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INTRODUCTION: During real-time monitoring of the ultrafiltration coefficient (Kuf) in haemodiafiltration (HDF), it was noticed that the ultrafiltration performance of polysulphone membrane dialysers increased when hypertonic glucose (D50%) was administered through the venous blood return. METHODS: This observation was explored in six non-diabetic chronic dialysis patients during 48 HDF sessions using 1.8 m(2) polysulphone membrane dialysers. In all six patients, 24 sessions were performed with glucose supplementation (as a continuous D50% (500 g/l) infusion at 40 ml/h) and 24 sessions without supplementation. RESULTS: Glucose supplementation led to a marked increase in Kuf from 22.8+/-2.2 (without D50%, n=24) to 32. 1+/-3.9 ml/h/mmHg (with D50%, n=24) (P<0.0001). An increase in percentage reduction ratios for urea and creatinine were also consistently observed during the sessions with glucose administration (from respective mean values of 75+/-5 and 68+/-4% to 79+/-4 and 74+/-10%). Mean double-pool Kt/V, calculated from serum urea concentrations, rose from 1.65+/-0.24 (n=24) to 1.86+/-0.24 (n=24) (P<0.005). Similar results were observed in a subgroup of 18 HDF sessions (nine with glucose and nine without) monitored with an on-line urea sensor of spent dialysate. No detrimental effects were induced at any time. CONCLUSIONS: We conclude that intravenous glucose administration during high-flux HDF using polysulphone membranes increases significantly both ultrafiltration capacity and dialysis dose delivery.

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Oxidized LDL (low density lipoprotein) are considered to be the major initiating event in atherogenesis. In vitro models have been studied but no mathematic modeling can assess quantitatively the oxidability of LDL and antioxidant effects. We have developed a mathematic modeling allowing quantification of different kinetic parameters to LDL oxidation. This model has been validated by means of a software (software NELOP) in normal population (HV) and in a cardiovascular risk population, hemodialysis (HD). LDL are collected and purified by sequential ultracentrifugations from 12 healthy volunteers and hemodialysis patients. LDL oxidability (0.1 microM) is initiated by 5 microM copper and monitored continuously by conjugated diene production. All parameters are evaluated and correlated to those obtained by NELOP. Significant correlations between measured and calculated parameters (Vmax: r2 = 0.99, p < 0.05) allow to validate NELOP in both populations. Our results show that hemodialysis LDL present an enhanced susceptibility to copper induced oxidation (lag time: 96.6 +/- 48.6 mn in HV versus 54.5 +/- 22.2 mn in HD). NELOP seems to be a useful tool to evaluate LDL oxidation in cardiovascular risk populations.

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Dialysis-related pathology (DRP) observed in long-term haemodialysis patients is increasingly reported. Among DRP manifestations, cardiovascular disease is the most frequent, being the first cause of mortality in haemodialysis patients. Alterations in lipid metabolism and oxidative stress are recognised as major risk factors that could be prevented or reduced by optimal therapy. In order to evaluate the rationale for preventive intervention against oxidative damage we review the factors that are implied and may be responsible for the imbalance between prooxidative and antioxidative mechanisms in haemodialysis patients. Oxidative stress resulting from this imbalance is responsible for increasing stress markers and enhancing susceptibility to LDL oxidation. Factors implied in this prooxidative state belong to four groups: (1) uremia and comorbid status of the end stage renal disease (ESRD) patient; (2) losses of antioxidant substances via the dialysis; (3) haemoincompatibility of the dialysis system; (4) adjuvant therapy. Such prooxidant status could have further deleterious consequences since it has been recently shown that antioxidant status could modulate cell functions such as reactive oxygen species (ROS) production, adhesive molecule expression and/or cell proliferation. Preventive modalities, including use of biocompatible membrane, ultrapure dialysate, exogenous supplementation of antioxidant vitamins, extracorporeal removal of ROS and oxidatively-modified substances, would appear highly desirable to reduce complications of long-term dialysis patients.

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Direct dialysis quantification offers several advantages compared with conventional blood urea kinetic modeling, and monitoring urea concentration in the effluent dialysate with an on-line urea sensor is a practical approach. Such a monitoring device seems desirable in the short-term dialysis setting to optimize and personalize both renal replacement therapy and nutritional support of acutely ill patients. We designed a urea monitoring device consisting of a urea sensor, a multichannel hydraulic circuit, and a PC microcomputer. The sensor determines urea from catalysis of its hydrolysis by urease in liquid solution during neutral conditions. Hydrolysis of urea produces NH4+, and creates an electrical potential difference between two electrodes. Each concentration determination of urea is the average value of 10 measurements; samples are diverted and measured every 7 min. Laboratory calibration of the urea sensor has demonstrated linearity over the range 2-35 mmol/L. Urea monitoring was performed throughout the treatment course, either on the effluent dialysate or ultrafiltrate in seven acutely ill patients treated by either hemofiltration (n=5) or hemodiafiltration (n=2). The slope of the concentration of urea in the effluent over time was used to calculate an index of the dialysis dose delivered (Kt/V), urea mass removal, and protein catabolic rate. In addition, samples of the effluent were drawn every 21 min, and sent to the central laboratory for measurement of urea concentrations using an autoanalyzer. Kt/V values also were calculated with Garred's equation using pre and post session concentrations of urea in blood. Concentrations of urea in the effluent determined by the urea sensor were found to be very close to those obtained from the central laboratory over a wide range of values (3 to 42 mmol/L). In addition, Kt/V values for both hemofiltration and hemodiafiltration, when calculated with concentrations of urea in the effluent obtained by the urea sensor, did not significantly differ from Kt/V values obtained from the laboratory concentrations of urea in the effluent. On-line urea sensor monitoring of the effluent suppresses the cumbersome task of total effluent collection, and the complexity of urea kinetic analysis. The multipurpose prototype described here represents a new, simple, and direct assessment of dialysis dose and protein nutritional status of acutely ill patients, and is suitable for various modalities.

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The ultrasound dilution technology (Transonic Systems, Ithaca, NY) is a reliable method to assess blood flow (Qb) and recirculation rates (R) in vascular access during hemodialysis. However, the information available on these parameters for central venous dialysis catheters remains scarce at this point. Real Qb and R were evaluated in 33 well-functioning TwinCath (Medcomp, Harleysville, PA) inserted as mid- or long-term hemodialysis vascular access (mean duration since insertion, 270 +/- 253 days); all were implanted into the right internal jugular vein with their multiperforated distal tips located in the superior vena cava or right atrium. Several types of dialysis machines were used (Monitral and AK100, Hospal-Gambro, Lyon, France; 2008E and 4008E, Fresenius, Bad Homburg, Germany). Real Qb was measured with the ultrasound dilution method and compared with the set Qb (indicated by the dialysis machine); R, also evaluated by ultrasound dilution, was evaluated at various Qb with nonreversed lines; therefore, a total of 121 measures were performed. Arterial and venous pressures (PA and PV) were recorded simultaneously. The 33 measures at a set Qb of 200 mL/min showed a mean effective Qb of 210 +/- 18 mL/min and a mean R of 5.3 +/- 5.3%. At a Qb of 300 mL/min, 33 repeated measures resulted in mean effective Qb of 303 +/- 21 mL/min and R of 8.5 +/- 7.0%; 28 measures performed at a set Qb of 350 mL/min showed that the effective Qb was 336 +/- 24 mL/min and that R was 7.8% +/- 6.7%. Finally, an effective Qb of 372 +/- 26 mL/min and an R of 10.9 +/- 8.6% were found for the 27 measures performed at an indicated Qb of 400 mL/min. The difference between indicated and effective Qb was particularly significant for set Qb equal to or above 350 mL/min (P < 0.001). Variable correlations were observed between obtained parameters: Qb eff and R (r = 0.34), PV and R (r = 0.36), Qb eff and PV (r = 0.78), Qb eff and PA (r = 0.71), and PV and PA (r = 0.53). In conclusion, TwinCath delivers an effective Qb of nearly 375 mL/min when Qb is set at 400 mL/min on most dialysis machines. Mean R in TwinCath varies between 5% and 11% for Qb within the range of 200 to 400 mL/min. In well-functioning TwinCath, the ratio between PV and Qb remains usually below 0.5.

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Membrane permeability is a key determinant of dialyzer performance; in vivo, membrane hydraulic permeability is affected by the formation of a protein cake on its surface, reducing ultrafiltration and convective fluxes. The purpose of this work was to evaluate the real hydraulic permeability of high flux polysulfone membrane under conditions of hemodiafiltration, and to consequently develop a mathematical model to estimate ultrafiltration Kuf and protein adsorption Kc coefficients. The DIB08 data acquisition system adapted to the Fresenius 2008E dialysis machine (Fresenius, Bad Homburg, Germany) allowed the recording of useful information for dialysis quantification, which was then processed by a bedside computer. The system was able to evaluate Kuf(t) profile, by calculation from the transmembrane pressure over time (TMP(t)) and ultrafiltration rate (Quf):Kuf (t) = Quf/TMP (t). Subsequent modeling of Kuf involved the determination of two key parameters: Kufhd (dialyzer permeability during diffusion only) (in mL/h/mmHg), and Kc (protein adsorption coefficient) (in mL/h/mmHg2). The model chosen was the following: Kuf (t) = Kuf0 x (1 - (Kc/Kuf0) x In(t + 1)) where Kuf0 represents the initial Kuf obtained at the beginning of the session. Thirty-one sessions were evaluated by real kinetic analysis, from which the mathematical model was derived. It included 27 postdilutional on-line hemodiafiltration and four hemodialysis sessions performed in four patients with nonreused HF80s dialyzers. For the analysis, three subgroups were defined: Group 1, first session of the week (Monday or Tuesday); Group 2, second session of the week (Wednesday or Thursday); and Group 3, third session of the week (Friday or Saturday). Results of Kuf and Kc obtained by real kinetic analysis are presented. The midweek session was associated with a higher membrane hydraulic permeability, most likely relative to lesser ultrafiltration rates and an associated relative decrease in membrane protein coating, represented by Kc. The described data acquisition system allowed the assessment of real time membrane hydraulic permeability and the subsequent development of a mathematical model to estimate this fundamental parameter as it functions to hemodialyzer performance.

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