Academic literature on the topic 'Drying equipment'

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Journal articles on the topic "Drying equipment"

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Vant Land, C. M. "INDUSTRIAL DRYING EQUIPMENT." Drying Technology 10, no. 3 (June 1992): 807–8. http://dx.doi.org/10.1080/07373939208916479.

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Lamm, É. L. "New drying and drying-calcinating equipment." Chemical and Petroleum Engineering 42, no. 3-4 (March 2006): 173–83. http://dx.doi.org/10.1007/s10556-006-0074-5.

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Raouzeos, Georgios, and Walther Schwenk. "SPECIALIZED DRYING PROCESSING EQUIPMENT." Drying Technology 17, no. 7-8 (August 1999): 1593–601. http://dx.doi.org/10.1080/07373939908917638.

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KIYOTA, Masanori, Junichiro FUKUTOMI, Takeshi NISHI, and Norio TERASHIMA. "Drying Performance of a New Type Drying Equipment." Japan Journal of Food Engineering 9, no. 4 (December 15, 2008): 303–9. http://dx.doi.org/10.11301/jsfe2000.9.303.

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Ma, Xiao Lu, and Yong Zhang. "Drum Sludge Drying Equipment Energy Dissipation Factor Analysis." Applied Mechanics and Materials 249-250 (December 2012): 213–17. http://dx.doi.org/10.4028/www.scientific.net/amm.249-250.213.

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Drum sludge drying equipment is used widely both at home and abroad, and the energy consumption is the key factor of measuring sludge drying equipment. Based on the basis of study of drum sludge drying equipment energy consumption, this paper conducts a comprehensive analysis of drum sludge drying equipment energy consumption factor, and points out that the drum sludge drying equipment energy consumption mainly depends on heat source and drying system configuration, aims to provide reference and research for drum sludge drying equipment.
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Sniezhkin, Yu F., and R. О. Shapar. "ENERGYEFFICIENT EQUIPMENT FOR DEHYDRATION THERMOBILE MATERIALS." Thermophysics and Thermal Power Engineering 42, no. 2 (June 24, 2020): 5–17. http://dx.doi.org/10.31472/ttpe.2.2020.1.

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The article substantiates the relevance of processing thermolabile materials into dried foods, as one of the alternative options for fresh fruits and vegetables. It is noted that drying, as a method of conservation, is characterized by high energy intensity and increased requirements for the quality and safety of the final product. The naturalness of the dried products and the environmental cleanliness of the process come to the fore. The criteria of quality and efficiency of the process are combined into a single task: increasing the efficiency of the drying process and creating energy-efficient equipment. The analysis of heat and mass transfer during convective drying allowed us to establish methods and ways to improve the energy efficiency of the process. Based on a synthesis of theoretical and experimental studies, the optimal heat and humidity parameters of dehydration were determined, according to which the temperature of the material during drying does not exceed the maximum permissible value. This contributes to the preservation of valuable nutrients in the final product. Prevention of excess material temperature above the acceptable level is confirmed by the nature of the change in the numerical value of the Rebinder effect and is provided by drying in multi-stage dehydration modes, including high-temperature high-moisture method using zone drying installations of tunnel and belt type, as well as heat-pump drying installations with low heat consumption. It was emphasized that the drying of thermolabile materials is carried out in an environment of pure hot air without the use of inert and chemically synthesized substances. Non-contact air heating is carried out using traditional fuels as well as secondary and renewable energy sources. It is noted that the design features of the drying equipment make it possible to distribute the intensity of the thermal effect on the material, depending on its moisture content into zones, and also automatically maintain and control these parameters for a specific type of raw material. The adopted recirculation system of the drying agent helps prevent emissions of waste coolant and reduces thermal pollution of the environment.
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Kemp, Ian. "Industrial drying equipment; Selection and application." Powder Technology 73, no. 1 (November 1992): 98. http://dx.doi.org/10.1016/0032-5910(92)87017-5.

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Shukla, Banshi D. "DRYING TECHNOLOGY AND EQUIPMENT IN INDIA." Drying Technology 19, no. 8 (August 31, 2001): 1807–24. http://dx.doi.org/10.1081/drt-100107274.

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Yunindanova, Mercy Bientri, Dimas Rahadian Aji Muhammad, and Sigit Prabawa. "Peningkatan Kualitas dan Kuantitas Biji Kakao Melalui Intensifikasi Perawatan Kakao, Introduksi Alat Budidaya, dan Pengering Sistem Hybrid." Abdihaz: Jurnal Ilmiah Pengabdian pada Masyarakat 3, no. 1 (June 30, 2021): 8. http://dx.doi.org/10.32663/abdihaz.v3i1.1512.

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Putat village, Patuk district, Gunung Kidul regency is one of cocoa production center in Yogjakarta. Cocoa bean products in this region have been marketed not only in Yogjakarta but also several areas in Indonesia. In order to support production continuity of cocoa bean productions, to date the farmers face obtacles in cacao plantation maintenance and cocoa beans drying. Thus, this activity aimed to increase quality and quantity of cocoa beans through maintenance intensifications of cacao and introduction of cacao cultivation equipments and cocoa beans drying hybrid system. Partner in this activities were Kelompok Tani Kakao Sido Dadi and cocoa dan chocolate production industry “Joglo Coklat” located in Patuk, Gunung Kidul, Yogjakarta. The activities were conducted in several stages including 1) basic data collection, 2) socialization of cacao plantation maintenance, 3) socialization of cocoa beans drying, 4) introduction of cultivation equipments, 5) contruction of drying chamber, 6) handover of equipment, and 7) evaluation of parnter response. The results of the activity indicated that the provision of information and the introduction of equipment for cacao plant maintenance activities had a positive impact on partners. From the questionnaires, the partners stated the benefits of this activity and the desire for sustainable activities. The introduction of maintenance equipment and cocoa beans drying made it easier for farmers to carry out cultivation, harvest and post-harvest activities of cocoa beans so would be able to improve the quality and quantity of cocoa beans.
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Safin, R. R., I. F. Khakimzyanov, and A. F. Garaeva. "Energy Saving Equipment for Crushed Materials Drying." Procedia Engineering 206 (2017): 1246–51. http://dx.doi.org/10.1016/j.proeng.2017.10.626.

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Dissertations / Theses on the topic "Drying equipment"

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Platten, A. K. "A study of evaporation and drying in porous building materials." Thesis, University of Manchester, 1985. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.373625.

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McFarland, Elizabeth Gramling. "Infrared absorption characteristics of fabrics." Thesis, Georgia Institute of Technology, 1998. http://hdl.handle.net/1853/10185.

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Daian, Mihai Stelian. "Thedevelopment and evaluation of new microwave equipment and its suitability for wood modification." Swinburne Research Bank, 2006. http://hdl.handle.net/1959.3/38305.

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Thesis (PhD) - Swinburne University of Technology, Industrial Research Institute Swinburne, Faculty of Engineering and Industrial Sciences, 2006.
[A thesis submitted for the degree of Doctor of Philosophy], Industrial Research Institute Swinburne, Faculty of Engineering and Industrial Sciences, Swinburne University of Technology, 2006. Typescript. Includes bibliographical references (p. 157-165)
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Mutshekwa, Ndivhuho. "Effect of time-based hot air drying method on chemical composition of jatropha zeyheir tea." Thesis, University of Limpopo, 2017. http://hdl.handle.net/10386/1914.

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Thesis (M. Sc. (Agriculture)) --University of Limpopo, 2017
Tea is one of the most popular consumed beverages in the world, which has beneficial properties such as anti-oxidization, anti-carcinoma and preventing arteriosclerosis. The major essential components of catechins present in tea leaves, includes epigallocatechin gallate (EGCG), epigallocatechin (EGC), epicatechin gallate (ECG), epicatechin (EC), gallocatechin (GC) and catechin (C). Influence of time-based hot air drying method on chemical composition of the Jatropha zeyheri Sond, widely consumed in rural communities of Zebediela (Khureng village), Limpopo Province, South Africa, was investigated. Four treatments, namely; 0, 24, 48, and 72 hours, were arranged in completely randomised design (CRD), replicated five times. The study demonstrated that drying significantly increased total phenolic content, total antioxidant capacity and tannin content. It also demonstrated that drying significantly increased minerals elements; Mg, K, P, S, Al, Co, Mn, Si and Zn content and decreased Na, Ca and Ni and Zn quantities. Sodium-potassium ratio was very low across drying periods. Drying time did not significantly influence proximate chemicals; energy, protein, carbohydrates, ash and fibre content. Moisture and fat were significantly increased by drying period. Results of the study suggested that time-based hot air drying method improved the chemical composition of J. zeyheri, which has the potential of enhancing nutrition in marginal rural communities of Limpopo Province.
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Kulasiri, G. Don. "Simulation of deep-bed drying of Virginia peanuts to minimize energy use." Diss., Virginia Tech, 1990. http://hdl.handle.net/10919/39762.

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A deep-bed drying model simulating the drying of peanuts in a fixed bed is required for designing energy-efficient and automatically controlled dryers. A deep-bed drying model consists of a thin-layer drying model to calculate the moisture release from the material and a set of mass and energy balances. An experimental setup was constructed to determine drying rates of Virginia-type peanuts under 14 different drying air conditions. Selected empirical and semi-theoretical models available for modeling thin-layer drying rates were fitted to the collected data using nonlinear regression techniques. The modified Page's model and the two-term exponential model fitted the data better than other models considered. A deep-bed drying model PEATECH based on four coupled partial differential equations consisting of four variables, air temperature, peanut temperature, air humidity, and peanut moisture content was developed. Validation of the model was accomplished by using the data collected from 36 deep-bed drying experiments conducted using three laboratory dryers during 1987, 1988, and 1989. PEATECH predicted the variables within a peanut bed with an accuracy of less than ± 6%. The energy saving potential of exhaust-air recirculation was established by conducting simulated experiments using a modified version of PEATECH.
Ph. D.
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Sosle, Venkatesh. "A heat pump dehumidifier assisted dryer for agri-foods /." Thesis, McGill University, 2002. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=38285.

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The motivation of the research presented in this thesis was to investigate the potential of using a commercial 2.3 kW heat pump dehumidifier (HPD) simultaneously as a dryer for high-moisture agricultural products and for other domestic dehumidification/heating applications. A drying system incorporating the HPD was designed and constructed, along with instrumentation to gather data on the properties of process air as well as real-time weight of the material being dried. The HPD was equipped with an external water-cooled condenser that rejected excess heat out of the system. The design of the system allowed for conducting drying with recirculation of air as well as use of electrical heaters. In an open mode, the drying could be carried out simultaneously with room dehumidification and water heating in the secondary condenser.
The drying experiments were conducted with apple, tomato and agar gels. The system was found to be more effective in drying of material with higher amount of free moisture such as tomato. Comparisons were made between HPD assisted drying (partial and complete) and hot air drying (at 45°C and 65°C) in the same system using apple as the test material. Colour changes (L*a*b* values) in the samples were compared between treatments. It was observed that the degree of undesirable colour change was least in case of the HPD assisted system. The HPD dried fruit exhibited better rehydration properties than the hot air dried samples. Water activity of the HPD dried samples was noticeably lower than that of the hot air dried samples at the same water content, indicating that the residual moisture was probably held under higher tension. Histological observation indicated that there was a lesser degree of damage to the cellular structure of apple when dried with the HPD than when dried with hot air alone.
In terms of energy consumption, the process of HPD assisted drying is more expensive. Much of the energy input is rejected at the secondary condenser as excess heat. Unless this heat is recovered for another purpose, or the system is modified to reuse it for drying, the drying process must carry this loss entirely. The specific moisture extraction rate (SMER) for apple was as low as 0.1 kg per kWh with the HPD assisted system. The SMER values for drying at 45°C was 0.5 kg per kWh and was almost 0.8 kg per kWh at 65°C.
The HPD assisted drying system demonstrated the ability of heat pumps to link different energy related activities viz., drying, space dehumidification and water heating. The energy expenditure is expected to be impressive when considered for all the related applications. The concept of utilizing heat pumps on farms to link up different energy streams for better utilization of the low-grade heat sources is discussed. A possible drying efficiency assessment in the form of energy-based evaluation is proposed.
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Ngo, Thanh Binh. "Design and creation of control board for drying equipment based on development of a soft self-tuning PID controller." Technische Universität Dresden, 2018. https://tud.qucosa.de/id/qucosa%3A32721.

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This article introduces a versatile control board design that can be used in many drying systems using direct heat transfer solutions in combination with static tray distribution based on development of a flexible self-tuning PID controller. The product is applied for a small oven drying solid waste samples or plant materials for further analysis of some parameters. The control board is built based on the Arduino embedded system using a flexible soft PID (Proportional–Integral–Derivative) controller that can automatically change its gains according to the required temperature thresholds to best meet the setpoint of temperatures. The system has a small steady-state error (SSE), fast response to the setpoints and keep stable with temperature deviation when reaching the required threshold around ± 0.5 0C. In addition, the controller board can operate in a variety of modes, including direct temperature operation, pre-set operation, and switching mode.
Bài báo này giới thiệu một thiết kế mạch điều khiển đa năng có thể áp dụng trong nhiều hệ thống sấy sử dụng các giải pháp truyền nhiệt trực tiếp kết hợp phân phối khí kiểu khay tĩnh trên cơ sở phát triển bộ điều khiển PID mềm tự chỉnh linh hoạt. Sản phẩm được ứng dụng cho một mô hình lò nhỏ sấy mẫu chất thải rắn hoặc mẫu thực vật phục vụ các nghiên cứu phân tích thành phần một số chất. Mạch điều khiển được chế tạo trên nền tảng hệ thống nhúng Arduino sử dụng bộ điều khiển PID mềm linh hoạt, có khả năng tự động thay đổi tham số theo ngưỡng nhiệt yêu cầu để đáp ứng nhiệt độ tốt nhất so với ngưỡng nhiệt độ đặt. Hệ thống có độ quá điều chỉnh nhỏ, nhanh đáp ứng tới các ngưỡng đặt và giữ ổn định với sai lệch nhiệt độ khi đạt ngưỡng yêu cầu trong khoảng ±10C. Ngoài ra, bộ điều khiển còn có thể hoạt động theo nhiều chế độ khác nhau, bao gồm hoạt động theo chế độ đặt nhiệt độ trực tiếp, hoạt động theo chu trình đặt trước, và chuyển chế độ hoàn toàn tự động.
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Egolf, Arthur R. "Design and testing of a sawdust dryer and a suspension sawdust burner." Thesis, This resource online, 1992. http://scholar.lib.vt.edu/theses/available/etd-03172010-020701/.

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Li, Ping-Lun, and 李秉倫. "Helical Tube Heat Exchanger on Freeze-Drying Equipment." Thesis, 2008. http://ndltd.ncl.edu.tw/handle/6y363c.

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碩士
國立臺北科技大學
能源與冷凍空調工程系碩士班
96
We used theory and numerical value to discuss the phenomenon of heat transfer for helical tube heat exchanger and to observe its possible parameter on freeze-drying equipment. The inner part of helical tube is more complex because it has double phase flows. Using methods of Experiment Formula and Log-Mean-Temperature Difference (LMTD) as the base to design the length of helical tube; and then we compared the difference between theory and experiment through the experimental results. For the outer part of helical tube, we made use of CFD package FLUENT_6.3 to simulate various cases and analyze the field of temperature and velocity. According to the theory of heat transfer, we found that selecting flows with high convection coefficient could increase the efficiency of heat transfer. In addition, increasing the surface area or raising mass flows could achieve the same situation. However, on the commercial cost basis, it doesn’t guarantee it could get the positive advantage. By simulating multiple cases, the results are as follows: 1.) Changing the tube diameter without changing overall surface area couldn’t get obvious improvement in heat transfer. 2.) Moving the direction of inlet from the top of shell to the bottom. By doing this, it will occur dramatic changes and will largely raise the efficacy of heat convection. 3.) Adding baffles to change the direction of flows and increase turbulent. This way will lead to raise the choices of heat exchanger. We arranged multiple cases along with geometric manufactured condition, trying to enhance the heat convection coefficient and the heat exchanger efficiency. It’s a suggestion that we improve the efficiency of heat exchanger up to 8.53 percent as the reference of improving the efficiency on freeze-drying equipment.
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Chen, Tsan-Chi, and 陳贊吉. "Improvement of IR Drying Equipment Stability Using Taguchi Method." Thesis, 2017. http://ndltd.ncl.edu.tw/handle/fj666m.

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碩士
國立勤益科技大學
工業工程與管理系
105
The drying process is a crucial procedure in the chemical industry. Since the inception of IR drying technique, its applications have been multiplied exponentially as it features several advantages, including highly efficient heat transfer, short heating time and the ease to be absorbed by many materials. As a result, IR drying has been introduced in the production of numerous products. To improve the process yield for the IR drying process, it is necessary to identify and improve the problems of illumination evenness with IR lamps before the competitiveness in the market is maintained. The IR dryer designed by a company was selected for the purpose of this study to establish the optimized setup parameters for near-IR lamps. The 33 development lines of TRIZ were combined with the development of technology roadmap and expert discussion to identify possible key factor of influence. Next, the Taguchi method was introduced to design the L9 orthogonal table for the comparison between optimized parameters and optimized response surface in the attempt to locate the optimized parameters for key factors, construct the basis for the stability optimization for near IR lamps, improve the evenness within the effective process area for near IR lamps and provide a reference for quality improvement for relevant industries. The experimental result indicated the increase of Cpk for the process ability of the Taguchi method from 0.79 to 1.30 and Cpk for the process of response surface method from 0.79 to 1.68. The experiment proved that the improvement solution proposed was capable of increasing process ability, and did reduce process variation.
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Books on the topic "Drying equipment"

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Industrial drying equipment: Selection and application. New York: M. Dekker, 1991.

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Mujumdar, Arun S. Guide to industrial drying: Principles, equipment and new developments. Prabhadevi, Mumbai: Colour Publications Pvt. Ltd., 2004.

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Comber, Peter La. Drying characteristics of milled peat. Dublin: University College Dublin, 1996.

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American Institute of Chemical Engineers. Equipment Testing Procedures Committee. AIChE equipment testing procedure: Packed columns : a guide to performance evaluation. 2nd ed. New York, NY: American Institute of Chemical Engineers, 1990.

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Shirley, Bills, ed. Dehydrating food: A beginner's guide. New York, NY: Skyhorse Pub., 2010.

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Cummins, Sinéad M. Monitoring and modelling of commercial malt drying. Dublin: University College Dublin, 1996.

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American Institute of Chemical Engineers. Equipment Testing Procedures Committee. AIChE equipment testing procedure: Continuous direct-heat rotary dryers : a guide to performance evaluation. 3rd ed. Hoboken, N.J: Wiley-Interscience, 2006.

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Committee, American Institute of Chemical Engineers Equipment Testing Procedures. AIChE equipment testing procedure: Continuous direct-heat rotary dryers : a guide to performance evaluation. 2nd ed. New York, N.Y: American Institute of Chemical Engineers, 1985.

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AIChE equipment testing procedure: Continuous direct-heat rotary dryers : a guide to performance evaluation. 3rd ed. Hoboken, N.J: John Wiley, 2005.

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Spray dryers: A guide to performance evaluation. 2nd ed. New York: American Institute of Chemical Engineers, 2003.

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Book chapters on the topic "Drying equipment"

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Pinkerton, H. L. "Drying Practices and Equipment." In Electroplating Engineering Handbook, 710–15. Boston, MA: Springer US, 1996. http://dx.doi.org/10.1007/978-1-4613-2547-5_33.

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Wang, Yingqiang, Min Zhang, and Arun S. Mujumdar. "Microwave-Assisted Drying of Foods - Equipment, Process and Product Quality." In Modern Drying Technology, 279–315. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2014. http://dx.doi.org/10.1002/9783527631704.ch09.

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Wang, Yingqiang, Min Zhang, and Arun S. Mujumdar. "Microwave-Assisted Drying of Foods - Equipment, Process and Product Quality." In Modern Drying Technology, 279–315. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2014. http://dx.doi.org/10.1002/9783527631728.ch37.

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Misnawi, Ariefandie Febrianto Noor, and Tunjung Sari Ariza Budi. "Roasting Equipment for Cocoa Processing." In Drying and Roasting of Cocoa and Coffee, 47–62. Boca Raton, Florida : CRC Press, [2020] | Series: Advances in drying science and technology: CRC Press, 2019. http://dx.doi.org/10.1201/9781315113104-3.

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Carneiro Nogueira, Vanúsia Maria, and Thomas Koziorowski. "Roasting Equipment for Coffee Processing." In Drying and Roasting of Cocoa and Coffee, 235–66. Boca Raton, Florida : CRC Press, [2020] | Series: Advances in drying science and technology: CRC Press, 2019. http://dx.doi.org/10.1201/9781315113104-8.

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Evranuz, E. Özgül. "Drying Vegetables: New Technology, Equipment, and Examples." In Handbook of Vegetables and Vegetable Processing, 299–315. Oxford, UK: Wiley-Blackwell, 2011. http://dx.doi.org/10.1002/9780470958346.ch14.

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Yu, Xinqi, and Zhaoyang Wang. "Structure Design and Analysis of Coal Drying Equipment." In Advanced Manufacturing and Automation VIII, 668–73. Singapore: Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-13-2375-1_85.

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Brosnan, Denis A. "Drying Fundamentals: Evaluating Dryer Performance." In Materials & Equipment/Whitewares: Ceramic Engineering and Science Proceedings, Volume 20, Issue 2, 167–73. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2008. http://dx.doi.org/10.1002/9780470294543.ch16.

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MILLER, BRITTON D. F., and ROY A. GILLESPY. "Chapter 4: Unit Operations and Equipment. II. Drying and Dryers." In Breakfast Cereals and How They Are Made, 133–59. 3340 Pilot Knob Road, St. Paul, Minnesota 55121-2097, U.S.A.: AACC International, Inc., 2000. http://dx.doi.org/10.1094/1891127152.004.

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Du, Liqing, Xinghao Tu, Hong Zhang, and Kun Li. "Effect of bleached shellac on the quality of the fluidized-bed drying process." In Advances in Energy Science and Equipment Engineering II, 869–72. Taylor & Francis Group, 6000 Broken Sound Parkway NW, Suite 300, Boca Raton, FL 33487-2742: CRC Press, 2017. http://dx.doi.org/10.1201/9781315116174-9.

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Conference papers on the topic "Drying equipment"

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Siyu, Chen, Bai Bing, Liu Chunshan, Tao Changchun, and Zhao Yang. "Fungus Rotating Drying Control Equipment." In 2016 International Conference on Intelligent Transportation, Big Data & Smart City (ICITBS). IEEE, 2016. http://dx.doi.org/10.1109/icitbs.2016.32.

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Hang, Du, Peng Runling, Yang Zhao, and Yang Zhuoyu. "Finite Element Analysis of the Drying Chamber of Freeze-drying Equipment." In Proceedings of the 2019 International Conference on Precision Machining, Non-Traditional Machining and Intelligent Manufacturing (PNTIM 2019). Paris, France: Atlantis Press, 2019. http://dx.doi.org/10.2991/pntim-19.2019.53.

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Menshutina, Natalia. "SUPERCRITICAL DRYING PROCESS MODELING AND EQUIPMENT DESIGN." In 17th International Multidisciplinary Scientific GeoConference SGEM2017. Stef92 Technology, 2017. http://dx.doi.org/10.5593/sgem2017/61/s24.044.

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Bahmyari, Hossein, Mohsen Ajdari, and Hamed Nabizadeh. "Effect of Wetting-Drying on a Stabilized Expansive Soil." In International Foundations Congress and Equipment Expo 2021. Reston, VA: American Society of Civil Engineers, 2021. http://dx.doi.org/10.1061/9780784483411.024.

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Schuch, Eduardo, Magaiver Lamp, Mateus Hartmann, Ismael Schroer, and Angela Moura. "DEVELOPMENT OF A COMPUTATIONAL STUDY ON A DRYING EQUIPMENT." In 25th International Congress of Mechanical Engineering. ABCM, 2019. http://dx.doi.org/10.26678/abcm.cobem2019.cob2019-1655.

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Gratton, Luca J. "Transient Stefan Flows at Wet and Heated Equipment Boundaries." In ASME 2005 Power Conference. ASMEDC, 2005. http://dx.doi.org/10.1115/pwr2005-50139.

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With emphasis on thermal losses from internally heated equipment in process applications, the results of conjugate heat and mass transfer modeling are presented for a category of Stefan flow involving vaporization in a semi-permeable heterogeneous media. The model simulates the initial stages of the drying process for wet, partially saturated insulation material abutting heated equipment. Dimensionless forms of the governing equations constitute the model basis for a transient, one-dimensional problem abstraction. Numerical solutions are obtained using finite-difference techniques. Model results are presented to demonstrate drying rate variation at high heat rates in the materials of interest to the applications. Summary results include drying rate, saturation distribution, and fluid velocity profiles with comparison of observed drying front penetration depth to existing literature.
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7

Chen, Jie-Liang, Zhen Deng, Wen-Di Chen, Lu-Kai Lyu, and Fei Wang. "Comparative Study on Drying Characteristics of Sewage Sludge in Two Kinds of Indirect Heat Drying Equipment." In 2nd 2016 International Conference on Sustainable Development (ICSD 2016). Paris, France: Atlantis Press, 2017. http://dx.doi.org/10.2991/icsd-16.2017.2.

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8

Oh, Sang Hyun, Ki Ho Park, Byoung Hyuk Yu, and Sung Il Kim. "Drying characteristics of wastewater sludge according to outside air inflow conditions." In 21st International Drying Symposium. Valencia: Universitat Politècnica València, 2018. http://dx.doi.org/10.4995/ids2018.2018.7790.

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The purpose of this study is to analyze the changes of drying efficiency according to the inflow conditions of outside air into the drying equipment during the drying process in order to reduce the energy used in the drying process of sludge. We conducted the experiment using a vertical thin film dryer. Materials used for the experiment are sewage sludge. As a result of the study, higher drying efficiency was obtained in the case of outside air inflow than in the case of no outside air inflow. In addition, optimum condition of outside air inflow was derived. Keywords: Drying; Sludge; Drying efficiency; Air inflow condition
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9

Koç, Banu, Nazan Çağlar, and Gamze Atar. "Functional properties of dried tarragon affected by drying method." In 21st International Drying Symposium. Valencia: Universitat Politècnica València, 2018. http://dx.doi.org/10.4995/ids2018.2018.7834.

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Tarragon is a small shrubby perennial herb in the Asteraceae family. It is cultivated for the use of its aromatic leaves in seasoning, salads, sauces, vinegars, mustard and spices. In this study, tarragon was dried in two different drying equipment (infrared (ID) and microwave dryers (MD)) to compare the drying and final product properties (moisture content, water activity and colour change). Three different output power levels of 125, 250 and 500 W were used for MD, whereas the ID treatment involved three drying temperature levels that were 60, 70 and 80°C. A comparison of the drying kinetics, MD was more effective in shortening drying time when compared with ID. Keywords: Tarragon, microwave drying, infrared drying, color change
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10

Barrozo, Marcos A. S., M. V. C. Machado, I. A. Resende, R. M. Lima, R. J. Brandão, M. R. Pivello, S. M. Nascimento, and C. R. Duarte. "The role of boundary conditions on the dynamics of green coffee beans in a rotated dryer." In 21st International Drying Symposium. Valencia: Universitat Politècnica València, 2018. http://dx.doi.org/10.4995/ids2018.2018.7455.

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Coffee drying and roasting are usually performed in rotated dryers; therefore, the study of particle dynamics in this equipment is of great relevance to improve their efficiency and hence the quality of the final product. Thus, this work aimed to investigate experimentally and numerically the dynamics of coffee beans in a rotary dryer. The Euler-Euler model was employed to reproduce the particle velocity profile in the rolling regime under different boundary conditions. The results shown that the lower specularity coefficient (0.01), which characterizes the smooth wall and free slip condition, reproduced the bed behavior that most resembled the experimental one. On the other hand, the other coefficients (0.1 and 1.0) showed an increasing deformation in the bed surface, different from the observed experimental behavior. It was also verified that, as the filling degree increases, the bed surface deformation becomes more pronounced. Keywords: coffee; rotated dryer; simulation; specularity coefficient.
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Reports on the topic "Drying equipment"

1

PHILIPP, B. L. Cold Vacuum Drying (CVD) Electrical Equipment Hydrogen Hazard Protection. Office of Scientific and Technical Information (OSTI), January 2000. http://dx.doi.org/10.2172/801154.

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2

IRWIN, J. J. Spent nuclear fuel project cold vacuum drying facility safety equipment list. Office of Scientific and Technical Information (OSTI), February 1999. http://dx.doi.org/10.2172/781563.

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Graves, D. B. Hanford spent nuclear fuel cold vacuum drying process equipment skid modification work plan. Office of Scientific and Technical Information (OSTI), May 1998. http://dx.doi.org/10.2172/345067.

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4

IRWIN, J. J. Spent Nuclear Fuel (SNF) Project Cold Vacuum Drying (CVD) Facility Master Equipment List. Office of Scientific and Technical Information (OSTI), September 1999. http://dx.doi.org/10.2172/798069.

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5

Rice, Robert W., Jeffrey L. Howe, R. Sidney Boone, and John L. Tschernitz. Kiln drying lumber in the United States : a survey of volume, species, kiln capacity, equipment, and procedures, 1992-1993. Madison, WI: U.S. Department of Agriculture, Forest Service, Forest Products Laboratory, 1994. http://dx.doi.org/10.2737/fpl-gtr-81.

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