The course of hematocrit value along the length of a dialyzer's fiber: Hemoconcentration modeling and validation methods

Intensification of Middle- and High-Molecular-Weight Toxins Removal in Dialysis Process

A novel extracorporeal circuit for hemodialysis is described, which enhances the removal of middle- and high-molecular-weight toxins. To enhance the removal of especially high-molecular toxins, a recirculation pathway for dialysate flow is added to conventional circuit. The influence of an increase in the ratio of recirculation to dialysate flow rate and the ultrafiltration rate (UFR) on the removal of toxins was investigated to evaluate the removal of different toxins in clinical conditions. Removal of toxins was also modeled by an analytical method and solved by the MATLAB software (The MathWorks, Inc., Natick, MA). A significant increase in removal of urea (up to 31%) and vitamin B12 (11%) was achieved when the UFR is low (≤50 ml/h) or zero. The model showed an excellent agreement with the experimental results, which indicates its applicability for the removal of different toxins in an extracorporeal circuit. Increase in recirculation flow, while adjusting the UFR near zero, improves the mass transfer coefficient and can lead to enhanced especially middle- and high-molecular-weight toxin removal.

Quantification of dissolved H2 and continuous monitoring of hydrogen-rich water for haemodialysis applications: An experimental study

The prevalence of oxidative and inflammatory stress in end-stage renal disease (ESRD) patients has often been associated with chronic haemodialysis therapies. Over the past decades, several reports have shown the potential of hydrogen molecule as an antioxidant in the treatment of various medical conditions in animal models, as well as in pilot studies with human patients. Recently, a hydrogen-enriched dialysate solution has been introduced, holding promise in reducing the oxidative and/or inflammatory complications arising during haemodialysis. To this end, a standardised measuring method to determine the levels of hydrogen in dialysate and subsequently in blood is required. This study explores the possibility of quantifying hydrogen concentration using a novel contactless sensor that detects dissolved hydrogen in liquids. An experimental circuit is assembled to validate the sensitivity and accuracy of the hydrogen monitoring system (Pureron Japan Co., Ltd) through in vitro investigations with physiological solutions. Measurements of dissolved molecular hydrogen concentration are corroborated by an established oxygen sensor providing continuous partial pressure readings. The relationship between the applied H₂ content in the gaseous mixture and the H₂ concentration value at equilibrium is linear. At the same time, the hydrogen monitoring system has a rather long response time, and its readings seem to slightly diverge from sensor to sensor as well as at different temperatures. For this reason, a sensor recalibration might be necessary, which could become part of the product's ongoing development. Nevertheless, the aforementioned minor deficiencies can be mostly considered negligible in applications such as haemodialysis.

The effect of ultrafiltration transmembrane permeation on the flow field in a surrogate system of an artificial kidney

Renal Replacement Therapies generally associated to the Artificial Kidney (AK) are membrane-based treatments that assure the separation functions of the failing kidney in extracorporeal blood circulation. Their progress from conventional hemodialysis towards high-flux hemodialysis (HFHD) through the introduction of ultrafiltration membranes characterized by high convective permeation fluxes intensified the need of elucidating the effect of the membrane fluid removal rates on the increase of the potentially blood-traumatizing shear stresses developed adjacently to the membrane. The AK surrogate consisting of two-compartments separated by an ultrafiltration membrane is set to have water circulation in the upper chamber mimicking the blood flow rates and the membrane fluid removal rates typical of HFHD. Pressure drop mirrors the shear stresses quantification and the modification of the velocities profiles. The increase on pressure drop when comparing flows in slits with a permeable membrane and an impermeable wall is ca. 512% and 576% for $ \mathrm{CA}22/5\%{\mathrm{SiO}}_2 $ and $ \mathrm{CA}30/5\%{\mathrm{SiO}}_2 $ membranes, respectively.