Secondary abstract: |
Increased demand on kefir grains, as key component in many commerciallyvisional industrial applications, either in food or biochemical processing, requires improvement of existent batch and simultaneously intensive development of new economically efficient continuous grains production plants with higher capacity. Accordingly, the technological innovations on the field of reactor systems for kefir grains production are the key issue. This doctoral dissertation describes an innovative design of continuous reactor systems for traditional kefir grains production with cultivation in milk. The main goal of the dissertation was to determine the optimal volumes of reactors in one-, twoor multi-stage reactor systems. For this purpose a new complex mathematical expressions and non-linear programming(NLP) problem for estimating the optimal volumes of reactors at different conversions with regard to pH value of fermentation media and kefir grains production capacities have been developed. Among one-stage reactor systems, the continuously stirred tank reactor (CSTR) and plug flow reactor (PFR) have been analyzed. Moreover, among two- or multi-stage systems, the cascades of CSTR and PFR, two CSTRs and N CSTRs have been examined. In doctoral dissertation, a so-called threedimensional predictive (TDP) model, presenting explicit mathematical formulation for calculating the optimal volume of j-th reactor in cascade of N CSTRs, has also been developed and validated. TDP model simplifies the complex non-linear problem of estimating the optimal CSTRs volumes in different reactor systems and therefore presents efficient and simultaneously user friendly alternative technological tool. Up to date, no scientific studies concerning the dissertation topic have been published. Therefore, the new approach for development of reactor systems for kefir grains production, which is based on so-called structured and experimentally supported design methodology, has been proposed. Summarily, thenew models or methods for estimating the optimal volumes of continuous reactors, which consider unique kefir grains characteristics, have been developed by integrated usage of results of preliminary research and growth curve modeling. Consequently, in extended context the doctoral dissertation also includes experimental optimization of process parameters of batch kefir grains cultivation in milk, improvement of kefir grains activation procedure, statistical comparison between predictive growth models of classically and optimally activated kefir grains, etc. The present doctoral dissertation dealswith the most demanding aspects of knowledge based complex reactor systemdesign and therefore, it is undoubtedly individual original scientific contribution on the field of bioreaction engineering. Consequently, the work presents globally important step toward improvement of existent and development of new continuous kefir grains production plants. |