Multi-Pass Sorption Drying of Paddy Using Rice Husk Adsorbent: Experiments and Simulation

A single-stage sorption drying of paddy with rice husk adsorbent cannot reduce its moisture content to a safe level since the relative humidity of air inside the mixing tank is very high. To obtain a safe moisture content, multi-pass sorption drying was used and the effect of operating parameters—i.e., rice husk density, rice husk initial moisture content, and volumetric mixing ratio of paddy to rice husk—on the drying time and paddy quality were investigated for two paddy varieties, Suphanburi 1 and Khao Dawk Mali 105. A mathematical model associated with the transfers of heat and mass between the grain and adsorbent was also formulated to explore the sensitivity of the operating parameters to the drying time. Both the experiment and the simulation showed that the drying time was shorter by using a lower initial moisture content of rice husk, a higher rice husk bulk density, and a higher volumetric mixing ratio, the last factor being less important. For quality assessment, the color of white rice for both paddy varieties changed insignificantly under the influence of all the operating parameters, but the head rice quality was rather sensitive to the operating conditions especially for the Khao Dawk Mali 105, which had a 6–10% lower in head rice yield compared to that of the reference samples.     

Effects of inlet air temperature and spray rate of coating solution on quality attributes of turmeric extract coated rice using top-spray fluidized bed coating technique

The addition of natural antioxidants onto white rice kernel can improve its functionality. Curcuminoids that present in turmeric rhizomes possess high antioxidant activity and heat stability. The objective of this study was to investigate the effects of inlet air temperatures and spray rates of turmeric extract solution on quality attributes of the turmeric extract coated rice (TCR) using the top-spray fluidized bed coating technique. The experimental results have shown that inlet air temperature and spray rate of coating solution strongly affected the final moisture content and percentage of fissured kernel of TCR. Almost all of TCR kernels in the bed cracked when their final moisture content was lower than 11.8% wet basis. However, the head coated rice yield of fissured TCR slightly decreased from that of white rice. The color of TCR was uniform over the entire surface. Texture of cooked TCR insignificantly changed from that of uncoated sample. Increasing spray rate provided higher both total phenolic content (TPC) and total antioxidant capacity (TAC) whilst increasing inlet temperature yielded lower TPC but it did not affect TAC. Retentions of TPC and TAC of TCR after cooking remained higher than 90%.     

Effect of Adsorption Conditions on Effective Diffusivity and Textural Property of Dry Banana Foam Mat

Foamed banana product, a crispy snack, can quickly adsorb the moisture from the moist air, leading to loss of textural property. The main purpose of this research was therefore to study moisture adsorption kinetics of dry banana foam mat and its texture quality change. The adsorption isotherm experiments were carried out with a standard static method using saturated salt solutions over a wide range of relative humidities from 32 to 82% and temperatures of 35, 40, and 45°C. Three dry banana foam densities of 0.21, 0.26, and 0.30 g/cm³ adsorbed water vapor under controlled conditions. Fick's second law coupled with an optimization technique was used to estimate the effective moisture diffusivity at sorption conditions. Empirical equations with two and three constant parameters for describing the dependence of the effective moisture diffusivity on moisture content were tested. The two constant parameters could suitably describe the variation of the effective moisture diffusivity with moisture content. The initial foam density, relative humidity, and temperature significantly affected the effective moisture diffusivity. The banana foam mats for all densities lost their crispy texture at moisture content of 0.078 kg/kg db.     

A Comparative Study of Pork Drying Using Superheated Steam and Hot Air

Drying with superheated steam and hot air were comparatively studied for pork. Transport, physical, and chemical properties, i.e., effective diffusivity, color, microstructure, and rehydration ability, were investigated. The experimental results have shown that the decrease of pork moisture content in an early drying time was more rapid in superheated steam than in hot air and appeared to be lower in a latter time. The pork surface as examined by SEM was noticeably different for the samples dried by superheated steam and hot air. The fewer pores at the surface of superheated steam-dried pork caused a slower water penetration into the interior during rehydration, in addition to the lower drying rate. The color of the product from superheated steam was a relatively more intense brown than that obtained from hot air as presented by a lower L? value and a higher a? value.     

Effects of Peeled and Unpeeled Garlic Cloves on the Changes of Drying Rate and Quality

Reducing moisture content as fast as possible, together with minimizing loss of quality, is important to food processing. To reach these objectives, experimental investigations were conducted to examine the effects of both peeled and unpeeled garlic cloves as well as operating parameters such as temperature and superficial velocity on the drying rate and quality of dried product. Peel resistance to moisture diffusion is considerably dominated and yields the longer drying time. Drying at high temperature shows the shrinkage of garlic clove to be lower than that at low temperature, whereas the product color is browner and the sizes of produced pores as revealed by scanning electron microscope are larger. The loss of volatile oil is insignificantly different among low- and high-temperature drying. The peel effect exhibits negative results on the product color, giving lower luminosity than the peeled sample, in particular at low temperature, because of longer drying time.     

Experiments on In-Store Paddy Drying Under Tropical Climate: Simulation and Product Quality

The main objective of this work is to study the rice whiteness and paddy qualities of rice in terms of hardness, stickiness, cohesiveness, and germination of rice. The prediction results of moisture content and whiteness are compared with the experimental results using a near-equilibrium drying model, which is modified by including whiteness kinetics of rice kernel. The long grain rice (Suphanburi 1 high amylose indica variety), which consists of 27% amylose was used for all experiments. The experiments were carried out at the average ambient temperature range of 28.6-30.8°C, average relative humidity of 65.2-80.6% with a fixed bed depth of 1.0 m. Specific air flow rates of 0.65 and 0.93 m³/min-m³ of paddy were forced continuously through the paddy bulk at initial moisture contents of 18.5% and 20.1% wet basis, respectively. The desired final moisture content of paddy is about 13.3 ± 0.6% wet basis. The results show that drying rate and the whiteness predictions are in good agreement with those from the experiments. The in-store drying using ambient air condition did not produce notable effect on the rice whiteness, head rice yield, and the percentage of paddy germination. However, the hardness, stickiness, and cohesiveness of rice were changed.     

Influence of hot air fluidized bed drying on quality changes of purple rice

The influence of drying using a fluidization technique on the quality of purple rice was investigated in this study. The results demonstrated that the initial moisture of rice was 28.3% dry basis (db). Compared to the sun-dried or reference purple rice samples, the influence of drying at temperatures ranging from 100 to 150°C did not affect the quality of color, anthocyanin content, total phenolic content, or antioxidant activity. At this initial moisture level, samples should be dried at 150°C air because such temperatures yield the highest drying rate. Drying at this temperature also causes an increase in the head purple rice yield because of the gelatinization of starch. In the case of an initial moisture content of 33.3% (db), the drying temperature should not exceed 130°C.     

Performance Study of a Double-Pass Thermoelectric Solar Air Collector with Flat-Plate Reflectors

In this paper the results of the influence of flat-plate reflectors made of aluminum foil on the performance of a double-pass thermoelectric (TE) solar air collector are presented. The proposed TE solar collector with reflectors was composed of transparent glass, an air gap, an absorber plate, TE modules, a rectangular fin heat sink, and two flat-plate reflectors. The flat-plate reflectors were placed on two sides of the TE solar collector (east and west directions). The TE solar collector was installed on a one-axis sun-tracking system to obtain high solar radiation. Direct and reflected incident solar radiation heats up the absorber plate so that a temperature difference is created across the TE modules to generate a direct current. Only a small part of the absorbed solar radiation is converted to electricity, while the rest increases the temperature of the absorber plate. Ambient air flows through the heat sink located in the lower channel to gain heat. The heated air then flows to the upper channel, where it receives additional heating from the absorber plate. Improvements to the thermal energy and electrical power outputs of the system can be achieved by the use of the double-pass collector system with reflectors and TE technology. It was found that the optimum position of the reflectors is 60°, which gave significantly higher thermal energy and electrical power outputs compared with the TE solar collector without reflectors.     

DRYING OF CHOPPED SPRING ONION USING FLUIDIZATION TECHNIQUE

Abstract

This research investigates several parameters affecting the drying characteristics of chopped spring onion and develops an empirical model for predicting its drying behaviour in a fluidized bed dryer. Experimental results showed that at air temperature of 32 °C and relative humidity of 62 %, the minimum fluidization velocities were approximately 1.36, 1.20, 0.95 and 0.62 m/s at initial moisture contents of 95, 71, 56 and 5% w.b., respectively. Drying air temperature and specific air flow rate were parameters which affected drying rate. Page's model could predict the value closest to the experimental data. The air-product temperature should be kept lower than 53 °C to maintain the acceptable green color of the dried product.