Lactogenic hormone signal transduction

Dialyzers are reused in approximately three quarters of the dialysis units in the United States, but the effect of reprocessing on dialyzer performance has not been extensively evaluated. In a crossover study of six chronic hemodialysis patients, we determined urea, creatinine, phosphate, and beta2-microglobulin clearances and dialysate protein loss for two types of low-flux and two types of high-flux dialyzers during use numbers 1, 2, 5, and 15. Dialyzers were reprocessed by an automated machine using Renalin (Renal Systems, Plymouth, MN) as the germicide. Dialyzer arterial and venous blood and dialysate outflow samples were obtained at 5 and 180 minutes of each dialysis session to evaluate solute clearances. Urea, creatinine, and phosphate clearances were calculated using dialysate concentrations, whereas beta2-microglobulin clearance was calculated using plasma concentrations to include its removal by adsorption to the dialysis membrane. There was a trend for urea, creatinine, and phosphate clearances to decrease with reuse for both low-flux and high-flux dialyzers, but these differences were not statistically significant. The clearance of beta2-microglobulin and dialysate total protein concentration was small for low-flux dialyzers; these values were not dependent on reuse. There was a trend for beta2-microglobulin clearance and dialysate total protein concentration to decrease during a dialysis treatment using high-flux dialyzers. More significantly, beta2-microglobulin clearance and dialysate total protein concentration decreased substantially with the reuse of high-flux dialyzers. These observations show that the maintenance of small solute clearances during reuse of high-flux dialyzers does not ensure the maintenance of large solute clearances.     

Effect of truncation and mutation of the carboxyl-terminal region of the beta subunit on membrane assembly and activity of the pyridine nucleotide transhydrogenase of Escherichia coli

Among the several disadvantages of reprocessed dialyzers is the concern that reuse could decrease the clearance of uremic toxins, leading to a decrease in the delivered dose of dialysis. To examine this possibility in the clinical setting, the clearances of small molecular weight solutes (urea and creatinine) and middle molecular weight substances (beta 2 microglobulin) were compared during dialysis with "high-efficiency" cellulose (T220L) and "high-flux" polysulfone (F80B) dialyzers reprocessed with formaldehyde and bleach. In a crossover study, six chronic hemodialysis patients were alternately assigned to undergo 21 dialysis treatments with a single T220L dialyzer or F80B dialyzer. Each patient was studied during first use (0 reuse), 2nd reuse (3rd use), and 5th, 10th, 15th, and 20th reuse of each dialyzer. Urea, creatinine, and beta 2 microglobulin clearances were measured at blood flow rates of 300 ml/min (Qb 300) and 400 ml/min (Qb 400). Total albumin loss into the dialysate was measured during each treatment. Urea or creatinine clearance of new T220L dialyzers was not significantly different from that of new F80B dialyzers at either Qb. Urea clearance of F80B dialyzers at Qb 300 decreased from 241 +/- 2 ml/min for new dialyzers to 221 +/- 5 ml/min after 20 reuses (P < 0.001), and Qb 400 from 280 +/- 4 ml/min for new dialyzers to 253 +/- 7 ml/min after 20 reuses (P = 0.001). Similarly, with reuse, creatinine clearance of F80B dialyzers also decreased at Qb 300 (P = 0.07) and Qb 400 (P = 0.03). In contrast, urea or creatinine clearance of T220L dialyzers did not decrease with reuse at either Qb. Urea clearance of T220L dialyzers was significantly higher than that of F80B at Qb 300 at the 5th, 10th, 15th, and 20th reuse (P < 0.001, = 0.005, = 0.004, and = 0.006, respectively), and Qb 400 at the 2nd, 5th, 10th, 15th, and 20th reuse (P = 0.04, 0.008, 0.03, 0.02, and 0.008, respectively). Beta 2 microglobulin clearance of T220L dialyzers was < 5.0 ml/min across the reuses studied. Beta 2 microglobulin clearance of F80B was < 5.0 ml/min for new dialyzers, but increased to 21.2 +/- 5.3 ml/min (Qb 300) and 23.6 +/- 3.3 ml/min (Qb 400) after 20 reuses (P < 0.001). Throughout the study, albumin was undetectable in the dialysate with T220L dialyzers. With F80B dialyzers, albumin was detected in the dialysate in four instances (total loss during dialysis, 483 mg to 1.467 g). In summary, the results of this study emphasize the greater need for information on dialyzer clearances during clinical dialysis, especially with reprocessed dialyzers. A more accurate knowledge of dialyzer performance in vivo would help to ensure that the dose of dialysis prescribed is indeed delivered to the patients.     

Switch from conventional to high-flux membrane reduces the risk of carpal tunnel syndrome and mortality of hemodialysis patients

The use of a high-flux membrane, which eliminates larger molecular weight solutes with better biocompatibility, has steadily increased since the discovery of beta-2 microglobulin (beta 2m) amyloidosis in 1985. The long-term effects of a dialyzer membrane on morbidity and mortality are not completely understood. To examine the membrane effect as a factor of carpal tunnel syndrome onset and mortality, multivariate Cox regression analysis with time-dependent covariate was conducted on 819 patients from March 1968 to November 1994 at a single center. Two hundred and forty-eight of the patients were either switched from the conventional to high-flux membrane or treated only with a high-flux membrane. Fifty-one patients underwent a CTS operation and 206 died. Membrane status (on high-flux or on conventional) was considered as time-dependent covariate and risk was adjusted for age, gender, type of renal disease and calendar year of dialysis initiation. The relative risk of CTS was reduced to 0.503 (P < 0.05) and mortality 0.613 (P < 0.05) by dialysis on the high-flux membrane, compared to the conventional membrane. Serial measurements of beta 2m indicated significantly lower beta 2m to persist in patients on the high-flux membrane. The high-flux membrane decreased the risk of morbidity and mortality substantially. Larger molecule elimination was shown important not only for preventing beta 2m amyloidosis, but for prolonging survival of dialysis patients as well.     

Transmembrane passage of cytokine-inducing bacterial products across new and reprocessed polysulfone dialyzers

The widespread use of bicarbonate dialysate and reprocessed high-efficiency and "high-flux" dialyzers has raised concerns about the increased risk of reverse-transfer of dialysate contaminants into the blood compartment. To evaluate this concern, the reverse-transfer of bacterial products from contaminated bicarbonate dialysate into the blood compartment was compared during in vitro dialysis with new or reprocessed high-flux polysulfone dialyzers. In vitro dialysis was carried out at 37 degrees C by use of a counter-current recirculating loop dialysis circuit with either new high-flux polysulfone dialyzers or dialyzers reprocessed once or 20 times with formaldehyde (0.75%) and bleach (< 1%) with an automated system. Heparinized whole blood from healthy volunteers was circulated through the blood compartment, and bicarbonate dialysate was circulated in the dialysate compartment. The dialysate was challenged sequentially by 1:1000 and 1:100 dilutions of a sterile Pseudomonas aeruginosa culture supernatant (bacterial challenge). Samples were drawn from the blood and dialysate compartments 1 h after each challenge. Peripheral blood mononuclear cells (PBMC) were harvested by Ficoll-Hypaque separation from whole blood in the blood compartment and a 5 x 10(6) PBMC/mL cell suspension was prepared. Likewise, dialysate samples (0.5 mL) were added to 0.5 mL suspension of 5 x 10(6) PBMC/mL drawn at baseline. All PBMC suspensions were incubated upright in a humidified atmosphere at 37 degrees C with 5% CO2 for 24 h, and total interleukin-1 alpha (IL-1 alpha) and tumor necrosis factor-alpha (TNF alpha) cytokine production (cell-associated and secreted) was measured by radioimmunoassay. Eight experiments were performed for each arm of the study with the same donor for each arm. One hour after contaminating the dialysate with a 1:1000 dilution of the bacterial challenge, IL-1 alpha production by PBMC harvested from the blood compartment was 160 +/- 0, 171 +/- 11, and 270 +/- 35 pg, respectively, for new dialyzers, dialyzers reprocessed once, and dialyzers reprocessed 20 times (P = 0.004). One hour after challenging the dialysate with 1:100 dilution, IL-1 alpha production by PBMC harvested from the blood compartment was 188 +/- 20, 228 +/- 35, and 427 +/- 67 pg, respectively, for new dialyzers, dialyzers reprocessed once, and dialyzers reprocessed 20 times (P = 0.006). IL-1 alpha production by PBMC from dialyzers reprocessed 20 times was significantly greater than both new and dialyzers reprocessed once. However, there were no significant differences between new dialyzers and dialyzers reprocessed once. Similarly, after the 1:1000 challenge, TNF alpha production by PBMC harvested from the blood compartment was 160 +/- 0, 160 +/- 0, and 213 +/- 22 pg, respectively, for new dialyzers, dialyzers reprocessed once, and dialyzers reprocessed 20 times (P = 0.008). After the 1:100 challenge, TNF alpha production was 168 +/- 8, 188 +/- 20, and 225 +/- 32 pg, respectively, for new dialyzers, dialyzers reprocessed once, and dialyzers reprocessed 20 times (P = 0.20). These results demonstrate that reprocessing of high-flux polysulfone dialyzers with bleach increases the risk of reverse-transfer of bacterial products from contaminated dialysate, and this risk appears to increase with the number of reuses. Consequently, units that reprocess membranes with bleach and have suboptimal water quality might subject their patients to a higher risk of cytokine-related morbidity.     

Influence of cuprophane membrane surface dialyzers on beta2-microglobulin serum concentration in patients during hemodialysis

In 14 patients beta 2-microglobulin serum concentration before and after haemodialysis using cuprophane capillary dialyzers with 0.7; 1.2 and 1.5 m2 surface was measured. beta 2-microglobulin concentration did not change during the haemodialysis procedure using 0.7 m2 dialyzers and was 31.15 +/- 7.58 mg/l before the dialysis and 31.10 +/- 13.59 mg/l after the procedure. Using 1.2 m2 dialyzers beta 2-microglobulin serum level increased (not significantly) from 29.40 +/- 7.53 mg/l before dialysis up to 36.29 +/- 11.70 mg/l after dialysis. When employed 1.5 m2 dialyzers the increase of beta 2-microglobulin serum concentration was higher and statistically significant (p < 0.02). The values of beta 2-microglobulin serum level before and after the haemodialysis were 29.89 +/- 2.44 mg/l and 38.04 +/- 5.89 mg/l respectively. There was a significant increase of number of patients with higher beta 2-microglobulin serum level (p < 0.01) according to the increase of dialyzers surface. beta 2-microglobulin concentration after the haemodialysis procedure using 0.7 m2 dialyzers was lower than calculation of protein changes could show. However using 1.2 and 1.5 m2 dialyzers beta 2-microglobulin serum level was markedly higher (statistically significant (p < 0.05) when employed 1.5 m2 dialyzers), than expected using the some above calculation. The increase of beta 2-microglobulin showed positive, but statistically not significant correlation with the index of haemodialysis intensitivity. The above mentioned data indicate that the increase of beta 2-microglobulin after haemodialysis is not related to biocompatibility of cuprophane membrane, but is dependent on intensivity of haemodialysis, which associated with the surface of the membrane.     

Influence of blood flow on adsorption of beta2-microglobulin onto AN69 dialyzer membrane

Adsorption onto the dialyzer membrane is a contributing factor to the elimination of beta2-microglobulin (beta2M) from the sera of uremic patients. The purpose of this prospective study was to ascertain the influence of the blood flow rate on adsorption of beta2M onto the polyacrylonitrile (AN69) hollow-fiber dialyzer membrane in 8 patients during regular hemodialysis (HD). Blood first passed through a low-flux polysulfone dialyzer and then through an AN69 dialyzer, which was not in contact with the dialysis fluid. During the investigation period (first hour of the HD session), the blood flow rate was 100 ml/ min (first part of the study), 200 ml/min (second part of the study), and 300 ml/min (third part of the study). Ultrafiltration was not performed during the investigation period. At the start of the HD sessions, the serum concentration of beta2M in the afferent blood line did not differ significantly among the 3 parts of the study. Serum beta2M was measured in samples taken from the afferent and efferent blood lines of the AN69 dialyzer at 5, 10, 15, 30, 45, and 60 min. The serum beta2M concentration decreased significantly in blood that had passed through the AN69 dialyzer. This decrease, indicating membrane adsorption, was maximal during the first part and minimal during the third part of study. The decrease in the contact time between the blood and the AN69 could be the underlying cause. The calculated quantities of beta2M adsorbed onto the AN69 membrane (44.2 +/- 10.2, 43.2 +/- 12.1, and 42.6 +/- 17.3 mg) did not differ significantly among the 3 parts of the study. These results suggest that an increase in blood flow rate from 100 to 300 ml/min did not significantly affect the quantity of beta2M adsorbed onto the AN69 membrane.     

Development of a new cellulose triacetate membrane with a microgradient porous structure for hemodialysis

Dialytic performance and biocompatibility of a newly developed cellulose triacetate (CTA) membrane with a microgradient porous structure, produced without using polyvinylpyrrolidone (PVP) and liquid paraffin, were compared with those of a conventional polysulfone (PS) membrane dialyzer. In vitro and clinical results demonstrated no significant difference in the dialytic performance and biocompatibility of the two dialyzers, but the CTA dialyzer lost less albumin during dialysis than the PS. These results suggest that a CTA membrane dialyzer with a porous microgradient structure attained comparable performance and biocompatibility to PS, and the risk of albumin loss was suppressed by the new CTA membrane.     

In vivo verification of an automatic noninvasive system for real time Kt evaluation

It is generally accepted that morbidity and mortality of hemodialysis patients is related to dialysis quantitation. Currently available methods for the quantitation of dialysis require blood sampling or a continuous measurement of changes in urea concentration during treatment. These maneuvers are time consuming and expensive, and are generally performed, at most, once per month. The authors introduce an on-line, automated method for measurement of dialyzer electrolyte clearance comparable to urea clearance by using dialysate conductivity sensors placed pre and post dialyzer, and measuring conductivity at three different pre dialyzer levels. Conditions that reduce clearance, such as recirculation or fiber clotting, are automatically taken into account so that the method measures effective clearance rather than dialyzer clearance. In vitro and in vivo studies validate the method. Results are immediately available and can be used to address problems such as improper needle placement and access recirculation. In addition, repetitive electrolyte clearance data can serve to enhance quality assurance programs with respect to verifying the function of reused or new dialyzers. Appropriate algorithms can be used to calculate delivered Kt/V.     

Absence of bacteremia and endotoxemia despite contaminated dialyzate

Fevers associated with hemodialysis have been attributed to the transfer of relatively large endotoxin molecules and/or bacteria from contaminated dialyzate across the dialyzing membrane. We evaluated 27 patients during hollow-fiber dialysis when, due to a malfunction, dialysis fluids contained bacteria and endotoxin at levels previously reported to be associated with pyrogenic reactions. Neither endotoxin nor bacteria was detected in 54 venous and arterial blood specimens collected at the termination of hemodialysis. Temperature elevations did not occur during or within 1/2 hr after dialysis. In an extended study, 20 dialyzers were collected after single patient use and the dialyzate compartment was filled with highly contaminated dialyzate, while the blood compartment was filled with sterile pyrogen-free saline. Following 5 to 7 days incubation, bacteria were present in the blood compartments of 4 of 20 dialyzers, probably due to contamination during dialyzer handling. However, the much smaller endotoxin molecule could not be detected in the absence of bacterial contamination. These results indicate that the intact cellophane membrane is an effective barrier to endotoxin and bacteria under clinical conditions.     

Optimizing sodium balance in hemodialysis

this paper develops and tests a mathematical model for Na+ kinetics applied to standard hemodialysis. The volume of distribution of exchangeable Na+, dialyzer surface area, blood and dialysis fluid flow rate, target weight loss, treatment duration and the Na+ diffusibility constant are taken into account. The model is used to compute the optimal hour by hour dialysis fluid Na+ concentration required to achieve the prescribed end-dialysis natremia and maintain a constant end-dialysis body Na+ pool, while providing a nearly uniform removal of Na+ over dialysis. The model was preliminary tested on 10 consecutive dialyses in a single patient using special dialyzer which generates a part of ultrafiltrate uncontaminated by dialysate.     

Vancomycin elimination during high-flux hemodialysis: kinetic model and comparison of four membranes

Vancomycin clearance was measured in five patients during dialysis with cuprophane (CU), polysulfone (PS), cellulose triacetate (CT), and polyacrylonitrile (PAN) dialyzers. Vancomycin was significantly cleared during routine high-flux (HF) hemodialysis (HD) with the latter three membranes, but not by CU. Postdialytic rebound of serum vancomycin concentrations was noted following HF dialysis, necessitating use of a two-compartment pharmacokinetic model. Measurement of serum vancomycin concentration immediately postdialysis significantly overestimates intradialytic removal, possibly resulting in inappropriate dose adjustment. Vancomycin infusion during HF HD results in significant drug removal during its administration to the patient, complicating the calculation of an adequate dose.     

POEMS syndrome in a patient with diabetic ketoacidosis: case report and review

This article summarise the main data in the literature on the role of bacteriological contamination of the dialysate fluid in inflammatory reactions in hemodialysis. Pyrogenic substances of small molecular weight from Gram-negative bacteria grown in dialysate can pass across intact dialyzer membrane to stimulate cytokine production by peripheral blood mononuclear cells. Cellulosic hemodialysis membranes are more permeable to endotoxins than synthetic membranes. Polysulfone membranes and polyamide membranes are able to adsorb bacterial toxins on the dialysate side. The diffusive transfer of bacterial products across dialysis membrane from dialysate fluid was demonstrated. Transmembrane passage of cytokine-inducing bacterial products across reprocessed dialyzers is greater than across new dialyzers. Bacteriological contamination of the dialysate fluid is a problem which must be considered with much more care by nephrologists, especially as LAL test is unable to detect all the bacterial products which can contaminate the dialysate fluid.     

The use of heated citric acid for dialyzer reprocessing

Dialyzer reprocessing with heated water (100 to 105 degrees C) for 20 h can be used safely in lieu of chemical methods for disinfection. All infective agents including spores are destroyed and depyrogenation may occur. However, these temperatures may result in structural damage to the dialyzer, limiting reuse. Dialyzer reprocessing by using 1.5% citric acid heated to 95 degrees C for 20 h is an alternative method that produces equivalent microbiologic effects. Citric acid is well known as a disinfecting agent used for dialysis equipment. Because there is little structural damage to dialyzer components at 95 degrees C, reuse statistics are improved (mean reuse increased to 12.8). Both small and large molecule clearances and the sieving coefficient for protein are insignificantly altered by the process. Whereas the procedure is relatively simple, quality-assurance indicators are essential. The method has appeal because it avoids the use of chemical germicides. However, at present it has only been tested thoroughly in polysulfone dialyzers with heat-resistant polycarbonate casings and polyurethane resin. The clinical experience is favorable.     

Improved biochemical variables, nutrient intake, and hormonal factors in slow nocturnal hemodialysis: a pilot study

OBJECTIVE: To determine whether slow nocturnal hemodialysis (SNHD) can be safely performed in patients with end-stage renal disease to improve the biochemical and clinical outcome. MATERIAL AND METHODS: We conducted an 8-week pilot study in nondiabetic adult patients, who underwent dialysis 6 nights per week for 8 hours each night. A dialysate flow rate of 300 mL/min and a blood flow rate of 250 mL/min, through an internal jugular dual-lumen venous catheter, were used. The equipment used was a COBE Centry System 3 dialysis machine and Fresenius F-80 (1.8 m2) or Baxter CT 190 (1.9 m2) dialyzers. Five patients were enrolled in the study. RESULTS: Two patients did not complete the study because of catheter-related infections--one at day 7 and one after 4 weeks of SNHD. All patients had improved blood pressure control, and no intradialytic adverse events occurred. Dietary intake improved, urea and creatinine levels significantly decreased, and weekly delivery of dialysate increased on SNHD. Potassium, chloride, beta 2-microglobulin, phosphorus, calcium, and high-density lipoprotein cholesterol all improved on SNHD. Serum testosterone increased in the three men on SNHD, but parathyroid hormone, luteinizing hormone, and follicle-stimulating hormone remained unchanged. Erythropoietin levels increased on SNHD, despite no change in exogenous erythropoietin doses in three patients and discontinuation of administration of erythropoietin in one. The following biochemical factors did not change significantly: serum sodium, bicarbonate, vitamin B12, folate, alkaline phosphatase, total cholesterol, triglycerides, and albumin. CONCLUSION: Higher doses of hemodialysis benefit nutrition, improve biochemical variables, and may improve many hormonal systems.     

A comparison of solute clearance and ultrafiltration volume in peritoneal dialysis with total or fractional (50%) intraperitoneal volume exchange with the same dialysate flow rate

BACKGROUND: The most efficient way to perform automated peritoneal dialysis (APD) has not yet been defined. Tidal peritoneal dialysis (TPD) has been claimed to be more efficient than traditional intermittent peritoneal dialysis (IPD), but few comparative studies have been done keeping dialysate flow the same in the two treatment techniques. METHODS: Six patients were treated with 10, 14 and 24 litres total dialysis fluid volume during 9 h (flow rate 18.5, 25.9 and 44.4 ml/min), receiving the treatments both as IPD and TPD. Glucose concentration in the fluid was held constant during all treatments. Transperitoneal clearances (ml/min) for urea, creatinine and uric acid and ultrafiltration volume was calculated, and comparisons made between TPD and IPD. The total intraperitoneal dwell time was calculated for each treatment session. A peritoneal equilibration test was also done for each patient. RESULTS: The ratio of the creatinine concentration in dialysate to the concentration in plasma at 4 h obtained with the peritoneal equilibration test (PET) averaged 0.77 (range 0.69-0.82). Urea clearance was higher for IPD than for TPD with 10 litres: 14.3 +/- 2.4 and 13.3 +/- 2.7 (P = 0.0092). For 14 and 24 litres urea clearance for IPD and TPD was 16.9 +/- 2.3 and 15.9 +/- 3.5 (n.s.) and 20.9 +/- 3.6 and 19.9 +/- 5.6 (n.s.) respectively. Creatinine clearance was higher for IPD than for TPD with 10 litres: 9.6 +/- 1.3 and 8.9 +/- 1.3 (P = 0.0002). For 14 and 24 litres creatinine clearance for IPD and TPD was 11.0 +/- 0.7 and 9.9 +/- 2.0 (n.s.) and 12.3 +/- 1.2 and 12.4 +/- 2.2 (n.s.) respectively. Uric acid clearance was higher for IPD than for TPD with 10 litres: 8.4 +/- 1.3 and 7.7 +/- 1.0 (P = 0.0054). For 14 and 24 litres uric acid clearance for IPD and TPD was 9.3 +/- 1.7 and 8.9 +/- 2.2 (n.s.) and 11.3 +/- 2.9 and 10.6 +/- 2.6 (n.s.) respectively. IPD gave significantly higher ultrafiltration volume (ml) than IPD for both 10 and 14 litres: 944 +/- 278 and 783 +/- 200 (P = 0.0313) and 1147 +/- 202 and 937 +/- 211 (P = 0.0478). For 24 litres there was no significant difference between IPD and TPD: 1220 +/- 224 and 1253 +/- 256. CONCLUSION: With the lowest dialysate flow rate (18.5 ml/min), solute clearance and ultrafiltration volume was higher on IPD than on TPD. With the intermediate flow rate (25.9 ml/min) the ultrafiltration volume was higher on IPD, but no difference was found for solute clearance. With the highest flow rate (44.4 ml/min) there was no difference neither for ultrafiltration nor for solute clearances.     

Transurethral thermotherapy in the management of benign prostatic hyperplasia

To elucidate the intradialytic urea concentration gradients, we examined 26 hemodialysis patients wearing a double-lumen central venous catheter during their first or second fistula-punctured dialysis session. In 17 patients (group A), after 60 and 240 minutes of treatment with a mean blood flow of 196.4 +/- 9.9 mL/min, blood urea nitrogen (BUN) was measured in blood samples taken simultaneously from the central venous catheter, a vein in the arm opposite the access site, and the arterial and venous lines of the dialyzer. In 16 patients (group B), after 60 minutes of treatment with a mean blood flow rate of 197.5 +/- 12.3 mL/min, BUN was measured in blood samples taken from the dialyzer arterial line and then, after decreasing the blood flow to 50 to 60 mL/min for 1 minute, in samples taken from a vein in the arm opposite the access site, the central venous catheter, and the dialyzer arterial line. In group A, the mean BUN values in the dialyzer arterial line at 60 and 240 minutes were found to be 3.7% +/- 3.7% and 3.5% +/- 3.4% higher than the corresponding values in the central veins, respectively (P = NS between 60 and 240 minutes). In group B, after 1 minute of low blood flow, this difference was 1.5% +/- 2.4% (P = 0.06 compared with group A). The peripheral veins in group A patients at 60 and 240 minutes had 9.7% +/- 5.2% and 10.9% +/- 5.3% higher BUN values, respectively, compared with the central veins. This difference in group B patients after 1 minute of low blood flow was 6.8% +/- 4.2%. Urea access recirculation rate in group A, calculated by the classical three-samples method, was found to be 7.6% +/- 5.0% at 60 minutes and 9.9% +/- 5.8% at 240 minutes (P = NS). In group B, BUN values in the dialyzer arterial line after 1 minute of low blood flow increased significantly by 3.4% +/- 4.5% (P < 0.01). Our study shows that during conventional hemodialysis with a blood flow rate of 200 mL/min, urea concentration in the central veins is lower than in the dialyzer arterial line. This gradient after 1 minute of low-flow dialysis had a tendency to decrease. At the same time, however, the urea concentration gradient between the peripheral and central veins remained high, indicating that during conventional hemodialysis, intercompartmental disequilibrium plays a significant role in the arteriovenous gradient.     

Measurement of uric acid as a marker of oxygen tension in the lung

Changes in O2 tension such as those associated with hypoxic ischemia or hyperoxia may potentially modulate purine nucleotide turnover and production of associated catabolites. We used an isolated perfused rat lung preparation to evaluate the effect of O2 tension on pulmonary uric acid production. Three O2 concentrations (21%, normoxia; 95%, hyperoxia; 0%, hypoxia) were utilized for both pulmonary ventilation and equilibration of recirculating perfusate. All gas mixtures contained 5% CO2 and were balanced with N2. We used Certified Virus Free Sprague-Dawley male rats weighting 250-300 g, four to five rats in each exposure regimen. After a 10-min equilibration period, we measured uric acid levels at 0 and 60 min in lung perfusate and at 60 min in lung tissue. After 60 min of ventilation/perfusion, we observed significant uric acid accumulation in both lung tissue (25-60%) and perfusate (8- to 10-fold) for all three O2 regimens. However, hypoxia produced substantially greater net uric acid concentrations (net = the difference between zero and 60 min) than either normoxia or hyperoxia (1.5-fold in lung tissue, and 2-fold in perfusate, respectively). The data suggest that pulmonary hypoxia results in greater purine catabolism leading to increased uric acid production. Vascular space uric acid, as measured in the recirculating perfusate, was proportional to lung weight changes (r = 0.99) with hypoxia exhibiting the greatest values, possibly reflecting a linkage between tissue perturbation and uric acid release. Thus, measurement of uric acid may serve as a useful marker of adenine nucleotide turnover and lung injury.     

Renal proximal disfunction based on activity of n-acetyl-beta-d-glucosaminidase in urine of patients with kidney failure

N-acetyl-beta-D-glucosaminidase (NAG) urine activities of 63 patients with stable and unstable chronic renal failure have been investigated. The values of NAG activity obtained from these patients were compared with NAG activity of 33 normal controls. Abnormal NAG values (> 70 nmol/mg of creatinine) were found in 60 (95.2%) patients with chronic renal failure and the median of all values was 327.8 nmol/mg of creatinine. It was 14-fold greater than the median of values for normal controls. There were any significant differences of NAG values between the patients with massive proteinuria (> 1.5 g/24 h), moderate proteinuria and those without 24 hour proteinuria or non-significant proteinuria (respectively 423.5 +/- 286.3 vs 414.4 +/- 334.8 vs 453.0 +/- 451.3 nmol/mg of creatinine). There was no significant difference between the two subgroups of patients with NAG values above and below 280 nmol/mg of creatinine in age, gender, serum urea and uric acid levels. However, the incidence of patients with NAG values higher than 280 nmol/mg of creatinine was statistically significant in unstable course of renal insufficiency and raised serum creatinine levels. It is suggested that the measurement of NAG excretion may be helpful to monitor unstable process in renal failure.     

A comparison of molecular clearance rates during continuous hemofiltration and hemodialysis with a novel volumetric continuous renal replacement system

We developed a continuous, volumetrically controlled veno-venous renal replacement system that can be operated in filtration or dialysis modes. We compared the clearances of substances with a range of molecular weights (MW) in each mode. Ten patients with acute renal failure underwent serial postdilutional hemofiltration and hemodialysis, for 30 min each, in sequence and in randomized order. All were receiving vancomycin for concurrent sepsis. The system incorporated a Filtral 10 AN69 artificial kidney; blood flow rate was 200 ml/min, and dialysate/filtrate flow rate was 25 ml/min. Sieving (SC) and diffusion (DC) co-efficients, for hemofiltration and hemodialysis, respectively, were identical for urea (MW 60; 1.01 +/- 0.05 vs 1.01 +/- 0.07) and creatinine (MW 113; 1.00 +/- 0.09 vs 1.01 +/- 0.06), and clearance equated with dialysate/filtrate flow. There was a modest difference in uric acid clearance (MW 168; SC 1.01 +/- 0.04 vs DC 0.97 +/- 0.04; p < 0.05). Vancomycin (MW 1,800) removal was 19% greater during filtration compared with dialysis (SC 0.87 +/- 0.10 vs DC 0.74 +/- 0.06; p < 0.01). For small solutes, the two modalities were equivalent. Vancomycin clearance was appreciably greater with hemofiltration, which is consistent with a greater potential for convection-based therapy in the removal of uremic and other middle molecules.