Fed-batch high-cell-density fermentation strategies for Pichia pastoris growth and production

Pichia pastoris is extensively used to produce various heterologous proteins. Amounts of biopharmaceutical drugs and industrial enzymes have been successfully produced by fed-batch high-cell-density fermentation (HCDF) of this cell factory. High levels of cell mass in defined media can be easily achieved and therefore large quantities of recombinant proteins with enhanced activities and lower costs can be obtained through HCDF technology. A robust HCDF process makes a successful transition to commercial production. Recently, efforts have been made to increase the heterologous protein production and activity by the HCDF of P. pastoris. However, challenges around selecting a suitable HCDF strategy exist. The high-level expression of a specific protein in P. pastoris is still, at least in part, limited by optimizing the methanol feeding strategy. Here, we review the progress in developments and applications of P. pastoris HCDF strategies for enhanced expression of recombinant proteins. We focus on the methanol induction strategies for efficient fed-batch HCDF in bioreactors, mainly focusing on various stat-induction strategies, co-feeding, and the limited induction strategy. These processes control strategies have opened the door for expressing foreign proteins in P. pastoris and are expected to enhance the production of recombinant proteins.     

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.     

Improved production of human type II procollagen in the yeast <Emphasis Type="Italic">Pichia pastoris</Emphasis> in shake flasks by a wireless-controlled fed-batch system

Background  

Here we describe a new technical solution for optimization of Pichia pastoris shake flask cultures with the example of production of stable human type II collagen. Production of recombinant proteins in P. pastoris is usually performed by controlling gene expression with the strong AOX1 promoter, which is induced by addition of methanol. Optimization of processes using the AOX1 promoter in P. pastoris is generally done in bioreactors by fed-batch fermentation with a controlled continuous addition of methanol for avoiding methanol toxification and carbon/energy starvation. The development of feeding protocols and the study of AOX1-controlled recombinant protein production have been largely made in shake flasks, although shake flasks have very limited possibilities for measurement and control.     

Oxygen-limited fed-batch process: an alternative control for Pichia pastoris recombinant protein processes

An oxygen-limited fed-batch technique (OLFB) was compared to traditional methanol-limited fed-batch technique (MLFB) for the production of recombinant Thai Rosewood β-glucosidase with Pichia pastoris. The degree of energy limitation, expressed as the relative rate of respiration (q _O/q _O,max), was kept similar in both the types of processes. Due to the higher driving force for oxygen transfer in the OLFB, the oxygen and methanol consumption rates were about 40% higher in the OLFB. The obligate aerobe P. pastoris responded to the severe oxygen limitation mainly by increased maintenance demand, measured as increased carbon dioxide production per methanol, but still somewhat higher cell density (5%) and higher product concentrations (16%) were obtained. The viability was similar, about 90–95%, in both process types, but the amount of total proteins released in the medium was much less in the OLFB processes resulting in substantially higher (64%) specific enzyme purity for input to the downstream processing.     

Decrease of proteolytic degradation of recombinant hirudin produced by Pichia pastoris by controlling the specific growth rate

The effects of the specific growth rate and methanol concentration on the degradation of hirudin produced by recombinant Pichia pastoris were investigated. When a methanol-limited state and the specific growth rate of 0.02 h^–1 were maintained during the fermentation, a minimum degradation of hirudin and a maximum specific hirudin production rate were achieved. By this strategy, the production of intact recombinant hirudin Hir65 reached 0.7 g l^–1 in fed-batch fermentation. Its proportion was 35% to all forms of hirudin.     

Improving thermal hysteresis activity of antifreeze protein from recombinant Pichia pastoris by removal of N-glycosylation

To survive in a subzero environment, polar organisms produce ice-binding proteins (IBPs). These IBPs prevent the formation of large intracellular ice crystals, which may be fatal to the organism. Recently, a recombinant FfIBP (an IBP from Flavobacterium frigoris PS1) was cloned and produced in Pichia pastoris using fed-batch fermentation with methanol feeding. In this study, we demonstrate that FfIBP produced by P. pastoris has a glycosylation site, which diminishes the thermal hysteresis activity of FfIBP. The FfIBP expressed by P. pastoris exhibited a doublet on SDS-PAGE. The results of a glycosidase reaction suggested that FfIBP possesses complex N-linked oligosaccharides. These results indicate that the residues of the glycosylated site could disturb the binding of FfIBP to ice molecules. The findings of this study could be utilized to produce highly active antifreeze proteins on a large scale.     

Microscale Perfusion-Based Cultivation for Pichia pastoris Clone Screening Enables Accelerated and Optimized Recombinant Protein Production Processes

Pichia pastoris has emerged in the past years as a promising host for recombinant protein and biopharmaceutical production. In the establishment of high cell density fed-batch biomanufacturing, screening phase and early bioprocess development (based on microplates and shake flasks) still represent a bottleneck due to high-cost and time-consuming procedures as well as low experiment complexity. In the present work, a screening protocol developed for P. pastoris clone selection is implemented in a multiplexed microfluidic device with 15 μL cultivation chambers able to operate in perfusion mode and monitor dissolved oxygen content in the culture in a non-invasive way. The setup allowed us to establish carbon-limited conditions and evaluate strain responses to different input variables. Results from micro-scale perfusion cultures are then compared with 1L fed-batch fermentation. The best producer in terms of titer and productivity is rapidly identified after 12 h from inoculation and the results confirmed by lab-scale fermentation. Moreover, the physiological analyses of the strains under different conditions suggested how more complex experimental conditions are achievable despite the relatively easy, straight-forward, and cost-effective experimental setup. Implementation and standardization of these micro-scale protocols could reduce the demand for lab-scale bioreactor cultivations thus accelerating the development of protein production processes.     

Modeling of mini-proinsulin production in Pichia pastoris using the AOX promoter

An unstructured model based on mass balance equations for a recombinant methylotrophic yeast Pichia pastoris Mut^S (Methanol Utilization Slow) strain expressing the mini-proinsulin (MPI), was successfully established in quasi-steady state fed-batch fermentations with varying total quantity of biomass in a 7 l fermenter. The model describes the relationships between the total biomass and induction time, both in the batch and fed-batch phases. In addition, good correlations were obtained when the total quantity of MPI was correlated with the total biomass, demonstrating that the product of interest is associated with growth in the methanol phase. The parameters of the fermentation model obtained are similar to those reported by other researchers.     

Quantitative physiology of Pichia pastoris during glucose‐limited high‐cell density fed‐batch cultivation for recombinant protein production

Pichia pastoris has become one of the major microorganisms for the production of proteins in recent years. This development was mainly driven by the readily available genetic tools and the ease of high‐cell density cultivations using methanol (or methanol/glycerol mixtures) as inducer and carbon source. To overcome the observed limitations of methanol use such as high heat development, cell lysis, and explosion hazard, we here revisited the possibility to produce proteins with P. pastoris using glucose as sole carbon source. Using a recombinant P. pastoris strain in glucose limited fed‐batch cultivations, very high‐cell densities were reached (more than 200 g_CDW L^?1) resulting in a recombinant protein titer of about 6.5 g L^?1. To investigate the impact of recombinant protein production and high‐cell density fermentation on the metabolism of P. pastoris, we used ¹³C‐tracer‐based metabolic flux analysis in batch and fed‐batch experiments. At a controlled growth rate of 0.12 h^?1 in fed‐batch experiments an increased TCA cycle flux of 1.1 mmol g^?1 h^?1 compared to 0.7 mmol g^?1 h^?1 for the recombinant and reference strains, respectively, suggest a limited but significant flux rerouting of carbon and energy resources. This change in flux is most likely causal to protein synthesis. In summary, the results highlight the potential of glucose as carbon and energy source, enabling high biomass concentrations and protein titers. The insights into the operation of metabolism during recombinant protein production might guide strain design and fermentation development. Biotechnol. Bioeng. 2010;107: 357–368. © 2010 Wiley Periodicals, Inc.     

Optimization of the fermentation parameters for the production of Ganoderma lucidum immunomodulatory protein by Pichia pastoris

Abstract

In order to obtain a better fermentation parameter for the production of recombinant Ganoderma lucidum immunomodulatory protein (rFIP-glu), an engineered Pichia pastoris GS115 was investigated on the fermentation time, temperature, methanol concentration and initial pH of media, while immunomodulatory activities of the rFIP-glu was confirmed. L₉(3³) orthogonal experiment were firstly employed to optimize various fermentation parameters in the shake-flask level. The optimized fermentation parameters were subsequently verified in a 5?L fermenter. Biological activities including cell viability and tumor necrosis factor-alpha (TNF-α) mRNA of the rFIP-glu were evaluated on murine macrophage RAW264.7 cells. The results showed that the yield of rFIP-glu was up to 368.71?μg/ml in the shake-flask, and 613.47?μg/ml in the 5?L fermenter, when the Pichia pastoris was incubated in basic media with the methanol concentration 1.0% and initial pH 6.5, and with constant shaking at 280?rpm for 4?days at 26?°C. In vitro assays of biological activity indicated that rFIP-glu had significant toxicity against RAW264.7 cells, and possessed the ability to induce TNF-α mRNA expression in macrophage RAW264.7 cells. In conclusion, engineered P. pastoris showed a good fermentation property under the optimum fermentation parameters. It could be a candidate industrial strain for further study.     

A novel feeding strategy for enhanced protein production by fed-batch fermentation in recombinant Pichia pastoris

A novel feeding strategy for enhanced protein production of hepatitis B virus surface antigen (HBsAg) in fed-batch fermentation, recombinant Pichia pastoris, has been developed. A minimal salt medium was used to grow cells in the initial batch fermentation, followed by a glycerol+salts fed-batch phase. At the end of the fed-batch phase a dry cell weight of 130 g l⁻¹ was achieved. In the absence of basal salts, the same amount of glycerol feed resulted in only 90 g l⁻¹ cell dry weight. When a limited amount of casamino acids were also included every 24 h during methanol induction, there was a two-fold increase in expression levels of HBsAg. After 192 h of induction, the expression levels of HBsAg (soluble and insoluble) reached >1 g l⁻¹ using the Mut⁻ strain. Thus, the use of basal salts in the glycerol feed, along with the addition of limited amounts of casamino acids with the methanol feed, resulted in an increased expression of total HBsAg.     

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.     

Expression of hepatitis B surface antigen major subtypes in Pichia pastoris and purification for in vitro diagnosis

This study describes the expression in Pichia pastoris of hepatitis B surface antigens (HBsAg) corresponding to the S region of the four major subtypes: adr, adw2, ayr and ayw3 and to the preS2-S region of the two subtypes adr and adw2. The recombinant yeast strains have been selected amongst methanol utilization positive (Mut⁺) or sensitive strains (Mut^s) and cultivated to high cell density in bioreactor using a short protocol. Our results prove the efficiency of P. pastoris to produce all the major HBsAg subtypes and confirm the ability of the methanol regulated promoter of alcohol oxidase I gene (AOX) to express heterologous protein through phenotype Mut⁺ or Mut^s strains.All these recombinant HBsAg proteins, including subtype ayr, whose production has never been presented, have been highly purified using a short original sequence of steps which includes high-pressure cell disruption associated with detergent treatment, ultrafiltration and immunopurification chromatography using a mAb anti-HBs. The whole process avoids possible alterations of antigenic properties and allows to obtain with high yield, high quality reagents for in vitro diagnosis.     

Production and Purification of the Heavy-Chain Fragment C of Botulinum Neurotoxin, Serotype B, Expressed in the Methylotrophic YeastPichia pastoris

A recombinant H_cfragment of botulinum neurotoxin, serotype B (rBoNTB(H_c)), has been successfully expressed in a Mut⁺strain of the methylotrophic yeastPichia pastorisfor use as an antigen in a proposed human vaccine. The fermentation process consisted of batch phase on glycerol, followed by glycerol and methanol fed-batch phases yielding a final cell mass of 60 g/L (dcw) and was easily scaled-up to 60 L. A multistep ion-exchange chromatographic purification process was employed to produce 99% pure H_cfragment. The final yield of the purified antigen was 390 mg per kilogram of wet cell mass. The purified H_cfragment of serotype B was stable, elicited an immune response in mice, and protected upon challenge with native botulin.     

The secretome of Pichia pastoris in fed-batch cultivations is largely independent of the carbon source but changes quantitatively over cultivation time

The quantitative changes of the secretome of recombinant Pichia pastoris (Komagataella phaffii) CBS7435 over the time-course of methanol- or glucose-limited fed-batch cultures were investigated by LC-ESI-MS/MS to define the carbon source-specific secretomes under controlled bioreactor conditions. In both set-ups, no indication for elevated cell lysis was found. The quantitative data revealed that intact and viable P. pastoris cells secrete only a low number of endogenous proteins (in total 51), even during high cell density cultivation. Interestingly, no marked differences in the functional composition of the P. pastoris secretome between methanol- and glucose-grown cultures were observed with only few proteins being specifically affected by the carbon source. The ‘core secretome’ of 22 proteins present in all analysed carbon sources (glycerol, glucose and methanol) consists mainly of cell wall proteins. The quantitative analysis additionally revealed that most secretome proteins were already present after the batch phase, and depletion rather than accumulation occurred during the fed-batch processes. Among the changes over cultivation time, the depletion of both the extracellularly detected chaperones and the only two identified proteases (Pep4 and Yps1-1) during the methanol- or glucose-feed phase appear as most prominent.     

A simple Pichia pastoris fermentation and downstream processing strategy for making recombinant pandemic Swine Origin Influenza A virus Hemagglutinin protein

The present Influenza vaccine manufacturing process has posed a clear impediment to initiation of rapid mass vaccination against spreading pandemic influenza. New vaccine strategies are therefore needed that can accelerate the vaccine production. Pichia offers several advantages for rapid and economical bulk production of recombinant proteins and, hence, can be attractive alternative for producing an effective influenza HA based subunit vaccine. The recombinant Pichia harboring the transgene was subjected to fed-batch fermentation at 10 L scale. A simple fermentation and downstream processing strategy is developed for high-yield secretory expression of the recombinant Hemagglutinin protein of pandemic Swine Origin Influenza A virus using Pichia pastoris via fed-batch fermentation. Expression and purification were optimized and the expressed recombinant Hemagglutinin protein was verified by sodium dodecyl sulfate polyacrylamide gel electrophoresis, Western blot and MALDI-TOF analysis. In this paper, we describe a fed-batch fermentation protocol for the secreted production of Swine Influenza A Hemagglutinin protein in the P. pastoris GS115 strain. We have shown that there is a clear relationship between product yield and specific growth rate. The fed-batch fermentation and downstream processing methods optimized in the present study have immense practical application for high-level production of the recombinant H1N1 HA protein in a cost effective way using P. pastoris.     

Production of salmosin, a snake venom-derived disintegrin, in recombinant Pichia pastoris using high cell density fed-batch fermentation

Salmosin, a snake venom-derived disintegrin, was successfully expressed in the methylotrophic yeast Pichia pastoris and secreted into the culture supernatant, as a 6 kDa protein. High-cell density fermentation of recombinant P. pastoris was optimized for the mass production of salmosin. In a 5 L jar fermentor, recombinant P. pastoris was fermented in growth medium containing 5% (w/v) glycerol at the controlled pH of 5.0. After culturing for 21 h, glycerol feeding medium was fed at one time into the culture broth. After 7 h (a total of 28 h), induction medium that contained methanol was increasingly added until the culture time totaled 75 h. Finally, these optimized culture conditions produced a high cell density of recombinant P. pastoris (dry cell weight of 113.38 g/L) and led to the mass production of salmosin (a total protein concentration of 369.2 mg/L). The culture supernatant containing salmosin inhibited platelet aggregation, resulting in a platelet aggregation of 9% compared to that of 94% in the control experiment, without culture supernatant. These results demonstrate that recombinant salmosin in culture supernatant from high cell density fed-batch fermentation can serve as a platelet aggregation inhibitor.     

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.     

Operational strategies, monitoring and control of heterologous protein production in the methylotrophic yeast Pichia pastoris under different promoters: A review

The methylotrophic yeast Pichia pastoris has been widely reported as a suitable expression system for heterologous protein production. The use of different phenotypes under PAOX promoter, other alternative promoters, culture medium, and operational strategies with the objective to maximize either yield or productivity of the heterologous protein, but also to obtain a repetitive product batch to batch to get a robust process for the final industrial application have been reported. Medium composition, kinetics growth, fermentation operational strategies from fed-batch to continuous cultures using different phenotypes with the most common PAOX promoter and other novel promoters (GAP, FLD, ICL), the use of mixed substrates, on-line monitoring of the key fermentation parameters (methanol) and control algorithms applied to the bioprocess are reviewed and discussed in detail.