Abstract
A simple lumped-parameter mathematical model is developed for analysing the performance of a haemodialyser. Analytical solutions are derived for the exit concentration of solute in blood leaving the haemodialyser. A method of ana priori estimation of the model parameters is suggested. The validity of the model is illustrated by comparing it with the numerical solution of more exact 2-dimensional models and some experimental data on commercial dialysers. The utility of the model is illustrated by an application to the simulation of a patient-artificial-kidney system, wherein compact analytical expressions are shown to describe the whole complex system.
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Abbreviations
- a :
-
parameter defined in eqn. 14
- A 11,A 12 :
-
parameters defined by eqns. 32 and 33, respectively
- C b :
-
concentration of solute in blood, mole/cm3
- C bi :
-
concentration of solute in the blood entering the dialyser, mole/cm3
- C bo :
-
concentration of solute in the blood leaving the dialyser, mole/cm3
- C d :
-
concentration of solute in the dialysate fluid, mole/cm3
- C di :
-
concentration of solute in the dialysate entering, mole/cm3
- C do :
-
concentration of solute in the dialysate leaving, mole/cm3
- C dw :
-
concentration of solute at the wall in contact with the dialysate, mole/cm3
- C t :
-
concentration of solute in the intracellular fluid, mole/cm3
- C w :
-
concentration of solute at the wall in contact with the blood, mole/cm3
- D :
-
molecular diffusivity of solute in blood, cm2/s
- D 2 :
-
molecular diffusivity of solute in dialysate fluid, cm2/s
- D E :
-
axial dispersion coefficient, cm2/s
- h :
-
half-channel width of a parallel plate dialyser, cm
- I :
-
rate of production of urea in the body, mole/s
- k :
-
permeability of the tube wall, cm/s
- k d :
-
effective mass-transfer coefficient for the dialysate side fluid, cm/s
- k L :
-
effective mass-transfer coefficient from the blood to the tube wall, cm/s
- K :
-
exchange coefficient between intra and extracellular compartments, h−1 or s−1
- L :
-
length of the dialyser, cm
- N :
-
rate of removal of urea in the dialyser, mole/s
- P :
-
parameter defined by eqn. 12
- P e :
-
parameter defined by eqn. 13
- q :
-
ratio of flow ratio,Q B/QD
- Q B :
-
volumetric flow rate of blood, cm3/s
- Q D :
-
volumetric flow rate of dialysate, cm3/s
- R :
-
radius of the tubular haemodialyser, cm
- R A :
-
rate of solute removal at the wall, mole cm−2s−1
- t :
-
time elapsed since start of dialysis, s
- u b :
-
average velocity of blood, cm/s
- V C :
-
total volume of intracellular compartment, cm3
- V E :
-
total volume of extracellular compartment, cm3
- W :
-
width of the dialysate groove, cm
- x :
-
axial distance, cm
- x * :
-
dimensionless axial distance,x/L
- y :
-
dimensionless axial length of the dialyser (LD/u b R2 for tubular andLD/u b h2 for flat plate dialysers, respectively)
- α:
-
parameter defined in eqn. 15 or 16
- β 1,β 2 :
-
parameters defined in eqns. 42 and 43, respectively
- γ:
-
geometry factor (=1 for flat plate, 2 for cylinder)
- λ 1,λ 2 :
-
roots of eqn. 38
- ν:
-
dimensionless wall permeabilitykR/D
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Ramachandran, P.A., Mashelkar, R.A. Lumped-parameter model for haemodialyser with application to simulation of patient-artificial-kidney system. Med. Biol. Eng. Comput. 18, 179–188 (1980). https://doi.org/10.1007/BF02443292
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DOI: https://doi.org/10.1007/BF02443292