Comparison between Acrylic‐Polyurethane Hybrid Emulsions and Physical Blends

Identifieur interne : 001930 ( Main/Exploration ); précédent : 001929; suivant : 001931

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Comparison between Acrylic‐Polyurethane Hybrid Emulsions and Physical Blends

Auteurs : Dolores Kukanja [Slovénie] ; Matjaž Krajnc [Slovénie] ; Janvit Golob [Slovénie]

Source :

• Chemie Ingenieur Technik [ 0009-286X ] ; 2001-06.

RBID : ISTEX:5B012A7804F9D2FAAD4E3A63D5C7E92BDB36FE32

Descripteurs français

• Wicri :
  • geographic : Pays-Bas, Ukraine.
  • topic : Acide, Industrie chimique, Matériau composite, Distillation, éthanol, Industrie alimentaire, Projet d'investissement, Industrie mécanique, Méthanol, Polluant, Polymère, Prague, Simulation.

English descriptors

• KwdEn :
  • Absorption liquids, Absorption process, Absorption systems, Acetic acid, Acid, Adsorbent, Adsorption, Adsorptive reactors, Aerodynamic characteristics, Amino groups, Amsterdam, Annular flow, Aqueous alkanolamine solutions, Aston university, Behaviour, Best results, Better understanding, Bidisperse bubble swarms, Binary mixtures, Biochemical engineering, Bioprocess technology, Boreskov institute, Bubble, Bubble column, Bubble columns, Bubble size, Bubble size distribution, Bubbly flow, Carbon fibres, Catalyst, Catalytic, Catalytic distillation column, Catalytic packings, Caustic soda, Ceramic filters, Characterisation, Characterisation method, Chemical engineering, Chemical engineering department, Chemical equilibrium, Chemical industry, Chemical reaction, Chemical reactions, Chemical technology, Chemie, Chemie ingenieur technik, Chemische verfahrenstechnik, Chimique, Chromatographic, Chromatographic reactor, Chromatographic reactors, Chromatographic separation, Coalescence, Coalescence rates, Column internals, Common configuration, Composite materials, Composite sorbent, Computational fluid dynamics, Concentration profiles, Conventional reactor, Copper cations, Corresponding author, Couette device, Czech, Czech republic, Delft, Delft university, Design problem, Different types, Diffusion electrodes, Dioxide, Distillation, Dortmund, Dortmund university, Double layers, Droplet, Droplet separation kinetics, Dynamik komplexer technischer, Dynamik komplexer technischer systeme, Electric field, Electrical resistance, Electrochemical, Electrochemical application, Electrochemical detoxification, Electrochemical tracer method, Electrode, Electrodeposition potentials, Electrodialysis, Electrolyte, Electrophoretic separation process, Emulsion, Environmental engineering, Environmental process engineering, Environmental technology, Equilibrium conversion, Esterification, Esterification reaction, Ethanol, Eulerian approach, Experimental data, Experimental results, Experimental study, Experimental techniques, Fibre, Finite kinetics, First step, Flow behaviour, Flow pattern, Flow rate, Flow rates, Flow regime, Flow regimes, Flow visualisation, Food industry, Future challenges, Genie, Genie chimique, Glass beads, Glassy carbon electrode, Gmbh, Harting institut, Heat transfer, Heavy metals, Heyrovsky institute, High intensity, High purity hydrochloric acid, Hollow spray apparatus, Hybrid emulsions, Hydrodynamics, Hydrogen peroxide, Industrial plants, Ingenieur, Inorganic chemistry, Inorganic technology, Institut, Internals, Investment project, Ismr2, Karlsruhe, Kiev, Kiev polytechnic institute, Kinetic parameters, Kinetics, Krishna department, Laboratoire, Lauric acid, Lehrstuhl, Leipziger, Limestone suspension, Liquid circulation, Liquid phase, Liquid phase mass transfer, Liquid phases, Local effects, Magdeburg, Magnetic resonance imaging, Mass balances, Mass exchange ability, Mass transfer, Mass transfer area, Mass transfer rate, Mathematical model, Measurement techniques, Mechanical engineering, Mechanical process engineering, Mechanical properties, Mechanische verfahrenstechnik, Membrane, Membrane contactors, Membrane performance, Membrane reactor, Membrane reactor configuration, Membrane reactors, Methanol, Model catalyst, Modeling, Modelling, Molten carbonate fuel cell, Monolithic reactor, Multifunctional, Multifunctional reactor, Multiphase, Multiphase flows, Multiphase reactors, Multiphase systems, Multiphase systems figure, Multiple emulsions, Netherlands, Nichtklassische chemie, Nieuwe achtergracht, Nieuwe acthergracht, Nitrogen oxide absorption, Notre dame, Novel process, Numerical effort, Organic acids, Oxidative dehydrogenation, Parameter, Parametric sensitivity analysis, Peroxide, Pervaporation separation properties, Pfaffenwaldring stuttgart, Physical chemistry, Physical properties, Plant design, Pollutant, Polymer, Polymeric coating, Polyurethane dispersion, Polyvinyl particles, Pore, Pore size, Porous membrane, Prague, Preparation conditions, Pressure drop, Primary particles, Process conditions, Process design, Process engineers, Process intensification, Process technology, Production process, Prospekt palladina, Reactant, Reaction rate, Reaction time, Reaction zone, Reactive, Reactive distillation, Reactive distillation column, Reactive distillation process, Reactive separations, Reactor, Reactor concepts, Reactor performance, Relative velocity, Residence time, Rheological, Rheological behaviour, Rotational viscometer, Rwth aachen, Safety relief valves, Safety valve, Selectivity, Separation efficiency, Separation factor, Shear stress, Simulation, Single fractures, Size distribution, Small bubbles, Solar collectors, Solar gains, Solid oxygen carrier, Solid particles, Solid phase, Solubility, Steady state, Stuttgart, Sulfur dioxide, Sulfuric, Sulfuric acid, Supercritical fluids, Technical university, Technik, Technische thermodynamik, Temperature profile, Temperature range, Thermal behaviour, Thermische verfahrenstechnik, Thermodynamic equilibrium, Toulouse cedex, Tubular reactors, Ukraine, Universitat, Universitat kaiserslautern, Universitat karlsruhe, Universitat leipzig, Universitat stuttgart, Universite paul sabatier, Verfahrenstechnik, Void fraction, Wide range, Zeolite.
• Teeft :
  • Absorption liquids, Absorption process, Absorption systems, Acetic acid, Acid, Adsorbent, Adsorption, Adsorptive reactors, Aerodynamic characteristics, Amino groups, Amsterdam, Annular flow, Aqueous alkanolamine solutions, Aston university, Behaviour, Best results, Better understanding, Bidisperse bubble swarms, Binary mixtures, Biochemical engineering, Bioprocess technology, Boreskov institute, Bubble, Bubble column, Bubble columns, Bubble size, Bubble size distribution, Bubbly flow, Carbon fibres, Catalyst, Catalytic, Catalytic distillation column, Catalytic packings, Caustic soda, Ceramic filters, Characterisation, Characterisation method, Chemical engineering, Chemical engineering department, Chemical equilibrium, Chemical industry, Chemical reaction, Chemical reactions, Chemical technology, Chemie, Chemie ingenieur technik, Chemische verfahrenstechnik, Chimique, Chromatographic, Chromatographic reactor, Chromatographic reactors, Chromatographic separation, Coalescence, Coalescence rates, Column internals, Common configuration, Composite materials, Composite sorbent, Computational fluid dynamics, Concentration profiles, Conventional reactor, Copper cations, Corresponding author, Couette device, Czech, Czech republic, Delft, Delft university, Design problem, Different types, Diffusion electrodes, Dioxide, Distillation, Dortmund, Dortmund university, Double layers, Droplet, Droplet separation kinetics, Dynamik komplexer technischer, Dynamik komplexer technischer systeme, Electric field, Electrical resistance, Electrochemical, Electrochemical application, Electrochemical detoxification, Electrochemical tracer method, Electrode, Electrodeposition potentials, Electrodialysis, Electrolyte, Electrophoretic separation process, Emulsion, Environmental engineering, Environmental process engineering, Environmental technology, Equilibrium conversion, Esterification, Esterification reaction, Ethanol, Eulerian approach, Experimental data, Experimental results, Experimental study, Experimental techniques, Fibre, Finite kinetics, First step, Flow behaviour, Flow pattern, Flow rate, Flow rates, Flow regime, Flow regimes, Flow visualisation, Food industry, Future challenges, Genie, Genie chimique, Glass beads, Glassy carbon electrode, Gmbh, Harting institut, Heat transfer, Heavy metals, Heyrovsky institute, High intensity, High purity hydrochloric acid, Hollow spray apparatus, Hybrid emulsions, Hydrodynamics, Hydrogen peroxide, Industrial plants, Ingenieur, Inorganic chemistry, Inorganic technology, Institut, Internals, Investment project, Ismr2, Karlsruhe, Kiev, Kiev polytechnic institute, Kinetic parameters, Kinetics, Krishna department, Laboratoire, Lauric acid, Lehrstuhl, Leipziger, Limestone suspension, Liquid circulation, Liquid phase, Liquid phase mass transfer, Liquid phases, Local effects, Magdeburg, Magnetic resonance imaging, Mass balances, Mass exchange ability, Mass transfer, Mass transfer area, Mass transfer rate, Mathematical model, Measurement techniques, Mechanical engineering, Mechanical process engineering, Mechanical properties, Mechanische verfahrenstechnik, Membrane, Membrane contactors, Membrane performance, Membrane reactor, Membrane reactor configuration, Membrane reactors, Methanol, Model catalyst, Modeling, Modelling, Molten carbonate fuel cell, Monolithic reactor, Multifunctional, Multifunctional reactor, Multiphase, Multiphase flows, Multiphase reactors, Multiphase systems, Multiphase systems figure, Multiple emulsions, Netherlands, Nichtklassische chemie, Nieuwe achtergracht, Nieuwe acthergracht, Nitrogen oxide absorption, Notre dame, Novel process, Numerical effort, Organic acids, Oxidative dehydrogenation, Parameter, Parametric sensitivity analysis, Peroxide, Pervaporation separation properties, Pfaffenwaldring stuttgart, Physical chemistry, Physical properties, Plant design, Pollutant, Polymer, Polymeric coating, Polyurethane dispersion, Polyvinyl particles, Pore, Pore size, Porous membrane, Prague, Preparation conditions, Pressure drop, Primary particles, Process conditions, Process design, Process engineers, Process intensification, Process technology, Production process, Prospekt palladina, Reactant, Reaction rate, Reaction time, Reaction zone, Reactive, Reactive distillation, Reactive distillation column, Reactive distillation process, Reactive separations, Reactor, Reactor concepts, Reactor performance, Relative velocity, Residence time, Rheological, Rheological behaviour, Rotational viscometer, Rwth aachen, Safety relief valves, Safety valve, Selectivity, Separation efficiency, Separation factor, Shear stress, Simulation, Single fractures, Size distribution, Small bubbles, Solar collectors, Solar gains, Solid oxygen carrier, Solid particles, Solid phase, Solubility, Steady state, Stuttgart, Sulfur dioxide, Sulfuric, Sulfuric acid, Supercritical fluids, Technical university, Technik, Technische thermodynamik, Temperature profile, Temperature range, Thermal behaviour, Thermische verfahrenstechnik, Thermodynamic equilibrium, Toulouse cedex, Tubular reactors, Ukraine, Universitat, Universitat kaiserslautern, Universitat karlsruhe, Universitat leipzig, Universitat stuttgart, Universite paul sabatier, Verfahrenstechnik, Void fraction, Wide range, Zeolite.

Url:

• https://api.istex.fr/document/5B012A7804F9D2FAAD4E3A63D5C7E92BDB36FE32/fulltext/pdf

DOI: 10.1002/1522-2640(200106)73:6<743::AID-CITE7432222>3.0.CO;2-K

Affiliations:

• Slovénie

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