Lucrări ştiinńifice Zootehnie şi Biotehnologii, vol. 41(1) (2008), Timişoara TESTING OF THE EFFICIENCY OF SOME ENZYMATIC MIXTURES, CONCERNING THE CONVERSION OF SEVERAL LIGNOCELLULOSIC BIOMASS SOURSES, TO REDUCING SUGARS TESTAREA EFICIENłEI UNOR PREPARATE ENZIMATICE, PRIVIND CONVERSIA BIOMASEI LIGNOCELULOZICE DIN DIFERITE SURSE, LA GLUCIDE REDUCĂTOARE TAMBA-BEREHOIU RADIANA*, JURCOANE STEFANA*, POPA N. C**, BAGIU LILIANA***, ROSU ANA* * Faculty of Biotechnology, Bucharest, Romania ** S.C. FARINSAN S.A., Grădistea, Giurgiu ***Center of Microbial Biotechnology, Bucharest, Romania Three lignocelluloses substrates have been used, as following: Mischantus, Maize stalk and Wheat bran, in order to obtain fermentescible sugars, which will be transformed into bioethanol. The substrates were hydrolysed using commercial enzymes: MethaPlus (β-glucanase, xylanase, cellulase), Veron 191 (xylanase), Hep C (cellulase). The hydrolysis was performed at 55 0 C, for 20 h, at ph = 5,5. The best results were obtained by using MethaPlus enzyme. The efficiency of hydrolysis was 110.80 % for Miscanthus, 126.15 % for maize stalk and 118.76 % for wheat bran, reported to the control. The most enhanced quantities of reducing sugars were obtained in maize stalk, namely: 126.15 % using MethaPlus, 112.07 % using Veron 191 and 113.52 % using Hep C. The wheat bran was hydrolysed with enzymatic mixtures, for emphasizing the reducing sugars grow, coming from residual starch s content (flour). In comparison to the control, the efficiency of hydrolysis was of: 181.004 % for MethaPlus-Veron M4 mixture, 168.83 % for MethaPlus-Veron 393 mixture, 205.86 % for MethaPlus-BG α-malt mixture and of 176.57 % for MethaPlus-Veron MX mixture. The enzymatic mixture which contains BG α-malt was the most productive, the hydrolysis efficiency being superior to all other variants. Key words: enzymatic mixtures, enzymatic hydrolysis, reducing sugars, efficiency Introduction Quick consumption of fossil energetic resources needs step by step substitution with alternative resources, which must be environmental friendly and which could save the planet from a potential major crisis [1, 21]. The obtaining of bioethanol as a renewable energy resource, means the conversion of several types of biomass (glucidic wastes, lignocelluloses wastes etc), using different methods, 155
into reducing sugars (hexoses, mainly glucose, but also pentoses, like: xylose, arabinose), and lastly into bioethanol [13, 16]. The glucidic polymers in lignocelluloses fraction of biomass are composed of 28 35 % hemicelluloses (biopolymer of xylanose and arabinose) and 35 48 % cellulose, related to the source where they are coming from [1, 5, 11]. There are a lot of biomass sources, like: - energetically plants cultures, with high growing speed (poplar, acacia, eucalyptus, sweet cane, rape, sugar beet, switch grass like: Mischantus, Panicum Virgatum etc); - residues (wood, straw, stalk, bran, tea and coffee wastes etc); - wastes and by-products (sawdust, paper, organic garbage wastes). The efficient conversion of biomass was performed in more steps, such as: chemical pre-treatment, followed by a lignocelluloses biopolymers hydrolysis to reducing sugars (enzymatically or chemically), by alcoholic fermentation of reducing sugars, by distillation and purification of bioethanol [4, 8, 9, 12, 17, 19]. The hydrolysis of lignocelluloses biomass to glucose, could be ecologically and economically performed by a complex enzymatic system, mainly formed by three types of hydrolases: endoglucanases, exoglucanases, β-glycosidase, which act together, cutting the β glicosydic bonds [10, 14]. It was find out that the mixtures of cellulases and amylases enhance the hydrolysis efficiency. The productivity of hydrolysis is influenced by several factors, but the most important factors which are modelling the hydrolysis process are as following: the pre-treatment method, the substrate concentration, the pre-treatment quality, the enzymes mixtures, the temperature conditions, ph and the shaking conditions [7, 15, 20]. The goal of this research was the testing of efficiency of some enzymes and enzymatic mixtures, used for the hydrolysis of three lignocellulosic substrates, without performing chemical pre-treatment. Materials and Methods Three lignocelluloses substrates have been used such as: Miscanthus, maize stalk and wheat bran, which were ground (0.5 1 mm sieve diameter), as standard routine for enzymatic hydrolysis. The first step, which has been performed was the laboratory analysis concerning the % moisture content of the substrates (The Practical Reference Method, SR ISO 712/1999) [2]. After that, the lignocelluloses substrates were hydrolysed using some commercial enzyme preparations: MethaPlus (β-glucanase, xylanase, cellulase), Veron 191 (xylanase) and Hep C (cellulase). We also performed the hydrolysis of bran by using enzymatic mixtures, which contained Veron 393 (hemicellulase), Veron MX (xylanase) and amylases, namely: Veron M4 and BG α-malt, because we will always find flour traces in wheat bran (residual starch). The flour traces will substantial enhances the reducing sugars concentration, therefore the efficiency of bioethanol production [3]. 156
We used the enzymes concentrations showed in their technical specifications. Enzymatic hydrolysis was performed at 55 0 C, during 20 h period, at ph=5,5, on a rotary shaker at 200 rpm. We performed all the experiments in triplicate and presented them as mean value. It was also prepared a control sample (without enzyme), for each trial. The efficiency of hydrolysis was estimated by quantifying the amount of reducing sugars. The reducing sugars were determined as glucose, by reading the absorption at 640 nm, using 3.5-dinitrosalicilic (Peterson and Porath modified method) [6, 18]. Results and Discussions Table 1 shows the moisture of the substrates used for the enzymatic hydrolysis, such as: Miscanthus, maize stalk and wheat bran. Table 1 Moisture of the substrates used for enzymatic hydrolysis SUBSTRATE Moisture % Dry Matter % Miscanthus 16,44 83,56 Maize stalk 7, 83 92,17 Wheat bran 13,50 86,50 None of the substrates needed preconditioning, because moisture did not get over 17 %. Table 2 shows the hydrolysis results by using three enzymes, expressed in reducing sugars (calculated to dry matter), for Miscanthus, maize stalk and wheat bran. Table 2 Reducing sugars after enzymatic hydrolysis Substrate Enzyme Control/ Sample Reducing sugars g/100 g D.M. MethaPlus C 7.263 Miscanthus S 15.311 Xylanase Veron 191 S 13. 824 Cellulase Hep C S 11.558 MethaPlus C 15.510 Maize stalk S 35.077 Xylanase Veron 191 S 32.893 Cellulase Hep C S 33.118 MethaPlus C 8.502 Wheat bran S 18.599 Xylanaza Veron 191 S 15.236 Cellulase Hep C S 15.825 Figure 1 emphasizes the differences between substrates, concerning the efficiency of enzymatic hydrolysis, by using different enzymes. 157
Reducing sugars % 40 35 30 25 20 15 10 5 Miscanthus Maize stalk Wheat bran 0 Control MethaPlus Veron 191 Hep C Figure 1. Increase of reducing sugars concentrations after enzymatic hydrolysis The increasing of reducing sugars concentration, by enzymatic hydrolysis using MethaPlus, in comparison to control, was as follows: 110.80 % to Miscanthus, de 126.15 % to maize stalk and 118.76 % to wheat bran. The increase of reducing sugars concentration, by enzymatic hydrolysis using Veron 191, in comparison to control, was as follows: 99.30 % to Miscanthus, de 112.07 % to maize stalk and 79.20 % to wheat bran. The increasing of reducing sugars concentration, by enzymatic hydrolysis using Hep C, in comparison to control, was as follows: 59.13 % to Miscanthus, de 113.52 % to maize stalk and 86.13 % to wheat bran (table 3). Table 3 Hydrolysis efficiency, expressed as increase of reducing sugars percents, comparative to control sample Enzyme Increase of the reducing sugars concentration comparative to control sample % Miscanthus Maize stalk Wheat bran MethaPlus 110.08 126.15 118.80 Veron 191 99.30 112.07 79.20 Hep C 59.13 113.52 86.13 Wheat bran has been further incubated with enzymatic mixtures, process which enhanced the hydrolysis productivity, emphasizing the residual starch s contribution, to the reducing sugars whole concentration (table 4). 158
Table 4 The results of the wheat bran s hydrolysis with enzymatic mixtures Substrate Enzyme Control/ Sample Reducing sugars g/100 g D.M. MethaPlus C 8.502 S 15.311 S 23.891 Wheat bran Amylase Veron M4 S 22.856 Hemicelluloses Veron 393 S 26.005 Amylase BG α-malt Xylanase Veron MX S 23.514 All the enzymatic mixtures used for hydrolysis, enhanced its efficiency (figure 2). Conclusively, reducing sugars concentration raised with 56.03 % by using Veron M4, with 49.27 % by using Veron 393, with 69.84 % by using BG α- malt and with 53.57 % by using Veron MX, in comparison to the values obtained by using only MethaPlus (15,311 %). Reducing sugars % 30 25 20 15 10 5 8.502 15.311 23.891 22.856 26.005 23.514 0 Control MethaPlus amilase Veron M4 hemicelullase Veron 393 amilase BG alpha-malt xylanase Veron MX Figure 2. Concentration of reduced sugars after hydrolysis with enzymatic mixtures In comparison to the control, the efficiency of hydrolysis was: 181.004 % for MethaPlus-Veron M4 mixture, 168.83 % for MethaPlus-Veron 393 mixture, 205.86 % for MethaPlus-BG α-malt mixture and 176.57 % for MethaPlus-Veron MX mixture. It is easy to observe that the enzymatic mixture which contains BG α- 159
malt was the most efficient, the productivity of hydrolysis being superior to all others variants. Conclusions The results of the enzymatic hydrolysis of all substrates emphasize the increase of reducing sugars content, especially to the maize stalk, no matter the enzyme used. These phenomena dues to the large content of soluble sugars from maize stalk. The increase of reducing sugars content for Miscanthus and wheat bran is moderate. MethaPlus was more active than Veron 191 and Hep C, due to the fact that this product was already a commercial enzymatic mixture. Hep C cellulase was less active in hydrolyzing Miscanthus samples, in comparison to both: maize stalk and wheat bran (possible inhibiting factors). All enzymatic mixtures improved the efficiency of wheat bran s hydrolysis and determined the increase of reducing sugars content. BG α-malt enzymatic mixture produced the best result, concerning the reducing sugars randament, because of the residual starch s hydrolysis (flour) from the wheat bran. Veron M4 amylase had a smaller effect, comparative to BG α-malt amylase. Veron 393 hemicellulase and Veron MX xylanase had comparable effects, concerning the producing of reducing sugars in wheat bran. Conclusively, we may say that enzymatic mixtures, selected after the chemical composition of hydrolysed substrates, increase the reducing sugars content. We may also say that prior to enzymatic hydrolysis, chemical pretreatment are necessary, which will increase randaments. Acknowledgments. This research is part of a national project, financially supported by PNCDI 2, Partnership in priority domains (no. 3842, type PC, contract 21-058\2007-11-7, 2007-2009). Bibliography 1. Banu şi colab., (2006)- Bioalcoolul combustibilul viitorului, Editura Agir, Bucureşti 2. Bordei şi colab., (2007)- Controlul calităńii în industria panificańiei, metode de analiză, Ed. Academica, GalaŃi 3. Choteborska şi colab., (2004)- Processing of wheat bran to sugar solution, Journal of Food Engineering, 61, 561 565 4. Diguta şi colab., (2007)- Studies concerning hydrolysis of energy crops, Roum. Biotechnol. Lett., Vol. 12, No. 2, 3203-3207 160
5. Howard R.L., Abotsi E., Jansen Van Renseburg, E.L. and Howards S., (2003)- Lignocellulose biotechnology: issues of bioconversion and enzyme production, African Journal of Biotechnology, Vol. 2 (12), pp. 602-619, review 6. Iordachescu D., Dumitru I.F., (1980)- Biochimie practică Proteine şi enzime, Partea I, Tipografia UniversităŃii din Bucureşti 7. Fan, L.T., Lee, Y.H., Beardmore, D.H., (1981)- The influence of major structural features of cellulose on rate of enzymatic hydrolysis. Biotechnol Bioeng 23: 419-424. 8. Fan, L.T., Gharpuray, M.M., Lee, Y.H., (1987)- Cellulose hydrolisys biotechnology monographs,3, Springer-Verlag, Berlin 9. Jurcoane Ş., (2000)- Biotehnologii Fundamente-Bioreactoare-Enzime, Ed. Tehnică, Bucureşti 10. Jurcoane şi colab., (2006)- Tratat de Biotehnologie, Ed. Tehnică, Bucureşti 11. Kanuf M., Monirussaman M., (2004)- Lignocellulosic biomass processing : A perspective, International Sugar Journal, vol. 106, No. 1263, pp. 147-150 12. Kunaver, M., Jasiukaityte, E., Tisler. V., 2007, Liquefaction of lignocelluloses biomass and its potential applications, Journal of Biotechnology, 131S, S23-S31 13. Ronghou L., Jinxia L., Fei S., (2007)- Refining bioethanol from stalk juice of sweet sorghum by immobilized yeast fermentation, Renew Energy, doi: 10.1016/j.rennene.2007.05.046 14. Rosgaard L., Pederson S., Cherry J.R., Harris P., Meyer A.S., (2006)- Efficiency of new fungal cellulase systems in boosting enzymatic degradation of barley straw, Biotechnol Prog., Mar-Apr; 22(2):493-8 15. Sinistyn, A.P., Gusakov, A.V., Vlasen, E.Y., (1991)- Effect of structural and physico-chemical features of cellulosic substrates on the efficiency of enzymatic hydrolysis, Appl Biochem Biotechnol 30:43-59. 16. Tabka, M.G., Herpoel-Gimbert, I., Monod, F., Asther, M., Sigoilot, J.C., (2006)- Enzymatic saccharification of wheat straw for bioethanol production by a combined cellulose xylanase and feruloyl esterase treatament, Enzyme and Microbial Technology, 39, 897 902. 17. Taherdazeh M.J., Karimi K., (2007)- Enzyme-based hydrolysis processes for ethanol from lignocellulosic materials: A Review, BioResources 2(4) 707 738 18. Zăvoianu, D., Cuza, O., Bornaz, C., Nicolae, A., (1997)- Lucrări practice de chimie organică, Ed. UniversităŃii Bucureşti 19. Zhu Li, (2005)- Fundamental study of structural features affecting enzymatic hidrolsis of lignocellulosic biomas, Doctorate Thesis, Texas A&M Univerity 20. Walker, L.P., Wilson, D.B., (1991)- Enzymatic hdrolisis of celulose: An overview, Biores. Technol, 36:3-14. 21. *** EUROPEAN COMMISSION- EUR 21350 BIOMASS, 2005 - Green energy for Europe, Luxembourg: Office for Official Publications of the European Communities 161