نوع مقاله : مقاله پژوهشی

نویسندگان

• جلال دهقان نیا
• حامد باقری درویش محمد
• بابک قنبرزاده

دانشگاه تبریز

چکیده

مدل‌سازی فرآیند سرخ کردن در جهت آگاهی از روابط بین متغییرهای مختلف، می‌تواند گامی مناسب در جهت بهبود کیفیت محصول باشد. در این پژوهش، اثر پیش‌تیمار اولتراسوند تحت فرکانس‌های 28 و 40 کیلوهرتز به‌مدت 15 دقیقه و پیش‌تیمار مایکروویو با توان‌های 3 و 6 وات بر گرم به‌مدت 10 دقیقه بر میزان رطوبت سیب‌زمینی سرخ‌شده در درجه حرارت‌های 150، 170 و 190 درجه سانتی‌گراد به‌مدت 60، 120، 180 و 240 ثانیه موردبررسی قرار گرفت. برازش داده‌های تجربی افت رطوبت نمونه‌ها در طی فرآیند سرخ کردن با استفاده از شش مدل تجربی پیشنهادی و قانون فیک انجام شد. نتایج نشان داد که هر دو پیش‌تیمار اولتراسوند و مایکروویو در کلیه سطوح مورداستفاده، میزان رطوبت نهایی نمونه‌ها را به‌طور معنی‌داری در سطح احتمال 5 درصد کاهش دادند. همچنین، با افزایش دما، میزان رطوبت نمونه‌های سیب‌زمینی به‌شکل غیرمعنی‌دار در سطح احتمال 5 درصد کاهش یافت. از طرف دیگر، با افزایش زمان فرآیند، میزان رطوبت نمونه‌ها به‌طور معنی‌دار و به‌صورت نمایی کاهش پیدا کرد. همچنین، مدل‌های پیشنهادی در این پژوهش، با داشتن ضریب تبیین بالا (2R( و ریشه میانگین مربعات خطا (RMSE) پایین، به‌خوبی داده‌های تجربی را برازش نمودند. ضریب انتشار مؤثر رطوبت برای نمونه‌های مختلف در دامنه 8-10×57/3 الی 8-10×08/11 مترمربع بر ثانیه به‌دست آمد. اعمال پیش‌تیمارهای اولتراسوند و مایکروویو موجب افزایش ضریب انتشار مؤثر رطوبت و کاهش انرژی فعال‌سازی نمونه‌ها شدند.

کلیدواژه‌ها

• ضریب انتشار مؤثر رطوبت
• مدل تجربی
• محتوای رطوبت

عنوان مقاله [English]

Moisture Loss Kinetics Modeling during Deep-Fat Frying of Potato Strips Pretreated with Ultrasound and Microwave

نویسندگان [English]

• Jalal Dehghan nia
• Hamed Bagheri-Darvish-Mohammad
• Babak Ghanbarzadeh

University of Tabriz

چکیده [English]

Introduction: Deep-fat frying is a process of cooking foods through immersing them in edible oils at temperatures above the boiling point of water (150-200°C). During this complex unit operation, heat and mass transfer occur simultaneously.During frying, heat is transferred from edible oil to surface of the food and then transferred into it and at the same time, moisture is transferred from inside the food to outside.As a result of these phenomena and by continuing the process, food temperature increases and its moisture content decreases. This, in turn, creates favorable characteristics such as color, texture and taste of the product.Moisture content is one of the important features in the quality of fried products.In the frying process, moisture loss from food occurs by the mechanisms of molecular diffusion, capillary flow and pressure driven flow.The driving force of moisture loss is the partial water vapor pressure difference between the inside and the surface of the food product due to turning the water into vapor.Rate of moisture loss from the food during the frying process decreases exponentially with frying time and increases with increasing temperature.For information about therelationshipsbetweenvarious variables during the frying process, moisture loss kinetics modelingcan bea suitable steptowards improving thequality offried products.To our knowledge, there has been no study in literature associated with the effect of ultrasound and microwave on moisture loss during deep-fat frying of foods. This study aimed to evaluate the effect of these waves on moisture loss kinetics during frying of potato strips.

Materials and Methods: Potatoes (Agria variety) were purchased from a local market and kept in a cold room at 0°C. A mixture of sunflower, soy and cottonseed oil (Behshahr Industrial company), was used for frying potato strips.Inthis study, effect ofultrasound pretreatment at frequencies of 28 and 40 kHz for 15 min and microwave pretreatment at powers of 3 and 6 W/g for 10 min on moisture content of the fried potato slices at 150, 170 and 190°C for 60, 120, 180 and 240 s was investigated.The moisture content of the samples was measured by drying them in a convection oven at 105°C until the weight was constant.Moisture loss experimental data during frying were fitted with six empirical models proposed in this study as well as the Fick’s law of diffusion.The effective moisture diffusion coefficient was calculated based on the Fick's law. To calculate the effect of temperature on the effective moisture diffusion coefficient, the Arrhenius equation was used.

Results and Discussion: By increasing frying temperature, moisture content of the potato slices decreased; however the decrease was not significant at a probability level of 5 percent. The positive effect of oil temperature on moisture loss during deep-fat frying of potato strips has been well documented. This is due to the high kinetic energy of water molecules at higher temperatures, leading to a rapid loss of moisture. The moisture loss by diffusion of water molecules as well as the oil uptake during the frying process lead to the formation of cracks in the structure of the solid food. This, in turn, leads to structural damages and significant changes in terms of structural characteristics including porosity.On the other hand, moisture content of the samples significantly decreased in an exponential manner by increasing the process time. Rapid moisture loss in the first moments of frying is associated with the removal of surface moisture. By decreasing surface moisture over time, the rate of moisture loss was reduced accordingly.Results also showed that both the ultrasound and microwave pretreatments at all the studied levels significantly reduced the final moisture content of the samples at a probability level of 5 percent. The difference between the samples pretreated with two ultrasound frequencies of 28 and 40 kHz was not significant (P > 0.05), but with increasing frequency of the pretreatment, the moisture content decreased to a greater extent. Lower final moisture contents of the samples pretreated with ultrasound were probably due to the creation of microscopic channels in the food structure, which may facilitate moisture loss during frying. On the other hand, application of microwave pretreatment at powers of 3 and 6 watts per gram, decreased initial moisture content of the samples by 38 and 80%, respectively. This resulted in significant (P < 0.05) reduction of the final moisture contents of the samples pretreated with microwave. More moisture loss at higher microwave power is probably due to the high intensity of electromagnetic energy as a result of microwave volumetric heating.In addition, the applied modelswerewell fitted toexperimentaldata having high R2 and low RMSE. The effective moisture diffusion coefficient ranged between 3.57×10-8 to 11.08×10-8 m2/s. Results also demonstrated that the effective moisture diffusion coefficient is increased and the activation energy is decreased by implementing the ultrasound and microwave pretreatments.

کلیدواژه‌ها [English]

• effective moisture diffusion coefficient
• Empirical model
• Moisture content