Experimental investigations of multiple steady states in aerobic continuous cultivations of Saccharomyces cerevisiae

The steady-state behavior of a glucose-limited, aerobic, continuous cultivation of Saccharomyces cerevisiae CEN.PK113-7D was investigated around the critical dilution rate. Oxido-reductive steady states were obtained at dilution rates up to 0.09 h(-1) lower than the critical dilution rate by operating the bioreactor as a productostat, where the dilution rate was controlled on the basis of an ethanol measurement. Thus, the experimental investigations revealed that multiple steady states exist in a region of dilution rates below the critical dilution rate. The existence of multiple steady states was attributed to two distinct physiological effects occurring when growth changed from oxidative to oxido-reductive: (i) a decrease in the efficiency of ATP production and utilization (at ethanol concentrations below 3 g/L) and (ii) repression of the oxidative metabolism (at higher ethanol concentrations). The first effect was best observed at low ethanol concentrations, where multiple steady states were observed even when no repression of the oxidative metabolism was evident, i.e., the oxidative capacity was constant. However, at higher ethanol concentrations repression of the oxidative metabolism was observed (the oxidative capacity decreased), and this resulted in a broader range of dilution rates where multiple steady states could be found.     

An edeine resistant mRNA-dependent protein synthesis system from a Saccharomyces cerevisiae mutant

A cell-free protein synthesizing system from a mutant of Saccharomyces cerevisiae translated exogenous mRNA in the presence of 2 microM edeine, while a similar system from wild-type strain was completely inhibited by the drug. The mutant ribosomes showed an affinity for [125I]edeine comparable to the wild-type ribosomes, thereby suggesting that these macromolecules alone were not responsible for the edeine-resistant capacity of the mutant.     

A global S. cerevisiae small ubiquitin‐related modifier (SUMO) system interactome

The small ubiquitin‐related modifier (SUMO) system has been implicated in a number of biological functions, yet the individual components of the SUMO machinery involved in each of these activities were largely unknown. Here we report the first global SUMO system interactome. Using affinity purification coupled with mass spectrometry, we identify >450 protein–protein interactions surrounding the SUMO E2, Siz type E3s and SUMO‐specific proteases in budding yeast. Exploiting this information‐rich resource, we validate several Siz1‐ and Siz2‐specific substrates, identify a nucleoporin required for proper Ulp1 localization, and uncover important new roles for Ubc9 and Ulp2 in the maintenance of ribosomal DNA.     

Mimic of a large‐scale diafiltration process by using ultra scale‐down rotating disc filter

Ultra scale‐down (USD) approach is a powerful tool to predict large‐scale process performance by using very small amounts of material. In this article, we present a method to mimic flux and transmission performance in a labscale crossflow operation by an USD rotating disc filter (RDF). The Pellicon 2 labscale system used for evaluation of the mimic can readily be related to small pilot and industrial scale. Adopted from the pulsed sample injection technique by Ghosh and Cui (J Membr Sci. 2000;175:5‐84), the RDF has been modified by building in inserts to allow the flexibility of the chamber volume, so that only 1.5 mL of processing material is required for each diafiltration experiment. The reported method enjoys the simplicity of dead‐end mode operation with accurate control of operation conditions that can mimic well the crossflow operation in large scale. Wall shear rate correlations have been established for both the labscale cassette and the USD device, and a mimic has been developed by operating both scales under conditions with equivalent averaged shear rates. The studies using E. coli lysate show that the flux vs. transmembrane pressure profile follows a first‐order model, and the transmission of antibody fragment (Fab′) is independent of transmembrane pressure. Predicted flux and transmission data agreed well with the experimental results of a labscale diafiltration where the cassette resistance was considered. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Continuous removal of endocrine disruptors by versatile peroxidase using a two‐stage system

The oxidant Mn³⁺‐malonate, generated by the ligninolytic enzyme versatile peroxidase in a two‐stage system, was used for the continuous removal of endocrine disrupting compounds (EDCs) from synthetic and real wastewaters. One plasticizer (bisphenol‐A), one bactericide (triclosan) and three estrogenic compounds (estrone, 17β‐estradiol, and 17α‐ethinylestradiol) were removed from wastewater at degradation rates in the range of 28–58 µg/L·min, with low enzyme inactivation. First, the optimization of three main parameters affecting the generation of Mn³⁺‐malonate (hydraulic retention time as well as Na‐malonate and H₂O₂ feeding rates) was conducted following a response surface methodology (RSM). Under optimal conditions, the degradation of the EDCs was proven at high (1.3–8.8 mg/L) and environmental (1.2–6.1 µg/L) concentrations. Finally, when the two‐stage system was compared with a conventional enzymatic membrane reactor (EMR) using the same enzyme, a 14‐fold increase of the removal efficiency was observed. At the same time, operational problems found during EDCs removal in the EMR system (e.g., clogging of the membrane and enzyme inactivation) were avoided by physically separating the stages of complex formation and pollutant oxidation, allowing the system to be operated for a longer period (～8 h). This study demonstrates the feasibility of the two‐stage enzymatic system for removing EDCs both at high and environmental concentrations. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:908–916, 2015     

Ethanol addition on inactivation of Saccharomyces pastorianus by a two‐stage system with low‐pressure carbon dioxide microbubbles can accelerate the cell membrane injury

The effect of ethanol on the inactivation of Saccharomyces pastorianus by a two‐stage system with low‐pressure carbon dioxide microbubbles (two‐stage MBCO₂) was investigated. Zero and >5 log reductions of S. pastorianus populations suspended in physiological saline (PS) containing 0% and 10% ethanol, respectively, occurred by the two‐stage MBCO₂ at a mixing vessel pressure of 1 MPa and a heating coil temperature of 40°C. Conversely, the detected number of surviving S. pastorianus cells in PS containing 5% ethanol was higher in yeast and mold agar (YMA, an optimum agar) than YMA with 2.5% sodium chloride, followed by yeast nitrogen base agar (YNBA, a minimum agar). The fluorescence polarization of S. pastorianus in PS containing 5% and 10% ethanol increased similarly with exposure time in the heating coil of two‐stage MBCO₂ and was correlated with the surviving cell number measured in YNBA. The intracellular pH (pH_in) of S. pastorianus in PS containing 5% ethanol decreased linearly with exposure time in the heating coil of two‐stage MBCO₂. Also, the pH_in‐lowering of S. pastorianus in PS containing 10% ethanol was drastically caused by two‐stage MBCO₂ at 1 min exposure time in the heating coil but then stayed constant until 5 min, agreeing with the inactivation efficiency. Therefore, ethanol in S. pastorianus suspension was suggested to accelerate the cell membrane injury caused by two‐stage MBCO₂. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 34:282–286, 2018     

Ultra scale‐down device to predict dewatering levels of solids recovered in a continuous scroll decanter centrifuge

During centrifugation operation, the major challenge in the recovery of extracellular proteins is the removal of the maximum liquid entrapped within the spaces between the settled solids–dewatering level. The ability of the scroll decanter centrifuge (SDC) to process continuously large amounts of feed material with high concentration of solids without the need for resuspension of feeds, and also to achieve relatively high dewatering, could be of great benefit for future use in the biopharmaceutical industry. However, for reliable prediction of dewatering in such a centrifuge, tests using the same kind of equipment at pilot‐scale are required, which are time consuming and costly. To alleviate the need of pilot‐scale trials, a novel USD device, with reduced amounts of feed (2 mL) and to be used in the laboratory, was developed to predict the dewatering levels of a SDC. To verify USD device, dewatering levels achieved were plotted against equivalent compression (Gt_comp) and decanting (Gt_dec) times, obtained from scroll rates and feed flow rates operated at pilot‐scale, respectively. The USD device was able to successfully match dewatering trends of the pilot‐scale as a function of both Gt_comp and Gt_dec, particularly for high cell density feeds, hence accounting for all key variables that influenced dewatering in a SDC. In addition, it accurately mimicked the maximum dewatering performance of the pilot‐scale equipment. Therefore the USD device has the potential to be a useful tool at early stages of process development to gather performance data in the laboratory thus minimizing lengthy and costly runs with pilot‐scale SDC. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1494–1502, 2013     

Controllable extracellular biosynthesis of bismuth sulfide nanostructure by sulfate‐reducing bacteria in water–oil two‐phase system

Due to strong hydrolysis of Bi³⁺ as precursor in aqueous media, there are no reports on biosynthesis of bismuth sulfide (Bi₂S₃) nanomaterials. In this work, the water–oil two‐phase system was used to biosynthesize the Bi₂S₃ nanomaterials based on the coupling reaction of biological reduction and chemical precipitation process for the first time. The results showed that the water–oil two‐phase system successfully eliminated hydrolysis of the Bi³⁺ and controllably and extracellularly fabricated the Bi₂S₃ crystal with high purity. The nanorods with diameter of about 100 nm and length of about 1.0 μm were attained under high dose of lactic acid and SO₄^2?; while low dose obtained the nanobundles consisted of nanoneedles with tip diameter of 10–20 nm and length of about 5.0–10.0 μm. The Bi₂S₃ nanorods as photocatalyst almost completely degraded methylene blue from solution within 12 h; whereas the Bi₂S₃ nanobundles removed about 87% of the dye. The amount of the Bi₂S₃ nanorods decreased by 48% due to photocorrosion, whereas 52% with the nanobundles. The Bi₂S₃ nanorods had relatively higher photocatalysis activity and slightly stronger photocorrosion resistance than the Bi₂S₃ nanobundles. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:960–966, 2014     

Enhancement of glutathione production by altering adenosine metabolism of Escherichia coli in a coupled ATP regeneration system with Saccharomyces cerevisiae

Aims: Adenosine triphosphate (ATP) during the enzymatic production of glutathione is necessary. In this study, our aims were to investigate the reason for low glutathione production in Escherichia coli coupled with an ATP regeneration system and to develop a new strategy to improve the system. Methods and Results: Glutathione can be synthesized by enzymatic methods in the presence of ATP and three precursor amino acids (l ‐glutamic acid, l ‐cysteine and glycine). In this study, glutathione was produced from E. coli JM109 (pBV03) coupled with an ATP regeneration system, by using glycolytic pathway of Saccharomyces cerevisiae WSH2 as ATP regenerator from adenosine and glucose. In the coupled system, adenosine used for ATP regeneration by S. cerevisiae WSH2 was transformed into hypoxanthine irreversibly by E. coli JM109 (pBV03). As a consequence, S. cerevisiae WSH2 could not obtain enough adenosine for ATP regeneration in the glycolytic pathway in spite of consuming 400 mmol l^?1 glucose within 1 h. By adding adenosine deaminase inhibitor to block the metabolism from adenosine to hypoxanthine, glutathione production (8·92 mmol l^?1) enhanced 2·74‐fold in the coupled system. Conclusions: This unusual phenomenon that adenosine was transformed into hypoxanthine irreversibly by E. coli JM109 (pBV03) revealed that less glutathione production in the coupled ATP regeneration system was because of the poor efficiency of ATP generation. Significance and Impact of the Study: The results presented here provide a strategy to improve the efficiency of the coupled ATP regeneration system for enhancing glutathione production. The application potential can be microbial processes where ATP is needed.     

Strategy for comprehensive identification of human N‐myristoylated proteins using an insect cell‐free protein synthesis system

To establish a strategy for the comprehensive identification of human N‐myristoylated proteins, the susceptibility of human cDNA clones to protein N‐myristoylation was evaluated by metabolic labeling and MS analyses of proteins expressed in an insect cell‐free protein synthesis system. One‐hundred‐and‐forty‐one cDNA clones with N‐terminal Met‐Gly motifs were selected as potential candidates from ～2000 Kazusa ORFeome project human cDNA clones, and their susceptibility to protein N‐myristoylation was evaluated using fusion proteins, in which the N‐terminal ten amino acid residues were fused to an epitope‐tagged model protein. As a result, the products of 29 out of 141 cDNA clones were found to be effectively N‐myristoylated. The metabolic labeling experiments both in an insect cell‐free protein synthesis system and in the transfected COS‐1 cells using full‐length cDNA revealed that 27 out of 29 proteins were in fact N‐myristoylated. Database searches with these 27 cDNA clones revealed that 18 out of 27 proteins are novel N‐myristoylated proteins that have not been reported previously to be N‐myristoylated, indicating that this strategy is useful for the comprehensive identification of human N‐myristoylated proteins from human cDNA resources.     

Production of recombinant HIV‐1 nef protein using different expression host systems: A techno‐economical comparison

Three popular expression host systems Escherichia coli, Pichia pastoris and Drosophila S2 were analyzed techno‐economically using HIV‐1 Nef protein as the model product. On scale of 100 mg protein, the labor costs corresponded to 52–83% of the manufacturing costs. When analyzing the cost impact of the different phases (strain/cell line construction, bioreactor production, and primary purification), we found that with the microbial host systems the strain construction phase was most significant generating 56% (E. coli) and 72% (P. pastoris) of the manufacturing costs, whereas with the Drosophila S2 system the cell line construction and bioreactor production phases were equally significant (46 and 47% of the total costs, respectively). With different titers and production goal of 100 mg of Nef protein, the costs of P. pastoris and Drosophila S2 systems were about two and four times higher than the respective costs of the E. coli system. When equal titers and bioreactor working volumes (10 L) were assumed for all three systems, the manufacturing costs of the bioreactor production of the P. pastoris and Drosophila S2 systems were about two and 2.5 times higher than the respective costs of the E. coli system. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Effect of aeration and agitation on extractive fermentation of clavulanic acid by using aqueous two‐phase system

In this work, the effects of agitation and aeration rates on aqueous two‐phase system (ATPS)‐based extractive fermentation of clavulanic acid (CA) by Streptomyces variabilis DAUFPE 3060 were investigated through a 2² full factorial design, where oxygen transfer rate (OTR) and oxygen uptake rate (OUR) were selected as the responses. Aeration rates significantly influenced cell growth, OUR, and CA yield, while OTR was practically the same in all the runs. Under the intermediate agitation (950 rpm) and aeration conditions (3.5 vvm) of the central point runs, it was achieved OTR of 1.617 ± 0.049 mmol L^?1 h^?1, OUR of 0.132 ± 0.030 mmol L^?1 h^?1, maximum CA production of 434 ± 4 mg L^?1, oxygen mass transfer coefficient of 33.40 ± 2.01 s^?1, partition coefficient of 66.5 ± 1.5, CA yield in the top and bottom phases of 75% ± 2% and 19% ± 1%, respectively, mass balance of 95% ± 4% and purification factor of 3.8 ± 0.1. These results not only confirmed the paramount role of O₂ supply, broth composition and operational conditions in CA ATPS‐extractive fermentation, but also demonstrated the possibility of effectively using this technology as a cheap tool to simultaneously produce and recover CA. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1444–1452, 2016     

Transformation of ferulic acid to vanillin using a fed‐batch solid–liquid two‐phase partitioning bioreactor

Amycolatopsis sp. ATCC 39116 (formerly Streptomyces setonii) has shown promising results in converting ferulic acid (trans‐4‐hydroxy‐3‐methoxycinnamic acid; substrate), which can be derived from natural plant wastes, to vanillin (4‐hydroxy‐3‐methoxybenzaldehyde). After exploring the influence of adding vanillin at different times during the growth cycle on cell growth and transformation performance of this strain and demonstrating the inhibitory effect of vanillin, a solid–liquid two‐phase partitioning bioreactor (TPPB) system was used as an in situ product removal technique to enhance transformation productivity by this strain. The thermoplastic polymer Hytrel^® G4078W was found to have superior partitioning capacity for vanillin with a partition coefficient of 12 and a low affinity for the substrate. A 3‐L working volume solid–liquid fed‐batch TPPB mode, using 300 g Hytrel G4078W as the sequestering phase, produced a final vanillin concentration of 19.5 g/L. The overall productivity of this reactor system was 450 mg/L. h, among the highest reported in literature. Vanillin was easily and quantitatively recovered from the polymers mostly by single stage extraction into methanol or other organic solvents used in food industry, simultaneously regenerating polymer beads for reuse. A polymer–liquid two phase bioreactor was again confirmed to easily outperform single phase systems that feature inhibitory or easily further degraded substrates/products. This enhancement strategy might reasonably be expected in the production of other flavor and fragrance compounds obtained by biotransformations. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:207–214, 2014     

Evaluation of options for harvest of a recombinant E. Coli fermentation producing a domain antibody using ultra scale‐down techniques and pilot‐scale verification

Ultra scale‐down (USD) methods operating at the millilitre scale were used to characterise full‐scale processing of E. coli fermentation broths autolysed to different extents for release of a domain antibody. The focus was on the primary clarification stages involving continuous centrifugation followed by depth filtration. The performance of this sequence was predicted by USD studies to decrease significantly with increased extents of cell lysis. The use of polyethyleneimine reagent was studied to treat the lysed cell broth by precipitation of soluble contaminants such as DNA and flocculation of cell debris material. The USD studies were used to predict the impact of this treatment on the performance and here it was found that the fermentation could be run to maximum productivity using an acceptable clarification process (e.g., a centrifugation stage operating at 0.11 L/m² equivalent gravity settling area per hour followed by a resultant required depth filter area of 0.07 m²/L supernatant). A range of USD predictions was verified at the pilot scale for centrifugation followed by depth filtration. © 2016 The Authors Biotechnology Progress published by Wiley Periodicals, Inc. on behalf of American Institute of Chemical Engineers Biotechnol. Prog., 32:382–392, 2016     

A shift in protein S‐palmitoylation,with persistence of growth‐associated substrates,marks a critical period for synaptic plasticity in developing brain

In the mammalian cortex, the initial formation of synaptic connections is followed by a prolonged period during which synaptic circuits are functional, but retain an elevated capacity for activity‐dependent remodeling and functional plasticity. During this period, synaptic terminals appear fully mature, morphologically and physiologically. We show here, however, that synaptic terminals during this period are distinguished by their simultaneous accumulation of multiple growth‐associated proteins at levels characteristic of axonal growth cones, and proteins involved in synaptic transmitter release at levels characteristic of adult synapses. We show further that newly formed synapses undergo a switch in the dynamic S‐palmitoylation of proteins early in the critical period, which includes a large and specific decrease in the palmitoylation of GAP‐43 and other major substrates characteristic of growth cones. Previous studies have shown that a similar reduction in ongoing palmitoylation of growth cone proteins is sufficient to stop advancing axons in vitro, suggesting that a developmental switch in protein S‐palmitoylation serves to disengage the molecular machinery for axon extension in the absence of local triggers for remodeling during the critical period. Only much later does a decline in the availability of major growth cone components mark the molecular maturation of cortical synapses at the close of the critical period. © 1999 John Wiley & Sons, Inc. J Neurobiol 39: 423–437, 1999     

RANBP2 is an allosteric activator of the conventional kinesin‐1 motor protein,KIF5B,in a minimal cell‐free system

The association of cargoes to kinesins is thought to promote kinesin activation, yet the validation of such a model with native cargoes is lacking because none is known to activate kinesins directly in an in vitro system of purified components. The RAN‐binding protein 2 (RANBP2), through its kinesin‐binding domain (KBD), associates in vivo with kinesin‐1, KIF5B/KIF5C. Here, we show that KBD and its flanking domains, RAN GTPase‐binding domains 2 and 3 (RBD2/RBD3), activate the ATPase activity of KIF5B approximately 30‐fold in the presence of microtubules and ATP. The activation kinetics of KIF5B by RANBP2 is biphasic and highly cooperative. Deletion of one of its RBDs lowers the activation of KIF5B threefold and abolishes cooperativity. Remarkably, RBD2–KBD–RBD3 induces unfolding and modest activation of KIF5B in the absence of microtubules. Hence, RANBP2 is the first native and positive allosteric activator known to jump‐start and boost directly the activity of a kinesin.     

Optimization of the bioprocessing conditions for scale‐up of transient production of a heterologous protein in plants using a chemically inducible viral amplicon expression system

Use of transient expression for the rapid, large‐scale production of recombinant proteins in plants requires optimization of existing methods to facilitate scale‐up of the process. We have demonstrated that the techniques used for agroinfiltration and induction greatly impact transient production levels of heterologous protein. A Cucumber mosaic virus inducible viral amplicon (CMViva) expression system was used to transiently produce recombinant alpha‐1‐antitrypsin (rAAT) by co‐infiltrating harvested Nicotiana benthamiana leaves with two Agrobacterium tumefaciens strains, one containing the CMViva expression cassette carrying the AAT gene and the other containing a binary vector carrying the gene silencing suppressor p19. Harvested leaves were both infiltrated and induced by either pressure or vacuum infiltration. Using the vacuum technique for both processes, maximum levels of functional and total rAAT were elevated by (190 ± 8.7)% and (290 ± 7.5)%, respectively, over levels achieved when using the pressure technique for both processes. The bioprocessing conditions for vacuum infiltration and induction were optimized and resulted in maximum rAAT production when using an A. tumefaciens concentration at OD₆₀₀ of 0.5 and a 0.25‐min vacuum infiltration, and multiple 1‐min vacuum inductions further increased production 25% and resulted in maximum levels of functional and total rAAT at (2.6 ± 0.09)% and (4.1 ± 0.29)% of the total soluble protein, respectively, or (90 ± 1.7) and (140 ± 10) mg per kg fresh weight leaf tissue at 6 days post‐induction. Use of harvested plant tissue with vacuum infiltration and induction demonstrates a bioprocessing route that is fully amenable to scale‐up. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009