is influenced by different factors such as operating conditions
module characteristics
and membrane properties. The general aim of this study was to develop a suitable (flexible
comprehensive
and convenient to use) computational tool which is able to simulate osmosis through an asymmetric membrane oriented in pressure retarded osmosis (PRO) mode in a wide variety of scenarios. For this purpose
an agent-based model was created in NetLogo platform
which is an easy-to-use application environment with graphical visualization abilities and well suited for modeling a complex system evolving over time. The simulation results were validated with empirical data obtained from literature and a great agreement was observed. The effect of various parameters on process performance was investigated in terms of temperature
cross-flow velocity
length of the module
pure water permeability coefficient
and structural parameter of the membrane. Results demonstrated that the increase in all parameters
except structural parameter of the membrane and the length of module led to the increase of average water flux. Moreover
nine different draw solutes were selected in order to assess the influence of net bulk osmotic pressure difference between the draw solution (DS) and feed solution (FS) (known as the driving force of FO process) on water flux. Based on the findings of this paper
the performance of FO process (PRO mode) can be efficiently evaluated using the NetLogo platform.
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Isobaric vapor—liquid equilibrium for the binary system of methyl propionate and methyl methacrylate at 90.0, 75.0, 60.0, 45.0 and 30.0kPa
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Related Author
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Related Institution
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