• 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.

• 한국식품영양과학회지
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• 제43권6호
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• pp.884-892
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• 2014

본 연구에서는 원적외선 이용하여 단풍취를 박층 건조할 경우 건조온도와 송풍속도에 따른 건조특성과 건조제품의 색도 변화를 조사하였고, 건조 전후 취나물의 항산화 성분과 항산화력 변화를 분석함으로써 고품질의 원적외선 건조 취나물 제품 생산을 위한 기초 자료를 제시하고자 하였다. 단풍취의 건조속도는 원적외선 박층 건조온도와 송풍속도가 증가할수록 빨라지고, 건조시간이 단축되는 것으로 나타났다. 특히 원적외선 박층 건조온도 $50^{\circ}C$의 송풍속도 0.8m/sec에서 건조속도가 가장 빠른 것으로 나타났다. 본 연구에서 검증한 건조모델 중 Thompson 모델은 결정계수가 0.9826 이상, RMSE는 0.1277 이하로 나타나, Lewis, Page, Henderson 모델보다 단풍취의 원적외선 박층 건조 시 함수율비 예측 정밀도가 높은 것으로 나타났다. 원적외선 박층건조 후 단풍취의 ${\Delta}L$(명도)값은 원적외선 건조온도와 송풍속도가 빠를수록 증가하는 경향을 보였고, ${\Delta}a$(적색도/녹색도)와 ${\Delta}b$(황색도) 값은 원적외선 건조온도가 낮고, 송풍속도가 느릴수록 갈변하는 현상이 심화되는 것으로 나타났다. 원적외선 박층 건조 후 단풍취의 ${\Delta}E$(색차)값도 원적외선 건조온도가 낮고, 송풍속도가 느릴수록 증가하는 경향을 보였다. 항산화 성분인 폴리페놀 함량의 경우 원적외선 건조온도가 높을수록 감소량이 증가하였고 원적외선 박층 건조 후 37.36~55.21% 감소하는 경향을 보였으며, 원적외선 박층건조조건 중 원적외선 건조온도 $40^{\circ}C$의 송풍속도 0.8m/sec와 $45^{\circ}C$의 송풍속도 0.6 m/sec 조건에서 감소율이 낮은 것으로 나타났다. 플라보노이드 함량의 경우에도 원적외선 박층 건조 후 32.24~44.18% 감소하는 것으로 나타났고, 원적외선 건조온도 $40^{\circ}C$의 송풍속도 0.8 m/sec와 $45^{\circ}C$의 송풍속도 0.8 m/sec 조건에서 감소율이 낮은 것으로 나타났다. 항산화력의 경우에도 원적외선 건조온도가 높을수록 감소하는 경향을 보였고, 원적외선 건조조건 중 $40^{\circ}C$의 송풍속도 0.8 m/sec와 $45^{\circ}C$의 송풍속도 0.6 m/sec 조건에서 항산화력 감소율이 다른 건조조건보다 낮은 것으로 나타났다. 따라서 단풍취의 건조시간, 건조 중 변색, 항산화 성분 및 항산화력 등을 고려하면 단풍취 건조제품의 고품질화를 위해서는 원적외선 박층 건조온도 $45^{\circ}C$의 송풍속도 0.6, 0.8 m/sec가 적절한 건조조건으로 판단된다.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 2005년도 하계 학술대회 논문집
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• pp.137-145
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• 2005

The effects of air temperature and sample thickness on drying kinetics of strawberry leather were investigated. The mathematical modeling was performed by using three thin-layer dying models. The independent variables were sample thickness (S1 = 1.8, S2 = 2.7, and S3 = 3.6mm) and air temperature (50, 60, 70, and 80$^{\circ}$C). All samples took place in the falling rate period. The values of effective moisture diffusivity, D$_{eff}$ varied from 2.40 to 12.1$^{\times}$10-9m$^{2}$/s depending on drying conditions. The values of activation energy, E$_{a}$ were 35.57, 33.14, and 30.46 KJ/mol for each sample of S1, S2, and S3. The two-term exponential model was found to satisfactorily describe the thin-layer drying kinetics of strawberry leather.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 1993년도 Proceedings of International Conference for Agricultural Machinery and Process Engineering
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• pp.896-905
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• 1993

Thin-layers of wheat and barley are dried at near-ambient temperatures(3.5$^{\circ}C$ -5$0^{\circ}C$) in order to obtain the intrinsic drying data. The well established apparatus was modified to enable it to record all the sample weight data in still air by using a purpose -built automatically controlled sliding valve. The air could be diverted in less than 0.5seconds and a 7 second period was required to attain a steady weight reading. With this apparatus, very smooth drying curves were obtained. The data of sample weight , drying temperature and dew point temperature wee recorded continuously . The drying process was terminated when the moisture content change in 24 hours was less than 0.004 d.b. This was achieved by drying a sample for about a week . The final points were recorded as the dynamic equilibrium moisture content(EMC). The drying data were than fitted to the exponential Newton model and the dynamic EMC data were fitted to the Modified-Chung-Pfost Model . All the fitted parameters are given and comparison is made with previous published data. The comparisons who that the current drying constants are lower than the previous data, the dynamic EMC data obtained for wheat and barely agree with the previous data. The results show that to obtain the drying constant in the exponential Newton model, adequate drying time is necessary.

• Journal of Biosystems Engineering
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• 제41권4호
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• pp.342-356
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• 2016

Purpose: The drying of a thin layer of native cassava starch in a tray dryer was modeled to establish an equation for predicting the drying behavior under given conditions. Methods: Drying tests were performed using samples of native cassava starch over a temperature range of $40-60^{\circ}C$. We investigated the variation in the drying time, dynamic equilibrium moisture content, drying rate period, critical moisture content, and effective diffusivity of the starch with temperature. The starch diffusion coefficient and drying activation energy were determined. A modification of the model developed by Hii et al. was devised and tested alongside fourteen other models. Results: For starch with an initial moisture content of 82% (db), the drying time and dynamic equilibrium moisture content decreased as the temperature increased. The constant drying rate phase preceded the falling rate phase between $40-55^{\circ}C$. Drying at $60^{\circ}C$ occurred only in the falling rate phase. The critical moisture content was observed in the $40-55^{\circ}C$ range and increased with the temperature. The effective diffusivity of the starch increased as the drying temperature increased from 40 to $60^{\circ}C$. The modified Hii et al. model produced randomized residual plots, the highest $R^2$, and the lowest standard error of estimates. Conclusions: Drying time decreased linearly with an increase in the temperature, while the decrease in the moisture content was linear between $40-55^{\circ}C$. The constant drying rate phase occurred without any period of induction over a temperature range of $40-55^{\circ}C$ prior to the falling rate period, while drying at $60^{\circ}C$ took place only in the falling rate phase. The effective diffusivity had an Arrhenius relationship with the temperature. The modified Hii et al. model proved to be optimum for predicting the drying behavior of the starch in the tray dryer.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 1993년도 Proceedings of International Conference for Agricultural Machinery and Process Engineering
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• pp.906-911
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• 1993

There will be about 0.25 to 0.3billion tons of grain product including rice, wheat and corn etc. each year in China. An energy analysis on grain drying system on which electricity , oil , coal or sun power and batch, tower with thick or thin layer of grain, infra red radiation. fluidized flowing types grain drying systems were made and compared for the sake of energy saving is shown in this paper.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 1997년도 동계 학술대회 논문집
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• pp.149-154
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• 1997

• Journal of Biosystems Engineering
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• 제12권2호
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• pp.38-43
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• 1987

An experimental study was conducted to develop a thin-layer rewetting equation of short grain rough rice of Akihikari variety. Four thin-layer rewetting equations were experimentally determined from $25^{\circ}C$ to $45^{\circ}C$ and 70%RH to 85%RH conditions. Diffusion, Henderson, Page, and Thompson equations widely used as thin-layer drying equations were selected. Experimental data were fitted to these equations using linear regression analysis except diffusion equation. The diffusivity in the diffusion equation was determined by optimization method. Four equations were highly significant. In order to compare the goodness of fit of each equation, the error mean square of each equawas calculated. The diffusion model was not a very good model because the error mean square was very large. The other three models showed the same level or error mean square and could predict satisfactorily the rewetting rate or short grain rough rice.

• Journal of Biosystems Engineering
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• 제27권3호
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• pp.219-226
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• 2002

Desorption equilibrium moisture contents of oak mushroom were measured by the static method using salt solutions at flour temperature levels of 35$\^{C}$, 45$\^{C}$, 55$\^{C}$ and 6$\^{C}$ and five relative humidity levels in the range from 11.0% to 90.8%. EMC data were fitted to the modified Henderson, Chung-Pfost, modified Halsey and modified Oswin models using nonlinear regression analysis. Drying tests far oak mushroom were conducted in an experimental dryer equipped with air conditioning unit. The drying test were performed in triplicate at flour air temperatures of 35$\^{C}$, 45$\^{C}$, 55$\^{C}$ and 65$\^{C}$ and three relative humidities of 30%, 50% and 70% respectively. Measured moisture ratio data were fitted to the selected four drying models(Lewis, Page, simplified diffusion and Thompson models) using stepwise multiple regression analysis. The results of comparing root mean square errors for EMC models showed that modified Halsey was the best model, and modified Oswin models could be available far oak mushroom. The results of comparing coefficients of determination and root mean square errors of moisture ratio for four drying models showed that Page model were found to fit adequately to all drying test data with a coefficient of determination of 0.9990 and root mean square error of moisture ratio of 0.00739.

• Composites Research
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• 제32권6호
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• pp.314-318
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• 2019

본 연구에서는 습식 코팅 방식 중 하나인 다층박막적층법의 자동화 시스템을 제작하였다. 특히, 본 연구에서 제안한 자동화 시스템은 다층박막적층법의 공정 변수(예를 들어, 증착 재료, 코팅 깊이, 코팅 및 헹굼 시간)를 제어함으로써 손으로 작업하는 것과 동일한 변수 조작이 가능하게 설계되었다. 자동화 시스템을 통해 기판을 완벽하게 용액 안으로 침액시킬 수 있으며, 이를 통해 특별한 분자간 결합(예를 들어, 정전기적 인력, 공유 및 수소 결합)을 통해 기판 위에 균일한 다층의 박막 형성이 가능하다. 두 종류 이상의 용액으로 기판이 침액될 때, 이 기판은 다른 용액으로 이동되기 전에 청소 구역에서 헹굼과 건조 과정을 거친다. 이러한 담금, 헹굼, 건조 과정은 모두 컴퓨터 프로그램에 의해 제어 가능하다. 본 연구에서는 자동화 시스템을 통해 그래핀을 기반으로 하는 다층박막 샘플을 제작하였고, 균일한 그래핀의 적층 여부를 분석하기 위해 제작된 샘플의 흡광도와 두께를 측정하였다. 기판 위에 그래핀과 고분자 층의 적층이 진행될수록 흡광도와 두께가 균일하게 증가하는 결과를 통해, 본 연구에서 제작한 자동화 시스템이 수작업을 통한 다층박막의 적층을 완벽하게 대체 가능함을 알 수 있었다.