Mathematical modelling as a tool to study population dynamics between sulfate reducing and methanogenic bacteriaстатья
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Дата последнего поиска статьи во внешних источниках: 18 июля 2013 г.
Аннотация:The existing mathematical models of sulphate fed anaerobic reactors are reviewed. Special attention was put on pecularities of the description of sulphide inhibition and competition between sulphate reduction and methanogenesis in such systems. The paper also presents an integrated mathematical model of the functioning of a sulphate fed granular sludge reactor taking into account concentration gradients on substrates, intermediates, products and bacteria inside the reactor as well as multiple- reaction stoichiometry and kinetics. The developed model includes the following blocks: a) hydrodynamic block describing liquid flow as well as transport and distribution of the components along the reactor height; b) kinetic block including growth, metabolism, inhibition and competition of acidogenic, acetogenic, methanogenic and sulphate reducing bacteria in the system; c) physico-chemical block for calculation of pH in each compartment of the liquid phase; d) transfer block describing a mass transfer of gaseous components from the liquid to the gas phase. The integrated model was calibrated and validated using laboratory studies on the functioning of sulphidogenic granular sludge reactors, i.e. their start-up and the maximisation of sulphide yield in these reactors. The modelling of the reactor operation is supplemented with hypothetical computer simulations to illustrate the influence of engineering parameters on the operation performance and sulphate conversion of sulphidogenic reactors. An integrated mathematical model of the functioning of a sulfate-fed granular sludge reactor is presented, considering concentration gradients on substrates, intermediates, products, and bacteria inside the reactor, as well as the multiple-reaction stoichiometry and kinetics. The model includes: hydrodynamic block describing liquid flow, and transport and distribution of the components along the reactor height; kinetic block including growth, metabolism, inhibition, and competition of acidogenic, acetogenic, methanogenic, and sulfate reducing bacteria; physico-chemical block for the calculation of pH in each compartment of the liquid phase; and the transfer block describing a mass transfer of gaseous components from the liquid to the gas phase.