• Preventive Nutrition and Food Science
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• 제13권3호
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• pp.225-230
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• 2008

Onion slices were dehydrated in a single layer at drying air temperatures ranging from $50{\sim}70^{\circ}C$ in a laboratory scale convective hot-air dryer at an air velocity of 0.66 m/s. The effect of drying air temperature on the drying kinetic characteristics were determined. It was found that onion slices would dry within $210{\sim}460\;min$ under these drying conditions. Moisture transfer during dehydration was described by applying the Fick's diffusion model and the effective diffusivity changed between $1.345{\times}10^{-8}$ and $2.658{\times}10^{-8}\;m^2/s$. A non-linear regression procedure was used to fit 9 thin layer drying models available in the literature to the experimental drying curves. The Logarithmic model provided a better fit to the experimental drying data as compared to other models. Temperature dependency of the effective diffusivity during the hot-air drying process obeyed the Arrhenius relationship with estimated activation energy being 31.36 kJ/mol. The effect of the drying air temperature on the drying model constants and coefficients were also determined.

• 동력기계공학회지
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• 제10권2호
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• pp.54-61
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• 2006

In order to prevent the environmental pollution, the dryers are commonly used to treat sludge that one of sewages is polluting the quality of water. Generally, the drying method is various as to the property of material and use. Rotary dryer is a good apparatus to treat them. The rotary dryer is the way that is to make substance transmission and heating using hot air between sludge particles and heated gas. In this paper, we performed a numerical analysis of the inner air flow of the ANDRICH type dryer through the changing rotational speed from 3rpm to 10rpm. A PIV can be applied to research a inner flow of ANDRICH type dryer.

• 설비공학논문집
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• 제28권10호
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• pp.408-413
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• 2016

The objective of this study is to investigate the performance of a heat recovery heat pump dryer using a R245fa refrigerant experimentally. In this study, the main components of the heat pump dryer were an evaporator, a compressor, a condenser, and an expansion valve. As a result, when the amount of refrigerant varied from 15 kg to 16 kg, the hot air outlet temperature in the condenser and the heat transfer rate were almost kept constant. Therefore, the amount of refrigerant at 16 kg was considered to be a suitable amount in the heat pump. As the air inlet velocity varied from 0.5 m/s to 1.5 m/s, the highest temperature in the condenser could be obtained when the air inlet velocity was 0.5 m/s. The heat transfer rate, system (COP), and hot air outlet temperature were 5.6 kW, 3.4, and $102.5^{\circ}C$, respectively, when the bypass ratio and water temperature were 0% and $60^{\circ}C$.

• 한국산학기술학회논문지
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• 제13권9호
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• pp.3827-3834
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• 2012

최근 많은 열에너지를 필요로 하는 열풍식 건조기 대신 에너지 효율이 높은 히트펌프 건조기가 제지, 섬유, 목재, 식품 등 다양한 분야에서 사용되고 있다. 본 논문에서는 냉동 농산물 건조 초기에 전기히터 사용을 최소화하여 에너지 효율을 높이고자, 압축기 출구 고온가스 우회 시스템에 대한 히트펌프 사이클 특성을 이론적으로 고찰하였다. 또한, 추가 열을 확보하기 위하여 외부공기 유입을 위한 댐퍼를 고려하였고 이의 최적화를 통해 에너지 효율 향상이 가능함을 보였다.

• 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.

• 한국지열·수열에너지학회논문집
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• 제14권4호
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• pp.7-12
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• 2018

Energy performance of electric heater and geothermal source heat pump type hot air dryers are compared in this study. For set temperatures of $30^{\circ}C$, $35^{\circ}C$ and $40^{\circ}C$, radish is dried from initial mass 60 kg until it gets 5 kg, where the difference equals the amount of water removed. As set temperature is increased, drying time is shortened for both electric heater and heat pump types, however energy efficiency is decreased due to increasing electricity consumption. Moisture extraction rate(MER) of electric heater is 2.58~2.84 kg/h, and for heat pump type 2.56~2.71 kg/h, showing little difference between the two types. Specific moisture extraction rate (SMER) of electric heater is 0.94~0.96 kg/kWh, and for heat pump type 1.72~2.21 kg/kWh. SMER of heat pump type is greater by 0.78~1.25 kg/kWh than the electric heater hot air dryer, which is 1.8~2.3 times better in terms of energy efficiency.

• 에너지공학
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• 제19권4호
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• pp.228-233
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• 2010

기존의 열풍건조기의 효율은 약 30% ~ 50%인 반면, 최적 설계된 열풍-열펌프 건조기 효율은 약 60% ~ 80% 수준이므로 에너지 효율향상과 에너지 절약을 이룰 수 있다. 외국의 여러 사례에서는 기존 대비 약 60% ~ 80%의 에너지를 절약할 수 있으며, 밀폐형 순환방법을 사용하여 건조공기에 포함될 수 있는 환경오염물질의 외부로의 유출을 최소화 할 수 있어 기존의 건조기에 비해서 환경문제에 적극적으로 대응할 수 있을 것을 판단된다. 본 논문에서는 이와 같은 특성을 가진 건조기에 적용하기 위한 고온 생산이 가능한 열펌프를 얻기 위하여 시스템의 사이클을 설계하고 시스템을 구축하여 목표 성능을 만족하는지 여부를 확인하였다. 본 연구에서는 열펌프 복합건조기 적용을 위한 고온용 열펌프 시스템을 설계하고 제작한 후, 성능평가를 수행하여 다음의 결론을 얻었다. (1) 고온생산을 위한 시스템 설계는 2사이클이 가장 우수한 것으로 나타났다. (2) 2사이클 시스템은 저단이 R134a를, 고단이 R124를 냉매로 사용할 경우 가장 적합한 것으로 나타났다. (3) 사이클 운전을 통하여 상용압력으로 간주되는 범위에서 R134a시스템은 $75^{\circ}C$, R124시스템은 $95^{\circ}C$ 생산이 가능한 것으로 나타났다. (4) 수냉식 2사이클 시스템의 성능 시험을 수행한 결과 목표성능을 상회하는 결과를 얻어 고온 생산이 가능한 열펌프 시스템의 설계 및 제작이 가능한 것으로 나타났다.

• 대한용접접합학회:학술대회논문집
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• 대한용접접합학회 2006년도 춘계 학술대회 개요집
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• pp.146-147
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• 2006

In order to prevent the environmental pollution, the dryers are commonly used to treat sludge that one of sewages is polluting the quality of water. Rotary dryer is a good apparatus to treat them. The rotary dryer is the way that is to make substance transmission and heat using hot air between sludge particle and heated gas. In this paper, a numerical analysis was performed for the structural analysis of the 3-pass rotary dryer through the finite elemeny method and an experiment was done for the structural stability. And reasonable relation was found between analysis and experiment.

• 동력기계공학회지
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• 제10권2호
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• pp.36-40
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• 2006

In order to prevent the environmental pollution, the dryers are commonly used to treat sludge that one of sewages is polluting the quality of water. Generally, the drying method is various as to the property of material and use. Rotary dryer is a good apparatus to treat them. It is the way that is to make substance transmission and heat using hot air between sludge particle and heated gas. In this paper, we developed a 3-pass rotary dryer for a design program for the 3-pass rotary dryer with various conditions. The working conditions of dryer are a raw sludge feed rate, input & output water content and operation time etc.

• 접착 및 계면
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• 제17권2호
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• pp.62-66
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• 2016

수용성 접착제의 경화 공정은 일반적으로 열풍건조기를 대부분 사용하고 있다. 열풍건조기는 열에 의해서만 수용성 접착제를 경화시키는 방법으로서, 충분한 경화를 위해 $100^{\circ}C$ 이상의 높은 온도와 최소 20 min 이상의 경화 공정을 요구하는 단점을 가지고 있다. 경화 과정 중에 온도가 너무 높을 경우, 접착제의 점도가 낮아져 접착에 방해가 될 수 있으며, 경화 과정 중에 발생하는 수분에 의해 경화 조건이 일정하게 유지되기 어렵다. 본 연구에서는 제습 막 건조기 시스템을 활용하여, 수용성 접착제의 경화 공정을 일정하게 유지시키고 공정 중의 제습을 통해 건조공기의 공급으로 경화시간을 단축하고자 한다. 제습 막 건조기 시스템을 활용한 최적의 경화 조건을 찾고, 제습 막 건조기 시스템의 효과를 확인하기 위하여, 제습 막 건조기와 강제순환 건조기를 적용한 경화 과정을 통해 접착력(peel strength)을 측정하여 비교 분석해 보았다.