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Transport of target anions, chromate (Cr (VI)), arsenate (As (V)), and perchlorate (ClO4-), through RO, NF, and UF membranes.

Rejection and transport of chromate (Cr (VI)), arsenate (As (V)), and perchlorate (ClO4-) by and through reverse osmosis, nanofiltration, and ultrafiltration were found to be affected by solution pH and ionic strength. In this study, the rejection of these target ionic contaminants increased with increasing pH at the same conductivity (ionic strength) for the tested membranes, regardless of salt type. General trends showed that the rejection followed the order: CaCl2 < KCl < or = K2SO4, at the same pH and conductivity condition. The rejection also significantly decreased as conductivity was increased regardless of the salt type. These results support the notion that a more negative surface charge due to increasing pH and/or decreasing ionic strength (conductivity) enhances rejection; lower molecular weight cut-off also enhances rejection. Measured values of hindered diffusion coefficient through the membrane pores (Dp) for the target contaminants significantly decreased as pH was increased, regardless of salt type at the same conductivity. At the same pH and conductivity, the Dp of the target contaminants follows the order: CaCl2 > KCl > K2SO4, in the presence of different types of salts. The Dp of the target contaminants significantly increased as conductivity was increased regardless of the salt type. The rejection data were modeled by application of a non-equilibrium thermodynamic model. The rejection model has five transport parameters: the molecular transport coefficient (omega), osmotic pressure gradient (deltaII), molecular reflection coefficient (sigma), the average bulk fluid interfacial concentration between the feed and permeate side (C(avg)), and the solvent flux (Jv). The transport parameters were determined by independent measurements (and calculation with minimum assumptions.) Measurements and predictions of the target contaminant transport were in good agreement.

Arsenates↗

Rejection of trace organic compounds by high-pressure membranes.

High-pressure membranes, encompassing reverse osmosis (RO), nanofiltration (NF), and low-pressure RO, may provide an effective treatment barrier for trace organic compounds including disinfection by-products (DBPs), pesticides, solvents, endocrine disrupting compounds (EDCs) and pharmaceutically active compounds (PhACs). The objective is to develop a mechanistic understanding of the rejection of trace organic compounds by high-pressure membranes, based on an integrated framework of compound properties, membrane properties, and operational conditions. Eight trace organic compounds, four DBPs and four chlorinated (halogenated) solvents, are being emphasized during an initial study, based on considerations of compound properties, occurrence, and health effects (regulations). Four polyamide FilmTec membranes; three reverse osmosis/RO (BW-400, LE-440, XLE-440) and one nanofiltration/NF (NF-90); are being characterized according to pure water permeability (PWP), molecular weight cutoff (MWCO), hydrophobicity (contact angle), and surface charge (zeta potential). It is noteworthy that rejections of compounds of intermediate hydrophobicity by the candidate membranes were observed to be less than salt rejections reported for these membranes, suggesting that transport of these solutes through these membranes is facilitated by solute-membrane interactions. We are continuing with diffusion cell measurements to describe solute-membrane interactions by estimation of diffusion coefficients through membranes pores, either hindered or facilitated.

Diffusion↗

MBR/RO/ozone processes for TFT-LCD industrial wastewater treatment and recycling.

This research is mainly to explore the treatment capacity for TFT-LCD industrial wastewater recycling by the processes combined with membrane bioreactor (MBR), reverse osmosis (RO) and ozone(O3). The organic wastewater from the TFT-LCD industry was selected as the target. MBR, RO and ozone plants were established for evaluation. An MBR plant consisted of a 2-stage anoxic/aerobic bioreactor and an immersed UF membrane unit was employed. The effluent of MBR was conducted into the RO system then into the ozone system. The RO system consisted of a spiral membrane in the vessel. One bubble column, 75 cm high and diameter 5 cm, were used as the ozonation reactor. On the bottom of ozonation reactor is a porous diffuser for releasing gas, with an aperture of 100 microm (0.1 cm). Over the whole experimental period, the MBR process achieved a satisfactory organic removal. The COD could be removed with an average of over 98.5%. For the TOC item, the average removal efficiency was 97.4%. The stable effluent quality and satisfactory removal performance were ensured by the efficient interception performance of an immersed UF membrane device incorporated with the biological reactor. Moreover, the MBR effluent did not contain any suspended solids and the SDI value was under 3. After the treatment of RO, excellent water quality was found. The water quality of permeate was under 5 mg/I, 2 mg/l and 50 micros/cm for COD, TOC and conductivity respectively. The treated water can be recycled and reused for the cooling tower make-up water or other purposes. After the treatment of ozone, the treated water quality was under 5 mg/l and 0.852 mg/l for COD and TOC respectively. The test results of MBR, MBR/RO and MBR/RO/ozone processes were compared as possible appropriate treatment technologies applied in TFT-LCD industrial wastewater reuse and recycling.

Bioreactors↗

Development of an integrated membrane process for water reclamation.

An integrated membrane process (IMP) comprising a membrane bioreactor (MBR) and a reverse osmosis (RO) process was developed for water reclamation. Wastewater was treated by an MBR operated at a sludge retention time (SRT) of 20 days and a hydraulic retention time (HRT) of 5.5 h. The IMP had an overall recovery efficiency of 80%. A unique feature of the IMP was the recycling of a fraction of RO concentrate back to the MBR. Experimental results revealed that a portion of the slow- and hard-to-degrade organic constituents in the recycle stream could be degraded by an acclimated biomass leading to an improved MBR treatment efficiency. Although recycling concentrated constituents could impose an inhibitory effect on the biomass and suppress their respiratory activities, results obtained suggested that operating MBR (in the novel IMP) at an F/M ratio below 0.03 g TOC/g VSS.day could yield an effluent quality comparable to that achievable without concentrate recycling. It is noted in this study that the novel IMP could achieve an average overall TOC removal efficiency of 88.940% and it consistently produced product water usable for high value reuse applications.

Biomass↗

Human red blood cells' physiological water exchange with the plasma.

In the present paper, fundamental issues related to the mechanisms of human red blood cells' physiological water exchange with the plasma (for the stationary conditions) have been discussed. It has been demonstrated, on the basis of mechanistic transport equations for membrane transport that red blood cells are capable of exchanging considerable amounts of water with the plasma. Water absorption is osmosis-driven, and its removal occurs according to the hydromechanics principle, i.e. is driven by the turgor pressure of red blood cells. This newly-acquired knowledge of these issues may appear highly useful for clinical diagnosis of blood diseases and blood circulation failures.

Animals↗

[The progress of the concentration technology of extract of traditional Chinese medicine].

The concentration of extract of traditional Chinese medicine (TCM) is one of the important unit operations that affect the quality of the pharmaceutical products. However, there are some problems to be solved. The concentration process has the shortages of relatively high temperature, relatively long time or low efficient, some losses of active and volatile ingredients, more operation steps, easy fouling and emission of waste water. In order to solve these problems, many new technologies and installations have been developed in the past thirty years, including suspension freeze-concentration, progressive freeze-concentration, single- or multi-effect evaporation with an external natural circulating flow, on-line preventing fouling evaporation with vapor-liquid-solid flow, reverse osmosis concentration, membrane distillation, osmotic distillation, macro-porous resin adsorption etc. The system of the extract of TCM is very complex. The extract includes water and alcohol extracts. The composition of TCM is made of active and inactive ingredients. Hence, it is necessary to master the features of every concentration technologies and installations, including their merits and demerits, flexibilities, degree of maturations of techniques and so on to get a wise choice for the industry applications. New concentration technologies and installations of the extract of TCM developed recently are reviewed in this paper. The characteristics of each method are analyzed and discussed in order to guide the industry applications. At the same time, the further research directions of concentration techniques of extract of TCM are also given.

Drugs, Chinese Herbal↗

Theoretical search for the growth-temperature relationship in plants.

In this article we deal with the definition of a new phenomenological model with physical bases for the response of short-term cell expansion growth to temperature. Although the interest on both the biomechanical bases of elongation growth and on temperature responses has a long lasting development in plant biology and biophysics, yet the question of the mode of actions of temperature is a very relevant and still open one. The purpose of our paper was not to deal with all the complexity of the possible effects of temperature on a growing cell but to concentrate on two more focused questions: i) whether it is possible to specify an optimal temperature for growth responses all along development by defining some phenomenological equations for temperature response, ii) can we learn something from that on the temperature dependence of the cell wall expansion process using a minimal analytical modelling? To answer both questions we introduce (by extending Lockhart approach) the notion of temperature by simple thermodynamical reasoning. Assuming incompressibility of water (by the constant molar density n/V ) we also accounted for the role of osmosis and consequently - the role of water uptake in growing cell. This approach allowed us (by comparing theoretical solutions and experimental results) not only to determine the specific (resonance) temperature (or corresponding absorption energy kBT*) of the optimal growth but also draw conclusions about the cell wall extensibility dependence on temperature and its evolution in time. A straightforward application of our method to determine optimum growth temperature for different plant species in a greenhouse practice (as its simple implication) can also be recommended.

Biomechanical Phenomena↗

What is the value of plasma/serum aluminum in patients with chronic renal failure?

In a region with a relatively low incidence of aluminum toxicity water, dialysis fluid and plasma aluminum were monitored in hemodialysis patients before and after the introduction of reverse osmosis (RO) water. Before the use of RO water, there was a close correlation between plasma and dialysis fluid aluminum with exposure to aluminum being reflected equally by either water, dialysis fluid or plasma aluminum. Patients with clinical manifestations of aluminum toxicity were characterised by a plasma aluminum consistently greater than mumol/l and a dialysis fluid aluminum consistently greater than 1 mumol/l. No evidence of clinical toxicity was found in patients in whom the plasma aluminum was maintained up to 5 mumol/l. Following the introduction of RO water, the dialysis fluid aluminum was able to be maintained less than 1 mumol/l, the plasma aluminum fell and no new cases of clinical toxicity were identified over the following five years. An effect of aluminum hydroxide dosage on plasma aluminum could be identified only in patients in whom the dialysis fluid aluminum was less than 1 mumol/l. Plasma aluminum was found to be a poor guide to bone stores but appeared to correlate better with the presence of bone toxicity than total bone aluminum. Regular monitoring of dialysis fluid and plasma aluminum is recommended as a means of detecting exposure to aluminum as well as the source of exposure and as a guide to the risk of clinical toxicity.

Adult↗

Fluid electrolyte changes in physically healthy subjects during prolonged restriction of motor activity and daily hyperhydration.

The aim of this report was to present some of our results, in a compressed form, obtained from our previous studies on the effect of 364-d hypokinesia (decreased number of steps taken per day by the volunteers) on the following: (1) regulation of fluid volume and osmosis, (2) regulation of electrolytes, and (3) functional condition of the kidneys and its role in the fluid-electrolyte homeostasis on 30 physically healthy male volunteers aged 22-26 years. Prior to their exposure to hypokinesia all subjects were on 13.8 km/day (10,000 running steps/day) and were all well conditioned, with (oxygen uptake capacities (VO2 max 68 ml/kg-min). During the hypokinetic period of 364 days, the 1st group was subjected to pure hypokinesia (HK), that is without the use of physical exercise (PE), the 2nd group was subjected to a set of intensive PE (energy expenditure of 700 kcal/h) and the 3rd group submitted to a set of moderate PE (energy expenditure of 400 kcal/h). All volunteers consumed daily fluid and salt supplementation (FSS) aimed at increasing body hydration level during the hypokinetic period. For the simulation of the hypokinetic effect all volunteers were kept on 2.7 km/day (3000 walking steps per day). All volunteers were on a diet of freshly prepared food, with a daily intake of 2500-2700 kcal, 3340 ml water, 1500 mgs calcium, 500 mgs magnesium, 1200 mgs potassium, 1500 mgs phosphorus, 8.5 gms sodium and 9.8 gms chloride. The amount of fluid and electrolytes consumed and eliminated in urine, as well as their concentrations in the urine and blood plasma were determined. There were also measured urinary volume, osmolality, creatine, and urea changes in urine. During HK the amount of fluid and electrolytes consumed daily decreased while the rate of excretion increased significantly. During post HK the fluid and electrolytes concentrations in urine decreased significantly. The urinary urea, osmolality and creatinine increased significantly during HK. It was concluded that prolonged restriction of motor activity induced significant changes in fluid, excretion and concentration of electrolytes in plasma, as well as in the rate of their excretion by the kidneys.

Adult↗

Formaldehyde, sodium hypochlorite, and metabisulphite are equally effective as sterilants for central delivery systems.

Sterilants are used to disinfect reverse osmosis (RO) thin film composite membranes or peripheral loop water delivery systems. Formaldehyde (4.0% weight/volume) and metabisulphite (1.0%) were used to sterilize the RO and peripheral loop, and sodium hypochlorite (0.5%) was used to sterilize the peripheral loop with only acid/alkaline treatment of the RO; each sterilant was evaluated for 4 months. Sanitization at the machine was with sodium hypochlorite or glutaraldehyde. Quantitative RO processed water (weekly) and dialysate (4-6 from each station during the period of each sterilant) cultures were obtained. AAMI standards were used (< 200 CFU/ml RO water; < 2,000 CFU/ml dialysate). Bacterial growth exceeded Association for the Advancement of Medical Instrumentation (AAMI) limits in 16% of RO water and 4.7% of dialysate samples, but repeat cultures invariably failed to confirm initial abnormal results. Chi-square analysis showed no differences among sterilants. No difference among sterilants was noted in arithmetic or log10 mean colony counts. Sporadic low level gram positive and gram negative organism growth occurred with all sterilants. Continued "sterility" that met AAMI standards was obtained for 1 year, first with metabisulphite and then with acid/alkaline RO and sodium hypochlorite loop treatment. It is concluded that all three sterilants are effective for disinfection of hemodialysis delivery systems. Sodium hypochlorite is recommended because of its safety advantages and readily available test of adequate removal.

Colony Count, Microbial↗

Length of the selectivity filter of aquaporin-1.

We have characterized the selectivity filter of the water channel aquaporin-1 (AQP1) of proximal straight tubules (PST), as an equivalent cylindrical structure with a diameter of approximately 4.5 A, where water molecules single file. We report here efforts to evaluate its length. PST were dissected from rabbit kidneys, held with pipettes in a chamber bathed in a buffered mannitol isosmotic solution (MBS, 295 mOsm/kg). Changes in tubule cell volume with time (dV/Adt), were monitored, on line, with an inverted microscope, a TV camera and an image processor. Osmotic permeability coefficients, Pos, and reflection coefficients (sigma s) were measured with several solutes: mannitol (M), raffinose (R), sucrose (S), glycerol (G), acetamide (A) and urea (U). For this purpose PST were suddenly exposed (in approximately 80 ms and for 20 s) to a hyperosmolality step (delta Cs) achieved by adding to MBS a delta Cs of 35 mOsm/kg of either R, S, M, G, A or U. Cells shrunk within 500 ms of t = 0 to their osmometric volume and remained shrunk for the 20 s of the delta Cs. Pos was measured from the shrinking curves; Pos = 3000 +/- 25 microns/s with either R, S, M, G, A or U. This procedure also allowed to calculate sigma s; sigma s = 1.00 for R, S, M, G, A and U, indicating that these solutes do not penetrate the water channel. In contrast, the shrinking curves produced by a delta Cs = 35 mOsm/kg formamide (F) were 1/5th to 1/6th slower and smaller (subosmometric) than those produced by a delta Cs = 35 mOsm/kg of R, S, M, G, A or U. Furthermore, with F, cells did not remain shrunk. They recovered their original volume within 3 s. Pos (measured with F) is denoted as Pos*; Pos* = 480 +/- 30 microns/s. sigma s, formamide (denoted sigma sp) = 0.16 +/- 0.01. Use of sigma sp and Pos* values in Hill's equations for the bimodal theory of osmosis leads to n = 2-3, n being the number of water molecules single filing within the channel selectivity filter, whose length must lie within 6 to 9 A, a value lower than previous values calculated from the Pos/Pd* ratio.

Animals↗

Reduction of tissue edema by microdialysis.

OBJECTIVE: This is the first report (to our knowledge) of the use of tissue microdialysis to reduce tissue edema. In this study, a hyperosmotic solution was perfused through microdialysis catheters, allowing direct treatment of interstitial edema by osmosis. DESIGN: First, the catheter and perfusate characteristics were tested in vitro. A physiologic, controlled trial was then performed, with two outcome variables: osmolarity of the effluent and tissue water content. SUBJECTS: Twenty male Sprague-Dawley rats. One rat was withdrawn. INTERVENTIONS: Tissue microdialysis catheters were implanted in the rats. The control side of the animals was not perfused. The experimental side was perfused for 9 hours. RESULTS: Osmolarity of the perfusate was reduced 16.5 mOsm after passing through the catheter, indicating that fluid was removed from the tissue. Tissue edema was reduced by an average 1.8 mL of fluid per 100 g of wet tissue. CONCLUSIONS: Tissue microdialysis removed tissue fluid and reduced edema. This treatment may have a beneficial effect on edematous tissues. Potential use and limitations of this therapeutic modality are discussed.

Animals↗

Biomaterial properties and biocompatibility in cell culture of a novel self-inflating hydrogel tissue expander.

The aim of this study was to investigate the swelling properties and the biocompatibility of a novel tissue expander material. The self-inflating material is a hydrogel consisting of a modified copolymer of methylmethacrylate and N-vinyl-2-pyrrolidone, which takes up water by osmosis. To increase the swelling volume, the primarily neutral gel material was modified by converting it into an ionized gel. To study the swelling and pressure behavior of the material, the anhydrous gel cylinders were equilibrated in distilled water, saline, and sugar solutions. The biocompatibility was investigated in cell culture. We tested the hydrogel eluate after swelling for cytotoxicity and mutagenicity using the cell lines MRC-5 and P3X63 Ag8 653 (Ag8). Furthermore, particles of the material were added to cell cultures to induce foreign body reactions and to verify its influence on monocyte differentiation. The material has a swelling capacity (Q = maximum swelling volume/anhydrous volume) of 5 to 50 depending on the degree of ionization of the polymer network. In this study, two polymer modifications with a swelling equilibrium of Q = 11.1 and 30 in water were tested. The swelling ratio also depends on concentration and ion content of the equilibration medium. The highest swelling capacity was found in water, the lowest in Ringer's solution. The swelling of the anhydrous material with the swelling capacity of Q = 11.1 fits best the average purpose of material properties for tissue expansion and generates a maximal hydrostatic pressure of approximately 235 mmHg. Effects on cell proliferation were detected only at the highest eluate concentration tested (i.e., eluate: culture medium = 1:1), which was far beyond physiological values, whereas mutagenicity was absent. Monocytes neither migrated nor tightly attached to the hydrogel. They neither phagocytose the material nor did they show any sign of a foreign body reaction, e.g., formation of multinucleated giant cells or monocyte proliferation. In the presence of hydrogel material, the differentiation processes of monocytes to macrophages or dendritic cells, respectively, were found to be undisturbed. From these results, we conclude that there is a high biocompatibility of the expander material, which may be a favorable and interesting candidate for further clinical applications.

Animals↗

Urinary and serum silicon in normal and uraemic individuals.

The urinary excretion of silicon (Si) in humans was studied in normal subjects on a low Si diet, a normal diet, and after ingestion of silicate antacid. Measurements of 24-hour urinary excretion of Si showed that urinary Si was derived mainly from dietary intake. The serum concentration of Si was determined in normal individuals and in patients with chronic renal failure. In health, serum Si is maintained within a narrow range, but a significant hypersilicaemia occurs in uraemia. The concentration of Si was measured in the water supply, dialysate and pre-dialysis and post-dialysis serum in patients on regular haemo-dialysis in three areas with low, intermediate and high concentrations of Si in the water supply. Si was removed during dialysis in the region where it was naturally low in the water or where reverse osmosis was used, but it was dialysed into patients in regions with intermediate and high concentrations in the water. Serum Si levels returned to normal after renal transplantation. Preliminary analysis of the geographical variation in the Si content of tap water suggests that uraemic hypersilicaemia may protect haemodialysed patients from the development of aluminium dementia. The kidney would appear from these studies to be the major organ for elimination of absorbed Si.

Adult↗

The sieving of spheres during agarose gel electrophoresis: quantitation and modeling.

By use of agarose gel electrophoresis, the sieving of spherical particles in agarose gels has been quantitated and modeled for spheres with a radius (R) between 13.3 and 149 nm. For quantitation, the electrophoretic mobility has been determined as a function of agarose percentage (A). Because a previously used model of sieving [D. Rodbard and A. Chrambach (1970) Proc. Natl. Acad. Sci. USA 65, 970-977] was found incompatible with some of these data, alternative models have been tested. By use of an underivatized agarose, two models, both based on the assumption of a single effective pore radius (PE) for each A, were found to yield PE values that were independent of R and that were in agreement with values of PE obtained independently (PE = 118 nm X A-0.74): sieving by altered hydrodynamics in a cylindrical tube of radius, PE, and sieving by steric exclusion from a circular hole of radius, PE. The same analysis applied to a 6.5% hydroxyethylated commercial agarose yielded a steeper PE vs A plot and also agreement of the above two models with the data. The PE vs A plot was significantly altered by both further hydroxyethylation and factors that cause variation in the electro-osmosis found in commercial agarose.

Biopolymers↗

Reduction of embryotoxicity by protein in embryo culture media.

Experiments tested the hypothesis that one role of protein in embryo culture media is protection of embryos against potentially embryotoxic substances in the media. Mouse embryos were cultured in modified Krebs-Ringer bicarbonate medium and in modified Tyrode's medium, aliquots of which were supplemented with 4 mg/ml of the protein bovine serum albumin (BSA), while other aliquots were left protein free. The media were prepared using water samples that differed in purity, as reflected by differences in conductivity, with tap water being least pure (and considered to have the greatest potential for being embryotoxic) and water that had been purified by reverse osmosis, Milli-Q filtration, and triple distillation being most pure. Embryos were placed in the media while in the two-cell stage of development and their development was assessed after 24, 48, and 72 hr of culture. Rate of embryo development in BSA-supplemented media was greater than that in protein-free media only when the media were prepared with the least purified water samples. Because these water samples would have contained substances not contained in media prepared with purer water, or would have contained the substances in higher concentration, the data supported the hypothesis that protein can protect embryos during culture by negating effects of embryotoxic substances in the media.

Animals↗

Attenuating effects of natural organic matter on microcystin toxicity in zebra fish (Danio rerio) embryos -- benefits and costs of microcystin detoxication.

To contribute to the understanding of joined factors in the environment, impact of pure microcystins (-RR and -LF) on zebra fish (Danio rerio) embryos were investigated individually and in combination with a natural organic matter (NOM). The applied NOM was a reverse osmosis isolate from Lake Schwarzer See (i.e., Black Lake, BL-NOM). Teratogenic effects were evaluated through changes in embryonic development within 48 h of exposure. Detoxication activities were assessed by the activities of phase II biotransformation enzymes, soluble and microsomal glutathione S-transferase (s, mGST). Oxidative stress was assessed by determining both the production of hydrogen peroxide and by analyzing the activities of the antioxidative enzymes, guajacol peroxidase (POD), catalase (CAT), glutathione peroxidase (GPx), and the glutathione restoring enzyme glutathione reductase (GR). Energetic costs were evaluated by determining contents of fat, carbohydrates, and proteins in both exposed and control embryos. BL-NOM attenuated toxic effects of MC-LF and MC-RR verified by less pronounced teratological effects within 24 h, in particular, as well as less rise in the activity of s-GST, when compared with embryos exposed to either pure toxins or in combination with organic matter. BL-NOM also diminished oxidative effects caused by MC-LF; however, it failed to attenuate oxidative stress caused by MC-RR. Content of lipids was significantly reduced in exposed embryos following a trend similar to that obtained with teratological and enzymatic assays confirming the attenuating effect of BL-NOM. Physiological responses to microcystins and NOM required energetic costs, which were compensated to the expense of the energy resources of the yolk, which in turn might affect the normal development of embryos.

Animals↗

Centrifugal precipitation chromatography: principle, apparatus, and optimization of key parameters for protein fractionation by ammonium sulfate precipitation.

A novel chromatographic system introduced here internally generates a concentration gradient of ammonium sulfate (AS) through a long separation channel under a centrifugal force field. Protein samples are exposed to a gradually increasing AS concentration and precipitated along the channel. Then, chromatographic elution is initiated by gradually decreasing the AS concentration in the gradient which causes the proteins to repeat dissolution and precipitation through the channel. Consequently, they are eluted out in the order of their solubility in the AS solution. The separation column consists of a pair of disks equipped with mutually mirror-imaged spiral grooves. A dialysis membrane is sandwiched between the disks to form two identical channels partitioned by the membrane. The disk assembly is mounted on the sealless continuous-flow centrifuge. When a concentrated AS solution is eluted through one channel and water through the other channel in an opposite direction, an exponential AS gradient is formed through the water channel. A series of basic experiments was performed to study the rates of AS transfer and osmosis through the membrane, and the operational parameters including elution time, revolution speed, inclination of gradient, and sample size were optimized using stable protein samples. Preliminary applications were successful in purification of monoclonal antibody from cell culture supernatant and an affinity separation of recombinant ketosteroid isomerase from a crude Escherichia coli lysate.

Ammonium Sulfate↗