Characterisation of whey proteins of camel (Camelus dromedarius) milk and colostrum

Variation in the composition of whey proteins from camel (Camelus dromedarius) colostrum and milk was recorded over a 192 h period following parturition. Whey proteins were separated by cation-exchange fast protein liquid chromatography and identified by polyacrylamide gel electrophoresis. The main components of whey proteins in camel milk and colostrum were similar to that in bovine, except for the lack in β-lactoglobulin. Serum albumin was the major whey protein present in camel milk, with an average concentration of 10.8 g/l. Camel colostrum was rich in immunoglobulins G, which consist of IgG1, and the enzyme inhibitory antibodies IgG2 and IgG3. The concentration of these proteins decreased rapidly 48 h post partum. Lactophorin (proteose peptone-component 3) and basic whey protein were detected only within 48 h after parturition, reaching a level of 4.9 and 3.1 g/l at 192 h post partum, respectively. The maximum level of lactoferrin (2.3 g/l) was observed at 48 h after parturition. Camel milk and colostrum were shown to be rich in protective proteins, especially IgG2 and IgG3, which revealed to be a potential source of inhibitory antibodies.     

Bovine colostrum fraction as a serum substitute for the cultivation of mouse hybridomas

Summary Fractions of bovine colostrum were prepared and their ability to support the growth of mouse-mouse hybridomas in culture was tested. Whey was prepared from defatted colostrum by removal of casein using acid precipitation. An ultrafiltrate was obtained from cleared whey by filtration through membranes with a nominal molecular mass cut-off of 100 000 Da. Colostrum ultrafiltrate contained 1.16 g/l protein, 0.24 g/l immunoglobulin G (IgG) and less than 0.24 EU (endotoxin unit)/ml endotoxins. The effect of defatted colostrum, whey and ultrafiltrate as serum substitutes was examined by cultivation of hybridoma cells in minimal essential medium containing different concentrations of the supplements. Under optimal conditions in ultrafiltrate-supplemented medium, the maximal cell concentration was 35–40% of that obtained using 10% foetal bovine serum, and IgG production per cell was equal to that achieved using serum. In 1% defatted colostrum the maximum hybridoma concentration was about 30% of that in 10% serum, but at higher concentrations hybridoma growth was significantly reduced. The growth-promoting activity of whey was low. The results show that bovine colostrum ultrafiltrate provides a very attractive alternate to serum for production of monoclonal antibodies. Correspondence to: R. Pakkanen     

Physicochemical and immunochemical studies on bovine IgA and glycoprotein-a

1. Bovine secretory IgA (SIgA) from colostrum (mol. wt. about 410,000) is composed of four alpha-chains (mol. wt. 61,000), four light chains (mol. wt. 23,000) and one molecule of glycoprotein-a (mol. wt. 70,000-86,000). The alpha-chains are antigenically and physicochemically distinct from the heavy chains of IgM, IgG1 and IgG2 while the light chains are identical to those occurring on other bovine immunoglobulins. Glycoprotein-a and bovine free secretory component are identical and the former name should be abolished. Much of this protein is covalently bonded to IgA. 2. The gel filtration behavior of serum IgA suggests it is a dimer. 3. The elution behavior of IgA and SIgA from ion-exchange columns and the solubility characteristic of SIgA in the presence of Zn2+ are similar to those of human and rabbit IgA. 4. The disc electrophoretic behavior of IgA and SIgA are distinct from IgM, dimeric IgG1, 7-S IgG and glycoprotein-a. Dimeric IgG1 (s20,w = 9.5) is abundant in colostrum and is similar in size to SIgA. 5. Bovine IgA shows physicochemical and immunochemical heterogeneity when studied by gel filtration, disc electrophoresis, immunoelectrophoresis and ultracentrifugational analyses. Lacrimal and nasal SIgA possess antigenic determinants absent on colostral SIgA.     

Corticosteroid-binding proteins in human colostrum and milk and rat milk.

A corticosteroid-binding protein was detected in the whey of human colostrum and milk which resembles serum corticosteroid-binding globulin in certain respects: the equilibrium association constants for cortisol and progesterone binding and the apparent molecular size, as determined by Sephadex G-200 chromatography, were similar, and cortisol andd progesterone competed strongly for binding to the same site in each instance. Dexamethasone-binding activity could not be detected. The concentration of corticosteroid-binding protein in the colostrum obtained before parturition is about 0.1 muM; the concentration declines rapidly after parturition to about 0.01 muM. A corticosteroid-binding protein was found, also, in the whey of mature rat milk at levels of about 0.3 muM. This protein resembles rat serum corticosteroid-binding globulin: the equilibrium association constants for cortisol, corticosterone, and progesterone binding, and the apparent molecular size, as determined by Sephadex G-200 chromatography, were similar; the elution behavior of the respective proteins on anion exchange chromatography with DEAE-Sephadex A-50 was similar, also. Identity of the corticosteroid-binding proteins in whey with corticosteroid-binding globulin in serum is not presumed, however. Rat and human whey exhibited very little testosterone- or 17 beta-estradiol-binding activity. It is suggested the corticosteroid-binding proteins may play a significant physiological role in regulating the concentration of the bound and unbound forms of progesterone and cortisol in the fluids bathing the epithelial cells lining the mammary ducts and acini.     

Isolation of lactoperoxidase, lactoferrin, alpha-lactalbumin, beta-lactoglobulin B and beta-lactoglobulin A from bovine rennet whey using ion exchange chromatography

A mild and rapid method is described for isolating various milk proteins from bovine rennet whey. beta-Lactoglobulin from bovine rennet whey was easily adsorbed on and desorbed from a weak anion exchanger, diethylaminoethyl-Toyopearl. However, alpha-lactalbumin could not be adsorbed onto the resin. alpha-Lactalbumin and beta-lactoglobulin from rennet whey could also be adsorbed and separated using a strong anion exchanger, quaternary aminoethyl-Toyopearl. The rennet whey was passed through a strong cation exchanger, sulphopropyl-Toyopearl, to separate lactoperoxidase and lactoferrin. alpha-Lactalbumin and beta-lactoglobulin were adsorbed onto quaternary aminoethyl-Toyopearl. alpha-Lactalbumin was eluted using a linear (0-0.15 M) concentration gradient of NaCl in 0.05 M Tris-HCl buffer (pH 8.5). Subsequently, beta-lactoglobulin B and beta-lactoglobulin A were eluted from the column with 0.05 M Tris-HCl (pH 6.8), using a linear (0.1-0.25 M) concentration gradient of NaCl. The yields were 1260 mg alpha-lactalbumin, 1290 mg beta-lactoglobulin B and 2280 mg beta-lactoglobulin A from 1 l rennet whey.     

Preparation of a high-immunoglobulin product from bovine colostrum

An effective colostrum management programme is the most important factor in determining the health and survival of the neonatal calf. Commercially available colostrum replacers (CR) and colostrum supplements (CS) are an alternative to colostrum on farms that do not have an adequate, high-quality colostrum supply, or those farms that want to prevent transmission of disease from cow to calf. The present study aimed to obtain a high immunoglobulin (Ig), dried bovine colostrum product that could be used as a CR or CS for dairy calves. Dried whey was made from 6 batches of colostrum and an additional 6 batches were used to produce dried whey and curds. Dried whey had higher IgG concentration (P<0.05) and lactose (P<0.05), and less fat (P<0.05) compared to curds or the original colostrum. There was a strong linear relationship between initial colostrum IgG concentration and whey (R² = 0.86) with approximately 0.45 of the initial colostral IgG residing in curd. The high IgG and the composition of colostrum whey powder suggests it could be an effective CS product for use with dairy calves. The high fat and IgG content of the curd by-product indicate that it might be a potential weaning supplement in piglets or even a product for human consumption.     

Purification and characterization of a bovine colostrum-derived growth factor

A growth factor in bovine colostrum was purified to homogeneity by a combination of acid extraction, boiling, cation exchange chromatography, isoelectric focusing, and reverse phase HPLC. The bovine colostrum growth factor (BCGF) had an isoelectric point of about 10, a native mol wt of about 30,000, was resistant to inactivation by boiling and exposure to pH 1, but was inactivated by dithiothreitol. BCGF appeared to be structurally related to human platelet-derived growth factor (PDGF) and competed with human PDGF in a radioreceptor assay. However, while human PDGF appeared to be a heterodimer of 17,000 and 14,000 mol wt subunits, BCGF appeared to be a homodimer of 20,000 mol wt subunits. Purified BCGF had a specific activity in stimulating 3T3 cell proliferation of about 3-6 U/ng and was active at about 1-2 ng/ml.     

Rapid fractionation of bovine transferrin using immobilized gangliosides.

Bovine transferrin (BTF) was fractionated from bovine whey using ganglioside affinity chromatography. After loading the immobilized matrix with a 2% whey solution, the matrix was washed with sodium acetate buffer at pH 4 containing 1 M NaCl before elution of BTF with sodium phosphate buffers at pH 7. Concanavalin-A affinity and ion exchange chromatography were used for further purification. The ganglioside column showed a 74.2% BTF recovery from whey and BTF was enriched to 61% purity with ion exchange chromatography. Bovine transferrin was identified by SDS-PAGE and western analysis. The Concanavalin-A affinity and ion exchange chromatography steps enriched BTF in the samples and removed other whey proteins from ganglioside purified fractions. These results indicate that immobilized ganglioside can be used to fractionate BTF from bovine whey. Our novel ganglioside affinity chromatography is rapid and efficient for the fractionation of BTF from whey.     

Effect of a bovine colostrum whey supplementation on growth performance, faecal Escherichia coli population and systemic immune response of piglets at weaning

This study examined the effect of a bovine colostrum whey supplementation on growth performance, feed intake, faecal Escherichia coli population and systemic immune response of piglets at weaning. A total of 96 piglets weaned at 26 ± 2 days of age were assigned for 4 weeks to one of the two treatments: (1) the control (commercial diet with bovine milk whey powder) and (2) the colostrum (commercial diet with freeze-dried bovine colostrum whey) treatments. The two supplements were incorporated in the diet at a level of 20 g/kg during the first 2 weeks after weaning and lowered to a level of 10 g/kg for the next 2 weeks. BW and feed intake were measured weekly. Faecal E. coli counts were determined weekly on specific culture media. Blood samples were collected weekly and submitted to a cell counter analyser for their main components (red and white blood cells, platelets) and flow cytometry was used to determine the lymphocyte population (B, T, Th and Tc). Finally, total seric immunoglobulin (IgM, IgG and IgA) concentrations were determined by the ELISA method. During the first week of the trial, the piglets from the colostrum treatment had improved average daily gain (170 g/day v. 81 g/day, P < 0.001), average daily feed intake (346 g/day v. 256 g/day, P = 0.03) and feed efficiency (BW gain/feed intake) (0.48 v. 0.31, P = 0.04). The pigs fed the colostrum treatment had also a 25% increase in circulating IgA (P = 0.03) compared with the control treatment the first week. It is concluded that a distribution of bovine colostrum whey (20 g/kg diet) during the first week post-weaning induces a systemic IgA response and has a beneficial action on growth performances and feed efficiency.     

Amino Acid Sequence of αkSubstance,a Mating Pheromone of Saccharomyces kluyveri

A fraction containing IgA (IgA-rich fraction) was prepared from bovine colostrum by anion exchange chromatography using DEAE-Sephadex A-50 and gel filtration on Sephadex G-200. A large amount of IgG1-dimer was found in this fraction, which could not be separated from IgA by repeated gel filtration.

The Fc fragment of bovine colostral IgG (IgG-Fc) was prepared from papain digestion mixtures. IgG-Fc was found to be heterogeneous on DEAE-cellulose column chromatography. Two IgG-Fc fractions were obtained, but no antigenic difference was found between them. Anti-IgG-Fc antibodies raised in rabbits by injection of these Fc preparations reacted only with IgG1 and IgG2. An immunoadsorbent (anti-IgG-Fc-Sepharose) was prepared by coupling these anti-IgG-Fc antibodies to CNBr-activated Sepharose 4B.

IgA was purified from the IgA-rich fraction by affinity chromatography on anti-IgG-Fc-Sepharose adsorbent. IgG1-dimer was effectively removed by this treatment. The purified sample gave only one precipitin arc characteristic of IgA on immunoelectrophoresis with multiple anti-bovine colostral whey antiserum. A small amount of IgA was found to be adsorbed to the affinity column nonspecifically.

When a rabbit was immunized with the purified IgA, besides anti-IgA antibodies, antibodies against the secretory component (SC) were found in the antiserum. This finding leads us to expect that the purified IgA is secretory IgA containing SC.     

以聚乙二醇为层析伴侣同时制备SOD、过氧化氢酶和血红蛋白

发展了一条从红细胞裂解液中同时制备超氧化物歧化酶(SOD)、过氧化氢酶和血红蛋白的新工艺。采用0 75 %的聚乙二醇600作为层析伴侣,使血红蛋白直接流过阴离子交换层析柱,同时吸附SOD和过氧化氢酶。经过梯度洗脱获得SOD和过氧化氢酶组分,再经过疏水性相互作用层析与凝胶过滤层析相串联,使SOD和过氧化氢酶得到纯化。纯化后的SOD和过氧化氢酶的比活力分别达到15932u/mg和65918u/mg ,血红蛋白的纯度达到99.9%以上。总回收率为:SOD ,47.4% ;过氧化氢酶,29.6% ;血红蛋白,88.7%。     

The Interactions of Porcine and Ovine,Serum and Colostral Immunoglobulins with Staphylococcal Protein A

The purpose of these studies was to determine the proportion of each immunoglobulin class/subclass in blood and colostrum of the pig and sheep, which would bind to staphylococcal Protein A. The concentrations of porcine IgG, IgM, and IgA were determined for serum and colostral whey from five sows. Similar measurements were made on two fractions produced by elution of the sample through a Protein A-Sepharose column: fraction 1, immunoglobulins which did not bind to Protein A, and fraction 2, immunoglobulins which bound to Protein A. The concentrations of ovine IgG₁, IgG₂, IgM, and IgA were measured for serum and colostral whey from six ewes, and again similar measurements were made after elution of each ovine sample through Protein A-Sepharose. All classes/subclasses of porcine and ovine serum and colostral immunoglobulins bound to Protein A to some extent. More than 90% of IgG from both porcine colostral whey and serum bound to Protein A. Ovine IgG₁ from most ewes possessed a low affinity for Protein A whereas ovine IgG₂ generally possessed a high affinity; 100% of the IgG₂ in ovine colostral whey samples bound to Protein A. There was remarkable variation between individuals in the binding capacity of porcine IgM and each of the ovine immunoglobulins. For the ovine samples, in particular there were distinct differences between Protein A binding capacity of serum and colostral immunoglobulins of the same class/subclass.     

Isolation and identification of S-adenosylmethionine from human urine

Procedures are described for the isolation and identification of adenosylmethionine from human urine. Previously described preliminary separative procedures using anion and cation exchange columns and an XAD-4 resin column have been extended to permit the separation of adenosylmethionine. The adenosylmethionine has been identified by conversion to methylthioadenosine followed by rechromatography of the latter compound with three different types of columns and elution systems. Mean adenosylmethionine values for urine were as follows: adults, 0.26; children, 0.36 nmole/mumole creatinine. Recovery of adenosylmethionine added to urine and determined by this separative procedure was 52%.     

金属螯合亲和层析分离蛋白质的研究

金属螯合亲和层析是近20年发展起来的一项新型分离技术。它以配基简单、吸附量大、分离条件温和、通用性强等特点,逐渐成为分离纯化蛋白质等生物工程产品最有效的技术之一。本文从单组分蛋白质入手,考查了pH值、铵离子浓度、不同铵盐等对蛋白质洗脱的影响,并进行了分析。还对不同的金属螯合柱和不同性质蛋白质的洗脱性能进行了研究,比较了不同金属离子与蛋白质亲和力的区别,为实际体系的分离研究打下了基础。     

Continuous desalting of refolded protein solution improves capturing in ion exchange chromatography: A seamless process

Truly continuous biomanufacturing processes enable an uninterrupted feed stream throughout the whole production without the need for holding tanks. We have utilized microporous anion and cation exchangers into which only salts, but not proteins, can penetrate into the pores for desalting of protein solutions, while diafiltration or dilution is usually employed for feed adjustments. Anion exchange and cation exchange chromatography columns were connected in series to remove both anions and cations. To increase operation performance, a continuous process was developed comprised of four columns. Continuous mode was achieved by staggered cycle operation, where one set of columns, consisting of one anion exchange and one cation exchange column, was loaded during the regeneration of the second set. Refolding, desalting and subsequent ion exchange capturing with a scFv as the model protein was demonstrated. The refolding solution was successfully desalted resulting in a consistent conductivity below 0.5 mS/cm from initial values of 10 to 11 mS/cm. With continuous operation process time could be reduced by 39% while productivity was increased to 163% compared to batch operation. Desalting of the protein solution resulted in up to 7‐fold higher binding capacities in the subsequent ion exchange capture step with conventional protein binding resins.     

Innovative modular membrane adsorber system for high-throughput downstream screening for protein purification

To develop the most efficient strategy for the purification of proteins, two types of adsorber membrane devices with different functionalities were designed and tested: 8-strips and single spin columns. The most suitable type of membrane adsorber and the optimal chromatographic loading/elution conditions for several target proteins from different biological matrices could be determined simultaneously in microliter scale. Ion exchange (IEX), metal chelate (MC), and Concanavalin A (Con A) modified membrane types were tested in the devices. Bovine serum albumin (BSA) and lysozyme were used as model proteins for investigations of the binding capacity and protein recovery percentage of the 8-strip anion exchange and the cation exchange membrane. The isolation of His(6)-tagged proteins, Bgl-His and GFP-His from fermentation broth and lysate, respectively, was performed using an 8-strip metal chelate affinity membrane loaded with different metal ions. Separation behavior of a ternary protein mixture (BSA, lysozyme, and Bgl-His) was studied in 8-strips IEX and metal chelate membrane chromatography. The Con A affinity devices were developed on the basis of metal chelate membrane spin columns loaded with Cu(2+) ions and investigated using glucose oxidase (GOD) as model protein. In summary, the advantages of the membrane adsorber technology, such as fast processing and easy scale-up, were utilized. The devices made it possible to load the membrane directly with preclarified fermentation broth or cell lysate and separate the protein of interest often in a single step.     

L-谷氨酰胺在强酸性离子交换树脂上的稳定性

研究了谷氨酰胺在强酸性阳离子交换树脂「氢型」上离子交换时的化学稳定性,结果显示,在典型的及所述其他实验条件下,谷氨酰胺相当稳定。典型离交过程：１００ｍｌ去菌体谷氨酰胺发酵液含主要成份谷氨酰胺、谷氨酸和硫酸铵分别为３１２ｍｍｏｌ／Ｌ、６７．０ｍｍｏｌ／Ｌ和０．７５ｍｏｌ／Ｌ,离子交换柱床层体积２００ｍｌ,离交流速１．０ＢＶ／ｈ,０．５ｍｏｌ／Ｌ氨水洗脱流速０．５ＢＶ／ｈ。     

Fractionation of complex protein mixture by virtual three-dimensional liquid chromatography based on combined pH and salt steps

The complexity and diversity of biological samples in proteomics require intensive fractionation ahead of mass spectrometry identification. This work developed a chromatographic method called virtual three-dimensional chromatography to fractionate complex protein mixtures. By alternate elution with different pHs and salt concentrations, we implemented pH and salt steps by turns on a single strong cation exchange column to fully exploit its chromatographic ability. Given standard proteins that were not resolved solely by pH or salt gradient elution could be successfully separated using this combined mode. With a reversed phase column tandem connected behind, we further fractionated as well as desalted proteins as the third dimension. This present strategy could readily be adapted with respect to special complexity of biological samples. Crude plasma without depleting high abundance proteins were fractionated by this three-dimensional mode and then analyzed by reversed phase liquid chromatography coupled with LTQ mass spectrometry. In total, 1933 protein groups with wide dynamic ranges were identified from a single experiment. Some characteristics that correlated to the behavior of proteins on strong cation exchange columns are also discussed.     

离子交换法纯化α-淀粉酶抑制剂

采用离子交换法,利用弱碱性阴离子交换树脂D315吸附小麦粉初提液中的α-淀粉酶抑制剂,对其静态吸附以及洗杂洗脱条件进行研究。通过对静态吸附条件的摸索,得出静态下的最佳工艺条件:上样料液的蛋白质量浓度ρ0=2.5~3.5 mg/mL、pH=8.5~9.5、温度t=30℃、转速150 r/min。最佳洗脱条件:0.1 mol/L NaCl洗杂,0.5mol/L NaCl洗脱。在该条件下,α-淀粉酶抑制剂纯化倍数为4.25倍,收率为64.58%。     

Cathepsin L Causes Proteolytic Cleavage of Chinese-Hamster-Ovary Cell Expressed Proteins During Processing and Storage: Identification,Characterization, and Mitigation

A stochastic approach of copurification of the protease Cathepsin L that results in product fragmentation during purification processing and storage is presented. Cathepsin L was identified using mass spectroscopy, characterization of proteolytic activity, and comparison with fragmentation patterns observed using recombinant Cathepsin L. Cathepsin L existed in Chinese hamster ovary cell culture fluids obtained from cell lines expressing different products and cleaved a variety of recombinant proteins including monoclonal antibodies, antibody fragments, bispecific antibodies, and fusion proteins. Therefore, characterization its chromatographic behavior is essential to ensure robust manufacturing and sufficient shelf life. The chromatographic behaviors of Cathepsin L using a variety of techniques including affinity, cation exchange, anion exchange, and mixed mode chromatography were systematically evaluated. Our data demonstrates that copurification of Cathepsin L on nonaffinity modalities is principally because of similar retention on the stationary phase and not through interactions with product. Lastly, Cathespin L exhibits a broad elution profile in cation exchange chromatography (CEX) likely because of its different forms. Affinity purification is free of fragmentation issue, making affinity capture the best mitigation of Cathepsin L. When affinity purification is not feasible, a high pH wash on CEX can effectively remove Cathepsin L but resulted in significant product loss, while anion exchange chromatography operated in flow-through mode does not efficiently remove Cathepsin L. Mixed mode chromatography, using Capto™ adhere in this example, provides robust clearance over wide process parameter range (pH 7.7 ± 0.3 and 100 ± 50 mM NaCl), making it an ideal technique to clear Cathepsin L. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2732, 2019