Optimizing a rotor‐stator filter matrix for high‐gradient magnetic separation of functionalized magnetic particles

The processing of wines with enzymes is a process chain in which losses of biocatalyst are unavoidable. A promising technique for the minimization of these losses and for the reduction of processing time is the high‐gradient magnetic separation in combination with enzymes, which are immobilized onto functionalized magnetic particles. When magnetizable particles are used and magnetic separation is applied to separate these particles from nonmagnetizable particles and solutes, the enzymes can be recycled and used for several production batches. The magnetic filter used in this study had a filter matrix with concentrically stacked circular rotor and stator plates which are arranged in an alternating order. Different geometries of the filter plate notches were examined to optimize the reproducibility of particle retention. In computational fluid dynamic studies, the influence of the notch geometries on the shear rate generation was analyzed for the rinsing procedure. Separation experiments with an optimized geometry of the filter plates were carried out in water and white wine suspensions.     

Pilot-scale separation of lysozyme from hen egg white by integrating aqueous two-phase partitioning and membrane separation processes

A novel, cost-effective method of lysozyme separation from hen egg white was studied. This method integrates aqueous two-phase partitioning in the system EO₅₀PO₅₀/phosphates with membrane separation processes. The experiments were carried out in a pilot-scale on crude hen egg white.Initially, by forming an aqueous two-phase system, lysozyme was selectively extracted to the upper, polymer-rich phase while the other egg white proteins partitioned to the lower, phosphate-rich phase. Then, in order to recover lysozyme, thermoseparation of polymer-rich phase was applied. A novel approach for the simultaneous thermoseparation of the polymer-rich phase as well as for the recovery of the lysozyme was proposed, using a cross-flow microfiltration. Additionally, recovery of proteins by ultrafiltration from lower, phosphate-rich phase was also investigated.Lysozyme could be obtained after the thermal phase separation by means of microfiltration at a total recovery over the extraction steps of 47.5 and the purification factor of 10.5. The specific activity of lysozyme preparations was 34 188 U/mg of protein. Using cross-flow membrane techniques, it was found that the recovery of the polymer by microfiltration from the top phase was 83.9.     

Development of a novel disposable filter bag for separation of biomolecules with functionalized magnetic particles

The integration of disposable magnetic filters in combination with functionalized magnetic particles represents a fast and cost‐effective alternative for enzyme purification in comparison to solid/liquid separation by means of centrifugation followed by chromatographic purification. The main advantage of the particle‐based process is the solid/solid/liquid separation in one step combined with disposable equipment. Furthermore this combination provides the possibility to also process biocatalytic reactions in cell‐containing media into disposable equipment with preimmobilized enzymes onto the magnetic particles. The focus of the presented study is on the design and performance of a disposable filtration unit consisting of a plastic bag with an inlet and outlet and a stainless steel filter matrix. During magnetic separation, the magnetic particles selectively retard at the filter matrix due to the magnetic force, which counteracts the drag force. It was found that the length of a lengthwise aligned filter matrix should be longer than the magnetic pole surfaces in fluid flow direction. Hereby, a filtration capacity of 5.6 g magnetic particles was measured with a loss of below 0.5%. Introducing a two‐phase flow optimizes the cleaning of the bag after a magnetic filtration. The procedure offered a high cleaning efficiency. Herewith, the cleaned filter unit could be discarded with minimum losses of product and magnet particles.     

Analysis of lysozyme in cheese by immunocapture mass spectrometry

The enzyme lysozyme is used as a preservative to prevent late blowing of ripened cheese, caused by Clostridium tyrobutyricum. Since the enzyme is extracted from hen egg white, lysozyme has to be declared on food product labels as a potential allergen. Here, a method is reported that combines immunocapture purification and matrix-assisted laser desorption/ionization time-of-flight mass spectrometry (MALDI-TOF-MS) analysis for the detection of lysozyme in cheese samples. Cheese extracts were treated with magnetic particles coated with a monoclonal antibody directed against lysozyme. After immunocapture purification, lysozyme was detected by MALDI-TOF-MS. The limit of detection of the assay was about 5 mg/kg lysozyme in cheese. The method reliably distinguished between cheese samples which had been produced with and without lysozyme. Thus, the novel assay allows the reliable, sensitive, and specific detection of lysozyme in a food matrix. The assay could be easily adapted to other target peptides and proteins in complex food matrices and, therefore, has a broad application potential, e.g. for the analysis of allergens.     

Multi‐cycle recovery of lactoferrin and lactoperoxidase from crude whey using fimbriated high‐capacity magnetic cation exchangers and a novel “rotor–stator” high‐gradient magnetic separator

Cerium (IV) initiated “graft‐from” polymerization reactions were employed to convert M‐PVA magnetic particles into polyacrylic acid‐fimbriated magnetic cation exchange supports displaying ultra‐high binding capacity for basic target proteins. The modifications, which were performed at 25 mg and 2.5 g scales, delivered maximum binding capacities (Q_max) for hen egg white lysozyme in excess of 320 mg g^?1, combined with sub‐micromolar dissociation constants (0.45–0.69 µm) and “tightness of binding” values greater than 49 L g^?1. Two batches of polyacrylic acid‐fimbriated magnetic cation exchangers were combined to form a 5 g pooled batch exhibiting Q_max values for lysozyme, lactoferrin, and lactoperoxidase of 404, 585, and 685 mg g^?1, respectively. These magnetic cation exchangers were subsequently employed together with a newly designed “rotor–stator” type HGMF rig, in five sequential cycles of recovery of lactoferrin and lactoperoxidase from 2 L batches of a crude sweet bovine whey feedstock. Lactoferrin purification performance was observed to remain relatively constant from one HGMF cycle to the next over the five operating cycles, with yields between 40% and 49% combined with purification and concentration factors of 37‐ to 46‐fold and 1.3‐ to 1.6‐fold, respectively. The far superior multi‐cycle HGMF performance seen here compared to that observed in our earlier studies can be directly attributed to the combined use of improved high capacity adsorbents and superior particle resuspension afforded by the new “rotor–stator” HGMS design. Biotechnol. Bioeng. 2013; 110: 1714–1725. © 2013 Wiley Periodicals, Inc.     

General Properties of Endo-N-acetylmuramidase of Bacillus subtilis YT-25

The enzymatic behaviour, amino acid composition and some physical properties of a new endo-N-acetylmuramidase (B-enzyme) of Bacillus subtilis YT–25 were determined and compared with hen’s egg white lysozyme. The molecular weight was estimated to be about 13000 by the sedimentation equilibrium method. The isoelectric point was pH 9.8. The amino acid composition indicates that the enzyme is rich in basic amino acids, especially lysin. Maximal activity on the lysis of cell walls of M. lysodeikticus occurred at pH 6.2. The enzyme was stable at pH 3.5 ~ 6.0. The specific activity for the lysis of cell walls of M. lysodeikticus was less than fourth part of that of hen’s egg white lysozyme. Digest of cell walls of M. lysodeikticus with B-enzyme consisted greater numbers of high molecular products than digest with egg white lysozyme. Substrate specificity of B-enzyme seemed to be different from that of egg white lysozyme.     

Lysozyme extraction from hen egg white in an aqueous two-phase system composed of ethylene oxide–propylene oxide thermoseparating copolymer and potassium phosphate

The recovery and purification of lysozyme from hen egg white has been investigated in an aqueous two-phase systems composed of thermoseparating random copolymers of ethylene oxide (EO), propylene oxide (PO) and potassium phosphate. In the primary extraction step lysozyme was satisfactorily partitioned to the top polymer-rich phase in a system composed of 40% (w/w) EO₅₀PO₅₀, 10% (w/w) potassium phosphate, and 0.85 M sodium chloride at pH 9.0, diluted 3-fold with crude egg white, where contaminating proteins were discarded in the bottom phosphate-rich phase. After the primary phase separation the upper EO₅₀PO₅₀ phase was removed and subjected to temperature-induced (65 °C) phase separation, which resulted in the partitioning of pure lysozyme to the top water phase. The separation system was found to be efficient in achieving the purification of lysozyme in a high yield of 85% and specific activity of 32,300 U/mg of protein, with a purification factor of 16.9 and a concentration of lysozyme in the water phase of 2.3 g/l in two extraction steps.     

Separation of lysozyme using superparamagnetic carboxymethyl chitosan nanoparticles

Functionalized Fe(3)O(4) nanoparticles conjugated with polyethylene glycol (PEG) and carboxymethyl chitosan (CM-CTS) were developed and used as a novel magnetic absorbing carrier for the separation and purification of lysozyme from the aqueous solution and chicken egg white, respectively. The morphology of magnetic CM-CTS nanoparticles was observed by transmission electron microscope (TEM). It was found that the diameter of superparamagnetic carboxymethyl chitosan nanoparticles (Fe(3)O(4) (PEG+CM-CTS)) was about 15 nm, and could easily aggregate by a magnet when suspending in the aqueous solution. The adsorption capacity of lysozyme onto the superparamagnetic Fe(3)O(4) (PEG+CM-CTS) nanoparticles was determined by changing the medium pH, temperature, ionic strength and the concentration of lysozyme. The maximum adsorption loading reached 256.4 mg/g. Due to the small diameter, the adsorption equilibrium of lysozyme onto the nanoparticles reached very quickly within 20 min. The adsorption equilibrium of lysozyme onto the superparamagnetic nanoparticles fitted well with the Langmuir model. The nanoparticles were stable when subjected to six repeated adsorption-elution cycles. Separation and purification were monitored by determining the lysozyme activity using Micrococcus lysodeikticus as substrate. The lysozyme was purified from chicken egg white in a single step had higher purity, as determined by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE). Considering that the superparamagnetic nanoparticles possess the advantages of high efficiency, cost-effectiveness and excellent binding of a larger amount of lysozyme and easier separation from the reaction system, thus this type of superparamagnetic nanoparticles would bring advantages to the conventional separation techniques of lysozyme from chicken egg white.     

Affinity adsorption of lysozyme on a macroligand prepared with Cibacron Blue 3GA attached to yeast cells

The objective of this study was the development of affinity adsorbent particles with the appropriate characteristics to be applied in protein purification using the affinity ultrafiltration method. To prepare affinity macroligands Cibacron Blue 3GA, as a ligand molecule, was immobilized by covalent bonding onto yeast cell walls, the support material or matrix. The maximum attachment of the ligand to the matrix was 212 μmol/g (ligand dry weight/yeast dry weight). Lysozyme was selected as the protein model for the adsorption studies. Its adsorption onto the matrix without ligand and matrix with attached ligand were investigated batch-wise. The adsorption equilibrium isotherms appeared to follow a typical Langmuir isotherm. The maximum adsorption capacity (q(m)) of the Cell-Cibacron macroligand for lysozyme was 110 mg/ml of wet macroligand. The adsorbent was also employed for the separation of lysozyme from hen egg white. High purity lysozyme was obtained.     

高速逆流双水相色谱法纯化卵白蛋白

生物大分子的液_固色谱纯化过程中固相载体会产生产物吸附、变性等不良影响。高速逆流色谱无需固相载体 ,且具有高分便率和高回收率的优点 ,其中有机相 水相体系在分离天然产物中应用广泛 ,而应用双水相体系分离生物大分子尚处于研究阶段。双水相高速逆流色谱体系的建立与仪器设备及操作工艺条件密切相关 ,因此利用多分离柱高速逆流色谱仪 ,研究了PEG1000-无机盐双水相体系对标准蛋白质混合物以及卵白蛋白的分离。pH值和PEG浓度对不同种类蛋白质的分配系数影响不同 ,实验发现在pH9.2的150% (W/W)PEG1000 170% (W/W)磷酸钾盐体系中 ,细胞色素C、溶菌酶和肌红蛋白的分配系数差异较大 ,且分布合理 ,因而采用该体系在 0 8mL min流速 ,85 0r min转速的条件下 ,成功分离了细胞色素C、溶菌酶和肌红蛋白的混合物。实验也发现在pH9 2的 16 0 % (W/W)PEG10 0 0 17 0 % (W/W)磷酸钾盐体系中 ,鸡蛋清样品中的主要蛋白质成分:卵转铁蛋白、卵白蛋白和溶菌酶的分配系数差异最大 ,因而采用该体系在 1 8mL min流速、85 0r mi转速的条件下,200min内从鸡蛋清样品中成功分离卵白蛋白,其电泳纯度为100%,收率为95%.     

Development of a 3D‐printed single‐use separation chamber for use in mRNA‐based vaccine production with magnetic microparticles

Laboratory protocols using magnetic beads have gained importance in the purification of mRNA for vaccines. Here, the produced mRNA hybridizes specifically to oligo(dT)‐functionalized magnetic beads after cell lysis. The mRNA‐loaded magnetic beads can be selectively separated using a magnet. Subsequently, impurities are removed by washing steps and the mRNA is eluted. Magnetic separation is utilized in each step, using different buffers such as the lysis/binding buffer. To reduce the time required for purification of larger amounts of mRNA vaccine for clinical trials, high‐gradient magnetic separation (HGMS) is suitable. Thereby, magnetic beads are selectively retained in a flow‐through separation chamber. To meet the requirements of biopharmaceutical production, a disposable HGMS separation chamber with a certified material (United States Pharmacopeia Class VI) was developed which can be manufactured using 3D printing. Due to the special design, the filter matrix itself is not in contact with the product. The separation chamber was tested with suspensions of oligo(dT)‐functionalized Dynabeads MyOne loaded with synthetic mRNA. At a concentration of c_B = 1.6–2.1 g·L^–1 in lysis/binding buffer, these 1 μm magnetic particles are retained to more than 99.39% at volumetric flows of up to 150 mL·min^–1 with the developed SU‐HGMS separation chamber. When using the separation chamber with volumetric flow rates below 50 mL·min^–1, the retained particle mass is even more than 99.99%.     

Purification of the basic protein avidin using Gradiflow technology

The Gradiflow, a preparative electrophoresis instrument, which separates proteins on the basis of charge or size, was used to purify the basic protein avidin, pI 10, from chicken egg white. Using a charge based separation at pH 9.0, the high pI of avidin and lysozyme (pI 10.7) allows them to be easily separated from remaining egg white proteins, as these are the only positively charged proteins. In a second step at pH 10.2, the negatively charged avidin is separated from the positively charged lysozyme. This sequential two-step protocol was complete within 4.5h. Enzyme immunoassay of avidin fractions obtained indicated recoveries of 60-65% from one egg white with minimal lysozyme activity detected.     

Detection of chitinase activity after polyacrylamide gel electrophoresis

Commercial Streptomyces griseus and Serratia marcescens chitinases and purified wheat germ W1A and hen egg white lysozymes were subjected to polyacrylamide gel electrophoresis under native conditions at pH 4.3. After electrophoresis, an overlay gel containing 0.01% (W/V) glycol chitin as substrate was incubated in contact with the separation gel. Lytic zones were revealed by uv illumination with a transilluminator after staining for 5 min with 0.01% (W/V) Calcofluor white M2R. As low as 500 ng of purified hen egg lysozyme could be detected after 1 h incubation at 37 degrees C. One band was observed with W1A lysozyme and several bands with the commercial microbial chitinases. The same system was also used with native polyacrylamide gel electrophoresis at pH 8.9. Several bands were detected with the microbial chitinases. The same enzymes were also subjected to denaturing polyacrylamide gel electrophoresis in gradient gels containing 0.01% (W/V) glycol chitin. After electrophoresis, enzymes were renatured in buffered 1% (V/V) purified Triton X-100. Lytic zones were revealed by uv after staining with Calcofluor white M2R as for native gels. The molecular weights of chitinolytic enzymes could thus be directly estimated. In denaturing gels, as low as 10 ng of purified hen egg white lysozyme could be detected after 2 h incubation at 37 degrees C. Estimated molecular weights of St. griseus and Se. marcescens were between 24,000 and 72,000 and between 40,500 and 73,000, respectively. Some microbial chitinases were only resistant to denaturation with sodium dodecyl sulfate while others were resistant to sodium dodecyl sulfate and beta-mercaptoethanol.     

Development of an eco-friendly antibacterial textile: lysozyme immobilization on wool fabric

Lysozyme, a type of natural enzyme, has been widely used for bacteriostatic functionalization of various materials due to its efficient and selective antibacterial properties. Herein, we report the preparation and characterization of an eco-friendly antibacterial textile based on the immobilization of lysozyme from chicken egg white onto wool fibers. Tris(hydroxymethyl)phosphine (THP) was employed as the cross-linker for the immobilization of lysozyme on the surface of wool fiber. The mechanism of THP cross-linking was investigated via phosphorus test, energy-dispersive spectroscopy (EDX) and Fourier transform infrared spectroscopy (FT-IR). The surface staining, optimization of immobilization parameters, morphology, antibacterial properties, and durability of wool fibers with immobilized lysozyme were also assessed. The results show that hydroxymethyl groups of THP reacted with amino groups of wool fiber and lysozyme through Mannich reaction, which successfully immobilized lysozyme on the wool fiber. The wool fibers incorporated with lysozyme had better antibacterial properties and durability compared with the untreated wool fabric. This facile immobilization approach of lysozyme provides an effective strategy for environmentally benign modification and functionalization of keratin and keratin-containing materials.

     

The influence of molecular variation on protein interactions

We investigated the influence of solvation forces on protein-protein interactions for two forms of lysozyme: hen egg white (HEWL) and turkey egg white (TEWL). Turkey egg white has more surface exposed hydrophobic residues than HEWL and the protein-protein interactions of TEWL are shown to be more attractive than those of HEWL, for the conditions studied. The importance of including a solvation term in the potential of mean force model, to account for molecular variation in protein surface characteristics, is highlighted. We also show that the magnitude of this solvation term can be estimated using readily available data.     

High‐throughput process development of purification alternatives for the protein avidin

With an increased number of applications in the field of the avidin‐biotin technology, the resulting demand for highly‐purified protein avidin has drawn our attention to the purification process of avidin that naturally occurs in chicken egg white. The high‐throughput process development (HTPD) methodology was exploited, in order to evaluate purification process alternatives to commonly used ion‐exchange chromatography. In a high‐throughput format, process parameters for aqueous two‐phase extraction, selective precipitation with salts and polyethylene glycol, and hydrophobic interaction and mixed‐mode column chromatography experiments were performed. The HTPD strategy was complemented by a high‐throughput tandem high‐performance liquid chromatography assay for protein quantification. Suitable conditions for the separation of avidin from the major impurities ovalbumin, ovomucoid, ovotransferrin, and lysozyme were identified in the screening experiments. By combination of polyethylene glycol precipitation with subsequent resolubilization and separation in a polyethylene glycol/sulfate/sodium chloride two‐phase system an avidin purity of 77% was obtained with a yield >90% while at the same time achieving a significant reduction of the process volume. The two‐phase extraction and precipitation results were largely confirmed in larger scale with scale‐up factors of 230 and 133, respectively. Seamless processing of the avidin enriched bottom phase was found feasible by using mixed‐mode chromatography. By gradient elution a final avidin purity of at least 97% and yield >90% was obtained in the elution pool. The presented identification of a new and beneficial alternative for the purification of the high value protein thus represents a successful implementation of HTPD for an industrially relevant purification task. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:957–973, 2015     

Three-dimensional structure of goose-type lysozyme from the egg white of the Australian black swan, Cygnus atratus

The egg white of C. atratus contains two forms of lysozyme, a 'chick-type' which is similar to that found in the egg white of the domestic hen, and a 'goose-type' similar to that found in the egg white of the Embden goose. The molecular structure of the goose-type lysozyme has been determined at a resolution of a 2.8 A by X-ray crystallographic analysis. The structure consists of two domains linked by a long stretch of alpha-helix. In all, there are seven helical segments in the structure. While there is no amino acid sequence homology with either hen egg-white or bacteriophage T4 lysozymes, there are portions of the structure where the folding of the main chain is similar to that found in portions of either hen egg-white lysozyme or T4 lysozyme or both. In particular, there is a consistency of structure in the arrangement of acid groups in the catalytic site. G-o plots calculated for this structure and for the bacteriophage T4 lysozyme structure show that both have similar 'modules' of structure with boundaries occurring at structurally equivalent positions. Three of the common boundaries are equivalent structurally to three of the four module boundaries observed in G-o plots of hen egg-white lysozyme. The variation in the position of the remaining boundary may be related to differences in substrate binding.     

Structural evidence for lack of inhibition of fish goose-type lysozymes by a bacterial inhibitor of lysozyme

It is known that bacteria contain inhibitors of lysozyme activity. The recently discovered Escherichia coli inhibitor of vertebrate lysozyme (Ivy) and its potential interactions with several goose-type (g-type) lysozymes from fish were studied using functional enzyme assays, comparative homology modelling, protein–protein docking, and molecular dynamics simulations. Enzyme assays carried out on salmon g-type lysozyme revealed a lack of inhibition by Ivy. Detailed analysis of the complexes formed between Ivy and both hen egg white lysozyme (HEWL) and goose egg white lysozyme (GEWL) suggests that electrostatic interactions make a dominant contribution to inhibition. Comparison of three dimensional models of aquatic g-type lysozymes revealed important insertions in the β domain, and specific sequence substitutions yielding altered electrostatic surface properties and surface curvature at the protein–protein interface. Thus, based on structural homology models, we propose that Ivy is not effective against any of the known fish g-type lysozymes. Docking studies suggest a weaker binding mode between Ivy and GEWL compared to that with HEWL, and our models explain the mechanistic necessity for conservation of a set of residues in g-type lysozymes as a prerequisite for inhibition by Ivy.     

Primary Structure of Lysozymes from Man and Goose

The primary structure of goose egg white lysozyme seems to be distinct from that of hen egg white and human leukaemia lysozymes.     

Functionalization of whole‐cell bacterial reporters with magnetic nanoparticles

We developed a biocompatible and highly efficient approach for functionalization of bacterial cell wall with magnetic nanoparticles (MNPs). Three Acinetobacter baylyi ADP1 chromosomally based bioreporters, which were genetically engineered to express bioluminescence in response to salicylate, toluene/xylene and alkanes, were functionalized with 18 ± 3 nm iron oxide MNPs to acquire magnetic function. The efficiency of MNPs functionalization of Acinetobacter bioreporters was 99.96 ± 0.01%. The MNPs‐functionalized bioreporters (MFBs) can be remotely controlled and collected by an external magnetic field. The MFBs were all viable and functional as good as the native cells in terms of sensitivity, specificity and quantitative response. More importantly, we demonstrated that salicylate sensing MFBs can be applied to sediments and garden soils, and semi‐quantitatively detect salicylate in those samples by discriminably recovering MFBs with a permanent magnet. The magnetically functionalized cells are especially useful to complex environments in which the indigenous cells, particles and impurities may interfere with direct measurement of bioreporter cells and conventional filtration is not applicable to distinguish and harvest bioreporters. The approach described here provides a powerful tool to remotely control and selectively manipulate MNPs‐functionalized cells in water and soils. It would have a potential in the application of environmental microbiology, such as bioremediation enhancement and environment monitoring and assessment.