• Journal of Advanced Marine Engineering and Technology
• /
• 제25권3호
• /
• pp.588-594
• /
• 2001

The aim of this paper is to develop the low temperature vacuum dryer, with low initial investments and operating costs, easy operating method and trouble-free operation Usally operations just below atmospheric pressure, as with direct dryers, but some are built for vacuum operation with pressure as low 50 mmHg abs. The lowers the boiling point to $39^{\circ}C$ The experimental data of quantitative analysis for using practically were obtained by the constant drying rate period and reducing drying rate period according to the temperature of hot water which is the experimental parameters of present experiment. As the results, it took about 20 hours for material to reach about 18% of the final moisture content is order to store products for a long time about 450% of the early moisture content at the beginning of drying and maximum drying rate comes to about 0.30 kg/m2hr at about 350% of the moisture content.

• 한국식품영양과학회지
• /
• 제25권3호
• /
• pp.453-459
• /
• 1996

This study was carried out to determine the changes in quality during the drying process and the optimum drying condition for utilizing soybean curd residue. The quality criteria for soybean curd residue were acid value, peroxide value, fatty acid composition and microbial concentration. The acid values of soybean curd residue were 7.5, 4.5 and 5.9 KOH mg/g upon 12 hour drying with open-air sun, ambient-air blast and warm-air blast, respectively. The numbers of total aerobic bacteria and molds increased remarkably during drying with open-air sunlight, ambient-air blast and warm-air blast except for hot air blast. Among different drying methods, the hot air blast drying(1kg of sample) was the most effective methods, which completed in three hours. Also, the drying method demonstrated a typical drying curve ; settling down, constant rate drying and falling rate drying period were shown within one hour, from one and three hours and after three hours, respectively. Moreover, there was significant variation in the constant drying period for the quality of soybean curd residue.

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

• 한국식품과학회지
• /
• 제14권4호
• /
• pp.342-349
• /
• 1982

송풍식건조과정(送風式乾燥過程) 중의 말쥐치육의 건조기구(乾操機構)와 수분활성(水分活性)과의 관계를 검토하기 위하여 $47.5^{\circ}C$에서 풍속과 공기의 상대습도를 달리하여 실험한 결과를 요약하면 다음과 같다. 전체 건조과정은 정속건조기(定速乾燥期)와 감속건조기(減速乾燥期)로 구분되었다. 정속건조기(定速乾燥期)는 건조표면(乾燥表面)이 수분활성(水分活性) 1.0을 유지하는한 계속되었으며, 온도와 상대습도가 일정할 때 정속건조속도(定速乾燥速度)는 공기의 속도(速度)의 제곱근에 비례하였다. 감속건조기(減速乾燥期)는 건조기구(乾操機構)가 서로 다른 제(第)1 및 제(第)2감속건조기(減速乾燥期)로 구분되었다. 제(第)1감속건조기(減速乾燥期)는 모세관 응축수의 건조표면(乾燥表面)으로의 이동이 불충분한 불포화표면건조기(不飽和表面乾燥期)였으며, 이 때의 건조속도(乾燥速度)는 공기의 온도가 일정할 때 상대습도에 크게 좌우되었다. 제(第)1감속건조기(減速乾燥期)와 제(第)2감속건조기(減速乾燥期)의 변환점에서 표면경화현상(表面硬化現象)이 시작되었다. 상대습도의 변화에 따라 제(第)2감속건조기(減速乾燥期)가 시작될 때의 수분활성(水分活性)과 수분함량(水分含量)은 각각 다른 값을 나타내었다. 제(第)2감속건조기(減速乾燥期)는 다시 건조기구(乾操機構)를 달리하는 두 개의 건조기(乾燥期)로 구분되었다. 제(第)2감속건조기(減速乾燥期)의 1단계는 말쥐치육 내부의 모세관 응축수가 건조표면(乾燥表面)으로 확산, 증발하여 건조가 진행되었으며, 이때의 수분의 확산계수는 $47.5^{\circ}C$에서 $2.89{\cdot}10^{-10}m^2/sec$였다. 표면경화현상(表面硬化現象)은 말쥐치육의 수분활성(水分活性)이 0.7에 이를때까지 계속되었다. 제(第)2감속건조기(減速乾燥期)의 2단계는 수분활성(水分活性) 0.45에서 시작되었다. 이 때의 건조는 말쥐치육 내부에 다분자층(多分子層)으로 흡착(吸着)한 결합수의 건조표면(乾燥表面)으로의 확산, 증발에 의하여 진행되었다. 흡착수분(吸着水分)의 분자층(分子層)의 수는 4였으며, $47.5^{\circ}C$에서의 확산계수는 $4.38{\cdot}10^{-11}m^2/sec$였다.

• 한국식품과학회지
• /
• 제33권6호
• /
• pp.706-713
• /
• 2001

겉보리를 시료로 하여 건조조건을 다르게 하여 유동층 건조특성에 영향을 미치는 외부요인에 대해서 조사한 결과를 요약하면 다음과 같다. 겉보리의 유동층건조는 항률건조기가 없이 감률건조 1단계, 감률건조 2단계의 두 단계로 일어남을 알 수 있었다. 또한 건조속도상수는 충전량이 적을수록, 공기속도가 클수록, 공기온도가 높을수록, 상대습도가 낮을수록 컸으며, 감율건조단계에서 건조속도상수는 Arrhenius형의 plot에서 좋은 직선관계를 나타내어 이 단계가 활성화 과정임을 알 수 있으며, 감률건조 제1단계의 활성화 에너지는 1,100cal/gmol, 감률건조 제2단계의 활성화 에너지는 1,600cal/gmol을 각각 나타내었다.

• Applied Biological Chemistry
• /
• 제17권1호
• /
• pp.42-48
• /
• 1974

고추 건조방법(乾燥方法)의 개선(改善) 및 건조특성(乾燥特性)을 알기 위하여 원형(原形) 및 절단(切斷)고추에 대(對)하여 온도(溫度)및 풍속(風速)의 영향을 조사(調査)하고 고추 건조기작(乾燥機作)을 고찰(考察)하였다. 1) 원형(原形)고추 건조곡선(乾燥曲線)의 특징(特徵)은 건조초기(乾燥初期)에는 어느정도(程度)의 settling down period를 가졌고 그이 후 제일(第一), 이기(二期) 감율건조기(減率乾燥期)를 보였으나 저온건조(低溫乾燥)일수록 항속건조양상(恒速乾燥樣相)을 띠어 임계수분함량(臨界水分含量)에 이르는, 시간(時間)이 최저온도(最低溫度)인 $55^{\circ}C$에서 15시간(時間)이나 되었다. 2) 절단(切斷)고추의 건조곡선(乾燥曲線)에서는 건조속도(乾燥速度)의 변화(蠻化)가 급격(急激)하였다. 3) 절단(切斷)고추의 건조방법(乾燥方法)은 원형건조(原形乾燥)에 비해 보다 효과적(效果的)이어서 각(各) 건조온도(乾燥溫度)에서 모두 약(約) 2배(倍) 이상(以上)의 건조시간(乾燥時間)을 단축(短縮)할 수 있었다. 4) 원형(原形) 및 절단건조(努斷乾燥) 모두 건조속도상수(乾燥速度常數)(k)값은 일정(一定)하지않고 시간(時間)에따라 변화(變化)하였으나 양건조방법(兩乾燥方法)에서 k값의 시간(時間)에 대(對)한 변화양상(變化樣相)이 구별(區別)되었다. 5) 건조속도상수(乾燥速度常數) k 값을 일정(一定)한 평균치(平均値)로 택(擇)할 경우, 원형건조(原形乾燥)에 대(對)하여는 $M-M_e/M_o-M_e=e^{-0.118t}$식(式는)이 절단건조(切斷乾燥)에 대(對)하여는 $M-M_e/M_o-M_e=e(-0.342t^{0.128})$식(式)이 적용되었다.

• Journal of the Korean Wood Science and Technology
• /
• 제25권4호
• /
• pp.99-107
• /
• 1997

This study was executed to test the possibility of replacement for domestic Japanese larch(Larix leptolepis) for hardwoods and to acquire the information about the effects of drying temperature on internal temperature, moisture content and drying defects. In high-temperature drying, internal temperature increased rapidly to boiling point, immediately after that point the internal temperature rising rate was reduced. In the case of drying at temperature of $125^{\circ}C$, internal temperature could reach at boiling point in a very short time. Moisture content in high-temperature drying showed constant drying rate period and first period of falling rate drying together in 4 hours since experiment begun. There was no strong correlation between initial moisture content and final moisture content. Average drying rate at $115^{\circ}C$, $120^{\circ}C$ and $125^{\circ}C$ was 1.42%/hr, 1.88%/hr and 2.02%/hr, respectively; the case of drying temperature of $125^{\circ}C$ showed most rapid drying rate. Drying rate of $125^{\circ}C$ was so rapid that it showed more severe shrinkage, bow, collapse, end check, and internal check development than in other drying conditions. The result of this study showed the strong possibility of high-temperature drying for Japanese larch, and to dry Japanese larch optimally, dry bulb temperature should not exceed $120^{\circ}C$.

• Journal of the Korean Wood Science and Technology
• /
• 제22권2호
• /
• pp.61-70
• /
• 1994

This study was executed to find the applicability of press drying of tree disk by investigating the shrinkage and drying defect and to form appropriate model by comparing the actual moisture content(MC) and internal temperature in respect of drying time with calculated values based computer simulation to which was applied finite difference method. In press drying disk, heating period, constant drying rate period maintained plateau temperature at 100$^{\circ}C$ and falling drying rate period were significantly distinguished. Actual MC and internal temperature were analogous to those calculated at comparing points. Heat transfer model formed by Fourier's law using specific heat of moist wood and conduction coefficient considering fractional volume of each element of wood cell wall, bound water, free water and air showed applicability as basic data to developing heat expansion, shrinkage and drying stress during press drying. Also mass transfer model formed by Fick's diffusion law using water vapor diffusion coefficient showed applicability. Longitudinal shrinkage was developed by pressure of hot press and tangential shrinkage was restrained by hygrothermal recovery. The heart check, surface check and ring failure were occurred differently in species, but V-shaped crack didn't develop.

• Journal of Biosystems Engineering
• /
• 제6권2호
• /
• pp.48-57
• /
• 1982

In order to improve the quality of traditionally sun-dried red peppers and to increase the efficiency of drying performance, three types of solar dryers were designed and built, and drying performance of the solar dryers was compared to traditional sun drying. Results obtained from the experiment are summarized as fallows: 1. The air temperature and relative humidity profiles over a 8-hour period measured at the specified locations in the drying chamber of solar dryers appeared to have large variation in each dryer. The rate of drying increased with the temperature rise in the drying chamber of the solar dryer. 2. In general. drying with solar dryers proceeded faster than traditional sun drying. With A'-type of solar dryer developed in the second experiment it was possible to dry red peppers in seven days from an initial moisture content of 80% to safe storage conditions. The drying time with the A'-type solar drier was 50% shorter compared to traditional sun drying. 3. Red peppers appeared to have an increasing or constant-rate drying period until the weight of the product was reduced to about one half the initial weight, followed by a falling-rate drying period. When the dried red peppers were exposed to the atmospere during the night, the moisture content increased as much as 6%, which is much higher than for the grains. 4. It was suggested from the experiment that either a heat storage system or a supplemental heating system in the solar dryer was desirable for more efficient drying operation. 5. It was shown that the solar dryer developed in this study may be suitable for drying other vegetables and fishes, and also offered additional advantages of saving in drying time, maintaining sanitation and minimizing contamination by dust, insects and unfavorable weather condition.

• 한국응용과학기술학회지
• /
• 제33권1호
• /
• pp.58-66
• /
• 2016

저온진공건조 조건에 따른 곶감의 건조특성 및 품질적 변화를 분석하였다. 곶감의 건조 특성은 전형적인 항율건조기간과 감율건조기간이 존재함을 확인 할 수 있었다. 진공압력이 높을수록 가열온도가 높을수록 곶감의 당도, 당 함량, 경도 값은 높게 나타났으며 이에 비해 명도 값은 낮게 나타남을 알 수 있었다. 기존 천일 및 열풍건조를 대처할 수 있는 진공건조의 최적 조건은 진공압력이 40~50kPa abs., 가열온도 $30^{\circ}C$, 건조시간은 3~4일 이었다.