Extraction of tetracycline from fermentation broth using aqueous two-phase systems composed of polyethylene glycol and cholinium-based salts

Aiming at developing not only cheaper but also biocompatible and sustainable extraction and purification processes for antibiotics, in this work it was evaluated the ability of aqueous two-phase systems (ATPS) composed of polyethylene glycol (PEG) and cholinium-based salts to extract tetracycline from the fermented broth of Streptomyces aureofaciens. Conventional polymer/salt and salt/salt ATPS were also studied for comparison purposes. The novel systems here proposed are able to extract tetracycline directly from the fermentation broth with extraction efficiencies higher than 80%. A tailored extraction ability of these systems can also be achieved, with preferential extractions either for the polymer- or salt-rich phases, and which further depend on the cholinium-based salt employed. The gathered results support the applicability of biocompatible ATPS in the extraction of antibiotics from complex matrices and can be envisaged as valuable platforms to be applied at the industrial level by pharmaceutical companies.     

Evaluating aqueous two-phase systems for Yarrowia lipolytica extracellular lipase purification

In this study an aqueous two-phase system (ATPS) composed of polyethylene glycol (PEG) and potassium phosphate was tested for the purification of lipase from Yarrowia lipolytica IMUFRJ 50682. Ultrafiltration and precipitation with acetone and kaolin were also used as traditional comparison methods Ultrafiltration was a good method with a purification factor of 6.55, but protease was also purified in this extract. For the precipitation with acetone and kaolin lower values of lipase and protease activity were found in relation to the original crude enzyme extract. Under the best conditions of ATPS (pH 6 and 4 °C), the purification fold was greater than 40 and selectivity was almost 500. Lipase was recovered in the salty phase which makes it easier to purify it. The optimum pH and temperature ranges for purified lipase with this system was 6–7 and 35–40 °C, respectively. Lipase thermostability was increased in relation to crude extract after the purification with the PEG/phosphate buffer system for temperatures lower than 50 °C. All enzyme extracts showed good stability to a wide pH range. Y. lipolytca lipase was successfully purified by using ATPS in a single downstream processing step and presented good process characteristics after this treatment.     

Evaluation of the effects of the parameters involved in the purification of clavulanic acid from fermentation broth by aqueous two-phase systems

The purification of clavulanic acid (CA), which is an important β-lactam antibiotic produced by submerged cultivation of Streptomyces clavuligerus, was studied through the use of phosphate and polyethylene glycol-based aqueous two-phase systems. The parameters’ effect on the yield and purification was evaluated through an experimental design and the preliminary results showed that the polyethylene molecular mass and tie-line length and phase volume ratio exerted the strongest effect on the yield and distribution coefficient in the range tested. In addition, the response surface methodology was used to optimize the distribution coefficient, yield, and purification factor. The optimal conditions of yield and purification factor are in the regions where polyethylene has a low molecular mass, pH close to the isoelectric point, and lower top phase volume. A 100% yield and a 1.5-fold purification factor are obtained when extracting CA by maximizing the conditions of an aqueous two-phase system.     

Technological aspects of extractive fermentation using aqueous two-phase systems

World Journal of Microbiology and Biotechnology -     

Isolation of natural red colorants from fermented broth using ionic liquid-based aqueous two-phase systems

There is a growing demand for natural colorants. This is prompting the search for new alternative and “benign” separation systems allowing higher recoveries, extraction yields, and selectivities. This work investigates the use of aqueous two-phase systems (ATPS) based on ionic liquids as extraction processes for the recovery of red colorants from the fermented broth of Penicillium purpurogenum DPUA 1275. Several ATPS based on quaternary ammonium and imidazolium were studied in this work aiming at separating the red colorants produced from the remaining colorants and contaminant proteins present in the fermented broth. The results suggest that the red colorants can be isolated by an appropriate manipulation of some of the process conditions, such as the use of quaternary ammonium with short alkyl chains, alkaline media, and short tie-line lengths (extraction point systems with lower concentrations of ionic liquid). These conditions allow large partition coefficients for the red colorants (K _red = 24.4 ± 2.3), high protein removal (60.7 ± 2.8 %) and selectivity parameters (S _red/prot = 10.05).     

Preliminary application of light-pH sensitive recycling aqueous two-phase systems to purification of lipase

One key problem of aqueous two-phase systems (ATPS) is that phase-forming polymers could not be recycled efficiently. This results in high cost and environmental pollution. In this study, we introduced novel aqueous two-phase systems which are composed by pH-sensitive polymer P_ADB and light-sensitive polymer P_NNC. P_NNC is enriched in the top phase while P_ADB is found in the bottom phase. And recoveries of two-phase-forming polymers can both reach over 96%. This aqueous two-phase system was used for purification of lipase from its crude material. The influences of various process parameters such as concentration of the phase-forming polymer, system pH, different types and concentrations of neutral salts on partitioning of lipase are evaluated. It has been found that partition coefficient of pure lipase could reach 0.061 under optimized conditions. Lipase from crude material was purified with 83.7% recovery and a purification factor of approximately 18 folds.     

Single-step purification of lipase from Burkholderia multivorans using polypropylene matrix

Lipase from Burkholderia multivorans was purified with high yields directly from fermentation broth by a single-step purification protocol involving adsorption and desorption. The crude enzyme (lyophilized powder) from B. multivorans was loaded on Accurel (Membrana, Germany), a polypropylene matrix, using butanol as the solvent in a buffer at pH 9.0 and ambient temperature for a period of 12 h. The enzyme adsorbed onto the matrix with high specific activity (33 units mg^–1 protein). This was followed by desorption of the enzyme from the matrix using Triton X-100 as the eluent. The enzyme was finally recovered by precipitation with acetone (50%, v/v). Thus, an overall enzyme yield of 66% with a 3.0-fold purification was obtained. The purity of the enzyme was ascertained by SDS-PAGE. The phenomenon of adsorption and desorption on Accurel was studied for three more lipases, viz. Mucor meihei lipase (Sigma–Aldrich Co.), Lipolase (Novo Nordisk, Denmark) and Pseudomonas aeruginosa lipase (laboratory isolate).     

Analysis of continuous fermentation processes in aqueous two-phase systems

Simulations of continuous ethanol or acetonobutylic fermentations in aqueous two-phase systems show that at high substrate feed concentrations it is possible to obtain solvent productivities about 25–40% higher than in conventional systems with cell recycle if the biomass bleed rate is kept about one tenth of the value of D.List of Symbols a Volumetric fraction of dextran rich phase - B h^–1 Bleed rate - D h^–1 Dilution rate - P kg m^–3 Product concentration - PD kg m^–3 h^–1 Productivity - S kg m^–3 Substrate - X kg m^–3 Biomass - Partition coefficient     

Purification and in situ immobilization of lipase from of a mutant of Trichosporon laibacchii using aqueous two-phase systems

The crude intracellular lipase (cell homogenate) from Trichosporon laibacchii was subjected to partial purification by aqueous two-phase system (ATPS) and then in situ immobilization by directly adding diatomites as carrier to the top PEG-rich phase of ATPS. A partition study of lipase in the ATPS formed by polyethylene glycol–potassium phosphate has been performed. The influence of system parameters such as molecular weight of PEG, system phase composition and system pH on the partitioning behaviour of lipase was evaluated. The ATPS consisting of PEG 4000 (12%) and potassium phosphate (K₂HPO₄, 13%) resulted in partition of lipase to the PEG-rich phase with partition coefficient 7.61, activity recovery 80.4%, and purification factor of 5.84 at pH of 7.0 and 2.0% NaCl. Moreover, the in situ immobilization of lipase in PEG phase resulted in a highest immobilized lipase activity of 1114.6 U g^?1. The above results show that this novel lipase immobilization procedure which couples ATPS extract and enzyme immobilization is cost-effective as well as time-saving. It could be potentially useful technique for the purification and immobilization of lipase.     

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.     

Effective extraction and purification of beta-xylosidase from Trichoderma koningii fermentation culture by aqueous two-phase partitioning

Effective extraction of protein from bulk medium is an important technique in bioresearch. In the present study, we describe an extracellular beta-xylosidase from the fermentation supernatant of Trichoderma koningii G-39 that was successfully extracted and purified simultaneously in a single step by using an aqueous two-phase partitioning method. This two-phase system was prepared by dissolving suitable amount of poly(ethylene glycol) (PEG) and sodium dihydrogenphosphate (NaH(2)PO(4)) in aqueous solution. beta-Xylosidase was recovered with high yield and high concentration in the bottom salt-rich phase when 25% (w/v) PEG 1500 and 20-25% (w/v) NaH(2)PO(4) were applied. Based on a 1-liter scale extraction, the purity of the enzyme was enhanced at least 33-fold. The total activity increased 422% in comparison with that in the untreated filtrate. The effectiveness and simplicity may make this technique potentially useful in various applications. The transxylosylation activity of the enzyme purified by this technique was also investigated.     

The extractive purification of peroxidase from plant raw materials in aqueous two-phase systems

The extractive purification of peroxidase from Armoracia rusticana roots and Glycine max seed coats in temperature-induced and affinity microsphere-containing aqueous two-phase systems was stuied. The extractive purification of peroxidase from Glycine max seed coats was carried out in a temperature-induced aqueous two-phase system formed by Triton X-45, Triton X-100 and sodium acetate at pH 5.5 A 99% yield with a 6-fold purification factor was obtained. When the clear top phase was subjected to concanavalin-A affinity chromatography, the purification factor rose to 41 and the yield dropped to 28%. A two-step purification process for peroxidase from Armoracia rusticana roots was developed by adding concanavalin-A affinity microspheres to a PEG/phosphate aqueous two-phase system. The method allows a 60% recovery of high purity peroxidase (1,860 guaiacol units per mg). A lower recovery rate and degree of purification of this enzyme was achieved after temperature-induced aqueous two-phase partition or acetone precipitation and concanavalin-A affinity column chromatography.     

The use of detergent-based aqueous two-phase systems for the isolation of extracellular proteins: purification of a lipase from Pseudomonas cepacia.

The partitioning of a variety of extracellular lipases, both pro- and eucaryotic, in detergent-based aqueous two-phase systems was examined. The results revealed that all procaryotic lipases showed a clear preference for the detergent-rich coacervate phase. In contrast, all eucaryotic lipases were significantly excluded from this phase, most probably caused by their glycosylation. The potential of such detergent-based systems for the isolation of extracellular lipases directly from cell-free culture broth was analyzed using the bacterium Pseudomonas cepacia (DSM 50181). This strain was identified after a limited screening for lipase activity. About 76% of the lipase could be extracted into the coacervate phase in just one purification step, leading to a four-fold concentration of lipase and a purification factor of 24.     

Purification of lipase produced by a new source of Bacillus in submerged fermentation using an aqueous two-phase system

This work discusses the application of an aqueous two-phase system for the purification of lipases produced by Bacillus sp. ITP-001 using polyethylene glycol (PEG) and potassium phosphate. In the first step, the protein content was precipitated with ammonium sulphate (80% saturation). The enzyme remained in the aqueous solution and was dialyzed against ultra-pure water for 18 h and used to prepare an aqueous two-phase system (PEG/potassium phosphate). The use of different molecular weights of PEG to purify the lipase was investigated; the best purification factor (PF) was obtained using PEG 20,000g/mol, however PEG 8000 was used in the next tests due to lower viscosity. The influence of PEG and potassium phosphate concentrations on the enzyme purification was then studied: the highest FP was obtained with 20% of PEG and 18% of potassium phosphate. NaCl was added to increase the hydrophobicity between the phases, and also increased the purification factor. The pH value and temperature affected the enzyme partitioning, with the best purifying conditions achieved at pH 6.0 and 4°C. The molecular mass of the purified enzyme was determined to be approximately 54 kDa by SDS-PAGE. According to the results the best combination for purifying the enzyme is PEG 8000g/mol and potassium phosphate (20/18%) with 6% of NaCl at pH 6.0 and 4°C (201.53 fold). The partitioning process of lipase is governed by the entropy contribution.     

Porcine pancreatic lipase partition in potassium phosphate-polyethylene glycol aqueous two-phase systems

This research study examined porcine pancreatic lipase partition in aqueous two-phase systems formed by polyethylene glycol-potassium phosphate at pH 6.0, 7.0 and 8.0, the effect of polymer molecular mass, and NaCl concentration. The enzyme was preferentially partitioned into the polyethylene glycol rich phase in systems with molecular mass 4000-8000, while with polyethylene glycol of 10,000 molecular mass it was concentrated in the phosphate rich phase. The enthalpic and entropic changes found due to the protein partition were negative for all the polyethylene glycol molecular mass systems assessed. Both thermodynamic functions were shown to be associated by an entropic-enthalpic compensation effect suggesting that the water structure ordered in the ethylene chain of polyethylene glycol plays a role in the protein partition. The addition of NaCl increased the lipase affinity to the top phase and this effect was most significant in the system polyethylene glycol 2000-NaCl 3%. This system yielded an enzyme recovery more than 90% with a purification factor of approximately 3.4.     

Partitioning of amylase produced by Aspergillus niger in solid state fermentation using aqueous two-phase systems

Equilibrium data of aqueous two-phase systems composed of polyethylene glycol (4000 g mol⁻¹ or 6000 g mol⁻¹) and Li₂SO_4, (NH₄)₂SO₄ or Na₂SO₄ at pH 6.5 and 25 °C were obtained. The efficiency of these in the partition of amylases derived from Aspergillus niger was determined. The experimental data of binodal curves and tie lines were used to estimate the group interaction parameters using the UNIFAC model. Additionally, the influence of phases on the activity of the enzymes was investigated. The results indicate that the polymer molar mass did not influence the biphasic region size. However, the cations under study presented differences in induction to phase formation. It was verified that the systems formed with the Na⁺ presented a larger biphasic region. The increase in the molar mass of the polymer caused the increase in the exclusion volume from 3970.732 g mol⁻¹ to 5700.873 g mol⁻¹. The transfer Gibbs free energy of enzymes presented values between −1296.30 kJ mol⁻¹ and −2867.70 kJ mol⁻¹, that is, the process was spontaneous for all systems studied. The systems formed by (NH₄)₂SO₄ and PEG 4000 g mol⁻¹ presented the best K_e result (3.421) and theoretical recovery of 80.35 %.     

Isolation of a Aspergillus niger lipase from a solid culture medium with aqueous two-phase systems

The aim of this work is to find the best conditions to isolate lipase from a solid culture medium of Aspergillus niger NRRL3 strains using aqueous two-phase systems formed with polyethylene glycol and potassium phosphate or polyethylene glycol and sodium citrate. We studied the partitioning of a commercial lyophilizate from A. niger. Also, the lipase enzymatic activity was studied in all the phases of the systems and the results indicate that citrate anion increases lipase activity. An analysis by fluorescence spectroscopy of the interaction between lipase and the bottom and top phases of the systems shows that the protein tryptophan-environments are modified by the presence of PEG and salts. Separation of the enzyme from the rest of the proteins that make up the lyophilized was achieved with good yield and separation factor by ATPS formed by PEG 1000/Pi at pH 7, PEG 2000/Ci at pH 5.2 and PEG 4000/Ci at pH 5.2. The above mentioned systems were used in order to isolate extracellular lipase from a strain of A. niger in submerged culture and solid culture. The best system for solid culture, with high purification factor (30.50), is the PEG 4000/Ci at pH 5.2. The enzyme was produced in a solid culture medium whose production is simple and recovered in a phase poor in polymer, bottom phase. An additional advantage is that the citrate produces less pollution than the phosphate. This methodology could be used as a first step for the isolation of the extracellular lipase from A. niger.     

Biosurfactants and aqueous two-phase fermentation

The partition of surfactants and a biosurfactant-producing microorganism was studied in polyethylene glycol and dextran aqueous two-phase systems. In the presence of sodium phosphate, surfactants distributed themselves according to charge. Cationic surfactants preferred the bottom phase, while anionic surfactants were attracted to the top phase. Incresing the phosphate molarity or the pH resulted in a more 1-sided surfactant partitioning. Biosurfactant partitioning was weaker than synthetic surfactant partitioning due to the weaker effective charge and lack to strong specific affinity for any of the phase-forming polymers. Bacillus Subtilis cells partitioned very storngly to the bottom phase. The bioscurfactant, surfactin, produced by this microorganism partitioned to the top phase. Batch fermentations were carried out in an aqueous 2-phase system. Surfactin was produced in larger quanities in the 2-phase fermentation than in the regular mineral salts medium.     

Separation and purification of laccases from two different fungi using aqueous two-phase extraction

Selective purification still poses a challenge in the downstream processing of biomolecules such as proteins and especially enzymes. In this study a polyethylene glycol 3000 (PEG 3000)–phosphate aqueous two-phase system at 25 °C and pH 7 was successfully used for laccase purification and separation. Initially, the effect of phase forming components on enzyme activities in homogenous systems was studied. In the course of the extraction experiments tie lines, enzyme source, initial enzyme activities, phase ratio and sodium chloride concentrations were varied and their influence on the activity partitioning was determined. Partitioning results were validated using clear-native-PAGE and isoelectric focusing. Based on these results, the separation of laccases from Trametes versicolor and Pleurotus sapidus was investigated using the principle of superposition. Sodium chloride was used to adjust laccase partitioning in the applied aqueous two-phase system (ATPS). Finally, two modes of operation are proposed depending on the aim of the purification task. One mode with 0.133 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and without sodium chloride separates P. sapidus laccases from T. versicolor laccases with clearance factors of 5.23 and 6.45, respectively. The other mode of operation with 0.124 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and 0.013 g g⁻¹ of sodium chloride enables a partitioning of both laccases into the bottom phase of the ATPS resulting in a purification factor of 2.74 and 96% activity recovery.