SciELO - Scientific Electronic Library Online

vol.19 número5Buffering action of acetate on hydrogen production by Ethanoligenens harbinense B49 índice de autoresíndice de assuntospesquisa de artigos
Home Pagelista alfabética de periódicos  

Serviços Personalizados




Links relacionados

  • Em processo de indexaçãoCitado por Google
  • Não possue artigos similaresSimilares em SciELO
  • Em processo de indexaçãoSimilares em Google


Electronic Journal of Biotechnology

versão On-line ISSN 0717-3458

Electron. J. Biotechnol. vol.19 no.5 Valparaíso set. 2016 


Possibility of using apple pomaces in the process of propionic-acetic fermentation


Kamil Piwowarek*, Edyta Lipińska, Elżbieta Hać-Szymańczuk

Department of Biotechnology, Microbiology and Food Evaluation, Department of Biotechnology and Food Microbiology, Faculty of Food Technology, Warsaw University of Life Science, Nowoursynowska 159c Street, 02-776 Warsaw, Poland


Background: In 2014, apple production in EU countries amounted to 11.8 million tonnes. A constant increase in the production of these fruits will lead to the accumulation of thousands of tonnes of apple pomace (production waste). The amount of industrial apples is the highest — their proportiononthe market is estimated at 50-60%, of which over 95% is processed into juice. The proportion of pomace in the traditional pressing method accounts for 20% offruits used.

Results: Analysis of the growth dynamics of wild strain Propionibacterium freudenreichii T82 in micro-cultures using different carbon sources showed that the highest bacterial growth occurs in an environment with fructose and the most intense biosynthesis of metabolites was found in medium containing only saccharose. It has been found that P. freudenreichii T82 used apple pomaces as a source of carbon. Propionic acid biosynthesis reached its maximum value in the 120th hour of cultivation (1.771 g/L). At this time, the content of the acetic acid produced reached the level of 7.049 g/L.

Conclusions: Utilization of by-products is a significant challenge for manufacturing sites and the natural environment. The solution to this problem may involve the use of pomace as a medium component for microorganism cultivation, which is a source of industrially useful metabolites. This study examined the possibility of using apple pomace as a carbon source in the process of propionic-acetic fermentation via wild strain Propionibacterium freudenreichii T82 bacteria.

Keywords: Acetic acid, By-products, Carbon sources, Propionibacterium, Propionic acid, Waste materials.


1. Introduction

In terms of environmental occurrence, bacteria of Propionibacterium genus can be classified into two groups: cutaneous (acnes) and classical (dairy). The first group includes species found on human skin, mucous membranes of the oral cavity and the digestive tract: Propionibacterium acnes, Propionibacterium avidum, Propionibacterium propionicum, Propionibacterium granulosum, and Propionibacterium lymphophilum. The second group incorporates species of industrial use — propionic acid bacteria (PAB). This group is composed of Propionibacterium freudenreichii, Propionibacterium thoenii, Propionibacterium jensenii, and Propionibacterium acidipropionici. They are found, among others, on herbaceous plants, in soil, cattle rumen, feces of ruminants, cheese, dairy products and products of natural fermentation (silage).

The Propionibacterium spp. belongs to the group of microorganisms characterized by high cultivation requirements. In addition to basic compounds essential for growth (carbon source), this bacterium needs supplementation with specific stimulating substances: trace elements (iron, magnesium, cobalt, manganese, copper), vitamin B7, vitamin B5, or -cysteine hydrochloride. Propionic bacteria have been used in the production of cheese, silage food and silage feeding, and they are also used as probiotics in animal nutrition. An important characteristic of these organisms is their ability for metabolite biosynthesis, mainly propionic acid (a preservative of food and feed, raw material for production of plastics, herbicides and perfumes), acetic acid and vitamin B12. They exhibit the highest metabolic activity under anaerobic conditions, and are also classified as facultative anaerobes.

Currently, propionic acid synthesis only occurs through expensive petrochemical processes. In this respect, there is increasing interest in the production of this metabolite using microorganisms and cheap waste materials.P. freudenreichii, which has been awarded GRAS (Generally Regarded As Safe) status by the US FDA (Food and Drug Administration), is the most useful of these bacteria in the biosynthesis of propionic acid on an industrial scale.

Utilization of by-products of technological processes is one of the important problems for production sites and the natural environment. Therefore, appropriate waste management brings many advantages, among which one can include: reduction in the costs of cleaning and export, increasing levels of hygiene and acquisition of new products. For this reason, there is the constant search for innovative solutions for industrial waste management, e.g. via biotechnological approaches. Waste materials include, among others, by-products from the fruit juice factory — apple pomace. This is a source of many biologically active compounds: saccharides (glucose, fructose, saccharose), proteins, pectins, fiber, vitamins, and organic acids. Therefore, they should be treated as raw materials for further utilization. Biotechnological application of bacteria from the Propionibacterium genus may influence the reduction of contamination of the environment, not only through waste reduction, but also via conversion into useful components — propionic and acetic acid.

The objective of this study was to analyze apple pomaces in terms of the potential for their use as a potential source of carbon by P. freudenreichii T82 microorganisms in the process of propionic acid and acetic acid biosynthesis.

2. Materials and methods

2.1. Microorganisms

P. freudenreichii T82 wild strain derived from the collection of the Department of Biotechnology and Food Microbiology at Warsaw University of Life Science was used in the experiments. Microorganisms were stored at 4-6°C using VL (POCH) liquid medium.

2.2. Media

The experiments incorporated culture media which differed in terms of the type and the amount of carbon source. The composition of media is shown in Table 1. The following carbon sources were used: anhydrous glucose (POCH), fructose (POCH), saccharose (POCH), and apple pomace (derived from the production of fruit juices-DÒHLER-Natural Food & Beverage Ingredients). The media were sterilized in an autoclave at 117°C for 20 min, active acidity (pH) was set at 6.8-7 with the use of 25% aqueous ammonia solution.

2.3. Inoculum

Culture media inoculation was carried out for 48 h under static conditions at 30°C in 100 mL Erlenmeyer flasks containing 50 mL of VL medium with 2% anhydrous glucose. Before inoculation, media were sterilized in the autoclave at 117°C for 20 min. For inoculation of the appropriate medium, 10 vol% of suspension of proliferating cells in culture inoculation was used. Absorbance of the culture inoculum was set at 0.6-0.8.

2.4. Analysis of sugar profiles of media supplemented with apple pomaces

To a 50 mL measuring flask 2 mL of extract and 2 mL of 2% Ca(OH)2 were added to neutralize the environment. The flask was supplemented with distilled water to 50 mL. Before chromatographic separation, the resulting solutions were filtered using PA 0.45 μm syringe filters. For the analysis of media sugar profiles, high performance liquid chromatography was used (Shimadzu, Japan) together with an LC-10 ATV pump, an SIL 20AHT autosampler, a CO-10ASVp oven, a refractive index detector and a 10 μm Carbohydrate Analysis column (3.9 mm x 30 cm, Waters). Separation was performed using isocratic gradient. The eluent constituted a mixture of acetonitrile and water (800/200 v/v), flow rate was established at 1.5 mL/min. Injection volume of the sample was 20 μL. Glucose, fructose, saccharose and sorbitol were identified based on comparisons of retention times with standard solutions using a Shimadzu software.

2.5. Evaluation of growth dynamics of P. freudenreichii T82 strain in microcultivation using different carbon sources

Microcultures (medium volume of 300 μL) were grown in Bioscreen C oY AB Ltd., Growth Curves (Helsinki, Finland) were created by an automated analyzer after microbial growth for 120 h at 30°C. For each medium variant, five microcultures were grown. The growth of the tested bacteria was assessed by measurement of changes in optical density (OD) at a wavelength of 420-580 nm, performed automatically every hour. Based on the results obtained, growth curves of Propionibacterium, and lengths of the adaptive (tlag) and logarithmic (tlog) phases were evaluated. Moreover, minimum and maximum values of OD in the logarithmic growth phase (ODmin log and ODmax log) and during the total cultivation time (ODmin and ODmax), were determined. Furthermore, we determined the maximum speed of bacterial growth in the logarithmic phase with the formula: μmax = (lnODmax log -lnODmin log)/tlog, the generation time (g = ln2/|μmax)and the total increase in optical density (ΔOD = ODmax -ODmin).

2.6. Determination of reducing sugars using 3,5-dinitrosalicylic acid (DNS)

The principle of the method is based on the phenomenon that, in basic medium, nitro groups of 3,5-dinitrosalicylic acid are reduced to amino groups, while simultaneously the sugars are oxidized to corresponding acids. The resulting amine derivatives are orange, and measurement of the color intensity is performed at λ= 550 nm. To 0.5 mL of sample, 1.5 mL DNS was added and the mixture was stored for 5 min at 100°C. Then, after cooling, 8 mL of distilled water was added and 25 min after removal from the bath, the absorbance against a control sample was measured at a wavelength of 550 nm. The control sample consisted of 0.5 mL water, which was then processed in a similar manner to all the remaining samples. Calibration curves were plotted.

Table 1
Composition of culture media

2.7. Determination of volatile acidity

The principle of the method is based on re-distillation of the volatile acids with steam and then titration of the distillate obtained with NaOH standard solution against an indicator. To a flask of 250 mL, 25 mL of water was added, distillation was carried out with steam for 10 min in a BUCHI Labortechnik AG system. The distillate was heated, and then titrated with 0.1 M NaOH (CHEMPUR) against phenolphthalein (POCH S.A.) as an indicator. The amount of volatile acids was calculated according to the conversion: 1 mL 0.1 M NaOH balances 0.006 g of acetic acid. Volatile acidity was determined at three periods of cultivation: 24, 96 and 120 h.

2.8. Determination of organic acids

The process of propionic and acetic acid biosynthesis was carried out in 500 mL Erlenmeyer flasks containing 250 mL of culture medium with apple pomace inoculated with P. freudenreichii T82 inoculation. Experiments were carried out under static conditions for 120 h at 30°C. Samples for analyzes were collected at 24, 48, 96 and 120 h of the process.

The amount of propionic and acetic acid resulting from fermentation was determined. The analysis was conducted using gas chromatography with flame ionization detection (GC-FID). The carboxylic acid fraction was extracted from media utilizing a mixture of hexane and diethyl ether (1/1 v/v). Chromatographic separation was conducted using ZB-WAXplus column (30 m x 0.25 mm x 0.25 |am). Quantitative calculations were made against the internal standard (undecanoic acid — C11:0) using correction factors. Qualitative analysis of the sample was carried out based on retention times compared with standard solutions.

2.9. Statistical analysis

All experiments were performed in triplicates. Mathematical and statistical calculations were performed using computer programs such as Excel 2013 for Windows 10 and STATISTICA 6.0 PL Stat Soft, Inc. (2003). For optimization of the composition of carbon sources in the culture medium, we used design of experiment (DoE) methods. In the experiments, simplex plans for the ternary mixtures were used.

3. Results and discussion

An advanced enzyme system allows propionic acid bacteria to utilize a number of carbon sources (saccharides, organic acids). It creates the possibility of the disposal of waste materials containing essential nutrients. Moreover, it gives the opportunity for simultaneous acquisition of valuable metabolites. According to Bergey, P. freudenreichii T82 successfully utilizes, among others, glucose and fructose (positive reaction in 90 up to 100% strains), certain strains of this species also have the ability to ferment saccharose (positive reaction in 10 up to 40% strains).

Fig. 1. Sugar profile of medium before cultivation.

Fig. 2. Sugar profile of medium with the addition of apple pomace after 120 h of P. freudenreichii T82 cultivation.

Media prepared under laboratory conditions and containing apple pomace were subjected to an analysis of sugar profiles. Based on chromatographic separation, it was evident that, in this medium, the main saccharide was fructose, which accounted for 48.5% of all carbon sources. The remaining part was composed of saccharose, glucose and sorbitol (Fig. 1). After 120 h of P. freudenreichii T82 cultivation, we observed complete and partial consumption of fructose and glucose, respectively. Consequently, an increase in the proportion of saccharose and sorbitol — up to 83% and 7.7%, respectively - was reported in the medium (Fig. 2). The results clearly show that bacteria utilized fructose first. The saccharose molecule is composed of D-fructose and D-glucose linked by a (1 — 2)-β-O-glycosidic bond.

Hydrolysis of this disaccharide into simple sugars is related to, among others, energy expenditure, so that the bacteria more easily utilize available monosaccharides in the environment. It is assumed that propionic bacteria ferment fructose first due to the higher degree of reduction of this sugar compared to glucose and saccharose. After about 60 h of cultivation, inhibition of the growth of P. freudenreichii strain T82 was observed, probably due to the reduction in the active acidity of the environment. If optimum pH conditions had been created, it would be possible that even during cultivation bacteria would use other sugars. This would affect an increase in cell yield and maintenance of metabolic activity of these microorganisms, thereby leading to increased production of acids: propionic and acetic.

In the apple pomace, chromatographic separation using HPLC indicates the presence of fructose, glucose and saccharose. Therefore, for the purpose of determining the optimal culture medium for the growth of propionic bacteria, we evaluated media containing the above-mentioned carbon source.

Table 2
Parameters characterizing the growth of P. freudenreichii T82.

The bacterial strain tested demonstrated growth in all the types of media under study. The highest total increase in OD (1.235) was obtained in medium no. VI (Table 2). A similar increase in OD was observed in media nos. IV, VIII and X. Each of these was characterized by the presence of fructose. The lowest efficiency of OD increase was observed in media nos. III (1.027) and XI (0.907). In the media, in which fructose (II) and glucose (I) was the only carbon source, the total increase in OD was 1.156 and 1.074, respectively. A higher increase in OD was found in media in which fructose or glucose were mixed with other sugars. High concentrations of sugar (25 g/L) affected the increase in the osmotic pressure in the environment investigated. It led to the closure of the channels occurring in the cell membrane of bacteria necessary for nutrient uptake from a medium.

According to the literature, immediately after inoculation, a lag phase is observed in which microorganisms adapt to the conditions occurring in the culture medium. Then, the logarithmic growth phase begins in which the number of bacteria increases at a steady rate. The next step is the stationary phase induced by the consumption of nutrients and accumulation of toxic metabolites, in which we observed microbial growth inhibition. Based on the results, we found that the duration of the adaptive (lag) phase in the media investigated ranged from 3 to 8 h. Table 2 shows the kinetic parameters for P. freudenreichii T82. Based on these, it was found that the longest phase was observed in medium with apple pomace (XI, 8 h), and the shortest in culture no. II-X (3 h).

In terms of the logarithmic growth phase (log), we observed the opposite trend, which was the longest in medium with fructose (II, 29 h), and the shortest when pomace constituted the carbon source (XI, 15 h). In media I-X, a similarity in terms of the length of the adaptive and logarithmic growth phases was observed. In turn, in medium with pomace, an extension of the duration of the adaptation phase at the expense of the log phase was reported.

The large number of biologically active components found in apple pomace might also be the cause. After medium inoculation, we observed a period in which the lack of bacterial growth was significantly prolonged (8 h), as the culture medium was different from the inoculation medium. It is known that at this time the microorganisms synthesize enzymes essential for growth and metabolic activity in the new environment. The growth of microorganisms in media was inhibited after about 50-60 h, followed by the occurrence of the stationary phase (Fig. 3). This covers the increased intensity of metabolic processes, as evidenced by a simultaneous increase in the production of carboxylic acids.

Fig. 3. Changes in OD in the tested media during the cultivation of P. freudenreichii T82 bacteria.

The shortest generation time of P. freudenreichii T82 was reported in media nos. VI, IX (28.88 min) and VIII, X (30.14 min). Extension of the generation time was observed in the medium with apple pomace (38.51 min). Most likely, this is related to the change in medium composition compared to the inoculation medium and the need to synthesize enzymes by propionic bacteria necessary for the growth and activity in the new environment. The highest maximum speed (μmax), of P. freudenreichii T82 strain was demonstrated in media nos. VI, IX (0.024 h-1) and X (0.023 h-1)(Table 2).

Statistical analysis of the growth dynamics of P. freudenreichii T82 in micro-cultures with the use of different carbon sources (media I-IX) showed that the highest bacterial growth occurs in an environment with fructose. The addition of glucose and/or saccharose to the medium resulted in a smaller increase in the number of microorganisms, wherein saccharose affected the growth of bacteria more adversely compared to glucose. During the hours analyzed, the weakest microbial growth was observed in medium in which saccharose was the main carbon source (Fig. 4). In addition to evaluation of the growth dynamics, we determined the content of acids formed during the process of fermentation (Fig. 5). It was observed that in the 24th h of cultivation bacteria mainly used glucose for the production of metabolites. In the 96th h, the highest production of acids was found in media in which saccharose and glucose (>3 g/L) constituted the carbon sources.

In the 120th h of the process, the most intense biosynthesis of metabolites (>4.4 g/L) was found in medium containing only saccharose. Based on these results, it was concluded that the use of a sugar mixture affects the reduction of acid production. The higher the percentage of glucose and/or fructose in the medium, the less efficient the biosynthesis of metabolites. The results clearly show that the growth of P. freudenreichii T82 is the most intense when fructose is used, whereas the most efficient production of metabolites occurred during the use of saccharose by these bacteria. Intensification of fermentation processes was observed during the stationary growth phase of bacteria.

Fig. 6 shows the course of propionic fermentation in medium containing apple pomace. As a consequence of fermentation, two products emerged: propionic and acetic acid. Wang et al. and Kosmider et al., when using P. freudenreichii subsp. shermanii and glycerol as the carbon source, apart from the main product of fermentation — propionic acid, also observed two by-products: acetic and succinic acid. The biosynthesis of the additional metabolite in the form of succinic acid is probably dependent on the carbon source used. The proportion of acids changed during the fermentation process. Propionic acid biosynthesis reached its maximum value in the 120th h of cultivation (1.771 g/L). The efficiency of the process was 0.1 g of propionic acid/g of substrate. At this time, the content of the acetic acid produced reached the level of 7.049 g/L. The efficiency of the production of acetic acid per gram of substrate was 0.4 g. The highest increase in the production of both metabolites was found between the 96th and 120th h of cultivation. After the end of the experiment, we observed 1.84 g/L of reducing sugars in the post-culture medium.

Kośmider et al. used the P. freudenreichii ssp. shermani strain in the process of periodic fermentation conducted in media supplemented with glucose and glycerol. Total sugar consumption occurred in the 48th h of the process, biosynthesis of propionic acid reached the value of 10.2 g/L with an efficiency of 0.5 g of propionic acid per gram of substrate. The production of acetic acid was 2.4 g/L. In culture in which waste glycerol constituted a carbon source, it was found that the maximum value of the biosynthesis of propionic acid was observed in the 120th h of cultivation (11.6 g/L) — at that time, total consumption of glycerol was reported. After 120 h of the experiment, acetic acid was identified in trace amounts — approximately 0.7 g/L. More propionic acid after the 120th h of fermentation was obtained by Zhu et al.. At that time, the biosynthesis of the metabolite was 15.72 g/L with 1.2 g/L of acetic acid produced.

Fig. 4. Contour plot demonstrating an increase in OD in P. freudenreichii T82 bacterial culture depending on the composition of the carbon source in medium. The results obtained for medium I-X according to Table 1 were taken into account.

In comparison to the study conducted by Kosmider et al., the amount of propionic acid using apple pomace is low (1.771 g/L). On the other hand, a considerably higher amount of acetic acid was produced. The waste material used contains various compounds. A rich composition of medium may lead to decreased efficiency of the fermentation process by extending the adaptive phase. After medium inoculation, a period in which no growth is observed occurs. This results from the need to adapt bacteria to new cultivation conditions. Cultivation conditions used in the study may be a reason for the decreased production of propionic acid. Propionic acid bacteria exhibit the highest activity in neutral and oxygen-free environments. In studies conducted by Kosmider et al., the active acidity of media was stabilized at the level of 6.7-7 for the whole period of the experiment.

In the experiment with apple pomace, the pH of the environment was established once (6.7-7) — before the cultivation. Thus, we evaluated the possibility of P. freudenreichii T82 for growth and biosynthesis of metabolites at diverse pH levels (<7). Inhibition of bacterial growth occurred after about 60 h, when active acidity reached the value of 6. After 120 h of cultivation, the pH of the environment was 4.3. Despite the acidic pH, bacteria exhibited metabolic activity (the highest production of metabolites occurred between the 96th and 120th h of the experiment); however, inhibition of bacterial growth was also observed. The experiment was conducted under conditions of low oxygen supply, and thus a shift of fermentation processes toward biosynthesis of acetic acid was observed (aerobic conditions favor the production of acetic acid), which explains the increased production of this metabolite.

Excessive production of acetic acid leads to inhibition of the biosynthesis of propionate (and vice versa), which results from the need by bacterial cells to maintain balanced redox potential. It should also be noted that the use of waste material prolongs propionic fermentation. In the study conducted by Kośmider et al. and Himmi et al., glucose fermentation was already completed by the 48th h of cultivation, then complete consumption of the carbon source was observed. The use of waste glycerol resulted in an extended time period of the process of up to 120 h. At that time, we observed a complete refermentation of the carbon source in medium. The amount of propionic acid produced from these two nutrients differs by 1.4 g/L in favor of glucose.

In terms of acetic acid, the difference was 1.6 g/L (also in favor of glucose). The use of pomace also resulted in the extension of fermentation, in the 120th h of the process in the post-culture medium, we still found 1.8 g/L of sugars. It is possible that, despite the decreasing environmental pH, fermentation might extend by consecutive hours, until depletion of all the available compounds from the culture medium. Longer fermentation times with the use of waste materials are probably caused by the need for the adaptation of bacteria to culture medium conditions.

4. Conclusions

Waste substrates are much cheaper than glucose or other carbon sources and therefore may constitute an alternative for the production of propionic and acetic acid using microbiological approaches. The perspectives for the use of apple pomace in biotechnological processes seems to be attractive; however, this still requires further studies concerning, among others, selection of strains, optimization of cultivation conditions (e.g. suitable carbon sources, biostimulants) or regulation of the biosynthesis of propionic fermentation metabolites. In our experiments, we demonstrated the possibility of using apple pomace as a potential carbon source.

Fig. 5. Contour plot demonstrating the production of acids in P. freudenreichii T82 bacterial culture depending on the composition of the carbon source in medium. The results obtained for medium I-X according to Table 1 were taken into account.

Fig. 6. Propionic fermentation using apple pomace as the carbon source.

Conflict of interests

The authors declare no conflict of interest.

Appendix A. Supplementary data

Supplementary data to this article can be found online at http://dx.



1. Borawska J, Warmiñska-Radyko I, Darewicz M. Charakterystyka i znaczenie bakterii rodzaju Propionibacterium w produkcji zywnosci i pasz. Med Weter 2010;66:534-7.         [ Links ]

2. Leverrier P, Vissers JPC, Rouault A, Boyaval P, Jan G. Mass spectrometry proteomic analysis of stress adaptation reveals both common and distinct response pathways in Propionibacterium freudenreichii. Arch Microbiol 2004;181: 215-30.         [ Links ]

3. Pasciak M, Mordarska H. Rodzaj Propionibacterium -  heterogennosc taksonomiczna i biologiczna. Postepy Mikrobiol 1999;38:245-56.         [ Links ] 

4. Meile L, Dasen G, Miescher S, Stierli M, Teuber M. Classification of propionic acid bacteria and approaches to applied genetics. Lait 1999;79:71 -8.         [ Links ]

5. Ranadheera RDCS, Baines SK, Adams MC. Importance of food in probiotic efficacy. Food Res Int 2010;43:1-7.         [ Links ]

6. Coral J. Propionic acid production by Propionibacterium sp. using low-cos carbon sources in submerged fermentation. Curitiba: Biotechnology and bioprocesses engineering division federal University of Parana; 2008 1 -39.         [ Links ] 

7. Yazdani SS, Gonzalez R. Anaerobic fermentation of glycerol: A path to economic viability for the biofuels industry. Curr Opin Biotechnol 2007;18:213-9.         [ Links ]

8. Khan MM, Mir NA, Khan MM. Production of vitamin B12 by improved strains of Propionibacterium freudenreichii. Biotechnol Bioinf Bioeng 2011;1:19-24.         [ Links ]

9. Zarate G, Perez Chaia A, Oliver G. Some characteristics of practical relevance of the β-galactosidase from potential probiotic strains of Propionibacterium acidipropionici. Anaerobe 2002;8:259-67.         [ Links ]

10. Bzducha-Wróbel A, Blazejak S, Molenda M, Reczek L. Biosynthesis of β(1,3)/(1,6)-glucans of cell wall of the yeast Candida utilis ATCC 9950 strains in the culture media supplemented with deproteinated potato juice water and glycerol. Eur Food Res Technol 2014;240:1023-34.         [ Links ]

11. Holt JG, Krieg NR editors. Bergey's manual of determinative bacteriology'. 9th ed. Baltimore: The Williams & Wilkins Co; 1994.         [ Links ] 

12. Biochemia SL. Wydawnictwo Naukowe PWN, Warszawa; 2003 515-26.         [ Links ] 

13. Boyaval P, Deborde C, Corre C, Blanco C, Bégué É. Stress and osmoprotection in propionibacteria. Lait 1999;79:59-69.         [ Links ]

14. Lewicki PP, Porzecka-Pawlak R. Effect of osmotic dewatering on apple tissue structure. J Food Eng 2005;66:43-50.         [ Links ]

15. Piasecka E, Uczciwek M, Klewicki R. Odwadnianie osmotyczne owoców w roztworach zawierajacych fruktooligosacharydy, ZYWNOSC. Nauka Tech Jakosc 2009;2:138-53.         [ Links ] 

16. Baj J, Markiewicz Z. Biologia molekularna bakterii. Warszawa: Wydawnictwo naukowe PWN; 2012.         [ Links ]

17. Wang Z, Yang ST. Propionic acid production in glycerol/glucose co-fermentation by Propionibacterium freudenreichii subsp. shermanii. Bioresour Technol 2013;137: 116-23.         [ Links ]

18. Kosmider A, DdroZdzyñska A, Czaczyk K. Mozliwosci wykorzystania surowców odpadowych w procesie fermentacji propionowej. Zywnosc Nauka Tech Jakosc 2009;6:47-58.         [ Links ]

19. Zhu Y,Li J,Tan M, Liu L, Jiang L, Sun J, et al. Optimizationandscale-upof propionic acid production by propionic acid-tolerant Propionibacterium acidipropionici with glycerol as the carbon source. Bioresour Technol 2010; 101:8902-6.         [ Links ]

20. Kosmider A, DroZdzynska A, Blaszka K, Leja K, Czaczyk K Propionic acid production by Propionibacterium freudenreichii ssp. shermanii using crude glycerol and whey lactose industrial wastes. Pol J Environ Stud 2010;19:1249-53.         [ Links ]

21. Himmi EH, Bories A, Boussaid A, Hassani L. Propionic acid fermentation of glycerol and glucose by Propionibacterium acidipropionici and Propionibacterium freudenreichii ssp. shermanii. Appl Microbiol Biotechnol 2000;53:435-40.         [ Links ]


Article history: Received 8 February 2016 Accepted 29 June 2016 Available online 11 August 2016

*  Corresponding author. E-mail address: (K Piwowarek).

Copyright © 2016 Pontificia Universidad Católica de Valparaíso. Production and hosting by Elsevier B.V. All rights reserved. Peer review under responsibility of Pontificia Universidad Católica de Valparaíso.

Creative Commons License Todo o conteúdo deste periódico, exceto onde está identificado, está licenciado sob uma Licença Creative Commons