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Optimization of Protein Mixture Filtration

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F70883521%3A28110%2F19%3A63520654" target="_blank" >RIV/70883521:28110/19:63520654 - isvavai.cz</a>

  • Alternative codes found

    RIV/70883521:28140/19:63520654

  • Result on the web

    <a href="http://dx.doi.org/10.1007/978-3-319-97888-8_8" target="_blank" >http://dx.doi.org/10.1007/978-3-319-97888-8_8</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1007/978-3-319-97888-8_8" target="_blank" >10.1007/978-3-319-97888-8_8</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Optimization of Protein Mixture Filtration

  • Original language description

    In this paper there is described filtering process for separating reaction mix-ture after enzymatic hydrolysis to process the chromium tanning waste [1]. Filtration process of this mixture is very complicated because it is case of mixture filtration with compressible cake. Successful process strongly de-pends on mathematical describing of filtration, calculating optimal values of pressure difference, specific resistant of filtration cake and temperature maintenance which is connected with viscosity change. The mathematic model of filtration with compressible cake we verified in laboratory conditions on special filtration device developed on our department. Industrial filtration differs from that in laboratory merely in the quantity of material be-ing processed and in the necessity of processing it as cheaply as possible. In order to increase capacity while keeping filter dimensions not particularly large, the filter area per volume unit of plant gets increased as well as the difference between pressures before and behind the filtering screen or filter cake. A variety of different filter types are used and they depend on whether the particle content in liquid is low or high, whether the filter operates intermittently, semicontinously or continously, and on how the pressure difference is produced. Liquid flows through the cake and screen under the in-fluence of a difference between pressures before the cake and behind the screen. We solved problems connected with filtration of reaction mixture after enzymatic hydrolysis.

  • Czech name

  • Czech description

Classification

  • Type

    D - Article in proceedings

  • CEP classification

  • OECD FORD branch

    20402 - Chemical process engineering

Result continuities

  • Project

    Result was created during the realization of more than one project. More information in the Projects tab.

  • Continuities

    P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)<br>I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace

Others

  • Publication year

    2019

  • Confidentiality

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Data specific for result type

  • Article name in the collection

    Advances in Intelligent Systems and Computing, Volume 837

  • ISBN

    978-331997887-1

  • ISSN

    21945357

  • e-ISSN

    2194-5365

  • Number of pages

    11

  • Pages from-to

    93-103

  • Publisher name

    Springer Verlag

  • Place of publication

    Berlín

  • Event location

    Brno

  • Event date

    Jun 20, 2017

  • Type of event by nationality

    WRD - Celosvětová akce

  • UT code for WoS article