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1

Kaminsky, George J. "TWO STAGE DRYING OF SYNTHETIC DETERGENTS." Drying Technology 9, no. 3 (1991): 709–21. http://dx.doi.org/10.1080/07373939108916705.

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2

Namsanguan, Yuvanaree, Warunee Tia, Sakamon Devahastin, and Somchart Soponronnarit. "Drying Kinetics and Quality of Shrimp Undergoing Different Two-Stage Drying Processes." Drying Technology 22, no. 4 (2004): 759–78. http://dx.doi.org/10.1081/drt-120034261.

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3

Zheng, Yao, Shuaishuai Zhang, Liu Yang, Banghong Wei, and Quanyou Guo. "Prevention of the Quality Degradation of Antarctic Krill (Euphausia superba) Meal through Two-Stage Drying." Foods 13, no. 11 (2024): 1706. http://dx.doi.org/10.3390/foods13111706.

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To achieve a krill meal of high quality, a two-stage drying involving hot-air drying and vacuum drying was investigated. Five experimental groups were established according to the different drying conditions in the second stage, including 95 °C and 101 kPa, 95 °C and 60 kPa, 75 °C and 101 kPa, 75 °C and 60 kPa, and 75 °C and 20 kPa. The results showed that reducing the drying temperature and vacuum pressure in the second stage had a significant impact on the drying characteristics, sensory quality, and bioactive compounds of krill meal. Among all five groups, the drying condition of 75 °C and
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4

Zhang, Weipeng, Chang Chen, Zhongli Pan, and Zhian Zheng. "Vacuum and Infrared-Assisted Hot Air Impingement Drying for Improving the Processing Performance and Quality of Poria cocos (Schw.) Wolf Cubes." Foods 10, no. 5 (2021): 992. http://dx.doi.org/10.3390/foods10050992.

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The objective of this study was to develop an efficient drying technology for poria cubes in order to improve product quality. Poria cubes were dried using different methods, including air impingement drying, infrared-assisted air impingement drying, vacuum drying, two-stage vacuum drying, and infrared-assisted air impingement drying. The results were compared with those from hot air drying. For the two-stage drying, the tested conditions were the first stage of vacuum drying with temperatures between 65–85 °C and a switching moisture ratio of 70–90%. The second stage infrared-assisted air imp
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5

Wazed, Md Abdul, N. H. M. Rubel Mozumder, and Md Sazzat Hossain Sarker. "EFFECT OF TWO STAGE DRYING EMPLOYING FLUIDIZED BED DRYING, TEMPERING FOLLOWED BY FIXED BED DRYING ON HEAD RICE YIELD OF BRRI DHAN28 RICE VARIETY IN BANGLADESH." Sustainability in Food and Agriculture 2, no. 2 (2021): 74–78. http://dx.doi.org/10.26480/sfna.02.2021.74.78.

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Drying of high moisture paddy to achieve quality milled rice is an important issue in a paddy producing country like Bangladesh. This study has been conducted to investigate the impact of two stage drying technique namely, fluidized bed drying, tempering and followed by fixed bed drying method on quality of BRRI Dhan28 rice variety in terms of head rice yield (HRY). Moist paddy was dried in fluidized bed dryer (FBD) as first stage drying to reduce moisture from 25-27% to 18-19% using three drying temperatures of 120, 130, and 150°C at three bed thicknesses of 8, 10, and 12 cm. The first stage
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6

T., Antal. "Influence of two-stage drying methods on the physical properties and drying characteristics of sweet potato slices." Food Research 7, no. 5 (2023): 61–77. http://dx.doi.org/10.26656/fr.2017.7(5).348.

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The effects of single-stage freeze-drying, two-stage mid-infrared assisted freeze-drying and vacuum pre-drying and freeze finish-drying on the operational time, energy uptake, color and hardness properties of sweet potatoes were investigated. Prior to the drying procedure, the samples were unpretreated and pretreated in citric acid solution. Drying curves of sweet potato were determined for mid-infrared and vacuum pre-drying at different drying temperatures (40, 50 and 60°C). The combination of mid-infrared and freeze-drying showed the largest reduction in both drying time (52%) and specific e
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7

Hu, Jian Jun, Sheng Qiang Shen, Ting Zhou Lei, Hao Huang, and Quan Guo Zhang. "Research on Constant-Temperature Drying Test of Cotton Straw and Regression Analysis of Drying Rate." Advanced Materials Research 472-475 (February 2012): 1645–51. http://dx.doi.org/10.4028/www.scientific.net/amr.472-475.1645.

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Constant-temperature drying tests for cotton straw under different conditions were performed with an integrated thermal analyzer, and the influence of different drying conditions on the drying process was analyzed. The process was divided into preheating stage, constant-rate drying stage, and decelerating drying stage. Regression analysis was conducted for drying curves at the latter two stages, and then the drying time at the critical point was determined. Regression equations of drying rate at these stages were produced. Research results showed that the decelerating drying stage of cotton st
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8

Nimmol, Chatchai, and Anucha Hirunwat. "Multistage Impinging Stream Drying for Okara." Applied Engineering in Agriculture 33, no. 4 (2017): 445–50. http://dx.doi.org/10.13031/aea.12212.

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Abstract. In this study, a multistage drying concept (one-stage and two-stage drying) was applied in an attempt to enhance the performance and energy efficiency of an impinging stream dryer for okara, which is a soy residue obtained from soymilk production. The volumetric water evaporation rate, the volumetric heat transfer coefficient and the specific energy consumption of the drying system at various drying conditions were evaluated. For one-stage drying, the volumetric water evaporation rate increased with an increase in the okara feed rate and the drying temperature. The effect of the dryi
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9

Wang, J., and Y. S. Xi. "Drying characteristics and drying quality of carrot using a two-stage microwave process." Journal of Food Engineering 68, no. 4 (2005): 505–11. http://dx.doi.org/10.1016/j.jfoodeng.2004.06.027.

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10

Jittanit, Weerachet, George Srzednicki, and Robert Driscoll. "Energy cost of seed drying." ASEAN Journal on Science and Technology for Development 26, no. 1 (2017): 33–41. http://dx.doi.org/10.29037/ajstd.302.

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In this work, the energy costs of drying corn, rice and wheat seeds between 3 drying options were compared. They consisted of 1) two-stage drying by using fluidised bed dryer (FBD) in the 1st stage and in-store dryer (ISD) in the 2nd stage, 2) single-stage drying by fixed bed dryer (FXD) and 3) two-stage drying by using FXD in the 1st stage and ISD in the 2nd stage. The drying conditions selected for comparison were proved to be safe for seed viability by the previous studies. The results showed that the drying options 2 and 3 consumed less energy than option 1. However, the benefits from lowe
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11

ZAGORUIKO, MIKHAIL G., and SERGEY A. PAVLOV. "USE OF THE S-40 DRYER IN TWO-STAGE DRYING OF CORN GRAIN." Agricultural engineering, no. 3 (2021): 69–73. http://dx.doi.org/10.26897/2687-1149-2021-3-69-73.

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The paper provides rationale for safe modes and methods for calculating a two-stage drying technology with partial recirculation of grain, in which the grain is under-dried by 2…3% to the standard humidity in a grain dryer, and the hot grain is cooled by active ventilation with outside air, while drying it to the standard humidity. The safe mode of two-stage drying in S-40 provides for partial recirculation of grain with moisture removal close to the standard, and the moisture content of the recirculated mixture not exceeding 18%. The recirculation coeffi cient calculated based on this conditi
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12

Xu, Xingang, Tianyuan Zhao, Jianing Ma, Qi Song, Qiao Wei, and Weihong Sun. "Application of Two-Stage Variable Temperature Drying in Hot Air-Drying of Paddy Rice." Foods 11, no. 6 (2022): 888. http://dx.doi.org/10.3390/foods11060888.

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The aim of this study was to investigate the effect of two-stage variable temperature drying (VTD) on the quality and drying efficiency of paddy rice in the hot air-drying process. A constant temperature of 50 °C (CTD) was used as a control group. VTD and CTD methods were applied in a 15 ton batch type recirculating grain dryer. Three aspects (appearance quality, physical and chemical properties, taste quality) of the paddy rice samples from the dryer were measured and compared. It was observed that paddy rice with an initial moisture content of 25.3% (wet basis) was dried to 14% (wet basis).
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13

Akhtaruzzaman, Md, Md Hasan Tarek Mondal, Md Sazzat Hossain Sarker, Mrityunjoy Biswas, Shanjida Akthar Shanta, and Md Abdul Momin Sheikh. "Evaluation of drying characteristics, energy consumption and quality of parboiled paddy: Two stage drying." Journal of Agriculture and Food Research 8 (June 2022): 100284. http://dx.doi.org/10.1016/j.jafr.2022.100284.

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14

WANG, J., Y. W. WANG, J. W. WANG, and X. L. HE. "DRYING CHARACTERISTICS AND DRYING QUALITY OF KIDNEY BEANS USING A TWO-STAGE MICROWAVE PROCESS." Journal of Food Process Engineering 31, no. 3 (2008): 413–30. http://dx.doi.org/10.1111/j.1745-4549.2007.00170.x.

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15

Li, Chenyang, Takaaki Kasuga, Kojiro Uetani, Hirotaka Koga, and Masaya Nogi. "High-Speed Fabrication of Clear Transparent Cellulose Nanopaper by Applying Humidity-Controlled Multi-Stage Drying Method." Nanomaterials 10, no. 11 (2020): 2194. http://dx.doi.org/10.3390/nano10112194.

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As a renewable nanomaterial, transparent nanopaper is one of the promising materials for electronic devices. Although conventional evaporation drying method endows nanopaper with superior optical properties, the long fabrication time limits its widely use. In this work, we propose a multi-stage drying method to achieve high-speed fabrication of clear transparent nanopaper. Drying experiments reveal that nanopaper’s drying process can be separated into two periods. For the conventional single-stage evaporation drying, the drying condition is kept the same. In our newly proposed multi-stage dryi
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16

Milanovic, Mihailo, Tijana Urosevic, and Olivera Ecim-Djuric. "Influence of variable temperature drying on red beetroot chips drying kinetic parameters and specific energy consumption." Thermal Science, no. 00 (2025): 38. https://doi.org/10.2298/tsci240919038m.

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In this work, the influence of variable temperature drying, mass of the samples, and the blanching pretreatment were varied to determine the influence of these parameters on the kinetics and specific energy consumption of red beetroot chips during convective drying. Beetroot samples used for the analysis were fresh and blanched slices of 5mm thickness. Three different temperature regimes were used during drying experiments: first regime (I) was drying at a constant temperature of 70?C, second regime (II) was performed with two-stage drying at temperatures of 80?C and 55?C, and third regime (II
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17

Getahun, Eshetu, Nigus Gabbiye, Mulugeta A. Delele, Solomon W. Fanta, and Maarten Vanierschot. "Two-stage solar tunnel chili drying: Drying characteristics, performance, product quality, and carbon footprint analysis." Solar Energy 230 (December 2021): 73–90. http://dx.doi.org/10.1016/j.solener.2021.10.016.

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18

Akhtaruzzaman, Md, Md Mostafa Kamal, S. M. Shamiul Alam, Md Sazzat Hossain Sarker, and Md Hasan Tarek Mondal. "Impacts of two-stage drying techniques on drying characteristics, physical and nutritional quality of maize." Journal of Agriculture and Food Research 15 (March 2024): 101046. http://dx.doi.org/10.1016/j.jafr.2024.101046.

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19

MALIN, NIKOLAY I. "MODELING OF THE KINETICS OF TWO-STAGE RECIRCULATING GRAIN DRYING." INTERNATIONAL TECHNICAL-ECONOMIC JOURNAL 4 (2019): 7–14. http://dx.doi.org/10.34286/1995-4646-2019-67-4-7-14.

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20

Jittanit, Weerachet, George Srzednicki, and Robert Driscoll. "Corn, Rice, and Wheat Seed Drying by Two-Stage Concept." Drying Technology 28, no. 6 (2010): 807–15. http://dx.doi.org/10.1080/07373937.2010.485081.

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21

Nowamooz, Hossein. "Equilibrium Stage of Soil Cracking and Subsidence after Several Wetting and Drying Cycles." Geotechnics 3, no. 2 (2023): 193–211. http://dx.doi.org/10.3390/geotechnics3020012.

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This work investigates the equilibrium stage of the crack propagation of a fine-grained soil after several drying and wetting cycles (shrinkage and swelling hysteresis). This stage is found to be crucial in practical engineering since the soil continues to show its irreversible hydraulic settlement, which is a potential risk for some severe structural damages. The shrinkage area and the shrinkage crack area were determined by using the image processing method. For the cyclic experimental investigations, the shrinkage cracks were followed during six months of successive wetting and drying cycle
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22

Nikitin, D. V., Yu V. Rodionov, M. A. S. Makhmud, A. I. Skomorokhova, A. N. Pakhomov, and A. S. Zorin. "Liquid Ring Vacuum Pumps for Heat and Mass Transfer Processes." Vestnik Tambovskogo gosudarstvennogo tehnicheskogo universiteta 27, no. 3 (2021): 428–41. http://dx.doi.org/10.17277/vestnik.2021.03.pp.428-441.

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The paper examines the calculation of a liquid ring vacuum pump, using the example of the drying process of various materials. It was found that for two-stage convective vacuum-impulse drying it is economically efficient to use a two-stage liquid ring vacuum pump with the ability to turn off the second stage. A method for calculating the specific power of one-stage and two-stage liquid ring vacuum pumps, taking into account heat and mass transfer and thermal processes that occur during operation is proposed.
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23

Wang, Guangyu, Kai Zhang, Bocheng Huang, Kaihua Zhang, and Cong Chao. "Microwave Drying of Sewage Sludge: Process Performance and Energy Consumption." Processes 12, no. 3 (2024): 432. http://dx.doi.org/10.3390/pr12030432.

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The microwave drying of sewage sludge is characterized by its speed and safety. A novel method for identifying free and bound water is proposed in this study. Experiments were performed to investigate the process performance and energy consumption in a microwave drying unit. The results indicate that the microwave drying process can be described in three stages, i.e., the preheating stage, constant-rate stage, and decreasing-rate stage. The preheating and constant-rate stages mainly remove free water, while the decreasing-rate stage mainly removes bound water. The Linear model effectively desc
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24

Shi, Yong Chun, Jie Li, Xuan You Li, et al. "Experimental Study on Super-Heated Steam Drying of Lignite." Advanced Materials Research 347-353 (October 2011): 3077–82. http://dx.doi.org/10.4028/www.scientific.net/amr.347-353.3077.

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This paper applies super-heated steam drying technology to improve the quality of lignite. A unique experimental system was built up. In order to obtain the optimum operation conditions, the drying kinetics was measured. The temperature range of super-heated steam was from 120 to 200°C. The results showed that the drying process of super-heated steam drying of lignite can be well depicted by two stages, as a constant drying rate stage followed by a falling drying rate stage. The comparison of drying process to the hot air drying showed the superior advantages of super-heated steam drying on sa
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25

Murugesan, K., H. R. Thomas, and P. J. Cleall. "An investigation of the influence of two‐stage drying conditions on convective drying of porous materials." International Journal of Numerical Methods for Heat & Fluid Flow 12, no. 1 (2002): 29–46. http://dx.doi.org/10.1108/09615530210413154.

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26

Snezhkin, Yu F., V. M. Paziuk, Zh O. Petrova, and O. A. Tokarchuk. "DETERMINATION OF THE ENERGY EFFICIENT MODES FOR BARLEY SEEDS DRYING." INMATEH Vol.61 61, no. 2 (2020): 183–92. http://dx.doi.org/10.35633/inmateh-61-20.

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For a more accurate study of the kinetics of the barley seeds drying, a convective drying stand with a computerized system of data acquisition and processing on the change in the mass and temperature of the sample from the drying time was used. The kinetic curves of the drying process under the action of three factors were constructed: the temperature of the coolant, heating medium movement rate and the initial moisture content of the seeds. Studies were also conducted and the germination of barley seeds under the action of these factors was analysed. Studies have shown that all factors affect
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27

Naik, B. Kiran, Mullapudi Joshi, Palanisamy Muthukumar, et al. "Investigating Solid and Liquid Desiccant Dehumidification Options for Room Air-Conditioning and Drying Applications." Sustainability 12, no. 24 (2020): 10582. http://dx.doi.org/10.3390/su122410582.

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This study reports on the investigation of the performance of single and two-stage liquid and solid desiccant dehumidification systems and two-stage combined liquid and solid desiccant dehumidification systems with reference to humid climates. The research focus is on a dehumidification system capacity of 25 kW designed for room air conditioning application using the thermal models reported in the literature. RD-type silica gel and LiCl are used as solid and liquid desiccant materials, respectively. In this study, the application of proposed system for deep drying application is also explored.
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28

Malin, N. I. "MODELING OF THE KINETICS OF TWO-STAGE DIRECT-FLOW GRAIN DRYING." EurasianUnionScientists 5, no. 69 (2019): 11–16. http://dx.doi.org/10.31618/esu.2413-9335.2019.5.69.499.

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29

Djaeni, M., P. V. Bartels, C. J. van Asselt, J. P. M. Sanders, G. van Straten, and A. J. B. van Boxtel. "Assessment of a Two-Stage Zeolite Dryer for Energy-Efficient Drying." Drying Technology 27, no. 11 (2009): 1205–16. http://dx.doi.org/10.1080/07373930903263210.

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30

Thakur, Abhay Kumar, and A. K. Gupta. "Two stage drying of high moisture paddy with intervening rest period." Energy Conversion and Management 47, no. 18-19 (2006): 3069–83. http://dx.doi.org/10.1016/j.enconman.2006.03.008.

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31

Nimmol, Chatchai, and Thawatchai Kaewkamrop. "Moisture Content and Physical Properties of High-Moisture Agricultural Material Dried by Impinging Stream Dryer." Key Engineering Materials 728 (January 2017): 347–52. http://dx.doi.org/10.4028/www.scientific.net/kem.728.347.

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The objective of this research was to study the drying of high-moisture agricultural material using an impinging stream dryer with multi-stage drying concept. Okara was used in this study as the test agricultural material. Experiments were performed in one-stage and two-stage drying. The final moisture content of the okara at several drying conditions was examined. The physical properties of dried okara were analyzed in terms of color and rehydration ability. It was found from the experiment that with the use of multi-stage drying concept the moisture content of okara could be significantly re
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32

Ju, Hao-Yu, Qian Zhang, A. S. Mujumdar, Xiao-Ming Fang, Hong-Wei Xiao, and Zhen-Jiang Gao. "Hot-air Drying Kinetics of Yam Slices under Step Change in Relative Humidity." International Journal of Food Engineering 12, no. 8 (2016): 783–92. http://dx.doi.org/10.1515/ijfe-2015-0340.

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Abstract The drying kinetics and mathematical modeling of hot-air drying of yam slices were investigated under two-stage relative humidity (RH) control strategy with 60 °C and 1.5 m/s as its constant drying temperature and air velocity, respectively. Results indicate high RH in the initial stage results in high sample’s temperature that enhances water diffusion in the falling rate drying period. Within the scope of current work, change in RH in the later drying period has insignificant influence on sample’s temperature rise while low RH can accelerate the drying rate. Compared to drying at con
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33

Zhao, Dandan, Kejing An, Shenghua Ding, Lijun Liu, Zhiqiang Xu, and Zhengfu Wang. "Two-Stage Intermittent Microwave Coupled with Hot-Air Drying of Carrot Slices: Drying Kinetics and Physical Quality." Food and Bioprocess Technology 7, no. 8 (2014): 2308–18. http://dx.doi.org/10.1007/s11947-014-1274-1.

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34

Shahin, Lubana, Ajit K. Mahapatra, and Nirmal Joshee. "Effect of Drying Methods on the Leaf and Flower Tissues of Paulownia elongata and P. fortunei and Resultant Antioxidant Capacity." Antioxidants 14, no. 3 (2025): 280. https://doi.org/10.3390/antiox14030280.

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Paulownia leaves and flowers have been used to prepare medicinal tea in traditional Chinese medicine; however, there has been no scientific validation of bioactive compounds so far. A systematic study is presented to establish a suitable drying protocol for leaf and flower tissues that may be useful in preserving bioactive compounds and retaining high antioxidant capacity. Additionally, a suitable drying protocol is commercially imperative for improving the shelf life of these tissues. In this study, P. elongata and P. fortunei juvenile leaves and flowers at two stages (pre- and post-anthesis
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35

Ganeev, Ildar, Khasan Karimov, Valeri Permyakov, Salavat Mudarisov, and Eduard Khasanov. "Mathematical Model of the Rapeseed Drying Process with the Use of Electromagnetic Microwave Radiation Based on Heat Calculations." Mathematical Modelling of Engineering Problems 9, no. 1 (2022): 67–74. http://dx.doi.org/10.18280/mmep.090109.

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Few studies have been devoted to mathematical modelling of the drying process of various crops using microwave drying units. The paper presents a mathematical model of the rapeseed drying process using electromagnetic microwave radiation based on heat calculations. The research aims at mathematical modelling of thermal processes of rapeseed heating when treated by electromagnetic microwave radiation. The computational and technological scheme of drying has been developed. According to the scheme, the drying process includes several cycles, which, in turn, consist of two stages. In the first st
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36

Hassebrauck, Martin, and Gerrit Ermel. "Two examples of thermal drying of sewage sludge." Water Science and Technology 33, no. 12 (1996): 235–42. http://dx.doi.org/10.2166/wst.1996.0341.

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The increasing amount of sewage sludge, legal requirements and a change in the assessment of common disposal paths lead more and more to thermal drying of sewage sludge. During the last years a lot of sludge drying plants in Germany were planned, built and brought into service. This paper describes two different kinds of sludge drying plants with their determining and operating values, the costs and the reasons for the choice of the drying method. The examples given are the sludge drying plant at Darmstadt (2 lines with a 2 stage dryer) and in the surrounding area of Frankfurt (1 line with a d
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37

Grüter, H., M. Matter, K. H. Oehlmann, and M. D. Hicks. "Drying of Sewage Sludge – An Important Step in Waste Disposal." Water Science and Technology 22, no. 12 (1990): 57–63. http://dx.doi.org/10.2166/wst.1990.0100.

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Industrial drying techniques are successfully used processes. They are usually used for the production of base materials for industries such as food, chemical and pharmaceutical. These processes can be transferred without any difficulty for the drying of sewage sludge. Thermal drying as a process for the purpose of water removal is an important link in waste management between sludge production and sludge disposal. Two systems, convection and contact drying, are here compared. Contact drying in the thin film evaporation process is explained. Explanation and proposed uses of the single and two-
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38

Zhang, Zhentao, Wenye Lin, Luwei Yang, Yanhua Dong, and Biguang Zhang Yang. "Study of Wood Drying with Two-Stage Compression High Temperature Heat Pump." Advance Journal of Food Science and Technology 5, no. 2 (2013): 180–85. http://dx.doi.org/10.19026/ajfst.5.3241.

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39

Xu, Yanyang, Min Zhang, Arun S. Mujumdar, Xu Duan, and Sun Jin-cai. "A Two-Stage Vacuum Freeze and Convective Air Drying Method for Strawberries." Drying Technology 24, no. 8 (2006): 1019–23. http://dx.doi.org/10.1080/07373930600776209.

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40

Ramaswamy, H. S., and N. H. van Nieuwenhuijzen. "EVALUATION AND MODELING OF TWO-STAGE OSMO-CONVECTIVE DRYING OF APPLE SLICES." Drying Technology 20, no. 3 (2002): 651–67. http://dx.doi.org/10.1081/drt-120002822.

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41

Somjai, Thanutyot, Siva Achariyaviriya, Aree Achariyaviriya, and Kodkwan Namsanguan. "Strategy for longan drying in two-stage superheated steam and hot air." Journal of Food Engineering 95, no. 2 (2009): 313–21. http://dx.doi.org/10.1016/j.jfoodeng.2009.05.005.

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42

Boestean, Olga. "DRYING KINETICS OF APRICOTS KERNELS." Journal of Engineering Science XXV (2) (June 15, 2018): 89–94. https://doi.org/10.5281/zenodo.2579651.

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In this paper, we proposed convective and combined methods for drying wet kernels of apricot stones. Kernels of apricot stones are a very ambiguous food product, during their heat treatment in them occurs not only the loss of mass due to the removal of moisture, but also the loss of mass due to biochemical changes occurring at high temperatures. It was experimentally established that the drying process should be carried out in two stages: the first stage lasts until the critical moisture content of 110 % (by total weight of solids) is reached and it should be impl
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43

Saakian, Alexander. "Intensification of the use of electrical equipment in order to optimize energy resources in floor-type chamber dryers." АгроЭкоИнфо 2, no. 44 (2021): 26. http://dx.doi.org/10.51419/20212226.

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The article deals with the issues of intensification of the use of electrical equipment and the efficiency of energy saving in chamber grain dryers of the floor type. A cyclic technology of drying seeds in dryers of this type with the use of two-stage drying technology is proposed. Keywords: ENERGY SAVING, INTENSIFICATION, CHAMBER DRYER, DRYING MODES, OPTIMIZATION
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44

Hussary, Jumana, Adel Alowaisy, Noriyuki Yasufuku, Ryohei Ishikura, and Monther Abdelhadi. "Drying Front and Vaporization Plane Dynamics during Evaporation from Homogeneous Soil Profiles." E3S Web of Conferences 382 (2023): 21003. http://dx.doi.org/10.1051/e3sconf/202338221003.

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Global warming has caused many lands to degrade, making them vulnerable to desertification. Therefore, finding innovative solutions is essential to prevent such phenomena from exacerbating. However, this requires a comprehensive understanding of the unsaturated layer formed due to the high-water loss from soil profiles by evaporation. In the present study, a new technique to trace the unsaturated layer from drying soil profiles was developed, and its accuracy and reliability were confirmed. Consequently, the spatial and temporal development of the drying front, vaporization plane, and film reg
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45

Otaboev, Kh, D. Sherkuziev, Sh Namazov, R. Radjabov, and A. Seytnazarov. "Flow of simple superphosphate using two-stage decomposition of phosphorite." IOP Conference Series: Earth and Environmental Science 939, no. 1 (2021): 012055. http://dx.doi.org/10.1088/1755-1315/939/1/012055.

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Abstract The methods for producing simple superphosphate by two-stage sulfuric acid decomposition of natural phosphates are analyzed. For the first stage, the process of decomposition of high-carbonate powdered phosphorite is studied depending on the rate of sulfuric acid from stoichiometry to the formation of H3PO4, its concentration and the reaction time of the starting components. For the second stage, the process of neutralization of phosphoric acid is studied, depending on the norm of phosphate rock for the formation of Ca(H2PO4)2. The drying process of superphosphate is carried out, in w
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46

Antal, Tamás. "Effect of different drying techniques on the drying time and energy of blueberry." Analecta Technica Szegedinensia 15, no. 1 (2021): 23–30. http://dx.doi.org/10.14232/analecta.2021.1.23-30.

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Blueberries (Vaccinium corymbosum L.) were dried combining vacuum, infrared, hot-air and freeze drying technologies. In this paper, examined the drying time and energy consumption of dewatering methods. The rehydration as a physical property were evaluated in dried blueberries. Combination of vacuum dried and freeze dried blueberries had higher rehydration ratio, followed by the single freeze drying, combination of hot-air drying and freeze drying, and infrared-freeze drying methods. The performance evaluation indicated that combination drying of blueberries at two-stage infrared-freeze drying
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47

Ridho, Rosyid, Fakhrul Irfan Khalil, Oki Saputra, et al. "Analisis Kinerja Dome Solar Dryer Untuk Pengeringan Kopi Di Desa Karang Sidemen Kabupaten Lombok Tengah." JURNAL SAINS TEKNOLOGI & LINGKUNGAN 11, no. 2 (2025): 227–34. https://doi.org/10.29303/jstl.v11i2.735.

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Coffee drying is a crucial stage that influences the final product's quality and flavor. This process must be performed correctly to maintain the quality of the coffee beans and prevent mold growth. This study aims to compare two coffee drying methods, using a Solar Dome Dryer and direct sun drying. The research was conducted in Karang Sidemen Village, Central Lombok, using 100 kg of coffee beans, divided into two groups of 50 kg each for the two drying methods. The results showed that both methods successfully reduced the moisture content to 0%, but the drying with the Solar Dome Dryer was fa
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Chen, Chun Xiang, Xiao Qian Ma, Xiao Cong Li, and Wei Ping Qin. "Study on Drying Characteristics of Microalgae under Different Conditions." Advanced Materials Research 724-725 (August 2013): 296–99. http://dx.doi.org/10.4028/www.scientific.net/amr.724-725.296.

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To find out an alternative of coal saving, a kind of microalgae, Chlorella vulgaris (C. vulgaris) which is widespread in fresh water was studied by digital blast drying system. The effect of the moisture content, drying thickness and temperature on the drying process of C. vulgaris were investigated. The results indicated that when the drying temperature is high, the moisture content is low and the material thickness is small, the drying time is short. The drying process of C.vulgaris can be divided into two stages, and the mass loss is mainly occurred in the second stage . The results will pr
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49

Nebesniy, A. A., V. G. Kotov, O. M. Svyatenko, D. S. Filonenko, and A. I. Khovavko. "ASSESSMENT OF A POSSIBILITY OF QUALITY IMPROVING OF REDUCING GAS BY TWO STAGE NATURAL GAS CONVERSION." Energy Technologies & Resource Saving, no. 4 (December 20, 2019): 43–49. http://dx.doi.org/10.33070/etars.4.2019.06.

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The analysis of the method of reducing gas obtaining by natural gas air reforming with cooling and drying of obtained products on the first stage of the process, their heat treatment in the catalyst layer, chilling and drying — on the second stage is made. It is determined that the temperature of a thermal gas treatment at the second stage of the process, shall not be less than 850–950 °C, which allows to increase the ratio (CO + H2)/CO2 in the resulting reducing gas. The values of the minimum temperature of gas processing on the second stage of the process depending on the pressure in the sys
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Los, Josef, Jiří Fryč, and Zdeněk Konrád. "Evaluating the parameters of a mobile maize dryer in practice." Acta Universitatis Agriculturae et Silviculturae Mendelianae Brunensis 61, no. 6 (2013): 1779–84. http://dx.doi.org/10.11118/actaun201361061779.

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The method of drying maize for grain has been recently employed on a large scale in the Czech Republic not only thanks to new maize hybrids but also thanks to the existence of new models of drying plants. One of the new post-harvest lines is a plant in Lipoltice (mobile dryer installed in 2010, storage base in 2012) where basic operational measurements were made of the energy intensiveness of drying and operating parameters of the maize dryer were evaluated. The process of maize drying had two stages, i.e. pre-drying from the initial average grain humidity of 28.55% to 19.6% in the first stage
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