MEMBRANES FOR ULTRAFILTRATION,OF GRADUATED FINENESS DOWN TO MOLECULAR SIEVES

The use of cellophane in ultrafiltration is recommended. It is shown that after it has been swollen in water it does not hold back molecules such as sucrose but that it holds back all but the finest colloidal particles. Two methods are given for progressively decreasing the size of the pores until the cellophane becomes a very fine molecular sieve. A sieve structure as the chief factor seems most in accordance with our experience of this and other ultrafilters. Collodion membranes may also be used as molecular sieves but their properties are inconstant. Bedicher is a very fine and rapid filtering ultrafilter and pig''s bladder holds back a fair proportion of such molecules as sucrose and potassium chloride. Notes are made on the behavior of cellophane in aqueous and non-aqueous solutions. It is emphasized that ultrafiltration is distinctive and has but little relation to diffusion, dialysis, osmosis, electroosmosis or thermodynamics.     

一种浓缩噬藻体的反冲超滤技术

噬藻体(Cyanophage)是一类感染蓝藻的病毒,形态上同于噬菌体,近期的研究表明,噬藻体作为水体环境中活跃的动态因子,在控制水体初级生产力和有害藻类水华(Harmful Algal Bloom,HAB)方面可能发挥着重要的作用,甚至影响水体生态系统中食物链的结构,因此研究水体中噬藻体的生理生态学特性对于了解其生态功能是非常重要的,但是由于自然水体中的噬藻体浓度往往较低,难以直接对其进行定性或定量研究,所以对天     

Highly selective membranes in protein ultrafiltration

A new ultrafiltration technique based on a multimembrane stack has been developed to fractionate solutes closer in size than conventionally possible. The technique is illustrated here by obtaining a pure protein product from a binary protein mixture. By employing membranes in series without any gaskets or spacers in-between, ultrafiltration is carried out to separate two proteins relatively close in molecular weight or size. Flat YM30 regenerated cellulose membranes, all of the same molecular weight cut-off (MWCO) 30,000, are stacked together in the desired number, and ultrafiltration takes place. The membrane rejection of a protein is amplified with each additional membrane, ultimately resulting in a completely rejected species. Complete purification of the more permeable protein may be achieved regardless of the physicochemical condition that may be optimal or suboptimal for selective separation by a single membrane. Two systems, myoglobin and beta-lactoglobulin, as well as myoglobin and alpha-lactalbumin were studied, under various operating conditions. The solvent flux reduction encountered when each membrane is added may also be avoided, by operating at increased pressure, while still achieving the desired purification. Cleaning in situ is achievable with reproducible experimental results before and after on-line cleaning. The results clearly demonstrate that multimembrane stacks can be used for fractionation of proteins that are quite close in molecular weight/size.     

Separation of human serum albumin and human immunoglobulins using carrier phase ultrafiltration

The fractionation of the plasma proteins human serum albumin (HSA) and human immunoglobulins (HIgG) using the combination of two newly developed techniques, pulsed sample injection technique and carrier phase ultrafiltration (CPUF), is discussed in this paper. The effects of pH and ionic strength on the transmission of a single protein (i.e., either HSA or HIgG) through 100 and 300 kDa MWCO polyethersulfone (PES) membranes were quantified using the pulsed sample injection technique. The experimental results thus obtained suggested that it would be possible to fractionate these proteins by optimizing the solution pH and ionic strength. With 100 and 300 kDa PES membranes, effective separation of HSA and HIgG was achieved by CPUF using suitable conditions, i.e., pH 4.7 and low salt concentration. The fractionation of HSA and HIgG by "reverse selectivity" using 300 kDa membranes was also examined.     

Parameter scanning ultrafiltration: rapid optimisation of protein separation

High-resolution fractionation of proteins using ultrafiltration is feasible only at highly optimised conditions. Conventional process optimisation methodology demands both time and material. Pulsed sample injection ultrafiltration has been suggested as a rapid process optimisation technique. In the present work the scope of this technique is further extended by "parameter scanning ultrafiltration," which involves continuous change of a process parameter (e.g., pH, salt concentration). The time and material consumption are thus further reduced. The technique was validated using different proteins and membranes. Sieving coefficients at different pH and salt concentration were compared to those obtained in fixed parameter ultrafiltration experiments. As fractionation case studies the separation of monoclonal antibody from bovine serum albumin and separation of human IgG from human serum albumin were examined.     

Studies on Box-Behnken design experiments: cellulose acetate-polyurethane ultrafiltration membranes for BSA separation

Ultrafiltration membranes were prepared from mixtures of cellulose acetate-polyurethane blend membranes. During the last 1 or 2 decades, the concentration purification and separation of Albumin by ultrafiltration through semipermeable membranes have been put into practice and hence membrane separation is considered as the unit operation. The blend solution was prepared from cellulose acetate and polyurethane in polar solvent in presence of polyvinylpyrrolidone as additive. The performance of modified blend membranes applied for Bovine Serum Albumin (BSA) separation by ultrafiltration technique using Box-Behnken design with three variables: additive, time and pressure. Three different levels was studied to identify a significant correlation between the effect of these variables on the amount of separation of BSA. The methodology identifies the principal experimental variables, which have the greatest effect on the separation process. The experimental values are in good agreement with predicted values, the correlation coefficient was found to be 0.9871.     

FURTHER CHEMICAL STUDIES ON BLOOD-AQUEOUS HUMOR DYNAMICS

The proportion of SCN, Br, PO₄, urea, levulose, and Fe which remains freely diffusible when added to plasma has been determined by ultrafiltration and "differential" dialysis through a cellophane membrane. After injecting each of these substances as well as Mg and Li into rabbits a continuous record of their concentration in the plasma was obtained for each animal and the concentration in the aqueous humor was also determined and related to the maximum diffusible concentration in the plasma.     

THE PREPARATION OF THE GRADED COLLODION MEMBRANES OF ELFORD AND THEIR USE IN THE STUDY OF FILTERABLE VIRUSES

1. The method described by Elford for the preparation of graded collodion membranes suitable for ultrafiltration was found to give excellent results, and his findings are fully confirmed. 2. A formula is given for the preparation of collodion from which satisfactory membranes of graded porosity can be prepared. 3. The technique and apparatus used in the preparation, and standardization of membranes are described in detail. 4. The technique and apparatus required for ultrafiltration experiments are described, and some drawbacks encountered in the experiments are discussed. 5. The results of ultrafiltration experiments show that the pores of the membranes are remarkably uniform in size.     

Retention of small charged impurities during ultrafiltration

Ultrafiltration is used to remove small impurities from a variety of processing streams. However, the clearance of small charged impurities may be inadequate due to electrostatic exclusion by the charged ultrafiltration membranes, an effect that has been largely unappreciated. Ultrafiltration experiments were performed to evaluate the transmission of several model impurities with different electrical charge through ultrafiltration membranes having different surface charge characteristics. Highly charged impurities are strongly rejected by charged cellulose and polyethersulfone membranes even though these solutes are much smaller than the membrane pore size. These effects could be eliminated by using high ionic strength solutions to shield the electrostatic interactions. The sieving data are in good agreement with model calculations based on the partitioning of charged spheres into charged cylindrical pores. Guidelines are developed for estimating conditions needed to obtain effective removal of small charged impurities through charged ultrafiltration membranes.     

The use of ultrafiltration for concentration and purification of beta-galactosidase

A possibility of concentration and purification of culture fluid of Escherichia coli by the ultrafiltration technique using Soviet cellulose acetate membranes were studied. It is established that cellulose acetate membranes may be used for purification from low molecular weight protein and concentration of preliminarily purified culture fluid of Escherichia coli. Membranes YAM-300 are most preferable. At the temperature of 18 degrees C, pressure 0.16-0.24 MPa and 20-fold concentration the yield of the enzyme at the ultrafiltration stage was 84.5%.     

Salt-induced changes in plasmid DNA transmission through ultrafiltration membranes

Recent studies have demonstrated the feasibility of using ultrafiltration for the purification of plasmid DNA, but there is still little understanding of the factors governing DNA transmission. Experimental data were obtained for the transmission of a 3.0 kbp supercoiled plasmid DNA through composite regenerated cellulose ultrafiltration membranes as a function of solution ionic environment in a stirred ultrafiltration cell. The dependence on salt concentration was quite dramatic, with the sieving coefficient increasing by more than 80-fold as the NaCl concentration increased from 1 to 150 mM at a fixed filtrate flux. At the same total ionic strength, the sieving coefficient in an MgCl2 solution was significantly larger than that evaluated in NaCl. The sieving results are consistent with independent studies showing a reduction in the effective plasmid size due to salt specific shielding of intramolecular electrostatic interactions. DNA transmission was also a strong function of the filtrate flux, with negligible transmission below a critical value of the flux. The predicted values of the critical filtrate flux determined using a modified elongational flow model were in excellent agreement with the experimental data. These results clearly demonstrate that salt-induced changes in plasmid DNA structure have a significant effect on plasmid DNA transmission through ultrafiltration membranes.     

Anreicherung eines Hefezellwand-lysierenden Enzymgemisches aus Arthrobacter GJM-1

Two methods were employed in order to concentrate a large volume of an extracellular enzyme mixture for lysis of yeast cell walls: ultra-short-time evaporation and ultrafiltration. In the case of ultra-short-time evaporation there was a loss of activity by temperature while by ultrafiltration a good concentration could be received.     

Anomalous osmosis through a model membrane constructed with potassium polystyrenesulfonate solution

It is reported that anomalous osmosis can be observed through liquid membranes which are made by placing a potassium polystyrenesulfonate solution between two inert cellophane membranes. No anomalous osmosis is observed with pure water instead of polyelectrolyte solution.     

Enzyme diffusion from Trichoderma atroviride (= T. harzianum P1) to Rhizoctonia solani is a prerequisite for triggering of Trichoderma ech42 gene expression before mycoparasitic contact

A plate confrontation experiment is commonly used to study the mechanism by which Trichoderma spp. antagonize and parasitize other fungi. Previous work with chitinase gene expression (ech42) during the precontact period of this process in which cellophane and dialysis membranes separated Trichoderma harzianum and its host Rhizoctonia solani resulted in essentially opposite results. Here, we show that cellophane membranes are permeable to proteins up to at least 90 kDa in size but that dialysis membranes are not. ech42 was expressed during the precontact stage of the confrontation between Trichoderma atroviride and its host only if the cellophane was placed between the two fungi. These results are consistent with enzyme diffusion from T. atroviride to R. solani generating the trigger of ech42 gene expression.     

The circumfusion system for multipurpose culture chambers. I. Introduction to the mechanics, techniques, and basic results of a 12-chamber (in vitro) closed circulatory system

A self-contained mechanical system for circulating nutrient fluid through 12 tissue culture chambers is described in detail. This system utilizes nonperforated cellophane membranes in the chambers which separate the circulating nutrient from the tissue culture environments. The nutrient, therefore, is dialyzed through the cellophane of each chamber; some cell products are retained in the microenvironment between the closely apposed cellophane and cover slip, whereas the other cell products move from chamber to chamber in the circulating nutrient. The resultant environmental conditions directed by the circumfusion systems are highly favorable for maintaining the differentiation of chick embryo tissues over protracted periods; a number of micrographs are shown.     

Parameters for the recovery of proteases from surimi wash water.

Proteases are important bioactive compounds that have many applications in food processing. In this study, laboratory scale experiments were performed to establish conditions for recovery of a heat stable, acid protease from Pacific whiting (Merluccius productus) surimi process water. Reduction of proteinaceous solids and recovery of protease activity was maximized when process water was pre-treated with acid (pH 4) followed by heat (60 degrees C). In addition, acid plus heat treatment of process water appeared to improve membrane flux and concentration of protease activity (10-fold) was achieved in half as much time as treatments using acidification but not heat. Neither purification nor concentration of protease was effective using either 300 and 1000 kDa ultrafiltration or 0.3 microm microfiltration membranes. However, concentration of protease using 50 kDa ultrafiltration membranes was successful in recovering about 80% of original protease activity. Results provide conditions for further investigations into pilot plant recovery of protease from surimi process water.     

ULTRAFILTRATION THROUGH COLLODION MEMBRANES

It is obvious that the factors considered in this paper render data obtained by ultrafiltration open to criticism unless they are checked by other methods and precautions are taken for the elimination of the vitiating effects which have been described. As regards the mechanism of ultrafiltration, the view of a sieve-like action as most experimental evidence indicates, is adequate, if all the factors are considered which might modify the effective pore size. The behaviors of collodion membranes which seem contrary to a mechanism of ultrafiltration based on the existence of a system of pores, can be explained on the basis of a variable layer of adsorbed fluid on the walls of the pores. It is, therefore, unsound to make any deductions about living tissues from the demonstration of changes produced in the behavior of collodion membranes. Thus, the increase in the rate of filtration of water through collodion by diuretics (29) or the change of permeability due to the presence of surface-active materials, gives us no information about their action in the living organism. The effect of these substances on a sieve-like membrane of the type of collodion would not necessarily bear any analogy to that exerted on the emulsion type of membrane of living cells. The mechanisms of the reactions necessary to produce the same effects in such widely differing systems may be entirely unrelated.     

Trypsin concentration by ultrafiltration]

Criteria for the selection of membranes and optimal conditions for the trypsin concentration by ultrafiltration through acetylcellulose membranes have been developed. The possibility of a repeated concentration of trypsin by means of these membrances has been shown.     

Separation albumin-PEG: transmission of PEG through ultrafiltration membranes

Transmission of polyethylene glycol (PEG) through ultrafiltration membranes has been studied under various operating conditions of pressure, crossflow, and concentration, using different membranes cut-offs and two module designs with the aim of understanding the separation of PEG from BSA. The influence of protein adsorption and fouling of the choice of a membrane has also been considered. Retention depends in general on the molecule to average pore size ratio, as expected, but also on concentration polarization. Accordingly, all operating and design parameters favoring concentration polarization lead to higher transmission. At high fluxes, flexible macromolecules can pass through the membrane, even if the random coil is larger than the apparent average pore. From a process selectivity point of view, the best way to separate PEG from BSA would be to use a membrane totally retaining BSA and to enhance concentration polarization of PEG. Unfortunately, such conditions also increase fouling and concentration polarization by BSA, which limits flux and thus PEG concentration polarization and transmission. Consequences of such conditions on separation efficiency are discussed. (c) 1993 Wiley & Sons, Inc.     

Efficient Filtration and Sizing of Viruses with Membrane Filters

Untreated membrane filters retain viruses by adsorption, as well as by physical restriction which occurs when the pore diameter of the filter is smaller than that of the virus particle. As originally recommended by Elford, membranes had to be pretreated with proteinaceous material to preclude virus adsorption. However, coating materials that prevent adsorption of certain viruses do not necessarily prevent adsorption of other viruses. In contrast to proteins, salts enhance virus adsorption. Viruses treated with sodium lauryl sulfate to reduce the surface tension, or purified viruses in distilled water, are not adsorbed to membranes. A procedure is recommended by which viruses may be passed through membranes with a porosity twice the diameter of the virus. Such filtrates, which contain 50 to 100% of the initial virus concentration, should be used for sizing viruses by subsequent filtration through smaller pores. The determination of virus size would then be based on the major population of particles in the virus suspension. In the past, as little as 0.1 to 0.001% of the initial virus population was the basis for size determination, because more than 99.9% of the virus was often lost by adsorption to membranes during the clarifying procedures.