• 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.

• Journal of Advanced Marine Engineering and Technology
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• 제20권5호
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• pp.68-75
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• 1996

The vacuum drying characteristics of water-saturated porous media were studied experimentally. The water-saturated porous media, water-saturated sand layer, was heated by the isothermal bottom wall of the rectangular vessel. The vacuum drying rate and temperature distribution of the sand layer were measured and calculated under a variety of conditions of heated wall temperature, vacuum rate, and thickness of the test material. It was found that the drying rate due to the heat and mass teansfer is greatly influenced by the heated wall temperature, vacuum rate, and thickness of the test material.

• 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.

• 동력기계공학회지
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• 제15권3호
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• pp.46-51
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• 2011

Low temperature vacuum drying technique, whose drying time and quantity of exhausting energy is about 25~30% of hot air drying, is very excellent in the drying efficiency. This paper is made out in the aspects of heat engineering with the object of developing Korean drying machine which can dry once a large quantity of objects to be dried in the state of low temperature and vacuum. As the results, it took about 17 hours(3~4 days in case of hot air drying) for material to reach about 18% of the final moisture content in order to store products for a long time, from about 78~80% of the early moisture content at the beginning of drying, and maximum drying rate comes to about 0.35 kg/m2hr at about 400% of the moisture content.

• 동력기계공학회지
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• 제14권4호
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• pp.23-28
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• 2010

Of the roughly four million known substances, about 60,000 are processed and sold ; many of these must be dried. Many materials are processed in the liquid state - ideal for mixing and reacting - but most products are needed or wanted as dry, or relatively dry, solids. Usually operation is just below atmospheric pressure, as with direct dryers, but some are built for vacuum operation with pressures as low as 26.66kPa abs.. In spite of the global-class aquiculture agriculture and fisheries technology of our country, the processing technologies are lags behind the other nations relatively. These problems are considered to be caused directly by the lack of drying technologies. This paper is concerned to the experimental results of drying heat transfer characteristics for the green energy type vacuum dryer for the high quality agriculture and fisheries production.

• Journal of Advanced Marine Engineering and Technology
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• 제24권4호
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• pp.427-434
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• 2000

In tradition, there have been two kinds of drying methods, which are sun drying and artificial drying. The sun drying method which has been adopted traditionally has been replaced by the hot-air drying method which is one of the most general methods of artificial drying, with its simple drying system, low initial cost of drying plant, and easy operating method. But the hot-air drying method has some defects; (1) much energy loss happens due to the discharge of hot air during the drying process, (2) control of drying rate is not easy on account of changing relative humidity of inlet air for uniform hot air temperature, (3) high temperature of foods in drying process brings about the production of low-grade drying products. Vacuum drying takes advantage of energy saving and mass production because it reduces the drying time by increasing the drying rate under low temperature condition. The aim of this paper is to develop the low temperature vacum dryer, with low initial investments and operating costs, easy operating method and trouble-free operation.

• Journal of Biosystems Engineering
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• 제6권2호
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• pp.58-64
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• 1982

1. 생탈곡(生脫穀)벼의 관행(慣行) 평건(平乾)의 건조특성(乾燥特性)과 각종건조(各種乾燥) 환경이 건조속도(乾燥速度)와 동할미(胴割米)의 발생(發生)에 미치는 영향을 수원 264와 미네히까리 2개(個)의 품종(品種)에 대(對)하여 조사(調査)하였다. 2. 생탈곡(生脫穀)벼 야외(野外) 건조시(乾操時) 벼의 水分含量(수분함량)은 주(主)로 조사(照射)된 누계일사량(累計日射量)에 따라 결정되었으며 건조(乾燥) 시기(初期) 벼의 수분함량(水分含量)과 일사량(日射量)과의 관계를 수식화(數式化)하였다. 3. 생탈곡(生脫較)벼 건조특성(乾燥特性)은 대체적으로 항율건조특성(恒率乾燥特性)을 따랐으며 벼층(層)의 두께가 클수록 항율건조(恒率乾燥)에 따르는 경향이 더욱 뚜렷하였다. 4. 벼층(層)의 두께와 건조속도(乾操速度)와의 관계는 지수적(指數的)인 수식(數式)으로 나타낼 수 있었다. 5. 건조기간중(乾燥期癎中) 환적효과(換積效果)는 건조속도(乾操速度)의 면(面)에서는 벼층(層)두께의 감소(減少)에 상당하는 효과(效果)를 보였으며 동할미(胴割米) 발생율(發生率)을 현격히 줄이는 효과(效果)를 나타냈으며 수원(水原) 264와 같은 장위종(長粒種)에서 그 효과(效果)는 더욱 뚜렷하였다. 6. 생탈곡(生脫穀)벼의 건조장소(乾燥場所) 간(間)에는 뚜렷한 차이(差異)는 없었으며 일사량(日射量) 기준(基準) 벼의 건조효율(乾燥效率), 건조속도(乾燥速度) 및 동할미(胴割米)등을 고려(考慮)할 때 최적(最適) 벼층(層)의 두께는 6cm정도(程度)이었다.

• Journal of Advanced Marine Engineering and Technology
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• 제26권2호
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• pp.226-232
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• 2002

In tradition, there have been two kinds of drying methods, which are sun drying and artificial drying. The sun drying method which has been adopted traditionally has been replaced by the hot-air drying method which is one of the most general methods of artificial drying, with its simple drying system, low initial cost of drying plant, and easy operating method. But the hot-air drying method has some defects ; (1)much energy loss happens due to the discharge of hot air during the drying process, (2)control of drying rate is not easy on account of changing relative humidity of inlet air for uniform hot air temperature, (3)high temperature of floods in drying process brings about the production of low-grade drying products. Also, the hot-air drying method is inducing environmental and sanitary problems which are resulting from the emission of high temperature and high humidity air, including stick on the drying progress. Vacuum drying technique, whose drying time and 7uantity of exhausting energy is about 1/3 ~1/4 of hot air drying, is very excellent in the drying efficiency. As the results, it took about 20 hours for material to reach about 18% of the final moisture content in order to store products for a long time, from about 470% of the early moisture content at the beginning of drying, and maximum drying rate comes to about $0.35 kg/m^2hr$ at about 350% of the moisture content.

• 한국응용과학기술학회지
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• 제33권1호
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• pp.58-66
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• 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.

• 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.