• 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.

• Korean Journal of Food Science and Technology
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• v.13 no.3
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• pp.202-208
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• 1981

Contents of moisture, sugar and saponin, and color intensity of red ginseng tea (RGT) prepared at various drying conditions were investigated for quality evaluation. 1. The sorption isotherm of RGT showed step-wise isotherm. 2. The moisture content of RGT dried at $80,\;90\;and\;105^{\circ}C$ reached at nearly constant values below 1.5% after 3 hours. 3. The HPLC patterns of sugar and saponin at various drying temperatures were quality same but different in quantity. 4. The color intensity of RGT was changed little below $80^{\circ}C$, but significantly above $90^{\circ}C$. 5. A significant relationship was found between decrease of sugar content and increase of color intensity above $80^{\circ}C$.

• 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 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.

• Korean Chemical Engineering Research
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• v.56 no.3
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• pp.430-434
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• 2018

In this study, an effective diffusion coefficient and mass transfer coefficient were investigated in microwave-assisted drying of paclitaxel for removal of residual methylene chloride. At all the temperatures (35, 45, and $55^{\circ}C$), a large amount of the residual methylene chloride was initially removed during the drying, and the drying efficiency increased when increasing the drying temperature. The effective diffusion coefficient ($1.299{\times}10^{-13}{\sim}2.571{\times}10^{-13}m^2/s$) and mass transfer coefficient ($1.625{\times}10^{-11}{\sim}4.857{\times}10^{-11}m/s$) increased with increasing drying temperature. The small Biot number (0.0100~0.0151) indicated that the process of mass transfer was externally controlled.

• 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.

• 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.

• International Journal of Highway Engineering
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• v.11 no.4
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• pp.59-68
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• 2009

Torsional behavior of concrete pavement slabs due to temperature and moisture effects is constrained by self weight and friction etc, and causes stress as the result. The stress due to humidity variation in the slab is difficult to calculate while that due to temperature variation can easily be calculated by a commercial structural analysis program. Thus, the slab behavior can be predicted more accurately if the humidity effect is converted to equivalent temperature and is used as an input of structural analysis. In this study, a concrete pavement slab was constructed and strains of the slab due to environmental loadings were measured for long-term period. Thermal strains were subtracted from the measured strains by using thermal expansion coefficient of the concrete measured in a laboratory. Shrinkage strains, the remained strains, was supposed as additional thermal strains to calculate imaginary temperature with equivalent effect of the shrinkage by dividing the shrinkage with the thermal expansion coefficient. An existing shrinkage model was modified by considering the self weight and friction to be used in another model which can convert differential shrinkage between top and bottom of the slab to equivalent temperature difference. Addition research efforts on tensile stress reduction according to steady increase in the compressive strains are warranted for more accurate stress calculation.

• Food Science and Preservation
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• v.19 no.5
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• pp.703-711
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• 2012

This study was conducted to investigate the quality and organoleptic properties of dehydrated onions with steaming and heating. Sliced onions were treated as follows: steaming time ($X_1$, 5~25 min); drying temperature ($X_2$, $55{\sim}70^{\circ}C$) and drying time ($X_3$, 4~20 hr). All the variables were modelled and analyzed using a central composite design and response surface methodology (RSM). The coefficients ($R^2$) of the water content and water activity model induced from RSM were 0.9514 (p<0.01) and 0.9455 (p<0.01), respectively. The water content and water activity were affected by the drying temperature and time. The $R^2$ on the models of Hunter's L, a, b values were 0.9419 (p<0.05), 0.8818 (p<0.01) and 0.9360 (p<0.01), respectively. Hunter's L, a, b values were affected by the drying temperature and time, but Hunter's b value was not affected by the steaming time. In addition, the $R^2$ on the models of overall palatability was 0.8867 (p<0.05). The maximum palatability response was 5.92 when the steaming time was 13.14 min, the drying temperature was $63.11^{\circ}C$ and the drying time was 14.49 hr.

• Korean Journal of Agricultural Science
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• v.19 no.2
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• pp.179-186
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• 1992

This experiment was carried out to study the drying characteristics of model foods containing moisture, protein and starch on different concentration of additives such as sodium chloride and sucrose. Textural properties of model foods were measured by using UTM(instron). The results obtained are summaried as follows: As starch content and solute concentration of model foods increase, drying time was extended. The multiple regression equations for drying characteristics of additive concentration ($X_1$, %), drying time ($X_3$, hr), drying temperature ($X_2$, OC), starch content($X_4$, %) are : $$E(MC)=58.282-5.197X_3-15.151X_4-0.145X_2+2.672X_1\;R^2=0.798\;(NaCl)$$ $$E(MC)=56.651-7.253X_3-0.183X_2-42.844X_1+3.025X_4\;R^2=0.858\;(Sucrose)$$ As starch content, drying temperature and solute concentation increased, he hard ness of model foods increased.