Characterization and drying of caja bagasse (Spondias mombin L.) in a tray dryer using a factorial planning (original) (raw)

Kinetic of Drying of Sliced Fruit with Various Pretreatment Using Cabinet Dryer

2013

The objective of this research is to determine the kinetic of drying on sliced fruit with various pretreatments. The cabinet dryer with electric heater was used in this research. The drying temperatures were 50oC, 60oC, and 70oC. The sliced of pineapple, papaya, and snake fruit were used as samples. Pretreatment involved blanching, osmotic drying and add preservative material. The pretreatment of osmotic drying were conducted for reducing the initial moisture content of the fruit. The result showed that drying time of sliced fruit were about 10 to 24 hours. The osmotic drying has effect on reducing the drying rate. The drying rates at constant period for 50oC, 60oC, and 70 oC of papaya, pineapple and snake fruit were 40.72, 50.75, and 74.43%/h; 28.89, 33.99, and 45.90%/h; 23.97, 31.22, and 42.85%/h respectively. Therefore the activation energies of pineapple, papaya, and snake fruit were 6.6-47.2 kJ/mole, 20.3-45.9 kJ/mole, and 23.9-56.4 kJ/mole. The optimal condition for drying fru...

Evaluation of Design Parameters on Drying of Kiwi Fruit

Applied Sciences, 2018

In this study, the drying of kiwi fruit in a convective dryer is examined experimentally. Air velocity, thickness of the slices and drying time are the varied parameters in drying process. In the experimental study, kiwi slices having thickness of 4 and 8 mm are dried in the dryer under the conditions of 45 °C temperature of the drying air, 10% relative humidity and 0.5–1.5 m/s drying air velocity. In addition to the tests, the effects of mentioned drying parameters on drying are analyzed by ANOVA (Analysis of Variance) method to find the contribution rate of each parameter. For this aim, an orthogonal array is arranged by using Taguchi design of experiment method. As the results of experiments and variance analysis, it has been determined that, drying air velocity plays a significant effect on total drying time. The minimum drying time (225 min) is achieved for 1.5 m/s for 4 mm slices, and the maximum drying time (750 min) is achieved for 0.5 m/s for the kiwi sample sliced 8 mm thi...

A Review Paper on Different Drying Methods

International journal of engineering research and technology, 2019

Drying is one of the oldest preservation processes available to the mankind, on that we can track since prehistoric times. In today food market dried foods play an important role in the food supply chain. As for fruits and vegetables it can be estimated that they constitute about 1% of the total drying in the food industry, by large being the grains the most important. The main feature of this process consists on lowering the water content in order to avoid or slow down food spoilage by microorganism. For understanding some common words found are “drying” or “dehydration”, or even “dewatering”. There are various aspects that must be considered when drying small fruits and vegetables, whether for the food and functional food industries. A system which minimizes exposure to light, oxidation and heat, (i.e. high heat 70C and shorter time duration) may help conserve critical bioactive compounds. Natural convection method is normally used to produce quality of agricultural products and r...

A Design for Experimental Drying Apparatus for The Determination of The Impact of The Affecting Factors on The Drying Time and Performance for Fruits

2003

An experimental dryer was locally designed and fabricated in the Agricultural Engineering Department, Faculty of Agriculture, Cairo University for the determination of the impact of the affecting factors on the drying time of fruits due to the continuous variation in drying conditions along the drying period, the continuous changes in the moisture content of the drying fruit and vegetable and hence, the continuous variation in the drying rate during the whole drying process. All these facts make it difficult to determine the volume of air needed for any drying process, the energy requirement for the process, the time duration of the process, and the most suitable values for the affecting factors to accomplish a successful drying process. It was found that it is better to design a special apparatus and utilizing it as a thin layer dryer, in which all the affecting factors can be controlled to give all the variations expected in solar dryers. The experimental drying system employed a blower to force the drying air through a heating unit and then through the drying tray. The experimental apparatus was equipped with an electric balance for continuous recording of the drying tray weight with its fruit content throughout the whole period of drying. This dryer was tested for a period of 24 hours to assure the success of the control of the temperature, relative humidity, velocity of the drying air. After that, the dryer was used for determination of a thin-layer drying rates of fig fruits experimentally under different conditions of the drying air temperature, relative humidity, velocity and initial and final moisture contents of the fruits. The results show the high reliability of the results obtained from the utilization of the designed apparatus when conducting different drying experiments on fig fruits. The results also show that the drying air temperature, the fig fruits initial and final moisture content had the greatest effect on the drying rate of fig fruits followed by the drying air relative humidity. Air velocity had the least effect.

Kinetics and modeling of star fruit (Averrhoa carambola L.) drying in a tray dryer

Acta Scientiarum-technology, 2010

In this work, drying curves were obtained for the star fruit (Averrhoa carambola L.) in a tray dryer. From theses curves, drying rates and diffusivity data were also obtained and semi theoretical models were adjusted. The drying curves were obtained using a tray dryer with temperatures of 50, 60, and 70°C and an air flux of 1.5 m.s -1 . The Page, Henderson & Pabis, and Exponential models were fitted to the experimental data by nonlinear regression. All fitted models presented high determination coefficients (R 2 ). The Page model showed the best fit. It was observed that effective diffusivity, calculated by Fick’s law, increased with temperature.

Kinetic Models for Drying Techniques—Food Materials

Advances in Chemical Engineering and Science

Drying operations can help in reducing the moisture content of food materials for avoidance of microbial growth and deterioration, for shelf life elongation, to minimize packaging and improving storage for easy transportation. Thin-layer drying of materials is necessary to understand the fundamental transport mechanism and a prerequisite to successfully simulate or scale up the whole process for optimization or control of the operating conditions. Researchers have shown that to rely solely on experimental drying practices without mathematical considerations for the drying kinetics, can significantly affect the efficiency of dryers, increase the cost of production, and reduce the quality of the dried product. An effective model is necessary for the process design, optimization, energy integration and control; hence, the use of mathematical models in finding the drying kinetics of agricultural products is very important. The statistical criteria in use for the evaluation of the best model(s) has it that coefficient of determination (R 2 ) has to be close to unity while the rest statistical measures will have values tending to zero. In this work, the essence of drying using thin-layer, general approaches to modeling for food drying mechanisms thin layer drying models and optimization of the drying processes have been discussed.

Analysis of convective drying kinetics of yellow passion fruit bagasse

Acta Scientiarum. Technology, 2013

This study aimed to analyze the convective drying in fixed bed of yellow passion fruit bagasse. Firstly, the initial moisture of the bagasse was determined in stove, at 105 ± 3ºC for 24 hours. In the drying tests, it was collected the bagasse mass values over time, by using a convective dryer, operated at four temperatures (35, 45, 55 and 65ºC) and three air flow speeds at 0.8, 1.0 and 1.3 m s-1. Having the curves of the drying and of drying rates, it was observed that the temperature had a great influence on the bagasse drying, since as the temperature increases, the drying time is shortened, increasing thus the drying rate. The curves of drying and of drying rate were fitted to the models proposed by Page (1949 apud MOTTA LIMA et al., 2003)and Motta Lima et al. (2002), and the models set by Hogdes (1982) and Toffoli (2005 apud SANTOS et al., 2008), respectively. Other mathematical models were also fitted for each drying process, such as: Simple Exponential, Page, Henderson and Pabis, Logarithm, two-term exponential model, and Wang and Singh model. The best model was chosen by analysis of the highest R² and F-test, and the lowest root mean square error.

Drying kinetics of semi-finished cassava crackers: A comparative study

LWT - Food Science and Technology, 2008

Drying kinetics of semi-finished cassava crackers was investigated in this paper using a hot air dryer at seven levels of drying air temperatures in the rage of 50-80 1C, a fixed air flow velocity using a fan speed of 0.18 kW, and a fixed level of thickness at 1.5 mm. A comparative study was performed among mechanistic and empirical models: the diffusion model, Newton model, Page model, Modified Page model, Henderson and Pabis model, MFNN (Multilayer Feedforward Neural Network), and ANFIS (Adaptive-Network-based Fuzzy Inference System), to estimate dynamic drying behaviors of semi-finished cassava crackers. Among these models, MFNN was found to be the most suitable for predicting moisture ratio of the product based on r 2 (regression coefficient), and MSE (mean squared errors between the experimental data and predicted values).

Determination of water content of dried fruits by drying kinetics

Journal of Food Engineering, 1999

The aim of this work was to identify the kinetics of drying of dehydrated agricultural products, such as high-sugar containing fruits, as well as the kinetics of a decomposition reaction of the constituents of the fruits, such as sugars. The knowledge of the kinetics may lead to an identi®cation of the exact drying time of agricultural products and elimination of severe discrepancies from using dierent moisture content methodologies. The drying of currants at temperatures 65±97°C for elongated times showed that the weight did not reach equilibrium even after drying for several days, due to the decomposition of solids in addition to the water evaporation. Fructose was the primary source of decomposing material. Using the method of successive residuals, three simple ®rst order of reaction equations were found appropriate models describing the dual water evaporation/decomposition reaction phenomenon of dried fruits. By identi®cation of the three simultaneously occurring mechanisms, an algorithm for determination of the appropriate drying time of agricultural products was proposed, according to which there is a separation of the eect of weight reduction due to sugar decomposition, from the eect of weight reduction due to water evaporation. The proposed drying times for currants varied from 71 h at 65°C to 4.8 h at 97°C. Ó

Technological Revolution in Drying of Fruit and Vegetables

Historical evolution of different drying methods for drying fruit and vegetables was evolved gradually with time. Nowadays, every form of fruit and vegetables slices, chunks, paste, puree, solution can be dried using different available dryers. Recent research on drying methods focuses on the advancement in of energy consumption, product recovery and preservation of nutrients. Different combination dryers are also used as advancement for a particular dryer. Technological advancements in drying methods were triggered by the shortcomings of the existing one. This revolution clearly indicates that drying not only reduces moisture content to a safe storage level but also provides different edible forms