Production of wild-type and peptide fusion cutinases by recombinant Saccharomyces cerevisiae MM01 strains

This study focused on the growth of Saccha-romyces cerevisiae MM01 recombinant strains and the respective production of three extracellular heterologous cutinases: a wild-type cutinase and two cutinases in which the primary structure was fused with the peptides (WP)(2) and (WP)(4), respectively. Different cultivation and strategies were tested in a 2-L shake flask and a 5-L bioreactor, and the respective cell growth and cutinase production were analyzed and compared for the three yeast strains. The highest cutinase productions and productivities were obtained in the fed-batch culture, where wild-type cutinase was secreted up to a level of cutinase activity per dry cell weight (specific cell activity) of 4.1 Umg(-1) with activity per protein broth (specific activity) of 266 Umg(-1), whereas cutinase-(WP)(2) was secreted with a specific cell activity of 2.1 Umg(-1) with a specific activity of 200 Umg(-1), and cutinase-(WP)(4) with a specific cell activity of 0.7 Umg(-1) with a specific activity of 15 Umg(-1). The results indicate that the fusion of hydrophobic peptides to cutinase that changes the physical properties of the fused protein limits cutinase secretion and subsequently leads to a lower plasmid stability and lower yeast cell growth. These effects were observed under different cultivation conditions (shake flask and bioreactor) and cultivation strategies (batch culture versus fed-batch culture).     

Scale-up of recombinant cutinase recovery by whole broth extraction with PEG-phosphate aqueous two-phase

A whole broth extraction using an aqueous two-phase system (ATPS) composed by 5% (w/w) PEG 3350 and 15% (w/w) phosphate was used for the scale-up extraction and isolation of a recombinant Fusarium solani pisi cutinase, an extracellular mutant enzyme expressed in Saccharomyces cerevisiae, containing a fusion peptide (WP)₄. The experiments were carried out at three different scales (10 ml, 1 l and 30 l). Mixing time and stirrer speed were evaluated at lab scale (1 l) with two different system compositions. Stirrer speed between 400 and 800 rpm and mixing time between 2 and 5 min led to the highest recoveries of cutinase. In all cases, inclusive of pilot scale (30 l), the equilibrium was reached after a few minutes. The performance of ATPS was reproducible within the scale range of 0.010–30 l and provided a standard deviation of the yield lower than 8%, leading to (i) a partition coefficient over 50, (ii) a yield over 95% and (iii) a concentration factor over 5. The fusion of the peptide (WP)₄ to the cutinase protein enabled a 400 increase of the partition coefficient relative to the wild-type strain.     

Genetic engineering of the Fusarium solani pisi lipase cutinase for enhanced partitioning in PEG-phosphate aqueous two-phase systems

The Fusarium solani pisi lipase cutinase has been genetically engineered to investigate the influence of C-terminal peptide extensions on the partitioning of the enzyme in PEG-salt based aqueous two-phase bioseparation systems. Seven different cutinase lipase variants were constructed containing various C-terminal peptide extensions including tryptophan rich peptide tags ((WP)(2) and (WP)(4)), positively ((RP)(4)) and negatively ((DP)(4)) charged tags as well as combined tags with tryptophan together with either positively ((WPR)(4)) or negatively ((WPD)(4)) charged amino acids. The modified cutinase variants were stably produced in Escherichia coli as secreted to the periplasm from which they were efficiently purified by IgG-affinity chromatography employing an introduced N-terminal IgG-binding ZZ affinity fusion partner present in all variants. Partitioning experiments performed in a PEG 4000/sodium phosphate aqueous two-phase system showed that for variants containing either (WP)(2) or (WP)(4) peptide extensions, 10- to 70-fold increases in the partitioning to the PEG rich top-phase were obtained, when compared to the wild type enzyme. An increased partitioning was also seen for cutinase variants tagged with both tryptophans and charged amino acids, whereas the effect of solely charged peptide extensions was relatively small. In addition, when performing partitioning experiments from cell disintegrates, the (WP)(4)-tagged cutinase showed a similarly high PEG-phase partitioning, indicating that the effect from the peptide tag was unaffected by the background of the host proteins. Taken together, the results show that the partitioning of the recombinantly produced cutinase model enzyme could be significantly improved by relatively minor genetic engineering and that the effects observed for purified proteins are retained also in an authentic whole cell disintegrate system. The results presented should be of general interest also for the improvement of the partitioning properties of other industrially interesting proteins including bulk enzymes.     

Affinity purification and characterization of a cutinase from the fungal plant pathogen Monilinia fructicola (Wint.) honey

Trifluoromethyl ketones (TFK) are potent inhibitors of a variety of serine hydrolases. The TFK inhibitor, 3-(4-mercaptobutylthio)-1,1,1-trifluoro-2-propanone (MBTFP), was found to competitively inhibit cutinase activity (I50 = 9.4 x 10(-3)) from the fungal plant pathogen Monilinia fructicola and to serve as an effective affinity ligand for the purification of cutinases from culture filtrates. The TFK inhibitors, 3-n-octylthio-1,1,1-trifluoro-2-propanone (OTFP) and 3-n-pentylthio-1,1,1-trifluoro-2-propanone (PTFP), also inhibited cutinase activity with I50 values of 1.6 x 10(-6) and 2.3 x 10(-4) M, respectively. Buffer containing OTFP was the strongest eluant for cutinases of M. fructicola and provided the best purification factor and yield, although buffers containing OTFP, detergent, and salt were found to be effective for eluting cutinases bound to MBTFP-Sepharose. Buffer containing 0.5% Triton X-100 also selectively eluted cutinases from the affinity column. Two-dimensional electrophoretic analysis by SDS-PAGE and isoelectric focusing of the affinity-purified cutinase fraction indicated activity associated with proteins of pI 8.2 and molecular masses of approximately 18.6 and 20.8 kDa. These proteins hydrolyzed [3H]cutin and artificial substrates such as p-nitrophenylbutyrate and related esters, typical of other cutinases, but differ from previously characterized cutinases in molecular mass. The two low-molecular-weight proteins resolved by 2-D gel electrophoresis were subjected to in-gel digestion with Lys-C and the resulting peptide fragments were separated by Microbore-HPLC. The amino acid sequences of several internal peptide fragments had high homology with cutinase sequences from other fungi, particularly the plant pathogen Botrytis cinerea. Our study illustrates the potential of TFK ligands for the affinity purification of cutinases and indicates that the cutinases from M. fructicola have novel features warranting further study.     

Extraction of peptide tagged cutinase in detergent-based aqueous two-phase systems

Detergent-based aqueous two-phase systems have the advantage to require only one auxiliary chemical to induce phase separation above the cloud point. In a systematic study the efficiency of tryptophan-rich peptide tags was investigated to enhance the partitioning of an enzyme to the detergent-rich phase using cutinase as an example. Up to 90% enzyme activity could be extracted in a single step from whole broth of recombinant Saccharomyces cerevisiae expressing cutinase variants carrying a (WP)₄ tag. In contrast, the extraction yield of wild type cutinase was 2–3% only. The detergent concentration and the temperature are the main parameters to optimize the extraction yield. Considering availability, extraction yields, and price the detergent Agrimul NRE 1205 served best for enzyme recovery.     

Integration of the production and the purification processes of cutinase secreted by a recombinant Saccharomyces cerevisiae SU50 strain

By expanded bed adsorption (EBA) it was possible to simultaneously recover and purify the heterologous cutinase directly from the crude feedstock. However, it was observed that in a highly condensed and consequently economically advantageous purification process as EBA, the cultivation step highly influences the following purification step. Thus, the yeast cultivation and cutinase purification by EBA cannot be considered as independent entities, and the understanding of the interactions between them are crucial for the development of a highly cost effective overall cutinase production process. From the cultivation strategies studied, one batch, one continuous and two fed-batch cultivations, the strategy that resulted in a more economical cutinase overall production process was a fed-batch mode with a feeding in galactose. This last cultivation strategy, exhibited the highest culture cutinase activity and bioreactor productivity, being obtained 3.8-fold higher cutinase activity and 3.0-fold higher productivity that could compensate the 40% higher cultivation medium costs when compared with a fed-batch culture with a feeding on glucose and galactose. Moreover, a 3.8-fold higher effective cutinase dynamic adsorption capacity and 3.8-fold higher effective purification productivity were obtained in relation to the fed-batch culture with the feeding on glucose and galactose. The cultivation strategy with a feeding on galactose, that presented 5.6-fold higher effective purification productivity, could also compensate the 32% effective adsorption capacity obtained with a continuous cultivation broth. Furthermore, a 205-fold higher cutinase activity, 24-fold higher bioreactor productivity and 6% of the cultivation medium costs were obtained in relation to the continuous culture.     

Influence of tryptophan tags on the purification of cutinase, secreted by a recombinant Saccharomyces cerevisiae, using cationic expanded bed adsorption and hydrophobic interaction chromatography

During cationic bed adsorption (EBA), with cutinase with varying length tryptophan tags (WP)(2)and (WP)(4), 33% and 10% of adsorption capacity and 80% and 32% eluted specific activity were observed in relation to wild type (wt)-cutinase in the conventional process. Therefore, as the hydrophobicity of the protein increases, it is important to integrate the EBA step with a hydrophobic interaction chromatography (HIC) process. As the length of the hydrophobic tag-(WP) increases from n = 2 to n = 4, the purification factor obtained by HIC was 1.8 and 2.2-fold higher than wt-cutinase. However, the recovery yield obtained in HIC decreases substantially as the length of hydrophobic tag increases (97%, 84% and 70% for wt-cutinase, cutinase-(WP)(2) and cutinase-(WP)(4)). The integration of two purification steps, EBA followed by HIC, resulted in the highest overall purity level for cutinase-(WP)(2), and the highest overall recovery yield for wt-cutinase. When optimizing the design of a hydrophobic tag fused to a protein secreted by Saccharomyces cerevisiae it must be considered that the cultivation parameters could impair the downstream process, and consequently the optimum tag is not necessarily the one that presents the highest purification factor in HIC.     

Economic simulation of batch and continuous aqueous two-phase purification for viral products

Vaccine manufacturing strategies that lower capital and production costs could improve vaccine access by reducing the cost per dose and encouraging localized manufacturing. Continuous processing is increasingly utilized to drive lower costs in biological manufacturing by requiring fewer capital and operating resources. Aqueous two-phase systems (ATPS) are a liquid–liquid extraction technique that enables continuous processing for viral vectors. To date, no economic comparison between viral vector purifications using traditional methods and ATPS has been published. In this work, economic simulations of traditional chromatography-based virus purification were compared to ATPS-based virus purification for the same product output in both batch and continuous modes. First, the modeling strategy was validated by re-creating a viral subunit manufacturing economic simulation. Then, ATPS capital and operating costs were compared to that of a traditional chromatography purification at multiple scales. At all scales, ATPS purification required less than 10% of the capital expenditure compared to chromatography-based purification. At an 11 kg per year production scale, the ATPS production costs were 50% less than purification with chromatography. Other chromatography configurations were explored, and may provide a production cost benefit to ATPS, but the purity and recovery were not experimentally verified. Batch and continuous ATPS were similar in capital and production costs. However, manual price adjustments suggest that continuous ATPS plant-building costs could be less than half that of batch ATPS at the 11 kg per year production scale. These simulations show the significant reduction in manufacturing costs that ATPS-based purification could deliver to the vaccine industry.     

Pilot-scale extraction of an intracellular recombinant cutinase from E. coli cell homogenate using a thermoseparating aqueous two-phase system

A thermoseparating aqueous two-phase system for extraction of a recombinant cutinase fusion protein from Escherichia coli homogenate has been scaled up to pilot scale. The target protein ZZ-cutinase-(WP)(4) was produced in a fed batch process at 500 l to a concentration of 12% of the total protein and at a cell concentration of 19.7 g l(-1). After harvest and high-pressure homogenisation a first extraction step was performed in an EO(50)PO(50) (50% (w/w) ethylene oxide and 50% (w/w) propylene oxide) thermopolymer/amylopectin rich Waxy barley starch system. The (WP)(4) tag was used for enhanced target protein partitioning to the EO(50)PO(50) phase while the cell debris was collected in the starch phase. A second extraction step followed where the recovered EO(50)PO(50) phase from the first step was supplemented with a non-ionic detergent (C(12-18)EO(5)) and heated to the cloud point (CP) temperature (45 degrees C). One polymer-rich liquid phase and one almost pure aqueous phase were formed. The target protein could be obtained in a water phase after the thermal phase separation at a total recovery over the extraction steps of 71% and a purification factor of 2.5. We were able to demonstrate that a disk-stack centrifugal separator could be adapted for rapid separation of both primary and thermoseparated phase systems.     

AQUEOUS TWO-PHASE EXTRACTION FOR THE PURIFICATION OF ALKALINE AGARASES FROM CULTURE EXTRACTS OF Pseudomonas aeruginosa AG LSL-11

The agarases were purified for the first time an using aqueous two-phase system (ATPS) consisting of polyethylene glycol (PEG) and phosphate salt. The three extracellular, alkaline agarases produced by Pseudomonas aeruginosa AG LSL-11 were efficiently extracted into the top PEG-rich layer. The influencing factors on the partition of agarases—molecular weight of the PEG, system pH, system temperature, and NaCl concentration—were investigated. All the factors were found to have a significant effect on the partition of agarases except NaCl. The optimal ATPS parameters for the partitioning and purification of agarases were found to be 12% PEG 600 and 11.9% (w/w) phosphate salt at pH 8.0 and 4°C. All three agarases were concentrated in the top PEG phase with 6.19-fold purity and 71.21% recovery. The ATPS was found to be more convenient and economical than the conventional ion-exchange chromatography (IEC) method for extraction of three agarases and could be significantly employed for the purification of agarases from fermentation broth.     

Aqueous two-phase extraction for the purification of alkaline agarases from culture extracts of Pseudomonas aeruginosa AG LSL-11

The agarases were purified for the first time an using aqueous two-phase system (ATPS) consisting of polyethylene glycol (PEG) and phosphate salt. The three extracellular, alkaline agarases produced by Pseudomonas aeruginosa AG LSL-11 were efficiently extracted into the top PEG-rich layer. The influencing factors on the partition of agarases--molecular weight of the PEG, system pH, system temperature, and NaCl concentration--were investigated. All the factors were found to have a significant effect on the partition of agarases except NaCl. The optimal ATPS parameters for the partitioning and purification of agarases were found to be 12% PEG 600 and 11.9% (w/w) phosphate salt at pH 8.0 and 4°C. All three agarases were concentrated in the top PEG phase with 6.19-fold purity and 71.21% recovery. The ATPS was found to be more convenient and economical than the conventional ion-exchange chromatography (IEC) method for extraction of three agarases and could be significantly employed for the purification of agarases from fermentation broth.     

Continuous processing of fusion protein expressed as an Escherichia coli inclusion body

In this study we develop the components of an integrated process for the continuous extraction and purification of a histidine-tagged fusion protein expressed as an inclusion body in Escherichia coli. Lac21 was selected as a model peptide and was expressed as a fusion to ketosteroid isomerase. A purification strategy was developed on a 1-ml batch column before successful scale-up and transfer to a continuous purification system, having a bed volume of 240 ml. Preliminary experiments proved cleavage of the fusion protein. The use of chemical extraction and continuous chromatography gives a flowsheet far superior to the traditional methods for inclusion body processing.     

Identification and characterization of bacterial cutinase

Cutinase, which exists in both fungi and bacteria, catalyzes the cleavage of the ester bonds of cutin. Fungal cutinases have been extensively studied, however, reports on bacterial cutinases have been limited due to the lack of knowledge concerning the identity of their open reading frames. In the present study, the cutinase from Thermobifida fusca was induced by cutin and purified to homogeneity by following p-nitrophenyl butyrate hydrolyzing activity. Peptide mass fingerprinting analysis of the wild-type enzyme matched two proteins, Tfu_0883 and Tfu_0882, which are 93% identical in sequence. Both proteins were cloned and overexpressed in their mature form. Recombinant Tfu_0883 and Tfu_0882 display very similar enzymatic properties and were confirmed to be cutinases by their capability to hydrolyze the ester bonds of cutin. Comparative characterization of Fusarium solani pisi and T. fusca cutinases indicated that they have similar substrate specificity and catalytic properties except that the T. fusca enzymes are thermally more stable. Homology modeling revealed that T. fusca cutinases adopt an alpha/beta-hydrolase fold that exhibits both similarities and variations from the fungal cutinase structure. A serine hydrolase catalytic mechanism involving a Ser(170)-His(248)-Asp(216) (Tfu_0883 numbering) catalytic triad was supported by active site-directed inhibition studies and mutational analyses. This is the first report of cutinase encoding genes from bacterial sources.     

Impaired Secretion of a Hydrophobic Cutinase by Saccharomyces cerevisiae Correlates with an Increased Association with Immunoglobulin Heavy-Chain Binding Protein (BiP)

This study focuses on the different efficiencies of secretion of two fungal cutinases by Saccharomyces cerevisiae, a wild-type cutinase (CY000) and a hydrophobic mutant cutinase (CY028). Both cutinases are placed under control of the GAL7 promoter, by which the expression levels can be regulated. Wild-type cutinase was secreted at up to 25 mg per g (dry weight), while CY028 was secreted at a level of 2 mg per g (dry weight); this difference is nearly independent of the expression level. Pulse-chase experiments revealed that whereas CY000 cutinase is secreted, CY028 is irreversibly retained in the cell. Immunogold labelling followed by electron microscopy revealed colocalization of CY028 with immunoglobulin heavy-chain binding protein (BiP) in the endoplasmic reticulum (ER). The increase of wild-type cutinase expression did not result in higher levels of the molecular chaperone BiP, but BiP levels are raised by increased induction of the hydrophobic mutant cutinase. Immunoprecipitation studies showed that in contrast to the wild-type cutinase, the hydrophobic mutant cutinase interacts with BiP. These results indicate that the introduction of two exposed hydrophobic patches in cutinase results in a higher affinity for BiP which might cause the retention of this mutant cutinase in the ER.     

Biochemical characterization of the cutinases from Thermobifida fusca

Thermobifida fusca produces two cutinases which share 93% identity in amino acid sequence. In the present study, we investigated the detailed biochemical properties of T. fusca cutinases for the first time. For a better comparison between bacterial and fungal cutinases, recombinant Fusarium solani pisi cutinase was subjected to the similar analysis. The results showed that both bacterial and fungal cutinases are monomeric proteins in solution. The bacterial cutinases exhibited a broad substrate specificity against plant cutin, synthetic polyesters, insoluble triglycerides, and soluble esters. In addition, the two isoenzymes of T. fusca and the F. solani pisi cutinase are similar in substrate kinetics, the lack of interfacial activation, and metal ion requirements. However, the T. fusca cutinases showed higher stability in the presence of surfactants and organic solvents. Considering the versatile hydrolytic activity, good tolerance to surfactants, superior stability in organic solvents, and thermostability demonstrated by T. fusca cutinases, they may have promising applications in related industries.     

Potential Aqueous Two‐Phase Processes for the Primary Recovery of Colored Protein from Microbial Origin

The primary recovery of c‐phycocyanin and b‐phycoerythrin from Spirulina maxima and Porphyridium cruentum, respectively, using an established extraction strategy was selected as a practical model system to study the generic application of polyethylene glycol (PEG)‐phosphate aqueous two‐phase systems (ATPS). The generic practical implementation of ATPS extraction was evaluated for the recovery of colored proteins from microbial origin. A comparison of the influence of system parameters, such as PEG molecular mass, concentration of PEG as well as salt, system pH and volume ratio, on the partition behavior of c‐phycocyanin and b‐phycoerythrin was carried out to determine under which conditions target colored protein and contaminants concentrate to opposite phases. One‐stage processes are proposed for the primary recovery of the colored proteins. PEG1450‐phosphate ATPS extraction (volume ratio (V_R) equal to 0.3, tie‐line length (TLL) of 34 % w/w and system pH 7.0) for the recovery of c‐phycocyanin from Spirulina maxima resulted in a primary recovery process that produced a protein purity of 2.1 ± 0.2 (defined as the relationship of 620 nm to 280 nm absorbance) and a product yield of 98 % [w/w]. PEG1000‐phosphate ATPS extraction (i.e., V_R = 1.0, PEG 1000, TLL 50 % w/w and system pH 7.0) was preferred for the recovery of b‐phycoerythrin from Porphyridium cruentum, which resulted in a protein purity of 2.8 ± 0.2 (defined as the relationship of 545 nm to 280 nm absorbance) and a product yield of 82 % [w/w]. The purity of c‐phycocyanin and b‐phycoerythrin from the crude extract increased 3‐ and 4‐fold, respectively, after ATPS. The results reported herein demonstrated the benefits of the practical generic application of ATPS for the primary recovery of colored proteins from microbial origin as a first step for the development of purification processes.     

Purification and Characterization of Polyphenol Oxidase From Waste Potato Peel by Aqueous Two-Phase Extraction

Potato peel from food industrial waste is a good source of polyphenol oxidase (PPO). This work illustrates the application of an aqueous two-phase system (ATPS) for the extraction and purification of PPO from potato peel. ATPS was composed of polyethylene glycol (PEG) and potassium phosphate buffer. Effect of different process parameters, namely, PEG, potassium phosphate buffer, NaCl concentration, and pH of the system, on partition coefficient, purification factor, and yield of PPO enzyme were evaluated. Response surface methodology (RSM) was utilized as a statistical tool for the optimization of ATPS. Optimized experimental conditions were found to be PEG1500 17.62% (w/w), potassium phosphate buffer 15.11% (w/w), and NaCl 2.08 mM at pH 7. At optimized condition, maximum partition coefficient, purification factor, and yield were found to be 3.7, 4.5, and 77.8%, respectively. After partial purification of PPO from ATPS, further purification was done by gel chromatography where its purity was increased up to 12.6-fold. The purified PPO enzyme was characterized by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE), followed by K_m value 3.3 mM, and V_max value 3333 U/mL, and enzyme stable ranges for temperature and pH of PPO were determined. These results revealed that ATPS would be an attractive option for obtaining purified PPO from waste potato peel.     

Direct product sequestration of a recombinant cutinase from batch fermentations of Saccharomyces cerevisiae

The recovery of cutinase of Fusarium solani pisi produced by the yeast Saccharomyces cerevisiae was studied in a fluidised bed adsorption system directly integrated with a productive fermenter (so-called direct product sequestration; DPS). The relative efficiency of this system was compared with the one of a conventional purification process by discrete sequences of fermentation, broth clarification, ultrafiltration and fixed bed anion exchange chromatography. By direct product sequestration of the extracellular heterologous cutinase it was possible, through only one unit operation: (i) to perform broth clarification, (ii) to obtain a high cutinase concentration factor, and (iii) to recover cutinase with a specific activity that equalled that obtained with the conventional purification process. It was also possible (iv) to substantially reduce the total process time, (v) to improve the overall yield, and (vi) to increase cutinase productivity. Furthermore, the procedure outlined is suitable for large scale bioprocess exploitation.     

Design of ionic liquids for lipase purification

Aqueous two-phase systems (ATPS) are considered as efficient downstream processing techniques in the production and purification of enzymes, since they can be considered harmless to biomolecules due to their high water content and due to the possibility of maintaining a neutral pH value in the medium. A recent type of alternative ATPS is based on hydrophilic ionic liquids (ILs) and salting-out inducing salts. The aim of this work was to study the lipase (Candida antarctica lipase B - CaLB) partitioning in several ATPS composed of ionic liquids (ILs) and inorganic salts, and to identify the best IL for the enzyme purification. For that purpose a wide range of IL cations and anions, and some of their combinations were studied. For each system the enzyme partitioning between the two phases was measured and the purification factors and enzyme recoveries were determined. The results indicate that the lipase maximum purification and recovery were obtained for cations with a C(8) side alkyl chain, the [N(CN)(2)] anion and ILs belonging to the pyridinium family. However, the highest purification parameters were observed for 1-methyl-3-octylimidazolium chloride [C(8)mim]Cl, suggesting that the IL extraction capability does not result from a cumulative character of the individual characteristics of ILs. The results indicate that the IL based ATPS have an improved performance in the lipase purification and recovery.     

High-level expression and characterization of Fusarium solani cutinase in Pichia pastoris

High-level extracellular production of Fusarium solani cutinase was achieved using a Pichia pastoris expression system. The cutinase-encoding gene was cloned into pPICZαA with the Saccharomyces cerevisiae α-factor signal sequence and methanol-inducible alcohol oxidase promoter by two different ways. The additional sequences of the c-myc epitope and (His)₆-tag of the vector were fused to the C-terminus of cutinase, while the other expression vector was constructed without any additional sequence. P. pastoris expressing the non-tagged cutinase exhibited about two- and threefold higher values of protein amount and cutinase activity in the culture supernatant, respectively. After simple purification by diafiltration process, both cutinases were much the same in the specific activity and the biochemical properties such as the substrate specificity and the effects of temperature and pH. In conclusion, the high-level secretion of F. solani cutinase in P. pastoris was demonstrated for the first time and would be a promising alternative to many expression systems previously used for the large-scale production of F. solani cutinase in Saccharomyces cerevisiae as well as Escherichia coli.