Separation of gamma-aminobutyric acid from fermented broth

Gamma-aminobutyric acid (GABA) is a non-proteinaceous amino acid that is widely distributed in nature and acts as the major inhibitory neurotransmitter in the mammalian brain. This study aimed to find a separation method for getting high-purity GABA from a fermented broth. Firstly, a fermented broth with a high content of GABA (reaching 997 ± 51 mM) was prepared by fermentation with Lactobacillus brevis NCL912. GABA purification was conducted by successive centrifugation, filtration, decoloration, desalination, ion-exchange chromatography (IEC), and crystallization. Inorganic salt (Na₂SO₄) was removed from the both by desalination with 70% ethanol solution. A ninhydrin test strip was designed for the real-time detection of GABA during IEC. The recovery rate for the whole purification process was about 50%. The purified product was characterized by thin-layer chromatography and HPLC, and its purity reached 98.66 ± 2.36%.     

Separation of lactic acid from fermented broth by reactive extraction

The separation of lactic acid from complex fermentation broth was examined. Liquid–liquid extraction using reversible chemical complexation for reactive extraction was chosen to be the separation method. Over 50% yield of lactic acid was obtained from fermented broth in a single extraction step, when using the tertiary amine as the extractant, 1-dekanol as the diluent and trimethylamine (TMA) as the stripping solution. The effect of complex media on the extraction behaviour has hardly been examined previously.     

Extractive fermentation of clavulanic acid by Streptomyces DAUFPE 3060 using aqueous two-phase system

The influence of four variables, specifically PEG molar mass (400, 1,000, and 8,000 g/mol), concentrations of PEG and phosphate salts (15, 20, and 25% for both), and agitation intensity (110, 150, and 200 rpm), on clavulanic acid (CA) extraction by extractive fermentation with PEG/phosphate salts aqueous two-phase system was investigated in shaken flasks using a 2(4-1) -fractional factorial design. After selection of the two most significant variables (agitation intensity and PEG molar mass), an optimization study conducted according to a 2(2) -central composite design revealed that 25% PEG 8,000 g/mol and phosphate salts at 240 rpm (run 6) were the best conditions for the extractive fermentation, leading to the best results in terms of partition coefficient (k = 8.2), yield of CA in the PEG-rich phase (η(T) = 93%) and productivity (P = 5.3 mg/Lh). As a first attempt to make a scale-up of these results, the effectiveness of the extractive fermentation was then checked in a bench-scale bioreactor under conditions as close as possible to the optimum ones determined in flasks. The highest CA concentration obtained in the PEG-rich phase (691 mg/L) was 30% higher than in flasks, thus demonstrating the potential of such a new process, integrating the production and extraction steps, as a promising, low-cost tool to obtain high yields of this and similar products.     

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.     

Extraction of amino acids by aqueous two-phase partition

Summary Amino acids, including lysine, glutamic acid, and phenylalanine, in pure solution or in fermentation broth, were extracted with the aqueous two-phase system consisting of polyethylene glycol and salts, giving a very sharp separation. The partition is influenced by the type and the amount of salts used, pH and components of the broth.     

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).     

Separation of yeast protoplasts from membrane ghosts using an aqueous two-phase system

Protoplasts, prepared from Saccharomyces cerevisiae, were separated from membrane ghosts using an aqueous two-phase system of Dextran T 500, 5% (w/w) and polyethylene glycol (PEG) 8000, 5% (w/w). The protoplast preparation was prewashed in the top phase. After resuspension in fresh top phase an equal volume of bottom phase was added. A protoplast preparation almost free from membrane ghosts was obtained as a precipitate in the bottom phase. The membrane ghosts partitioned to the interphase.     

影响克拉维酸生物合成的氨基酸

发酵液的氨基酸分析显示,谷氨酸,精氨酸,天门冬氨酸,丙氨酸易被棒状链霉菌利用,发酵培养基中添加上述氨基酸后,谷氨酸,精氨酸有利于克拉维酸的生物合成,适时添加谷氨酸,精氨酸可分别提高克拉维酸的产量约25%和12%;而蛋氨酸,半胱氨酸含S氨基酸对克拉维酸生物合成不利,不同来源的黄豆粉作发酵培养基氮源,因其组成中某些氨基酸含量的差异。可使克拉维酸的产量相差百分之十几。     

Separation of presumptive plasma membranes from mitochondria by partition in an aqueous polymer two-phase system

Light-induced absorbance changes (LIAC), indicating the reversible reduction of a b-type cytochrome, and with a possible connection to blue light photomorphogenesis, have been found in a presumptive plasma membrane rich centrifuge fraction from LIAC could be due to plasma membrane vesicles turned inside out or to cytochromes localized in other organelles. Phase partition proved to be a rapid method (results technique membrane particles are separated according to differences in surface properties rather than size and density. LIAC could be separated into two fractions: one partitioning into the polyethylene glycol rich upper phase and another preferring the dextram rich lower phase. Mitochondria (cytochrome c oxidase) were recovered in the lower phase. A dual distribution of LIAC was found with all materials tested: corn coleoptiles, corn shoots, barley shoots and cauliflower inflorescences. About 80–90% of the cytochromes in the upper phase were related to LIAC, whereas only 10–15% of those in the lower phase were of this kind. The LIAC preferring the upper phase was probably bound to the plasma membrane, since plasma membrane vesicles are known to have a high partition in these phase systems. The lower phase LIAC could be due to plasma membrane vesicles turned inside out or to cytochromes localized in other organelles. Phase partition proved to be a rapid method (results within one hour after the initial pelleting) for purification of presumptive plasma membranes, yielding a preparation which contained five times less mitochondrial contamination than the preparation obtained with sucrose gradient centrifugation (the 33/45% w/w sucrose interface fraction).     

Purification of acetohydroxy acid synthase by separation in an aqueous two-phase system

Extraction in a polyethylene glycol (PEG)–phosphate aqueous two-phase system was considered as a primary step in purification of the acetohydroxy acid synthase III large catalytic subunit from an E. coli extract. Extraction optimization was achieved by varying the system parameters. Two systems with the following weight compositions were chosen for purification: PEG-2000 (16%)–phosphate (6%) and PEG-4000 (14%)–phosphate (5.5%)–KCl (8%), both at pH 7.0 and 1 mg total protein per 1 g system. Significant purification was achieved by a single extraction step with 70% recovery of the enzyme. After an additional ion-exchange chromatography step, pure enzyme was obtained in a 50% overall yield.     

Reversing the amino acid sequence of a dipeptide changes its partition in an aqueous two-phase system

Summary Reversing the amino acid sequence of a dipeptide produces distinct differences in how they partition between a polyethylene glycol/potassium phosphate aqueous two-phase system. The partition coefficients for twenty-three dipeptides in this biphasic system are recorded.     

Purification of (S)-3-cyano-5-methylhexanoic acid from bioconversion broth using an acetone/ammonium sulfate aqueous two-phase system

(S)-3-Cyano-5-methylhexanoic acid ((S)-CMHA) is the key chiral intermediate of pregabalin. In this paper, an aqueous two-phase system (ATPS) was developed to extract (S)-CMHA from nitrilase-catalyzed bioconversion broth. Inorganic salts and hydrophilic solvents were screened to form ATPS, among which an acetone/ammonium sulfate ATPS was investigated in detail, including phase diagram, effect of phase composition and stability of (S)-CMHA. The maximum product recovery of 99.15% was obtained by an optimized ATPS system composed of 15% (w/w) ammonium sulfate and 35% (w/w) acetone with the removal of 99% cells and 86.27% proteins. The total (S)-CMHA yield reached 92.11% after back-extraction. The recycling use of ammonium sulfate was investigated, and 93.10% of salt in the salt-rich phase was recovered with the addition of methanol. The results demonstrated the efficiency of the two-step extraction process for separation of (S)-CMHA.     

Purification of adenovirus messenger ribonucleic acid by an aqueous polymer two-phase system.

An aqueous polymer phase system containing 6.3% (w/w) dextran and 3.5% (w/w) poly(ethylene glycol) in 10 mM phosphate buffer (pH 8.0) was developed to select RNA-DNA hybrids from unhybridized RNA. The top phase of this phase system, which contains DNA and the RNA-DNA hybrids, can be used to purify adenovirus messenger RNA both early and late in the infectious cycle. The hybrids can be melted by heat in the top phase and the messenger RNA selected by oligo(dT)cellulose chromatography whereupon the polymers and the DNA percolate and the polyadenylated messenger RNA absorb to the column. The isolated messenger RNA appears to be almost quantitatively recovered at a purity from 70 to 90% depending on the concentration of the specific messenger RNA in the starting material. Early and late viral messenger RNA were selected on the complementary strands of adenovirus DNA according to this procedure.     

Separation of human rosette- and nonrosette-forming lymphoid cells by countercurrent distribution in an aqueous two-phase system.

Mixtures of aqueous solutions of dextran and of poly(ethylene glycol) form immiscible two-phase systems suitable for the separation (by partition) of cells based on subtle differences in membrane surface properties. Lymphoid cells from human tonsils were subjected to countercurrent distribution in such a system. Analysis of cells from different parts of the countercurrent extraction train by the sheep red blood cell rosette test indicates a separation of rosette-forming and nonrosette-forming lymphocytes with the former having the higher partition coefficient. Since a major determinant of cell partition in these phases is a membrane-charge associated property it appears likely that the rosette-forming cells have a higher surface charge than the nonrosette-forming cells.     

The transport of amino acids,amino acid derivatives and ions across ion-exchange membranes

The passage of inorganic salts, glucose, amino acids and peptides across polystyrene-backed double membranes (negative-positive fixed-charge junctions) was studied in a two-compartment cell and compared to a known cellular system, the Ehrlich-Lettre ascites carcinoma. It was concluded that passage proceeds by a 1 : 1 exchange of diffusing ions in the membrane. The more rapidly transported systems reflected an increased probability of exchange in all cases, as evidenced both by a saturation effect and by the degree to which the space charge was perturbed at the membrane. The amino group (as NH₃⁺) of the amino acid involved in the exchange process was vital for transport. The presence of a second amino group, either ionized or as -NH₂, accelerated the exchange. The presence of electron-attracting groups on the side chain or of a methyl group on the alpha carbon also facilitated passage. Cation dependence was seen. Passage was hindered by a second carboxyl group, an alcoholic group, or a lengthened side chain. Use of double membranes permits experimental electrodic transport modelling and may facilitate design of a drug delivery system.     

Substitutions of surface amino acid residues of cutinase probed by aqueous two-phase partitioning

The surface properties of a protein are often crucial for recognition and interaction with other molecules. Important functional residues can be identified by mutational analysis. There is a need for rapid methods to study protein surfaces and surface changes due to mutations. Partitioning in aqueous two-phase systems has the potential to be used in this respect since protein partitioning depends on the surface properties of the protein. The influence of surface-exposed amino acid residues in protein partitioning has been studied with cutinase variants, which differed in one or several amino acid residues as a result of site-directed mutagenesis. The solvent accessibility of the mutated residues was determined with a computer program, Graphical Representation and Analysis of Surface Properties. The aqueous two-phase system was composed of dextran and a random copolymer of ethylene oxide and propylene oxide. It was shown, for the first time, to what extent surface-exposed amino acid residues influence the partition coefficient in an aqueous two-phase system. The effect on partitioning could be described only taking into account solvent accessibility and type of residue substitution. The results demonstrate that the system can be used to detect conformational changes in mutant proteins since the expected effect on partitioning due to a mutation can be calculated. The aqueous two-phase system used here does indeed provide a rapid and convenient method to study protein surfaces and slight surface changes due to mutations.     

双极膜电渗析分离发酵液中L-乳酸

采用三室型双极膜电渗析装置将发酵液中的L-乳酸钠转化为L-乳酸。探讨操作电压、流速、进料L-乳酸钠质量浓度等工艺参数对转化过程的影响,考察电渗析过程参数对转化率、物料损失率、电流效率和能耗等技术指标的影响。在最优操作条件下（流速40L／h,电压15V）对2L的100．25g／L乳酸钠发酵液进行分批重复电渗析处理。结果表明：整个过程的转化率为81．22％,损失率为1．5％,能耗为0．81kW·h／kg,电流效率为91．8％,得到的L-乳酸质量浓度可达144．31g／L．电渗析残液补糖后可回到发酵罐中用于发酵生产L-乳酸.