泡沫分离技术研究进展

本综述了泡沫分离技术的研究进展,介绍了分离过程中操作参数（气流速度,泡沫区高度,液相高度,温度）,溶液体系性质（进料浓度,pH值,离子强度,表面活性剂种类）,分离设备等因素对分离效果的影响,并介绍了泡沫分离在固体粒子,溶液中的离子分子,废水处理以及生物产品的分离过程中的应用,指出了泡沫分离技术目前存在的问题及发展方向。     

Isolation and purification of protease from human placenta by foam fractionation

The effect of operating parameters like pH, protein concentration, column geometry, and gas flow rate on the separation efficiency of proteolytic enzymes from crude human placental homogenate has been studied in a batch foam column. Purification has been found to be optimum at pH 8.0, close to the isoelectric pH, at which the surface adsorption of the protein on the foam bubbles is maximum. Both purification and recovery varied significantly with total protein concentration. Stable bubble formation was hindered at lower protein concentrations, while extraneous proteins rather than the protease were preferentially adsorbed at higher protein concentrations, decreasing the purification efficiency. Column diameter and column height should be optimized for any specific feed protein concentration and gas flow rate. However, the enrichment ratio was found to decrease with the increase in flow rate. The results indicate that foam fractionation is an effective separation process for recovering valuable biochemicals from biological materials.     

Performance of a continuous foam separation column as a function of process variables

Enrichment and recovery of bovine serum albumin has been examined in a continuous foam separation column. The effects of the operating factors, superficial air velocity, feed flow rate, feed concentration and pH on the above characteristics was investigated. The protein enrichment decreased with the increase in the value of each of these parameters. Protein recovery increased with increasing air velocity, decreased with increasing feed flow rate and did not change very much with increasing feed concentration. Maximum protein recovery was obtained at the isoelectric point (pH 4.8) of the protein. Maximum protein recovery was found to be a strong function of the air velocity in the range 0.05-0.15 cm/s. Further increase in air velocity did not have much effect on recovery because of very large bubbles formed as a result of coalescence. Bubble size was determined as a function of the above factors in the liquid and foam sections of the column. It was found to be dependent on protein concentration, feed flow rate and solution pH. The effect was more significant in the foam section of the column. The bubbles in the foam section were significantly larger (about 3-10 times) than those in the liquid, with a sharp change at the foam-liquid interface. The bubble size measurements were used to calculate the interfacial area and it was shown that the rate of protein removal increases with increasing interfacial area.     

Effect of pH on successive foam and sonic droplet fractionation of a bromelain-invertase mixture

A droplet fractionation method was previously developed to concentrate a dilute nonfoaming protein solution. In that earlier study with invertase, it was demonstrated that droplets created by ultrasonic energy waves could be enriched up to 8 times that of the initial dilute invertase solution. In this study, a mixture of bromelain (a foaming protein) and invertase (a nonfoaming protein) is investigated as a preliminary step to determine if droplet fractionation can also be used to separate a non-foaming protein from foaming proteins. The foaming mixture containing bromelain is first removed by bubbling the binary mixture with air. After the foam is removed, the protein rich air-water interfacial layer is skimmed off (prior to droplet fractionation) so as not to interfere with the subsequent droplet production from the remaining bulk liquid, rich in non-foaming protein. Finally, sonic energy waves are then applied to this residual bulk liquid to recover droplets containing the non-foaming protein, presumed to be invertase. The primary control variable used in this droplet fractionation process is the pH, which ranged for separate experiments between 2 and 9. It was observed that the maximum overall protein partition coefficients of 5 and 4 were achieved at pH 2 and 4, respectively, for the initial foaming experiment followed by the post foaming droplet fractionation experiment.     

Foam fractionation of globular proteins

Foam fractionation of bovine serum albumin (BSA) was studied as a model system for potato wastewater. The effects of feed concentration, superficial gas velocity, feed flow rate, bubble size, pH, and ionic strength on the enrichment and recovery of BSA were investigated in a single-stage continuous foam fractionation column. Enrichments ranged from 1.5 to 6.0 and recoveries from 5 to 85%. The feed concentrations were varied from 0.01 to 0.2 wt %, and enrichments were found to increase with lower feed concentrations. Enrichments also increased with lower superficial gas velocities and larger bubble sizes. At sufficiently low feed flow rates, enrichment was found to increase with an increase in the flow rate, eventually becoming insensitive to the feed flow rate at higher values. The pH was varied from 3.5 to 7.0 and ionic strength from 0.001M to 0.2M. The effects of pH and ionic strength were found to be coupled with bubble size. A minimum bubble size was found at pH 4.8, the isoelectric point of BSA, resulting in a minimum in the enrichment. Bubble size, and thus enrichment, was found to increase as the ionic strength decreased from 0.2M to 0.01M. Previous models(1,2) for the hydrodynamics of foam column were extended for a singlestage continuous foam fractionation column for the prediction of enrichment and recovery. The model assumed adsorption equilibrium, infinite surface viscosity, and bubbles of the same size. Though coalescence was formally accounted for in the model by considering bubble size as a function of foam height, calculations for the experimental runs were performed only for the case of no coalescence. Quantitative predictions of enrichment and recovery could not be made with a single representative bubble size because of the broad inlet bubble size distribution as well as broadening of the distribution as a result of coalescence. The experimental enrichments were higher and recoveries were lower than the model predictions, the discrepancy being more pronounced at lower feed concentrations because of increased coalescence. The higher enrichments are due to the predominant effect of internal reflux as a result of coalescence whereas the lower recoveries are a result of detrimental effects of broadening bubble size distributions.     

Enrichment in axial direction of aqueous foam in continuous foam separation

Estimation of overhead production enrichment in continuous foam separation was conducted with a surfactant: sodium n-dodecylbenzenesulfonate (SDBS) and soluble proteins: ovalbumin (OA) and hemoglobin (HB). Axial profiles of the volumetric flow rate and the concentration of the collapsed foam liquid within the column were measured, and the enrichment ratio and the liquid holdup in axial direction were determined experimentally. The proposed model was fitted to the experimental results obtained with various experimental conditions (superficial gas velocity, feed concentration and pH) and was in reasonable agreement with the experimental data by using the least square regression. The present model makes it possible to estimate the foamate concentration at a desired foam height.     

Contribution of Disulfide Bonds to the Characteristics of Casein Micelles

Drainage in foam was analyzed by the capillary model proposed by Haas and Johnson. Foam was produced by introducing air into an ovalbumin solution through a spinneret. The electric conductivity at selected positions in the foam and the drained liquid height below the foam were measured at constant intervals. The measured electric conductivity was converted to the liquid volume fraction by Prager’s equation. The capillary model described well not only the liquid leakage rate from foam but also the liquid volume fraction in foam. The ratio of the liquid volume fraction in foam to the volume fraction of the Plateau border was much larger than the value estimated from Haas and Johnson’s result. It was confirmed that a time constant, T, involved in the model was suitable for estimating foam stability only by one parameter. However, T is affected not only by material characteristics but also by the foam height. On the other hand, since the ratio of the liquid volume fraction in foam to the volume fraction of the Plateau border reflects the material characteristics, it may be used for comparing the foam stability between materials with the same viscosity and density.     

Submerged Production, Purification, and Crystallization of Acid Carboxypeptidase from Penicillium janthinellum IFO-8070

Penicillium janthinellum IFO-8070 produced an acid carboxypeptidase of molecular weight 51,000 in a liquid medium at 25 C. Maximum enzyme concentration was obtained within 3 to 6 days in a medium containing 2% wheat bran, 1% defatted soybean, and 1% KH(2)PO(4); the initial pH was 2 to 4. When submerged aerobic conditions were used, a 51,000-molecular-weight acid carboxypeptidase was produced and no detectable amounts of 160,000-molecular-weight acid carboxypeptidase were produced. Acid carboxypeptidase with a molecular weight of 51,000 was purified 330-fold from koji culture to yield a crystalline protein which was demonstrated by disc electrophoresis to be homogeneous. The purification method included ammonium sulfate fractionation, Amberlite CG-50 chromatography, acetone fractionation, Amberlite CG-50 rechromatography, and concentration in a collodion bag. The specific activity of the enzyme was about three times more than that of the acid carboxypeptidase from Aspergillus saitoi.     

Rhamnolipids as affinity foaming agent for selective collection of β-glucosidase from cellulase enzyme mixture

Selective and effective separation can potentially be achieved with affinity foam fractionation using simple foaming setup and operation. In this study the use of affinity foam fractionation for selective collection and enrichment of β-glucosidase from a cellulase enzyme mixture was evaluated. Rhamnolipids, a group of glycolipids produced most commonly by Pseudomonas aeruginosa, were used as the affinity foaming agent, because of their foaming property and the presence of dirhamnose moiety (a potential substrate analog for β-glucosidase) in some rhamnolipids. The effects of aeration rate, medium pH, cellulase concentration and rhamnolipid concentration on the foam fractionation performance were examined. Among the pH studied (3.1, 5.0, 7.0 and 9.0), pH 5 was clearly the optimal for selective enrichment of β-glucosidase, presumably corresponding to the high binding affinity between the enzyme and the substrate analog (dirhamnose). With adequate rhamnolipid concentrations (≥0.1 g/L), the aeration rate of 0.1L/min (i.e., 2VVM) for 50 ml test samples was found to give the highest enrichment; higher aeration rates produced wetter foam and, thus, lower (diluted) enzyme activity in the foamate. The enrichment increased with the increasing rhamnolipids-to-cellulase ratio, in the range of 0-2 (w/w) investigated in this study. The finding indicated that rhamnolipids were the limiting compounds in these systems so that the amount of surfactant-enzyme complexes formed and removed into the foam phase would increase when more rhamnolipids were added. At the rhamnolipids-to-cellulase ratio of 2, the β-glucosidase activity in the foamate was about 9 times as high as the activity in the original sample of cellulase mixture and about 17 times the activity in the remaining solution (after foaming). The overall FPU (filter paper unit, a measurement of total cellulase activity) and the activities of endo- and exo-glucanases were only enriched 70-150%. The feasibility of affinity foam fractionation was demonstrated.     

Separation of gentamicin by foaming

In order to develop a more economical separation method and to determine the feasibility of such a method for the recovery of gentamicin from fermentation broth, a foam separation process was evaluated using a batch system. The effects of such process variable as surface-active agent, pH, collector–colligent ratio, and the gas flow rate on the separation efficiency of gentamicin were studied. Form the experimental results, the optimal operating conditions selected were: pH below 9.0, collector-to-colligent ratio of 3, and airflow rate at 0.5 vol air/vol liquid/min. Under these operation conditions, the average recovery efficiency of gentamicin was 73% when sodium dodecyl sylfate was used as a collector. A mathematical expression for the foam separation rate was derived. The theoretically predicted values of separation efficiencies agreed reasonably well with the experimental results.     

Purification of turkey pancreatic phospholipase A2

Turkey pancreatic phospholipase (TPP) has been purified from delipidated pancreases. The purification included ammonium sulfate fractionation, acidic (pH 5) treatment, followed by sequencial column chromatographies on DEAE-cellulose, Sephadex G-75, and reverse phase high pressure liquid chromatography. The purified enzyme was found to be a monomeric protein with molecular mass of 14 kDa. The optimal activity was measured at pH 8 and 37 degrees C using egg yolk emulsion as substrate. Our results show that the enzyme (TPP) was not stable for 1 h at 60 degrees C, and that bile salt and Ca2+ were required for the expression of the purified enzyme. The sequence of the N-terminal amino acids of the purified enzyme shows a very close similarity between TPP and all other known pancreatic phospholipases.     

Purification of Turkey Pancreatic Phospholipase A2

Turkey pancreatic phospholipase (TPP) has been purified from delipidated pancreases. The purification included ammonium sulfate fractionation, acidic (pH 5) treatment, followed by sequencial column chromatographies on DEAE-cellulose, Sephadex G-75, and reverse phase high pressure liquid chromatography. The purified enzyme was found to be a monomeric protein with molecular mass of 14 kDa. The optimal activity was measured at pH 8 and 37°C using egg yolk emulsion as substrate. Our results show that the enzyme (TPP) was not stable for 1 h at 60°C, and that bile salt and Ca²⁺ were required for the expression of the purified enzyme. The sequence of the N-terminal amino acids of the purified enzyme shows a very close similarity between TPP and all other known pancreatic phospholipases.     

Purification and properties of gamma-glutamylcyclotransferase from human erythrocytes.

1. GAMMA-Glutamylcyclotransferase was purified 10000-fold from human erythrocytes. 2. The purification steps involved fractionation with (NH4)(2)SO(4) and chromatography on Sephadex G-75, DEAE-cellulose and hydroxyapatite. The purified enzyme was found to be homogeneous on density-gradient polyacrylamide-gel electrophoresis. 3. The maximum reaction rate was observed at pH9.0 and the apparent Km value for gamma-glutamyl-L-alanine was 2.2mM. 4. The molecular weight (25250) of the purified enzyme agreed well with the value (25500) in fresh haemolysates, indicating no apparent structural modification of the enzyme during purification. However, rapid processing of the blood through the initial (NH4)(2)SO(4) and Sephadex-chromatography steps was required to prevent formation of a high-molecular-weight aggregate with substantially lower specific activity. 5. gamma-Glutamylcyclotransferase catalyses the formation of 5-oxoproline from gamma-glutamyl dipeptides. The role of this enzyme in erythrocytes is of particular interest, because gamma-glutamyl-L-cysteine serves as a substrate for both gamma-glutamylcyclotransferase and glutathione synthetase. Thus the cyclotransferase could modulate glutathione synthesis.     

Flotation for cell recovery from small volumes of yeast cultures

Flotation or cell recovery in foams (proportion of the total cells in the medium transferred to the foam) and flotation efficiency (proportion of the cells transferred from an initial volume of medium equal to the residual volume after flotation) are functions of time, aeration rate, initial volume of medium, and initial concentration of cells. Cell recovery reached constant values (around 96.4 ± 6.3%) and flotation efficiency decreased (owing to increases in the liquid content of the foam), with increases in air flow rate (above 6–7 ml air s^–1) and volumes of medium (above 11 ml) added to the column. Increases in concentration of cells in the medium led to increases in the concentration of cells in the foam.     

A new biochemical engineering approach to the fractional precipitation of proteins

A biochemical engineering framework for optimizing the design and operation of fractional protein precipitation has been developed. The method utilizes a fractionation diagram to represent the purification of a product protein relative to total contaminating protein. The purification factor for a single or double-cut fractional precipitation is obtained as the gradient of an appropriate operating tie-line. A computer algorithm has been devised to maximize the tie-line gradient for a given yield enabling a plot of optimum purification factor versus yield to be constructed. The recovery of the enzyme alcohol dehydrogenase from clarified bakers homogenate using saturated ammonium sulphate has been examined. Fractionation and purification versus yield diagrams were used to investigate the effects of such process parameters as pH, temperature, and initial total protein concentration on fractionation efficiency. The results are discussed in terms of the underlying solubility and mixing phenomena and the industrial application of fractional precipitation.     

Purification and some kinetic properties of catalase from parsley (Petroselinum hortense Hoffm., Apiaceae) leaves

In this study, catalase (CAT: EC 1.11.1.6) was purified from parsley (Petroselinum hortense) leaves; analysis of the kinetic behavior and some properties of the enzyme were investigated. The purification consisted of three steps, including preparation of homogenate, ammonium sulfate fractionation, and fractionation by DEAE-Sephadex A50 ion exchange chromatography. The enzyme was obtained with a yield of 9.5% and had a specific activity of 1126 U (mg proteins)(-1). The overall purification was about 5.83-fold. A temperature of 4 degrees C was maintained during the purification process. Enzyme activity was spectrophotometrically measured at 240 nm. In order to control the purification of the enzyme, SDS-polyacrylamide gel electrophoresis was carried out in 4% and 10% acryl amide for stacking and running gel, respectively. SDS-polyacrylamide gel electrophoresis showed a single band for the enzyme. The molecular weight was found to be 183.29 kDa by Sephadex G-200 gel filtration chromatography. The stable pH, optimum pH, and ionic strength were determined for phosphate and Tris-HCl buffer systems. In addition, K(M) and V(max) values for H(2)O(2), at optimum pH and 25 degrees C, were determined by means of Lineweaver-Burk plots.     

Assay for acetyl-CoA: arylamine N-acetyltransferase by high-performance liquid chromatography applied to serotonin N-acetylation

A specific assay to measure the activity of the enzyme acetyl-CoA:arylamine N-acetyltransferase (EC 2.3.1.5) from pigeon liver is described. The assay is based on the HPLC analysis of N-acetylserotonin formed by the enzymatic reaction. A reversed-phase column (Spherisorb 5-μm ODS 2; 150 × 3.2 mm) eluted with 0.1 M sodium acetate (pH 4.75)/methanol (75:25) permits baseline separation of serotonin and N-acetylserotonin within 5.3 min. Several variables on the enzyme reaction were studied to obtain maximum activity. The enzyme is most active in glycine buffer at pH 9.5. The apparent K_m value for serotonin (at 0.6 mM CoASAc) is 0.246 mM and 9.9 μM for CoASAc (at 1.5 mM serotonin). To avoid acetyl-CoA or N-acetylserotonin consumption in side-reactions, the enzyme was purified. A two-step purification process (ammonium sulfate fractionation and affinity chromatography on immobilised amethopterin) yielded 60–70% of the initial enzyme activity with a purification factor of 455–560.     

Foam fractionation of protein: correlation of protein adsorption onto bubbles with a pH-induced conformational transition

A foam fractionation apparatus was prepared to aid protein separation at the gas–liquid interface. Using lysozyme as a model protein, we investigated the alteration of enzymatic and optical activities through foaming. The lysozyme transferred to the gaseous nitrogen phase after 5 min of bubbling with no exogenous detergent. The bacteriolytic and optical activities of lysozyme from the foamate were nearly equivalent to those of the original lysozyme. This result indicated that lysozyme did not irreversibly denature during foam fractionation. We then performed protein separation using binary mixtures of lysozyme and α-amylase. When the two proteins were dissolved in bulk solution of pH 10.5, which is close to the isoelectric point (pI) of lysozyme (10.7), selective fractionation of lysozyme from the foam was observed. Indeed, this fractionation was identical to that from a single component solution of lysozyme. Similarly, selective fractionation of α-amylase was achieved in pH 3.0 buffer. Furthermore, circular dichroism (CD) and subsequent model fitting revealed that the protein had a reduced or nearly complete absence of α-helical content, whereas the amount of β-sheet structure and random coil was elevated in the buffer conditions that promoted protein adsorption. These results indicate that a pH-induced conformational transition might correlate with protein foaming.     

碱性蛋白酶工程菌发酵条件及重组酶的纯化和性质的研究

在5L发酵罐中对重组碱性蛋白酶工程菌株BP071高产碱性蛋白酶的条件进行了研究,通过提高通气量和改变搅拌转速,BP071可在发酵40 h内达到产酶高峰,酶活力最高可达24480 u/mL。利用快速蛋白液相层析（FPLC）技术,建立了快速高效纯化碱性蛋白酶的方案。发酵液通过硫酸铵沉淀、DEAE-A-50脱色及聚乙二醇浓缩得粗酶,再经过CM-Sephadex-C-50、Sephadex-G-75柱层析后得到了单一组份的重组碱性蛋白酶,酶纯度提高了76.2倍。SDS-PAGE显示重组碱性蛋白酶分子量为28 kD。酶学性质研究表明,酶的最适作用pH为11,最适作用温度为60℃,具有良好的pH稳定性和热稳定性。Ca²⁺、Mg²⁺对酶的稳定性有促进作用,Hg²⁺、Ag⁺、PMFS和DFP能强烈抑制酶的活力。SDS和Urea对酶的活力无影响。     

On the denaturation of enzymes in the process of foam fractionation

Experimental study on the denaturation of enzyme during the separation by foaming was conducted with trypsin and catalase in aqueous medium as model system respectively. The effects of operating pH and sparging gas composition on the denaturation of an enzyme were examined respectively. The oxidative deactivation of enzyme at the gas-liquid interface was identified, which could be reduced by applying nitrogen or carbon dioxide as sparging gas. At suitable conditions, the loss of enzyme activity can be reduced to less than 10% in case of trypsin and to zero in case of catalase. With its proven mildness and effectiveness, foam fractionation in a loop bubble column is applicable for recovery and concentration of enzymes from aqueous solutions.