Ion exchange immobilization of changed beta-galactosidase fusions for lactose hydrolysis

The use of charged peptides fused to enzymes for immobilization onto ion-exchange membranes was explored for the enzyme x-galactosidase. The additional charged peptides, containing 1, 5, 11, and 16 aspartates, fused to x-galactosidase, for the most part did not interfere with the kinetic behavior for lactose hydrolysis. There was a 2-fold decline in V(m) for the 16-aspartate fusion, but the others were quite similar to the wild type enzyme (BGWT). BGWT and the fusions all retained approximately 50% of their activities when adsorbed onto ion-exchange membranes. In contrast to BGWT, the enhanced binding strength of the 11 aspartate fusion provided the ability to hydrolyze whey permeate at 0.3 M ionic strength without enzyme leakage, and to immobilize the enzyme directly from diluted cell extract with 83% purity. (c) 1994 John Wiley & Sons, Inc.     

Immobilization of beta-galactosidase for application in organic chemistry using a chelating peptide

The strong interaction of hexa-histidine fusion proteins with metal chelate adsorbents was utilized to immobilize beta-galactosidase with a hexa-histidine peptide at the N-terminus to the Ni(2+)-nitrilotriacetic acid adsorbent. The fusion protein was cloned and expressed in Escherichia coli. The purified soluble fusion protein showed the same specific activity as the purified beta-galactosidase and retained 64 percent of its beta-galactosidase activity when bound to the adsorbent. To demonstrate the potential of the immobilized beta-galactosidase in organic chemistry, allyl-beta-D-galactosidase was synthesized from lactose and allyl alcohol on a gram scale. The same enzyme preparation was reused in three subsequent batches to prepare the model compound with high yield. (c) 1993 John Wiley & Sons, Inc.     

A single-cell assay of beta-galactosidase in recombinant Escherichia coli using flow cytometry

A flow cytometric method was developed for the assay of beta-galactosidase in single Escherichia coli cells. A new fluorogenic substrate for beta-galactosidase, C(12)FDG, contains a lipophilic group that allows the substrate to penetrate through cell membranes under normal conditions. When the substrate is hydrolyzed by intracellular beta-galactosidase, a green fluorescent product is formed and retained inside the cell. Consequently, the stained beta-galactosidase-positive cells exhibit fluorescence, which is detected by flow cytometry. This new assay was used to analyze the segregational instability caused by a reduction in specific growth rate of the plasmid-bearing cells in the T7 expression system. Induction results in a substantial accumulation of intracellular beta-galactosidase along with a rapid increase in the fraction of plasmid-free cells. Once the cells lose the plasmid, they no longer produce beta-galactosidase, which is reduced by at least half every generation; thus, after staining, the fluorescent, plasmid-bearing cells can be distinguished from the nonfluorescent, plasmid-free cells using flow cytometry. This article describes the feasibility of the flow cytometric assay for single E. coli cells and reports the optimal assay conditions. A direct relationship between beta-galactosidase activity and green fluorescence intensity was found, and the fractions of recombinant cells in batch cultures were analyzed after various levels of induction.     

Structural comparisons of TIM barrel proteins suggest functional and evolutionary relationships between beta-galactosidase and other glycohydrolases

Beta-galactosidase (lacZ) from Escherichia coli is a 464 kDa homotetramer. Each subunit consists of five domains, the third being an alpha/beta barrel that contains most of the active site residues. A comparison is made between each of the domains and a large set of proteins representative of all structures from the protein data bank. Many structures include an alpha/beta barrel. Those that are most similar to the alpha/beta barrel of E. coli beta-galactosidase have similar catalytic residues and belong to the so-called "4/7 superfamily" of glycosyl hydrolases. The structure comparison suggests that beta-amylase should also be included in this family. Of three structure comparison methods tested, the "ProSup" procedure of Zu-Kang and Sippl and the "Superimpose" procedure of Diederichs were slightly superior in discriminating the members of this superfamily, although all procedures were very powerful in identifying related protein structures. Domains 1, 2, and 4 of E. coli beta-galactosidase have topologies related to "jelly-roll barrels" and "immunoglobulin constant" domains. This fold also occurs in the cellulose binding domains (CBDs) of a number of glycosyl hydrolases. The fold of domain 1 of E. coli beta-galactosidase is closely related to some CBDs, and the domain contributes to substrate binding, but in a manner unrelated to cellulose binding by the CBDs. This is typical of domains 1, 2, 4, and 5, which appear to have been recruited to play roles in beta-galactosidase that are unrelated to the functions that such domains provide in other contexts. It is proposed that beta-galactosidase arose from a prototypical single domain alpha/beta barrel with an extended active site cleft. The subsequent incorporation of elements from other domains could then have reduced the size of the active site from a cleft to a pocket to better hydrolyze the disaccharide lactose and, at the same time, to facilitate the production of inducer, allolactose.     

Optimization of alkyl beta-D-galactopyranoside synthesis from lactose using commercially available beta-galactosidases

Commercially available lactase (beta-D-galactoside galactohydrolase, EC 3.2.1.23) enzymes produced from Kluyveromyces fragilis and Kluyveromyces lactis were accessed as catalysts for use in the production of beta-galactopyranosides of various alcohols using lactose as galactosyl donor. The yield of galactoside was enhanced by using the highest practical concentrations of both lactose and alcohol acceptor. The concentrations and thus yield, were limited by the solubility of the substrates. The increase in galactoside yield with increasing lactose concentration appeared to be specific to the lactose substrate and not due to water activity alterations, because addition of maltose to a fixed concentration of lactose had no effect. During the course of the reaction, the yield of galactoside peaked after around 70% to 80% of the lactose was consumed, due to hydrolysis of the product by the enzyme. A wide variety of compounds with primary or secondary hydroxyl groups could act as acceptors, the essential requirement being at least some water solubility. Addition of organic cosolvents had little effect on galactoside yield except when it increased the water solubility of sparingly soluble alcohols. Some galactosides were synthesized on a gram scale to determine practical product recoveries and improve purification methods for large-scale synthesis. Initial purification by hydrophobic chromatography (for galactosides of hydrophobic alcohols) or strong anion-exchange chromatography (for galactosides of hydrophilic alcohols) separated galactosides, galactobiosides, and higher oligomers from reducing sugars. A facile separation of the galactoside and galactobioside could then be effected by flash chromatography on silica gel. (c) 1993 John Wiley & Sons, Inc.     

Separation of alpha-lactalbumin and beta-lactoglobulin using membrane ultrafiltration

There is considerable commercial interest in the preparation of individual whey proteins as high-value food additives, nutraceuticals, and therapeutics. This study examined the use of membrane filtration for the separation of alpha-lactalbumin and beta-lactoglobulin. Stirred cell filtration experiments were performed using both cellulosic and polyethersulfone membranes to determine the optimal pH, ionic strength, and filtration conditions. Selectivities of greater than 55 could be achieved at pH 5.5 and 50 mM ionic strength using a 30-kD cellulose membrane. A diafiltration process was then designed for the protein separation. A 16-diavolume filtration yielded beta-lactoglobulin as the retentate product with a purification factor of 100 and recovery of 90%. The alpha-lactalbumin was recovered in the filtrate with a purification factor of more than 10 and nearly 99% yield. Model calculations were in good agreement with the experimental data.     

Capture of a recombinant protein from unclarified canola extract using streamline expanded bed anion exchange

The feasibility of applying expanded bed adsorption technology to recombinant protein recovery from extracts of transgenic canola (rapeseed) was assessed. The extraction step results in a suspension of high solids content that is difficult to clarify. The coarse portion of the solids can be removed easily, and our aim was to operate the expanded bed in the presence of the recalcitrant particulates. Recombinant beta-glucuronidase (rGUS) produced in transgenic canola seed was the model system. Diethylaminoethyl (DEAE) and Streamline DEAE resin exhibited similar binding and elution properties for both rGUS and native canola proteins. More than 95% of native canola proteins did not bind to DEAE resins at pH 7.5, whereas the bound proteins were fractionated by two-step salt elution into two groups with the first peak, containing 70% of total bound proteins, at 20 mS/cm, followed by elution of rGUS at 50 mS/cm. The adsorption isotherm was only slightly influenced by the presence of up to 14 mg solids/mL extract; C(m) and K(d) changed by -1% and +39%, respectively. Bed expansion was semiquantitatively predictable from physical properties of the fluid together with Stokes's law and the Richardson-Zaki correlation for both clarified and partially clarified extracts. The presence of 1.4% solids did not change rGUS breakthrough behavior of the expanded bed; however, a small difference between expanded bed and packed bed was observed early in the sample loading stage, during which bed expansion adjusts. Canola solids moved through the column in approximately plug flow with no detriment to bed stability. Seventy-two percent recovery of 34-fold purified rGUS was obtained after initial loading of 1.4% (w/w) solids extract to 25% breakthrough.     

Purification of the two major proteins from whey concentrate using a cation‐exchange selective adsorption process

The packed‐bed adsorption and elution of aqueous solutions of whey concentrate powders were investigated at pH 3.7 using a 5‐mL SP Sepharose FF column to separate and isolate two major proteins namely, α‐lactalbumin (ALA) and β‐lactoglobulin (BLG) from these solutions. ALA displaced and eluted BLG from the column in a pure form. Pure ALA could then be eluted with good recovery. A novel consecutive two‐stage separation process was developed to separate ALA and BLG from whey concentrate mixtures. Almost all of the BLG in the feed was recovered, with 78% being recovered at 95% purity and a further 20% at 86% purity. In addition, 67% of ALA was recovered, 48% at 54% purity and 19% at 60% purity. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Purification and characterization of a thermostable beta-galactosidase from kidney beans (Phaseolus vulgaris L.) cv. PDR14

Using five different steps, beta-Galactosidase has been purified from kidney beans to apparent electrophoretic homogeneity with approximately 90-fold purification with a specific activity of 281 units mg-1 protein. A single band was observed in native PAGE. Activity staining of the native gel with 5-bromo 4-chloro 3-indoxyl beta-D-galactopyranoside (X-Gal) at pH 4.0 also produced a single band. Analytical gel filtration in Superdex G-75 revealed the molecular mass of the native protein to be approximately 75 kD. 10% SDS-PAGE under reducing conditions showed two subunits of molecular masses, 45 and 30 kD, respectively. Hence, beta-galactosidase from kidney beans is a heterodimer. A typical protein profile with lambda max at 280 nm was observed and A280/A260 ratio was 1.52. The N-terminal sequence of the 45 kD band showed 86% sequence homology with an Arabidopsis thaliana and 85% with Lycopersicon esculentum putative beta-galactosidase sequences. The Electrospray Mass Spectrometric analysis of this band also revealed a peptide fragment that had 90% sequence homology with an Arabidopsis thaliana putative beta-galactosidase sequence. The N-terminal sequencing of the 30 kD band as well as mass spectrometric analysis both by MALDI-TOF and ES MS revealed certain sequences that matched with phytohemagglutinin of kidney beans. The optimum pH of the enzyme was 4.0 and it hydrolysed o- and p-nitrophenyl beta-D galactopyranoside with a Km value of 0.63 mmol/L and 0.74 mmol/L, respectively. The energy of activation calculated from the Arrhenius equation was 14.8 kcal/mol enzyme site. The enzyme was found to be comparatively thermostable showing maximum activity at 67 degrees C. Thermal denaturation of the enzyme at 65 degrees C obeys single exponential decay with first order-rate constant 0.105 min-1. Galactose, a hydrolytic product of this enzyme was a competitive inhibitor with a Ki of 2.7 mmol/L.     

Foreign gene expression (beta-galactosidase) during the cell cycle phases in recombinant CHO cells

Recombinant mammalian cultures for heterologous gene expression typically involve cells traversing the cell cycle. Studies were conducted to characterize rates of accumulation of intracellular foreign protein in single cells during the cell cycle of Chinese hamster ovary (CHO) cells transfected with an expression vector containing the gene for dihydrofolate reductase (dhfr) and the lacZ gene for bacterial beta-galactosidase (a nonsecreated protein). The lacZ gene was under the control of the constitutive cytomegalovirus promoter. These normally attachment-grown cells were adapted to suspension culture in 10(-7) M methotrexate, and a dual-laser flow cytometer was used to simultaneously determine the DNA and foreign protein (beta-galactosidase) content of single living cells. Expression of beta-galactosidase as a function of cell cycle phase was evaluated for cells in the exponential growth phase, early plateau phase, and inhibited traverse of the cell cycle during exponential growth. The results showed that the beta-galactosidase production rate is higher in the S phase than that in the G1 or G2/M phases. Also, when cell cycle progression was stopped at the S phase by addition of aphidicolin, beta-galactosidase content in single cells was higher than that in exponential phase or plateau phase cells and increased with increasing culture time. Although the cells did not continue to divide after aphidicolin addition, the production of beta-galactosidase per unit volume of culture was very similar to that in normal exponential growth. (c) 1993 John Wiley & Sons, Inc.     

Fractionation of β‐Lactoglobulin from whey by mixed matrix membrane ion exchange chromatography

Mixed matrix membranes (MMMs), which incorporate adsorptive particles during membrane casting, can be prepared simply and have performances that are competitive with other membrane chromatography materials. The application of MMM chromatography for fractionation of β‐Lactoglobulin from bovine whey is described in this article. MMM chromatography was prepared using ethylene vinyl alcohol polymer and lewatit anion exchange resin to form a flat sheet membrane. The membrane was characterized in terms of structure and its static and dynamic binding capacities were measured. The optimum binding for β‐Lactoglobulin was found to be at pH 6.0 using 20 mM sodium phosphate buffer. The MMM had a static binding capacity of 120 mg/g membrane (36 mg/mL membrane) and 90 mg/g membrane (27 mg/mL membrane) for β‐Lactoglobulin and α‐Lactalbumin, respectively. In batch fractionation of whey, the MMM showed selective binding towards β‐Lactoglobulin compared to other proteins. The dynamic binding capacity of β‐Lactoglobulin in whey solution was about 80 mg/g membrane (24 mg β‐Lac/mL of MMM), which is promising for whey fractionation using this technology. This is the first reported application of MMM chromatography to a dairy feed stream. Biotechnol. Bioeng. 2009;103: 138–147. © 2008 Wiley Periodicals, Inc.     

Discovery of potent and selective inhibitors of 11beta-HSD1 for the treatment of metabolic syndrome

High throughput screening efforts have identified a novel class of dichloroaniline amide 11β-HSD1 inhibitors. SAR studies initiated from dichloroaniline 4 focused on retaining the potency and selectivity profile of the lead.     

Discrimination of outer membrane proteins using machine learning algorithms

Discriminating outer membrane proteins (OMPs) from other folding types of globular and membrane proteins is an important task both for identifying OMPs from genomic sequences and for the successful prediction of their secondary and tertiary structures. In this work, we have analyzed the performance of different methods, based on Bayes rules, logistic functions, neural networks, support vector machines, decision trees, etc. for discriminating OMPs. We found that most of the machine learning techniques discriminate OMPs with similar accuracy. The neural network-based method could discriminate the OMPs from other proteins [globular/transmembrane helical (TMH)] at the fivefold cross-validation accuracy of 91.0% in a dataset of 1,088 proteins. The accuracy of discriminating globular proteins is 88.8% and that of TMH proteins is 93.7%. Further, the neural network method is tested with globular proteins belonging to 30 different folding types and it could successfully exclude 95% of the considered proteins. The proteins with SAM domain such as knottins, rubredoxin, and thioredoxin folds are eliminated with 100% accuracy. These accuracy levels are comparable to or better than other methods in the literature. We suggest that this method could be effectively used to discriminate OMPs and for detecting OMPs in genomic sequences.     

Scaled-up separation of cellobiohydrolase1 from a cellulase mixture by ion-exchange chromatography

Enzymatic hydrolysis of cellulose often involves cellulases produced by Trichoderma reesei, of which cellobiohydrolase1 (CBH1) is the most abundant (about 60% of total cellulases) and plays an important role in the hydrolysis of crystalline cellulose. A method for separating sufficient quantities from the bulk cellulase cocktail is highly desirable for many studies, such as those that aim to characterize binding and hydrolysis kinetics of CBH1. In this work, CBH1 was separated from other Spezyme CP cellulases by ion-exchange chromatography using an efficient modification of a smaller scale process. The ion-exchange column was connected to a vacuum manifold system to provide a steady flow through parallel columns and thus achieve scale-up for enzyme separation. With five 5-mL columns running in parallel, about 55 mg of CBH1 was separated from 145 mg of Spezyme CP in a single separation. Step elution was used to replace the continuous gradient used at smaller scale. The purified CBH1 was collected in the fraction eluted with a buffer containing 0.33 M salt and showed comparable purity and activity as the enzyme purified by a fast protein liquid chromatography system. The stability of separated CBH1 was studied for up to 2 days and good thermal stability was observed. Separated CBH1 also showed both high adsorption to bacterial microcrystalline cellulose with ~4 μmol/g maximum adsorption and a K(a) of 5.55 ± 2.34 μM(-1) , and good hydrolytic activity based on atomic force microscopy observations that show a reduction in fiber height.     

Use of the lacZ reporter gene as an internal control for GUS activity in microprojectile bombarded plant tissue

A protocol is described for simultaneous histochemical detection of LacZ and Gus activity in plant tissues after microprojectile bombardment. The suitability of two different Gus substrates (Salmon-glcA, Magenta-β- -glcA) is compared. This detection system is used to assay the number of cells expressing either or both reporter gene. This technique is used as a qualitative assay to demonstrate the tissue specificity of a Hrgp promoter in maize embryos, and to measure ABA responsiveness of a Lea promoter in Arabidopsis. The promoter to be studied is linked to the gus reporter gene and the lacZ reporter gene linked to the CaMV 35S promoter is used as a constitutive internal control. The use of an internal control drastically reduces the data variation inherent to microprojectile bombardment.     

Architecture of beta-barrel membrane proteins: analysis of trimeric porins.

We have analyzed the known three-dimensional structures of trimeric porins from bacterial outer membranes. The distribution of surface-exposed residues in a direction perpendicular to the membrane is similar to that in helical membrane proteins, with aliphatic residues concentrated in the central 20 A of the bilayer. Outside these residues is a layer of aromatic residues, followed by polar and charged residues. Residues in the trimer interface are more conserved than residues not in the interface. By comparing the interface and noninterface residues, an interface preference scale has been derived that may be used as a basis for predicting interface surfaces in monomer models.     

Catalytic function and affinity purification of site-directed mutant β-cyclodextrin glucanotransferase from alkalophilic Bacillus firmus var. alkalophilus

Subsites −3 and −7 in the active site of β-cyclodextrin glucanotransferase (β-CGTase) from alkalophilic Bacillus firmus var. alkalophilus were modified through site-directed mutagenesis to obtain novel mutant CGTases. Four mutant CGTases, H59Q, Y96M, 90-PPI-92, and Δ(154–160) were constructed and produced using a recombinant E. coli with a secretive expression system extracellularly. The secreted mutant β-CGTases were purified by one-step affinity adsorption chromatography using a β-cyclodextrin (CD) polymer as an adsorbent to nearly homogeneous purity. The catalytic activities were modified significantly compared to the wild-type. In particular, the Y96M and Δ(154–160) mutants increased cyclization activity around 1.5 times without any significant reduction of coupling and hydrolyzing activities. Meanwhile, the Y96M and Δ(154–160) mutants exhibited a much higher conversion yield into CDs from 28.6 to 39% without any recognizable change in the CD ratio. The conversion yield into linear maltooligosaccharides was also significantly reduced. The catalytic functions of subsites −3 and −7 in the active site of β-CGTase would appear to be related to the overall productivity of CDs rather than the product specificity.     

Involvement of BNIP1 in apoptosis and endoplasmic reticulum membrane fusion

BNIP1, a member of the BH3-only protein family, was first discovered as one of the proteins that are capable of interacting with the antiapoptotic adenovirus E1B 19-kDa protein. Here we disclose a totally unexpected finding that BNIP1 is a component of the complex comprising syntaxin 18, an endoplasmic reticulum (ER)-located soluble N-ethylmaleimide-sensitive factor (NSF) attachment protein (SNAP) receptor (SNARE). Functional analysis revealed that BNIP1 participates in the formation of the ER network structure, but not in membrane trafficking between the ER and Golgi. Notably, a highly conserved leucine residue in the BH3 domain of BNIP1 plays an important role not only in the induction of apoptosis but also in the binding of alpha-SNAP, an adaptor that serves as a link between the chaperone ATPase NSF and SNAREs. This predicts that alpha-SNAP may suppress apoptosis by competing with antiapoptotic proteins for the BH3 domain of BNIP1. Indeed, overexpression of alpha-SNAP markedly delayed staurosporine-induced apoptosis. Our results shed light on possible crosstalk between apparently independent cellular events, apoptosis and ER membrane fusion.     

Enhanced beta-galactosidase production by high cell-density culture of recombinant Bacillus subtilis with glucose concentration control

Cell concentration, recombinant protein (beta-galactosidase) level, and the specific enzyme expression level were increased from 19 to 184 g/L, 18.3 to 129 U/mL, and 3.2 to 5.7 U/mg protein, respectively, in fed-batch culture of recombinant Bacillus subtilis when glucose concentration was controlled at 1 g/L as compared with those of conventional fed-batch culture. Glucose concentration of the culture broth was monitored by an automatic on-line glucose analyzer and controlled with a moving identification combined with optimal control (MICOC) strategy. When glucose concentrations were controlled at 10, 1, and 0.2 g/L, accumulated propionic acid concentrations and specific enzyme activities were 18.5, 4.4, and 0.6 g/L and 2.9, 5.7, and 7.1 U/mg protein, respectively. The addition of various concentrations of sodium propionate to the growth medium in batch cultures resulted in a drastic decrease in the growth rate with respect to propionate concentration. The propionic acid was shown to be responsible for cell growth inhibition and enzyme activity reduction in fed-batch culture. (c) 1992 John Wiley & Sons, Inc.