gradient and then react with one another.