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.     

粘虫中肠α-淀粉酶活性的敏感性研究

研究了不同酶反应缓冲体系、pH值、氯离子浓度以及噁唑哒嗪对5龄2日粘虫 Pseudaletia separata Walker 中肠α－淀粉酶活性的影响。结果表明,乙酸-乙酸钠缓冲体系（pH 5.8）和磷酸氢二钠-磷酸二氢钠缓冲体系（pH 8.0）有利于增强α-淀粉酶活性,比活力最高分别达到4.49和4.97。在乙酸-乙酸钠缓冲体系（pH 5.8）中,5、10、20、40和80 mmol/L氯离子浓度引起α-淀粉酶活性呈现先减弱后增强的变化规律,而在磷酸氢二钠-磷酸二氢钠缓冲体系（pH 8.0）中仅呈现减弱的趋势。1.4 mmol/L噁唑哒嗪对α-淀粉酶活性的抑制率可达70%,但抑制程度随着反应体系中蛋白含量的增加而逐渐降低。     

Investigation of structural changes of β-casein and lysozyme at the gas-liquid interface during foam fractionation

Purification and separation of proteins play a major role in biotechnology. Nowadays, alternatives to multistep operations suffering from low product yields and high costs are investigated closely amidst which one of the promising options is foam fractionation. The molecular behavior at the gas-liquid interface plays an important role in the formation and stabilization of enriched foam. This study for the first time correlates the physico-chemical parameters to the molecular structure in view of protein enrichment during foam fractionation of the two relatively different proteins lysozyme and β-casein employing biophysical techniques such as circular dichroism (CD) spectroscopy and infrared reflection absorption spectroscopy (IRRAS). In case of lysozyme, high enrichment was achieved at pH相似文献   

Effect of invertase on the batch foam fractionation of bromelain

Foam fractionation can be used to enrich a hydrophobic protein such as bromelain from an aerated dilute protein solution because the protein foams. On the other hand, a protein such as invertase, which is hydrophilic, is not likely to foam under similar aerated conditions. While a foam fractionation process may not be approapriate for recovering a hydrophilic protein alone, it is of interest to see how that non-foaming protein affects the foaming protein when the two are together in a mixture. The bromelain enrichment, activity and mass recovery were observed as a function of the solution pH in order to explore how invertase can affect the recovery of bromelain in a foam fractionation process.     

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.     

Continuous foaming for protein recovery: part II. Selective recovery of proteins from binary mixtures

Foam separation may have potential for protein recovery. However, for foam separation to be a viable protein recovery technique it is important to demonstrate, not only that high enrichments and recoveries can be achieved for single proteins, but also that high enrichments and recoveries, together with selectivity of partition, can be achieved for recovery from multi-component mixtures. Most process streams which require purification are indeed complex multi-component mixtures, for example, fermentation broths. In this study, three binary protein mixtures were chosen for continuous foam separation: beta-casein:lysozyme; Bovine serum albumin (BSA):lysozyme and beta-casein:BSA (mixtures 1, 2, and 3, respectively). For each of these mixtures, the expected outcome of each experiment, based on a previous knowledge and determination of relevant protein physical properties, was that the first protein should be preferentially separated into the foam phase. On the basis of results reported in Part I of this study for the continuous foam separation of beta-casein, conditions found to favor maximum enrichment were selected. For each mixture a range of concentrations of both proteins was considered. For mixture 1, maximum protein recoveries in the foam phase were 85.6% and 25% for beta-casein and lysozyme, respectively; and for mixture 2, maximum recoveries of 77. 6% and 18.9% were obtained for BSA and lysozyme, respectively. Maximum enrichment ratios in the foam phase were 79.4 and 2.5 for beta-casein and lysozyme respectively in mixture 1; and 74.0 and 1.4 for BSA and lysozyme respectively in mixture 2. Selective partitioning of beta-casein and BSA into the foam phase was obtained in mixtures 1 and 2, respectively, particularly for protein concentrations at which dilute protein films are known to form at the gas-liquid interface in the foam. Maximum partition ratios for mixtures 1 and 2 were 31.8 and 52.8, respectively. For mixture 3, both BSA and beta-casein were enriched into the foam phase. Maximum enrichments were 42.9 and 24.7 for BSA and beta-casein, respectively; however, selective partitioning in mixture 3 was limited (maximum partition ratio being 1.8).     

Continuous foaming for protein recovery: part I. Recovery of beta-casein

Foam separation is known to have potential for separation of biological molecules with a range of surface activities. A statistical study (factorial design) was carried out to establish the optimum operating conditions for the continuous foam separation of beta-casein. Maximum values of enrichment of beta-casein into the foam phase were found for low levels of initial feed protein concentration, gas flow rate, feed-flow rate, and high foam heights. Maximum values of protein recovery, were generally found at high levels of initial feed protein concentration, gas-flow rate, feed-flow rate, and low foam heights. The highest values obtained for enrichment and separation ratio were 54.7 and 181.3, respectively, with a simultaneous protein recovery of 62%; thus, illustrating the potential effectiveness of this technique. The effect of foaming on protein conformation is also important, and in this study protein structure was analyzed before and after foam separation experiments. Techniques used were: native polyacrylamide gel electrophoresis (PAGE), UV absorbance spectroscopy, circular dichroism, and fluorescence. Native PAGE showed no detectable changes in protein structure. However, absorbance scanning, fluorimetry, and circular dichroism revealed some conformational changes over a range of concentration effects.     

Purification of recombinant α-amylase with immuno-affinity chromatography using monoclonal antibody

A monoclonal antibody against recombinant thermostable α-amylase produced by Escherichia coli was isolated from serum-free medium and immobilized on Sepharose 4B. The adsorption equilibrium between α-amylase and the immobilized immuno-adsorbent showed a Langmuir type isotherm. The breakthrough curve calculated numerically using the averaged volumetric coefficient coincided well with the experimental data. More than 90% of the activity of bound α-amylase could be recovered by eluting with glycine-HCl buffer (pH 2.5). The elution profile at pH 2.5 became sharper with increasing temperature. By using an immuno-affinity column, the recombinant α-amylase produced by E. coli could be purified homogeneously from crude extract enzyme solution with two-step elution.     

Culture conditions for the production of amylolytic enzymes by a thermophilic Clostridium sp.

The growth of a thermophilic Clostridium sp. and the production of α-glucosidase, α-amylase and pullulanase were studied under anaerobic conditions using different carbon and nitrogen sources and varying pH values and temperatures. Growth and enzyme activities were highest with soybean meal as the nitrogen source. The optimum concentration was 2.5% [w/v] for the production of α-amylase as well as pullulanase and 2% [w/v] for α-glucosidase. The best carbon source proved to be soluble starch for α-amylase, and pullulanase and maltose for α-glucosidase. Growth and enzyme production reached their optimum at pH 6.5 to 7.0 and 70°C. Under these conditions, the enzyme activities followed exponential growth with maximum yields of α-glucosidase, α-amylase and pullulanase at 28, 36, and 44 h.     

Effect of solution conditions on protein damage in foam

In this study we investigated the conditions under which protein damage during foaming could be reduced. We used bovine serum albumin (BSA), immunoglobulin G (IgG), pepsin, catalase and lysozyme. The parameters examined were ionic strength, pH, protein concentration and the addition of sugars (trehalose and sucrose). Results showed that protein damage can be reduced by operating at optimal ionic strength and pH, and to a lesser extent, by the addition of sugars. Solution conditions under which the native structure of the protein was stabilised in solution favoured a reduction in the amount of damage, due to lower surface adsorption. The actual quantity of protein damaged in foaming was found to be relatively insensitive to changes in the bulk protein concentration, provided that the concentration was near to, or greater than, the apparent CMC value.     

Molecular dynamics simulation and experimental validation of the effect of pH on protein desorption in hydrophobic charge induction chromatography

The ligands in hydrophobic charge induction chromatography (HCIC) are hydrophobic and ionisable. Thus, the pH is crucial for the separation performance in HCIC, especially for elution. However, it is difficult to obtain the microscopic information in HCIC through experimental means. In this work, molecular dynamics simulations are performed to examine the effect of pH on elution and protein conformational transition in HCIC, using a 46-bead β-barrel coarse-grained model protein and an HCIC adsorbent pore model constructed in an earlier work. Corresponding experiments are carried out for the validation of simulation results, using lysozyme and MEP Hypercel. Both the activities and fluorescence of lysozyme are examined to evaluate the conformational transition. The simulations indicate that the elution efficiency of protein increases with decreasing pH value in a non-linear manner. This is qualitatively consistent with the experimental results. MD simulations indicate that protein unfolding occurs in elution at all pH values. However, the experimental data show that the activity and conformation of lysozyme is independent of pH of the elution buffer. The microscopic information from simulation shows that protein unfolding is mainly observed on the adsorbent surface, but it cannot be detected in the experiments that only probe the proteins in the bulk liquid.     

Partition of protein from binary mixtures by a batch foaming process

An experimental study to assess the partition of 3 binary protein mixtures when foam separated is presented (proteins considered were bovine serum albumin (BSA), conalbumin and lysozyme). Results show that selective partition of protein can be achieved and under certain conditions it is possible to strip the initial solution of BSA. However, purity of the foam phase is limited due to the non-selective carry-up of other proteins in the interstitial liquid.     

The effect of pH on the foam fractionation of beta-glucosidase and cellulase

The surface tension-pH profile of beta-glucosidase was established to determine its relationship to the corresponding profile of cellulase and to the foam fractionation of that cellulase. The goal of this work was to determine the optimal foaming points for both cellulase and cellobiase. This data may prove useful in the separation of certain components of cellulase, since the non-foaming hydrophilic beta-glucosidase does not foam as well as the hydrophobic components of cellulase at low concentrations. A key finding from these experiments was that there are two local minima in the surface tension-pH trajectory for Trichoderma reesei cellulase, as contrasted to the usual single minimum. The lower of these minimum points corresponds to the cellulase isoelectric point. The double minimum surface tension-pH profile was also observed for cellobiase alone. The optimal foaming pH for cellobiase alone was determined to be around 10.5, while for cellulase it was between 6 and 9.     

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。     

Biochemical properties of latices from the Euphorbiaceae

Latex sera from 18 Euphorbia species were surveyed for protein, carbohydrate and total solid contents. Protease, esterase, alkaline and acid phosphatase, N-acetyl-β-glucosaminidase, α-mannosidase, α- and β-galactosidase, α- and β-glucosidase, α-amylase, lysozyme, leucine amino peptidase and cellulase activities were also measured. The effects of nine protease inhibitors were assayed as were haemagglutinating (lectin) contents. Two-dimensional (isoelectric focusing and SDS) PAGE maps of the sera were made. The results obtained show that the latices have widely varying biochemical properties.     

Effects of Group 3 LEA protein model peptides on desiccation-induced protein aggregation

Group 3 late embryogenesis abundant (G3LEA) proteins have amino acid sequences with characteristic 11-mer motifs and are known to reduce aggregation of proteins during dehydration. Previously, we clarified the structural and thermodynamic properties of the 11-mer repeating units in G3LEA proteins using synthetic peptides composed of two or four tandem repeats originating from an insect (Polypedilum vanderplanki), nematodes and plants. The purpose of the present study is to test the utility of such 22-mer peptides as protective reagents for aggregation-prone proteins. For lysozyme, desiccation-induced aggregation was abrogated by low molar ratios of a 22-mer peptide, PvLEA-22, derived from a P. vanderplanki G3LEA protein sequence. However, an unexpected behavior was noted for the milk protein, α-casein. On drying, the resultant aggregation was significantly suppressed in the presence of PvLEA-22 with its molar ratios>25 relative to α-casein. However, when the molar ratio was <10, aggregation occurred on addition of PvLEA-22 to aqueous solutions of α-casein. Other peptides derived from nematode, plant and randomized G3LEA protein sequences gave similar results. Such an anomalous solubility change in α-casein was shown to be due to a pH shift to ca. 4, a value nearly equal to the isoelectric point (pI) of α-casein, when any of the 22-mer peptides was mixed. These results demonstrate that synthetic peptides derived from G3LEA protein sequences can reduce protein aggregation caused both by desiccation and, at high molar ratios, also by pH effects, and therefore have potential as stabilization reagents.     

Purification and Some Properties of Acid-stable α-Amylases from Shochu koji (Aspergillus kawachii)

Aspergillus kawachii α-amylase [EC 3.2.1.1] I and II were purified from shochu koji extract by DEAE Bio-Gel A ion exchange chromatography, Sephacryl S-300 gel chromatography (pH 3.6), coamino dodecyl agarose column chromatography and Sephacryl S-200 gel chromatography. By gel chromatography on a Sephacryl S-300 column, the molecular weights of the purified α-amylase I and II were estimated to be 104,000 and 66,000, respectively. The isoelectric points of α-amylase I and II were 4.25 and 4.20, respectively. The optimal pH range of α-amylase I was 4.0 to 5.0, and the optimum pH of α-amylase II was 5.0. The optimum temperatures of both α-amylases were around 70°C at pH 5.0. Both α-amylases were stable from pH 2.5 to 6.0 and up to 55°C, retaining more than 90% of the original activities. Heavy metal ions such as Hg^{2 +} and Pb^{2 +} were potent inhibitors for both α-amylases.     

Correlation of second virial coefficient with solubility for proteins in salt solutions

In this work, osmotic second virial coefficients (B(22)) were determined and correlated with the measured solubilities for the proteins, α-amylase, ovalbumin, and lysozyme. The B(22) values and solubilities were determined in similar solution conditions using two salts, sodium chloride and ammonium sulfate in an acidic pH range. An overall decrease in the solubility of the proteins (salting out) was observed at high concentrations of ammonium sulfate and sodium chloride solutions. However, for α-amylase, salting-in behavior was also observed in low concentration sodium chloride solutions. In ammonium sulfate solutions, the B(22) are small and close to zero below 2.4 M. As the ammonium sulfate concentrations were further increased, B(22) values decreased for all systems studied. The effect of sodium chloride on B(22) varies with concentration, solution pH, and the type of protein studied. Theoretical models show a reasonable fit to the experimental derived data of B(22) and solubility. B(22) is also directly proportional to the logarithm of the solubility values for individual proteins in salt solutions, so the log-linear empirical models developed in this work can also be used to rapidly predict solubility and B(22) values for given protein-salt systems.     

Studies on α-amylase production by Bacillus licheniformis MIR-61

An acid α-amylase hyperproducing strain, designated as MIR-61, was isolated in a screening procedure from South American soil samples. MIR-61, a 60°C thermoresistant strain, was identified using 98 biochemical and morphological tests and characterized as Bacillus licheniformis by numerical taxonomy. Batch cultures of B. licheniformis MIR-61 showed extracellular α-amylase and α-glucosidase activities during the exponential growth phase. The production of α-amylase was studied at free and constant pH values at 37 and 45°C. Maximum α-amylase activity (4,767 kU/dm³ in a liquid medium) was detected at 45°C at a constant pH (7.0) in the late exponential phase. The α-amylase production by B. licheniformis MIR-61 is 10 to 300 times higher than the enzyme production reported in strains of the same species. Optimum α-amylase activity was found at 50 to 67°C in an acid pH range from 5.5 to 6.0. These properties would allow its use in starch industry processes.     

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.