Single-step chromatography for simultaneous purification of C-phycocyanin and allophycocyanin with high purity and recovery from <Emphasis Type="Italic">Spirulina</Emphasis> (<Emphasis Type="Italic">Arthrospira</Emphasis>) <Emphasis Type="Italic">platensis</Emphasis>

The cyanobacterium Spirulina (Arthrospira) platensis is a good source of phycobiliprotein purification. C-phycocyanin (C-PC) is the major phycobiliprotein, while allophycocyanin (APC) is less abundant in S. platensis. Previously reported methods for C-PC purification are only able to offer either high purity or high efficiency. This paper describes one-step anion exchange chromatography method with continuous pH gradient elution for simultaneous purification of C-PC and APC with high purity and high recovery. Crude C-PC and APC were extracted and concentrated by ammonium sulfate fractionation at saturation of 25% and 60%, then purified on a DEAE-Sepharose Fast Flow chromatography column with continuous pH gradient elution from pH 5.0 to 3.6. After this single-step chromatography, C-PC and APC with high purity and recovery were simultaneously obtained. The purity ratios of C-PC and APC reached 5.59 (A₆₂₀/A₂₈₀) and 5.19 (A₆₅₀/A₂₈₀), respectively. Their purity was further demonstrated by electrophoresis and fluorescence emission spectroscopy. Moreover, the total recovery yield of pure C-PC and APC were 67.04% and 80.0%, representing 111.83 and 29.28 mg·g⁻¹ lyophilized weight, respectively. The obtained C-PC and APC remained stable over a pH range of 4–9. This purification method for high purity and recovery of C-PC and APC proved to be fairly efficient compared with previously reported methods.     

Recovery of a monoclonal antibody from hybridoma culture supernatant by affinity precipitation with Eudragit S-100

An IgG₁ monoclonal antibody (MAB) was isolated from hybridoma culture supernatant by affinity precipitation with an Eudragit S-100-based heterobifunctional ligand. Affinity binding was performed in a homogeneous aqueous phase at pH 7.5 followed by precipitation of the bound affinity complex by lowering the pH to 4.8. After two washing steps, elution of specifically bound MAB was achieved by incubating the precipitate with 0.1 M glycine.HCl pH 2.5. The influence of elution volume and time on the recovery of active MAB and the overall purification factor were studied. The best conditions enabled the recovery of 50.2% of active MAB with a purification factor of 6.2. A further dialysis against 50 mM Tris.HCl pH 8.0 increased the activity yield and the purification factor to 68.4% and 8.3, respectively. This result showed that part of the antibody activity loss during affinity precipitation was due to a reversible inactivation process, being easily recovered after a refining dialysis step.     

Separation and purification of lipase using reverse micellar extraction: Optimization of conditions by response surface methodology

Downstream processing of lipase involving reverse micellar extraction of lipase using cationic surfactant cetyltrimethylammonium bromide (CTAB) was investigated. Effect of various process parameters on both forward and backward extraction of lipase from crude extract was studied to optimize its yield and purity. Complex interaction of salt concentration (0.05∼0.15M), surfactant concentration (0.10∼0.30 M), and pH (6.0∼9.0) for forward extraction, as well as, salt concentration (0.5∼1.5 M) and pH (6.0∼9.0) for backward extraction have been studied using response surface methodology. Optimum processing conditions, namely, salt concentration 0.16M, surfactant concentration 0.20 M, and pH 9.0 for forward extraction, as well as, salt concentration 0.80 M and pH 7.23 for backward extraction, fulfill the conditions to obtain activity recovery of lipase ≥78% and purification factor of lipase ≥4.0. The study demonstrated that response surface methodology can be used for optimization of the conditions for reverse micellar extraction of lipase.     

Expanded bed adsorption as a unique unit operation for the isolation of bacteriocins from fermentation media

Expanded bed adsorption using a strong cation exchanger allowed the direct isolation of amylovorin L471, a bacteriocin from Lactobacillus amylovorusDCE 471, from the fermentation medium. The pH of the loading and elution buffer were optimised in a packed bed with cell-free culture supernatant. Bound bacteriocin was eluted with 1.0 M NaCl. The highest recovery (30%) was obtained at the lowest pH (3.6). At higher pH values the recovery was lower, namely 12%, 15% and 7% at pH 4.5, 6.5 and 8.0, respectively. In expanded bed mode, direct isolation of the bacteriocin from the fermentation medium at pH 3.6 (loading and elution) initially resulted in a recovery of 12%. After optimisation of the pH (loading and elution at pH 3.6 and 6.5, respectively), the recovery for amylovorin L471 increased up to 30% and higher. Recovery of enterocin A from Enterococcus faeciumCTC 492 fermentation medium averaged 15% (loading and elution at pH 3.6 and 6.0, respectively). With pediocin, produced by Pediococcus acidilactici ATCC 8042, 26% recovery was obtained at a pH of 6.5 during loading and elution. Low recoveries can be ascribed to non-optimal operation conditions (pH of loading and elution buffer), inactivation of the bacteriocin on a cationic resin, and the formation of more insoluble and less active, strongly hydrophobic bacteriocin aggregates upon further purification.     

Partial purification properties of human epidermal growth factor from recombinant Escherichia coli by expanded bed adsorption

Human epidermal growth factor is a polypeptide hormone having many diverse biological functions. This paper first presents the recovery results of human epidermal growth factor (hEGF) immediately from the fermentation broth of recombinant Escherichia coli by using an expanded bed system (a couple of STREAMLINE25 and ÄKTA explorer 100). The influences of operational conditions such as linear flow rate, gradient length of NaCl concentration, pH and sample concentration on the purification performances of hEGF in expanded and packed bed modes with STREAMLINE DEAE resin were systematically evaluated. After optimization, the practical recovery procedure in the expanded bed mode was carried out on a scaled-up system under the conditions of linear flow rates of 183 cm/h (upward) and 37 cm/h (downward), sample volume of 300 ml and column bed height of 13.8 cm which yielded a primary product of hEGF from the cell-free supernatant containing hEGF after centrifugation at 4000 rev/min for 15 min. As a result, the hEGF concentration in the product was higher than 20% (w/v), the concentration factor was greater than 4.3 and the total yield was higher than 80%, respectively. At the same time, the results of hEGF recovery by using expanded bed adsorption (EBA), packed bed chromatography (PBC) and salting out were compared. The results show that the procedure of hEGF recovery in expanded bed adsorption has some advantages over the other two procedures, because of its higher concentration factor, recovery yield, productivity, hEGF concentration in the primary product and shorter duration of purification run.     

Silver Nanoparticles as a New Solid-Phase Adsorbent and Its Application to Preconcentration and Determination of Lead from Biological Samples

A new, simple, and fast method for preconcentration and determination of trace amount of lead from biological samples was developed by modified silver nanoparticle-based solid-phase extraction technique and graphite furnace atomic absorption spectrometry. In this study, morin was used as a complexing agent. Some factors influencing the recovery of lead including pH, sample flow rate, type, flow rate, and least amount of the eluent for elution of the lead from silver nanoparticles were studied and optimized. Under the optimum conditions, the detection limit of this method was 68 ng L⁻¹, and the relative standard deviation was 4.1% (n = 10, c = 20 μg L⁻¹). The developed procedure was validated by the analysis of certified reference material and applied to the recovery and determination of lead in biological samples.     

Production and characterization of a collagenolytic serine proteinase by <Emphasis Type="Italic">Penicillium aurantiogriseum</Emphasis> URM 4622: A factorial study

A 2⁴ full factorial design was used to identify the main effects and interactions of the initial medium pH, soybean flour concentration, temperature and orbital agitation speed on extracellular collagenase production by Penicillium aurantiogriseum URM4622. The most significant variables for collagenase production were soybean flour concentration and initial medium pH that had positive main effects, and temperature that had a negative one. Protein concentration in soybean flour revealed to be a significant factor for the production of a collagenase serine proteinase. The most favorable production conditions were found to be 0.75% soybean flour, pH 8.0, 200 rpm, and 28°C, which led to a collagenase activity of 164 U. The enzyme showed an optimum activity at 37°C and pH 9.0, was stable over wide ranges of pH and temperature (6.0 ∼ 10.0 and 25 ∼ 45°C, respectively) and was strongly inhibited by 10 mM phenylmethylsulphonylfluoride. The firstorder rate constants for collagenase inactivation in the crude extract, calculated from semi-log plots of the residual activity versus time, were used in Arrhenius and Eyring plots to estimate the main thermodynamic parameters of thermoinactivation (E* _d = 107.4 kJ/mol and ΔH* _d = 104.7 kJ/mol). The enzyme is probably an extracellular neutral serine collagenase effective on azocoll, gelatin and collagen decomposition.     

Recovery of Nuclease Produced by Lactococcus Lactis Using Expanded Bed Ion Exchange Chromatography

Expanded bed-ionic exchange chromatography (EB-IEC) was used for the recovery and purification of recombinant staphylococcal nuclease secreted by Lactococcus lactis. At the end of the fermentation process, the nuclease activity reached 39 U ml⁻¹. The EB-IEC performances were firstly evaluated with clarified culture broth. The isocratic elution with 0.5 M NaCl led to approximately 80% of nuclease recovery. Proceeding with 3-fold bed expansion resulted in a reduction of the resin capacity by a factor of 32% compared to the process in a packed bed configuration. Simplification of the early purification steps was reached by loading immediately the unclarified culture broth previously diluted to reduce conductivity. Presence of Cells did not affect the chromatography performances resulting in 55-fold purification with the same yield.     

Evaluation of kinetic parameters and mass transfer of glucose-fed granules under hypoxic conditions

This study demonstrated that the availability of oxygen influenc the kinetic parameters of sludge granules for the utilization and mass transfer of substrates. Batch experiments revealed that substrate utilization of the coupled sludge granules followed Monod’s kinetic model under hypoxic conditions and at initial substrate concentrations ranging from 1,350 to 4,456 mg/L. The corresponding kinetic coefficients of ks (maximum specific substrate glucose utilization rate), Ks (half saturation coefficient), and Y (growth yield) were 5.6 ∼ 7.8/day, 58 ∼ 64 mg/L, and 0.11 ∼ 0.17 mg of MLSS/mg of COD, respectively. Low dissolved oxygen content suppressed the activity of aerobic enzymes, which resulted in a ks value between those of aerobic granules and anaerobic granules. The maximum oxygen consumption rate (ko = 0.89/day) was relatively higher while the half-saturation constant (Ko = 1.71 mg/L) was significantly lower than those of aerobic granules. These results imply that dissolved oxygen was used more efficiently under hypoxic conditions. Thiele modulus (ϕ) and effectiveness factor (η) analysis revealed that the activity of microorganisms inside the granules was limited by the availability of oxygen. These properties differed from those found in aerobic granules, anaerobic granules, and activated sludge.     

Isolation and properties of a <Emphasis Type="Italic">levo-</Emphasis>lactonase from <Emphasis Type="Italic">Fusarium proliferatum</Emphasis> ECU2002: a robust biocatalyst for production of chiral lactones

A fungus strain ECU2002, capable of enantioselectively hydrolyzing chiral lactones to optically pure hydroxy acids, was newly isolated from soil samples through two steps of screening and identified as Fusarium proliferatum (Matsushima) Nirenberg. From the crude extract of F. proliferatum ECU2002, a novel levo-lactonase was purified to homogeneity, with a purification factor of 460-folds and an overall yield of 9.7%, by ultrafiltration, acetone precipitation, and chromatographic separation through DEAE-Toyopearl, Butyl-Toyopearl, Hydroxyapatite, Toyoscreen-Super Q, and TSK-gel columns. The purified enzyme is a monomer; with a molecular mass of ca 68 kDa and a pI of 5.7 as determined by two-dimensional electrophoresis. The catalytic performance of the partially purified levo-lactonase was investigated, giving temperature and pH optima at 50°C and 7.5, respectively, for γ-butyrolactone hydrolysis. The substrate specificity of the partially purified lactonase was also examined using several useful lactones, among which α-hydroxy-γ-butyrolactone was the best substrate, with 448-fold higher lactonase activity as compared to γ-butyrolactone. The F. proliferatum lactonase preferentially hydrolyzed the levo enantiomer of butyrolactones, including β-butyrolactone, α-hydroxy-γ-butyrolactone, α-hydroxy-β,β-dimethyl-γ-butyrolactone (pantolactone), and β-hydroxy-γ-butyrolactone, affording (+)-hydroxy acids in high (94.8∼98.2%) enantiomeric excesses (ee) and good conversions (38.2∼44.2%). A simple immobilization of the crude lactonase with glutaraldehyde cross-linking led to a stable and easy-to-handle biocatalyst for catalytic resolution of chiral lactones. The immobilized lactonase also performed quite well in repeated batch resolution of dl-pantolactone at a concentration of 35% (w/v), retaining 67% of initial activity after ten cycles of reaction (corresponding to a half life of 20 cycles) and affording the product in 94∼97% ee, which can be easily enhanced to >99% ee after the d-hydroxy acid was chemically converted into l-lactone and crystallized.     

Overexpression,purification and characterization of a recombinant secretary catalase from <Emphasis Type="Italic">Bacillus subtilis</Emphasis>

A recombinant Bacillus subtilis strain (KN25) was generated for the large-scale preparation of catalase. The B. subtilis katA gene encoding for catalase was cloned into the shuttle vector PRB374, downstream of the constitutively active vegII promoter, followed by transformation of the B. subtilis strain WB600 with the plasmid. The transformant strain, KN25 secretes high levels (3,500 U/ml) of catalase, which facilitates its purification. Three simple purification steps yielded nearly homogeneous catalase, with ∼70% recovery. The purified recombinant catalase has a specific activity of 34,600 U/mg under optimal conditions, and is more resistant to acidic conditions than bovine liver catalase.     

Rapid Affinity Purification Processes for Cyclodextrin Glycosyltransferase from <Emphasis Type="Italic">Bacillus</Emphasis><Emphasis Type="Italic">circulans</Emphasis>

Two rapid and easy-to-scale-up methods for the purification of cyclodextrin glycosyltransferase (CGTase) from Bacillus circulans were developed: affinity precipitation with starch and aqueous two-phase partition. The first method, optimised by a factorial design, gave an 80% CGTase adsorption at 11% starch and 1.6% ammonium sulphate, and a 65% recovery after elution with 10 mM α-cyclodextrin. The purification factor was 17. Aqueous two-phase partition yielded a 72% CGTase recovery in a two-step procedure; CGTase was obtained in the bottom phase with a purification factor of 37.     

External Protons Enhance the Activity of the Hyperpolarization-activated K Channels in Guard Cell Protoplasts of Vicia faba

Hyperpolarization-activated K channels (K _H channels) in the plasmalemma of guard cells operate at apoplastic pH range of 5 to over 7. Using patch clamp in a whole-cell mode, we characterized the effect of varying the external pH between 4.4–8.1 on the activity of the K _H channels in isolated guard cell protoplasts from Vicia faba leaves. Acidification from pH 5.5 to 4.4 increased the macroscopic conductance of the K _H channels by 30–150% while alkalinization from pH 5.5 to 8.1 decreased it only by roughly 15%. The voltage-independent maximum cell conductance, increased by ∼60% between pH 8.1 and 4.4 with an apparent pK _a of 5.3, most likely owing to the increased availability of channels. Voltage-dependent gating was affected only between pH 5.5 and 4.4. Acidification in this range shifted the voltage-dependent open probability by over 10 mV. We interpret this shift as an increase of the electrical field sensed by the gating subunits caused by the protonation of external negative surface charges. Within the framework of a surface charge model the mean spacing of these charges was ∼30 ? and their apparent dissociation constant was 10^−4.6. The overall voltage sensitivity of gating was not altered by pH changes. In a subgroup of protoplasts analyzed within the framework of a Closed-Closed-Open model, the effect of protons on gating was limited to shifting of the voltage-dependence of all four transition rate constants. Received: 26 April 1996/Revised: 29 June 1996     

High-performance liquid chromatography of proteins on deformed nonporous agarose beads. Affinity chromatography of dehydrogenases based on cibacron blue-derivatized agarose

Nonporous agarose beads, prepared by shrinkage and cross-linking in organic solvents, were derivatized with Cibacron Blue F3G-A. A compressed bed of these beads was used for purification of dehydrogenases (glucose-6-phosphate dehydrogenase, lactate dehydrogenase and alcohol dehydrogenase). The chromatographic conditions for the purification of glucose-6-phosphate dehydrogenase were optimized by varying the pH of the buffer; the concentrations of eluting agents, i.e. NADP (specific elution) and sodium chloride (nonspecific elution); flow rate; residence time of the protein on the column bed; and protein load. Specific elution with NADP (2 mM in 0.025 M Tris-HCl, pH 8.0) gave the highest recovery (140%) and highest purification factor (200-fold) of the enzyme. The ability of the compressed bed of nonporous agarose beads to tolerate high flow rates was essential, since the recovery of the enzyme activity increased with an increase in flow rate.     

High-Performance Liquid Chromatography of Proteins on Deformed Nonporous Agarose Beads. Affinity Chromatography of Dehydrogenases Based on Cibacron Blue-Derivatized Agarose

Nonporous agarose beads, prepared by shrinkage and cross-linking in organic solvents, were derivatized with Cibacron Blue F3G-A. A compressed bed of these beads was used for purification of dehydrogenases (glucose-6-phosphate dehydrogenase, lactate dehydrogenase and alcohol dehydrogenase). The chromatographic conditions for the purification of glucose-6-phosphate dehydrogenase were optimized by varying the pH of the buffer; the concentrations of eluting agents, i.e. NADP (specific elution) and sodium chloride (nonspecific elution); flow rate; residence time of the protein on the column bed; and protein load. Specific elution with NADP (2 mM in 0.025 M Tris-HCl, pH 8.0) gave the highest recovery (140%) and highest purification factor (200-fold) of the enzyme. The ability of the compressed bed of nonporous agarose beads to tolerate high flow rates was essential, since the recovery of the enzyme activity increased with an increase in flow rate.     

Efficient two-step chromatographic purification of penicillin acylase from clarified Escherichia coli ultrasonic homogenate

A two-step chromatographic purification procedure from clarified Escherichia coli ultrasonic homogenate was evaluated. The capture step included immobilized metal affinity chromatography with Cu²⁺ as metal ion. Two elution methods were performed: 1 M NH₄Cl and 0.01 M imidazole. Respectively, we obtained a different purification fold (16.5 to 3.15) and a similar result for the recovery of activity (90–99%). The best elution method was chosen for the procedure. The second step, hydrophobic interaction chromatography, gave a 3.8-fold purification with 77.7% of activity. The total procedure gave a 66-fold purification in relation to the initial crude extract with 70% for the recovery of activity and was performed without any conditioning step and at the same pH value.     

Effect of crab shell size on bio-demineralization with lactic acid-producing bacterium, <Emphasis Type="Italic">Lactobacillus paracasei</Emphasis> subsp. <Emphasis Type="Italic">tolerans</Emphasis> KCTC-3074

Demineralization (DM) from crab shell (CS) waste was carried out using a lactic acid-producing bacterium, Lactobacillus paracasei subsp. tolerans KCTC-3074 for 7 days at 25, 30, and 35°C. DM rates were 89∼92% and slightly affected by temperature. DM was also performed for four particle-sized shell samples (0.84∼3.35, 3.35∼10, 10∼20, and 20∼35 mm) with 10% inoculum, 5% shell, and 10% glucose at 30°C and 180 rpm for 7 days. It was found out that the shell size had a slight effect on the rate of DM. Negative relationships were found between DM and residual dry weight (r² = 0.960), and between DM and pH (r² = 0.906). Conversely, positive relationships were found between DM and medium protein (r² = 0.696), and between DM and total titratable acidity (r² = 0.630).     

Inactivation of plasmalemma conductance in alkaline zones of <Emphasis Type="Italic">Chara corallina</Emphasis> after generation of action potential

A microelectrode study with Chara corallina cells has shown that post-excitation changes of membrane potential and plasmalemma resistance, induced by the action potential (AP) generation, differ substantially for cell areas producing zones of high and low external pH. In cell regions producing alkaline zones, the AP generation was followed by post-excitation hyperpolarization by about 50 mV, concomitant with four- to eightfold increase in plasmalemma resistance and a considerable drop of pericellular pH. In the acidic areas the post-excitation hyperpolarization was weak or absent, and the membrane resistance showed no significant increase within 1–2 min after AP. The membrane excitation in the acidic zones was accompanied by a noticeable pH increase near the cell surface, indicative of the inhibition of plasma membrane H⁺ pump. The results suggest that the high local conductance of the plasmalemma is closely related to alkaline zone formation and the depolarized state of illuminated cell under resting conditions. Excitation-induced changes of membrane potential and pH in the cell vicinity were fully reversible, with the recovery period of ∼15 min at a photon flux density of ∼100 μE/(m² s). At shorter intervals between excitatory stimuli, differential membrane properties of nonuniform regions turned smoothed and could be overlooked. It is concluded that the origin of alkaline zones in illuminated Chara cells cannot be ascribed to hypothetical operation of H⁺/HCO₃⁻ symport or OH⁻/HCO₃⁻ antiport.     

An improved method for purification of recombinant truncated heme oxygenase-1 by expanded bed adsorption and gel filtration

Recombinant truncated human heme oxygenase-1 (hHO-1) expressed in Escherichia coli was efficiently separated and purified from feedstock by DEAE-ion exchange expanded bed adsorption. Protocol optimization of hHO-1 on DEAE adsorbent resulted in adsorption in 0 M NaCl and elution in 150 mM NaCl at a pH of 8.5. The active enzyme fractions separated from the expanded bed column were further purified by a Superdex 75 gel filtration step. The specific hHO-1 activity increased from 0.82 ± 0.05 to 24.8 ± 1.8 U/mg during the whole purification steps. The recovery and purification factor of truncated hHO-1 of the whole purification were 72.7 ± 4.7 and 30.2 ± 2.3%, respectively. This purification process can decrease the demand on the preparation of feedstock and simplify the purification process.     

Separation of phycocyanin from <Emphasis Type="Italic">Spirulina platensis</Emphasis> using ion exchange chromatography

This paper presents the evaluation of some important parameters for the purification of phycocyanin using ion exchange chromatography. The influences of pH and temperature on the equilibrium partition coefficient were investigated to establish the best conditions for phycocyanin adsorption. The equilibrium isotherm for the phycocyanin-resin system was also determined. The separation of phycocyanin using the Q-Sepharose ion exchange resin was evaluated in terms of the pH and elution volume that improved the increase in purity and recovery. The highest partition coefficients were obtained in the pH range from 7.5 to 8.0 at 25 degrees C. Under these conditions the equilibrium isotherm for phycocyanin adsorption was well described by the Langmuir model, attaining a Q (m) of 22.7 mg/mL and K (d) of 3.1 x 10(-2) mg/mL. The best conditions for phycocyanin purification using the ion exchange column were at pH 7.5 with an elution volume of 36 mL, obtaining 77.3% recovery and a 3.4-fold increase in purity.