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Slovak Society <strong>of</strong> Chemical EngineeringInstitute <strong>of</strong> Chemical and Environmental EngineeringSlovak University <strong>of</strong> Technology in BratislavaPROCEEDINGS37 th International Conference <strong>of</strong> Slovak Society <strong>of</strong> Chemical EngineeringHotel HutníkTatranské Matliare, SlovakiaMay 24 – 28, 2010Editor: J. MarkošISBN 978-80-227-3290-1Mackul’ak, T., Prousek, J., Olejníková, P., Bodík, I.: <strong>The</strong> <strong>using</strong> <strong>of</strong> <strong>enzymes</strong> <strong>for</strong> <strong>degradation</strong> <strong>of</strong> <strong>cellulose</strong> <strong>substrate</strong><strong>for</strong> <strong>the</strong> production <strong>of</strong> biogas, Editor: Markoš, J., In Proceedings <strong>of</strong> <strong>the</strong> 37th International Conference<strong>of</strong> Slovak Society <strong>of</strong> Chemical Engineering, Tatranské Matliare, Slovakia, 1407–1412, 2010.


37th International Conference <strong>of</strong> SSCHEMay 24–28, 2010, Tatranské Matliare, SlovakiaPo-Th-6, 116p.pdf<strong>The</strong> Using Of Enzymes For Degradation Of Cellulose Substrate For <strong>The</strong>Production Of BiogasTomáš Mackuľak, Josef Prousek, Petra Olejníková a , Igor Bodík,Department <strong>of</strong> Environmental Engineering, Institute <strong>of</strong> Chemical and Environmental Engineering,Faculty <strong>of</strong> Chemical and Food Technology, Slovak University <strong>of</strong> Technology, Radlinskeho 9, 812 37Bratislava, Slovak RepublicaDepartment <strong>of</strong> Biochemistry and Microbiology, Institute <strong>of</strong> Biochemistry, Nutrition and HealthProtection, Faculty <strong>of</strong> Chemical and Food Technology, Slovak University <strong>of</strong> Technology, Radlinskeho9, Bratislava 812 37, Slovak Republic,e-mail: mackulakt@azet.skKey wordsenzymatic hydrolysis, <strong>cellulose</strong> <strong>substrate</strong>, glucoseAbstract<strong>The</strong> main purpose <strong>of</strong> this article is to describe different kinds <strong>of</strong> <strong>cellulose</strong> <strong>degradation</strong> processes such asenzymatic hydrolysis. As <strong>the</strong> <strong>cellulose</strong> <strong>substrate</strong>s <strong>the</strong> sawdust, leaves and cartons were used. Anaerobic<strong>degradation</strong> processes utilized <strong>for</strong> <strong>the</strong> biogas production can be accelerated by this way.1. IntroductionAs <strong>substrate</strong>s <strong>for</strong> biogas production waste materials which contain polysaccharides, lipids and proteinscan be used. Plant origin <strong>substrate</strong>s contain mainly <strong>cellulose</strong> (Fig. 1), hemi<strong>cellulose</strong> and lignin [1]. <strong>The</strong>structure <strong>of</strong> <strong>cellulose</strong> consists <strong>of</strong> parallel glucan chains and is stabilized by hydrogen bonds.Fig. 1. Cellulose structure<strong>The</strong> main structural unit <strong>of</strong> <strong>cellulose</strong> is D – glucose [3]. Cellulose is resistant to different types <strong>of</strong><strong>degradation</strong> [2]. <strong>The</strong> <strong>cellulose</strong> <strong>substrate</strong> contains various representation <strong>of</strong> lignin, which influences <strong>the</strong>resistance <strong>of</strong> <strong>substrate</strong> and also increases <strong>the</strong> cost <strong>of</strong> pretreatment. Usage <strong>of</strong> hay, straw and recycledpaper as a <strong>substrate</strong> containing ligno<strong>cellulose</strong>s <strong>for</strong> increasing biogas production is currently beingtested and interesting topic.A mechanical pretreatment is <strong>the</strong> first step in <strong>the</strong> pretreatment <strong>of</strong> ligno<strong>cellulose</strong>s <strong>substrate</strong>. In next stepsis possible to degrade <strong>cellulose</strong> by chemical or enzymatic hydrolysis [5, 8]. <strong>The</strong> chemical hydrolysis byH 2 SO 4 and HCl leads to breaking <strong>cellulose</strong> into cellotetrose and cellobiose [2, 4, 8]. By Fenton reactionis possible to degrade cellotetrose and cellobiose to glucose, a simple aldehydes and ketones. Directway to degrade <strong>cellulose</strong> into glucose is enzymatic hydrolysis.Enzymatic hydrolysis <strong>of</strong> <strong>cellulose</strong> takes place with a mixture <strong>of</strong> <strong>enzymes</strong> – cellulases [1, 5-9], at 36 –37 °C. Cellulases break down <strong>cellulose</strong> in three ways. Endoglucanases convert chains <strong>of</strong> <strong>cellulose</strong> from1407


37th International Conference <strong>of</strong> SSCHEMay 24–28, 2010, Tatranské Matliare, SlovakiaPo-Th-6, 116p.pdf<strong>the</strong> inside, creating new ends <strong>of</strong> shorter chains [1]. Exoglucanases separated from non-reducting ends<strong>of</strong> new chains cellobiotic units. In consequent steps cellotetrose and cellobiose are decomposed toglucose in liquid phase by <strong>the</strong> enzyme β-glucosidase [1]. Cellulases are produced by different types <strong>of</strong>bacteria and filamentous fungi [5,7]. Research <strong>of</strong> different tribes <strong>of</strong> filamentous fungi isolated fromwaste waters from paper production, which are able to produce <strong>cellulose</strong> in large scale seems to beinteresting nowadays [5,7]. Lignocellullase <strong>substrate</strong> pre-treated in this way can be used to increase <strong>the</strong>quality and quantity <strong>of</strong> produced biogas.2. Experimental partCellulose <strong>substrate</strong>Cellulose <strong>substrate</strong> was inactivated with lime (Fig. 2). Total solids were 43% and volatile solids were44%.Fig. 2. Cellulose <strong>substrate</strong>Principes <strong>of</strong> glucose determinationOxidation <strong>of</strong> glucose with oxygen was pre<strong>for</strong>med with enzymatic catalysis by glucose oxidase <strong>for</strong>hydrogen peroxide and gluconate. Formed hydrogen peroxide was determinated by oxidationcopulation with substitued phenol and 4- aminoantipyrine and cotalised with peroxidase.Determination <strong>of</strong> glucoseOperating solution was mixed with serum or sample, standard glucose solution and distilled water(control solution) in <strong>the</strong> ratio 100:1 or 150:1 in three tubes. Incubation was pre<strong>for</strong>med <strong>for</strong> 30 min. at15- 25 °C or <strong>for</strong> 15 min. at 37°C. <strong>The</strong> incubation mixture must be protected from direct light. Whitin40 min. after incubation <strong>the</strong> absorbance <strong>of</strong> sample (A 1 ) and absorbance <strong>of</strong> sample (A 2 ) was measuredand compared with control solution.CalculationGlucose (mmol.l -1 ) = a. A 1 /A 2 ,where a is glucose contentration in standard solution [mmol.l -1 ].Enzymatic hydrolysisIn various experiments with <strong>enzymes</strong> different amounts <strong>of</strong> enzyme mixture <strong>for</strong> <strong>cellulose</strong> <strong>substrate</strong><strong>degradation</strong> were used (Fig. 3). <strong>The</strong> effectiveness <strong>of</strong> individual experiments on <strong>the</strong> measurement <strong>of</strong>COD value (mg.l -1 ) and glucose concentration was determined (g.l -1 ). Procedures and results in<strong>degradation</strong> <strong>of</strong> <strong>the</strong> <strong>substrate</strong> are given in experiments No. 1-3, and Fig. 4-5.1408


37th International Conference <strong>of</strong> SSCHEMay 24–28, 2010, Tatranské Matliare, SlovakiaPo-Th-6, 116p.pdfFig. 3. Enzymatic hydrolysisExperiment No. 1 (E1)In <strong>the</strong> first series <strong>of</strong> experiments with compound <strong>of</strong> <strong>enzymes</strong> 5mg <strong>of</strong> <strong>enzymes</strong> were added into 200 ml<strong>of</strong> deionized water. <strong>The</strong> solution was stirred until dissolved <strong>enzymes</strong>. In <strong>the</strong> next step 3 g <strong>of</strong> <strong>cellulose</strong><strong>substrate</strong> were added. <strong>The</strong> temperature was 37°C and mixture wasn’t stirred. Degradation <strong>of</strong> <strong>substrate</strong>to glucose was determined by glucose- oxidation test and by measurement <strong>of</strong> COD values.Experiment No. 2 (E2)In ano<strong>the</strong>r series <strong>of</strong> experiments 50 mg <strong>of</strong> compound <strong>of</strong> <strong>enzymes</strong> were dissolved in 200 ml <strong>of</strong> deionizedwater. <strong>The</strong> solution was stirred until dissolved <strong>enzymes</strong>. In <strong>the</strong> next step 3 g <strong>of</strong> <strong>cellulose</strong> <strong>substrate</strong> wereadded. <strong>The</strong> temperature was 37°C and mixture wasn’t stirred. Degradation <strong>of</strong> <strong>substrate</strong> to glucose wasdetermined by glucose- oxidation test and by measurement <strong>of</strong> COD values.Experiment No. 3 (E3)In final series <strong>of</strong> experiments with compound <strong>of</strong> <strong>enzymes</strong> 450 mg <strong>of</strong> <strong>enzymes</strong> were dissolved in 200 ml<strong>of</strong> deionized water. <strong>The</strong> solution was stirred until dissolved <strong>enzymes</strong>. In <strong>the</strong> next step 3 g <strong>of</strong> <strong>cellulose</strong><strong>substrate</strong> were added. <strong>The</strong> temperature was 37°C and mixture wasn’t stirred. Degradation <strong>of</strong> <strong>substrate</strong>to glucose was determined by glucose- oxidation test and measurement <strong>of</strong> COD values.3. Results and discussionEnzymatic hydrolysis decomposes <strong>cellulose</strong> to cellotetrose and cellobiose in first step. Subsequentlycellotetrose and cellobiose are degradated to glucose, lower aldehydes and ketones (Fig. 4). Products <strong>of</strong>enzymatic hydrolysis depends on <strong>the</strong> type and composition <strong>of</strong> <strong>the</strong> <strong>substrate</strong>, <strong>the</strong> reaction time, <strong>the</strong> typeand quantity <strong>of</strong> <strong>the</strong> <strong>enzymes</strong> and <strong>the</strong> reaction temperature. Glucose itself can be enzymatic degraded toaldehydes and ketones.Compound <strong>of</strong> <strong>enzymes</strong> was used <strong>for</strong> <strong>the</strong> <strong>degradation</strong> <strong>of</strong> cellulosic <strong>substrate</strong>. Time dependence <strong>of</strong>glucose production resulting from <strong>substrate</strong> <strong>degradation</strong> is shown in figure 5. From each experiment isappeared that <strong>the</strong> production <strong>of</strong> glucose is affected by <strong>the</strong> amount <strong>of</strong> <strong>enzymes</strong> used, quantity <strong>of</strong><strong>substrate</strong>, reaction temperature and time. <strong>The</strong> highest glucose yield was achieved in <strong>the</strong> experiments no.3. In experiment No. 2 and 3. a decrease in glucose concentration after 24 hrs. was observed, whichwas caused by <strong>the</strong> amount <strong>of</strong> used <strong>enzymes</strong> (Tab. 1, Fig. 4).1409


37th International Conference <strong>of</strong> SSCHEMay 24–28, 2010, Tatranské Matliare, SlovakiaPo-Th-6, 116p.pdfFig. 4. Expected mechanism <strong>of</strong> <strong>cellulose</strong> <strong>degradation</strong> by enzymatic hydrolysis0,350,300,25glucose g.l -10,200,150,10E 1E 2E 30,050,000 10 20 30 40 50 60 70 80t(h)Fig. 5. Time dependance <strong>of</strong> glucose production by enzymatic <strong>degradation</strong> <strong>of</strong> <strong>cellulose</strong> <strong>substrate</strong>.Tab. 1. Time dependance <strong>of</strong> glucose production by enzymatic <strong>degradation</strong> <strong>of</strong> <strong>cellulose</strong> <strong>substrate</strong> inexperiments no. 1-3.Time (hours) Glucose (g.l -1 )E 1 E 2 E 36 0.1 0.2 0.2224 0.2 0.26 0.3248 0.22 0.3 0.2872 0.26 0.26 0.241410


37th International Conference <strong>of</strong> SSCHEMay 24–28, 2010, Tatranské Matliare, SlovakiaPo-Th-6, 116p.pdfTab. 2. Time dependence <strong>of</strong> COD value in experiments no. 1- 3 <strong>of</strong> glucose production by enzymatic<strong>degradation</strong> <strong>of</strong> <strong>cellulose</strong> <strong>substrate</strong>.Time (hours) COD (mg.l -1 )E 1 E 2 E 36 200 250 34024 360 540 59048 430 580 62072 600 650 6807 0 06 0 05 0 0CHSK (mg.l -1 )4 0 03 0 02 0 0E 1E 2E 31 0 000 1 0 2 0 3 0 4 0 5 0 6 0 7 0 8 0t ( h )Fig. 6. Comparation <strong>of</strong> experiments no. 1-3 by COD value.4. ConclusionFrom results it can be concluded that lignocellulosic <strong>substrate</strong>s can be succesfully modified byenzymatic hydrolysis. We dealt with <strong>the</strong> use <strong>of</strong> enzymatic hydrolysis in experiments No. 1-3. It isobtained possible to decompose <strong>cellulose</strong> <strong>substrate</strong> to glucose by <strong>enzymes</strong>. Yield <strong>of</strong> glucose is dependson quantity <strong>of</strong> <strong>substrate</strong> used, amount <strong>of</strong> used <strong>enzymes</strong> used, reaction temperature and time (Fig. 5).Substrate is decomposed to glucose and lower aldehydes <strong>for</strong> prolonged exposure to <strong>enzymes</strong>.Efficiency and progress <strong>of</strong> enzymatic hydrolysis is affected by content <strong>of</strong> lignin in <strong>substrate</strong>. Celluloseis covered by lignin and <strong>the</strong>reby increase <strong>the</strong> resistance <strong>of</strong> <strong>cellulose</strong> to enzymatic <strong>degradation</strong>. It is<strong>the</strong>re<strong>for</strong>e possible to combine <strong>the</strong> procedures <strong>for</strong> remove lignin (e.g., chemical hydrolysis) andsubsequently enzymatic hydrolysis or microbial <strong>degradation</strong> can be used. <strong>The</strong> effectiveness <strong>of</strong>enzymatic hydrolysis can be regulated or completely inhibited by temperature increasing. Enzymatichydrolysis is one <strong>of</strong> <strong>the</strong> processes by which we can pretreated <strong>cellulose</strong> <strong>substrate</strong>s such as sawdust,leaves, hay, straw, recycled paper and thus accelerated <strong>the</strong> processes <strong>of</strong> <strong>degradation</strong> under anaerobicconditions. Products <strong>of</strong> enzymatic <strong>degradation</strong> <strong>of</strong> <strong>substrate</strong>s are glucose and lower aldehydes, which are1411


37th International Conference <strong>of</strong> SSCHEMay 24–28, 2010, Tatranské Matliare, SlovakiaPo-Th-6, 116p.pdfhighly degraded in anaerobic processes. Substrates treated in this way are easier and fasterbiodegradabiled and can be used to increase biogas yield and quantity.5. References1. Straka F. a kol. (2006).: Bioplyn. Praha: GAS s.r.o.,706 s.2. Görner F., Valík Ľ. (2004).: Aplikovaná mikrobiológia požívatín. Malé Centrum, Bratislava.3. Šulák M., Šmogrovičová D. (2008).: Bioetanol : Súčasné trendy vo výskume a v praxi : Chem.Listy 102, 108−115.4. Sun Y., Cheng J. (2002).: Hydrolysis <strong>of</strong> lignocellulosic materials <strong>for</strong> ethanol production.Bioresource Technology., 83, 1-11.5. Tanaka H., Koike K., Itakura S., Enoki A. (2009).: Degradation <strong>of</strong> wood and enzyme productionby Ceriporiopsis subvermispora. Enzyme Microb. Technol. doi:10.1016/j.enzmictec.2009.06.003.6. Romsaiyud A, Songka S.W., Nopharatana A., Chaiprasert P. (2009).: Combination effect <strong>of</strong> pHand acetate on enzymatic <strong>cellulose</strong> hydrolysis. J. Environ. Sci. 21, 965–970.7. Solange I.M., Marcela F., Adriane M.F.M, Inˆes C.R. (2008).: Effect <strong>of</strong> hemi<strong>cellulose</strong> and ligninon enzymatic hydrolysis <strong>of</strong> <strong>cellulose</strong> from brewer’s spent grain. Enzyme Microb. Technol. 43,124–129.8. Voet D., Voetová J.G. (1995).: Biochemie. Victoria Publishing a.s.,Praha, 268-283.9. Mackuľak T., Prousek J., Bodík I. (2009).: Predúprava a využitie celulózového substrátu z výrobypapiera na produkciu bioplynu. Zborník konferencie: Výstavba a provoz bioplynových stanic.Třeboň, október 15.-16, str. 83-89. ISBN-978-80-254-5455-8.Acknowledgements<strong>The</strong> presented contributions was created as a part <strong>of</strong> project SK00023 financed by Norwegian FinancialMechanism, Financial Mechanism <strong>of</strong> EEA and <strong>the</strong> State Budget <strong>of</strong> <strong>the</strong> Slovak Republic(www.eeagrants.com). This work was supported by <strong>the</strong> Slovak Research and Development Agencyunder <strong>the</strong> contract No. LPP-0019-09.1412

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