Moisture Sorption Isotherm Characteristics of Taro Flour

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World Journal of Dairy & Food Sciences 5 (1): 01-06, 010 ISSN 1817-308X IDOSI Publications, 010 Moisture Sorption Isotherm Characteristics of Taro Flour 1 Budi Nurtama and Jenshinn Lin 1 Department of Tropical Agriculture and International Cooperation, National Pingtung University of Science and Technology, Pingtung 9101, Taiwan Department of Food Science, National Pingtung University of Science and Technology, Pingtung 9101, Taiwan Abstract: It is very important to control moisture content of food during processing and storage since water has many roles in food reactions and food quality. Knowledge of sorption isotherm has a great importance in food dehydration. Taro (Colocasia esculenta L. Schott) is one of important sources of carbohydrate in Africa and Asia. The fresh taro, which has high moisture content, can be kept only within a few weeks after harvest. Processing the corms by drying and changing into flour is one solution for easy handling and long-term storage. Moisture sorption isotherm information is clearly needed for processing of taro flour. However, the published literature about the sorption isotherms of taro flour is limited. The objectives of this work were (a) to obtain data on adsorption and desorption isotherms of taro flour at 18, 5 and 35 C; and (b) to evaluate three sorption isotherm models (BET, GAB and DLP models). It was concluded that the sorption isotherms had sigmoid-shape profiles. The hysteresis effects of the sorption isotherms at the three temperatures were distinctly expressed. The Double Log Polynomial (DLP) model was the most appropriate model for the sorption isotherms of taro flour. Key words:moisture sorption isotherm Mathematical modeling Hysteresis Taro (Colocasia esculenta L. Schott) INTRODUCTION modified Halsey equations were the adequate models. Using the previously published data, the adequacy of Controlling of food moisture content during ERH models for high-starch products were evaluated. processing and storage is very important since water The Guggenheim-Anderson-de Boer (GAB) model was has many roles in food reactions and food quality. not adequate and a simplified linear empirical model Al-Muhtaseb [1] stated that the knowledge of was developed to describe the sorption data. According sorption isotherm is an extremely important tool in to K aymak-ertekin and Gedik [3], the Halsey, GAB, food dehydration, especially to predict the shelf life of Oswin and modified Halsey equations are suitable for dried foods. Modeling for water sorption isotherms has representing the sorption behaviour of potatoes a special interest for many aspects of food preservation, containing high starch. Their results showed a good including the thermodynamic functions of the water agreement with the results of McLaughlin and Magee [4]. absorption. Samapundo et al. [5] studied the adsorption and There were many studies on moisture sorption desorption isotherms of yellow dent corn at 5, 30 and isotherms of foods over the last two decades. Some of 37 C. The isotherms showed Type II behaviour and the these works were related to the determination of equilibrium moisture content decreased with increase in moisture sorption isotherms and others were related to temperature. The GAB model was the best fit model for the mathematical modeling to represent the moisture the experimental data. The isosteric heat of sorption was sorption isotherms. The Equilibrium Relative Humidity found to decrease with increase in moisture content. (ERH) and Equilibrium Moisture Content (EMC) of sweet Oyelade et al. [6] constructed adsorption and desorption potato slices at five temperatures were investigated by (sorption) moisture isotherms for yam flour at the Chen []. It was found that the modified Oswin and temperature of 7, 3, 37 and 40 C, in the water activity Corresponding Author: Jenshinn Lin, Department of Food Science, National Pingtung University of Science and Technology, Pingtung 9101, Taiwan. E-mail: jlin@mail.npust.edu.tw 1

World J. Dairy & Food Sci., 5 (1): 01-06, 010 (a ) range of 0.10 0.80. There were significant effects of w temperature on the isotherms which appeared sigmoid. Five widely recommended three parameters sorption models were fitted to the data and desorption isotherms appeared well fitted than adsorption isotherms. The modified Oswin model described the sorption characteristics of yam flour better than other models. Taro (Colocasia esculenta L. Schott) can be considered as one of important sources of carbohydrate for people in Africa and Asia [7, 8]. The fresh corms, which have high moisture content, must be consumed within a few weeks after harvest. It has to be dried to lower moisture content and processed into flour for easy and long-term storage. Therefore, moisture sorption isotherm information is required for drying and storing of taro flour. However, the published literature about the sorption isotherms of taro flour is limited. The objectives of this work were (a) to obtain data on adsorption and desorption isotherms of taro flour at 18, 5 and 35 C; and (b) to compare fittings of three sorption isotherm models (BET, GAB and DLP models). MATERIALS AND METHODS Taro Flour Preparation: Fresh taro was purchased from a local farmer in Kaohsiung and kept in an open paper bag at room temperature for 3 days prior to their use. After washing, peeling and slicing, taro was dried using a hot air dryer at 45 C for 1 hours [9]. The dried taro was milled using a lab use grinder to make taro flour. Samples used in the experiment were taro flour 40 mesh. Figure 1 shows the steps in the preparation of taro flour. Measurement of Sorption Isotherm [10, 11]: Moisture Analyzer MX-50 was used to determine the moisture contents of taro flour samples immediately before measuring the sorption isotherms of the taro flour. A sample of 5 g was placed in the sample dish and the temperature was set up at 105 C. Three replications were done for each isotherm temperature. The average values of the moisture contents, which were calculated in % dry basis, were used in analyzing data of the sorption isotherms. AquaSorp Isotherm Generator (Decagon Devices, Inc., Pullman, Washington, USA) was used to construct moisture sorption isotherms of taro flour at 18, 5 and 35 C. The Aquasorp creates isotherms using a water activity and gravimetric analysis method called Dynamic Dewpoint Isotherm (DDI). Samples used in each temperature were ± 700 mg. The instrument was set up as m = m = Fresh Taro Washing awmoc 1 a [1 a c 1 ] ( ) + ( ) w Peeling Slicing Hot air drying (45 C, 1 hrs) Milling Sieving Taro flour Fig. 1: The processing steps in preparation of taro flour followed: range of a w was 0.10-0.85, adsorption minimum, total sorption = (adsorption and desorption) and pump flow rate 300 ml/min. The software for data analysis is TM SorpTrac Version 1.14 for AquaSorp Isotherm Generator. There were three sorption isotherm models: Brunauer- Emmett-Teller (BET), Guggenheim-Anderson-de Boer (GAB), Double Log Polynomial (DLP) models that were evaluated. The equations of the three models are as follows: (1) BET equation: Where m is the moisture in g/100 solids or g/g solids at water activity aw and mo is the monolayer value in the same units. The constant c is calculated by: Q s w c = exp RT Where Q is the surface interaction energy in J/mole, s R is the gas constant (8.314 J/mol K) and T (K) is the temperature. () GAB equation: m k ca o b w ( 1 k a )( 1 k a + k ca ) b w b w b w Where m is the moisture in g/100 solids or g/g solids, kb is a constant in the range of 0.70 to 1 and c is a constant in the range of 1 to 000. In addition, mo is the monolayer moisture content in the same units as m and a w is the water activity at moisture m.

World J. Dairy & Food Sci., 5 (1): 01-06, 010 (3) DLP equation: 5.67±0.03% for 18, 5 and 35 C, respectively. The moisture sorption isotherms had sigmoid-shape profiles 3 m = b3 + b + b1 + b0 for all of the three temperatures which were similar with yam flour [6]. The hysteresis effects at the three Where m is the moisture in g/100 solids or g/g temperatures were distinctly expressed. The increasing solids, =ln[-ln(a w)] and b 0 b3 are empirical constants. temperatures resulted in the less hysteresis effect on The software fitted the generated sorption isotherm taro flour which meant the adsorption and desorption data into the three models and calculated the coefficients curves were closer. of equations, standard errors (SE) and coefficient of Table 1 listed the results of the coefficients of determinations (R ) for each model at the three equations, standard errors (SE) and coefficient of temperatures. determinations (R ) for BET, GAB and DLP models of taro flour at 18, 5 and 35 C. The three models had low SE RESULTS AND DISCUSSION values (less than or close to 0.50) and high R values (higher than 0.9). Thus, it can be concluded that the three Figures, 3 and 4 showed the adsorption and models were well fitted for the sorption isotherms of taro desorption isotherms of taro flour at 18, 5 and 35 C, flour. However, SE values of the GAB model were higher respectively. The data points for each adsorption and than the other two models. It should also be noted that desorption curve were generated by the Aquasorp the BET equation is generally applicable up to a w value of during the measurement of sorption isotherms. The 0.45-0.50 [10]. Therefore, the DLP model could be moisture contents of taro flour, in % dry basis, measured considered as the most appropriate model for the moisture before isotherm testing were 7.86±0.11, 6.00±0.13 and sorption isotherms of taro flour. 30.00 5.00 0.00 15.00 10.00 5.00 Adsorption Desorption 0.00 0.000 0.00 0.400 0.600 0.800 1.000 Water activity (a w ) Fig. : Sorption isotherm of taro flour at 18 C Adsorption Desorption 30.00 5.00 0.00 15.00 10.00 5.00 0.00 0.000 0.00 0.400 0.600 0.800 1.000 Water activity (a w ) Fig. 3: Sorption isotherm of taro flour at 5 C 3

World J. Dairy & Food Sci., 5 (1): 01-06, 010 30.00 5.00 0.00 15.00 10.00 5.00 Adsorption Desorption 0.00 0.000 0.00 0.400 0.600 0.800 1.000 Water activity (a w ) Fig. 4: Sorption isotherm of taro flour at 35 C 30 5 0 15 10 5 18 deg C 5 deg C 35 deg C 0 0.0 0. 0.4 0.6 0.8 1.0 Water activity a w ( ) Fig. 5: Adsorption isotherms of taro flour based on DLP model at 18, 5 and 35 C 30 5 0 15 10 5 18 deg C 5 deg C 35 deg C 0 0.0 0. 0.4 0.6 0.8 1.0 Water activity a w) ( Fig. 6: Desorption isotherms of taro flour based on DLP model at 18, 5 and 35 C Figure 5 and 6 showed the adsorption and desorption isotherm curves of taro flour based on DLP model, respectively. In general, the moisture content decreased with increase in temperature which agreed with the results of Samapundo et al. [5] and Oyelade et al. [6]. For the adsorption isotherms (Figure 5), the curves closed each other as water activity increased especially at a w value higher than 0.60. While the desorption isotherms in figure 6 showed that the 18 C curve was separated from the other two curves. 4

World J. Dairy & Food Sci., 5 (1): 01-06, 010 Table 1: Coefficients, standard errors (SE) and coefficient of determinations (R ) of the sorption isotherm models for taro flour Adsorption Desorption ------------------------------------------------------------------ ----------------------------------------------------------------------- Temp Model Coefficients SE R Coefficients SE R 18 C BET c: 85.9989 0.05 0.996 c: 7.4508 0.04 0.999 m o: 3.981 m o: 5.519 GAB c: 34.0454 0.5 0.998 c: 11.4165 0.53 0.994 k b: 0.983 k b: 0.901 m o: 4.160 m o: 6.4713 DLP b : 6.0048 0.16 0.999 b : 7.7315 0.37 0.997 0 0 b : -3.8918 b : -6.464 1 1 b :.4653 b : 3.1883 b : -0.65 b : 0.5740 3 3 5 C BET c: 6.0463 0.03 0.998 c: 15.0891 m o: 3.5764 m o: 4.9338 0.03 0.999 GAB c: 8.701 0.3 0.997 c: 8.6190 0.38 0.996 k b: 0.9845 k b: 0.938 m o: 4.86 m o: 5.8703 DLP b : 5.1 0.14 0.999 b : 6.9193 0.8 0.998 0 0 b : - 4.3796 b : -6.038 1 1 b :.84 b :.706 b = - 0.4017 b : 0.1056 3 3 35 C BET c: 11.8095 0.08 0.990 c: 7.8585 0.05 0.998 m o: 3.660 m o: 4.7046 GAB c: 5.556 0.5 0.998 c: 4.1109 0.48 0.995 k b: 0.975 k b: 0.9167 m o: 4.4196 m o: 6.517 DLP b : 4.974 0.09 1.000 b : 5.9699 0.31 0.998 0 0 b : - 4.77 b : -6.63 1 1 b :.6386 b : 3.943 b : - 0.3789 b : 0.4896 3 3 Tabel : Predicted moisture content values (m) of taro flour using DLP model at different water activities (a ) w Temperature ------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------- 18 C 5 C 35 C --------------------------------------------------- --------------------------------------------------------- ----------------------------------------------------- aw m adsorption (% db) m desorption (% db) m adsorption (% db) m desorption (% db) m adsorption (% db) m desorption (% db) 0.10 4.11 4.9 3.30 3.83.65 3.0 0.60 9.9 13.31 9.56 1.16 9.45 11.76 0.80 19.50.61 19.50 1.70 19.7 1.66 0.85 4.97 6.49 4.91 6.18 4.54 5.94 The values of the predicted moisture contents of expressed. The Double Log Polynomial (DLP) model was taro flour at four values of water activities were listed the most appropriate model for the sorption isotherms of in Table. The best model, the DLP equation, was used taro flour. The increasing temperature in adsorption and to calculate the moisture contents of adsorption and desorption isotherms showed decreasing in moisture desorption at the three temperatures. Most foods can not content at a given water activity support growth of microorganisms at a w less than 0.60 and mold growth at a w equal to 0.80 [10]. ACKNOWLEDGEMENTS It was concluded that the moisture sorption isotherms of taro flour at 18, 5 and 35 C had sigmoid- The first author wishes to thank the Democratic shape profiles. The hysteresis effects of the sorption Pacific Union (DPU) for granting Ph.D. Scholarship and isotherms at the three temperatures were distinctly National Pingtung University of Science and Technology 5

World J. Dairy & Food Sci., 5 (1): 01-06, 010 (NPUST) for giving an opportunity to take Ph.D. degree. 7. Masalkar, S.D. and B.G. Keskar, 1998. Other roots, The assistance and support of Dr. Jenshinn Lin and his tubers and rhizomes. In Handbook of Vegetable students are greatly acknowledged. Science and Technology: Production, Composition, REFERENCES Storage and Processing, Eds., Salunkhe, D.K. and S.S. Kadam. New York: Marcel Dekker, Inc., pp: 151-155. 1. Al-Muhtaseb, A.H., W.A.M. McMinn and 8. Onwueme, I., 1999. Taro Cultivation in Asia and the T.R.A. Magee, 00. Moisture Sorption Isotherm Pacific. FAO Regional Office for Asia and the Pacific, Characteristics of Food Products: A Review. Food pp: 4. and Bioproducts Processing, 80(): 118-18. 9. Nurtama, B., J. Lin and H.H. Chen, 009.. Chen, C., 00. Sorption Isotherms of Sweet Potato Mathematical Modelling of Low Temperature Slices. Biosystems Engineering, 83(1): 85-95. Drying of Taro (Colocasia esculenta L. Schott). J. 3. Kaymak-Ertekin, F. and A. Gedik, 004. Sorption Intl. Cooperation, 4(): 136-144. isotherms and isosteric heat of sorption for 10. Bell, L.N. and T.P. Labuza, 000. Moisture Sorption: grapes, apricots, apples and potatoes. Lebensmittel- Practical Aspects of Isotherm Measurement and Wissenschaft und-technologie, 37(4): 49-438. Use. St. Paul, USA: American Association of Cereal 4. McLaughlin, C.P. and T.R.A. Magee, 1998. The Chemists, Inc. pp: 49-5. Determination of Sorption Isotherm and the Isosteric 11. Decagon Devices, Inc., 007. Moisture Sorption Heats of Sorption for Potatoes. J. Food Engineering, Isotherm Generator: Operator s Manual. Version 3.0. 35(3): 61-80. Pullman, Washington, USA: Decagon Devices, Inc. 5. Samapundo, S., F. Devlieghere, B. De Meulenaer, pp: 8-84. A. Atukwase, Y. Lamboni and J.M. Debevere, 007. Sorption isotherms and isosteric heats of sorption of whole yellow dent corn. J. Food Engineering, 79(1): 168-175. 6. Oyelade, O.J., T.Y. Tunde-Akintunde and J.C. Igbeka, 008. Predictive equi-librium moisture content equations for yam (Dioscorea rotundata, Poir) flour and hysteresis phenomena under practical storage conditions. J. Food Engineering, 87(): 9-35. 6