• 분석과학
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• 제10권6호
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• pp.418-426
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• 1997

고주파를 이용한 오니의 건조특성에 대하여 살펴보고 재래식 건조특성과 비교 분석하였다. 고주파 건조는 빠른 속도와 높은 효율을 보였다. 재래식 건조에서는 항율건조기간이 나타나지 않았고 수분은 모세관현상에 의하여 이동하였다. 오니의 수분 중 자유수와 결합수는 존재하지 않았다. 고주파 건조에서 감율건조기간이 두 부분으로 나타났으며, 수분의 이동은 확산에 의하여 일어났다. 증발 표면적이 커질수록 수분의 제거가 촉진되었고, 오니의 지름이 커질수록 넓은 범위의 항율건조 기간이 나타났으며, 모양에 따라서도 건조특성이 다르게 나타났다. 고주파 건조에서는 오니의 중심부에서 가장 먼저 온도가 상승하였으며, 항율건조기간에서 $80{\sim}100^{\circ}C$로 일정하게 유지되면서 가장 높았다.

• 한국수산과학회지
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• 제21권1호
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• pp.16-20
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• 1988

다시마의 건조와 수축특성을 알기위한 기초자료를 얻고자 건조중인 다시마의 건조 및 수축특성에 미치는 채취부위, 공기의 온도, 상대습도 및 풍속의 영향에 관하여 실험한 결과를 요약하면 다음과 같다. 1) 다시마의 열풍건조과정은 항률건조 기간이 없이 바로 감률건조기가 나타났으며 이것은 다시 감률건조 1단계 및 2단계로 구분되었다. 2) 두께가 얇은 선단부가 기부보다 수축이 더 많이 되었으며 공기의 온도 $50^{\circ}C$, 상대습도 $30\%$, 유속 0.4m/s의 일정한 건조 조건하에서 다시마의 선단부, 중간부 및 기부를 120분까지 건조하였을 경우 수축율은 각각 $57.5\%,\;54.0\%,\;42.7\%$이었다. 3) 상대습도가 낮은것은 높은것에 비해 건조속도 및 수축속도는 빨랐으나 함수률 $20\%$까지 건조하였을 경우 수축율은 오히려 상대습도가 높은것이 증가하였다.

• Applied Biological Chemistry
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• 제17권1호
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• pp.42-48
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• 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 Advanced Marine Engineering and Technology
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• 제25권3호
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• pp.588-594
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• 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
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• 제25권3호
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• pp.453-459
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• 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.

• 환경위생공학
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• 제13권1호
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• pp.9-15
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• 1998

Microwave heating and drying processes have been well established in various industrial applications. Feasibilities of successful application of microwave drying to many material have been shown on the laboratory or pilot-plant scale. The microwave drying behavior of plating sludge are considered in this paper. The plating sludge containing 70%, 80% and 90% water exposed to microwave power at 2,450 MHz, 700W. An experimental microwave drying apparatus was designed and constructed to monitor weight loss during drying. By studying the drying characteristic curve, the moisture in sludge was almost classified into two categories : free moisture and intestinal moisture. And the critical moisture contents at which the drying rate ceases to be constant were from 10.1 to 10.5%. A simple drying model is proposed which may be used to describe drying behavior of plating sludge. The constant rate and the falling rate periods in microwave drying were addressed separately. From the eqation of constant rate period the drying rate constants decreased exponentially with increasing depth. Microwave heating compared with conventional heating offered higher heating rates from 9 to 16 times. Therefore, microwave drying process can be effective in removing moisture from plating sludge.

• 한국식품영양과학회지
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• 제21권1호
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• pp.64-69
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• 1992

Blanching 처리가 고추의 건조율 및 색도에 미치는 효과를 조사하고자 실험실 규모의 열풍 건조기를 제작하였으며 strain gage형의 load cell과 strain amplifier를 이용하여 건조 중의 중량을 연속적으로 기록, 측정하였다. 고추의 건조특성곡선은 대조군에서는 예비, 항율, 감율건조기간이 뚜렷한 반면, blanching 처리군은 감율건조기간만 존재하였으며, 시료의 건조율과 건조상수 값은 blanching 처리 온도와 시간에 비례하여 증가하는 경향이었고, $100^{\circ}C$, 3분 blanching 처리군이 가장 높게 나타났다. Capsanthin 함량 역시 대조군에 비해 처리군이blanching 처리온도와 시간에 비례하였으며 색도 값의 경우 $80^{\circ}C$, 3분 blanching군이 가장 우수하였다. blanching 처리는 전반적으로 고추의 건조율 증진 및 색도 보존에 효과적이며 $80^{\circ}C$, 3분 blanching 처리가 비교적 적합하였다.

• Food Science and Biotechnology
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• 제18권1호
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• pp.202-206
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• 2009

Drying characteristics of fresh Korean-type rehmannia (jiwhang) noodle was investigated to determine drying kinetic parameters under the experimental conditions of 5 temperatures (30, 40, 60, 80, and $90^{\circ}C$). Drying curve of the noodle showed a biphasic pattern of decrease in drying rate with initial rapid drying followed by slow dehydration as the progress in drying. In all drying conditions, only falling drying rate period was observed and the drying rate of the noodle was greatly influenced by the drying temperature. The effective diffusion coefficients ($D_{eff}$) were determined by the diffusion model and their temperature dependency was determined using an Arrhenius equation. The activation energy ($E_a$) values for the drying of the noodle were 19.94 and 21.09 kJ/mol at the initial and the latter stage of dehydration, which were comparable to those of pasta or Japanese udong dehydration.

• Journal of Biosystems Engineering
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• 제11권1호
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• pp.52-63
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• 1986

This study was performed to find out drying characteristics and develop drying model for the design of an efficient dryer or drying system of red peper. The basic model which describes drying phenomenon of red pepper was firstly established, and drying tests were conducted at 14-different drying conditions. In this test, the effects of drying air temperature and relative humidity on the rate of drying were undertaken. Finally, a new drying model based on these experimental results was developed to describe the drying characteristics of red pepper. The results from this study may be summarized as follows. 1. Drying constant of the basic model established from Lewis' experimental model and diffusion equation was theoretically deduced as a function of moisture content and inner-temperature of red pepper. 2. From the results of drying tests, drying air temperature was found to have the greatest effect on the rate of drying. However, the effect of temperature was small for the condition of high relative humidity, and for low temperature, the effect of relative humidity was found to be large even though the range of relative humidity was low. 3. Modified Henderson equation was found to be better than Chung equation as the EMC model for the estimation of the equilibrium moisture content of red Pepper. 4. Constant-rate drying period did not exist in the red pepper drying test. And falling-rate drying period was divided into three distinct phases. Drying rate was dependent on the moisture content, the inner-temperature of red pepper and the change of physical property due to drying. 5. Drying constant increased with decrease of free moisture content, but it decreased at the end of the drying period. Also, drying constant was dependent on the drying air temperature and relative humidity. 6. The new drying model developed in this study was found to be most suitable in describing the drying characteristics of red pepper. Therefore, it may be concluded that drying time could be accurately estimated by the new drying model.

• 한국식품과학회지
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• 제18권1호
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• pp.61-65
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• 1986

홍옥(紅玉)을 시료(試料)로 하여 건조조건(乾燥條件)을 다르게하여 건조특성(乾燥特性), 수분이동현상(水分移動現像), 건조중(乾燥中) 시료온도(試料溫度) 및 내부수분(內部水分)의 분포(分布)를 조사하였다. 사과의 수분확산계수(水分擴散係數)는 $1.1470{\sim}2.2148{\times}10^{-5}cm^2/sec$, 확산활성화(擴散活性化)에너지는 6.6 kcal/g mole 이었으며 Fick's law에서 아래의 식을 유도할 수 있었다. $${\In}\;{\Delta}t=In\;{\Delta}to-{\frac{D{\pi}^2{\theta}}{4d^2}}$$ 건조중(乾燥中) 내부수분분포(內部水分分布)의 이론치(理論値)와 실측치(實測値)는 거의 일치하였다.