Design and Experiment on Flank Type of Cropland Plot Breeding Wheat Drying Car

2013 ◽  
Vol 423-426 ◽  
pp. 1920-1923
Author(s):  
Fei Dai ◽  
Wu Yun Zhao ◽  
Feng Wei Zhang ◽  
Zheng Sheng Han
Keyword(s):  
Drying Methods ◽  
Test Results ◽  
Wheat Seed ◽  
Drying Time ◽  
Effective Time ◽  
Hot Air ◽  
Effective Contact ◽  
Maximum Angle ◽  
Collecting Efficiency ◽  
Drying Efficiency

In order to meet the drying demand of breeding wheat in China, the flank type of cropland plot breeding wheat drying car was designed, which was equipped with the solar collector automatically adjusting device and ensured that with the sun azimuth maximum angle of radiation, increased heat collecting efficiency in effective time. Used alternate partition drying storehouse and double duct W type corrugated plate collector to increase the effective contact time and heating effect about dry hot air with the breeding wheat, so improved the drying efficiency of wheat seed. The test results showed that the flank type of cropland plot breeding wheat drying car could easy to move within the cropland plot, when conducive to the breeding wheat drying operations, the average drying rate was 1.471%/h, and compared with the traditional drying methods, the average drying time was relatively reduced by 36.4%.

scholarly journals Comparative Study of Hot Air Drying and Microwave Drying for Dewatered Sludge

2021 ◽  
Author(s):  
Wittawat Wulyapash ◽  
Awassada Phongphiphat ◽  
Sirintornthep Towprayoon
Keyword(s):  
Microwave Power ◽  
Specific Energy Consumption ◽  
Microwave Drying ◽  
Drying Methods ◽  
Drying Time ◽  
Hot Air ◽  
Air Temperatures ◽  
Dewatered Sludge ◽  
Dried Sludge ◽  
Seafood Processing

Abstract Large amounts of sludge are generated from wastewater treatment in seafood processing industries. Most of the dewatered sludge in Thailand is not utilized and disposed by landfilling. The dried sludge utilization as refuse-derived fuel (RDF) is an alternative solution due to the gross calorific value (GCV), which is greater than 21.9 MJ/kg. However, the key obstacle is its high moisture content of 87.4% (wet basis). Therefore, drying methods using hot air and microwave techniques were investigated for preparing dried sludge. The effects of hot air temperatures (100-150 °C) and microwave power levels (100-800 W) were compared on drying kinetics, specific energy consumption (SEC), and characteristics of the dried products. The results showed that drying times were decreased by increasing the hot air temperatures. In the same way, the increase in microwave power levels decreased the drying time. The application of microwaves contributed to reducing the drying time by more than 46% compared to the hot air. The reduction of drying times resulted in the saving SEC. The GCV of the dried sludge decreased with the decrease in the volatile matter (VM) due to the high component of VM as 79.5-80.3% (dry ash-free basis). The sludge dried by the microwaves showed a lower GCV than the hot air products. However, dried sludges still had high GCV (≥ 20.8 MJ/kg). Furthermore, the minimal variation of the product characteristics demonstrated that the microwave technique could be applied as an alternative drying method with a rapid process compared to the conventional hot air technique.

Effects of drying methods on color retention and chlorophyll of celery (ApiumgraveolensL.), spinach (Spinacia oleraceaL.), Malabar spinach (Basella albaL.)

2020 ◽  
pp. 53-61
Author(s):  
Dat Q Tran
Keyword(s):  
Microwave Drying ◽  
Drying Methods ◽  
Hot Air Drying ◽  
Drying Time ◽  
Air Drying ◽  
Color Retention ◽  
Hot Air ◽  
Drying Techniques ◽  
Dried Vegetables

Dried vegetables are considered convenient for storage, transportation and preservation. The different drying techniques could influence the quality of resulting products. This study aimed to evaluate the effects of three distinguish drying methods as hot-air drying, foam-mat drying and microwave drying on the color retention and chlorophyll of green vegetables powder. Fresh spinach(Spinacia oleraceaL.), celery (Apium graveolensL.), Malabar spinach (Basella albaL.) were dried by different methods: hot air at 60oC, foam-mat at 60oC and microwave at 270 W until the samples reached approximately 9% of moisture content (wb). The drying time of the dried samples by microwave, foam-mat and hot-air method were 60, 210 and 240 min, respectively. Foam-mat dried vegetables were found to have the best quality in terms of color and the residual chlorophyll content. The findings suggest that foam-mat drying is promising in dried vegetable processing

Experiments on Hot-Air and Infrared Drying Characteristics of LiCoO2 Cathode Coating for Lithium-Ion Battery

2020 ◽  
Vol 1003 ◽  
pp. 260-267
Author(s):  
Xian Feng Wu ◽  
Xu Jia Li ◽  
Xin Zhi Bei
Keyword(s):  
Lithium Ion Battery ◽  
Radiation Power ◽  
Influencing Factor ◽  
Lithium Ion ◽  
Drying Time ◽  
Infrared Drying ◽  
Hot Air ◽  
Constant Rate ◽  
Drying Conditions ◽  
Drying Efficiency

Based on the drying technology principle of lithium-ion battery cathode coating, the variation law of dry base moisture content and drying rate in the process of hot-air drying and infrared drying was studied. The experimental results show that the cathode coating of lithium-ion battery dried under hot-air and infrared conditions can be divided into three stages: increasing-rate, constant-rate, and falling-rate. The constant-rate stage is the main drying stage, accounting for more than 50% of the weight loss, the falling-rate stage is the main energy consumption stage, accounting for more than 50% of the time. Under the condition of hot-air, the change level of airspeed is the main influencing factor of the drying process, and the drying time can be reduced by about 35% for each 0.7 m/s increase in airspeed. Under infrared conditions, the change level of radiation power is the main influencing factor of the drying process, and the drying time can be reduced by about 34.1% for every 100W of power increase. The optimal drying conditions under hot-air conditions are: air temperature 90 °C, airspeed 2.3 m/s; the optimal drying conditions under infrared conditions are: radiation distance 13 cm, radiation power 200 W. By comparing the best conditions of hot-air and infrared, it can be known that the drying efficiency is higher in the infrared condition and the drying duration is 160 s, but the energy utilization rate in the falling-rate stage in the infrared condition is lower than that in the hot-air condition. Therefore, when infrared drying enters the falling-rate stage, it can be supplemented by hot-air drying to further improve the drying efficiency.

scholarly journals Köpük Kurutma Yöntemi ile Gıdaların Kurutulması

2017 ◽  
Vol 5 (6) ◽  
pp. 637
Author(s):  
Emine Varhan ◽  
Mehmet Koç
Keyword(s):  
Food Product ◽  
Process Conditions ◽  
Drying Methods ◽  
Powder Form ◽  
Drying Time ◽  
Foam Structure ◽  
Foaming Agents ◽  
Product Increase ◽  
Foam Drying ◽  
Drying Efficiency

The foam mat drying is one of drying methods applied to produce powdered food in the food industry. Foam mat drying, which is better than other methods of drying in terms of drying time and cost, is used to convert powder form of various foods such as fruit, milk and seafood. The formation of the foam structure is provided with foaming agents and/or stabilizers. The surface area and drying efficiency of food product increase with conversion to foam structure. In this review, knowledge about the process conditions applied during the process of converting the food into powder form by foam drying method, the obtained product properties and the applicability of foam mat drying to various foods are presented.

Effect of microwave, infrared, and convection hot-air on drying kinetics and quality properties of okra pods

2021 ◽  
Vol 0 (0) ◽  
Author(s):  
Hany S. EL-Mesery ◽  
Mona A. Elabd
Keyword(s):  
Energy Consumption ◽  
Air Temperature ◽  
Specific Energy ◽  
Specific Energy Consumption ◽  
Drying Methods ◽  
Air Velocity ◽  
Rehydration Ratio ◽  
Drying Time ◽  
Shrinkage Ratio ◽  
Hot Air

Abstract Okra pods were dried using the following drying regimes; microwave (MWD), infrared (IRD) and convective hot-air drying (CHD). The objective of this investigate was to report the influences of drying methods on okra quality under different drying conditions. Data analysis showed that rehydration ratio and colour change increased with increase in drying air temperature and air velocity while specific energy consumption and shrinkage ratio decreased with increase in drying air temperature under (CHD). The rehydration ratio and colour of dried okra increased with increase in both infrared intensity but it also increased with a decrease in air velocity under (IRD). In the MWD method, drying time, specific energy consumption and shrinkage ratio decreased with increases in microwave power while the rehydration ratio and colour increased. Optimum drying period, specific energy consumption, colour, shrinkage and rehydration ratio were obtained for microwave drying. The model of Midilli et al. is the greatest for describing the drying curves of okra under all the drying processing conditions.

Effect of Pre-Treatments and Drying Air Temperature on the Quality of Dehydrated Oyster Mushroom (Pleurotus Florida)

2019 ◽  
Vol 56 (1) ◽  
pp. 34
Author(s):  
Parul Bora ◽  
Asha Kawatra
Keyword(s):  
Citric Acid ◽  
Oyster Mushroom ◽  
Drying Methods ◽  
Rehydration Ratio ◽  
Drying Time ◽  
Drying Characteristics ◽  
Drying Temperature ◽  
Hot Air ◽  
Adverse Influence

<em>Experiments were conducted on pre treated dehydrated oyster mushroom with steeping in citric acid and sodium chloride and blanching to investigate the effect of pre treatments and drying methods on drying characteristics of mushroom and quality of dried oyster mushroom. Drying was accomplished in a cabinet dryer using hot air at 40<sup>O </sup>C, 60<sup>O</sup>C and by sun drying. The drying characteristics of mushroom were not affected by the pre-treatments significantly. However, the rate of drying increased with the increase in drying temperature. Increase in drying temperature significantly reduced the total drying time. Pre treatments and drying temperature had adverse influence on the rehydration ratio, hardness and colour of the dehydrated mushrooms. Blanching improves the colour of the dehydrated mushroom but increased hardness also. A loss of protein was observed during blanching</em>

scholarly journals Behavior of a portable solar dryer for pineapple fiber

2012 ◽  
Vol 36 (6) ◽  
pp. 674-683 ◽  
Author(s):  
Róger Moya ◽  
Marco Solano
Keyword(s):  
Costa Rica ◽  
Relative Humidity ◽  
Solar Radiation ◽  
Heating System ◽  
Drying Methods ◽  
Drying Time ◽  
Hot Air ◽  
Solar Dryer ◽  
The Hours ◽  
Pineapple Leaves

In Costa Rica, there has been a growing interest to use pineapple fiber from plant, for which current processes need to be improved or new processes need to be developed, with emphasis on drying methods. This work presents the design and evaluation of the behavior of a prototype portable solar dryer in four sites of Costa Rica. The design describes the main parts of the dryer, as well as how they were constructed. The behavior was evaluated according to temperature and relative humidity inside e outside the chamber, and the influence of direct and indirect solar radiation. In order to achieve improved dryer efficiency, a dehumidifier was used to control relative humidity, and a heating system was implemented during the hours of low temperature, low solar radiation and high relative humidity. Based on drying time, final moisture content of fibers of pineapple leaves from plant, and the varying hours when fibers were put to dry, the evaluation of the dryer revealed that the best fiber-drying interval is from 6h00 to 14h00, and after that, it is convenient to inject hot air and use a dehumidifier in the dryer in order to increase its efficiency.

scholarly journals Determination of Drying Patterns of Radish Slabs under Different Drying Methods Using Hyperspectral Imaging Coupled with Multivariate Analysis

Foods ◽  
2020 ◽  
Vol 9 (4) ◽  
pp. 484 ◽  
Author(s):  
Dongyoung Lee ◽  
Santosh Lohumi ◽  
Byoung-Kwan Cho ◽  
Seung Hyun Lee ◽  
Hyunmo Jung
Keyword(s):  
Moisture Content ◽  
Hyperspectral Image ◽  
Partial Least Square ◽  
Least Square ◽  
Moisture Distribution ◽  
Microwave Drying ◽  
Drying Methods ◽  
Drying Method ◽  
Drying Time ◽  
Hot Air

Drying kinetics and the moisture distribution map of radish slabs under different drying methods (hot-air drying (HAD), microwave drying (MD), and hot-air and microwave combination drying (HMCD)) were determined and visualized by hyperspectral image (HSI) processing coupled with a partial least square regression (PLSR)-variable importance in projection (VIP) model, respectively. Page model was the most suitable in describing the experimental moisture loss data of radish slabs regardless of the drying method. Dielectric properties (DP, ε ) of radish slices decreased with the decrease in moisture content (MC) during MD, and the penetration depth of microwaves in radish was between 0.81 and 1.15 cm. The PLSR-VIP model developed with 38 optimal variables could result in the high prediction accuracies for both the calibration ( R c a l 2 = 0.967 and RMSEC = 4.32 % ) and validation ( R v a l 2 = 0.962 and RMSEC = 4.45 % ). In visualized drying patterns, the radish slabs dried by HAD had a higher moisture content at the center than at the edges; however, the samples dried by MD contained higher moisture content at the edges. The nearly uniform drying pattern of radish slabs under HMCD was observed in hyperspectral images. Drying uniformity of radish slabs could be improved by the combination drying method, which significantly reduces drying time.

Impacts of Explosion Puffing Drying Combined with Hot-Air and Freeze Drying on the Quality of Papaya Chips

2017 ◽  
Vol 13 (2) ◽  
Author(s):  
Jian Lyu ◽  
Jianyong Yi ◽  
JinFeng Bi ◽  
He Gao ◽  
Mo Zhou ◽  
...  
Keyword(s):  
Freeze Drying ◽  
Drying Methods ◽  
Total Carotenoids ◽  
Drying Time ◽  
Hot Air ◽  
Color Differences ◽  
Porous Microstructure ◽  
Air Explosion ◽  
Porous Microstructures

AbstractEffects of two combination drying methods as well as two single drying methods on the quality of papaya chips were studied. The longest drying time was found in freeze drying (FD), while the shortest drying time was found in hot-air-explosion puffing drying (HA-EPD). The papaya chips dried by FD exhibited the lowest shrinkage, while the highest shrinkage was found in the hot-air drying (HAD) dried sample. The lowest and highest total color differences (△E) were found in the FD and FD-EPD. The FD dehydrated papaya chips showed the highest retention of ascorbic acid and total carotenoids. The fastest rehydration rate was also observed in samples dried by FD. The worst rehydration capacity was found in FD-EPD, which related to the collapsed porous microstructure. Papaya chips prepared by FD-EPD showed crispier texture, which were in line with their expanded porous microstructures. In conclusion, the application of combining with EPD may improve the retention of nutrition of papaya.

Assessment of Quality Attributes of Banana Slices Dried by Different Drying Methods

2014 ◽  
Vol 10 (2) ◽  
pp. 251-260 ◽  
Author(s):  
Kianoosh Pirnazari ◽  
Ali Esehaghbeygi ◽  
Morteza Sadeghi
Keyword(s):  
Moisture Transfer ◽  
Color Change ◽  
Drying Methods ◽  
Drying Method ◽  
Hot Air Drying ◽  
Drying Time ◽  
Moisture Movement ◽  
Air Drying ◽  
Hot Air ◽  
Significant Difference

Abstract In the present study, banana slices were dried and compared using electrohydrodynamic (EHD) drying method at 4.5, 6.5, and 8.5 kV/cm; oven at 50, 60, and 70°C; and hot-air drying at 50, 60, and 70°C at a constant air velocity of 1.5 m/s. ANOVA showed that drying method had a significant effect on drying time, rehydration capacity, shrinkage, color features (L*, a*, b*, and ∆E), and consumed energy. The values of consuming energy for EHD at 8.5 kV/cm, oven, and hot-air drying at 70°C were 2.99, 20.9, and 81.7 kJ/g run on full capacity of each dryer, respectively. Oven drying led to a greater color change than did hot-air. No significant difference was observed between the color change feature ∆E for EHD and hot-air dried samples in the orthogonal contrast analysis. The falling rate period for EHD moisture movement showed that diffusion was describing the moisture gradients and the internal moisture transfer was dominant. EHD is not fast; however, its advantages like less energy needed, lower shrinkage, and great rehydration capacity make it a good choice for combining with other convection drying methods.

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