کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
150301 456447 2012 9 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Modelling of hydrodynamic behaviour of a two-stage bioreactor with cell recycling dedicated to intensive microbial production
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Modelling of hydrodynamic behaviour of a two-stage bioreactor with cell recycling dedicated to intensive microbial production
چکیده انگلیسی

An innovative two-stage continuous bioreactor with cell recycle (TSCB) previously allowed us to reach very high ethanol productivity (41 kg m−3 h−1) with the yeast Saccharomyces cerevisiae under high cell densities (∼100 gCDW/L) suitable for industrial transposition. Nevertheless, bioreactor performances and complex interactions between hydrodynamics (gas, liquid and solid phases) and biological activity (viability, conversion yield, ethanol stress) need to be investigated.In this work, an overall TSCB hydrodynamic identification (under abiotic conditions) was carried out by using residence time (RTD) and internal age (IAD) distribution studies, according to a suitable methodology.First, experiments led to identify and formulate the analytical RTD and IAD functions in continuous mode with and without recycling. Mixing time experiments were carried out in order to characterize batch mode for the liquid phase. Secondly, a systemic approach was used to identify the model parameters and characterize their evolution within the investigated operating conditions, and then to corroborate the reliability of the model by considering the experiments with recycling. For the gas phase, it was shown that each stage (R1 and R2) exhibited independent behaviour and could be modelled as a plug-flow reactor associated to j Continuous Stirred Tank Reactor, CSTR in series; the values of the model parameters (α, j) remained constant within the investigated operating range (VVM, Re and ReA). For the liquid phase, the hydrodynamic behaviour of R1 and R2 could be represented by CSTR behaviour. A plug-flow reactor is thus proposed to describe the permeate compartment behaviour.


► Mixing time experiments were carried out in order to characterize batch mode for the liquid phase.
► In continuous mode, hydrodynamic identification was carried out by using RTD.
► A systemic approach was used to identify the model parameters.
► In continuous mode, recycling was used in order to validate the robustness of models.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Journal - Volume 183, 15 February 2012, Pages 222–230
نویسندگان
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