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    Wyświetlanie 1-4 z 4
    Tytuł:
    Test Reactions To Study Efficiency Of Mixing
    Autorzy:
    Jasińska, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/185281.pdf
    Data publikacji:
    2015
    Wydawca:
    Polska Akademia Nauk. Czytelnia Czasopism PAN
    Tematy:
    micromixing
    efficiency of mixing
    IEM model
    engulfment model
    chemical test
    reactions
    mikromieszanie
    wydajność mieszania
    model IEM
    model zatopienia
    test chemiczny
    Opis:
    Effects of mixing on the course of fast chemical reactions are relatively well understood, especially in homogeneous systems. This enables to design and operate chemical reactors with the goal to achieve a high yield of a desired product and use systems of complex reactions as a chemical probe (chemical test reactions) to identify progress of mixing and quality of mixture. Recently, a number of studies have focused on the application of chemical test reactions to identify energy efficiency of mixing, being a convenient way of comparing mixers and reactors in terms of their mixing efficiency. This review offers a presentation of chemical test reactions available in the literature and methods of applications of test reactions to identify the energy efficiency of mixing. Also methods to assess the extent of micromixing by measuring product distribution or segregation index, and to determine the time constant for mixing are presented for single phase homogeneous systems and two-phase liquid-liquid systems.
    Źródło:
    Chemical and Process Engineering; 2015, 36, 2; 171-208
    0208-6425
    2300-1925
    Pojawia się w:
    Chemical and Process Engineering
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Energetic Efficiency of Mixing and Mass Transfer in Single Phase and Two-Phase Systems
    Autorzy:
    Bałdyga, J.
    Jasińska, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/184853.pdf
    Data publikacji:
    2017
    Wydawca:
    Polska Akademia Nauk. Czytelnia Czasopism PAN
    Tematy:
    chemical test reaction
    energetic efficiency
    mass transfer
    mixing
    chemiczne reakcje testowe
    wydajność energetyczna
    transfer masy
    mieszanie
    Opis:
    In this work a concept of energetic efficiency of mixing is presented and discussed; a classical definition of mixing efficiency is modified to include effects of the Schmidt number and the Reynolds number. Generalization to turbulent flows is presented as well. It is shown how the energetic efficiency of mixing as well as efficiencies of drop breakage and mass transfer in twophase liquid-liquid systems can be identified using mathematical models and test chemical reactions. New expressions for analyzing efficiency problem are applied to identify the energetic efficiency of mixing in a stirred tank, a rotor stator mixer and a microreactor. Published experimental data and new results obtained using new systems of test reactions are applied. It has been shown that the efficiency of mixing is small in popular types of reactors and mixers and thus there is some space for improvement.
    Źródło:
    Chemical and Process Engineering; 2017, 38, 1; 79-96
    0208-6425
    2300-1925
    Pojawia się w:
    Chemical and Process Engineering
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Energetic efficiency of mass transfer accompanied by chemical reactions in liquid-liquid systems
    Autorzy:
    Jasińska, M.
    Bałdyga, J.
    Powiązania:
    https://bibliotekanauki.pl/articles/185369.pdf
    Data publikacji:
    2017
    Wydawca:
    Polska Akademia Nauk. Czytelnia Czasopism PAN
    Tematy:
    chemical test reactions
    energetic efficiency of mixing
    mass transfer\liquid-liquid
    system
    rotor-stator mixer
    chemiczne reakcje testowe
    efektywność energetyczna mieszania
    przeniesienie masy
    ciecz
    Opis:
    Energetic efficiency depicting the fraction of energy dissipation rate used to perform processes of drop breakup and mass transfer in two-phase, liquid-liquid systems is considered. Results of experiments carried out earlier in two types of high-shear mixers: an in-line rotor-stator mixer and a batch rotor-stator mixer, have been applied to identify and compare the efficiency of drop breakage and mass transfer in both types of mixers. The applied method is based on experimental determination of both: the product distribution of chemical test reactions and the drop size distributions. Experimental data are interpreted using a multifractal model of turbulence for drop breakage and the model by Favelukis and Lavrenteva for mass transfer. Results show that the energetic efficiency of the in-line mixer is higher than that of the batch mixer; two stator geometries were considered in the case of the batch mixer and the energetic efficiency of the device equipped with a standard emulsor screen (SES) was higher than the efficiency of the mixer equipped with a general purpose disintegrating head (GPDH) for drop breakup but smaller for mass transfer.
    Źródło:
    Chemical and Process Engineering; 2017, 38, 3; 433-444
    0208-6425
    2300-1925
    Pojawia się w:
    Chemical and Process Engineering
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Effect of sonication reactor geometry on cell disruption and protein release from yeast cells
    Autorzy:
    Bałdyga, J.
    Jasińska, M.
    Dzięgielewska, M.
    Żochowska, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/950394.pdf
    Data publikacji:
    2018
    Wydawca:
    Polska Akademia Nauk. Czytelnia Czasopism PAN
    Tematy:
    cell disruption
    protein release
    Saccharomyces cerevisiae ultrasonication yeast
    dezintegracja komórek
    uwalnianie białka
    drożdże
    Opis:
    The measured rate of release of intercellular protein from yeast cells by ultrasonication was applied for evaluating the effects of sonication reactor geometry on cell disruption rate and for validation of the simulation method. Disintegration of two strains of Saccharomyces cerevisiae has been investigated experimentally using a batch sonication reactor equipped with a horn type sonicator and an ultrasonic processor operating at the ultrasound frequency of 20 kHz. The results have shown that the rate of release of protein is directly proportional to the frequency of the emitter surface and the square of the amplitude of oscillations and strongly depends on the sonication reactor geometry. The model based on the Helmholtz equation has been used to predict spatial distribution of acoustic pressure in the sonication reactor. Effects of suspension volume, horn tip position, vessel diameter and amplitude of ultrasound waves on the spatial distribution of pressure amplitude have been simulated. A strong correlation between the rate of protein release and the magnitude of acoustic pressure and its spatial distribution has been observed. This shows that modeling of acoustic pressure is useful for optimization of sonication reactor geometry.
    Źródło:
    Chemical and Process Engineering; 2018, 39, 4; 475--489
    0208-6425
    2300-1925
    Pojawia się w:
    Chemical and Process Engineering
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
      Wyświetlanie 1-4 z 4

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