Downstream antibody purification using aqueous two‐phase extraction

The extraction of antibodies using a polyethylene glycol (PEG)‐citrate aqueous two‐phase system (ATPS) was investigated. Studies using purified monoclonal antibody (mAb) identified operating ranges for successful phase formation and factors that significantly affected antibody partitioning. The separation of antibody and host cell protein (HCP) from clarified cell culture media was examined using statistical design of experiments (DOE). The partitioning of antibody was nearly complete over the entire range of the operating space examined. A model of the HCP partitioning was generated in which both NaCl and citrate concentrations were identified as significant factors. To achieve the highest purity, the partitioning of HCP from cell culture fluid into the product containing phase was minimized using a Steepest Descent algorithm. An optimal ATPS consisting of 14.0% (w/w) PEG, 8.4% (w/w) citrate, and 7.2% (w/w) NaCl at pH 7.2 resulted in a product yield of 89%, an approximate 7.6‐fold reduction in HCP levels relative to the clarified cell culture fluid before extraction and an overall purity of 70%. A system consisting of 15% (w/w) PEG, 8% (w/w) citrate, and 15% (w/w) NaCl at pH 5.5 reduced product‐related impurities (aggregates and low molecular product fragments) from ～40% to less than 0.5% while achieving 95% product recovery. At the experimental conditions that were optimized in the batch mode, a scale‐up model for the use of counter‐current extraction technology was developed to identify potential improvements in purity and recovery that could be realized in the continuous operational mode. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Purification of lipase derived from Burkholderia pseudomallei with alcohol/salt-based aqueous two-phase systems

Alcohol/salt-based aqueous two-phase systems (ATPSs) were used to recover lipase derived from Burkholderia pseudomallei (B. pseudomallei). Nine biphasic systems, comprised of an alcohol-based top phase (ethanol, 2-propanol and 1-propanol) and a salt-based bottom phase (ammonium sulfate, potassium phosphate and sodium citrate), were evaluated for their effectiveness in lipase recovery. The stability of lipase in each of the solutions was tested, and phase diagrams were constructed for each system. The optimum partition efficiency for the purification of lipase was obtained in an ATPS of 16% (w/w) 2-propanol and 16% (w/w) phosphate in the presence of 4.5% (w/v) NaCl. The purified lipase had a purification factor of 13.5 and a yield of 99%.     

Manipulation of culture strategies to enhance capsaicin biosynthesis in suspension and immobilized cell cultures of Capsicum chinense Jacq. cv. Naga King Chili

Manipulation of culture strategies was adopted to study the influence of nutrient stress, pH stress and precursor feeding on the biosynthesis of capsaicin in suspension and immobilized cell cultures of C. chinense. Cells cultured in the absence of one of the four nutrients (ammonium and potassium nitrate for nitrate and potassium stress, potassium dihydrogen orthophosphate for phosphorus stress, and sucrose for sugar stress) influenced the accumulation of capsaicin. Among the stress factors studied, nitrate stress showed maximal capsaicin production on day 20 (505.9 ± 2.8 μg g^?1 f.wt) in immobilized cell, whereas in suspension cultures the maximum accumulation (345.5 ± 2.9 μg g^?1 f.wt) was obtained on day 10. Different pH affected capsaicin accumulation; enhanced accumulation of capsaicin (261.6 ± 3.4 μg g^?1 f.wt) was observed in suspension cultures at pH 6 on day 15, whereas in case of immobilized cultures the highest capsaicin content (433.3 ± 3.3 μg g^?1 f.wt) was obtained at pH 5 on day 10. Addition of capsaicin precursors and intermediates significantly enhanced the biosynthesis of capsaicin, incorporation of vanillin at 100 μM in both suspension and immobilized cell cultures resulted in maximum capsaicin content with 499.1 ± 5.5 μg g^?1 f.wt on day 20 and 1,315.3 ± 10 μg g^?1 f.wt on day 10, respectively. Among the different culture strategies adopted to enhance capsaicin biosynthesis in cell cultures of C. chinense, cells fed with vanillin resulted in the maximum capsaicin accumulation. The rate of capsaicin production was significantly higher in immobilized cells as compared to freely suspended cells.     

Aqueous biphasic system for the partial purification of Bacillus subtilis carboxymethyl cellulase

Carboxymethyl cellulase (CMCase) hydrolyses cellulose into glucose and is useful in various industrial applications. Conventional CMCase purification methods are rather complicated and time-consuming; thus, a cost-effective strategy for CMCase recovery is on demand. Polyethylene-glycol (PEG)/sodium citrate aqueous biphasic system (ABS) was adopted in this study to investigate the effectiveness of the ABS in the recovery of extracellular Bacillus subtilis CMCase from fermentation broth. Comprehensive optimization steps were executed that took into consideration the ABS variables of PEG molecular weight, tie-line length (TLL), volume ratio (V_R), crude loading, pH and the addition of sodium chloride (NaCl). A CMCase recovery yield (Y_B) of 88.82% ± 0.69, a purification fold (P_F) of 4.8 and a partition coefficient (K) of 0.44 ± 0.03 were achieved from the bottom phase of the PEG 6000/citrate ABS with TLL of 42.16% (w/w), V_R of 0.29, 1% of (w/w) NaCl, pH 7.0, and 20% (w/w) crude loading. CMCase was mainly segregated to the salt-rich bottom phase because of the hydrophilicity of the enzyme surface. The highly effective recovery technique was further confirmed by SDS-PAGE analysis. Overall, the present study suggests that the ABS is a potential purification strategy for extracellular CMCase.     

Effects of pH profiles on nisin fermentation coupling with foam separation

Online foam separation was proposed to recover nisin during fermentation of Lactococcus lactis subsp. lactis ATCC 11454. Firstly, the optimal pH profile of nisin fermentation was investigated including different realkalization set values and pH drop gradients. Then the selected pH profiles of 5.75 ± 0.05 and 6.25–5.75 (±0.02) were used to perform nisin fermentation coupling with foam separation. The results showed that pH profile of 5.75 ± 0.05 was better than that of 6.25–5.75 (±0.02) for online foam separation. With the optimal pH profile, an aeration of 20 ml min⁻¹ that started at 8 h of incubation and lasted for 2 h resulted in 6.6 times higher specific productivity than that of the fermentation without aeration. Nisin synthesis was therefore prolonged with low sucrose concentration in the culture broth, which indicated that the feedback inhibition of nisin is more influential than the substrate limitation of sucrose in the late phase of nisin fermentation. Total nisin production (4,870 ± 180 IU ml⁻¹) was increased by 30.3% with online foam separation. This effective online recovery method for nisin production could be easily scaled up due to the facile operation of foaming process.     

Partitioning of amino acids in the aqueous biphasic system containing the water‐miscible ionic liquid 1‐butyl‐3‐methylimidazolium bromide and the water‐structuring salt potassium citrate

In biotechnology, extraction by means of aqueous biphasic systems (ABS) is known as a promising tool for the recovery and purification of bio‐molecules. Over the past decade, the increasing emphasis on cleaner and environmentally benign extraction procedures has led to enhanced interest in the ABS containing ionic liquids (ILs)—a new class of non‐volatile alternative solvents. ABS composed of the hydrophilic IL {1‐butyl‐3‐methylimidazolium bromide ([C₄mim]Br)} and potassium citrate—which is easily degraded—represents a clean media to green separation of bio‐molecules. In this regard, here, the extraction capability of this ABS was evaluated through its application to the extraction of some amino acids. To gain an insight into the driving forces of amino acid partitioning in the studied IL ‐based ABS, the distribution of five model amino acids (L ‐tryptophan, L ‐phenylalanine, L ‐tyrosine, L ‐leucine, and L ‐valine) at different aqueous medium pH values and different phase compositions was investigated. The studies indicated that hydrophobic interactions were the main driving force, although electrostatic interactions and salting‐out effects were also important for the transfer of the amino acids. Moreover, based on the statistical analysis of the driving forces of amino acid partitioning in the studied IL ‐based ABS, a model was established to describe the partition coefficient of three model amino acids, L ‐tryptophan, L ‐phenylalanine, and L ‐valine, and employed to predict the partition coefficient of two other model amino acids, L ‐tyrosine and L ‐leucine. © 2011 American Institute of Chemical Engineers Biotechnol. Prog., 2011     

Potential Aqueous Two‐Phase Processes for the Primary Recovery of Colored Protein from Microbial Origin

The primary recovery of c‐phycocyanin and b‐phycoerythrin from Spirulina maxima and Porphyridium cruentum, respectively, using an established extraction strategy was selected as a practical model system to study the generic application of polyethylene glycol (PEG)‐phosphate aqueous two‐phase systems (ATPS). The generic practical implementation of ATPS extraction was evaluated for the recovery of colored proteins from microbial origin. A comparison of the influence of system parameters, such as PEG molecular mass, concentration of PEG as well as salt, system pH and volume ratio, on the partition behavior of c‐phycocyanin and b‐phycoerythrin was carried out to determine under which conditions target colored protein and contaminants concentrate to opposite phases. One‐stage processes are proposed for the primary recovery of the colored proteins. PEG1450‐phosphate ATPS extraction (volume ratio (V_R) equal to 0.3, tie‐line length (TLL) of 34 % w/w and system pH 7.0) for the recovery of c‐phycocyanin from Spirulina maxima resulted in a primary recovery process that produced a protein purity of 2.1 ± 0.2 (defined as the relationship of 620 nm to 280 nm absorbance) and a product yield of 98 % [w/w]. PEG1000‐phosphate ATPS extraction (i.e., V_R = 1.0, PEG 1000, TLL 50 % w/w and system pH 7.0) was preferred for the recovery of b‐phycoerythrin from Porphyridium cruentum, which resulted in a protein purity of 2.8 ± 0.2 (defined as the relationship of 545 nm to 280 nm absorbance) and a product yield of 82 % [w/w]. The purity of c‐phycocyanin and b‐phycoerythrin from the crude extract increased 3‐ and 4‐fold, respectively, after ATPS. The results reported herein demonstrated the benefits of the practical generic application of ATPS for the primary recovery of colored proteins from microbial origin as a first step for the development of purification processes.     

Lysozyme extraction from hen egg white in an aqueous two-phase system composed of ethylene oxide–propylene oxide thermoseparating copolymer and potassium phosphate

The recovery and purification of lysozyme from hen egg white has been investigated in an aqueous two-phase systems composed of thermoseparating random copolymers of ethylene oxide (EO), propylene oxide (PO) and potassium phosphate. In the primary extraction step lysozyme was satisfactorily partitioned to the top polymer-rich phase in a system composed of 40% (w/w) EO₅₀PO₅₀, 10% (w/w) potassium phosphate, and 0.85 M sodium chloride at pH 9.0, diluted 3-fold with crude egg white, where contaminating proteins were discarded in the bottom phosphate-rich phase. After the primary phase separation the upper EO₅₀PO₅₀ phase was removed and subjected to temperature-induced (65 °C) phase separation, which resulted in the partitioning of pure lysozyme to the top water phase. The separation system was found to be efficient in achieving the purification of lysozyme in a high yield of 85% and specific activity of 32,300 U/mg of protein, with a purification factor of 16.9 and a concentration of lysozyme in the water phase of 2.3 g/l in two extraction steps.     

Reversibility of structural transition of cytochrome c on interacting with and releasing from alternating copolymers of maleic Acid and alkene

The interaction of cytochrome c (cyt c) with poly(isobutylene-alt-maleic acid) (PIMA) and poly(1-tetradecene-alt-maleic acid) (PTMA) was studied using circular dichroism, absorption spectroscopy, and atomic force microscopy to investigate the electrostatic and hydrophobic influence of the copolymers on the structure of cyt c. At pH 7.4, the interaction of PIMA with cyt c can only partly disturb the integrity of the heme pocket, while PTMA has very intensive influence on the structure of cyt c. After adding 0.15 M NaCl, PIMA-cyt c complexes dissociate, and the released cyt c recovers its native structure, whereas NaCl has no significant influence on PTMA-cyt c complexes. GuHCl (0.5 M) destroys PTMA-cyt c complexes, forming GuHCl-PTMA precipitates; the cyt c released from the complexes regenerates its native structure. In comparison with electrostatic interaction, hydrophobic interaction leads to more stable polymer-cyt c complexes and more intensive influence on cyt c structure, but cyt c can recover its native state after release.     

Recovery of residual soluble protein by two-step precipitation process with concomitant COD reduction from the yeast-cultivated cheese whey

The present study was conducted to recover the residual soluble protein after cultivation of yeast (K. marxianus) in cheese whey. Cheese whey continuous fermentation with cell recycle system was carried out at 40 °C and pH 3.5. The yeast biomass was separated from the fermented broth by centrifugation and residual soluble protein from fermented whey supernatant was precipitated by heat treatment (at 100 °C, pH 4.5 and 10 min incubation). The maximum soluble protein recovery up to 53 % was achieved at pH 4.5 with 54 % residual COD removal. However, gravity sedimentable precipitates were obtained at pH 3.5 with 47 % protein recovery. Therefore, the reactor (scale up) study was conducted at pH 3.5 with agitation, which resulted in 68 % of residual soluble protein recovery and simultaneously residual COD removal of 62 %. Further precipitation/coagulation of soluble protein was also evaluated using carboxymethylcellulose (CMC) and then two precipitation (thermal followed by CMC precipitation) processes were combined to increase the protein precipitation, which finally reached up to 81 % of total soluble protein recovery from the supernatant. This optimized process could be applied to recover the residual protein left after fermentation of cheese whey without centrifugation.     

Reversible, nonionic, and pH-dependent association of cytochrome c with cardiolipin-phosphatidylcholine liposomes.

Membrane association of cytochrome c (cyt c) was monitored by the efficiency of resonance energy transfer from a pyrene-fatty acid containing phospholipid derivative (1-palmitoyl-2[6-(pyren-1-yl)]hexanoyl-sn-glycero-3-phosphocholine (PPHPC)) to the heme of cyt c. Liposomes consisted of 85 mol% egg phosphatidylcholine (egg PC), 10 mol% cardiolipin, and 5 mol% PPHPC. Cardiolipin was necessary for the membrane binding of cyt c over the pH range studied, from 4 to 7. In accordance with the electrostatic nature of the membrane association of cyt c at neutral pH both 2 mM MgCl2 and 80 mM NaCl dissociated cyt c from the vesicles completely. At neutral pH also adenine nucleotides in millimolar concentrations were able to displace cyt c from liposomes, their efficiency decreasing in the sequence ATP > ADP > AMP. In addition, both CTP and GTP were equally effective as ATP. The detachment of cyt c from liposomes by nucleotides is likely to result from a competition between cardiolipin and the nucleotides for a common binding site in cyt c. When pH was decreased to 4 there was a small yet significant increase in the apparent affinity of cyt c to cardiolipin containing liposomes. Notably, at pH 4 the above nucleotides as well as NaCl and MgCl2 were no longer able to dissociate cyt c and, on the contrary, they slightly enhanced the quenching of pyrene fluorescence by cyt c. The above results do suggest that the membrane association of cyt c at acidic pH was non-ionic and presumably due to hydrogen bonding. The pH-dependent binding of cyt c to membranes was fully reversible. Accordingly, in the presence of sufficient concentrations of either nucleotides or salts rapid detachment and membrane association of cyt c could be induced by varying pH between neutral and acidic values, respectively.     

Enhancing Manganese Recovery from Low-Grade Ores by Using Mixed Culture of Indigenously Isolated Bacterial Strains

Conventional leaching methods for manganese (Mn) recovery require strong acids and are threatening to the environment. Alternatively, the use of microbes for Mn recovery is environment friendly in nature. The present investigation compares the capacity of pure and mixed cultures of native bacterial strains for bioleaching of low-grade Mn ores. The ability of the isolated microorganisms to recover Mn was evaluated in shake flasks for 20 days under optimized conditions of pulp density (2%), sucrose concentration (2 g/100 mL), initial pH 6.5, and 30°C incubation temperature. In pure culture form, Acinetobacter sp. MSB 5 (70%) was found to have a higher bioleaching potential than Lysinibacillus sp. MSB 11 (67%). Mixed culture of Acinetobacter sp. MSB 5 and Lysinibacillus sp. MSB 11 was found to perform better than the pure cultures with 74% extraction of Mn. The presence of mixed culture increased the dissolution rate and the recovery percentage of Mn. The respective growth pattern of the cultures was in synchronization to their Mn bioleaching performances. This study underlines the importance of mixed cultures and Mn solubilizing activity of native bacterial strains for efficient Mn biorecovery.     

Production and Partial Purification of Tannase from Aspergillus ficuum Gim 3.6

A novel fungal strain, Aspergillus ficuum Gim 3.6, was evaluated for its tannase-producing capability in a wheat bran-based solid-state fermentation. Thin-layer chromatography (TLC) analysis revealed that the strain was able to degrade tannic acid to gallic acid and pyrogallol during the fermentation process. Quantitation of enzyme activity demonstrated that this strain was capable of producing a relatively high yield of extracellular tannase. Single-factor optimization of process parameters resulted in high yield of tannase after 60 hr of incubation at a pH of 5.0 at 30°C, 1 mL of inoculum size, and 1:1 solid–liquid ratio in the presence of 2.0% (w/v) tannic acid as inducer. The potential of aqueous two-phase extraction (ATPE) for the purification of tannase was investigated. Influence of various parameters such as phase-forming salt, molecular weight of polyethylene glycol (PEG), pH, and stability ratio on tannase partition and purification was studied. In all the systems, the target enzyme was observed to preferentially partition to the PEG-rich top phase, and the best result of purification (2.74-fold) with an enzyme activity recovery of 77.17% was obtained in the system containing 17% (w/w) sodium citrate and 18.18% (w/w) PEG1000, at pH 7.0.     

Detection and automatic control of ammonium ion concentration in miceobial culture with an ammonium ion selective electrode

An ammonium ion selective electrode (AISE) had a membrane of polyvinyl chloride in which the antibodies nonactin and monacin were embedded. The detection range was 0.1–200 mM. The step response was 90% in 20 seconds. The output of the AISE increased 6% with a 1°C rise temperature. The output of the AISE was constant between pH 4–7. The selectively coefficient of potassium ion was 0.158 and hence its interferring effect must be considered. The selectivity coeficcients of other cations were small enough to be negligible. Throughout a batch culture of Escherichia coli, values calculated by subtrating (selectivity coefficient) × (potassium ion concentration) from the detected output of the AISE agreed with actual concentrations of ammonium ion. An automatic. constant-value, feebdack control system of ammonium ion concentration was attempted by on-off controlled supply of solution containing both ammonium and potassium ions, the proportion of whose concentration was made equal to the proportion of their average volumetric consumption rates by a microorganism in batch culture. By this control system, ammonium ion concentrations in culture supernatants of fed-batch cultures of Escherichia coli and Saccharomyces cerevisiae could be maintained vitrually at constant levels (5±0.8 mM for the cultivation of E. coli and 50±5 M for the cultivation of S. cerevisiae).     

The effects of environmental conditions on persistence and inactivation of Brucella suis on building material surfaces

Aims: The purpose of this study was to evaluate the effects of environmental conditions and material type on persistence and inactivation of Brucella suis. Methods and Results: Brucella suis (approx. 1 × 10⁸ CFU) was spiked onto surfaces (glass, aluminium and wood) by liquid inoculation. Persistence was evaluated over 56 days at 22 ± 2°C, 40 ± 15% r.h. and 5 ± 3°C, 30 ± 15% r.h. In addition, three readily available decontaminants (pH‐adjusted bleach, 70% ethanol and 1% citric acid) were evaluated for their effectiveness at inactivating Br. suis on these materials. Decontaminations were conducted following 0 and 28 days exposure to the two conditions. Results indicated that Br. suis can persist on environmental surfaces for at least 56 days. Persistence was highest at low temperature. Decontamination was most challenging on wood with all three decontaminants. Conclusions: Following a Br. suis contamination incident, passive decontamination (through attenuation) may not be feasible, as this organism can persist for months. In addition, the results suggest that some sporicidal decontaminants may be ineffective on materials such as wood, even for vegetative biological agents such as Br. suis. Significance and Impact of Study: This study aids incident commanders and remediation experts to make informed decisions regarding decontamination after a biological contamination incident.     

Determination of free serum didanosine by ultrafiltration and high-performance liquid chromatography

An isocratic reversed-phase high-performance liquid chromatographic method was developed to determine free didanosine concentrations in human serum. An ultrafiltration technique was used to recover didanosine from the samples. Didanosine was analyzed using a 150 mm × 3.9 mm I.D. Nova-Pak phenyl column and a mobile phase of 0.02 M sodium citrate (pH 5)-isopropanol (97.5:2.5, v/v) with detection set at 250 nm. Linearity was verified from 25 to 3000 ng/ml. The limit of detection at a signal-to-noise ratio of 3 was 25 ng/ml. The mean recovery of didanosine added to serum at 50, 100, 250 and 750 ng/ml was 97.4%, 97.3%, 92.9% and 95.4%, respectively. A within-day variation of 3.6% at 50 ng/ml and 1.7% at 250 ng/ml, and a day-to-day variation of 9.3% at 50 ng/ml and 3.6% at 230 ng/ml were found. Stability studies indicated that didanosine is stable in serum for at least 8.5 months at 20°C, 4°C and −20°C.     

The pH-dependent recovery of smooth muscle from storage at -13 degrees C in unfrozen media.

The function of isolated strips of smooth muscle from the guinea pig were assessed by isometric contractile responses to histamine before and after storage at ?13 °C in high potassium, Pipes-buffered solutions containing 30% (w/v) Me₂SO and having different pH values. The structural integrity of the tissue during and after cooling was also assessed by electron microscopy.The pH-dependence of tissue recovery in these muscles was clearly demonstrated after about 17-hr storage at ?13 °C. Despite the wide difference in functional recoveries between groups of muscles cooled in either “high” (7.7) or “low pH” (6.4) media, however, there were no apparent ultrastructural differences between the two differently treated groups of muscles. Muscles from both pH groups, fixed after rewarming to 37 °C, showed the morphological characteristics typically seen in noncooled muscles. An examination of muscle cells which were fixed at ?13 °C (w/v) Me₂SO revealed that the contractile myofibrils of specimens in both experimental groups had undergone a noticeable reorganization and aggregation.     

溴化1-己基-3-甲基咪唑对斜生栅藻谷胱甘肽及其代谢酶的影响

研究了浓度为0、1、5、10、15、20 mg/L的新兴离子液体溴化1-己基-3-甲基咪唑([C6mim]Br)在24h、48h、72h和96h对斜生栅藻还原型谷胱甘肽（GSH）及其代谢酶-谷胱甘肽过氧化物酶（GPX）、谷胱甘肽转硫酶（GST）和谷胱甘肽还原酶（GR）的影响。结果表明：GSH含量在24h、48h和72h时,在最低处理浓度下不变,其他处理浓度下随胁迫浓度增加而降低,96h时则与对照无差异或较小;GPX和GST的活性在72h之前明显升高（最高浓度组的GST活性有波动）,96h时均降低至对照水平;GR活性在24h时,[C6mim]Br=1 mg/L时升高,之后降低,在48h增高至对照水平,72h时,[C6mim]Br≥10 mg/L的处理组高于对照水平,96h时,除最低处理组外,均降至对照水平以下。GR是GSH系统中的限速酶,GST则是该系统中活性和灵敏性最高的酶,可作为[C6mim]Br胁迫时的敏感的生物标志物。1 mg/L的[C6mim]Br可引起藻细胞的氧化胁迫,具有环境毒性。     

Improving cell viability using counterflow centrifugal elutriation

BackgroundCell viability is an important release criterion in the manufacturing of cell therapy products. Low cell viability can have significant impact on product quality and manufacturing efficiency. Counterflow centrifugation technology has been applied to the manufacturing of cell therapy products, to enable cell separation based on size and density. This study evaluated the utility of counterflow centrifugation technology for dead cell removal to improve cell viability of the final product.MethodsJurkat cell cultures with low and high dead cell burden were subjected to counterflow centrifugal elutriation to determine the correlation between process parameters (e.g., flow rate, centrifugal force) and processing outcomes (i.e., cell recovery and viability). Subsequently, the optimized parameters were applied to dead cell elutriation using expanded T cells and freshly isolated human amniotic epithelial cells (hAECs). The efficiency of dead cell removal, cell function and post-thaw viability were compared.ResultsElutriation using a low flow rate allowed better control of viable cell recovery from both low and high dead cell burden cultures of Jurkat cells. The viability of T cells and hAECs was improved by counterflow centrifugal processing, from 80.67% ± 2.33 to 94.73% ± 1.19 and 79.19% ± 5.35 to 90.34% ± 3.59, respectively. Processing increased the proliferation rate of T cells, while the metabolic activity of hAECs was unchanged.ConclusionCounterflow centrifugal elutriation can be added as an integrated step to the automated wash-and-concentrate protocol for cell manufacturing to remove dead cells and improve cell viability of the final product.     

Salting-out extraction and crystallization of succinic acid from fermentation broths

In this study, salting-out extraction (SOE) and crystallization were combined to recover succinic acid from fermentation broths. Of the different SOE systems investigated, the system consisting of organic solvents and acidic salts appeared to be more favorable. A system using acetone and ammonium sulfate was investigated to determine the effect of phase composition and pH. The highest partition coefficient (8.64) and yield of succinic acid (90.05%) were obtained by a system composed of 30% (w/w) acetone and 20% (w/w) ammonium sulfate at a pH of 3.0. Additionally, 99.03% of cells, 90.82% of soluble proteins, and 94.89% of glucose could be simultaneously removed from the fermentation broths. Interestingly, nearly 40% of the pigment was removed using the single-step salting-out extraction process. The analysis of the effect of pH on salting-out extraction indicates that a pH lower than the pK of succinic acid is beneficial for the recovery of succinic acid in an SOE system. Crystallization was performed for the purification of succinic acid at 4 °C and pH 2.0. By combining salting-out extraction with crystallization, an identical total yield (65%) and a higher purity (97%) of succinic acid were obtained using a synthetic fermentation broth compared with the actual fermentation broth (65% and 91%, respectively).