BACKGROUND: Hemodialysis using high flux membranes today is a commonly used therapy. The primary advantage is the larger spectrum of molecules removed with these membranes, and the mechanism of removal is in part due to a phenomenon of filtration and backfiltration along the length of the hollow fibers. We hypothesized that increasing the filtration and backfiltration fluxes by modifying the structure of the dialyzer could enhance the convective transport of various solutes. METHODS: A modified high flux dialyzer was compared to the standard model in terms of pressure profiles, filtration-backfiltration rates and solute clearances. The modification consisted on the placement of a O-ring around the fiber bundle to create a resistance for the flow of the dialysis solution external to the fibers. The study on filtration fluxes was carried out using a scintigraphic method previously described, and solute clearances were studied during ultrafiltration-controlled hemodialysis sessions. RESULTS: Utilizing a net filtration condition proximal to zero, the rates of proximal filtration and distal backfiltration in the experimental dialyzer were significantly enhanced in comparison with the standard dialyzer. The pressure drop in the dialysate compartment could be increased significantly, thus permitting an increase in the positive transmembrane pressure in the first half of the dialyzer and a parallel increase in the negative transmembrane pressure in the second half of the dialyzer. This resulted in a significant enhancement of the convective transport of middle-large solutes as demonstrated by the increase in vitamin B12 and inulin clearances. CONCLUSIONS: This approach suggests that changes in design of the dialyzer may affect its performance. The use of internal filtration is suggested to improve convection and dialyzer efficiency for larger solutes without the requirement for high volumes of replacement fluid, as is the case for current hemodiafiltration techniques.
BACKGROUND: Hemodialysis using high flux membranes today is a commonly used therapy. The primary advantage is the larger spectrum of molecules removed with these membranes, and the mechanism of removal is in part due to a phenomenon of filtration and backfiltration along the length of the hollow fibers. We hypothesized that increasing the filtration and backfiltration fluxes by modifying the structure of the dialyzer could enhance the convective transport of various solutes. METHODS: A modified high flux dialyzer was compared to the standard model in terms of pressure profiles, filtration-backfiltration rates and solute clearances. The modification consisted on the placement of a O-ring around the fiber bundle to create a resistance for the flow of the dialysis solution external to the fibers. The study on filtration fluxes was carried out using a scintigraphic method previously described, and solute clearances were studied during ultrafiltration-controlled hemodialysis sessions. RESULTS: Utilizing a net filtration condition proximal to zero, the rates of proximal filtration and distal backfiltration in the experimental dialyzer were significantly enhanced in comparison with the standard dialyzer. The pressure drop in the dialysate compartment could be increased significantly, thus permitting an increase in the positive transmembrane pressure in the first half of the dialyzer and a parallel increase in the negative transmembrane pressure in the second half of the dialyzer. This resulted in a significant enhancement of the convective transport of middle-large solutes as demonstrated by the increase in vitamin B12 and inulin clearances. CONCLUSIONS: This approach suggests that changes in design of the dialyzer may affect its performance. The use of internal filtration is suggested to improve convection and dialyzer efficiency for larger solutes without the requirement for high volumes of replacement fluid, as is the case for current hemodiafiltration techniques.
Authors: Kamyar Kalantar-Zadeh; Linda H Ficociello; Jennifer Bazzanella; Claudy Mullon; Michael S Anger Journal: Int J Nephrol Renovasc Dis Date: 2021-01-20