The invention relates to a continuously operating process for producing nitrobenzene, comprising the following steps: a) nitriding benzene in adiabatic conditions with sulfuric acid and nitric acid, using a stoichiometric excess of benzene in relation to the nitric acid, in multiple parallel reactors; b) first combining the raw process products of the nitridation from the parallel reactors to form a mixed flow in a device provided specifically for this purpose, then separating the mixed flow into a sulfuric acid phase and a nitrobenzene phase in a downstream phase separation apparatus; and c) processing the nitrobenzene phase, obtaining nitrobenzene. The invention also relates to a production plant suitable for carrying out the claimed process.

The invention relates to a continuously operating process for producing nitrobenzene, comprising the following steps: a) nitriding benzene in adiabatic conditions with sulfuric acid and nitric acid, using a stoichiometric excess of benzene in relation to the nitric acid, in multiple parallel reactors; b) first combining the raw process products of the nitridation from the parallel reactors to form a mixed flow in a device provided specifically for this purpose, then separating the mixed flow into a sulfuric acid phase and a nitrobenzene phase in a downstream phase separation apparatus; and c) processing the nitrobenzene phase, obtaining nitrobenzene. The invention also relates to a production plant suitable for carrying out the claimed process.

The invention relates to a continuously operating process for producing nitrobenzene, comprising the following steps: a) nitriding benzene in adiabatic conditions with sulfuric acid and nitric acid, using a stoichiometric excess of benzene in relation to the nitric acid, in multiple parallel reactors; b) first combining the raw process products of the nitridation from the parallel reactors to form a mixed flow in a device provided specifically for this purpose, then separating the mixed flow into a sulfuric acid phase and a nitrobenzene phase in a downstream phase separation apparatus; and c) processing the nitrobenzene phase, obtaining nitrobenzene. The invention also relates to a production plant suitable for carrying out the claimed process.

The present invention relates to processes of preparing N-((1,2,3,4,5,6,7-hexahydro-s-indacen-4-yl)carbamoyl)-1-iso-propyl-1H-pyrazole-3-sulfonamide and salts thereof. The present invention further relates to pharmaceutical compositions comprising such compounds and to the use of such compounds in the treatment and prevention of medical disorders and diseases, most especially by NLRP3 inhibition.

The present invention relates to processes of preparing N-((1,2,3,4,5,6,7-hexahydro-s-indacen-4-yl)carbamoyl)-1-iso-propyl-1H-pyrazole-3-sulfonamide and salts thereof. The present invention further relates to pharmaceutical compositions comprising such compounds and to the use of such compounds in the treatment and prevention of medical disorders and diseases, most especially by NLRP3 inhibition.

The present disclosure provides a method for preparing 2-ethyl-4-fluoro-1-nitrobenzene, including: (1) nitrifying 3-fluoroacetophenone with a nitration reagent, to obtain 1-(5-fluoro-2-nitrophenyl)ethanone; (2) reducing 1-(5-fluoro-2-nitrophenyl)ethanone with a reducing agent, to obtain 4-fluoro-2-(1-hydroxyethyl)-1-nitrobenzene; (3) iodinating 4-fluoro-2-(1-hydroxyethyl)-1-nitrobenzene, to obtain 4-fluoro-2-(1-iodoethyl)-1-nitrobenzene; and (4) reducing 4-fluoro-2-(1-iodoethyl)-1-nitrobenzene with a reducing agent, to obtain 2-ethyl-4-fluoro-1-nitrobenzene.

The present disclosure provides a method for preparing 2-ethyl-4-fluoro-1-nitrobenzene, including: (1) nitrifying 3-fluoroacetophenone with a nitration reagent, to obtain 1-(5-fluoro-2-nitrophenyl)ethanone; (2) reducing 1-(5-fluoro-2-nitrophenyl)ethanone with a reducing agent, to obtain 4-fluoro-2-(1-hydroxyethyl)-1-nitrobenzene; (3) iodinating 4-fluoro-2-(1-hydroxyethyl)-1-nitrobenzene, to obtain 4-fluoro-2-(1-iodoethyl)-1-nitrobenzene; and (4) reducing 4-fluoro-2-(1-iodoethyl)-1-nitrobenzene with a reducing agent, to obtain 2-ethyl-4-fluoro-1-nitrobenzene.

The present disclosure provides a method for preparing 2-ethyl-4-fluoro-1-nitrobenzene, including: (1) nitrifying 3-fluoroacetophenone with a nitration reagent, to obtain 1-(5-fluoro-2-nitrophenyl)ethanone; (2) reducing 1-(5-fluoro-2-nitrophenyl)ethanone with a reducing agent, to obtain 4-fluoro-2-(1-hydroxyethyl)-1-nitrobenzene; (3) iodinating 4-fluoro-2-(1-hydroxyethyl)-1-nitrobenzene, to obtain 4-fluoro-2-(1-iodoethyl)-1-nitrobenzene; and (4) reducing 4-fluoro-2-(1-iodoethyl)-1-nitrobenzene with a reducing agent, to obtain 2-ethyl-4-fluoro-1-nitrobenzene.

A method for continuously producing a product (A1) by way of at least two coupled-together chemical reactions (C1, C2), wherein at least two input substances (E1, E2) are fed to a first chemical reaction (C1), wherein a plurality of intermediate substances (Z1, Z2) are produced from the input substances (E1, E2) by the first chemical reaction (C1), wherein at least one of the intermediate substances (Z2) is fed to a second chemical reaction (C2), wherein the at least one fed intermediate substance (Z2) is further processed by the second chemical reaction (C2), in particular using at least one further substance (W1, W2) in a second chemical reaction (C2) to form a plurality of output substances (A1, A2), that is to say to form the chemical product (A1) and at least one further output substance (A2), wherein the flow rates (F.sub.i) of the fed substances (E1, E2, Z1, W1, W2, A2) that are fed to one of the reactions (C1, C2) are set by a respective actuating element (V.sub.E1, V.sub.E2, V.sub.W1, V.sub.W 2, V.sub.Z 2, V.sub.A1), wherein each of the fed substances is assigned a separate actuating element, wherein a manipulated variable (S.sub.E2,R, S.sub.i,R) that is stipulated by a controller (R.sub.E2, R.sub.i) is respectively applied to at least one of the actuating elements, wherein, for changing the production rate of the chemical product (A1), a temporary manipulated variable (S.sub.E2,temp, S.sub.i,temp) is respectively applied during a transient phase (II, III) to at least one of these actuating elements (V.sub.E2, V.sub.i) instead of the manipulated variables (S.sub.E2, R, S.sub.i,R) stipulated by the respective controllers (R.sub.E2, R.sub.i), wherein the temporary manipulated variable (S.sub.E2,temp, S.sub.i,temp) or the temporary manipulated variables is/are generated by at least one control unit (SE) in dependence on a default value (NV).

A method for continuously producing a product (A1) by way of at least two coupled-together chemical reactions (C1, C2), wherein at least two input substances (E1, E2) are fed to a first chemical reaction (C1), wherein a plurality of intermediate substances (Z1, Z2) are produced from the input substances (E1, E2) by the first chemical reaction (C1), wherein at least one of the intermediate substances (Z2) is fed to a second chemical reaction (C2), wherein the at least one fed intermediate substance (Z2) is further processed by the second chemical reaction (C2), in particular using at least one further substance (W1, W2) in a second chemical reaction (C2) to form a plurality of output substances (A1, A2), that is to say to form the chemical product (A1) and at least one further output substance (A2), wherein the flow rates (F.sub.i) of the fed substances (E1, E2, Z1, W1, W2, A2) that are fed to one of the reactions (C1, C2) are set by a respective actuating element (V.sub.E1, V.sub.E2, V.sub.W1, V.sub.W 2, V.sub.Z 2, V.sub.A1), wherein each of the fed substances is assigned a separate actuating element, wherein a manipulated variable (S.sub.E2,R, S.sub.i,R) that is stipulated by a controller (R.sub.E2, R.sub.i) is respectively applied to at least one of the actuating elements, wherein, for changing the production rate of the chemical product (A1), a temporary manipulated variable (S.sub.E2,temp, S.sub.i,temp) is respectively applied during a transient phase (II, III) to at least one of these actuating elements (V.sub.E2, V.sub.i) instead of the manipulated variables (S.sub.E2, R, S.sub.i,R) stipulated by the respective controllers (R.sub.E2, R.sub.i), wherein the temporary manipulated variable (S.sub.E2,temp, S.sub.i,temp) or the temporary manipulated variables is/are generated by at least one control unit (SE) in dependence on a default value (NV).