• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2002.11a
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• pp.59-62
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• 2002

유동층 건조법은 다공판으로 된 베드 위에 피건조물을 두고 아래쪽에서 열풍을 보내어 열풍속에서 재료를 부유시켜 열풍과 혼합함으로써 건조되는 방식으로 분체의 건조에 유효한 건조방법으로 알려져 있다. 열 및 물질 전달이 상당히 커서 건조가 빠르게 일어나고 온도가 균일하며 균일한 건조가 가능하다. 또한 건조장치의 처리용량이 비교적 크고 장치의 구조가 단순하여 건조장치의 경제성과 신뢰성이 우수하다.(중략)

• Korean Journal of Food Science and Technology
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• v.38 no.5
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• pp.635-641
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• 2006

In an attempt to find ways of improving the quality and sanitary state of dried squid, this study compared artificial drying methods i.e. hot air drying and cold air drying with natural drying method. The drying rates of squid were in the order of hot air, cold air and natural drying. However, cold-air drying was slower than natural drying at $7^{\circ}C$. The drying rates increased with increasing drying temperature. When drying temperature was close to the dew point on a dehumidifier surface, which was the case with cold air drying at $7^{\circ}C$, the driving force for dehumidification was lower than under other drying conditions, which resulted in a lower drying rate. There were little color differences between the drying methods and temperature. Squid dried by cold air-drying had better mechanical texture and sensory qualities than with other drying methods. In addition, the cold air drying method maintained superior quality in terms of the contents of amino acids, taurine, EPA, DHA, other fatty acids and a low TBA value than the other drying methods.

• Journal of Energy Engineering
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• v.25 no.4
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• pp.53-61
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• 2016

Unburned Carbon(UBC) and NOx emissions from High-moisture coal and Dried coal were investigated in Drop Tube Furnace(DTF). When the same amount of the High-moisture coal and Dried coal were oxidized in DTF, the results show that UBC and NOx emissions of Dried coal case is higher than High-moisture coal case. As the moisture in coal decreases from 40% to 10%, the average gas temperature increases but the moisture concentration in DTF decreases. As the wall temperature increases from $900^{\circ}C$ to $1500^{\circ}C$, the UBC decreases and NOx emissions increases. Especially, the difference for UBC between High-moisture coal and Dried coal decreases with increasing wall temperature.

• Journal of the East Asian Society of Dietary Life
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• v.11 no.6
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• pp.479-484
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• 2001

The absorption characteristics of persimmon powder related to different drying methods and various storage temperatures was investigated. The physical properties of persimmon powder by different drying methods displayed the largest amount of porosity in the freeze-dried sample, and the smallest in hot air dried sample. Equilibrium moisture was reached in 6 days. Monolayer moisture contents were predicted to 0.09687~0.19712(freeze drying), 0.07820~0.18617(vacuum drying) and 0.07715~0.18056(hot air drying) g H2O/g solid respectively using the BET equation. BET equation for isothermal absorption curve showed over 0.95 R-square for all dried methods. Monolayer moisture contents were increased as storage temperature was incremented because water molecular movement was more active and there was a greater chance to clash with the absorption surface area.

• Journal of Biosystems Engineering
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• v.13 no.4
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• pp.38-45
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• 1988

The freeze drying of garlic juice was carried out in a vacuum freeze dryer, laboratory size, by backface heating. The factors which influence the rate of freeze drying, the pressure of drying chamber, the plate temperature, the concentration and the thickness of a sample, were discussed in this study. The drying rate was in proportion to the drying chamber pressure and when the pressure was at 1.5 torr, the foaming occured on the surface of materials, so this condition was not suitable for freeze drying. As the temperature of plate increased, drying rate increased, but when the temperature was $20^{\circ}C$, it was impossible to accomplish freeze drying because the foaming and the dispersion occured in a sample. The higher the concentration of a sample was, the lower drying rate was.

• KOREAN JOURNAL OF CROP SCIENCE
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• v.51 no.spc1
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• pp.198-203
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• 2006

This study was conducted to select the temperature for hot air drying method, cutting method, and solution that inhibits enzymatic browning in making high quality powder from sweetpotato roots. It was observed that $70^{\circ}C$ was the best temperature for air drying method wherein the dry matter rating, dry matter time, flour yield and chemical component were considered. The proper cutting thickness should be 2.0 mm considering the vitamin C content and sensory evaluation of sweetpotato flour. Also, 1% vitamin C solution inhibited enzymatic browning of sweetpotato.

• Proceedings of the Korean Society of Postharvest Science and Technology of Agricultural Products Conference
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• 2003.10a
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• pp.173.2-174
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• 2003

국내 보급되고 있는 곡물건조기는 열풍형 순환식 곡물건조기가 주종을 이루고 있는데, 이건조기의 경우 곡물이 순환하면서 열풍공급과 템퍼링과정을 반복하면서 건조가 이루어지는 대류열전달 방식을 채택하고 있다. 대류열전달 방식은 복사열전달 방식에 비해 열전달률이 낮기 때문에 건조속도와 열효율이 떨어지며, 건조시 미질 향상과 건조비용 절감에 한계가 있어 왔다. 따라서 건조에너지의 절감과 동시에 고품질 쌀 생산을 할 수 있는 새로운 형식의 곡물건조기술을 확립하고자 원적외선 곡물건조기를 개발하였다. 원적외선은 0.56~l,000$\mu\textrm{m}$의 전자파로서 세라믹 도료표면에 열을 가하면 원적외선 파장대의 강한 에너지를 얻을 수 있다. 이같은 원적외선 에너지를 농산물에 조사시키면 열이 침투하게되고 동시에 농산물의 내부온도가 상승함에 따라 활발한 분자운동을 하면서 수분을 표면으로 이동시키기 때문에 열풍건조방법에 비해 열전달효율이 높고, 농산물을 보다 균일하게 건조가 가능하므로 좋은 품질의 쌀을 생산할 수 있는 특징을 가지고 있다. 시작기는 1회 3,800kg을 건조할 수 있도록 설계하였고, 템퍼링실, 건조실, 열풍실, 승강기 등으로 구성되었다. 원적외선 방사체의 형태는 실린더형이고, 방사체가 설치된 열풍실 위쪽은 타공망, 아래쪽은 방사량을 높이기 위하여 일부 개방된 구조로 제작하였다. 본 연구에서 구명된 원적외선 방사체 길이와 조사거리는 각각 1,470mm, 125mm가 적절한 것으로 나타났다. 시작기의 성능시험을 열풍건조기(대비구)와 비교한 결과 소음은 대비구에서의 94.12dB보다 13% 가량 낮게 나타났고, 건조온도를 45$^{\circ}C$로 설정하고 벼를 건조했을 때 건감률 0.58%,wb로 대비구의 0.47%,wb 보다 23% 높았고, 건조소요에너지도 470kcal/kg - water로 2%의 절감되었다. 또한 건조한 벼를 도정하여 색, 냄새, 윤기, 찰기 등에 대한 관능검사결과는 원적외선 건조방법이 종합기호도가 6.37으로 열풍건조방법 6.13보다 우수한 평가를 받았다. 건조비용은 시작기의 구입가격이 20% 비싸기 때문에 시간당 고정비가 높았으나, 건조성능이 우수하여 건조비용이 69,350원/톤으로 대비구보다 14% 절감되는 것으로 나타났다.

• Journal of the Korean Society of Food Science and Nutrition
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• v.11 no.1
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• pp.37-43
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• 1982

Constant rate period, falling rate period and diffusion coefficient using filefish fillet as sample during drying in hot air drier were determined under controlled conditions of temperature, humidity and air velocity. Drying rate curve consisted of a short period of constant rate and two stages of falling rate period. When 1 to 3m/see of air velocities were applied, diffusion coefficients were in the range of 1.9130 to $2.6187\;{\times}\;10^{-6}\;\textrm{cm}^2/sec$ at $50^{\circ}C$. 2.4806 to $3.5342\;{\times}\;10^{-6}\;\textrm{cm}^2/sec$ at $60^{\circ}C$ and 4.3405 to $5.3042\;{\times}\;10^{-6}\;\textrm{cm}^2/sec$ at $70^{\circ}C$, respectively. Available lysine content was decreased by 15%. 16% and 20% in the fillet dried at $50^{\circ}C$, $60^{\circ}C$ and $70^{\circ}C$, respectively.

• Journal of the Korean Society of Food Science and Nutrition
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• v.25 no.5
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• pp.768-773
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• 1996

The changes in amino acid contents of sea mussel and baby clam during drying at 40, 50 and 6$0^{\circ}C$ and storage at low temperature(4$^{\circ}C$) and room temperature(2$0^{\circ}C$) were investigated. Amino acids of 17kinds were analyzed in sea mussel and baby clam. Total amino acids content of raw sample were similar to sea mussel and baby clam(6575.30mg%, 6764mg%), decreased during drying and rate of decreasing was higher in baby clam than that of sea mussel. The content of Glx was highest in sea mussel(790.55mg%) and baby clam(990.89mg%), other amino acids differed from samples. The content of amino acids of low drying temperature(40 and 5$0^{\circ}C$) decreased was higher than that of high drying temperature(6$0^{\circ}C$). The rate of decreasing was higher at room temperature(2$0^{\circ}C$) storage and short storage periods than that of low temperature(4$^{\circ}C$) storage and long storage periods.

• Korean Journal of Fisheries and Aquatic Sciences
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• v.27 no.1
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• pp.7-12
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• 1994

The kinetics of browning reaction of dried shrimp powder samples were investigated during storage. The temperature conditions of the ding process were $25^{\circ}C\;and\;45^{\circ}C$, and the samples were stored at water activity ($a_w$) of 0.33, 0.44, 0.52, 0.65 and temperatures of $35^{\circ}C,\;45^{\circ}C,\;55^{\circ}C$ and temperature fluctuations between $33^{\circ}C\;and\;55^{\circ}C$. When the shrimp was dried at $25^{\circ}C$ the activation energies obtained from the Arrhenius plot ranged from 13.57 to 14.33 kcal/mol. From these energies of activation, the $Q_{10}$ values at $25^{\circ}C$ showed 1.93 to 2.00. In the case of drying at $45^{\circ}C$ the activation energies were $13.12{\sim}13.61\;kcal/mol$ and $Q_{10}$ values were $1.89{\sim}1.93$, respectively. In addition, a storage study under square-wave fluctuating temperature conditions was carried out by varying the shrimp sample temperature between $35^{\circ}C\;and\;55^{\circ}C$ within 7 days regular fluctuation cycle. The data obtained from the fluctuating temperature storage study will be used in the prediction of shelf-lives. The shelf-lives assessed at $25^{\circ}C$ from the accelerated shelf-life tests ranged from 4 days at aw 0.65 to 139 days at aw 0.33.