Production of alkaline protease by Bacillus licheniformis in an aqueous two-phase system

Alkaline protease production by Bacillus licheniformis was studied in an aqueous two-phase system composed of 5% (w/w) polyethylene glycol 6000 (PEG 6000) and 5% (w/w) dextran T500. The top phase was continuous and rich in PEG while the bottom phase was dispersed and rich in dextran. The cells were retained in the bottom phase and at the interface. The two-phase system produced less enzyme in total amount than the control in the early phase, but after 50 h the enzyme produced in the control system decreased while the aqueous two-phase system continued its production and finally the total enzyme activity reached 1.3 times that of the control culture. In order to improve the productivity of protease, repeated batch cultivation were successfully carried out four times by optimizing the top phas composition of freshly added media, which resulted in 13.8, 35.9, 27.8 and 34.7 units ml⁻¹ h⁻¹ of protease based on the amounts of replaced top phases, respectively.     

Control of autolysis of Bacillus subtilis for selective production of the intracellular enzyme glucose-6-phosphate dehydrogenase in aqueous two-phase systems

A method for the release of intracellular enzyme by autolysis of Bacillus subtilis cells is presented. Both the growth and lysis processes were further applied to aqueous two-phase systems (ATPS). Lysis induced by the addition of Triton X-100 and by low-temperature treatment facilitated the release of cytoplasmic enzyme glucose-6-phosphate dehydrogenase (G6PDH) in ATPS. The release selectivity increased when lysis was regulated by the addition of 50 μM or 100 μM Triton X-100. Cardiolipin efficiently inhibited the autolytic process. Control of the autolytic system promoted the selective release of G6PDH. B. subtilis cells could be grown and lysed in aqueous two-phase systems in a similar fashion to the conventional single-phase medium solutions. The released enzymes were partitioned according to their surface properties. G6PDH were extracted to the top phase in a PEG1540/Dex100K-200K sytem. Cells were partitioned to the bottom phase or the interface, and could be recycled into the fermentor. The selectivity of enzyme production was also increased in two-phase systems by the addition of cardiolipin.     

Extractive fermentation for enhanced gellan-hydrolysing enzyme production by Bacillus thuringiensis H14

A new extractive fermentation process using PEG and potassium phosphate aqueous two-phase system (ATPS) was developed for enhanced production of gellan-hydrolysing enzyme by Bacillus thuringiensis H14. Five different Bacillus sp. were tested for their ability to synthesize gellan-hydrolysing enzyme. Bacillus thuringiensis H14 was found to be the best organism for gellan-hydrolysing enzyme production. The enzyme showed maximum activity at pH 7.5 and 40 °C. The partition studies of gellan-hydrolysing enzyme in the system using PEG X (X = 9000, 6000, 4000) and potassium phosphate–water and PEG–sodium citrate–water system indicated at PEG (4000)– potassium phosphate–water is the best system for partitioning of gellan-hydrolysing enzyme into the PEG phase (K = 4.99). Gellan-hydrolysing enzyme production by Bacillus thuringiensis H14 was studied in ATPSs composed of PEG X (X = 9000, 6000, 4000) and potassium phosphate. The top phase is continuous and rich in PEG while the bottom phase is dispersed and is rich in phosphate, microbial cells being mainly retained in the bottom phase. The gellan-hydrolysing enzyme produced during fermentation partitioned into the upper PEG phase and total gellan-hydrolysing enzyme produced was 2.12, 2.29 and 2.40 times higher than that of homogeneous fermentation when the fermentations were carried out using PEG 9000–potassium phosphate–water, PEG 6000–potassium phosphate–water, PEG 4000–potassium phosphate–water systems respectively.     

Aqueous two-phase system formed by thermoreactive vinyl imidazole/vinyl caprolactam copolymer and dextran for partitioning of a protein with a polyhistidine tail

A new type of aqueous two-phase system (ATPS) has been developed for application combining two attractive concepts in downstream processing: the immobilised metal affinity partitioning and the use of thermoprecipitating polymers. ATPS consisting of the thermoprecipitating copolymer of N-vinyl caprolactam/1-vinyl imidazole loaded with Cu ions (Cu-poly-VI-VCL) in the top phase and dextran T70 in the bottom phase was used for purification of recombinant lactate dehydrogenase carrying an affinity tag of 6 histidine residues (His-LDH ) from a crude E. coli extract. The enzyme partitioned preferentially into the top Cu-poly-VI-VCL-rich phase. After phase separation, the latter was mixed with EDTA. Temperature increase to 45°C resulted in thermoprecipitation of VCL/VI-polymer, which could subsequently be recycled. His-LDH remained solubilized in the aqueous phase resulting in 8-fold purification and 80 % recovery in a single step.     

α-amylase production in aqueous two-phase systems with Bacillus subtilis

The production of α-amylase (1,4-α-d-glucan glucanohydrolase, EC 3.2.1.1) by Bacillus subtilis has been studied in repeated batch fermentations in aqueous two-phase systems. In a phase system composed of PEG 600, 8% (w/w), PEG 3350, 5% (w/w)/Dextran T 500, 2% (w/w), 82% of the enzyme partitioned to the top phase. The enzyme concentration in the top phase reached 0.85–1.35 U ml^?1 during the fermentations compared with 0.58 U ml^?1 in the reference fermentation. In the phase system composed of PEG 3350, 9% (w/w)/Dextran T 500, 2% (w/w), 73% of the enzyme partitioned to the top phase. However, the enzyme concentration in this phase system reached only 0.35 U ml^?1 in the top phase. The bacterial cells were microscopically observed to partition totally to the bottom phase in the aqueous two-phase system used. The results are discussed in relation to recirculation of cells by immobilizing to a solid matrix. Extraction of the product to the top phase and the effect of the phase polymers, especially PEG, on the production are also discussed.     

Enhanced production of Trichoderma reesei endoglucanases and use of the new cellulase preparations in producing the stonewashed effect on denim fabric

Trichoderma reesei strains were constructed for production of elevated amounts of endoglucanase II (EGII) with or without cellobiohydrolase I (CBHI). The endoglucanase activity produced by the EGII transformants correlated with the copy number of the egl2 expression cassette. One copy of the egl2 expression cassette in which the egl2 was under the cbh1 promoter increased production of endoglucanase activity 2.3-fold, and two copies increased production about 3-fold above that of the parent strain. When the enzyme with elevated EGII content was used, an improved stonewashing effect on denim fabric was achieved. A T. reesei strain producing high amounts of EGI and -II activities without CBHI and -II was constructed by replacing the cbh2 locus with the coding region of the egl2 gene in the EGI-overproducing CBHI-negative strain. Production of endoglucanase activity by the EG-transformant strain was increased fourfold above that of the host strain. The filter paper-degrading activity of the endoglucanase-overproducing strain was lowered to below detection, presumably because of the lack of cellobiohydrolases.     

Semicontinuous cellulase production in an aqueous two-phase system with Trichoderma reesei rutgers C30

Cellulases [see 1,4(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] from Trichoderma reesei, Rutgers C30, can be semicontinuously produced in an aqueous two-phase system composed of dextran and poly(ethylene glycol) using Solka Floc BW 200 as substrate. When substrate was intermittently added along with fresh top phase, which replaced the withdrawn top phase containing the produced enzymes, a yield of 1740 U endo-β-d-glucanase/g cellulose and 59.3 FPU/g cellulose was extracted with the top phase. Without fresh substrate added, a yield of 3920 U endo-β-d-glucanase/g cellulose and 127.7 FPU/g cellulose was extracted after five runs.     

内切葡聚糖酶高产菌株的诱变选育

【目的】建立里氏木霉(Trichoderma reesei)高产突变菌株的快速筛选方法,选育出高产内切葡聚糖酶的突变株。【方法】对里氏木霉T306菌株的初筛培养基进行优化,建立快速筛选方法;通过紫外诱变手段选育内切葡聚糖酶高产突变菌株,并对突变菌株的产酶培养基进行优化。【结果】在初筛培养基中添加浓度为0.1%(W/V)的乳糖、蛋白胨及脱氧胆酸钠有利于菌株的筛选。诱变后筛选出菌落形态发生明显变化的内切葡聚糖酶高产突变株0516,其羧甲基纤维素酶活力(CMC酶)较出发菌株提高了38.9%。其产酶培养基经优化后,得到最适碳、氮源分别为:乳糖1.50%、硫酸铵0.14%、尿素0.05%、蛋白胨0.10%,优化后CMC酶活力达64.2 U/mL,较优化前提高了2.3倍。【结论】建立了里氏木霉高产突变菌株的快速筛选方法,通过紫外诱变育种获得了产内切葡聚糖酶能力高且遗传稳定的突变株0516。     

Type-specific separation of animal cells in aqueous two-phase systems using antibody conjugates with temperature-sensitive polymers.

A new type of aqueous two-phase system (ATPS) has been developed in which a temperature-sensitive polymer, poly-N-isopropylacrylamide [poly (NIPAM)] was used as a ligand carrier for the specific separation of animal cells. Monoclonal antibodies were modified with itaconic anhydride and copolymerized with N-isopropylacrylamide, and the ligand-conjugated carriers were added to the polyethylene glycol 8000-dextran T500 aqueous two-phase systems. The antibody-polymer conjugates were partitioned to the top phase in the absence or presence of 0.15 M NaCl. When ligand-conjugated carriers were used, more than 80% of the cells were specifically partitioned to the top phase in the presence of NaCl up to 0.1 M. The cells were partitioned almost completely to the bottom phase at 0.1 M NaCl or above, when no antibody-conjugate was added in the ATPS. As a model system, CD34-positive human acute myeloid leukemia cells (KG-1) were specifically separated from human T lymphoma cells (Jurkat) by applying anti-CD34 conjugated with poly-N-isopropylacrylamide in the aqueous two-phase system. By the temperature-induced precipitation of the polymer, about 90% of the antibody-polymer conjugates were recovered from the top phase, which gave approximately 75% cell separating efficiency in the next cycle of reuse.     

Biodegradation of cellulose in novel recyclable aqueous two-phase systems with water-soluble immobilized cellulase

Aqueous two-phase systems (ATPS) are an attractive technology in bioseparation engineering. However, one key problem is that phase-forming copolymer could not be recycled efficiently. This results in high cost and environmental pollution. In this study, we have developed recyclable aqueous two-phase systems composed by pH-response copolymer P_MDB and thermo-response copolymer P_NB and have carried out biodegradation of cellulose in the ATPS. The phase-forming copolymers could be recycled with over 95.0% recovery. In the systems, cellulase was immobilized on pH-response copolymer P_MDB by using 1-ethyl-3-(3-dimethyllaminopropyl)-carbodiimide hydrochloride as cross-linker, and optimized partition coefficient of product was 3.68. Insoluble substrate and immobilized enzyme were biased in bottom phase, while product was partitioned in top phase. Microcrystalline cellulose was catalyzed into reducing sugar, then the product entering into the top phase. In the end, inhibition of product was removed, and the yield of reducing sugar in ATPS was increased 10.94% compared with the reaction in the single aqueous phase. The saccharification in ATPS could reach 40.16% when the reaction reached equilibrium.     

Extractive fermentation for enhanced production of alkaline phosphatase from Bacillus licheniformis MTCC 1483 using aqueous two-phase systems

A study was made to find out maximum partitioning of Bacillus licheniformis alkaline phosphatase in different ATPSs composed of different molecular weight of PEG X (X = 2000, 4000, 6000) with salts (magnesium sulphate, sodium sulphate, sodium citrate) and polymers (dextran 40, dextran T500). Physicochemical factors such as effect of system pH, system temperature and production media were evaluated for partitioning of alkaline phosphatase. PEG 4000 [9.0% (w/v)] and dextran T500 [9.6% (w/v)] were selected as most suitable system components for alkaline phosphatase production by B. licheniformis based on greater partition coefficient (k = 5.23). The two-phase system produced fewer enzymes than the homogeneous fermentation (control) in early stage of fermentation, but after 72 h the enzyme produced in the control system was less than that in the ATPS. Total alkaline phosphatase yield in ATPS fermentation was 3907.01 U/ml and in homogeneous fermentation 2856.50 U/ml.     

Improving production of hyperthermostable and high maltose-forming alpha-amylase by an extreme thermophile Geobacillus thermoleovorans using response surface methodology and its applications

By cultivating Geobacillus thermoleovorans in shake flasks containing cane molasses medium at 70 degrees C, the fermentation variables were optimized by 'one variable at a time' approach followed by response surface methodology (RSM). The statistical model was obtained by central composite design (CCD) using three variables (cane-molasses, urea and inoculum density). An overall 1.6- and 2.1-fold increase in enzyme production was achieved in the optimized medium in shake flasks and fermenter, respectively. The alpha-amylase titre increased significantly in cane-molasses medium (60 U ml(-1)) as compared to that in the synthetic medium (26 U ml(-1)). Thus the cost of enzyme produced in cane molasses medium (0.823 euros per million U) was much lower than that produced in the synthetic starch-yeast extract-tryptone medium (18.52 euros per million U). The shelf life of bread was improved by supplementing dough with alpha-amylase, and thus, the enzyme was found to be useful in preventing the staling of bread. Reducing sugars liberated from 20% and 30% raw pearl millet starch were fermented to ethanol; ethanol production levels attained were 35.40 and 28.0 g l(-1), respectively.     

Primary recovery of a genetically engineered Trichoderma reesei endoglucanase I (Cel 7B) fusion protein in cloud point extraction systems

Here we present data to demonstrate how partitioning of a hydrophilic enzyme can be directed to the hydrophobic detergent-enriched phase of an aqueous two-phase system by addition of short stretches of amino acid residues to the protein molecule. The target enzyme was the industrially important endoglucanase I, EGI (endo-1,4-beta-D-glucan-4-glucanohydrolase, EC 3.2.1.4, Cel7B) of Trichoderma reesei. We investigated the partitioning of three EGI variants containing various C-terminal peptide extensions including Trp-Pro motifs of different lengths and localizations. Additionally, a recently developed system composed of the thermoseparating copolymer HM-EOPO was utilized to study the effects of fusion tags. The addition of peptides containing tryptohan residues enhanced the partitioning of EGI to the HM-EOPO-rich phase. The system composed of a nonionic detergent (Agrimul NRE1205) resulted in the highest partition coefficient (K = 31) and yield (90%) with the construct EGI(core-P5)(WP)(4) containing (Trp-Pro)(4) after a short linker stretch. A recombinant strain of T. reesei Rut-C30 for large-scale production was constructed in which the fusion protein EGI(core-P5)(WP)(4) was expressed from the strong promoter of the cellulase gene cbh1. The fusion protein was successfully expressed and secreted from the fungus during shake-flask cultivations. Cultivation in a 28-L bioreactor however, revealed that the fusion protein is sensitive to proteases. Consequently, only low production levels were obtained in large-scale production trials.     

(R)-phenylacetylcarbinol production in aqueous/organic two-phase systems using partially purified pyruvate decarboxylase from Candida utilis

Aqueous/organic two-phase systems have been evaluated for enhanced production of (R)-phenylacetylcarbinol (PAC) from pyruvate and benzaldehyde using partially purified pyruvate decarboxylase (PDC) from Candida utilis. In a solvent screen, octanol was identified as the most suitable solvent for PAC production in the two-phase system in comparison to butanol, pentanol, nonanol, hexane, heptane, octane, nonane, dodecane, methylcyclohexane, methyl tert butyl ether, and toluene. The high partitioning coefficient of the toxic substrate benzaldehyde in octanol allowed delivery of large amounts of benzaldehyde into the aqueous phase at a concentration less than 50 mM. PDC catalyzed the biotransformation of benzaldehyde and pyruvate to PAC in the aqueous phase, and continuous extraction of PAC and byproducts acetoin and acetaldehyde into the octanol phase further minimized enzyme inactivation, and inhibition due to acetaldehyde. For the rapidly stirred two-phase system with a 1:1 phase ratio and 8.5 U/mL carboligase activity, 937 mM (141 g/L) PAC was produced in the octanol phase in 49 h with an additional 127 mM (19 g/L) in the aqueous phase. Similar concentrations of PAC could be produced in the slowly stirred phase separated system at this enzyme level, although at a much slower rate. However at lower enzyme concentration very high specific PAC production (128 mg PAC/U carboligase at 0.9 U/mL) was achieved in the phase separated system, while still reaching final PAC levels of 102 g/L in octanol and 13 g/L in the aqueous phase. By comparison with previously published data by our group for a benzaldehyde emulsion system without octanol (50 g/L PAC, 6 mg PAC/U carboligase), significantly higher PAC concentrations and specific PAC production can be achieved in an octanol/aqueous two-phase system.     

Characteristics of an aqueous two-phase system for α-amylase production

The characteristics of an aqueous two-phase system for the overproduction of extracellular enzyme through α-amylase fermentation by Bacillus amyloliquefaciens were investigated. With higher molecular weight of polyethylene glycol (PEG) or lower molecular weight of dextran, the partition coefficient of α-amylase was increased. α-Amylase biosynthesis was increased when PEG 6000 was included in the medium compared to the medium without PEG. Phosphate addition to the PEG-dextran system improved the partition coefficient of α-amylase, but deactivated α-amylase severely. By using sodium sulfate instead of phosphate, α-amylase deactivation was negligible, and high partitioning of the enzyme in the top phase was obtained.     

Purification of recombinant phenylalanine dehydrogenase by partitioning in aqueous two-phase systems

This study presents the partitioning and purification of recombinant Bacillus badius phenylalanine dehydrogenase (PheDH) in aqueous two-phase systems (ATPS) composed of polyethylene glycol 6000 (PEG-6000) and ammonium sulfate. A single-step operation of ATPS was developed for extraction and purification of recombinant PheDH from E. coli BL21 (DE3). The influence of system parameters including; PEG molecular weight and concentration, pH, (NH(4))(2)SO(4) concentration and NaCl salt addition on enzyme partitioning were investigated. The best optimal system for the partitioning and purification of PheDH was 8.5% (w/w) PEG-6000, 17.5% (w/w) (NH(4))(2)SO(4) and 13% (w/w) NaCl at pH 8.0. The partition coefficient, recovery, yield, purification factor and specific activity values were of 92.57, 141%, 95.85%, 474.3 and 10424.97 U/mg, respectively. Also the K(m) values for L-phenylalanine and NAD(+) in oxidative deamination were 0.020 and 0.13 mM, respectively. Our data suggested that this ATPS could be an economical and attractive technology for large-scale purification of recombinant PheDH.     

Production of cyclodextrin homologues using aqueous two-phase system

Cyclodextrin homologues (CDs), produced by cyclodextrin glycosyltransferase (CGTase), were simultaneously partitioned in aqueous two-phase system (ATPS). Partition coefficients of CDs were measured in PEG/salt and PEG/dextran systems. Phosphate, citrate, sulfate were tested as salt. ATPS of PEG/salt and PEG/dextran had the partition coefficients of the CDs, larger than unity. However, PEG/dextran system was observed better than PEG/salt as CGTase activity decreased sharply with salt concentration. Enzymatic reaction occurred mainly in PEG-rich bottom phase because of the low partition coefficient of CGTase. The resulting CDs transferred to the PEG-rich top phase, obeying the diffusional partition. In the ATPS of 7% PEG (M.W. 20,000) and 9% dextran (M.W. 40,000), 7 mg/ml of CDs were obtained in top phase at 4.5 hours.     

Simultaneous production and partition of chitinase during growth of Serratia marcescens in an aqueous two-phase system

Summary Partition and production of the extracellular chitinase from Serratia marcescens were studied in PEG/dextran aqueous two-phase systems. The enzyme partitions into the bottom phase and the cells segregate into the top phase. The best system is 2% (w/v) PEG 20000 and 5% (w/v) dextran T500. The cell growth and enzyme production kinetics are similar in the aqueous two-phase system and in the polymer-free reference system. However, the maximum enzyme concentration in the former system is 1.5 times that in the latter one.     

Response surface methodology for the extraction of wedelolactone from Eclipta alba using aqueous two-phase extraction

Abstract

Aqueous two-phase extraction of wedelolactone from Eclipta alba was studied using the polymer-salt system. The system consisted of polyethylene glycol (PEG) as a top phase (polymer) and sodium citrate as a bottom phase (salt). Process parameters such as PEG concentration, PEG molecular weight, salt concentration, and pH have been optimized using response surface methodology (RSM) with the help of central composite design (CCD). The optimized conditions for aqueous two-phase system (ATPS), in the case of one factor at a time approach, were found as PEG 6000, PEG concentration 18% (w/v), salt concentration 16% (w/v), and pH 7; with maximum extraction yield of 6.52?mg/g. While, RSM studies showed maximum extraction yield of 6.73?mg/g with the optimized parameters as PEG 6000, PEG concentration 18% (w/v), salt concentration 17.96% (w/v), and pH 7. ATPS was found to give a 1.3 fold increase in the extraction yield of wedelolactone as compared to other conventional extraction methods.