Patent classifications
B01J2219/00191
DEVICES, SYSTEMS AND METHODS FOR AUTOMATIC EXTRACTION, STORAGE AND ENCAPSULATION OF FATTY COMPOUNDS
A device for automatic extraction, storage and encapsulation of fatty compounds, the device may include: an extraction unit configured to provide a liquid mixture comprising fatty compounds extracted from biological material and a liquid solvent; an evaporation and reaction unit; a storage unit comprising one or more storage outlet ports; and a controller configured to: control delivery of the liquid mixture from the extraction unit to the evaporation and reaction unit; control evaporation of the solvent from the liquid mixture in the evaporation and reaction unit; control delivery of the liquid mixture from the evaporation and reaction unit to the storage unit; detect safe connection of each of at least one of one or more capsules to one of the one or more storage outlet ports of the storage unit; and control filling of at least one of the one or more connected capsules with the liquid mixture.
LEARNING APPARATUS, OPERATION METHOD OF LEARNING APPARATUS, OPERATION PROGRAM OF LEARNING APPARATUS, AND OPERATING APPARATUS
There are provided a learning apparatus, an operation method of the learning apparatus, an operation program of the learning apparatus, and an operating apparatus capable of further improving accuracy of prediction of a quality of a product by a machine learning model in a case where learning is performed by inputting, as learning input data, multi-dimensional physical-property relevance data, which is derived from multi-dimensional physical-property data of the product, to the machine learning model. In the learning apparatus, a first processor derives, as learning input data, multi-dimensional physical-property relevance data which is related to multi-dimensional physical-property data. A first processor inputs the learning input data to the machine learning model, performs learning, and outputs the machine learning model as a learned model to be provided for actual operation.
FLOW REACTION FACILITY AND FLOW REACTION METHOD
A flow reaction facility 10 includes a reaction section 23, a collecting section 26, a system controller 15, a first flow velocimeter to a third flow velocimeter 35a to 35c, a thermometer 35d, and a soft sensor 38. The first flow velocimeter to the third flow velocimeter 35a to 35c and the thermometer 35d detect reaction conditions in the reaction section 23, and output the detected reaction conditions as detection information. The soft sensor 38 applies the above detection information to a prediction function generated in advance using measurement data, and calculates a reaction result in the reaction section 23 as an arithmetic reaction result. The system controller 15 controls the reaction section 23 on the basis of the arithmetic reaction result.
FLOW REACTION SUPPORT APPARATUS, FLOW REACTION SUPPORT METHOD, FLOW REACTION FACILITY, AND FLOW REACTION METHOD
A flow reaction support apparatus includes a computing section and a determination section. The computing section generates a prediction data set by calculating a prediction result for each reaction condition whose reaction result is unknown, using measurement data. The computing section extracts the reaction condition of the prediction result closest to a target result as an extracted reaction condition. The determination section determines whether or not a difference between the reaction result under the extracted reaction condition and the prediction result is within an allowable range, and adds, in a case where the difference is not within the allowable range, reaction information in which the extracted reaction condition and the reaction result are associated with each other to the measurement data.
Slurry Loop Reactor Polymerization Rate and Quality Controller
A process and system for maintaining optimum polymerization production in a loop polymerization reactor by continuously and periodically obtaining polymerization results, such as melt index (MI), production rate and ash content of the polymer produced, determining whether each of the results is within desired ranges, storing and averaging recently obtained results in a database within a reaction rate controller program, and when one of the results is out of the desired range modifying at least one reaction parameter set-point such as monomer concentration, catalyst feed rate and reactor temperature to drive any out-of-range polymerization result(s) toward the desired range for that result.
METHOD FOR CONTINUOUSLY PRODUCING A PRODUCT BY WAY OF AT LEAST TWO COUPLED-TOGETHER CHEMICAL REACTIONS
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).
Augmented reality procedural system
An augmented reality device is provided to assist users in performing new or unfamiliar experimental techniques, identify materials and products utilized in a documented action set and within a work environment, identify equipment and instruments needed in the documented action set and within the work environment, assist in performing single person (autonomous) work, collaborate with other workers, and record data and observations in an electronic laboratory notebook.
Method for continuously producing a product by way of at least two coupled-together chemical reactions
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).
Automated purification and formulation device for radiopharmaceutical compounds
A device for purifying and formulating a radiopharmaceutical compound includes an automated purification subsystem that automates the loading of a sample into a sample loop for downstream purification via HPLC. A column selector valve is provided to select from one of a plurality of columns. Fractions can be collected as well as the desired product. The device includes an automated formulation subsystem that first sends the product to a dilution reservoir prior to being pneumatically pushed onto a solid phase extraction (SPE) cartridge. Automated rinse, elution, and reconstitution are also performed with the automated formulation subsystem. The device may be directly coupled to the output of an automated radiosynthesizer.
Method for evaluating lifting force in a heat exchanger
A method and a control unit for evaluating lifting force of a gas phase of a substantially vertical upward two-phase flow of a first fluid in a heat exchanger. The first fluid comprises the gas phase and a liquid phase. The method comprises determining that the lifting force of the gas phase is insufficient for lifting the liquid phase based on hot end approach of the heat exchanger and/or on pressure drop of the first fluid over the heat exchanger. The control unit is configured to determine that the lifting force of the gas phase is insufficient for lifting the liquid phase based on hot end approach of the heat exchanger and/or on pressure drop of the first fluid over the heat exchanger. A heat exchanger assembly comprising a heat exchanger and the control unit.