Operational characteristics of continuous renal replacement modalities used for critically ill patients with acute kidney injury.

Renal replacement therapy (RRT) is required in a significant percentage of patients developing acute kidney injury (AKI) in an intensive care unit (ICU) setting. One of the foremost objectives of continuous renal replacement therapy (CRRT) is the removal of excess fluid and blood solutes that are retained as a consequence of decreased or absent glomerular filtration. Because prescription of CRRT requires goals to be set with regard to the rate and extent of both solute and fluid removal, a thorough understanding of the mechanisms by which solute and fluid removal occurs during CRRT is necessary. The following provides an overview of solute and water transfer during CRRT and this information is placed in the appropriate clinical context with a discussion of recent clinical trials assessing the relationship between CRRT dose and patient survival. Moreover, the differences between solute removal in CRRT and other dialysis modalities, especially sustained low-efficiency dialysis (SLED) and extended daily dialysis (EDD), along with the potential clinical implications are discussed.

CRRT efficiency and efficacy in relation to solute size.

Removal of blood solutes in patients with decreased or absent glomerular filtration is the prime objective of continuous renal replacement therapies (CRRTs). However, because these blood solutes are of different molecular weights, factors such as the porosity and hydrophobicity of the filter membranes and the extracorporeal flow rates determine the CRRT that is the most effective filtration system. This article discusses both small and large solute removal, the interaction of convection and diffusion, and the potential for CRRTs to remove particular inflammatory mediators of acute renal failure.

Effects of dialysis membrane on intradialytic vancomycin administration.

STUDY OBJECTIVE: To quantify the influence of hemodialyzers on vancomycin removal when the drug was infused during hemodialysis. DESIGN: Prospective, controlled, crossover study with three arms. SETTING: A university-affiliated medical center. PATIENTS: Eight subjects receiving outpatient hemodialysis. INTERVENTIONS: The three treatment arms were vancomycin 1000 mg infused after dialysis was completed (control), and the same dosages infused during the last hour of hemodialysis with a cellulose triacetate (CT) and a cellulose acetate (CA) hemodialyzer. MEASUREMENTS AND MAIN RESULTS: The areas under the curve from time zero to 44 hours (AUC0-44 hrs) for the three study arms were significantly different (p < 0.05), with the mean vancomycin AUC0-44 hrs being significantly lower when administered during CT and CA dialysis (73.7% and 87.2% of control; p < 0.05 vs control). The mean vancomycin peak concentration achieved during CT dialysis was significantly lower than for the CA and control arms (20.5, 23.9, 27.0 mg/L, respectively). Forty-four-hour postinfusion concentrations were similarly lower. CONCLUSION: Clinicians should recognize that the composition of the hemodialyzer significantly influences vancomycin serum concentrations when the drug is administered during hemodialysis.

Exosurf treatment following wood smoke inhalation.

Pulmonary surfactant deactivation is an important factor in the pathophysiology caused by wood smoke inhalation. Surfactant replacement is beneficial in treatment of surfactant-deficient neonates and possibly the adult respiratory distress syndrome (ARDS). In this study, the effect of exogenous Exosurf treatment for acute wood smoke injury was examined in four groups of rabbits. All groups were anaesthetized, placed on a ventilator, and surgically prepared for haemodynamic, peak airway pressure (P(aw)), and blood gas measurements. Rabbits were monitored for 2 h following smoke or sham smoke inhalation. At the conclusion of the experiment pulmonary oedema and surfactant function were measured. A Control group (n = 5) was followed without intervention. A Smoke group (n = 4) was ventilated with wood smoke for 3 min. A third group (Smoke+Exo, n = 4) was subjected to smoke followed by pulmonary instillation of Exosurf (5 ml/kg). Saline (5 ml/kg) was instilled into the lungs of the fourth group (n = 3) as a control for Exosurf instillation. Saline, Smoke and Smoke+Exo all significantly lowered PO2 and elevated P(aw) compared to baseline and the Control group. Exosurf treatment did not reduce the pulmonary oedema or restore surfactant function caused by smoke exposure. This study indicates that wood smoke inhalation acutely damages the lung and that administration of Exosurf by instillation is not an effective treatment.

Clinical evaluation of a new high efficiency hemodialyzer: polysynthane.

Two increasingly common characteristics of the American chronic hemodialysis (HD) population, high hematocrit and large body size, may render the currently recommended adequacy targets difficult to achieve, even with very efficient dialyzers. In a group of patients with these characteristics, we assessed the ability of a new high efficiency dialyzer (PSN210; Baxter Healthcare Corporation) to achieve the currently recommended adequacy targets. Six patients (mean pre-HD weight and hematocrit, 90.3 +/- 18.0 kg and 0.40 +/- 0.03 kg, respectively) were evaluated. At prescribed blood and dialysate flow rates of 400 and 800 ml/min, respectively, and a mean treatment duration of 4 hrs, mean delivered urea Kt/V and reduction ratio (URR) were 1.38 +/- 0.25 and 0.73 +/- 0.07, respectively. For the same flow rates, whole blood clearances for urea, creatinine, and phosphate were 315 +/- 13, 246 +/- 28, and 260 +/- 27 ml/min, respectively. These data indicate this dialyzer has an efficient mass transfer design allowing adequate dialysis to be delivered even to very large patients under high efficiency conditions.

A modified equivalent annulus model for the hollow fiber hemodialyzer.

Experimental approaches to optimize hollow fiber hemodialyzer design are expensive and time-consuming. Computer modeling is an effective way to study mass transfer in the hemodialyzer because a substantial reduction in experimental time and cost can be achieved. This paper presents a two-dimensional modified "equivalent annulus" model, which employs Navier-Stokes (N-S) equations to describe blood and dialysate flow, and Kedem-Katchalsky (K-K) equations to calculate transmembrane flow. N-S equations and K-K equations must be coupled together in the process of computing. The corresponding experiments were designed to validate this model, and experimental results agreed well with numerical results. The distribution of velocity, pressure and solute concentration were investigated in detail, presenting a clear insight into dialyzer mass transfer. This model can be applied to help optimize hemodialyzer design.

Hemodialyzer membranes and configurations: a historical perspective.

The principle of hemodialysis (HD) was first described over a century ago while the first human HD treatment was performed in 1923 with collodion tubes. Since that time, a variety of different hemodialyzer configurations and membranes have been used. The purpose of this article is to provide a historical review of these various configurations and membranes. The rotating drum, coil, parallel flow, and hollow fiber artificial kidneys are discussed. Emphasis is placed on the factors that have influenced the shaping of the contemporary HD market.

The toxic shock syndrome in a burn victim.

A case of toxic shock syndrome (TSS) in a 6-year-old boy with a 5 per cent body surface area partial thickness scald burn is reported. Biobrane was the wound dressing used initially. The clinical and laboratory characteristics of the syndrome are listed. The syndrome is caused by an exotoxin of Staph. aureus and can occur in the absence of invasive infection. The syndrome, first described in menstruating women who used tampons, has occurred in patients with a variety of wounds. Reports of the TSS syndrome in burn victims are limited to children whose wounds were covered. Children are most vulnerable to the development of TSS because of their limited prior exposure to the toxin.

Use of a balanced bowel preparation solution in urological surgery.

A balanced bowel preparation solution was used in 25 patients undergoing cystectomy and in 31 undergoing radical retropubic prostatectomy. No significant problems occurred during the preparation, intraoperatively or postoperatively. Metronidazole and neomycin were used for antibiotic coverage. Consistent with the findings of other studies no significant physiological shifts occurred and patient acceptance was good. Savings were noted in cost, duration of hospitalization, time needed for nursing care and nutritional status. The balanced bowel preparation solution is an attractive and equally effective alternative to the standard laxative-enema bowel preparations for urological operations.

Determinants of haemodialyser performance and the potential effect on clinical outcome.

The performance of a dialyser is determined by several factors. Many of these factors relate to the dialyser membrane, including mean pore size, pore size distribution, wall thickness, surface area, and adsorptivity. In this article, several of these factors are reviewed. The potential impact of these factors on the clinical outcome of chronic haemodialysis patients is also discussed.

Vancomycin mass transfer characteristics of high-flux cellulosic dialysers.

BACKGROUND: In comparison to conventional haemodialysis membranes, highly permeable membranes allow a broader spectrum of solute removal, including enhanced elimination of vancomycin (1448 Daltons). However, the mass transfer characteristics of vancomycin removal by highly permeable membranes have not been adequately assessed. An understanding of vancomycin's predominant dialytic mass transfer mechanism under a given set of operating conditions, including dialyser type and flow rates, may permit more accurate dosing of the drug. METHODS: We performed a mass transfer analysis of vancomycin removal by a high-flux dialyser, cellulose triacetate (CT). In a cross-over fashion with a 3-week washout between treatments, eight subjects received vancomycin 1000 mg (1) during the last hour of CT haemodialysis; or (2) after dialysis. Serial urea and vancomycin serum concentrations were used to assess dialytic removal. RESULTS: Dialysis removed 26.2% (mean; range 16-44%) of the administered vancomycin dose. While vancomycin removal and (Kt/V)urea were directly correlated (r = 0.88; P < 0.005), no correlation was observed between vancomycin removal and weight-normalized ultrafiltration rate. CONCLUSIONS: These findings suggest that for the CT dialyser and dialysis operating conditions employed in this study, vancomycin clearance was primarily mediated by diffusion. As such, these data challenge the general concept that convection is primarily responsible for the removal of solutes in the same molecular weight class as vancomycin during high-flux dialysis.

Effect of membrane composition and structure on solute removal and biocompatibility in hemodialysis.

Effect of membrane composition and structure on solute removal and biocompatibility in hemodialysis. Significant changes in extracorporeal membranes have occurred over the past five decades in which hemodialysis (HD) has been available as a therapy for both acute renal failure (ARF) and end-stage renal disease (ESRD). For cellulosic membranes, these changes have included a reduction in thickness, hydroxyl group substitution, and an increase in pore size. These modifications have resulted in enhanced efficiency of small solute removal, a broader spectrum of overall solute removal, and an attenuation of complement activation in comparison to the thick, unsubstituted cellulosic membranes of low permeability used in the early days of HD therapy. Synthetic membranes, originally developed specifically for use in high-flux HD and hemofiltration, have also evolved during this same time period. In fact, the initially clear distinction between low-flux regenerated cellulosic and high-flux synthetic membranes has become blurred, as membrane formulators have developed products designed to appeal to enthusiasts for both membrane formats. The purpose of this review is to characterize both the solute removal and biocompatibility characteristics of dialysis membranes according to their composition (that is, polymeric makeup) and structure. In this regard, the manner in which membrane biocompatibility interacts with flux is highlighted.

Membrane adsorption of beta 2-microglobulin: equilibrium and kinetic characterization.

Enhanced extracorporeal removal of beta 2-microglobulin (beta 2m) may prevent the development of dialysis-related amyloidosis (DRA). One mechanism of beta 2m removal is membrane adsorption. Therefore, we fundamentally characterized beta 2m adsorption to the highly permeable polyacrylonitrile (PAN) membrane. Porous and nonporous PAN fragments were incubated in buffer containing 125I-beta 2m. Over a concentration range of 8 to 60 mg/liter, the equilibrium adsorption isotherm was linear (r = 0.99) for porous PAN while the isotherm for nonporous PAN suggested either multilayer binding or adsorption of proteins with differing orientations. In kinetic analyses, the approach to equilibrium versus (time)1/2 was evaluated. For both porous and nonporous PAN, this relationship was linear (r = 0.99), consistent with a diffusion-controlled process. Adsorption reversibility was assessed by comparing the amount bound at varying residence times (0 to 4 hr) to the amount remaining adsorbed after a subsequent incubation in buffer. The fractions remaining bound at 60, 120, and 240 minutes (0.34 +/- 0.02, 0.36 +/- 0.06, and 0.44 +/- 0.03; mean +/- SEM) were significantly greater (P < 0.05) than the value at five minutes (0.23 +/- 0.01). This suggests membrane-induced conformational changes in adsorbed beta 2m. This investigation permits the comparison of beta 2m adsorptive properties of PAN to those of other membrane-based and nonmembrane-based therapies designed to prevent DRA.

Plasma protein adsorption to highly permeable hemodialysis membranes.

Although membrane adsorption of plasma proteins is one of several factors determining the biocompatibility and mass transfer characteristics of a hemodialyzer, this process has not been evaluated rigorously. We performed an equilibrium and kinetic analysis of the binding of proteins of differing molecular weight to highly permeable membranes of differing hydrophobicity and surface change. Hydrophobic, anionic polyacrylonitrile (PAN) and hydrophilic, uncharged cellulose triacetate (CT) membrane fragments were incubated in buffer containing radioiodinated beta 2-microglobulin (beta 2m) or bovine serum albumin (BSA). From an initial solution concentration of 50 mg/liter, both membranes adsorbed significantly more beta 2m than BSA at equilibrium (PAN, 352 +/- 30 vs. 32.1 +/- 2.4 ng; CT, 87.0 +/- 0.6 vs. 30.8 +/- 1.7 ng). These results were consistent with membrane pore exclusion of BSA. Comparison of the slopes of the equilibrium isotherm lines (concentration range, 0 to 220 mg/liter) showed the PAN binding affinity for beta 2m and BSA was 28 and 1.4 times that of CT, respectively. In kinetic studies, the approach to equilibrium versus (time)1/2 was assessed. For all protein-membrane combinations, this relationship was linear, consistent with a diffusion-controlled process. This latter characteristic permitted the determination of beta 2m membrane diffusivity values for both PAN and CT, which were found to be 0.30 and 3.25 x 10(-7) cm2/sec, respectively. These data suggest membrane hydrophobicity more significantly influences the binding of low-molecular weight proteins than that of pore-excluded proteins. In addition, these results demonstrate electrostatic membrane-protein interactions may influence the kinetics of both the adsorption and transmembrane mass transfer of plasma proteins.

Alveolar function following surfactant deactivation.

In vivo cinemicroscopic studies of subpleural alveoli were conducted in dogs for 4 h after pulmonary lavage with 5% Tween 20 and after lavage with normal saline. Saline-lavaged alveoli showed little change in alveolar size during tidal ventilation, whereas Tween lavage resulted both in alveolar recruitment and marked variation in alveolar size from end expiration to peak inspiration, with total collapse frequently occurring by end expiration. Following Tween, alveolar stability decreased, but alveolar capillary perfusion increased. Marked recovery of stability by 4 h was noted in most alveoli. Wilhelmy balance studies on lung extracts showed a decrease in surfactant function 30 min after Tween and a partial recovery of surfactant activity after 4 h. This study provides in vivo evidence that normal surfactant function is critical to alveolar stability and that alveolar stability is markedly restored 4 h after acute deactivation or displacement by Tween. Surfactant deactivation and loss of alveolar stability are associated with increased alveolar capillary perfusion creating significant ventilation-perfusion ratio abnormalities.