Journal of Engineering Science and Technology Special Issue on SOMCHE 2014 & RSCE 2014 Conference, January (2015) 1 - 8 © School of Engineering, Taylor’s University HYDROLYSIS OF STARCH IN PORANG FLOUR USING ALPHA AMYLASE FADILAH*1,2, ROCHMADI2, S. SYAMSIAH2, HARYADI3 1 Chemical Engineering Department Sebelas Maret University, Jl. Ir. Sutami 36 A Surakarta 57126, Indonesia Chemical Engineering Department Gadjah Mada University, Jl. Grafika 2 Yogyakarta 55281, Indonesia 3 Faculty of Agricultural Technology Gadjah Mada University, Jl. Flora No. 1 Bulaksumur Yogyakarta 55281, Indonesia *Corresponding Author: [email protected] 2 Abstract To obtain high purity glucomannan extracted from porang corm (Amorphophallus muelleri Blume), an attempt was made to enzymatically hydrolyse the starch which is considered as impurity. Purity of glucomannan has great influence to its physicochemical properties. Starch hydrolysis was carried out simultaneously with extraction of glucomannan. The objective of the work was to study the effect of various factors, namely stirring speed, solid to liquid ratio and the amount of enzyme added on the hydrolysis process. The experiment was started by heating phosphate buffer solution to the desired temperature and then adding certain amount of amylase. The porang flour was then added into the solution and this time was considered as the starting time of hydrolysis. Samples was taken at different time during the hydrolysis and analysed for their sugar content. The result showed that all variable studied give remarkable effect on the reducing sugar liberated during the process. By increasing the stirring speed, the solid to liquid ratio and the amount of enzyme added, the amount of reducing sugar increased. Increasing solid to liquid ratio by 3 fold (3.33 g/L to 10 g/L) has increased the sugar produced by 4.6, while increasing the stirring speed from 400 rpm to 600 rpm only increased the reducing sugar concentration by 1.52 times and increasing the amount of enzymes added by 4 fold (5 mL to 20 mL) only resulted in 1.24 times higher of sugar produced. This indicates that solid/liquid ratio give more significant effect in enzymatic hydrolysis of starch in porang compared with stirring speed and the amount of enzymes do. Keywords: Glucomannan purification, Starch, Alpha amylase, Reducing sugar. 1 2 Fadilah et al. Abbreviations EFSA FDA TCM USDA European Food Safety Authority Food and Drug Administration Traditional Chinese Medicine US Department of Agriculture 1. Introduction Among natural biopolymers, glucomannan has received a great interest for various important purposes. It has been used as TCM for thousands of years for treatment of asthma, cough, hernia, breast pain, burns and skin disorders [1]. Currently, clinical studies show that glucomannan has ability to lower blood sugar, lower blood cholesterol, helping weight loss and promote healthy micro flora in intestinal [2]. Glucomannan is also used as emulsifier and stabilizer for foods, drinks, and cosmetics products for its unique rheological and gelling properties [1]. The use of glucomannan as food additive had been approved in USA by FDA in 1994 and by USDA in 1996. Glucomannan is also authorized in Europe by given an E425 agreement number by EFSA [1]. In pharmaceutical area, glucomannan is used in drug delivery system due to its biodegradability and good gel-forming ability [3, 4]. Glucomannan is a neutral polysaccharides composed mainly of ß,1-4 linked D-mannose and D-glucose with molar ratio of 1.6:1. The backbone is lightly branched, which short side branches at the C-3 position of the mannoses. Some acetyl groups randomly present at the C-6 position of the sugar units [5]. This acetyl groups, which is believed to contribute to the solubility and gelling properties are located every 9 to 19 sugar units. Glucomannan have unique properties. Its 1% solution has high viscosity, i.e., 30,000 cP, which is the highest among 12 polysaccharides tested [6]. This relates to its high water absorbance (100 g of water per g of glucomannan), and its high molecular weight, 105 – 106. Glucomannan can be extracted from many botanical sources, but in large quantity it could be only from the tuber of Amorphophallus sp. This perennial herb is native to East Asia and belongs to the family of Araceae. As source of glucomannan, Porang (Amorphophallus muelleri Blume) is cultivated in Indonesia, as secondary crops under the teak, mahogany or sonokeling plantation [7]. In recent days, glucomannan can be extracted from the corms of Amorphophallus sp. either by dry or wet processing method. Dry processing method involves mechanical means in which the dried slice corms is grounded and then purified via wind shifting or sieving. For its low quality, the product of dry processing method have used in food industry. Product with higher quality can be obtained by wet processing method. This method includes ethanol isolation [8], use of aluminum sulphate solution [9], water extraction [8] and enzymatic processing [10, 11]. Chua et al. [12] and Sugiyama [8] have conducted glucomannan extraction at room temperature in relatively long time (three hours) to avoid gelatinization of starch, which may entrained to glucomannan extract. To enhance the glucomannan yield and to shorten the extraction time, it is needed to carry out the extraction at higher temperatures. The gelatinization of the starch could be overcome by hydrolysing it with amylase so the hydrolysate can be easily Journal of Engineering Science and Technology Special Issue 6 1/2015 Hydrolysis of Starch in Porang Flour Using Alpha Amylase 3 separated from the extracted glucomannan. Fadilah et al. [13] reported that using commercial amylase commonly used in glucose factory was not appropriate for this purpose. Commercial amylse may contain mannanase that would cleavage the glucomannan chain. The use of amylase that free from mannanase is then preferable. This work deals with simultaneous glucomannan extraction and starch hydrolysis by amylase, especially focusing on the influence of time, stirring speed, solid to liquid ratio and the amount of enzyme added on the hydrolysis of starch in porang flour. 2. Materials and Methods 2.1. Materials Porang flour was prepared following the method used by Fadilah et al. [13]. Alpha amylase from Sigma (A 3403 Bachillus licheniformis) was diluted to 500 U/mL. Phosphate buffer solutions containing Na2HPO4 and NaH2PO4 at pH 6 used as medium for carrying out the simultaneous glucomannan extraction and enzymatic hydrolysis of starch. Other chemicals used were 96% ethanol and 0.1 N HCl solutions. 2.2. Hydrolysis process The hydrolysis processes were carried out according to the procedure followed by Fadilah et al. [14] except for the treatment of the samples. At a certain time interval, 100 ml of sample was taken out. An amount of 12.5 mL of this sample was then added with 12.5 mL of 0.1 N HCl to stop the hydrolysis. All samples were then centrifuged at 4000 rpm for 5 minutes. The reducing sugar content was analysed using Nelson-Somogyi method with maltose used as the standard. To study the influence of the solid to liquid ratio (mass of porang per volume of solution), the experiments were conducted by keeping the stirring speed at 500 rpm, with the amount of enzyme of 20 mL, at temperature of 70 °C and solid to liquid ratio were 3.33, 6.67 and 10 g/L. The influence of stirring speed were conducted by carrying out the experiments with solid to liquid ratio was 10 g/L at the temperature of 70 °C with stirring speed varied at 400, 500 and 600 rpm. Experiments was also conducted by varying amount of enzyme added by conducting the experiments with solid to liquid ratio was 10 g/L by keeping the stirring speed at 500 rpm, at the temperature of 70 °C and with the amount of enzyme added were 5, 10 and 20 mL. 3. Results and Discussion During the process, it was observed that the starch granules took up water and swelled. The starch underwent gelatinization. It is expected that the shearing effect of stirring will remove the gelatinized outer layer and these long chained starch molecules dissolved into solution [15]. Thus, hydrolysis will occur. At this stage, amylase cleaves randomly the inner part of the starch molecule as it is an endo type enzyme. Dextrines would be formed in the beginning, and as the process continues the maltoses will accumulate, in which one of the molecules of glucose has a free glucoside group and hence has reducing properties [16]. Journal of Engineering Science and Technology Special Issue 6 1/2015 4 Fadilah et al. The experimental results of reducing sugar liberated during starch hydrolysis by amylase at various solid to liquid ratio are shown in Fig. 1. As seen, higher solid to liquid ratio produces higher initial rate (indicated by steeper slop of the profile) and higher reducing sugar concentration. This fact may be related to the quantity of the starch available to be hydrolysed. As the reaction rate is proportional to the concentration of substrates, the higher the concentration of starch the faster the reaction. 0.9 0.8 3.33 g/L 6.67 g/L 20 40 10 g/L reducing sugar, g/L 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 0 60 time, minutes 80 100 120 Fig. 1. Reducing sugar liberated during hydrolysis of starch in porang flour at various solid to liquid ratio (70 °C, 500 rpm, 20 mL enzymes). As noticed, reducing sugar for all solid to liquid ratios increased rapidly during the first 30 minutes of hydrolysis then decreased drastically before it slowly increased again. The profile tended to reach constant value after 80 minutes. This winding curve differs from the results obtained by Kolusheva and Marinova [16] and Sunaryanto et al. [17] which the profile of reducing sugar released formed curves that constantly increase before it reached a constant value. This phenomenon is still under investigation. The highest concentration of reducing sugar obtained from different solid to liquid ratios was 0.606 g/L, 0.198 g/L and 0.131 g/L from the solid to liquid ratios of 10 g/L, 6.67 g/L and 3.33 g/L respectively. It is indicated that increasing production of reducing sugar at solid to liquid ratio 10 g/L was 3 times higher compared with that at 6.67 g/L and 4.6 times higher compared with that at 3.33 g/L. Figure 2 shows the influence of stirring speed on the reducing sugar liberated during the hydrolysis. Increasing the stirring speed has increased the amount of liberated reducing sugar. It means that the enzymatic reaction was faster in the higher stirring speed. Highest concentration of reducing sugar obtained from different stirring speed was 0.775 g/L, 0.645 g/L and 0.51 g/L from the stirring speeds at 600 rpm, 500 rpm and 400 rpm. The increasing of reducing sugar liberated at 600 rpm was 1.2 times higher compared to at 500 rpm and 1.52 times higher compared to at 400 rpm. This phenomenon can be attributed to the higher Journal of Engineering Science and Technology Special Issue 6 1/2015 Hydrolysis of Starch in Porang Flour Using Alpha Amylase 5 turbulence when the stirring speed increases, in which dissolution of gelatinized starch increase too. Higher turbulence also means better contact between the enzymes and the substrates. This leads to the higher products of reaction. 0.9 0.8 reducing sugar, g/L 0.7 0.6 0.5 0.4 0.3 0.2 0.1 400 rpm 500 rpm 600 rpm 0 0 20 40 60 80 time, minutes 100 120 Fig. 2. Reducing sugar liberated during hydrolysis of starch in porang flour at various stirring speed (Solid to liquid ratio 10 g/L, 20 mL enzyme , 70 OC). The influence of amount of amylase added can be seen in Fig. 3. Again the same phenomenon of winding curves was observed. As seen in Fig. 3, higher reducing sugar released at higher enzyme concentration. Highest reducing sugar liberated during hydrolysis obtained from different amount of enzyme added were 0.52 g/L, 0.55 g/L and 0.65 g/L from the amount of enzyme added were 5 mL, 10 mL, and 20 mL respectively. Increasing the amount of enzyme added from 5 mL to10 mL only increased the reducing sugar 1.05 times, and increasing the amount of enzyme from by 4 fold (5 mL to 20 mL) only increased the reducing sugar 1.24 times. More enzymes gave more site for substrate to form enzyme-substrate complex, so enhanced the reaction. From the three variables studied affecting the hydrolysis, solid to liquid ratio, i.e., the concentration of substrates, was more pronounced than two others. Ingesson et al. [18] in their study also found similar results that the conversion of cellulose was more affected by the substrate rather than shaking regime employed. Sunaryanto et al. [17] studied the effect of different sago starch concentration on the liquefaction using alpha amylase and reported that increasing substrate concentration produced more reducing sugar but at very high concentration less reducing sugar produced. The increasing of stirring speed and the amount of enzyme has less effect to hydrolysis. This may be due to the high viscosity of the solution as the starch hydrolysis conducted simultaneously with glucomannan extraction. The presence of extracted glucomannan made the solution very viscous. This viscous media likely restricted the mobility of the enzyme thus affect the interaction of substrateenzyme and hence reduced the product reaction. Journal of Engineering Science and Technology Special Issue 6 1/2015 6 Fadilah et al. 0.8 0.7 reducing sugar, g/L 0.6 0.5 0.4 0.3 0.2 0.1 5 mL 10 mL 20 mL 0 0 20 40 60 time, minutes 80 100 120 Fig 3. Reducing sugar liberated during hydrolysis of starch in porang flour at various amount of Amylase added (Solid to liquid ratio 10 g/L, 500 rpm, 70oC). Starch content in the porang flour was 12.28% (w/w). With solid to liquid ratio 10 g/L, the concentration of the starch was 1.228 g/L. The highest reducing sugar concentration obtained with this solid to liquid ratio was 0.775 g/L. with stirring speed at 600 rpm and the amount of enzyme added was 20 mL. This amount of enzyme is equal to 10,000 U. This enzyme dosage seem higher than used by Kolusheva et al. [16], which was used 1,800 U for concentration of starch 250 g/L. Higher enzyme dosage was needed to ensure the starch hydrolysis run well as it carried out in viscous solution. 4. Conclusions Starch in porang flour hydrolyzed using amylase and the hydrolysis rate and yield were influenced by stirring speed, amount of enzymes and ratio of solid to liquid. Increasing the stirring speed, amount of enzyme and ratio of solid to liquid increased the production of reducing sugar. The conversion of starch was more affected by the ratio of solid to liquid, i.e., the concentration of substrates, rather than stirring speed and the amount of enzymes. Triplicating the ratio of solid to liquid from 3.33 g/L to 10 g/L increased the reducing sugar 4.6 times higher, while increasing the stirring speed from 400 rpm to 600 rpm only increased the reducing sugar concentration by 1.5 times and increasing the amount of enzymes added by 4 fold times only gave 1.24 times higher. Acknowledgement The authors would like to acknowlegde The Directorate General of Higher Education, Indonesia, for financial support of this work through scholarship of doctorate program (BPPS) at Gadjah Mada University to Fadilah and the research Journal of Engineering Science and Technology Special Issue 6 1/2015 Hydrolysis of Starch in Porang Flour Using Alpha Amylase 7 grant Hibah Penelitian Disertasi Doktor atau Doktor Baru (PDDB) PNBP 2014 Sebelas Maret University. References 1. 2. 3. 4. 5. 6. 7. 8. 9. 10. 11. 12. 13. Chua, M.; Baldwin, T.C.; Hocking, T.J.; and Chan, K. (2010). Traditional uses and potential health benefits of Amorphophallus konjac K. Koch ex NE Br. Journal of Ethnopharmacology, 128(2), 268-278. Yao-ling, L.; Rong-hua, D.; Ni, C.; Juan, P.; and Jie, P. (2013). Review on Konjac Glucomannan: Isolation, structure, chain conformation and bioactivities. Journal of Single Molecule Research, 1(1), 7-14. Zhang, Y.; Xie, B.J.; and Gan, X. (2005). Advance in the applications of Konjac Glucamannan and its derivatives. Carbohydrate Polymers, 60, 27-31. Alonso-Sande, M., Teijeiro-Osorio, D., Remuñán-López, C., & Alonso, M.J. (2009). Glucomannan, a promising polysaccharide for biopharmaceutical purposes. European Journal of Pharmaceutics and Biopharmaceutics, 72(2), 453-462. Katsuraya, K.; Okuyama, K.; Hatanaka, K.; Oshima, R.; Sato, T.; and Matsuzaki, K. (2003). Constitution of konjac glucomannan: chemical analysis and 13 C NMR spectroscopy. Carbohydrate polymers, 53(2), 183-189. Yaseen, E.I.; Herald, T.J.; Aramouni, F.M.; and Alavi, S. (2005). Rheological properties of selected gum solutions. Food Research International, 38(2), 111-119. Perum Perhutani (2013). Retrieved at August 29, 2013, from http://perumperhutani.com/2013/02/kembangkan-tanaman-porang-perhutaniterapkan-sistem-bagi-hasil/. Sugiyama, N.; Shimahara, H.; and Andoh, T. (1972). Studies on mannan and related compounds. I. The purification of konjac mannan. Bulletin of the Chemical Society of Japan, 45(2), 561-563. Tatirat, O.; and Charoenrein, S. (2011). Physicochemical properties of konjac glucomannan extracted from konjac flour by a simple centrifugation process. LWT-Food Science and Technology, 44(10), 2059-2063. Wootton, A.N.; Luker‐Brown, M.; Westcott, R.J.; and Cheetham, P.S. (1993). The extraction of a glucomannan polysaccharide from konjac corms (elephant yam, Amorphophallus rivierii). Journal of the Science of Food and Agriculture, 61(4), 429-433. Khanna, S.; and Tester, R.F. (2006). Influence of purified konjac glucomannan on the gelatinisation and retrogradation properties of maize and potato starches. Food Hydrocolloids, 20(5), 567-576. Chua, M.; Chan, K.; Hocking, T.J.; Williams, P.A.; Perry, C.J.; and Baldwin, T.C. (2012). Methodologies for the extraction and analysis of konjac glucomannan from corms of Amorphophallus konjac K. Koch. Carbohydrate Polymers, 87(3), 2202-2210. Fadilah; Rochmadi; Syamsiah, S.; and Haryadi. (2013). Investigation of mannanase activity in commercial a-amylase: preliminary research on purification of glucomannan from porang (Amorphophallus muelleri Blume). Proceeding of Regional Symposium on Chemical Engineering 2013, Bohol, Phillippines. Journal of Engineering Science and Technology Special Issue 6 1/2015 8 Fadilah et al. 14. Fadilah; Rochmadi; Syamsiah, S.; and Haryadi. (2014). Simple kinetic model for extraction of glucomannan from porang (Amorphophallus muelleri Blume). International Proceedings of Chemical, Biological & Enviromental Engineering, Chemical Engineering and Applications V, 74, 11-15. 15. Davey, M.J.; Landman, K.A.; McGuinness, M.J.; Wellington, N.E.W.; and Jin, H.N. (2002). Mathematical modelling of rice gelatinisation and dissolution in beer production. AIChE Journal, 48(8), 1811-1826. 16. Kolusheva, T.; and Marinova, A. (2007). A study of the optimal conditions for starch hydrolysis through thermostable α-amylase. Journal of the University of Chemical Technology and Metallurgy, 42(1), 93-96. 17. Sunaryanto, R.; Handayani, B.H.; and Safitri, R. (2013). Enzymatic and acid hydrolysis of sago starch for preparation of ethanol production. Microbiology Indonesia, 7(2), 68-74. 18. Ingesson, H.; Zacchi, G.; Yang, B.; Esteghlalian, A.R.; and Saddler, J.N. (2001). The effect of shaking regime on the rate and extent of enzymatic hydrolysis of cellulose. Journal of Biotechnology, 88(2), 177-182. Journal of Engineering Science and Technology Special Issue 6 1/2015
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