Transcriptional regulatory proteins in central carbon metabolism of Pichia pastoris and Saccharomyces cerevisiae.

System-wide interactions in living cells and discovery of the diverse roles of transcriptional regulatory proteins that are mediator proteins with catalytic domains and regulatory subunits and transcription factors in the cellular pathways have become crucial for understanding the cellular response to environmental conditions. This review provides information for future metabolic engineering strategies through analyses on the highly interconnected regulatory networks in Saccharomyces cerevisiae and Pichia pastoris and identifying their components. We discuss the current knowledge on the carbon catabolite repression (CCR) mechanism, interconnecting regulatory system of the central metabolic pathways that regulate cell metabolism based on nutrient availability in the industrial yeasts. The regulatory proteins and their functions in the CCR signalling pathways in both yeasts are presented and discussed. We highlight the importance of metabolic signalling networks by signifying ways on how effective engineering strategies can be designed for generating novel regulatory circuits, furthermore to activate pathways that reconfigure the network architecture. We summarize the evidence that engineering of multilayer regulation is needed for directed evolution of the cellular network by putting the transcriptional control into a new perspective for the regulation of central carbon metabolism of the industrial yeasts; furthermore, we suggest research directions that may help to enhance production of recombinant products in the widely used, creatively engineered, but relatively less studied P. pastoris through de novo metabolic engineering strategies based on the discovery of components of signalling pathways in CCR metabolism. KEY POINTS: • Transcriptional regulation and control is the key phenomenon in the cellular processes. • Designing de novo metabolic engineering strategies depends on the discovery of signalling pathways in CCR metabolism. • Crosstalk between pathways occurs through essential parts of transcriptional machinery connected to specific catalytic domains. • In S. cerevisiae, a major part of CCR metabolism is controlled through Snf1 kinase, Glc7 phosphatase, and Srb10 kinase. • In P. pastoris, signalling pathways in CCR metabolism have not yet been clearly known yet. • Cellular regulations on the transcription of promoters are controlled with carbon sources.

Hybrid-architectured double-promoter expression systems enhance and upregulate-deregulated gene expressions in Pichia pastoris in methanol-free media.

Double-promoter expression system (DPES) design as de novo metabolic engineering strategy enables fine-tuned and enhanced gene expression. We constructed a collection of monodirectional hybrid-architectured DPESs with engineered promoter variants PADH2-Cat8-L2 and PmAOX1 and with the naturally occurring promoter PGAP to enhance and upregulate-deregulated gene expressions in Pichia pastoris in methanol-free media. Reporter red fluorescent protein (mApple) and enhanced green fluorescent protein (eGFP) were expressed under PADH2-Cat8-L2 and PmAOX1 or PGAP, respectively, enabling the determination of the transcription period and strength of each constituent in the DPESs. We determined fluorescent protein expressions in batch cultivations on 2% (v/v) ethanol, excess glucose, and excess glycerol, and compared them with single-promoter expression systems constructed with PADH2-Cat8-L2, PmAOX1, and PGAP. The transcription- and expression-upregulation power of bifunctional DPESs was higher than that of twin DPESs (two-copy expression systems). Our findings answer long-standing questions regarding the high- (or multi-) copy clone results in the literature. Our first conclusion is that increasing identical components in the DPES architectures linearly increases the concentrations of cis-acting DNA sites and increases the demand for key transcription factors (TFs) that perturb their good coupling of supply and demand. The next is that the synthesis of some amino acids may create bottleneck(s) as rate-limiting amino acid(s) in recombinant protein synthesis. With bifunctional DPESs, each constituent upregulated the transcription and increased the expression and reduced the demand for the same TF(s) in the generation of novel regulatory circuits, due to the increased number of nonidentical cis-acting DNA sites. We tested superior DPES performances in extracellular human growth hormone (rhGH) production. Thereby, the indications related to the rate-limiting amino acids were verified. Compared with its constituents PADH2-Cat8-L2 and PmAOX1, the bifunctional DPES4 enhanced rhGH production by 1.44- and 2.02-fold, respectively. The DPES design method, with its constraint and parameters, enables the generation of promising r-protein production platforms with high impact on industrial-scale production processes and opens up new avenues for research in yeasts. KEY POINTS: • Design method with the constraint and parameters for the construction of the DPESs is presented. • Hybrid-architectured de novo DPESs are designed to enhance and fine-tune gene expression. • Bifunctional DPESs demonstrate enhanced transcription and expression. • Twin DPESs linearly increase cis-acting DNA sites and consequently increase the demand for the same TFs. • Bifunctional DPESs enable good coupling of supply and demand to bind with TFs. • Ethanol-controlled Snf1 pathway and crosstalk enable fine-tuned transcription and enhanced expression.

Engineering of alcohol dehydrogenase 2 hybrid-promoter architectures in Pichia pastoris to enhance recombinant protein expression on ethanol.

The aim of this work is to increase recombinant protein expression in Pichia pastoris over the ethanol utilization pathway under novel-engineered promoter variants (NEPVs) of alcohol dehydrogenase 2 promoter (PADH2 ) through the generation of novel regulatory circuits. The NEPVs were designed by engineering of transcription factor binding sites (TFBSs) determined by in silico analyses and manual curation systematically, by (a) single-handedly replacement of specified TFBSs with synthetic motifs for Mxr1, Cat8, and Aca1 binding, and synthetic TATA-box integration; and, (b) nucleosome optimization. PADH2-Cat8-L2 and PADH2-Cat8-L1 designed by the integration of synthetic Cat8 binding sites were superior, and then PADH2-NucOpt . Compared to that with PADH2 at t = 20 hr of the fermentations, PADH2-Cat8-L2 allowed the highest increase in enhanced green fluorescent protein expression as 4.8-fold on ethanol and 3.8-fold on methanol; and, PADH2-NucOpt upregulated the expression 1.5-fold on ethanol and enhanced 3.2-fold on methanol. Using the superior two tools, Cat8-L2 and NucOpt, we designed PADH2-NucOpt-Cat8-L2 . With PADH2-NucOpt-Cat8-L2 , the expression in the fermentation of ethanol was upregulated 3.7-fold that is distinctly higher than that with PADH2-NucOpt but lower than that with PADH2-Cat8-L2 ; while on methanol compared to that with PADH2 , the expression was enhanced 8.8-fold. Extracellular recombinant human serum albumin production was also studied with PADH2-Cat8-L2 and PADH2-NucOpt , and average recombinant human serum albumin yield (YP/X ) on ethanol was 1.13 and 0.38 mg/gWCW, respectively; whereas with PADH2 , YP/X was 0.26 mg/gWCW . We conclude that as upregulation of transcription and enhanced expression correlate with the sequence of synthetic motifs and their location in the hybrid-promoter architectures of NEPVs in coordination with trans-acting factors, which are the design parameters in the engineering of binding sites; the NEPVs generated promising recombinant protein production platforms with a high impact on industrial scale production processes, as well as would open up new avenues for research in P. pastoris.

Transcriptional engineering of the glyceraldehyde-3-phosphate dehydrogenase promoter for improved heterologous protein production in Pichia pastoris.

The constitutive glyceraldehyde-3-phosphate dehydrogenase promoter (PGAP ), which is one of the benchmark promoters of Pichia pastoris, was analyzed in terms of putative transcription factor binding sites. We constructed a synthetic library with distinct regulatory properties through deletion and duplication of these putative transcription factor binding sites and selected transcription factor (TF) genes were overexpressed or deleted to understand their roles on heterologous protein production. Using enhanced green fluorescent protein, an expression strength in a range between 0.35- and 3.10-fold of the wild-type PGAP was obtained. Another model protein, recombinant human growth hormone was produced under control of selected promoter variants and 1.6- to 2.4-fold higher product titers were reached compared to wild-type PGAP . In addition, a GAL4-like TF was found to be a crucial factor for the regulation of PGAP , and its overexpression enhanced the heterologous protein production considerably (up to 2.2-fold compared to the parental strain). The synthetic PGAP library generated enabled us to investigate the different putative transcription factors which are responsible for the regulation of PGAP under different growth conditions, ergo recombinant protein production under PGAP . Biotechnol. Bioeng. 2017;114: 2319-2327. © 2017 Wiley Periodicals, Inc.

Double promoter expression systems for recombinant protein production by industrial microorganisms.

Using double promoter expression systems is a promising approach to increase heterologous protein production. In this review, current double promoter expression systems for the production of recombinant proteins (r-proteins) by industrially important bacteria, Bacillus subtilis and Escherichia coli; and yeasts, Saccharomyces cerevisiae and Pichia pastoris, are discussed by assessing their potentials and drawbacks. Double promoter expression systems need to be designed to maintain a higher specific product formation rate within the production domain. While bacterial double promoter systems have been constructed as chimeric tandem promoters, yeast dual promoter systems have been developed as separate expression cassettes. To increase production and productivity, the optimal transcriptional activity should be justified either by simultaneously satisfying the requirements of both promoters, or by consecutively stimulating the changeover from one to another in a biphasic process or via successive-iterations. Thus, considering the dynamics of a fermentation process, double promoters can be classified according to their operational mechanisms, as: i) consecutively operating double promoter systems, and ii) simultaneously operating double promoter systems. Among these metabolic design strategies, extending the expression period with two promoters activated under different conditions, or enhancing the transcriptional activity with two promoters activated under similar conditions within the production domain, can be applied independently from the host. Novel studies with new insights, which aim a rational systematic design and construction of dual promoter expression vectors with tailored transcriptional activity, will empower r-protein production with enhanced production and productivity. Finally, the current state-of-the-art review emphasizes the advantages of double promoter systems along with the necessity for discovering new promoters for the development of more effective and adaptive processes to meet the increasing demand of r-protein industry.

Beet molasses-based feeding strategy enhances recombinant thermostable glucose isomerase production by Escherichia coli BL21 (DE3).

The aim of this work was to develop an effective fed-batch feeding strategy to enhance recombinant glucose isomerase (r-GI) production by recombinant Escherichia coli BL21 (DE3) pLysS on an industrially relevant feedstock without the application of an exogenous inducer. Following the batch operation (0 < t < 7 H), the effects of pulse and/or continuous feeding of hydrolyzed beet molasses were investigated under five different feeding strategies. The two most promising strategies with respect to r-GI activity were (i) PM-0.05, designed with one pulse feed (t = 7 H) followed by a continuous feed and (ii) 2PMF -0.05, designed with two consecutive pulse feeds (t = 7 and 10 H) followed by a continuous feed. The continuous feeding of molasses for both fermentation strategies employed the same precalculated feeding rate, µo = 0.05 H-1 . The maximum r-GI activities exhibited by PM-0.05 and 2PMF -0.05 were 29,050 and 30,642 U dm-3 , respectively. On the one hand, compared to PM-0.05 r-GI activity reached its maximum within a shorter cultivation time (∆tmax = 2 H) at 2PMF -0.05, which could be preferable in terms of manufacturing costs and possible risks; on the other hand, PM-0.05 is a simpler fermentation regime compared to 2PMF -0.05 with respect to manipulations that should be considered in large-scale production.

Endogenous signal peptides in recombinant protein production by Pichia pastoris: From in-silico analysis to fermentation.

For extracellular recombinant protein production, the efficiency of five endogenous secretion signal peptides (SPs) of Pichia pastoris, SP13 (MLSTILNIFILLLFIQASLQ), SP23 (MKILSALLLLFTLAFA), SP24 (MKVSTTKFLAVFLLVRLVCA), SP26 (MWSLFISGLLIFYPLVLG), SP34 (MRPVLSLLLLLASSVLA), selected based on their D-score which quantifies the signal peptide-ness of a given sequence segment, was investigated using recombinant human growth hormone (rhGH) as the model protein. The expression was conducted under glyceraldehyde-3-phosphate dehydrogenase promoter (PGAP). The highest secretion efficiency among endogenous SPs was obtained by SP23 followed by SP24, SP34, SP13 and SP26, respectively. The fermentation characteristics of rhGH production by the use of SP23, the most favorable endogenous SP of P.pastoris, and Saccharomyces cerevisiae α-mating factor prepro sequence (α-MF) were compared. With respect to the SP23 which is 73 amino acids shorter in length compared to α-MF, in high cell density cultures, where carbon and energy source are limited, the substitution of SP23 for α-MF seems promising. α-MF higher secretion efficiency was verified by major physicochemical properties including hydropathy index, isoelectric point, and aliphatic index. Regarding the examined endogenous SPs, there was no clear correlation between secretion efficiency and major physicochemical properties when each of these properties was considered independently. To find a correlation, factors such as protein N-terminus effect, length of the SP, secondary structure of the SP, and interactions of the selected properties should also be investigated.

Oxygen transfer as a tool for fine-tuning recombinant protein production by Pichia pastoris under glyceraldehyde-3-phosphate dehydrogenase promoter.

Effects of oxygen transfer on recombinant protein production by Pichia pastoris under glyceraldehyde-3-phosphate dehydrogenase promoter were investigated. Recombinant glucose isomerase was chosen as the model protein. Two groups of oxygen transfer strategies were applied, one of which was based on constant oxygen transfer rate where aeration rate was Q O/V = 3 and 10 vvm, and agitation rate was N = 900 min(-1); while the other one was based on constant dissolved oxygen concentrations, C DO = 5, 10, 15, 20 and 40 % in the fermentation broth, by using predetermined exponential glucose feeding with µ o = 0.15 h(-1). The highest cell concentration was obtained as 44 g L(-1) at t = 9 h of the glucose fed-batch phase at C DO = 20 % operation while the highest volumetric and specific enzyme activities were obtained as 4440 U L(-1) and 126 U g(-1) cell, respectively at C DO = 15 % operation. Investigation of specific enzyme activities revealed that keeping C DO at 15 % was more advantageous with an expense of relatively higher by-product formation and lower specific cell growth rate. For this strategy, the highest oxygen transfer coefficient and oxygen uptake rate were K L a = 0.045 s(-1) and OUR = 8.91 mmol m(-3) s(-1), respectively.

Lignocellulose degrading extremozymes produced by Pichia pastoris: current status and future prospects.

In this review article, extremophilic lignocellulosic enzymes with special interest on xylanases, ß-mannanases, laccases and finally cellulases, namely, endoglucanases, exoglucanases and ß-glucosidases produced by Pichia pastoris are reviewed for the first time. Recombinant lignocellulosic extremozymes are discussed from the perspectives of their potential application areas; characteristics of recombinant and native enzymes; the effects of P. pastoris expression system on recombinant extremozymes; and their expression levels and applied strategies to increase the enzyme expression yield. Further, effects of enzyme domains on activity and stability, protein engineering via molecular dynamics simulation and computational prediction, and site-directed mutagenesis and amino acid modifications done are also focused. Superior enzyme characteristics and improved stability due to the proper post-translational modifications and better protein folding performed by P. pastoris make this host favourable for extremozyme production. Especially, glycosylation contributes to the structure, function and stability of enzymes, as generally glycosylated enzymes produced by P. pastoris exhibit better thermostability than non-glycosylated enzymes. However, there has been limited study on enzyme engineering to improve catalytic efficiency and stability of lignocellulosic enzymes. Thus, in the future, studies should focus on protein engineering to improve stability and catalytic efficiency via computational modelling, mutations, domain replacements and fusion enzyme technology. Also metagenomic data need to be used more extensively to produce novel enzymes with extreme characteristics and stability.

In-silico determination of Pichia pastoris signal peptides for extracellular recombinant protein production.

In-silico identified novel secretory signal peptides (SPs) are required in vivo to achieve efficient transfer or to prevent other cellular proteins from interfering with the process in extracellular recombinant protein (r-protein) production. 56 endogenous and exogenous secretory SPs, have been used or having the potential to be used in Pichia pastoris for r-protein secretion, were analyzed in-silico using the softwares namely SignalP4.1, Phobius, WolfPsort0.2, ProP1.0, and NetNGlyc1.0. Among the predicted 41 endogenous secretory SPs, five of them have been used in P. pastoris, and regarded as positive controls; whereas, 36 of them have not been used. Amongst, the predicted cleavage site for each of the 32 endogenous secretory SPs was found to be same by the three programs. The secretory SPs having the highest D-scores, the score quantifying the signal peptide-ness of a given sequence segment, were: MKILSALLLLFTLAFA (D=0.932), MRPVLSLLLLLASSVLA (D=0.932), MFKSLCMLIGSCLLSSVLA (D=0.918). As D-scores of these SPs are higher than that of Saccharomyces cerevisiae α-mating factor signal peptide which has been widely used for r-protein production, they can be considered as the promising candidates. Among the predicted 15 exogenous SPs, 11 have been used in P. pastoris: therefore, they were evaluated as positive controls. The three programs predicted a unique cleavage site for each of the 10 exogenous SPs; and D-scores of these SPs were within D=0.805-0.900; whereas, four exogenous secretory SPs, which have not been used in P. pastoris, have D-scores within D=0.494-0.702.

Codon optimization of xylA gene for recombinant glucose isomerase production in Pichia pastoris and fed-batch feeding strategies to fine-tune bioreactor performance.

The objectives of this work are the optimization of the codons of xylA gene from Thermus thermophilus to enhance the production of recombinant glucose isomerase (rGI) in P. pastoris and to investigate the effects of feeding strategies on rGI production. Codons of xylA gene from T. thermophilus were optimized, ca. 30 % of the codons were replaced with those with higher frequencies according to the codon usage bias of P. pastoris, codon optimization resulted in a 2.4-fold higher rGI activity. To fine-tune bioreactor performance, fed-batch bioreactor feeding strategies were designed as continuous exponential methanol feeding with pre-calculated feeding rate based on the pre-determined specific growth rate, and fed-batch methanol-stat feeding. Six feeding strategies were designed, as follows: (S1) continuous exponential methanol- and pulse- sorbitol feeding; (S2) continuous exponential methanol- and peptone- feeding; (S3) continuous exponential methanol- and pulse- mannitol feeding; (S4) continuous exponential methanol- and peptone- feeding and pulse-mannitol feeding; (S5) methanol-stat feeding by keeping methanol concentration at 5 g L(-1); and, (S6) methanol-stat feeding by keeping methanol concentration at 5 g L(-1) and pulse-mannitol feeding. The highest cell and rGI activity was attained as 117 g L(-1) at t = 66 h and 32530 U L(-1) at t = 53 h, in strategy-S5. The use of the co-substrate mannitol does not increase the rGI activity in methanol-stat feeding, where 4.1-fold lower rGI activity was obtained in strategy-S6. The overall cell yield on total substrate was determined at t = 53 h as 0.21 g g(-1) in S5 strategy.

Feeding strategy design for recombinant human growth hormone production by Bacillus subtilis.

Defined and semi-defined medium-based feeding strategies were developed to enhance recombinant human growth hormone (rhGH) production by Bacillus subtilis BGSC-1A178 (scoC (-)) strain carrying pMK4::pre(subC)::hGH. Defined medium-based feeding strategies were designed by exponential feeding of glucose and (NH4)2HPO4 at two pre-determined specific growth rates, µ 0 = 0.10 and 0.17 h(-1). Semi-defined medium-based feeding strategies were designed by exponential feeding of substrate solution consisting of glucose, (NH4)2HPO4, peptone, and trace salt solution (PTM1) at three pre-determined specific growth rates, µ 0 = 0.10, 0.17, and 0.25 h(-1). At all the strategies applied, transition cultivation time from batch to fed-batch operation was t T = 4 h. The highest rhGH concentration was obtained as C rhGH = 0.5 g L(-1) with semi-defined medium-based feeding strategy designed with µ 0 = 0.25 h(-1) using feed substrate stock solution containing 200 g L(-1) glucose, 117 g L(-1) (NH4)2HPO4, 100 g L(-1) peptone, and 5 mL L(-1) PTM1 at t = 22 h when the cell concentration reached to C X = 8.29 g L(-1). The overall product and cell yields on glucose were obtained as [Formula: see text] = 7.21 mg g(-1) and [Formula: see text] = 0.12 g g(-1), respectively. The results indicate the requirement of designing continuous feed stream in fed-batch production to enhance rhGH production by r-B. subtilis.

A rapid method for detection of genetically modified organisms based on magnetic separation and surface-enhanced Raman scattering.

In this study, a new method combining magnetic separation (MS) and surface-enhanced Raman scattering (SERS) was developed to detect genetically modified organisms (GMOs). An oligonucleotide probe which is specific for 35 S DNA target was immobilized onto gold coated magnetic nanospheres to form oligonucleotide-coated nanoparticles. A self assembled monolayer was formed on gold nanorods using 5,5'-dithiobis (2-nitrobenzoic acid) (DTNB) and the second probe of the 35 S DNA target was immobilized on the activated nanorod surfaces. Probes on the nanoparticles were hybridized with the target oligonucleotide. Optimization parameters for hybridization were investigated by high performance liquid chromatography. Optimum hybridization parameters were determined as: 4 µM probe concentration, 20 min immobilization time, 30 min hybridization time, 55 °C hybridization temperature, 750 mM buffer salt concentration and pH: 7.4. Quantification of the target concentration was performed via SERS spectra of DTNB on the nanorods. The correlation between the target concentration and the SERS signal was found to be linear within the range of 25-100 nM. The analyses were performed with only one hybridization step in 40 min. Real sample analysis was conducted using Bt-176 maize sample. The results showed that the developed MS-SERS assay is capable of detecting GMOs in a rapid and selective manner.

Hybrid-architectured promoter design to deregulate expression in yeast.

Hybrid-architectured promoter design to deregulate expression in yeast under modulating power of carbon sources involves replacing native cis-acting DNA sequence(s) with de novo synthetic tools in coordination with master regulator transcription factor (TF) to alter crosstalk between signaling pathways, and consequently, transcriptionally rewire the expression. Hybrid-promoter architectures can be designed to mimic native promoter architectures in yeast's preferred carbon source utilization pathway. The method aims to generate engineered promoter variants (EPVs) that combine the advantages of being an exceptionally stronger EPV(s) than the naturally occurring promoters and permit "green-and-clean" production on a non-toxic carbon source. To implement the method, a predetermined essential part of the general transcription machinery is targeted. This targeting involves cis-acting DNA sequences to be replaced with synthetic cis-acting DNA sites in coordination with the targeted TF that must bind for transcription machinery activation. The method needs genomic and functional information that can lead to the discovery of the master TF(s) and synthetic cis-acting DNA elements, which enable the engineering of binding of master regulator TF(s). By introducing our recent work on the engineering of Pichia pastoris (syn. Komagataella phaffii) alcohol oxidase 1 (AOX1) hybrid-promoter architectures, we provide the method and protocol for the hybrid-architectured EPV design to deregulate expression in yeast. The method can be adapted to other promoters in different substrate utilization pathways in P. pastoris, as well as in other yeasts.

Hybrid-architectured promoter design to engineer expression in yeast.

Engineered promoters are key components that allow engineered expression of genes in the cell-factory design. Promoters having exceptional strength are attractive candidates for designing metabolic engineering strategies for tailoring de novo production strategies that require directed evolution methods by engineering with de novo synthetic biology tools. Engineered promoter variants (EPVs) of naturally occurring promoters (NOPs) can be designed using metabolic engineering strategies and synthetic biology tools if the genes encoding the activating transcription factors (TFs) exist in the genome and are expressed and synthesized at non-limiting concentrations within the cell. The hybrid-architectured EPV design method targets an essential and predetermined part of the general transcription machinery. That is cis-acting DNA site(s) in coordination with the trans-acting factor(s) that must bind for the regulated transcription machinery activation. The method needs genomic and functional information that can lead to the discovery of the master TF(s) and synthetic cis-acting DNA elements, enabling the engineering of binding of master regulator TF(s). The method aims to generate EPVs that combine the advantages of being an exceptional stronger EPV(s) than the NOPs and permit "green-and-clean production" on a non-toxic carbon source, such as ethanol or glucose. By introducing our recent work on the engineering of ADH2 hybrid-promoter architectures to enhance recombinant protein expression on ethanol, we provide the method and protocol for the design of ADH2 hybrid-promoter architectures that can be adapted to other promoters in different substrate utilization pathways in Pichia pastoris (syn. Komagataella phaffii), as well as in other yeasts.

Metabolic flux analysis for recombinant protein production by Pichia pastoris using dual carbon sources: Effects of methanol feeding rate.

The intracellular metabolic fluxes through the central carbon pathways in the bioprocess for recombinant human erythropoietin (rHuEPO) production by Pichia pastoris (Mut(+)) were calculated to investigate the metabolic effects of dual carbon sources (methanol/sorbitol) and the methanol feed rate, and to obtain a deeper understanding of the regulatory circuitry of P. pastoris, using the established stoichiometry-based model containing 102 metabolites and 141 reaction fluxes. Four fed-batch operations with (MS-) and without (M-) sorbitol were performed at three different constant specific growth rates (h(-1)), and denoted as M-0.03, MS-0.02, MS-0.03, and MS-0.04. Considering the methanol consumption pathway, the M-0.03 and MS-0.02 conditions produced similar effects and had >85% of formaldehyde flux towards the assimilatory pathway. In contrast, the use of the dual carbon source condition generated a shift in metabolism towards the dissimilatory pathway that corresponded to the shift in dilution rate from MS-0.03 to MS-0.04, indicating that the methanol feed exceeded the metabolic requirements at the higher micro(0). Comparing M-0.03 and MS-0.03 conditions, which had the same methanol feeding rates, sorbitol addition increased the rHuEPO synthetic flux 4.4-fold. The glycolysis, gluconeogenesis, and PPP pathways worked uninterruptedly only at MS-0.02 condition. PPP and TCA cycles worked with the highest disturbances at MS-0.04 condition, which shows the stress of increased feeding rates of methanol on cell metabolism.

Human growth hormone-specific aptamer identification using improved oligonucleotide ligand evolution method.

LETEG is a method developed and used for the separation and purification of proteins employing a single-step ligand (aptamers) evolution in which aptamers are eluted with an increasing temperature gradient. Using recombinant human growth hormone (rhGH) as the test purification target, and after avoiding cross reactions of aptamers with Bacillus subtilis extracellular proteins by negative SELEX, the effects of time and pH on aptamer binding to rhGH were investigated. The highest binding efficiency of aptamers on rhGH-immobilized microparticles was obtained at pH 7.0. The aptamers that interacted with rhGH were eluted by a multi-stage step-up temperature gradient in DeltaT=10 degrees C increments within the range T=55-95 degrees C; and the strongest affinity binding was disrupted at T=85 degrees C where C(Apt)=0.16muM was eluted. The equilibrium binding data obtained was described by a Langmuir-type isotherm; where the affinity constant was K(D)=218nM rhGH. RhGH was separated from the fermentation broth with 99.8% purity, indicating that the method developed is properly applicable even for an anionic protein.

Engineered Deregulation of Expression in Yeast with Designed Hybrid-Promoter Architectures in Coordination with Discovered Master Regulator Transcription Factor.

Engineered promoters are key components in the cell-factory design, allowing precise and enhanced expression of genes. Promoters having exceptional strength are attractive candidates for designing metabolic engineering strategies for tailoring de novo production strategies that require directed evolution methods by engineering with de novo synthetic biology tools. Here, the custom-designed AOX1 hybrid-promoter architectures in coordination with targeted transcription factors are shown, transcriptionally rewired the expression over methanol-free substrate-utilization pathway(s) and converted methanol-dependent Pichia pastoris alcohol oxidase 1(AOX1) promoter (PAOX1 ) expression into a non-toxic carbon-source-regulated system. AOX1 promoter variants are engineered by replacing specified cis-regulatory DNA elements with synthetic Adr1, Cat8, and Aca2 cis-acting DNA elements for Mxr1, Cat8, and Aca1 binding, respectively. Applications of the engineered-promoters are validated for eGFP expression and extracellular human serum albumin production. The hybrid-promoter architecture designed with single Cat8 cis-acting DNA element deregulates the expression on ethanol. Compared with PAOX1 on methanol, the expression on ethanol is increased with i) PAOX1/Cat8-L3 (designed with single Cat8 cis-acting element) to 74%, ii) PAOX1/Adr1-L3/Cat8-L3 (designed with single- Cat8 and Adr1 cis-acting elements) to 85%, and for further consolidation of deregulated expression iii) PeAOX1 (designed with triplet- Cat8 and Adr1 cis-acting elements) 1.30-fold, at t = 20 h of batch cultivations.

Fed-batch methanol feeding strategy for recombinant protein production by Pichia pastoris in the presence of co-substrate sorbitol.

Batch-wise sorbitol addition as a co-substrate at the induction phase of methanol fed-batch fermentation by Pichia pastoris (Mut(+)) was proposed as a beneficial recombinant protein production strategy and the metabolic responses to methanol feeding rate in the presence of sorbitol was systematically investigated. Adding sorbitol batch-wise to the medium provided the following advantages over growth on methanol alone: (a) eliminating the long lag-phase for the cells and reaching 'high cell density production' at t = 24 h of the process (C(X) = 70 g CDW/l); (b) achieving 1.8-fold higher recombinant human erythropoietin (rHuEPO) (at t = 18 h); (c) reducing specific protease production 1.2-fold; (d) eliminating the lactic acid build-up period; (e) lowering the oxygen uptake rate two-fold; and (f) obtaining 1.4-fold higher overall yield coefficients. The maximum specific alcohol oxidase activity was not affected in the presence of sorbitol, and it was observed that sorbitol and methanol were utilized simultaneously. Thus, in the presence of sorbitol, 130 mg/l rHuEPO was produced at t = 24 h, compared to 80 mg/l rHuEPO (t = 24 h) on methanol alone. This work demonstrates not only the ease and efficiency of incorporating sorbitol to fermentations by Mut(+) strains of P. pastoris for the production of any bio-product, but also provides new insights into the metabolism of the methylotrophic yeast P. pastoris.

Effects of pulse feeding of beet molasses on recombinant benzaldehyde lyase production by Escherichia coli BL21(DE3).

The effect of fed-batch operation (FBO) strategy was investigated using pretreated-beet molasses, containing galactose that induces the lac promoter, on benzaldehyde lyase (BAL) production by recombinant Escherichia coli BL21(DE3)pLySs. After batch cultivation with 30 g l(-1) pretreated-beet molasses consisting of 7.5 g l(-1) glucose and 7.5 g l(-1) fructose, three FBO strategies were applied at dissolved oxygen (=40%) cascade to air-flow rate. In FBO1 when air-flow rate decreased considerably, feed was given to the system in pulses in such a way that pretreated-beet molasses concentration increased by 10 kg m(-3) (containing 2.5 g l(-1) glucose+2.5 g l(-1) fructose); however, decrease in air-flow rate demonstrated only the absence of glucose but not fructose. Thus, in FBO2 when fructose and glucose were completely utilized, pretreated-beet molasses was pulse-fed and its concentration increased by 10 g l(-1). In FBO3 with the decreased amount of pretreated-beet molasses (6 g l(-1)), shift response time from glucose to fructose consumption was avoided, and glucose and fructose consumptions were well correlated with air-flow rate, and the highest CX (8.04 g l(-1)) and BAL (2,315 U ml(-1)) production were obtained (t=24 h) with the highest substrate yield on cell and product formation.