Adieh Anvar; Behzad Nasehi; Mohammad Noshad; Hassan Barzegar
Abstract
In the present study, the effects of addition of quince pomace powder (0- 15%) and water content (25- 35%) on the batter rheological properties, physicochemical characterizes and sensory properties of sponge cake were evaluated. The results showed that increasing substitution of quince pomace increased ...
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In the present study, the effects of addition of quince pomace powder (0- 15%) and water content (25- 35%) on the batter rheological properties, physicochemical characterizes and sensory properties of sponge cake were evaluated. The results showed that increasing substitution of quince pomace increased the viscosity and consistency batter and the dietary fiber, firmness, overall acceptability of cake and reduced the moisture content, and density of cake. Results of RSM based desirability function showed cakes formulated with 12.56% of quince pomace powder and 29.62% of water content had the most and desired physicochemical quality. Total phenol content (7.71 mg/g), iron (0.263 mg/Kg dry weight) and calcium (340 mg/Kg dry weight) of the control sponge cake was improved to 8.32 (mg/g), 0.361 (mg/Kg dry weight) and 1160 (mg/Kg dry weight) in the optimal sponge cake, respectively. SEM results showed the quince powder increased in the number of cavities in the cake's structure and the uniformity of these cavities.
Adieh Anvar; Behzad Nasehi; Mohammad Noshad; Hassan Barzegar
Abstract
In this study, microwave drying conditions of quince pomace optimized with respect to quality attributes (moisture content, color change and consumer acceptance). Response surface methodology (RSM) technique was used to develop models to respond to the microwave power (100, 2000, 300 W), and microwave ...
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In this study, microwave drying conditions of quince pomace optimized with respect to quality attributes (moisture content, color change and consumer acceptance). Response surface methodology (RSM) technique was used to develop models to respond to the microwave power (100, 2000, 300 W), and microwave time (5, 10, 15 min). The models obtained from the responses were adequate and acceptable because the coefficient of determination R2 of the models was relatively high. Microwave power of 200W and microwave time of 8 minutes were concluded as the optimum conditions prior to air-drying at 50°C. To describe the drying process, the experimental data for moisture loss was converted to moisture ratios. The effective moisture diffusivity increased with increase in microwave power and its values varied from 1.83-4.87×10-9 m2/s. Using an exponential expression based on Arrhenius equation the activation energy and was found to be 16.41 W/mm.