Temperature management strategy for efficient gene expression in a thermally inducible <Emphasis Type="Italic">Escherichia coli</Emphasis>/bacteriophage system

In a two-phase operation, E. coli containing λSNNU1 (Q ⁻ S ⁻) in the chromosome is typically cultured at 33°C and cloned gene expression is induced by elevating the temperature. At least 40°C is necessary for complete induction of cloned gene expression; however, temperatures above 40°C have been shown to inhibit cloned gene expression. This suggests that a three-phase operation, which has an induction phase between the growth and production phases, may result in higher gene expression. In this study, optimal temperature management strategies were investigated for the three-phase operation of cloned gene expression in thermally inducible E. coli/bacteriophage systems. The optimal temperature for the induction phase was determined to be 40°C. When the temperature of the production stage was 33°C, the optimal time period for the induction phase at 40°C was determined to be 60 min. In contrast, when the temperature of the production phase was 37°C, the optimal period for the induction phase at 40°C was 20∼30 min. When the three-phase temperature and temporal profile were set at a growth phase of 33°C, an induction phase at 40°C for 30 min, and a production phase at 37°C, the highest level of cloned gene expression was achieved.     

pHsh vectors,a novel expression system of <Emphasis Type="Italic">Escherichia coli</Emphasis> for the large-scale production of recombinant enzymes

Gene expression system Hsh is developed to increase enzyme production and to decrease the cost in the induction of gene expression in Escherichia coli. The vectors of Hsh system were constructed by combining a synthesized heat-shock promoter with a synthesized terminator and an origin of replication derived from pUC19 in which the expression of foreign genes was regulated by an alternative sigma factor, σ³² of E. coli. In comparison, the Hsh promoter gave a 2.4-fold higher production for xynIII gene encoding a xylanase than existing heat-shock inducible promoter p _L, 1.2-fold and 3-fold production for xar gene encoding a arabinosidase than trc and T₇ promoter, respectively. The flow-in-heat technique created a rapid rise in temperature for effective induction of gene expression in bioreactor scale.     

Optimization of norovirus virus‐like particle production in Pichia pastoris using a real‐time near‐infrared bioprocess monitor

The production of norovirus virus‐like particles (NoV VLPs) displaying NY‐ESO‐1 cancer testis antigen in Pichia pastoris BG11 Mut⁺ has been enhanced through feed‐strategy optimization using a near‐infrared bioprocess monitor (RTBio^® Bioprocess Monitor, ASL Analytical, Inc.), capable of monitoring and controlling the concentrations of glycerol and methanol in real‐time. The production of NoV VLPs displaying NY‐ESO‐1 in P. pastoris has potential as a novel cancer vaccine platform. Optimization of the growth conditions resulted in an almost two‐fold increase in the expression levels in the fermentation supernatant of P. pastoris as compared to the starting conditions. We investigated the effect of methanol concentration, batch phase time, and batch to induction transition on NoV VLP‐NY‐ESO‐1 production. The optimized process included a glycerol transition phase during the first 2 h of induction and a methanol concentration set point of 4 g L^?1 during induction. Utilizing the bioprocess monitor to control the glycerol and methanol concentrations during induction resulted in a maximum NoV VP1‐NY‐ESO‐1 yield of 0.85 g L^?1. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:518–526, 2016     

A gene cloning system for the siomycin producer <Emphasis Type="Italic">Streptomyces sioyaensis</Emphasis> NRRL-B5408

Streptomyces sioyaensis NRRL-B5408 produces a siomycin complex (a group of thiopeptide antibiotics structurally related to thiostrepton). Development of genetic tools for the detection of siomycin production and DNA transfer into this strain is described. The existing tipA-based reporter system for determination of siomycin production was modified to achieve its stable integration into actinomycete genomes. Various replicative plasmids (pKC1139, pKC1218E, pSOK101) as well as actinophage ϕC31- and VWB-based vectors pSET152 and pSOK804, respectively, were conjugally transferred from E. coli into the siomycin producer at a frequency ranging from 3.7 × 10⁻⁹ to 1.1 × 10⁻⁵. The transconjugants did not differ from wild type in their ability to produce siomycin. There is one attB site for each integrative plasmid. The utility of temperature sensitive replicon of pKC1139 for insertional gene inactivation in S. sioyaensis has been validated by disruption of putative nonribosomal peptide synthetase gene.     

Induction of phr gene expression by irradiation of ultraviolet light in Escherichia coli

Summary To measure the degree of phr gene induction by DNA-damaging agents, the promoter region was fused to the coding region of the lacZ gene in plasmid pMC1403. The new plasmids were introduced into Escherichia coli cells having different repair capabilities. More efficient induction of phr gene expression was detected in a uvrA ^– strain as compared with the wild-type strain. In addition, obvious induction was detected in uvrA ^– cells treated by 4-nitroquinoline 1-oxide and mitomycin C. Nalidixic acid, an inhibitor of DNA gyrase, also induced phr gene expression. In contrast, little induced gene expression was noted in UV-irradiated lexA ^– and recA ^– strains. It is suggested from these results that induction of the phr gene is one of the SOS responses. Possible nucleotide sequences which could be considered to constitute an SOS box were found at the regulator region of the phr gene.Abbreviations phr photoreactivation - UV ultraviolet light - 4NQO 4-nitroquinoline 1-oxide - MMC mitomycin C - PRE photoreactivating enzyme - E. coli Escherichia coli     

Biosynthesis of Yersiniabactin, a Complex Polyketide-Nonribosomal Peptide, Using Escherichia coli as a Heterologous Host

The medicinal value associated with complex polyketide and nonribosomal peptide natural products has prompted biosynthetic schemes dependent upon heterologous microbial hosts. Here we report the successful biosynthesis of yersiniabactin (Ybt), a model polyketide-nonribosomal peptide hybrid natural product, using Escherichia coli as a heterologous host. After introducing the biochemical pathway for Ybt into E. coli, biosynthesis was initially monitored qualitatively by mass spectrometry. Next, production of Ybt was quantified in a high-cell-density fermentation environment with titers reaching 67 ± 21 (mean ± standard deviation) mg/liter and a volumetric productivity of 1.1 ± 0.3 mg/liter-h. This success has implications for basic and applied studies on Ybt biosynthesis and also, more generally, for future production of polyketide, nonribosomal peptide, and mixed polyketide-nonribosomal peptide natural products using E. coli.     

Parallel steady state studies on a milliliter scale accelerate fed‐batch bioprocess design for recombinant protein production with Escherichia coli

In general, fed‐batch processes are applied for recombinant protein production with Escherichia coli (E. coli). However, state of the art methods for identifying suitable reaction conditions suffer from severe drawbacks, i.e. direct transfer of process information from parallel batch studies is often defective and sequential fed‐batch studies are time‐consuming and cost‐intensive. In this study, continuously operated stirred‐tank reactors on a milliliter scale were applied to identify suitable reaction conditions for fed‐batch processes. Isopropyl β‐d ‐1‐thiogalactopyranoside (IPTG) induction strategies were varied in parallel‐operated stirred‐tank bioreactors to study the effects on the continuous production of the recombinant protein photoactivatable mCherry (PAmCherry) with E. coli. Best‐performing induction strategies were transferred from the continuous processes on a milliliter scale to liter scale fed‐batch processes. Inducing recombinant protein expression by dynamically increasing the IPTG concentration to 100 µM led to an increase in the product concentration of 21% (8.4 g L^?1) compared to an implemented high‐performance production process with the most frequently applied induction strategy by a single addition of 1000 µM IPGT. Thus, identifying feasible reaction conditions for fed‐batch processes in parallel continuous studies on a milliliter scale was shown to be a powerful, novel method to accelerate bioprocess design in a cost‐reducing manner. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1426–1435, 2016     

Algicide production by the filamentous cyanobacteriumFischerellasp. CENA 19

The biosynthesis of algicides produced by a novelFischerellastrain was investigated. Two allelochemicals were identified, the aminoacylpolyketide fischerellin A (FsA) and the alkaloid 12-epi-hapalindole F (HapF). Based on the structure of FsA, genes that could be involved in its biosynthesis, including those encoding nonribosomal peptide synthetases (NRPSs) and a polyketide synthase (PKS), were identified by the polymerase chain reaction (PCR). By showing that the expression of NRPSs and PKSs is concomitant with algicide production we suggest that the identified genes may be involved in algicide biosynthesis. Analysis of an algicide preparation of the Brazilian-Amazonian strainFischerellasp. CENA 19 revealed the production of FsA,m/z409 (MH⁺), HapF,m/z370 (MH⁺), and other potential isoforms of the latter compounds, which were identified by high-performance liquid chromatography (HPLC) and matrix-assisted laser-desorption ionization time-of-flight (MALDI-TOF) mass-spectrometry. The production of HapF was confirmed after purification by HPLC, analysis by NMR, and high-resolution mass-spectrometry (HRMS). Two-NRPS and a PKS gene were identified after specific amplification using a degenerate PCR. The expression of these synthetases was confirmed by Western blot analysis employing enzyme family-specific antibodies. These analyses revealed the presence of three NRPSs and a single PKS inFischerellasp. CENA 19. The structure of FsA indicates both aminoacyl- and polyketide moeities, suggesting that its biosynthesis may require an integrated NRPS/PKS enzyme system, possibly involving the genes and the synthetases identified.     

Influence of acetate on the growth of recombinant Escherichia coli JM103 and product formation

The influence of the acetate addeed to the M9 minimal medium and to the Luria-Bertani medium without and with glucose supplement on the growth of recombinant Escherichia coli J103 with three different types of multicopy plasmids and on the production of the fusion protein SpA :: EcoRI were investigated in shake flasks without and with induction of the gene expression by a temperature shift from 30 °C to 42 °C. At the beginning of the induction of gene expression concentrated LB-medium was added to the shake flask. Without this supplement of M9 medium no gene expression occurred.List of Symbols LB Luria Bertani cultivation medium (Table 2) - M9 cultivation medium (Table 1) - P enzym activity [U ml^–1] - te]TCC total cell count [10⁶ cells ml^–1] - specific growth rate [h-1]     

Sulphur deprivation limits Fe-deficiency responses in tomato plants

The aim of this work was to clarify the role of S supply in the development of the response to Fe depletion in Strategy I plants. In S-sufficient plants, Fe-deficiency caused an increase in the Fe(III)-chelate reductase activity, ⁵⁹Fe uptake rate and ethylene production at root level. This response was associated with increased expression of LeFRO1 [Fe(III)-chelate reductase] and LeIRT1 (Fe²⁺ transporter) genes. Instead, when S-deficient plants were transferred to a Fe-free solution, no induction of Fe(III)-chelate reductase activity and ethylene production was observed. The same held true for LeFRO1 gene expression, while the increase in ⁵⁹Fe²⁺ uptake rate and LeIRT1 gene over-expression were limited. Sulphur deficiency caused a decrease in total sulphur and thiol content; a concomitant increase in ³⁵SO₄ ²⁻ uptake rate was observed, this behaviour being particularly evident in Fe-deficient plants. Sulphur deficiency also virtually abolished expression of the nicotianamine synthase gene (LeNAS), independently of the Fe growth conditions. Sulphur deficiency alone also caused a decrease in Fe content in tomato leaves and an increase in root ethylene production; however, these events were not associated with either increased Fe(III)-chelate reductase activity, higher rates of ⁵⁹Fe uptake or over-expression of either LeFRO1 or LeIRT1 genes. Results show that S deficiency could limit the capacity of tomato plants to cope with Fe-shortage by preventing the induction of the Fe(III)-chelate reductase and limiting the activity and expression of the Fe²⁺ transporter. Furthermore, the results support the idea that ethylene alone cannot trigger specific Fe-deficiency physiological responses in a Strategy I plant, such as tomato.     

Process development for an inducible rituximab-expressing Chinese hamster ovary cell line

Inducible mammalian expression systems are becoming increasingly available and are not only useful for the production of cytotoxic/cytostatic products, but also confer the unique ability to uncouple the growth and production phases. In this work, we have specifically investigated how the cell culture state at the time of induction influences the cumate-inducible expression of recombinant rituximab by a GS-CHO cell line. To this end, cells grown in batch and fed-batch cultures were induced at increasing cell densities (1 to 10 × 10 ⁶ cells/mL). In batch, the cell specific productivity and the product yield were found to reduce with increasing cell density at induction. A dynamic feeding strategy using a concentrated nutrient solution applied prior and postinduction allowed to significantly increase the integral of viable cells and led to a 3-fold increase in the volumetric productivity (1.2 g/L). The highest product yields were achieved for intermediate cell densities at induction, as cultures induced during the late exponential phase (10 × 10 ⁶ cells/mL) were associated with a shortened production phase. The final glycosylation patterns remained however similar, irrespective of the cell density at induction. The kinetics of growth and production in a 2 L bioreactor were largely comparable to shake flasks for a similar cell density at induction. The degree of galactosylation was found to decrease over time, but the final glycan distribution at harvest was consistent to that of the shake flasks cultures. Taken together, our results provide useful insights for the rational development of fed-batch cell culture processes involving inducible CHO cells. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2742, 2019     

HdaA, a class 2 histone deacetylase of Aspergillus fumigatus, affects germination and secondary metabolite production

Histone deacetylases (HDACs) play an important role in regulation of gene expression through histone modifications. Here we show that the Aspergillus fumigatus HDAC HdaA is involved in regulation of secondary metabolite production and is required for normal germination and vegetative growth. Deletion of the hdaA gene increased the production of several secondary metabolites but decreased production of gliotoxin whereas over-expression hdaA increased production of gliotoxin. RT-PCR analysis of 14 nonribosomal peptide synthases indicated HdaA regulation of up to nine of them. A mammalian cell toxicity assay indicated increased activity in the over-expression strain. Neither mutant affected virulence of the fungus as measured by macrophage engulfment of conidia or virulence in a neutropenic mouse model.     

Cytochrome c Oxydase Subunit I Gene is Up-regulated by Cadmium in Freshwater and Marine Bivalves

Inhibition of the mitochondrial electron transfer chain and induction of reactive oxygen species (ROS) production are one of the roots of cadmium (Cd) toxicity. To appreciate the impact of Cd on mitochondria, we focused on the expression of CoxI gene which encodes the subunit I of the Cytochrome c oxidase (complex IV of the respiratory chain). CoxI gene expression was studied by real-time quantitative PCR in three species: two freshwater bivalves (Corbicula fluminea and Dreissena polymorpha) and one marine bivalve (diploid or triploid Crassostrea gigas). Bivalves were exposed for 10 or 14 days to 0.13 μM Cd²⁺ and 15.3 μM Zn²⁺ in controlled laboratory conditions. We demonstrate that in the three mollusk species CoxI gene was up-regulated by Cd. Zinc (Zn), which is known to have antioxidant properties, had no effect on CoxI gene expression. In the presence of Cd and Zn, CoxI gene inducibility was lower than after a single Cd exposure, in each species; result that could not be fully explained by a decreased Cd accumulation. CoxI gene induction by Cd was 4.8-fold higher in triploid oysters than in diploid ones, indicating a possible influence of triploidy on animal responses to Cd contamination.     

Fermentation conditions for efficient production of thermophilic protease in Escherichia coli harboring a plasmid

Escherichia coli TG1, transformed with an expression plasmid pAQN carrying the aqualysin I (AQI) gene derived from Thermus aquaticus YT-1 under the control of the tac promoter, was cultivated under various conditions in order to find fermentation conditions for the efficient production of the thermophilic protease, AQI. The amount of AQI produced was closely related to the growth phase at the time of isopropyl--d-thiogalactopyranoside (IPTG) induction, and the highest production was obtained when it was added during the exponential growth phase. The addition of yeast extract had a greater effect on AQI production than did Polypeptone or casamino acids, and AQI productivity increased from 1.1 × 10³ kU/g to 2.7 × 10³ kU/g cells when 2 g/l yeast extract was supplied. Furthermore, the specific growth rate improved from 0.35 h^–1 to 0.89 h^–1 when 5 g/l yeast extract was supplied. The culture temperature also affected AQI gene expression. When the temperature was shifted from 37°C to 34°C at the time of IPTG induction, 19 kU/ml enzymatically active AQI was obtained, corresponding to a 28% increase over the amount produced in a batch culture without a shift. This is about a 44-fold higher yield than was obtained from the original strain, T. aquaticus YT-1.     

The effect of short-term low-temperature treatments on gene expression in Arabidopsis correlates with changes in intracellular Ca2+ levels

The role of changes in intracellular calcium ion concentration ([Ca²⁺]_i) in low‐temperature signal transduction in plants has lately been supported by several studies. An analysis to determine whether the low‐temperature‐induced increase in cytosolic Ca²⁺ concentration ([Ca²⁺]_cyt) could be correlated with a downstream response such as gene expression was carried out. The induction of the low‐temperature‐regulated gene LTI78 was used as an end point marker of the signal transduction pathway. It was found that this gene is induced by very brief low‐temperature exposures and that the induction does not depend on a continuous exposure to low temperature. By altering the cooling rate, different patterns of the Ca²⁺ response were obtained which could be correlated with different patterns of LTI78 induction. Furthermore, reducing the Ca²⁺ transients by pre‐treatment with the Ca²⁺ channel blocker La³⁺ also led to a reduced level of gene induction. The results show that brief exposures to low temperature results in the onset of a signalling pathway that leads to the induction of gene expression. This indicates the involvement of changes in [Ca²⁺]_cyt in low‐temperature signalling leading to LTI78 expression but the presence of multiple signalling pathways is suggested.     

Development of a high yielding E. coli periplasmic expression system for the production of humanized Fab' fragments

Humanized Fab′ fragments may be produced in the periplasm of Escherichia coli but can be subject to degradation by host cell proteases. In order to increase Fab′ yield and reduce proteolysis we developed periplasmic protease deficient strains of E. coli. These strains lacked the protease activity of Tsp, protease III and DegP. High cell density fermentations indicated Tsp deficient strains increased productivity two fold but this increase was accompanied by premature cell lysis soon after the induction of Fab′ expression. To overcome the reduction in cell viability we introduced suppressor mutations into the spr gene. The mutations partially restored the wild type phenotype of the cells. Furthermore, we coexpressed a range of periplasmic chaperone proteins with the Fab′, DsbC had the most significant impact, increasing humanized Fab′ production during high cell density fermentation. When DsbC coexpression was combined with a Tsp deficient spr strain we observed an increase in yield and essentially restored “wild type” cell viability. We achieved a final periplasmic yield of over 2.4g/L (final cell density OD₆₀₀ 105), 40 h post Fab′ induction with minimal cell lysis.The data suggests that proteolysis, periplasm integrity, protein folding and disulphide bond formation are all potential limiting steps in the production of Fab′ fragments in the periplasm of E. coli. In this body of work, we have addressed these limiting steps by utilizing stabilized protease deficient strains and chaperone coexpression. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 33:212–220, 2017     

Process optimization for large-scale production of TGF-α-PE40 in recombinant Escherichia coli: effect of medium composition and induction timing on protein expression

The effects of medium composition and induction timing on expression of a chimeric fusion protein TGF-α -PE40 (TP-40) in Escherichia coli strain RR1 were examined using a complex medium at several fermentor scales. Two distinctive phases in E. coli catabolism were identified during fermentation based on preferential utilization between protein hydrolysate and glycerol. Maximum specific and volumetric productivities were achieved by inducing the culture when the cells were switching substrate utilization from protein hydrolysate to glycerol. By increasing the yeast extract concentration in the production medium, initiation of the catabolic switch was delayed until high cell mass was achieved. The final titer of TP-40 at the 15-L fermentation scale was doubled from 400 mg L⁻¹ to 850 mg L⁻¹ by increasing the yeast extract concentration from 1% to 4% (w/v) and delaying the time of induction. This fermentation process was rapidly scaled up in 180-L and 800-L fermentors, achieving TP-40 titers of 740 and 950 mg L⁻¹, respectively. Received 26 August 1996/ Accepted in revised form 10 December 1996