Electronic Journal of Polish Agricultural Universities (EJPAU) founded by all Polish Agriculture Universities presents original papers and review articles relevant to all aspects of agricultural sciences. It is target for persons working both in science and industry,regulatory agencies or teaching in agricultural sector. Covered by IFIS Publishing (Food Science and Technology Abstracts), ELSEVIER Science - Food Science and Technology Program, CAS USA (Chemical Abstracts), CABI Publishing UK and ALPSP (Association of Learned and Professional Society Publisher - full membership). Presented in the Master List of Thomson ISI.
2015
Volume 18
Issue 4
Topic:
Biotechnology
ELECTRONIC
JOURNAL OF
POLISH
AGRICULTURAL
UNIVERSITIES
Piegza M. , Jurkiewicz M. , Kancelista A. , £aba W. , Witkowska D. 2015. MOULDS LYTIC ENZYMES IN THE PRODUCTION OF YARROWIA HIGH-PROTEIN FEED ADDITIVES, EJPAU 18(4), #04.
Available Online: http://www.ejpau.media.pl/volume18/issue4/art-04.html

MOULDS LYTIC ENZYMES IN THE PRODUCTION OF YARROWIA HIGH-PROTEIN FEED ADDITIVES

Micha³ Piegza, Marcin Jurkiewicz, Anna Kancelista, Wojciech £aba, Danuta Witkowska
Department of Biotechnology and Food Microbiology, Wroc³aw University of Environmental and Life Sciences, Poland

 

ABSTRACT

The optimal conditions for the degradation of the cell wall of Yarrowia lipolytica yeast, leading to the release of intracellular proteins by hydrolases of Trichoderma and Aspergillus moulds, were determinated. Hydrolysis of Y. lipolytica yeast biomass was performed with the use of various amounts of concentrated or non-concentrated enzymes, as well as yeast biomass subjected or not subjected to thermal inactivation. The analysis of enzymatic hydrolysis process demonstrated that the most effective was the 8-hour hydrolysis of thermally not inactivated Y. lipolytica yeast biomass with 6-fold concentrated enzymatic preparation, which resulted in the release of 127.86 mg of intracellular proteins per 1 g dry biomass.

Key words: chitinases, SCP, Trichoderma, Aspergillus, laminarinases.

INTRODUCTION

The search for cheap and efficient protein sources has been one of the most important issues in the field of animal husbandry. In order to solve this problem, biotechnology has offered a good source of SCP (single cell protein) such as the biomass of yeast and enzymes, to additionally increase the accessibility of protein contained in yeast cells.

Trichoderma spp. are filamentous fungi living in the soil and within the ecosystem of roots. They constitute the largest group of moulds isolated from soils of most climatic zones, where their count reaches 101–103 colony forming units per gram. It has been proven that some strains are capable of long-term colonization of the surface of plants roots and the epidermis of roots to a depth of several layers of cells, which is referred to as "rhizosphere competence". It is the ability to colonize the roots of plants and to grow on their surface [6, 7, 13].

These moulds produce a wide range of compounds, induce plant resistance to pathogens and directly participate in their active growth control. This process – referred to as biocontrol – prevents plant diseases and promotes their growth and development. A number of mechanisms are responsible for this [5, 8, 11]. It was noted, however, that mycoparasitism which is one of the most important and best-known bio-control mechanisms is based on the ability to degrade the components of pathogen cell wall with the use of the enzymes produced by Trichoderma [7].

The enzymes produced by the fungi, which also degrade polysaccharide cell wall components and belong to the group of cell wall degrading enzymes (CWDE), including: chitinases, β-glucanases and β-glycosidases, are involved in the process of mycoparasitism [12, 17, 23]. It is considered that the most important among them are β-1,3-glucanases due to wide spreading of β-1,3-glucan in cell walls of moulds against which these proteins show their enzymatic activity [15]. An important role is also played by chitinases and β-1,6-glucanases, although chitin and β-1,6-glucan represent a small percentage of the components of the cell wall of moulds [4, 16].

Because of the fact that the enzymes biosynthesized by the Trichoderma exhibit activity towards polysaccharides – present in fungal cells – an attempt was made to use these enzymes to degrade specific components of yeast cell wall, bearing in mind the similarity in the construction of their walls. In yeast cells, two layers which constitute the cell wall are built with only four classes of macromolecules linked with covalent bonds: chitin, β-1,3-glucan, β-1,6-glucan and cell wall proteins [10]. However, with the use of yeast biomass as a potential high-protein feed additive, those components of yeast cell wall polysaccharide, which are hard to digest by animals, can significantly reduce the availability of intracellular proteins. Hence hydrolases produced by moulds can be successfully used for yeast cell wall degradation due to the presence of components, constituting substrates to these enzymes, and therefore contribute to the release of intracellular proteins.

The purpose of this research was to determine optimal conditions for the degradation of the cell wall of Y. lipolytica yeast [14] , leading to the release of intracellular proteins, with hydrolases of Trichoderma mouldsselected in terms of effective lytic properties.

MATERIALS AND METHODS

Microorganisms
Five strains of moulds: Aspergillus cervinus 219; Aspergillus niger XP; Trichoderma citrinoviride C1; Trichoderma hamatum T2; Trichoderma harzianum T33, that originated from the collection of the Department of Biotechnology and Food Microbiology at the Wrocław University of Environmental and Life Sciences, as well as biomass of Yarrowia lipolytica 8665 UV1 yeast (from the American Type Culture Collection), whose cell wall biopolymers constitute a source of carbon and energy and induce lytic enzymes, were used in the study.

Strains were kept on agar slants at a temperature of + 4°C.

Media
Mould strains were stored on PDA culture medium, whereas the yeast strain on YM agar medium. For selection of mould strains and production of enzymatic preparation, a modified Saunders mineral medium (g/ml) was used KH2PO4 (0.20); K2HPO4 (0.15); NaH2PO4 · H2O (2); Na2HPO4 (1.50); NH4NO3 (0.60); NaNO3 (3); MgSO4 · 7H2O (0.30) enriched with dried biomass of Y.lipolytica yeast (20, 30, 40, 50, 60) and wheat germs (source of biologically-active substances) in the amount of 10 g/ml.

To obtain spores of filamentous fungi the PDB medium (12 g/ml) with glucose (10 g/ml) was applied.

The medium for the production of yeast biomass contained [g/ml]: bactopeptone (0.75); yeast extract YE (1); glycerin fraction (40); (NH4)2SO4 (10); KH2PO4 (0.125); MgSO4 · 7H2O (0.5). Media were sterilized in an autoclave (120°C, 20 min).

Cultures of microorganisms

Selection of effective strain and proper composition of culture medium
The five mold strains were cultivated in 250-mL Erlenmeyer flasks. The medium consisted of: mineral Saunders medium (50 mL) with 1% m/v addition of wheat germs and 1, 2, 3, 4, 5 or 6% addition of Y. lipolytica 8665 UV1 dried biomass (inducer of lytic enzymes biosynthesis and carbon source). The cultures were inoculated with 0.5 mL of a suspension of microorganisms with a density of 108 cells/mL obtained from slant with 0.1% Tween 80 solution. A suspension of cells of a certain density was achieved with the use of Thoma chamber.

The culturing process was conducted in a rotary shaker (170 rpm) at a temperature of 25–28°C for 7 days. During that process, pH value was maintained at 5.5 with a sterile solution of 1 M NaOH and 1 M HCl. After 3, 5 and 7 days of culture, the samples were collected under sterile conditions (0.5 mL) for enzymatic activity assay.

The selection of effective strain was performed on the basis of the evaluation of enzymatic activity of chitinases and laminarinases in supernatants obtained after centrifugation (centrifugation with cooling (4°C), 5450 g, 15 min).

Production of enzymatic preparation with a selected strain was conducted as described above, but in larger flasks (500 mL) and with inducer concentration determined in the above experiments. Cultures were continued until the maximum enzymatic activity was achieved in supernatants.

The crude enzymatic preparation was obtained after centrifugation of solids from the liquid medium (centrifugation with cooling, 5450 g, 15 min).

Culture of Y. lipolytica yeast to produce biomass
The culture was carried out in a 3.5-L AK-3 bioreactor with a working volume of 1.1 L (after its inoculation with 30% inoculum from the shaking culture) at 30°C at stirring speed of 550 rpm and aeration rate of 1 vvm until all nutrients had been consumed. During that process, the pH value was maintained at 3.5–4.0 via automatic control with 20% NaOH solution. Once the process had been completed, the culture was centrifuged for 25 minutes at 5450 g.

Dry matter of yeast biomass was measured after it had been washed three times with sterile, distilled water and centrifuged (5450 g, 25 min) with a WPS moisture analyzer 110S by Radwag company.

Concentration of the enzymatic preparation
From the liquid obtained in the process of culturing a selected strain of moulds, as a result of solid matter centrifugation (with cooling, 5450g, 15 min.), a crude enzymatic preparation was obtained, which was concentrated afterwards.

The process of concentration was carried out with the use of TFF Labscale ultrafiltration system with Millipore Pellicon membrane containing polyether sulphate (Pellicon XL) with MWCO of 30 kDa.

As a result of that process the following two fractions were obtained: concentrated liquid containing protein with a molecular weight over 30 kDa, and permeate containing protein with a molecular weight lower than 30 kDa.

Each of the fractions was analyzed for the activity of chitinases and laminarinases, as well as for the content of proteins.

Determination of the optimal temperature of lytic enzymes
In order to determine the optimal temperature of enzymes activity in the concentrated enzymatic preparation, the enzymatic activity of chitinases and laminarinases were determined at temperatures of: 25, 30, 35, 40, 45, 50, 55 and 60°C

Process of hydrolysis of cell walls in the biomass of Y. lipolytica yeast with the use of enzymatic preparation.
Enzymatic hydrolysis process was conducted in 2-mL Eppendorf’s test tubes. To 0.2 g (0.039 g d. m.) of wet biomass of Y. lipolytica yeast (both thermally inactivated at 120°C or non-inactivated), various amounts of the enzymatic preparation were added: 0, 0.2, 0.4, 0.6, 0.8 or 1 mL of solution, and completed with acetate buffer (0.05 M, pH 4.8) to 1 mL.

The reaction was carried out in a TS-100 Thermo-Shaker by Biosan company (at temperatures optimal for the lytic enzymes, 1000 rpm) for 1, 4, 8 and 12 hours. The reaction was stopped by centrifugation (10 920 g, 10 min). The quantity of released protein was determined in the supernatant.

Determination of enzymatic activity
The activity of β-1,3-glucanase (laminarinases) and chitinases was determined according to Witkowska and Maj [22], using substrates: laminarin, and chitin respectively, by running the enzymatic reaction at 50°C, pH 5.0 and for 30 min. Reaction products, i.e. glucose in the case of β-1,3-glucanase and glucosamine in the case of chitinases were determined colorimetrically using dinitrosalicylic acid (Sigma). Activities of the analyzed enzymes were expressed as nKat/mL.

Determination of protein content in enzymatic hydrolysates by Bradford method [1].
The obtained complex of proteins with Coomassie Brilliant Blue G-250 was determined by spectrophotometry at a wavelength of λ = 595 nm. A mixture of 0.02 mL of the sample with 1 mL of the diluted Bradford reagent was intensively mixed for 10 min at room temperature. Then absorbance was measured at λ = 595 nm.

Statistical analysis. Statistical analysis was performed to support outcoming conclusions, nevertheless no relevant information has been acquired.

RESULTS AND DISCUSSION

In order to obtain enzyme preparation which would include active laminarinases and chitinases, necessary for the degradation of cell walls of yeast, potential bio-synthesizers of these enzymes – Trichoderma and Aspergillus strains – were cultivated in this study.

The ability of T. citrinoviride C1, T. hamatum T2, T. harzianum, T33, A. cervinus 219 and A. niger XP to produce lytic enzymes, such as chitinases and laminarinases, was shown in shaking cultures in the presence of yeast biomass as a carbon source and anr of the biosynthesis of enzymes. While analyzing the individual cultures of moulds, differences were observed in the levels of the activity of the tested enzymes depending on both the amount of added yeast biomass and incubation time (Fig. 1 and 2).

Fig. 1. Dynamics of laminarinases biosynthesis by filamentous strains tested depending on Yarrowia lipolytica biomass addition to the culture

Fig. 2. Dynamics of the chitinases biosynthesis by filamentous strains tested depending on Yarrowia lipolytica biomass addition to the culture

In general, all tested strains showed greater ability to synthesize laminarinases than chitinases, with activities of 6.32–13.22 nKat/mL and 0.14–1.38 nKat/mL (maximum values for a given strain), respectively.

Trichoderma citrinoviride C1 turned out to be effective in the biosynthesis of both laminarinases as well as chitinases in cultures with 4% addition of yeast biomass laminarinase activity was 12.57 nKat/mL at day 3 and chitinase activity 1.39 nKat/mL atas day 5 of the culture. The remaining tested strains showed the maximum activity at a similar (e.g. laminarinases, T33) or significantly poorer level compared to the C1 strain. In the case of the C1strain, it was observed that the secretion of extracellular laminarinases (in nKat/mL) was approximately at the same level (12.34–13.23–12.57–12.47 nKat/mL) in all cultures, with different levels (2%–3%–4%–5%) of yeast biomass used as carbon add the.

In the case of Aspergillus strains, the maximum secretion of laminarinases was reported in the cultures with 2 or 3% addition of yeast biomass, mostly on day 7 of culture, whereas in the case of Trichoderma strains – in cultures with 4 or 6% yeast biomass addition, and in most cases on day 7 of the culture (Fig. 1).

Concerning chitinases, (as judged by the maximum values obtained in cultures), strain C1 produced chitinase activity at 1.5 to 5 times higher level than the other tested strains of Trichoderma and at 3 to 10 times higher level in comparison to the strains of Aspergillus (Fig. 2). In the majority of tested strains, the maximum activity of chitinases was measured in the 3–5 day of incubation, i.e. slightly earlier than in the case of laminarinases (7 day).

In the presented study, the hydrolysis process of cell walls of Y. lipolytica yeast with crude C1 preparation (C1 supernatant) was shown, which was characterized by the highest activity of laminarinases and chitinases among the tested strains.

The culture supernatant was subjected to the process of ultrafiltration– with the use of membrane stopping particles with a molecular weight of > 30 kDa and allowing particles with < 30 kDa – for its concentration and partial purification from ballast proteins. As a result, a 6-time greater liquid density was obtained. The fraction > 30 kDa was referred to as concentrated preparation C1 (Fig. 3).

Fig. 3. Protein separation in the ultrafiltration process of C1 post-culture liquid

In the < 30 kDa fraction chitinase activity was not observed whereas laminarinase activity was low (2.5% compared to the activity in the fraction > 30 kDa). Both activities were found in the fraction of > 30 kDa, which proves that the analyzed enzymatic proteins are molecules with molecular weight over 30 kDa.

Thus, as a result of the 6-fold concentration of supernatant with the ultrafiltration method (with the use of MWCO membrane = 30kDa), 5 times higher degree of purification of chitinases was achieved, as well as nearly 11 times higher degree of laminarinases purification (Tab. 1, Fig. 3).

Table 1. Specific activity and purification level of chitinases and laminarinases of C1 culture and concentrated preparation
Activityand purification
chitinases
laminarinases
in culture
concentrated
in culture
concentrated
Specific activity [nKat/mg protein]
0.10
0.50
1.50
16.48
Purification level
1
5
1
11

A research by El-Katatny et al. [2, 3] showed that the preparation produced upon ultrafiltration (MWCO = 30 kDa) of supernatant from the culture of T. harzianum Rifai T24 strain allowed 25% inhibition of growth of S. rolfsii phytopathogen (even in 10 x dilution). While concentrating the liquid with the use of MWCO 10kDa membrane, a very weak inhibition effect had been observed, which indicated the presence of a lytic enzyme solely in the MWCO = 30 kDa fraction, which was also confirmed in the presented research.

In regard to the application of enzyme preparation in degradation of cell walls of phytopathogens, the optimum temperatures for laminarinases and chitinases were determined in the analyzed preparation. Within the tested range of temperatures 25–60°C, the optimum temperature was at 40°C for chitinases and at 50°C for laminarinases (Fig. 4 and 5).

Fig. 4. Activity of laminarinases in condensed preparation at different temperatures

Fig. 5. Activity of chitinases in condensed C1 preparation at different temperatures

Similar results were obtained by El-Katatny et al. [3] who examined the contribution of T. harzianum Rifai T24 strain in eradication of S. rolfsii phytopathogen by enzymatic degradation of cell walls, where maximum chitinase activity of 0.05 JCh was achieved at 40°C and that of laminarinase reaching 11.2 JL at 50–60°C. In turn, in studies conducted by Kapata and Panda [9] the best results of the maximum activity (0.96 JCh) of chitinases biosynthesized by T. harzianum NCIM 1185 strains was obtained upon the enzymatic reaction at a much lower temperature, i.e. 23°C.

The enzymatic hydrolysis of thermally inactivated and not inactivated Yarrowia lipolytica yeast biomass was conducted with C1 enzymatic preparation. The effect of the thermal inactivation on the hydrolysis was evaluated based on the quantity of proteins released from cells determined with Bradford method (Fig. 6).

Fig. 6. Quantity of released protein per 1 g of dry matter of yeast, with or without thermal inactivation, depending on the concentration of C1 preparation used and time of hydrolysis process

The results obtained indicate that apart from increasing quantities of enzymes (0.2–1 ml) in enzymatic reaction, a better effect of protein release from Y. lipolytica yeast biomass was observed, especially in case of thermally not inactivated biomass. After 4 hours of enzymatic reaction, 111.86 mg of protein were released per 1 g d. m. yeast with 1 mL of the preparation having the activity of 110 nKat/mL (Fig. 6). However, in the case of thermally inactivated yeast biomass used in the process of hydrolysis with the highest concentration of the same specimen, only 96.4 mg of protein per 1 g d. m. were obtained after 4 hours hydrolysis.

Few published papers deal with the application of lytic enzymes in the release of intracellular proteins. These include the research by Revah-Moiseeva and Carrod [19], where attempts were made to use chitinases for the utilization of chitinous waste and cellulose bioconversion to obtain microbial proteins (SCP-single cell protein). According to these authors, chitinase enzymes obtained in Serratia marcescens culture were used for hydrolysis of chitin and biomass of Pichia kudriavzevii yeast which was the source of SCP. In this case, protein release reached 45%.

Other sources [21], indicate that in order to obtain the SCP with the use of chitinases, the following types of yeast and moulds could also be used: Hansenula polymorpha, Myrothecium verrucaria, Candida tropicalis and Saccharomyces cerevisiae. Vyas (1991) [20, 21] used in their research M. verrucaria chitinases for chitin degradation and for obtaining SCP from S. cerevisiae biomass and achieved satisfactory results at 61% of free protein. This is due to a high activity of N-acetylglucosaminidases, which was demonstrated by a significantly high level of N-acetylglucosamine determined in the culture medium.

Most of the published papers, concerning Trichoderma spp. moulds and enzymes bio-synthesized by them, mainly focus on their involvement in the mycoparasite process. Numerous studies concentrated on the use of these enzymes in yeast cell protoplastization.

Xiao and Morell [25] have studied the use of Trichoderma harzianum enzymes in the protoplast formation of the germinative Ophiostoma picea cells, causing major timber defect – wood discoloration. Witkowska et al. [23, 24] used enzymes of Trichoderma reesei M7-1 in the Y. lipolytica and Schwaniomyces occidentalis yeast protoplast formation andachieved satisfactory results in the process. Another example of the application of lytic enzymes of moulds is described by Rattanakita et al. [18] use of chitinases biosynthesized by Aspergillus sp. S1-13 strain for waste disposal in the form of chitinous shells of shrimps. Chitin-lytic activity of this strain was observed only in the solid-state culture of waste received after shellfish processing. After selecting the optimum composition of the substrate and parameters, chitinases activity increased 3.5-fold. Studies have enabled selecting the effective strain for degradation of waste from shrimp and their processing into chitin.

Studies on the release of intracellular proteins from yeast biomass using enzymatic preparation obtained after the fungus culture are innovative and are to be continued, because there is still a lot of issues that need to be elucidated, and this process deserves special mention, since it affords the possibility of obtaining high-protein and easily-digestible feed additive at low cost, without the use of chemical reagents detrimental to the natural environment.

CONCLUSION

Of the five tested microorganisms, the strain of T. citrinoviride C1 turned out to possess the best lytic properties against cell was biomass of Y. lipolytica yeast. The most favorable conditions for the cultivation of T. citrinoviride C1 strain included 5-day culture with 4% addition of Y. lipolytica yeast biomass as a carbon source. Enzymatic hydrolysis of Y. lipolytica yeast biomass to thermal inactivation gave better results – in the form of intracellular protein – than hydrolysis of heat-inactivated biomass.

REFERENCES

  1. Bradford M.M., 1976. A rapid and sensitive method for the quantitation of microgram quantities of protein utilizing the principle of protein-dye binding. Analytical Biochemistry, 72, 248–254.
  2. El-Katatny M.H., Somitsch W., Robra K.H., El-Katatny M.S., Gübitz G.M., 2000. Production of chitinase and β-1,3-glucanase by Trichoderma harzianum for control of the phytopathogenic fungus Sclerotium rolfsii. Food Technology and Biotechnology, 38, 173–180.
  3. El-Katatny M.H., Gudelj M., Robra K.H., Elnaghy M.A., Gübitz G.M., 2001. Characterization of a chitinase and an endo-β-1,3-glucanase from Trichoderma harzianum Rifai T24 involved in control of the phytopathogen Sclerotium rolfsii. Applied Microbiology and Biotechnology, 56, 137–143.
  4. Fontaine T., Simenel C., Dubreucq G., Adam O., Delepierre M., Lemoine J., Vorgias C.E, Diaquin M., Latge J.P., 2000. Molecular organization of the alkali-insoluble fraction of Aspergillus fumigatus cell wall. Journal of Biological Chemistry, 275, 27594–27607.
  5. Hanson L.E., Howell C.R., 2004. Elicitors of plant defense responses from biocontrol strains of Trichoderma virens. Phytopathology, 94, 171–176.
  6. Harman G.E., 2000. Myths and dogmas of biocontrol. Changes in perceptions derived from research on Trichoderma harzianum T22. Plant Disease, 84, 377–393.
  7. Harman G.E., Howell C.R., Viterbo A., Chet I., Lorito M., 2004. Trichoderma species: opportunistic, avirulent, plant symbionts. Nature Reviews Microbiology, 2, 43–56.
  8. Howell C.R., 2002. Cotton seedling preemergence damping–off incited by Rhizopus oryzae and Pythium spp. and its biological control with Trichoderma spp. Phytopathology, 92, 177–180.
  9. Kapat A., Panda T., 1997. pH and thermal stability studies of chitinase from Trichoderma harzianum: a thermodynamic consideration. Bioprocess Engineering, 16, 269–272.
  10. Kapteyn J.C., Van den Ende H., Klis F.M., 1999. The contribution of cell wall proteins to the organization of the yeast cell wall. Biochimica et Biophysica Acta, 1426, 373–383.
  11. Kubicek C.P., Mach R.L., Peterbauer C.K., Lorito M., 2001. Trichoderma: from genes to biocontrol. Journal of Plant Pathology, 83, 11–23.
  12. Markovich N.A., Kononova G.L., 2003. Lytic enzymes of Trichoderma and their role in plant defense from fungal diseases: a review. Applied Biochemistry and Microbiology, 39, 341–351.
  13. Metcalf D.A., Wilson C.R., 2001. The process of antagonism of Sclerotium cepivorum in white rot affected onion roots by Trichoderma koningii. Plant Pathology, 50, 249–257.
  14. Michalik B., Biel W., Lubowicki R., Jacyno E., 2014. Chemical composition and biological value of proteins of the yeast Yarrowia lipolytica growing on industrial glycerol. Canadian Journal of Animal Science, 94, 99–104. doi:10.4141/CJAS2013-052
  15. Noronha E.F., Kipnis A., Junqueira-Kipnis A.P., Ulhoa C.J., 2000. Regulation of 36-kDa β-1,3-glucanase synthesis in Trichoderma harzianum. FEMS Microbiology Letters, 188, 19–22.
  16. Patil R.S., Ghormade V., Desphande M.V., 2000. Chitinolytic enzymes: an exploration. Enzyme and Microbial Technology, 26, 473–483.
  17. Piegza M., Szlączka K., Łaba W., Witkowska D., 2014. Effect of carbon source on the production of lytic enzymes by filamentous fungi of the Trichoderma genus. EJPAU, 17(2), 06.
  18. Rattanakit N., Plikomol A., Yano S., Wakayama M., Tachiki T., 2002. Utilization of shrimp shellfish waste as a substrate for solid-state cultivation of Aspergillus sp. S 1–13: Evaluation of a culture based on chitinase formation which is necessary for chitin–assimilation. Journal of Bioscience and Bioengineering, 93, 550–556.
  19. Revah-Moiseev S., Carroad P.A., 1981. Conversion of the enzymatic hydrolysate of shellfish waste chitin to single-cell protein. Biotechnology & Bioengineering, 23, 1067–1078.
  20. Vyas P.R., 1991. Studies on chitinolytic enzymes. Pune. University of Pune. Ph. D. thesis.
  21. Vyas P.R., Deshpande M.V., 1991. Enzymatic hydrolysis of chitin by Myrothecium verrucaria chitinase complex and its utilization to produce SCP. The Journal of General and Applied Microbiology, 37, 267–275.
  22. Witkowska D., Maj A., 2002. Production of lytic enzymes by Trichoderma sp. and their effect on the growth of phytopathogenic fungi. Folia Microbiologica, 47, 279–282.
  23. Witkowska D., Stempniewicz R., Maj A., 1999. Lytic enzymes from Trichoderma and their utilization of yeast protoplast formation. Polish Journal of Food and Nutrition Sciences, 49, 245–252.
  24. Witkowska D., Stempniewicz R., Wojtatowicz M., 1997. Production of lytic enzymes using Trichoderma reesei M7-1 in yeast protoplast formation. Polish Journal of Food and Nutrition Sciences, 6, 51–60.
  25. Xiao Y., Morrell J.J., 2004. Production of protoplasts from cultures of Ophiostoma picea. Journal of Wood Science, 50, 445–449.

Accepted for print: 13.10.2015


Micha³ Piegza
Department of Biotechnology and Food Microbiology,
Wroc³aw University of Environmental and Life Sciences, Poland
Che³mońskiego 37/41
51-630 Wroc³aw
Poland
email: mikey@wnoz.ar.wroc.pl

Marcin Jurkiewicz
Department of Biotechnology and Food Microbiology,
Wroc³aw University of Environmental and Life Sciences, Poland
Che³mońskiego 37/41
51-630 Wroc³aw
Poland

Anna Kancelista
Department of Biotechnology and Food Microbiology,
Wroc³aw University of Environmental and Life Sciences, Poland
Che³mońskiego 37/41
51-630 Wroc³aw
Poland

Wojciech £aba
Department of Biotechnology and Food Microbiology,
Wroc³aw University of Environmental and Life Sciences, Poland
Che³mońskiego 37/41
51-630 Wroc³aw
Poland

Danuta Witkowska
Department of Biotechnology and Food Microbiology,
Wroc³aw University of Environmental and Life Sciences, Poland
Che³mońskiego 37/41
51-630 Wroc³aw
Poland
email: wit@ozi.ar.wroc.pl

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