Enhancement of alkaline polygalacturonate lyase production in recombinant Pichia pastoris according to the ratio of methanol to cell concentration

Enhancing Antimicrobial Peptide Productivity in Pichia pastoris (Muts Strain) by Improving the Fermentation Process Based on Increasing the Volumetric Methanol Consumption Rate

The instability of the protein expression in Pichia pastoris strains has been an issue for various peptide productions. Some modifications to the traditional fermentation process could potentially solve the problem. Here, we consider a four-stage fermentation process to express the CAP2 (cell-penetrating antimicrobial peptide 2) candidate in P. pastoris KM71H, a slow methanol utilization strain. During the fermentation process, CAP2 productivity is limited (6.15 ± 0.21 mg/L·h) by the low overall methanol consumption (approximately 645 g), which is mainly the result of the slow methanol utilization of the P. pastoris KM71H. To overcome this limitation, we increased the cell concentration two-fold prior to the induction stage. A fed-batch process with exponential and dissolved oxygen tension (DOT) stat feeding strategies was deployed to control the glycerol feed, resulting in an increase in cell concentration and enhancement of the volumetric methanol consumption rate. The improved fermentation process increased the overall methanol consumption (approximately 1070 g) and the CAP2 productivity (13.59 ± 0.24 mg/L·h) by 1.66 and 2.21 times, respectively. In addition, the CAP3 (cell-penetrating antimicrobial peptide 3) candidate could also be produced using this improved fermentation process at a high yield of 3.96 ± 0.02 g/L without any further optimization. Note that there was no oxygen limitation during the improved fermentation process operating at high cell density. This could be due to the controlled substrate addition via the DOT stat system.

Enhanced human lysozyme production by Pichia pastoris via periodic glycerol and dissolved oxygen concentrations control

In human lysozyme (hLYZ) production by Pichia pastoris, the glycerol fed-batch phase was generally implemented under the environment of "oxygen sufficient-glycerol limited" to achieve high cell-density cultivation during the cell growth phase. However, the structural and functional components in P. pastoris cells were irreversible damaged with more and more reactive oxygen species (ROS) accumulation when cells were exposed to the oxygen sufficient environments for long time, leading to a failure of hLYZ expression. In this study, a novel periodic glycerol and dissolved oxygen concentration (DO) control strategy was proposed to solve these problems. This strategy periodically switched the cultivation environments from "oxygen sufficient-glycerol limited" to "oxygen limited-glycerol sufficient" for 5 cycles. When using this strategy: (1) the highest dry cell weight (DCW) of 143.02 g-DCW/L and the lowest distribution of glycerol towards to cell maintenance (0.0400 1/h) were achieved during the glycerol feeding phase by maintaining ROS levels below 48.39 Fluorescence intensity/g-DCW; (2) the adaption time of P. pastoris cells to methanol induction environments was shortened for about 50%; (3) P. pastoris cell metabolic activities reflected by the activities of alcohol oxidase, formaldehyde dehydrogenase, formate dehydrogenase, and methanol consumption rate, etc., in the successive induction phase were largely enhanced; (4) hLYZ activity reached the highest level of 2.45 × 10⁵ IU/mL, which was about 2-fold than that obtained with the strategy of "oxygen sufficient-glycerol limited," when the same methanol induction strategy was adopted. KEY POINTS: • A novel periodic glycerol feeding strategy proposed/used for P. pastoris cell growth. • Higher cell density was obtained by controlling ROS at low level via this strategy. • The highest hLYZ activity was achieved when initiating induction at higher cell density.

An efficient expression tag library based on self-assembling amphipathic peptides

Background

Self-assembling amphipathic peptides (SAPs) may improve protein production or induce the formation of inclusion bodies by fusing them to the N-terminus of proteins. However, they do not function uniformly well with all target enzymes and systematic research on how the composition of SAPs influence the production of fusion protein is still limited.

Results

To improve the efficiency of SAPs, we studied factors that might be involved in SAP-mediated protein production using S1 (AEAEAKAK)₂ as the original SAP and green fluorescent protein (GFP) as the reporter. The results indicate that hydrophobicity and net charges of SAPs play a key role in protein expression. As hydrophobicity regulation tend to cause the formation of insoluble inclusion bodies of protein, an expression tag library composed of SAPs, which varied in net charge (from + 1 to + 20), was constructed based on the random amplification of S1nv1 (ANANARAR)₁₀. The efficiency of the library was validated by polygalacturonate lyase (PGL), lipoxygenase (LOX), l-asparaginase (ASN) and transglutaminase (MTG). To accelerate preliminary screening, each enzyme was fused at the C-terminus with GFP. Among the four enzyme fusions, the SAPs with + 2 – + 6 net charges were optimal for protein expression. Finally, application of the library improved the expression of PGL, LOX, ASN, and MTG by 8.3, 3.5, 2.64, and 3.68-fold relative to that of the corresponding wild-type enzyme, respectively.

Conclusions

This is the first report to study key factors of SAPs as an expression tag to enhance recombinant enzyme production. The SAP library could be used as a novel plug-and-play protein-engineering method to screen for enzymes or proteins with enhanced production.

Electronic supplementary material

The online version of this article (10.1186/s12934-019-1142-9) contains supplementary material, which is available to authorized users.

Optimizing Culture Conditions by Statistical Approach to Enhance Production of Pectinase from Bacillus sp. Y1

It was found that Bacillus sp. Y1 could secrete alkaline pectinase with suitable enzyme system for powerful and fast degumming of ramie fiber. In this study, the medium components and fermentation conditions were optimized by some statistical methods including mixture design, fractional factorial design, central composite design and response surface methodology, and single factor method for enhancing the alkaline pectinase production. The optimized conditions for pectinase production were that the culture was shaken at 34°C for 60 h in 50 mL of medium containing 10.5% (w/v) carbon source (consisting of 3.8% starch, 4.2% wheat bran, and 2.5% sucrose), 0.37% (NH₄)₂SO₄, 0.3% MgSO₄, and 0.1% Tween-80, with initial pH 8.2 and inoculation amount of 1.3 mL (with the OD600 of the seed medium about 5.77). Using the optimizing conditions, the activities of polygalacturonate lyase (PGL) and polygalacturonase (PG) in fermentation liquor were increased to 2.00-fold and 3.44-fold, respectively, and the fermentation time shortened 12 hours (from 72 h to 60 h), which showed good application potential in degumming of ramie.

Bioreactor-Scale Strategies for the Production of Recombinant Protein in the Yeast Yarrowia lipolytica

Recombinant protein production represents a multibillion-dollar market. Therefore, it constitutes an important research field both in academia and industry. The use of yeast as a cell factory presents several advantages such as ease of genetic manipulation, growth at high cell density, and the possibility of post-translational modifications. Yarrowia lipolytica is considered as one of the most attractive hosts due to its ability to metabolize raw substrate, to express genes at a high level, and to secrete protein in large amounts. In recent years, several reviews have been dedicated to genetic tools developed for this purpose. Though the construction of efficient cell factories for recombinant protein synthesis is important, the development of an efficient process for recombinant protein production in a bioreactor constitutes an equally vital aspect. Indeed, a sports car cannot drive fast on a gravel road. The aim of this review is to provide a comprehensive snapshot of process tools to consider for recombinant protein production in bioreactor using Y. lipolytica as a cell factory, in order to facilitate the decision-making for future strain and process engineering.

A xylanase from Streptomyces sp. FA1: heterologous expression, characterization, and its application in Chinese steamed bread

Xylanases (EC 3.2.1.8) are hydrolytic enzymes that have found widespread application in the food, feed, and paper-pulp industries. Streptomyces sp. FA1 xynA was expressed as a secreted protein in Pichia pastoris, and the xylanase was applied to the production of Chinese steamed bread for the first time. The optimal pH and the optimal temperature of XynA were 5.5 and 60 °C, respectively. Using beechwood as substrate, the K  m and V  max were 2.408 mg mL−1 and 299.3 µmol min−1 mg−1, respectively. Under optimal conditions, a 3.6-L bioreactor produced 1374 U mL−1 of XynA activity at a protein concentration of 6.3 g L−1 after 132 h of fermentation. Use of recombinant XynA led to a greater increase in the specific volume of the CSB than could be achieved using commercial xylanase under optimal conditions. This study provides the basis for the application of the enzyme in the baking industry.

An artificial neural network for membrane-bound catechol-O-methyltransferase biosynthesis with Pichia pastoris methanol-induced cultures

BACKGROUND

Membrane proteins are important drug targets in many human diseases and gathering structural information regarding these proteins encourages the pharmaceutical industry to develop new molecules using structure-based drug design studies. Specifically, membrane-bound catechol-O-methyltransferase (MBCOMT) is an integral membrane protein that catalyzes the methylation of catechol substrates and has been linked to several diseases such as Parkinson's disease and Schizophrenia. Thereby, improvements in the clinical outcome of the therapy to these diseases may come from structure-based drug design where reaching MBCOMT samples in milligram quantities are crucial for acquiring structural information regarding this target protein. Therefore, the main aim of this work was to optimize the temperature, dimethylsulfoxide (DMSO) concentration and the methanol flow-rate for the biosynthesis of recombinant MBCOMT by Pichia pastoris bioreactor methanol-induced cultures using artificial neural networks (ANN).

RESULTS

The optimization trials intended to evaluate MBCOMT expression by P. pastoris bioreactor cultures led to the development of a first standard strategy for MBCOMT bioreactor biosynthesis with a batch growth on glycerol until the dissolved oxygen spike, 3 h of glycerol feeding and 12 h of methanol induction. The ANN modeling of the aforementioned fermentation parameters predicted a maximum MBCOMT specific activity of 384.8 nmol/h/mg of protein at 30°C, 2.9 mL/L/H methanol constant flow-rate and with the addition of 6% (v/v) DMSO with almost 90% of healthy cells at the end of the induction phase. These results allowed an improvement of MBCOMT specific activity of 6.4-fold in comparison to that from the small-scale biosynthesis in baffled shake-flasks.

CONCLUSIONS

The ANN model was able to describe the effects of temperature, DMSO concentration and methanol flow-rate on MBCOMT specific activity, as shown by the good fitness between predicted and observed values. This experimental procedure highlights the potential role of chemical chaperones such as DMSO in improving yields of recombinant membrane proteins with a different topology than G-coupled receptors. Finally, the proposed ANN shows that the manipulation of classic fermentation parameters coupled with the addition of specific molecules can open and reinforce new perspectives in the optimization of P. pastoris bioprocesses for membrane proteins biosynthesis.

Construction of efficient xylose utilizing Pichia pastoris for industrial enzyme production

Background

Cellulosic biomass especially agricultural/wood residues can be utilized as feedstock to cost-effectively produce fuels, chemicals and bulk industrial enzymes, which demands xylose utilization from microbial cell factories. While previous works have made significant progress in improving microbial conversion of xylose into fuels and chemicals, no study has reported the engineering of efficient xylose utilizing protein expression systems for the purpose of producing industrial enzymes.

Results

In this work, using Pichia pastoris as an example, we demonstrated the successful engineering of xylose metabolizing ability into of protein expression systems. A heterologous XI (xylose isomerase) pathway was introduced into P. pastoris GS115 by overexpressing the Orpinomyces spp. XI or/and the endogenous XK (xylulokinase) gene, and evolutionary engineering strategies were also applied. Results showed that the XI pathway could be functionally expressed in P. pastoris. After 50 generation of sequential batch cultivation, a set of domesticated recombinant P. pastoris strains with different performance metrics on xylose were obtained. One evolved strain showed the highest xylose assimilation ability, whose cell yield on xylose can even be comparable to that on glucose or glycerol. This strain also showed significantly increased β-mannanase production when cultured on xylose medium. Furthermore, transcription analysis of xylose pathway genes suggested that overexpression of XI and XK might be the key factors affecting effective xylose assimilation.

Conclusions

To our best knowledge, this study is the first work demonstrating the construction of efficient xylose utilizing P. pastoris strains, thus providing a basis for using cellulosic biomass for bulk industrial enzyme production.

Optimization of heterologous expression of the phytase (PPHY) of Pichia anomala in P. pastoris and its applicability in fractionating allergenic glycinin from soy protein

The phytase (PPHY) of Pichia anomala has the requisite properties of thermostability and acidstability, broad substrate spectrum, and protease insensitivity, which make it a suitable candidate as a feed and food additive. The 1,389-bp PPHY gene was amplified from P. anomala genomic DNA, cloned in pPICZαA, and expressed extracellularly in P. pastoris X33. Three copies of PPHY have been detected integrated into the chromosomal DNA of the recombinant P. pastoris. The size exclusion chromatography followed by electrophoresis of the pure rPPHY confirmed that this is a homohexameric glycoprotein of ~420 kDa with a 24.3 % portion as N-linked glycans. The temperature and pH optima of rPPHY are 60 °C and 4.0, similar to the endogenous enzyme. The kinetic characteristics K(m), V(max), K(cat), and K(cat)/K(m) of rPPHY are 0.2 ± 0.03 mM, 78.2 ± 1.43 nmol mg(-1) s(-1), 65,655 ± 10.92 s(-1), and 328.3 ± 3.12 μM(-1) s(-1), respectively. The optimization of medium components led to a 21.8-fold improvement in rPPHY production over the endogenous yeast. The rPPHY titer attained in shake flasks could also be sustained in the laboratory fermenter. The rPPHY accounts for 57.1 % of the total secreted protein into the medium. The enzyme has been found useful in fractionating allergenic protein glycinin from soya protein besides dephytinization.

Enhancing production of alkaline polygalacturonate lyase from Bacillus subtilis by fed-batch fermentation

Alkaline polygalacturonate lyase (PGL, EC 4.2.2.2) is an enzyme used in many industries. We developed a fed-batch fermentation process that combines the enzymatic pretreatment of the carbon source with controlling the pH of the fermentative broth to enhance the PGL production from Bacillus subtilis 7-3-3 to decrease the production cost. Maintaining the fermentation broth at pH 6.5 prior to feeding with ammonia and at pH 6.0 after feeding significantly improved PGL activity (743.5 U mL-1) compared with the control (202.5 U mL-1). The average PGL productivity reached 19.6 U mL-1 h-1 after 38 h of fermentation. The crude PGL was suitable for environmentally friendly ramie enzymatic degumming.

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

High-level extracellular production of alkaline polygalacturonate lyase in Bacillus subtilis with optimized regulatory elements

The present work aims to construct a robust recombinant Bacillus subtilis to achieve secretory production of alkaline polygalacturonate lyase (PGL). First, 6 signal peptides (amyX, bpr, vpr, yvgO, wapA and nprE) were screened with a semi-rational approach and comparatively investigated their effects on the production of PGL. The signal peptide bpr directed efficient PGL secretory expression and increased PGL titer to 313.7 U mL(-1). By optimizing and applying strong promoter P43 and Shine-Dalgarno sequence, higher titer of 446.3 U mL(-1) PGL was achieved. Finally, the capacity of the recombinant B. subtilis WB43CB was evaluated with a fed-batch strategy in 3 L fermentor. The PGL titer reached 632.6 U mL(-1) with a productivity of 17.6 U mL(-1) h(-1), which was the highest secretory production of PGL by the B. subtilis system. The recombinant B. subtilis strain WB43CB constructed in the present work has great potential in production of alkaline PGL.

How to achieve high-level expression of microbial enzymes: strategies and perspectives

Microbial enzymes have been used in a large number of fields, such as chemical, agricultural and biopharmaceutical industries. The enzyme production rate and yield are the main factors to consider when choosing the appropriate expression system for the production of recombinant proteins. Recombinant enzymes have been expressed in bacteria (e.g., Escherichia coli, Bacillus and lactic acid bacteria), filamentous fungi (e.g., Aspergillus) and yeasts (e.g., Pichia pastoris). The favorable and very advantageous characteristics of these species have resulted in an increasing number of biotechnological applications. Bacterial hosts (e.g., E. coli) can be used to quickly and easily overexpress recombinant enzymes; however, bacterial systems cannot express very large proteins and proteins that require post-translational modifications. The main bacterial expression hosts, with the exception of lactic acid bacteria and filamentous fungi, can produce several toxins which are not compatible with the expression of recombinant enzymes in food and drugs. However, due to the multiplicity of the physiological impacts arising from high-level expression of genes encoding the enzymes and expression hosts, the goal of overproduction can hardly be achieved, and therefore, the yield of recombinant enzymes is limited. In this review, the recent strategies used for the high-level expression of microbial enzymes in the hosts mentioned above are summarized and the prospects are also discussed. We hope this review will contribute to the development of the enzyme-related research field.

An effective degumming enzyme from Bacillus sp. Y1 and synergistic action of hydrogen peroxide and protease on enzymatic degumming of ramie fibers

Enzymatic degumming, as an alternative to chemical processing, has attracted wide attention. However, to date, little information about other enzyme components with effective degumming except pectinase has been reported, and there is no report about the effect of bleaching agent (H₂O₂) on enzymatic degumming and combining enzymatic degumming and H₂O₂ bleaching process. In this study, we found that the crude enzyme of wild-type Bacillus sp. Y1 had a powerful and fast degumming ability. Its PGL activity was the highest at pH 9.6–10.0 and 60°C and stable at pH 7–10.5 and 30–50°C, having a wide scope of pH and temperature. Its PGL also had a high H₂O₂ tolerance, and the gum loss and brightness of fibers could be significantly improved when H₂O₂ was added into it for degumming. The synergistic action was also found between it and H₂O₂ on the degumming and bleaching of ramie fibers. All showed that it was very suitable for a joint process of enzymatic degumming and H₂O₂ bleaching. It also contained more proteins compared with a control pectinase, and its high protease content was further substantiated as a factor for effective degumming. Protease and pectinase also had a synergistic action on degumming.

Comparative analysis of heterologous expression, biochemical characterization optimal production of an alkaline α-amylase from alkaliphilic Alkalimonas amylolytica in Escherichia coli and Pichia pastoris

An alkaline α-amylase gene from alkaliphilic Alkalimonas amylolytica was synthesized based on the preferred codon usage of Escherichia coli and Pichia pastoris, respectively, and then was expressed in the according heterologous host, E. coli BL21 (DE3) and P. pastoris GS115. The alkaline α-amylase expressed in E. coli was designated AmyA, whereas that produced by P. pastoris was designated AmyB. The specific activity of AmyA and AmyB was 16.0 and 16.6 U/mg at pH 9.5 and 50°C, respectively. The optimal pH and pH stability of AmyA and AmyB were similar, whereas the optimum temperature and thermal stability of AmyB were slightly enhanced compared with those of AmyA. The AmyA and AmyB had a similar melting temperature of 64°C and the same catalytic efficiency (k(cat) /K(m) ) of 2.0 × 10(6) L/(mol min). AmyA and AmyB were slightly activated by 1 mM Co(2+) , Ca(2+) , or Na(+) , but inhibited by all other metal ions (K(+) , Mg(2+) , Fe(3+) , Fe(2+) , Zn(2+) , Mn(2+) , and Cu(2+) ). Tween 80 or Tween 60 (10% (w/v)) had little influence on the stability of AmyA and AmyB, while the 10% (w/v) sodium dodecyl sulfate caused the complete loss of AmyA and AmyB activities. The AmyA and AmyB were stable in the presence of solid detergents (washing powder), while were less stable in liquid detergents. Under the optimal conditions in 3-L bioreactor, the extracellular AmyB activity reached 600 U/mL, which was about 10 times as that of AmyA. These results indicated that P. pastoris was a preferable host for alkaline α-amylase expression and the produced alkaline α-amylase had a certain application potential in solid detergents.

Overproduction of a truncated poly (vinyl alcohol) dehydrogenase in recombinant Pichia pastoris by low-temperature induction strategy and related mechanism analysis

Based on the N-terminal sequencing of poly (vinyl alcohol) dehydrogenase (PVADH), a 1,644-bp gene encoding a truncated PVADH (tPVADH) was amplified using the synthetic gene (GenBank accession No. JQ235753) as a template, and was further transformed into Pichia pastoris GS115 with the vector pPIC9K. The maximal tPVADH activity reached 546 U/mL in shake flask. The influence of methanol concentration and induction temperature on tPVADH production was further investigated in 3-L bioreactor. When the methanol concentration and induction temperature were controlled at 15 g/L and 22 °C, respectively, the maximal tPVADH activity reached 8,464 U/mL, which was nearly 10 times that of mature PVADH expressed under the same condition and was the highest level ever reported. The reason responsible for the significant improvement of tPVADH production at low induction temperature was explored in terms of cell viability, extracellular proteases activity, and alcohol oxidase activity.

Increased production of alkaline polygalacturonate lyase in the recombinant Pichia pastoris by controlling cell concentration during continuous culture

Recombinant alkaline polygalacturonate lyase (PGL) production by recombinant Pichia pastoris GS115 was selected as a model to study as a continuous culture strategy for enhancing heterologous protein production based on controlling methanol feeding (CCCM culture) or on dual carbon source feeding (CCCD culture). Using the CCCM process with a dry cell weight of 75 g/L regulated by controlling methanol concentration in the induction media, the final PGL activity was 441.9 U/mL. The PGL productivity (Q(v)) and the average specific enzyme production rate (Q(x)) were 4.65 U mL(-1)h(-1) and 84.5 U g(-1)h(-1), an increase of 42.1% and 191.2%, respectively, over what was achieved with traditional fed-batch culture with high cell density. The control strategies also reduced proteolytic degradation by 84.1% in the fermentation broth and increased cell viability by 12.2%.

Development of an industrial medium and a novel fed-batch strategy for high-level expression of recombinant β-mananase by Pichia pastoris

An industrial medium, Corn Steep Liquor Powder Dextrose (CSD medium) was developed for constitutive expression of recombinant β-mananase by Pichia pastoris. The β-mananase activity (513 U/mL) with CSD medium was 1.64- and 2.5-fold higher than with YPD and BSM in shaken flasks. The β-mananase productivity with CSD medium was 61.0 U/mL h, which was 1.7- and 2.5-fold higher than with YPD and BSM in a 5-L fermenter based on a novel fed-batch strategy combining the real-time exponential feed mode with the DO-stat feed mode. The β-mananase activity, dry cell weight and the recombinant enzyme reached up to 5132 U/mL, 110.0 g/L and 4.50 g/L after 50 h cultivation in a 50-L fermenter. The high efficient expression of recombinant β-mananase by P. pastoris indicated that CSD medium and the novel fed-batch strategy have great potential for the production of recombinant β-mananase in industrial fermentation.

Development of a cultivation process for the enhancement of human interferon alpha 2b production in the oleaginous yeast, Yarrowia lipolytica

BACKGROUND

As an oleaginous yeast, Yarrowia lipolytica is able to assimilate hydrophobic substrates. This led to the isolation of several promoters of key enzymes of this catabolic pathway. Less is known about the behavior of Y. lipolytica in large bioreactors using these substrates. There is therefore a lack of established know-how concerning high cell density culture protocols of this yeast. Consequently, the establishment of suitable induction conditions is required, to maximize recombinant protein production under the control of these promoters.

RESULTS

Human interferon α2b (huIFN α2b) production in Yarrowia lipolytica was used as a model for the enhancement of recombinant protein production under the control of the oleic acid (OA)-inducible promoter POX2. Cell viability and heterologous protein production were enhanced by exponential glucose feeding, to generate biomass before OA induction. The optimal biomass level before induction was determined (73 g L(-1)), and glucose was added with oleic acid during the induction phase. Several oleic acid feeding strategies were assessed. Continuous feeding with OA at a ratio of 0.02 g OA per g dry cell weight increased huIFNα2b production by a factor of 1.88 (425 mg L(-1)) and decreased the induction time (by a factor of 2.6, 21 h). huIFN α2b degradation by an aspartic protease secreted by Y. lipolytica was prevented by adding pepstatin (10 μM), leading to produce a 19-fold more active huIFN α2b (26.2 × 10(7) IU mg(-1)).

CONCLUSION

Y. lipolytica, a generally regarded as safe (GRAS) microorganism is one of the most promising non conventional yeasts for the production of biologically active therapeutic proteins under the control of hydrophobic substrate-inducible promoter.

Overproduction of alkaline polygalacturonate lyase in recombinant Escherichia coli by a two-stage glycerol feeding approach

This work aims to achieve the overproduction of alkaline polygalacturonate lyase (PGL) with recombinant Escherichia coli by a two-stage glycerol feeding approach. First, the PGL coding gene from Bacillus subtilis WSHB04-02 was expressed in E. coli BL21 (DE3) under the strong inducible T7 promoter of the pET20b (+) vector. And then the influence of media composition, induction temperature, and inducer isopropyl β-D-1-thiogalactopyranoside (IPTG) concentration on cell growth and PGL production was investigated. Finally, a two-stage glycerol feeding strategy was proposed and applied in a 3-L fermenter, where cultivation was conducted at a controlled specific growth rate (μset=0.2) during pre-induction phase, followed by a constant glycerol feeding rate of 12 ml h(-1) at post-induction phase. The total PGL yield reached 371.86 U mL(-1), which is the highest PGL production by recombinant E. coli expression system.

Enhancement of cell viability and alkaline polygalacturonate lyase production by sorbitol co-feeding with methanol in Pichia pastoris fermentation

Alkaline polygalacturonate lyase (PGL) production by Pichia pastoris GS115 was used as a model to study the mechanism and strategy for enhancing heterologous protein production. In order to enhance cell viability and volumetric recombinant protein productivity, sorbitol, which had been confirmed to be a non-repressive carbon source, was added together with methanol during the induction phase. The resultant PGL activity was up to 1593 U mL(-1), which was enhanced 1.85-fold compared to the control (863 U mL(-1)) cultured with sorbitol added at a constant rate of 3.6 g h(-1)L(-1) after an induction period of 100 h. Further results revealed that an appropriate sorbitol co-feeding strategy not only decreased the cell mortality to 8.8% (the control is about 23.1%) in the end of fermentation, but also reduced the proteolytic degradation of PGL.