The present invention is directed to analytical methods for determining the concentration, and/or stereoisomeric excess, and/or absolute configuration of chiral analytes in a sample.

The present invention is directed to analytical methods for determining the concentration, and/or stereoisomeric excess, and/or absolute configuration of chiral analytes in a sample.

The present invention relates to a method of catalytic process characterization which comprises a reaction system having two or more reaction strands in a parallel arrangement, wherein an individual reaction strand comprises multiple series-connected reaction chambers or a single reaction chamber. In the method, which is also referred to as CPC method, each reaction strand is supplied with a reactant stream. The reactant streams supplied to the reaction strands are subjected to different numbers of process stages in the different reaction strands. The product streams discharged from the reaction strands are subjected to an analytical characterization, wherein the data achieved in the characterization are expressed in relative terms, here preferably including the forming of a difference. The CPC method can be used in a very versatile manner and is characterized by very high accuracy. The mass balance achieves a standard deviation of +/10% by weight or lower. Furthermore, the invention relates to an apparatus for performing the CPC method or else to an apparatus for simultaneously performing a multitude of CPC methods. The invention thus also relates to the field of high-throughput research.

The present invention relates to a method of catalytic process characterization which comprises a reaction system having two or more reaction strands in a parallel arrangement, wherein an individual reaction strand comprises multiple series-connected reaction chambers or a single reaction chamber. In the method, which is also referred to as CPC method, each reaction strand is supplied with a reactant stream. The reactant streams supplied to the reaction strands are subjected to different numbers of process stages in the different reaction strands. The product streams discharged from the reaction strands are subjected to an analytical characterization, wherein the data achieved in the characterization are expressed in relative terms, here preferably including the forming of a difference. The CPC method can be used in a very versatile manner and is characterized by very high accuracy. The mass balance achieves a standard deviation of +/10% by weight or lower. Furthermore, the invention relates to an apparatus for performing the CPC method or else to an apparatus for simultaneously performing a multitude of CPC methods. The invention thus also relates to the field of high-throughput research.

The present invention is directed to analytical methods for determining the concentration, and/or stereoisomeric excess, and/or absolute configuration of chiral analytes in a sample.

The present invention is directed to analytical methods for determining the concentration, and/or stereoisomeric excess, and/or absolute configuration of chiral analytes in a sample.

An apparatus for collecting helium gas includes: a first receptacle having a first flexible membrane for receiving a gas containing helium, the first receptacle being selectively couplable to an inlet of the apparatus; a second receptacle having a second flexible membrane for receiving the gas containing helium, the second receptacle being selectively couplable to the inlet of the apparatus; a pump having an inlet selectively couplable to an outlet of the first receptacle and selectively couplable to an outlet of the second receptacle; a purifier having an inlet couplable to an outlet of the pump; and an outlet of the apparatus couplable to an outlet of the purifier. A method of collecting and reusing helium gas is also described. Other valuable and/or rare gases may be recovered and reused.

An apparatus for collecting helium gas includes: a first receptacle having a first flexible membrane for receiving a gas containing helium, the first receptacle being selectively couplable to an inlet of the apparatus; a second receptacle having a second flexible membrane for receiving the gas containing helium, the second receptacle being selectively couplable to the inlet of the apparatus; a pump having an inlet selectively couplable to an outlet of the first receptacle and selectively couplable to an outlet of the second receptacle; a purifier having an inlet couplable to an outlet of the pump; and an outlet of the apparatus couplable to an outlet of the purifier. A method of collecting and reusing helium gas is also described. Other valuable and/or rare gases may be recovered and reused.

An apparatus and a method are used for investigating the naphtha reforming process in catalyst test devices with reactors arranged in parallel. The apparatus has a plurality of reactors arranged in parallel with reaction chambers (R1, R2, . . . ), a product fluid supply, a process control, and at least one analysis unit. Each individual reactor has an outlet line for the product fluid stream, wherein the analysis unit is operatively connected to each outlet line for the product fluid stream and the apparatus is functionally connected to the control of the apparatus. In carrying out the method, naphtha-containing reactant fluid streams are brought into contact with catalysts in the individual reactors and the product fluid streams are subsequently supplied to the online analysis unit from the respective outlet lines of the individual reactors and analyzed. Using the evaluation of the online analytical characterization data, the process parameters of the respective reactor unit are adapted. The process steps of analytical characterization, evaluation, and adaptation of process parameters are repeated for the duration of the investigation.

An apparatus and a method are used for investigating the naphtha reforming process in catalyst test devices with reactors arranged in parallel. The apparatus has a plurality of reactors arranged in parallel with reaction chambers (R1, R2, . . . ), a product fluid supply, a process control, and at least one analysis unit. Each individual reactor has an outlet line for the product fluid stream, wherein the analysis unit is operatively connected to each outlet line for the product fluid stream and the apparatus is functionally connected to the control of the apparatus. In carrying out the method, naphtha-containing reactant fluid streams are brought into contact with catalysts in the individual reactors and the product fluid streams are subsequently supplied to the online analysis unit from the respective outlet lines of the individual reactors and analyzed. Using the evaluation of the online analytical characterization data, the process parameters of the respective reactor unit are adapted. The process steps of analytical characterization, evaluation, and adaptation of process parameters are repeated for the duration of the investigation.