Abstract: The invention relates to a method for transferring a target substance (5), particularly a target molecule (5), between two liquid phases (4, 6; 6, 8; 6, 11), of which at least one phase (4, 6) comprises the target substance (5) to be transferred and at least one phase (4, 8, 11) is an aqueous phase, where at least the aqueous phase (4, 8, 11) is arranged in one of two electrode chambers (1a, 1b, 10a, 10b) which are electroconductively connected, preferably by charge carrier exchange, and separated in terms of the volumes thereof, preferably where the phases (4, 6; 6, 8; 6, 11) are arranged together in one of two electrode chambers (1a, 1b, 10a, 10b) which are electroconductively connected and separated in terms of the volumes thereof, and a pH-value modification is generated by the H and/or OH ions created during the electrolysis in the aqueous phase (4, 8, 11), said modification initiating a transfer process of the target substance (5) between the phases (4, 6; 6, 8; 6, 11).

Abstract: An integrated process for the solution polymerization and subsequent halogenation of butyl rubber in a common medium is disclosed. The process comprises providing a solution polymerization reactor containing a C6 medium mixed with a monomer mixture comprising at least an isoolefin monomer and a multiolefin monomer in a mass ratio of monomer mixture to medium of from 61:39 to 80:20. Once polymerized, residual unreacted monomer mixture is separated from the rubber solution using a distillation process. The residual monomers may then be purified and recycled back into the reactor. The separated rubber solution is then halogenated. The process obviates the need for separating the rubber from the medium following polymerization, then re-dissolving it in another solvent for halogenation, thereby saving energy cost. The process optionally employs heat exchangers for the reactor feed streams to further reduce energy consumption.

Abstract: A computer-implemented method for monitoring and analyzing energy consumption of a chemical plant in operation. Plant type specific theoretical energy consumption optimum value based on a corresponding modeled plant are determined, parameters contributing to increased energy consumption are identified and grouped. Energy consumption of a plant is periodically graphed starting from the theoretical energy consumption optimum value and getting up as an energy cascade to a current energy consumption, by adding the provided, partly retrieved single energy consumption rates of the respective parameters in groups such that the resulting energy cascade allows to monitor at least a part of the individual parameters and to automatically compare the current energy consumption of the at least one plant with an energy consumption of another plant and/or with a previous energy consumption of the at least one plant with respect to the individual parameters. Furthermore, an appropriate system is provided.

Abstract: A computer-implemented method for monitoring and analyzing energy consumption of at least one industrial building is provided, the method comprising determining a building type specific theoretical energy consumption optimum value (TEO) based on a corresponding modeled building, identifying and grouping parameters contributing to an increased energy consumption of the building due to an actual use of the building (CEC), due to intrinsic characteristics of the building (BEO), due to optimised designated operating conditions in an actual state of the building (OEO), respectively, providing energy contribution rates of the respective parameters, partly by an automatic, and whenever required, periodic retrieval, and periodically graphing the energy consumption of the at least one building via a bar graph starting from the building type specific theoretical energy consumption optimum value and arriving at a current energy consumption of the at least one building by adding the provided single energy consumption rat

Abstract: An integrated process for the solution polymerization and subsequent halogenation of butyl rubber in a common medium is disclosed. The process comprises providing a solution polymerization reactor containing a C6 medium mixed with a monomer mixture comprising at least an isoolefin monomer and a multiolefin monomer in a mass ratio of monomer mixture to medium of from 61:39 to 80:20. Once polymerized, residual unreacted monomer mixture is separated from the rubber solution using a distillation process. The residual monomers may then be purified and recycled back into the reactor. The separated rubber solution is then halogenated. The process obviates the need for separating the rubber from the medium following polymerization, then re-dissolving it in another solvent for halogenation, thereby saving energy cost. The process optionally employs heat exchangers for the reactor feed streams to further reduce energy consumption.

Abstract: The present disclosure refers to a computer-implemented method for monitoring and analyzing energy consumption of at least one operated chemical plant, the method comprising determining a plant type specific theoretical energy consumption optimum value based on a corresponding modeled plant, identifying and grouping parameters contributing to an increased energy consumption of the plant due to processes running on the plant, due to internal characteristics of the plant, due to operating conditions of the plant, respectively, providing, such as partly automatically retrieving energy contribution rates of the respective parameters, and periodically graphing the energy consumption of the at least one plant via a bar graph starting from the theoretical energy consumption optimum value and getting up as an energy cascade to a current energy consumption of the at least one plant by adding the provided, partly retrieved single energy consumption rates of the respective parameters in groups such that the resulting en