2017
DOI: 10.1016/j.memsci.2017.07.018
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Optimization of dialyzer design to maximize solute removal with a two-dimensional transport model

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Cited by 26 publications
(19 citation statements)
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“…A good agreement was found between the model-predicted and Islam et al in-silico results [22]. The trend of increase in clearance with dialysate flow is also validated by comparing with the Revaclear Max dialyzer experimental (reported in Bhimani et al [25]) and Donato et al in-silico results [21]. The difference between Revaclear Max and model-predicted data is due to the lack of a comprehensive dataset of module parameter values needed for model predictions.…”
Section: Effect Of Operating Conditions On Clearance Efficiencysupporting
confidence: 60%
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“…A good agreement was found between the model-predicted and Islam et al in-silico results [22]. The trend of increase in clearance with dialysate flow is also validated by comparing with the Revaclear Max dialyzer experimental (reported in Bhimani et al [25]) and Donato et al in-silico results [21]. The difference between Revaclear Max and model-predicted data is due to the lack of a comprehensive dataset of module parameter values needed for model predictions.…”
Section: Effect Of Operating Conditions On Clearance Efficiencysupporting
confidence: 60%
“…The velocity profiles on both the blood and dialysate side are portrayed with the Navier-Stokes equations [18]. Steady-state, isothermal conditions (T = 37 • C) and laminar flow prevail on both blood and dialysate side with high dilution of solutes [20,21]. It is assumed that the viscosity of both blood and dialysate does not change with applied share.…”
Section: Governing Equations-blood Side (I = B)mentioning
confidence: 99%
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“…Accordingly, alterations in the diameter and length of the hollow fibres and in membrane hydraulic permeability significantly affect the rate of internal filtration [ 44–46 ]. The effect of capillary internal diameter on the rate of internal filtration and the clearance of complement factor D (24 kDa) as an indicator of middle molecule removal is shown in Figure 2 [ 47 ].…”
Section: Approaches To the Development Of New Membranesmentioning
confidence: 99%
“… Effect of (A) fibre inner diameter on internal filtration rate and (B) clearance of complement factor D (24 kDa) at different blood flow rates studied computationally by employing a two-dimensional transport model [ 47 ] [net ultrafiltration: 0 mL/min; dialysate flow rate: 500 mL/min (blue lines), 800 mL/min (red lines); effective fibre length: 23.6 cm; membrane surface area: 1.7 m 2 ; fibre packing density: 56.1%; ultrafiltration coefficient: 48 mL/h/mmHg; sieving coefficient for complement factor D: 0.52]. …”
Section: Approaches To the Development Of New Membranesmentioning
confidence: 99%