• Journal of the Korean Wood Science and Technology
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• 제29권1호
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• pp.1-8
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• 2001

소나무, 잣나무, 낙엽송과 웨스턴 햄록의 5두께(3, 5, 7, 9 및 11cm) 제재를 3가지 종류의 건조스케줄을 적용한 가열판 압체식 진공건조에서 건조중 함수율, 제재두께와 건조속도의 관계, 제재두께와 건조시간계수의 관계 등을 구명한 결과에서 제재두께 초기함수율 및 건조시간에 따른 건조중 함수율을 추정할 수 있었다. 그리고 함수율 30%에서 15% 범위에서 평균 건조속도는 웨스턴 햄록이 가장 컸고 다음은 소나무, 잣나무, 낙엽송 순위였으며, 제재두께가 증가함에 따라 곡선적으로 감소하였다. 또한 건조시간계수는 제재두께가 증가함에 따라 곡선적으로 증가하였다.

• 한국식품과학회지
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• 제21권2호
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• pp.203-211
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• 1989

근채류를 열풍건조할 경우 수축변형 및 표면 경화현상을 일으켜 품질변화를 수반하게 되므로 본 연구에서는 온도, 상대습도 및 풍속을 조절할 수 있고 건조중의 시료크기 변화를 측정할 수 있는 실험실 규모의 건조장치를 제작하여 무우 및 고구마의 건조특성과 수축특성에 영향을 미치는 외부 요인들에 대해 조사하였다. 건조속도는 무우 및 고구마 모두 항률건조기, 감률건조기, 감률건조 2단계 a 및 b의 4단계로 구분되어 나타났다. 수축속도 곡선은 각각 건조속도에 대응하여 기울기가 다른 4단계로 나타났으며 항률건조 기간에서는 수축속도가 서서히 증가하다가 감률건조 1단계에서 급격히 증가하였고 감률건조 2단계의 초기에 상당하는 점에서 최대에 달하였다. 또한 시료의 두께. 상대습도 및 초기 함수율 등은 표면적 수축에 큰 영향을 미쳤고 시료의 두께가 얇을수록, 그리고 상대습도 및 초기 함수율이 높을수록 평형 상태에서의 수축율은 증가하였다.

• 품질경영학회지
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• 제44권3호
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• pp.487-508
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• 2016

Purpose: Current testing method for drying rate used in military textiles has different results according to the public testing institute. So the purpose of this study was to suggest the alternative method which secure the reliability of the drying rate test. Methods: We measured the drying rate by various test methods for military clothes 14 species including quick drying function and compared the test results. Also, the collected data through the test was analyzed using one-way ANOVA. The p-value of results was compared by various testing institutions. Results: The results of this study are as follow; A deviation occurred among the testing institutions in original test method(KS K 0815). Whereas it is verified that there is no deviation among the institutions in 5% significance level by another test method(ISO 17617). Also it would increase work efficiency by reducing the testing time required to test by using ISO 17617. Conclusion: Based on the results, we can suggest the reliable test method of the drying rate.

• International Journal of Advanced Culture Technology
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• 제3권2호
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• pp.138-143
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• 2015

This paper was aimed to study the drying kinetics of coffee and to investigate the thin-layer drying kinetics of coffee by using a convective air dryer. The coffee was dried for the temperatures of 40, 50 and $60^{\circ}C$ with relative humidity in the range of 14-25% the airflow rate fixed at 1 m/s. According to the experiment result, the drying rate curve showed that drying process took place only in the falling rate period. Seven thin layer drying models (Newton, Page, Henderson and Pabis, Logarithmic, Wang and Singh, Two terms, Modified Henderson and Pabis) were fitted to the experimental moisture content data. The Two-trem model was found to be a better model for describing the characteristics of coffee for the temperatures of 40, 50 and $60^{\circ}C$. The effective moisture diffusivity of coffee increased when the drying temperature increased. The value was in the range of $4.5028{\times}10^{-11}$ to $6.4803{\times}10^{-11}m^2/s$.

• 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.

• 한국식품과학회지
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• 제21권2호
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• pp.212-217
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• 1989

무우 및 고구마를 열풍건조하고 건조가 진행됨에 따라 표면적 변화를 측정하여 실험치와 잘 일치하는 건조수축식과 총괄적 건조 속도식을 구하였으며, 시료의 두께, 상대습도 및 풍속을 포함한 초기 건조속도의 함수관계 식을 구하였다. 건조속도 상수와 차수는 시료의 두께와 공기의 온도에 영향을 받았으며 일정한 건조 (d=4mm, $Ta=50^{\circ}C$, RH=10%, U=0.8m/s) 하에서 얻어진 총괄적 건조속도 식과 수축식은 무우는 $dx/dt=0.112{\times}10^{-2}{\cdot}A{\cdot}:(1-x)^{0.43}$, A=Ao(-0.480x+1)이었고, 고구마는 $dx/dt=0.115{\times}10^{-2}\;A(1-x)^{0.49}$, A=Ao(-0.368x+1)이었다. 또한 초기 건조속도의 변화는 시료의 두께, 상대습도, 및 풍속에 대해 무우는 $dx/dt=0.0648\;(RH)^{-0.31}\;(d)^{-0.75}\;(U)^{0.39}$이었고, 고구마는 $dx/dt=0.0547(RH)^{-0.28}\;(d)^{-0.63}\;(U)^{0.37}$이었다.

• 설비공학논문집
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• 제2권2호
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• pp.105-111
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• 1990

The drying rate in freeze drying was obtained by experiment of garlic moisture contents depending on the drying time. Freeze drying experiment of garlic juice was carried out in vaccum freeze drier of laboratory scale by backface heating, and a mathematical model is also used to simulate the process of simultaneous heat and mass transfer in freeze drying to compare with experimental data.

• 한국산림과학회지
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• 제87권4호
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• pp.577-583
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• 1998

우리 전통 악기용 밤나무와 오동나무 향판용재를 여름 초순부터 잔적하여 70일간 옥외 천연건조와 150일간 옥내 천연건조하여 함수율, 건조속도 및 건조시간을 비교하였다. 밤나무 판재의 평균 최종함수율과 건조속도는 옥외천연건조의 경우 각각 20.6%와 0.78%/일(日)이었고, 옥내 천연건조의 경우 각각 16.6%와 0.44%/일(日)이었다. 오동나무 판재의 평균 최종함수율과 건조속도는 옥외 천연건조의 경우 각각 16.7% 와 1.53%/일(日)이었고, 옥내 천연건조의 경우 각각 13.5%와 0.77%/일(日)이었다. 이들 수종의 옥외 평균 천연건조속도는 옥내 경우보다 2배 정도 더 컸었는데 섬유포화점(30%) 이상에서 매우 컸었으며 감율건조하다가, 섬유포화점 이하에서는 불규칙하게 감소하였다. 그러나 옥내 천연건조속도는 밤나무의 경우 함수율 55% 이상, 그리고 오동나무의 경우는 함수율 80% 이상에서 컸었으며 감율건조하다가, 이들 함수율 이하부터 불규칙하게 감소하였다.

• 한국환경과학회지
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• 제30권2호
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• pp.135-143
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• 2021

This study executed evaluation of drying characteristics based on the polymer injection rate (8%, 10% and 12%) and the drying method[NIF(near-infrared ray). According to this study analyzed VS, VS/TS, and calorific value compared with 'the auxiliary fuel standard of the thermoelectric power plant and the combined heat & power plant'. The results are as follows. In the case of NIR, the VS was slightly changed at the early stage of the material preheating period and the constant drying rate period with low moisture evaporation. But VS reduction was shown higher as moisture was dried. In the case of non-digested sludge with high VS content, the VS reduction rate by drying was shown lower than that of digested sludge. As the flocculant injection rate increased, the VS loss due th drying was found to be small. Also, the higher the flocculant injection rate was the longer the drying time. Especially, in the case of the NIR drying equipment, as the moisture content of sewage sludge decreased(moisture content 20~40%), the loss of net VS also showed a tendency to increase sharply. It is shown that the high calorific value according to the drying time of the non-digested sludge was changed from 590 kcaℓ/kg to 3,005 kcaℓ/kg and from 539 kcaℓ/kg to 2,796 kcaℓ/kg.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2006년도 하계학술발표대회 논문집
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• pp.1191-1196
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• 2006

Analysis of drying characteristics has been carried out with one-dimensional model in the dryer using the principle of the refraction of radiation. The dryer is composed of hot water tank, a plastic film conveyer belt, drying material, etc. The model considers the conduction and radiation within the plastic film and drying material. The film is semitransparent to radiation and the drying material is assumed to be semitransparent or opaque to radiation. The results shows that the effect of radiative transfer on the drying rate is relatively large when the thickness of drying material is small and the water temperature is high. When the material is thin, the drying rate by only conduction is also enhanced so that drying time can considerably be reduced.