• 제목/요약/키워드: Drying Temperature

검색결과 1,493건 처리시간 0.029초

열풍과 원적외선 겸용 연속식 백삼 건조기의 개발 (Development of a Prototype Continuous Flow Dryer using For Infrared Ray and Heated -air for White Ginseng)

  • 박승제;김성민;김명호;김철수;이종호
    • Journal of Biosystems Engineering
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    • 제25권2호
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    • pp.115-122
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    • 2000
  • This study was performed to develop a prototype continuous flow ginseng dryer with which better product quality and lower drying energy consumption could be achieved compared with conventional ginseng dryers. A dryer having both far infrared ray (IR) and heated-air as the drying energy sources was designed and fabricated . Dryer performance was studied by examining energy efficiencies and dryer performance evaluation indices (DPEI) during the drying tests of medium-sized four year ginseng roots with IR radiating plate temperature and drying air temperature in the range of 80-12$0^{\circ}C$ and 22-5$0^{\circ}C$, respectively. The DPEI of IR /heated -air combined drying was 1/3 of that of the conventional heated-air drying when ginseng were dried to the same final moisture ratio. When ginsengs were dried for 12 hours in the prototype IR/heated-air combination dryer, a linear relationship was found to exist between final moisture ratio and ginseng temperature. As the drying progressed, drying air temperature inside the dryer was nearly constant but ginseng temperature was drastically increased during the first two hours and gradually increased thereafter until the end of drying. With the prototype Ir/heated-air combination dryer, the drying rate changed little but the energy efficiency increased proportionally when the amount of ginseng to be dried increased. Drying capacity, energy efficiency, and DPEI of the prototype IR/heated-air combination ginseng dryer were estimated to 1.500 roots, 65% and 3.800kJ/kg-water , respectively.

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승화 건조모델에 대한 운전방법별 건조시간의 예측 (Prediction of the Drying Time under the Various Operational Conditions using a Sublimation Model)

  • 박노현;배신철
    • 대한기계학회논문집
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    • 제17권8호
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    • pp.2088-2098
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    • 1993
  • A mathematical model of freeze drying by sublimation was suggested and used to estimate the drying time. Under the various conditions, the drying time of pure water and carrot was numerically calculated for the suggested model. Optimal policies of freeze drying were investigated experimentally in a laboratory freeze dryer. It was found that the shortest drying times could be obtained when the chamber pressure and condenser temperature were kept at their lowest values and the best method of heat transfer for sublimation was the conduction involving radiation. The sublimation drying period was finished when the bottom temperature of material could be reached at near $0^{\circ}C$ from frozen temperature.

함수다공질층의 진공건조에 관한 실험적 연구 (Ⅰ) (An Experimental Study on Vacuum Drying of Water-Saturated Porous Media)

  • 박형진;김경근;김명환
    • Journal of Advanced Marine Engineering and Technology
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    • 제20권5호
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    • pp.68-75
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    • 1996
  • The vacuum drying characteristics of water-saturated porous media were studied experimentally. The water-saturated porous media, water-saturated sand layer, was heated by the isothermal bottom wall of the rectangular vessel. The vacuum drying rate and temperature distribution of the sand layer were measured and calculated under a variety of conditions of heated wall temperature, vacuum rate, and thickness of the test material. It was found that the drying rate due to the heat and mass teansfer is greatly influenced by the heated wall temperature, vacuum rate, and thickness of the test material.

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Simulation of Wheat Circulating Cross-flow Dryer

  • Kim, Oui-Woung;Kim, Hoon;Kim, Woong;Lee, Hyo-Jai;Han, Jae-Woong
    • Journal of Biosystems Engineering
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    • 제40권3호
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    • pp.232-237
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    • 2015
  • Purpose: In Korea, wheat is dried using circulating cross-flow grain dryers. However, there is no research on wheat drying which can be utilized for the dryers. Therefore, this study developed and evaluated a simulation of the circulating cross-flow dryer, and examined the effects of various factors on drying performance. Methods: The simulation program was developed using drying models and was evaluated against wheat-drying experiments with a dryer having a 30-ton capacity. The influence of drying temperature, air volume, and grain falling rate on drying performance were examined through the simulation. Results: The experimental results validated the simulation program by showing the same root mean square error (RMSE) for moisture content (0.286%) and drying rate (0.056%/h) in both the experimental data and the simulation values. The appropriate wheat-drying parameter values, considering drying conditions, were determined to be $50^{\circ}C$ for drying temperature, $500m^3/min$ for air volume, and a grain falling rate of $36.0m^3/h$. Conclusions: The developed simulation program for circulating cross-flow dryers analyzed the influences of performance factors such as drying temperature, air volume, and falling rate on drying performance.

Drying Kinetics of Onion Slices in a Hot-air Dryer

  • Lee, Jun-Ho;Kim, Hui-Jeong
    • Preventive Nutrition and Food Science
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    • 제13권3호
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    • pp.225-230
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    • 2008
  • Onion slices were dehydrated in a single layer at drying air temperatures ranging from $50{\sim}70^{\circ}C$ in a laboratory scale convective hot-air dryer at an air velocity of 0.66 m/s. The effect of drying air temperature on the drying kinetic characteristics were determined. It was found that onion slices would dry within $210{\sim}460\;min$ under these drying conditions. Moisture transfer during dehydration was described by applying the Fick's diffusion model and the effective diffusivity changed between $1.345{\times}10^{-8}$ and $2.658{\times}10^{-8}\;m^2/s$. A non-linear regression procedure was used to fit 9 thin layer drying models available in the literature to the experimental drying curves. The Logarithmic model provided a better fit to the experimental drying data as compared to other models. Temperature dependency of the effective diffusivity during the hot-air drying process obeyed the Arrhenius relationship with estimated activation energy being 31.36 kJ/mol. The effect of the drying air temperature on the drying model constants and coefficients were also determined.

Drying Characteristics of Korean-type Rehmannia (Jiwhang) Noodle

  • Rhim, Jong-Whan
    • Food Science and Biotechnology
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    • 제18권1호
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    • pp.202-206
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    • 2009
  • Drying characteristics of fresh Korean-type rehmannia (jiwhang) noodle was investigated to determine drying kinetic parameters under the experimental conditions of 5 temperatures (30, 40, 60, 80, and $90^{\circ}C$). Drying curve of the noodle showed a biphasic pattern of decrease in drying rate with initial rapid drying followed by slow dehydration as the progress in drying. In all drying conditions, only falling drying rate period was observed and the drying rate of the noodle was greatly influenced by the drying temperature. The effective diffusion coefficients ($D_{eff}$) were determined by the diffusion model and their temperature dependency was determined using an Arrhenius equation. The activation energy ($E_a$) values for the drying of the noodle were 19.94 and 21.09 kJ/mol at the initial and the latter stage of dehydration, which were comparable to those of pasta or Japanese udong dehydration.

Effects of Pretreatment for Controlling Internal Water Transport Direction on Moisture Content Profile and Drying Defects in Large-Cross-Section Red Pine Round Timber during Kiln Drying

  • Bat-Uchral BATJARGAL;Taekyeong LEE;Myungsik CHO;Chang-Jin LEE;Hwanmyeong YEO
    • Journal of the Korean Wood Science and Technology
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    • 제51권6호
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    • pp.493-508
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    • 2023
  • Round timber materials of 600 mm length, cut from large-cross-section round timber of red pine (Pinus densiflora S. et Z.) of 450 mm width and 4.2 m length, were prepared as the target of kiln drying in this study. After treating the target materials through end sealing (ES), end sealing - kerfing (ES-K), lateral sealing - end sealing - boring (LS-ES-B), or lateral sealing - partial end sealing (LS-PES), the effects of the treatment on the incidence of drying defects were determined. The target materials with exposed lateral surface and sealed cross surface were steamed at the initial temperature of 65℃ above the official pest control temperature of 56℃, followed by kiln drying toward the final temperature of 75℃. The target materials with sealed lateral surfaces, on the other hand, were dried at the initial temperature of 90℃ at almost the maximum temperature of conventional kiln drying, as there is no risk of early check formation caused by surface moisture evaporation. The final temperature was set at approximately 100℃. The drying time, taken for the target materials with initial moisture content of 70%-80% to reach the target moisture content of 19%, varied across treatment conditions. The measured drying time was 1,146 hours (approximately 48 days) for the timber with sealed cross surface and 745 hours (approximately 31 days) for the timber with sealed lateral surface, until the moisture content reached the target level. The formation of surface checks could not be prevented in the control and ES groups, but a definite preventive effect was obtained for the LS-ES-B and LS-PES groups.

산삼배양근의 원적외선 건조특성 (Far Infrared Rays Drying Characteristics of Tissue Cultured Mountain Ginseng Roots)

  • 리혁;강태환;녕효봉;조성찬;한충수
    • Journal of Biosystems Engineering
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    • 제34권3호
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    • pp.175-182
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    • 2009
  • This study was conducted to investigate the drying characteristics of tissue cultured mountain ginseng roots. The far infrared rays dryer of a double blast system used for this experiment can control the drying parameters such as far infrared heater temperature and air velocity. The far infrared rays drying tests of tissue cultured mountain ginseng roots were performed at air velocity of 0.4, 0.6, 0.8 m/s, under drying air temperature of 50, 60, and $70^{circ}C$, respectively. The results were compared with one obtained by the heated air drying method. The drying characteristics such as drying rate, color, energy consumption, saponin components and antioxidant activities were analyzed. The results showed that the drying rate of far infrared rays drying was faster than that of heated air drying and due to high temperature of drying air and fast air velocity, the far infrared rays drying of double blast type was superior to the heated air drying. The value of the color difference for heated air drying was 10.11${\sim}$12.99 and that of far infrared rays drying was in the range of 7.05${\sim}$7.54, which was in the same drying condition, also energy consumption of far infrared rays drying was in the range of 3575${\sim}$6898 kJ/kg-water. At the same time, the antioxidant activities using far infrared rays drying were higher than those using heated air drying.

냉풍건조공정을 이용한 마른오징어의 품질특성 (Quality Characteristics of Dried Squid (Todarodes Pacificus) by Cold Air Drying Process)

  • 홍주헌;배동호;이원영
    • 한국식품과학회지
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    • 제38권5호
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    • pp.635-641
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    • 2006
  • 본 연구에서는 자연건조 및 온풍건조에서의 문제점을 보완하고자 냉풍건조공정을 이용하여 말린 오징어의 품질 특성을 비교 하였다. 건조속도는 온풍건조가 15시간만에 목적하는 수분함량에 도달하여 가장 단시간에 건조가 완료되었으며 자연건조, 냉풍건조 순이었는데 $7^{\circ}C$ 냉풍건조가 건조시간이 165시간으로 가장 많이 소요되었다. 건조방법과 건조온도에 따른 ${\Delta}E$ 값은 자연건조가 57.78로 색의 변화가 가장 컸으며, 물성은 냉풍건조가 다른 간조방법에 비해 조직감이 우수하였다. TBA 가는 건조시간 및 온도가 증가할수록 높아지는 경향이었고 총아미노산 및 지방산 함량은 냉풍건조 $15^{\circ}C$가 다른 건조방법에 비해 우수하였다. 콜레스테롤 함량은 온풍건조 $30^{\circ}C$에서 488.5 mg/100 g으로 가장 많이 감소하여 건조조건이 마른오징어의 콜레스테롤 함량에 많은 영향을 끼침을 확인하였다. 종합적인 기호도는 지질의 산화에 의한 향미 변화와 갈변의 발생정도가 낮은 $15^{\circ}C$ 냉풍건조가 가장 우수하였다.

응축식 의류건조기의 효율적인 건조 조건 (Efficient Drying Conditions for a Condensing Clothes Dryer)

  • 정혜원;김효정;황소연
    • 한국의류산업학회지
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    • 제10권6호
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    • pp.1058-1063
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    • 2008
  • The use of clothes dryers is increasing in Korea and throughout Asia, because of preference for the drum type washer dryer. Clothes dryers consume more energy than almost any other home appliance. This paper suggests efficient ways for drying laundry with condensing clothes drier. We dried cotton fabrics with the condensing clothes dryers and observed the energy input, temperature and RH of the dryer during the drying process. In the early stages of drying process, the air temperature inside the clothes dryer decreased and the RH and the drying time increased as the weight of fabrics increased. We found that it was important to consider the total weight of the fabrics that included heat-sensitive fibers. It took more than half the drying time and the energy input for a 2.5 kg load that it did for a 5 kg load. Therefore, drying larger one load was more efficient than divided smaller loads, because increasing the weight of the fabrics reduced the energy input per kg of drying clothes. The lower the initial moisture regains of the fabrics were, the lower the energy input and the drying time were. The energy input for spinning after washing was much less than that for drying in the dryer. Consequently, it is more efficient to reduce the moisture content of the clothes by lengthening the spinning time of the washer to reduce the energy consumption and the drying time. During the drying process opening the door twice for 30 seconds each time lowered the air temperature and the RH of the dryer, but did not affect the moisture regain of the fabrics, the drying time, and the energy input.