Shrimp (Litopenaeus vannamei) trypsinogen production in Pichia pastoris bioreactor cultures

Recently, we engineered a Pichia pastoris Mut⁺ strain to produce and secrete recombinant Litopenaeus vannamei trypsinogen. Despite the observed toxicity of the recombinant shrimp trypsinogen to the P. pastoris cell host, when high density cell cultures in shake flasks with alanine in the induction medium were used recombinant shrimp trypsinogen could be produced. To further improve the product yield, in this work, we evaluated L. vannamei trypsinogen production in P. pastoris using a bioreactor and two recombinant P. pastoris strains with different methanol utilization (Mut) phenotypes. The effect of pH and temperature during the induction step on the trypsinogen production was also evaluated. The results indicate that temperature, pH, and Mut phenotypes influence the production of the recombinant protein, with almost no observed effect on cell growth. All cultures with the Mut⁺ strain had significant operational difficulties, such as in lowering the induction temperature, maintaining dissolved oxygen (DO) above 20%, and maintaining the methanol concentration at a constant value, and showed a decrease in metabolic activity due to trypsinogen toxicity to the cell host. In the culture with the Mut^s strain, however, the temperature, methanol concentration, and DO could be more easily controlled, the temperature could be easily decreased, and the trypsinogen caused the lowest toxicity to the host cells. After 96 h of Mut^s strain induction (pH 6 and 25°C), about 250 mg/L recombinant trypsinogen was detected in the culture medium. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2013     

Expression of HBsAg and preS2-S protein in different yeast based system: A comparative analysis

We have expressed both S and preS2-S genes coding for the hepatitis B small (S) and medium (M) proteins, respectively, in different yeast based expression systems and compared the production level of the recombinant proteins. In Saccharomyces cerevisiae, viral genes were expressed under the inducible Gal10/cyc1 and the constitutive PGK promoters using 2 μ replicating vectors. We showed that the yield of S protein was higher than M protein under both inducible (14.27 vs 10.9 mg/l) and constitutive (9.18 vs 6.39 mg/l) conditions, respectively. In the methylotrophic yeast Pichia pastoris, the viral genes were expressed in GS115 (Mut⁺: Methanol Utilizing) and KM71 (Mut^S: Methanol Utilizing Slow) under the control of the alcohol oxidase promoter (AOX1). In Mut^S background, both S and preS2-S genes were expressed at higher levels than in Mut⁺. In attempt to increase the yield of recombinant viral proteins in S. cerevisiae, we have co-expressed both inducible and constitutive vectors harboring the S or preS2-S genes leading to recombinant strains called UTS (containing pDP/S + pYePIT/S) and UTP (containing pDP/preS2-S + pYePIT/preS2-S). We showed that the recombinant S and preS2-S proteins were successfully detected and the production level reached 18.31 mg/l for the S and 13.22 mg/l for the M proteins.Our comparative study provides evidence that in small scale, S. cerevisiae is more suitable for HBsAg and preS2-S proteins production than P. pastoris under inducible rather than constitutive condition.     

High-level secretion and purification of recombinant acetylcholinesterase from human cerebral tissue in P. pastoris and identification by chromogenic reaction

The gene encoding human cerebral tissue acetylcholinesterase (AChE) was cloned from an 18-week fetal cerebral tissue and expressed in Pichia pastoris. Twenty-two positive transformants were obtained by Mut⁺/Mut^s phenotypes screening in MD/MM medium and polymerase chain reaction amplification, and four recombinant P. pastoris strains that could secrete active AChE at high level were identified by simple and specific development reaction with indoxyl acetate as the chromogenic substrate. In shake-flask culture induced with methanol, the recombinant human AChE (rhAChE) content was about 76% of the total secreted proteins, and rhAChE activity in supernatant was 40 U/ml. The enzyme was purified through anion-exchange and affinity chromatography. Purity of the rhAChE was up to 96% after the simple purification procedure. The enzymatic activity reached 200 U/mg.     

乙型肝炎病毒adr亚型NC-1毒株表面抗原基因的顺序测定与结构研究

用内引物法自pHBVNC-1质粒DNA经Sau3A1降解的1.3Kb片段中,快速、连续测定了HBV adr NC-1表面抗原基因全顺序,与其它三株adr亚型S基因比较,顺序同源性为99％,与adw及ayw亚型比较,同源性为94％。不同亚型间的错义突变比同一亚型不同毒株间的错义突变多。比较11株adr亚型、2抹adw亚型与2株ayw亚型的S基因全顺序,发现在第47,110,113,126,160位的密码子在r亚型中有同源性,在w亚型中也有同源性,所以是w/r亚型决定簇的候选部位。第46,68,134,159,168位的密码子在d亚型中有同源性,而在y亚型中也有同源性,所以是d/y亚型抗原决定簇的候选部位。     

Transcriptional analysis for carbon metabolism and kinetic modeling for heterologous proteins productions by Pichia pastoris in induction process with methanol/sorbitol co-feeding

It is difficult to control concentrations of methanol/dissolved oxygen at high levels simultaneously in heterologous proteins productions by Pichia pastoris during induction phase. Two strains, a methanol utilization slow (Mut^S) type and a plus (Mut⁺) type were used with methanol/sorbitol co-feeding strategy to induce porcine interferon-α and human serum albumin-human granulocyte colony stimulating factor respectively, under the conditions of “methanol sufficient-oxygen limited (MS-OL)” and “methanol limited-oxygen sufficient (ML-OS)”. For the Mut^S/Mut⁺ strains, the target proteins titers under “MS-OL” were 6-fold/19.2% of those under “ML-OS”. The key genes in methanol metabolism of the Mut^S strain were up-regulated under “MS-OL”, but they were not differently expressed in the Mut⁺ strain. Methanol utilization rate (r_MeOH) of the Mut^S strain reduced when decreasing methanol concentration, but r_MeOH of the Mut⁺ strain unchanged unless methanol concentration decreased to a low-limit of 0.6 g/L. Finally, kinetic models were designed to describe the methanol/sorbitol co-feeding process.     

Geographic distribution of HBsAg subtypes in Brazil

HBsAg positive serum samples (896) from five brazilian regions were analysed for HBsAg subtypes. The presence of five different subtypes (ayw2, ayw3, ayw4, adw2 and adw4) was detected. In Northern region subtypes adw4 (41.2%) and adw2 (37.2%) were predominant. In the North East only subtype adw2 was encountered. In Central West, South-East and South, subtypes ayw2, ayw3, adw2 and adw4 were present, with predominance of adw2 in Central West and South East (84.3% and 69.4% respectively) whereas in the South the predominant subtype was ayw3 (41.9%) followed by ayw2 (36.4%). Subtypes ayw1, ayr and adr were not found among the samples studied. These results show the difference in the incidence of HBsAg subtypes in the different regions of Brazil and their significance in relation to the colonization and migrations in this country.     

Two-phase fed-batch modification for 48 hour peak expression of hepatitis B surface antigen in Pichia pastoris shake flask system

A study of the Mut⁺ phenotype for the expression of recombinant hepatitis B surface antigen (HBsAg) in Pichia pastoris strain GS115 using the pPIC3.5K vector with a two-phase fed-batch protocol in a shake flask system is described. Expression levels of HBsAg protein of 6.74 g L^?1 Dry Cell Weight (DCW) and 26.07 mg L^?1 of HBsAg concentration were achieved 48 h from the induction point which added to a 120 h reduction in production period in comparison with Mut^S expression (168 h). The use of the pPIC3.5K-HBsAg plasmid in the Mut⁺ phenotype enhanced the expression of HBsAg by a nearly 13 times higher volumetric productivity in the first 24 h and 35 times higher at peak production concentration. Comparison of AOX expression cassettes relative to the HBsAg gene in the role of mRNA secondary structure during translation initiation revealed that HBsAg possesses lower folding stability with AOX1 Mut⁺ phenotype. The results from this study demonstrated that expression of HBsAg with Mut⁺ AOX1 promoter is adequate as an alternative for the production of HBsAg. In addition, the AOX promoter of the Mut⁺ phenotype was observed to be better suited for HBsAg expression, which correlates with the ease of translation initiation under shake flask conditions.     

Efficient 13C/15N double labeling of the avirulence protein AVR4 in a methanol-utilizing strain (Mut+) of Pichia pastoris

Cost effective ¹³C/¹⁵N-isotope labeling of the avirulence protein AVR4 (10 kDa) of the fungal tomato pathogen Cladosporium fulvum was achieved with the methylotrophic yeast Pichia pastoris in a fermentor. The ¹³C/¹⁵N-labeled AVR4 protein accumulated to 30 mg/L within 48 h in an initial fermentation volume of only 300 mL, while prolonged optimized overexpressions yielded 126 mg/L. These protein yields were 24-fold higher in a fermentor than in flask cultures. In order to achieve these protein expression levels, we used the methanol-utilizing strain (Mut⁺) of Pichia pastoris which has a high growth rate while growing on methanol as the only carbon source. In contrast, the methanol-sensitive strain (Mut^S) could intrinsically yield comparable protein expression levels, but at the expense of additional carbon sources. Although both strains are generally used for heterologous protein expression, we show that the costs for ¹³C-isotope labeling can be substantially reduced using the Mut⁺ strain compared to the Mut^S strain, as no ¹³C₃-glycerol is required during the methanol-induction phase. Finally, nitrogen limitations were precluded for ¹⁵N-labeling by an optimal supply of 10 g/L (¹⁵NH₄)₂SO₄ every 24 h.     

High expression of Trigonopsis variabilis -amino acid oxidase in Pichia pastoris

To explore a new approach of high expression of -amino acid oxidase (DAAO) in Pichia pastoris, a gene encoding DAAO from Trigonopsis variabilis (TvDAAO gene) deleted intron was prepared by PCR amplification and cloned into the intracellular expression vector pPIC3.5K. The expression plasmid pPIC3.5K-DAAO linearized by SalI was transformed into Pichia pastoris strain GS115 (his⁻mut⁺). By means of MM and MD plates and PCR, the recombinant P. pastoris strains (his⁺mut⁺) were obtained. Activity assay and SDS-PAGE demonstrated that DAAO was intracellularly expressed in P. pastoris with the induction of methanol. The recombinant strain PD27 with the highest expression of DAAO was screened through activity assay and its high-density fermentation was carried out in a 1-l fermentor. Activity assay and SDS-PAGE demonstrated that DAAO was intracellularly expressed in P. pastoris with the induction of methanol. The recombinant cells with high expression of DAAO were screened and the high-density fermentation was carried out in a 1-l fermentor. Interestingly, the DAAO expression level reached up to 473 U/g dry cell weight in fermentation yield. Finally, 1-hexanol was used to break recombinant cells and the specific activity of DAAO was 1.46 U/mg protein in crude extraction.     

Dextranase production by recombinant Pichia pastoris under operational volumetric mass transfer coefficient (kLa) and volumetric gassed power input (Pg/V) attainable at commercial large scale

Abstract

Most of the reported bioprocesses carried out by the methylotrophic yeast Pichia pastoris have been performed at laboratory scale using high power inputs and pure oxygen, such conditions are not feasible for industrial large-scale processes. In this study, volumetric mass transfer (k_La) and volumetric gassed power input (Pg/V) were evaluated within values attainable in large-scale production as scale-up criteria for recombinant dextranase production by Mut^S P. pastoris strain. Cultures were oxygen limited when the volumetric gassed power supply was limited to 2?kW m^?3. Specific growth rate, and then dextranase production, increased as k_La and Pg/V did. Meanwhile, specific production and methanol consumption rates were constant, due to the limited methanol condition also achieved at 2?L bioprocesses. The specific dextranase production rate was two times higher than the values previously reported for a Mut⁺ strain. After a scale-up process, at constant k_La, the specific growth rate was kept at 30?L bioprocess, whereas dextranase production decreased, due to the effect of methanol accumulation. Results obtained at 30?L bioprocesses suggest that even under oxygen-limited conditions, methanol saturated conditions are not adequate to express dextranase with the promoter alcohol oxidase. Bioprocesses developed within feasible and scalable operational conditions are of high interest for the commercial production of recombinant proteins from Pichia pastoris.     

Control of recombinant human endostatin production in fed-batch cultures of Pichia pastoris using the methanol feeding rate

Endostatin is a 20 kDa carboxyl-terminal fragment of collagen XVIII that strongly inhibits angiogenesis and tumor growth. The methylotrophic yeast, Pichia pastoris, is a robust expression system that can be used to study methods to improve the yields of rhEndostatin. We expressed rhEndostatin in P. pastoris under the control of the alcohol oxidase 1 (aox 1) promoter (Mut⁺ phenotype) as a model, and used a cell biomass of about 50 g l^–1 dry cell wt as a starting point for the induction phase and varied the methanol feed rate at 8 ml l^–1 h^–1, 11 ml l^–1 h^–1 and 15 ml l^–1 h^–1. While the cell growth rate was proportional to the rate of methanol delivery, protein production rate was not. These findings could be used to guide parameters for large-scale production of recombinant proteins in the P. pastoris system.     

Temperature limited fed-batch technique for control of proteolysis in <Emphasis Type="Italic">Pichia pastoris</Emphasis> bioreactor cultures

Background  

A temperature limited fed-batch (TLFB) technique is described and used for Pichia pastoris Mut⁺ strain cultures and compared with the traditional methanol limited fed-batch (MLFB) technique. A recombinant fusion protein composed of a cellulose-binding module (CBM) from Neocallimastix patriciarum cellulase 6A and lipase B from Candida antarctica (CALB), was produced and secreted by this strain.     

Effects of temperature and glycerol and methanol‐feeding profiles on the production of recombinant galactose oxidase in Pichia pastoris

Optimization of protein production from methanol‐induced Pichia pastoris cultures is necessary to ensure high productivity rates and high yields of recombinant proteins. We investigated the effects of temperature and different linear or exponential methanol‐feeding rates on the production of recombinant Fusarium graminearum galactose oxidase (EC 1.1.3.9) in a P. pastoris Mut⁺ strain, under regulation of the AOX1 promoter. We found that low exponential methanol feeding led to 1.5‐fold higher volumetric productivity compared to high exponential feeding rates. The duration of glycerol feeding did not affect the subsequent product yield, but longer glycerol feeding led to higher initial biomass concentration, which would reduce the oxygen demand and generate less heat during induction. A linear and a low exponential feeding profile led to productivities in the same range, but the latter was characterized by intense fluctuations in the titers of galactose oxidase and total protein. An exponential feeding profile that has been adapted to the apparent biomass concentration results in more stable cultures, but the concentration of recombinant protein is in the same range as when constant methanol feeding is employed. © 2014 The Authors Biotechnology Progress published by Wiley Periodicals, Inc. on behalf of American Institute of Chemical Engineers Biotechnol. Prog., 30:728–735, 2014     

A non-ionic surfactant reduces the induction time and enhances expression levels of bubaline somatotropin in Pichia pastoris

This study describes a simple approach for enhanced secretory expression of bubaline somatotropin (BbST) in the methylotropic yeast Pichia pastoris. A Mut^s Pichia transformant carrying multi-copy, non-codon optimized BbST cDNA sequence, expressed and secreted the recombinant protein into the culture medium to a level of 25 % of the total proteins in the culture supernatant, after 120 h of induction. Inclusion of polysorbate-80 in the inducing medium resulted in a significant improvement in the BbST expression (up to 45 % of the total culture supernatant proteins) with concomitant reduction in the induction time to 48 h. The amount of BbST obtained was 148 mg/L, which was around fivefold higher than that obtained without the surfactant. BbST was purified to near homogeneity by FPLC on Q-sepharose FF anion-exchange column. Protein authenticity was judged by SDS-PAGE and western blot analyses. A bioassay based on proliferation of Nb2 rat lymphoma cell lines confirmed that the purified, recombinant BbST is biologically active. Use of polysorbate-80 in combination with methanol, during the induction phase, is likely to have general applicability in lowering the induction time and enhancing the secretory expression of other commercially important proteins in Mut^s strains of P. pastoris.     

Enabler for process analytical technology implementation in Pichia pastoris fermentation: Fluorescence‐based soft sensors for rapid quantitation of product titer

Rapid quantitation of product titer is a critical input for control of any bioprocess. This measurement, however, is marred by the myriad components that are present in the fermentation broth, often requiring extensive sample pretreatment before analysis. Spectroscopy techniques such as fluorescence spectroscopy are widely recognized as potential monitoring tools. Here, we investigate the possibility of using fluorescence of the culture supernatant as a potential at‐line monitoring tool to measure the concentration of a recombinant therapeutic protein expressed in a Pichia pastoris fed‐batch fermentation. We propose an integrated method wherein both the target protein and total protein concentrations are predicted using intrinsic riboflavin fluorescence and extrinsic fluorescence, respectively. The root mean square error for estimating the concentrations of the target protein (using riboflavin fluorescence) and total protein (using extrinsic fluorescence) have been estimated to be <0.1 and <0.2, respectively. The proposed approach has been validated for two different biotherapeutic products, human serum albumin and granulocyte colony stimulating factor, that were expressed using Mut⁺ and Mut^s strains of P. pastoris, respectively. The proposed approach is rapid (1 min analysis time, 10 min total with at line sampling) and thus could be a significant enabler for process analytical technology implementation in Pichia fermentation.     

Angiostatin production in cultivation of recombinant Pichia pastoris fed with mixed carbon sources

A recombinant strain of Pichia pastoris with a phenotype of Mut^S was used to produce angiostatin. Due to the low methanol consumption rate of this strain, both methanol and glycerol feedings, that produced oscillation in dissolved O₂ concentration, were used during the expression phase to improve cell growth and angiostatin expression. However, enhanced cell growth led to nitrogen limitation that suppressed further production of angiostatin, but addition of ammonia allowed angiostatin concentration to reach 108 mg l^–1 after an expression period of 96 h. The ratio of consumed glycerol to methanol of 1.5:1 (w/w) in the expression phase suggested that methanol played an important role in the metabolism of carbon sources.     

Mixed-feed exponential feeding for fed-batch culture of recombinant methylotrophic yeast

A simple, accurate model capable of predicting cell growth and methanol utilization during the mixed substrate fed-batch fermentation of Mut^S recombinant Pichia pastoris was developed and was used to design an exponential feeding strategy for mixed substrate fed-batch fermentation at a constant specific growth rate. Mixed substrate feeding has been shown to boost productivity in recombinant fed-batch culture of P. pastoris, while fixed growth rate exponential feeding during fed-batch culture is a useful tool in process optimization and control.     

Characterization of methanol utilization negative Pichia pastoris for secreted protein production: New cultivation strategies for current and future applications

The methanol utilization (Mut) phenotype in the yeast Pichia pastoris (syn. Komagataella spp.) is defined by the deletion of the genes AOX1 and AOX2. The Mut⁻ phenotype cannot grow on methanol as a single carbon source. We assessed the Mut⁻ phenotype for secreted recombinant protein production. The methanol inducible AOX1 promoter (P_AOX1) was active in the Mut⁻ phenotype and showed adequate eGFP fluorescence levels and protein yields (Y_P/X) in small-scale screenings. Different bioreactor cultivation scenarios with methanol excess concentrations were tested using P_AOX1HSA and P_AOX1vHH expression constructs. Scenario B comprising a glucose-methanol phase and a 72-hr-long methanol only phase was the best performing, producing 531 mg/L HSA and 1631 mg/L vHH. 61% of the HSA was produced in the methanol only phase where no biomass growth was observed, representing a special case of growth independent production. By using the Mut⁻ phenotype, the oxygen demand, heat output, and specific methanol uptake (q_methanol) in the methanol phase were reduced by more than 80% compared with the Mut^S phenotype. The highlighted improved process parameters coupled with growth independent protein production are overlooked benefits of the Mut⁻ strain for current and future applications in the field of recombinant protein production.     

Genotype and subtype analyses of hepatitis B virus (HBV) and possible co-infection of HBV and hepatitis C virus (HCV) or hepatitis D virus (HDV) in blood donors, patients with chronic liver disease and patients on hemodialysis in Surabaya, Indonesia

Four subtypes (adw, adr, ayw, and ayr ) and eight genotypes (A to H) of the hepatitis B virus (HBV) have been identified. They appear to be associated with particular geographic distribution, ethnicity, and possibly clinical outcomes. In this study, hepatitis B surface antigen (HBsAg) subtyping and HBV genotyping were carried out on sera obtained from HBsAg-positive HBV carriers, including healthy blood donors; patients with acute hepatitis, chronic hepatitis, liver cirrhosis, and hepatocellular carcinoma; and patients on hemodialysis all located in Surabaya, Indonesia. We report here that all HBV isolates tested in Surabaya belonged to genotype B, with more than 90% of them being classified into subtype adw. Our results also revealed that prevalence of hepatitis C virus (HCV) co-infection among HBV carriers in Surabaya was approximately 10% for healthy blood donors and patients with chronic liver disease, and approximately 60% for patients on maintenance hemodialysis. Interestingly, HBsAg titers were lower in HBV carriers with HCV co-infection than in those without HCV co-infection. We also found that prevalence of hepatitis D virus (HDV) co-infection was < 0.5% among HBV carriers in Surabaya.