• 한국농림기상학회:학술대회논문집
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• 한국농림기상학회 2001년도 춘계 학술발표논문집
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• pp.139-142
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• 2001

국지기온 결정인자 가운데 특히 고도의 영향이 현저하므로 비관측점과 공간내삽에 사용되는 주변 관측점간 표고편차를 기온감율에 의해 보정해주는 간단한 방법은 상대적으로 복잡한 다른 기법들에 비해 우수한 결과를 보인다 (Nalder and Wein, 1998). 지구대기의 건조단열감율은 -0.0098$^{\circ}C$m$^{-1}$로 상수이지만, 수증기로 포화된 대기의 기온감율은 지표 부근의 -0.004$^{\circ}C$m$^{-1}$부터 대류권 중간의 -0.007$^{\circ}C$m$^{-1}$를 거쳐 권계면 부근에서는 건조단열감율과 거의 같아진다 (Wallace and Hobbs, 1997).(중략)

• 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.

• 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.

• 농업생명과학연구
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• 제43권6호
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• pp.111-115
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• 2009

본 연구는 국내에서 사용되는 건조방법 (열풍, 마이크로웨이브, 진공 등)으로는 물리적 한계에 의해 건조소요에너지, 품질 저하 및 건조속도의 한계 등이 새로운 건조방식의 요구를 만족 시켜주지 못하므로, 비가열 건조를 위해 실험용 초음파 건조기를 개발하였다. 건조조건은 4수준으로 하였으며, No. 1은 초음파 및 열풍 없이 외기, No. 2는 초음파만, No. 3은 열풍만, No. 4는 초음파 및 열풍으로 총 4가지 조건으로 당근 및 인삼 절편을 건조기 내에서 30분간 건조를 하였으며, 전 후의 중량을 측정하여 건조정도를 판단하였다. 초음파 및 열풍으로 건조한 No. 4가 건감율이 가장 높았으며, 당근 절편의 건감율은 22.4% (w.b.)/h 및 인삼 절편은 3.8%(w.b.)/h로 나타났으며, 건조물의 변색 및 절편의 뒤틀림은 거의 열풍만으로 건조한 No. 3과 거의 비슷한 정도로 나타났다.

• 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.

• 대한기계학회논문집B
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• 제35권7호
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• pp.735-742
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• 2011

인체에 유해한 질소산화물($NO_x$)의 생성을 억제하면서 열효율을 높일 수 있는 새로운 버너의 개념으로 촉매 버너가 제안되었고 본 연구에서는 대표적인 에너지 다소비 설비인 건조기에 사용하기 위한 촉매버너를 개발하였다. 산업용 건조기에 활용하기 위해 촉매버너는 평평한 매트 형태로 제작되어 열전달 면적을 극대화하였고 밀폐 공간인 건조실에 활용하기 위하여 예혼합 연소방식을 적용하였다. 새로 개발된 촉매 버너를 산업용 건조기에 적용하여 실험한 결과 열에너지가 원적외선 형태로 공급되어 감율건조 영역에서 식품과 같은 유기물을 효과적으로 건조할 수 있음을 확인하였다. 또한 건조기의 열효율은 건조속도보다 피건조물의 함수율에 보다 큰 상관관계를 나타내었다.