• Journal of the Korean Wood Science and Technology
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• 제29권1호
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• pp.1-8
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• 2001

소나무, 잣나무, 낙엽송과 웨스턴 햄록의 5두께(3, 5, 7, 9 및 11cm) 제재를 3가지 종류의 건조스케줄을 적용한 가열판 압체식 진공건조에서 건조중 함수율, 제재두께와 건조속도의 관계, 제재두께와 건조시간계수의 관계 등을 구명한 결과에서 제재두께 초기함수율 및 건조시간에 따른 건조중 함수율을 추정할 수 있었다. 그리고 함수율 30%에서 15% 범위에서 평균 건조속도는 웨스턴 햄록이 가장 컸고 다음은 소나무, 잣나무, 낙엽송 순위였으며, 제재두께가 증가함에 따라 곡선적으로 감소하였다. 또한 건조시간계수는 제재두께가 증가함에 따라 곡선적으로 증가하였다.

• 펄프종이기술
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• 제43권4호
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• pp.49-58
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• 2011

The maximum drying shrinkage velocity was proposed to verify bulk and stiffness improvement mechanism during drying according to papermaking parameters. It was based on the wet-web shrinkage behavior without the restraint of wet-web during drying, so intact drying impact could be measured. Bulking agent reduced the drying shrinkage and the maximum drying shrinkage velocity, so paper bulk increased and paper strength decreased. When adding cationic starch to stock with the bulking agent for strengthening, the bulk was increased further with additional decreasing of the drying shrinkage and the maximum drying shrinkage velocity. Paper strength also increased except tensile stiffness index with decreasing the drying shrinkage and the maximum drying shrinkage velocity. When using additional strength additives for strengthening of fiber interfaces extended by bulking agent and cationic starch, amphoteric strength additive increased paper stiffness without loss of paper bulk. It was considered that the added amphoteric strength additives were cross-linked to the stretched cationic starch and this cross-linking increased elasticity of fiber-polymer-fiber interfaces without changing the drying behavior. Paper bulk could be increased with decreasing the maximum drying shrinkage velocity. The drying shrinkage of paper also could be controlled by fiber-to-fiber bonding interfaces by the bulking agent. In this case, paper strength including stiffness was decreased by reducing fiber-to-fiber bonding but it could be improved by strengthening fiber-to-fiber interfaces with polymer complex without loss of bulk.

• 한국재료학회지
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• 제23권10호
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• pp.592-598
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• 2013

Graphene oxide powders prepared by two different drying processes, freeze drying and spray drying, were studied to compare the effect of the drying method on the physical properties of graphene oxide powder. The graphene oxide dispersion was prepared from graphite by chemical delamination with the aid of sulfuric acid and permanganic acid, and the dispersion was further washed and re-dispersed in a mixed solvent of water and isopropyl alcohol. A freeze drying method can feasibly minimize damage to the sample, but it requires a long process time. In contrast, spray drying is able to remove a solvent in a relatively short time, though this process requires exposure to a high temperature for a rapid evaporation of the solvent. The powders prepared by freeze drying and spray drying were characterized and compared by Raman spectroscopy, X-ray diffraction, field-emission scanning electron microscopy, transmission electron microscopy, and by an elemental analysis. The graphene oxide powders showed similar chemical compositions; however, the morphologies of the powders differed in that the graphene oxide prepared by spray drying had a winkled morphology and a higher apparent density compared to the powder prepared by freeze drying. The graphene oxide powders were reduced at $900^{\circ}C$ in an atmosphere of $N_2$. The effect of the drying process on the properties of the reduced graphene oxide was examined by SEM, TEM and Raman spectroscopy.

• Journal of Biosystems Engineering
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• 제18권3호
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• pp.270-274
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• 1993

Many researches have been performed to shorten drying time and cost of red pepper in Korea. Nevertheless, an effective drying method for red pepper is not developed yet. This study was conducted to analyze the effect of opening ratio of red pepper's surface on drying for development of an effective drying method. The drying method with punching treatment is expected to be effectively utilized for shortening drying time and improving quality of red pepper.

• 태양에너지
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• 제7권1호
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• pp.14-22
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• 1987

This paper presents an experimental study of a solar drying system designed and installed by KIER. Experiments have been performed using the KIER system for the drying of marine products, such as squid. Presented in detail are the experimental observations of collector air temperature, solar intensity, absorber plate temperature, drying chamber temperature, humidity and other measures of drying chamber performance with variation of air mass flow rate. As a result, average temperature attained in the drying chamber during autumn weather has been adequated for drying of squids.

• 한국축산시설환경학회지
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• 제8권3호
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• pp.177-182
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• 2002

녹용의 상품화를 위해서는 건조과정이 필요하다. 지금까지의 인공건조는 사육농가 스스로의 경험에 의한 건조가 대부분으로 이는 건조시설 및 건조방법의 미흡으로 비효율적이며, 건조 중 변질되거나 먼지, 세균 등에 오염되기 쉽다. 최근 선진국에서는 농산물의 고품질건조를 위한 다양한 건조방법들이 실용화되고 있으며 마이크로파를 이용한 건조방법도 그 중의 하나이다. 이러한 점에 착안한 본 연구에서는 우리가정에 널리 보급되어 있는 전자레인지를 이용한 녹용의 건조 가능성 여부를 검토하였으며 그 결과는 다음과 같다. 1. 녹용의 각질화 여부가 건조시간에 많은 영향을 끼치는 것으로 나타나, 건조시간과 건조소요에너지를 줄이기 위해서는 녹용을 부위별로 절편하여 건조시키는 것이 효과적인 것으로 나타났다. 2. 같은 건조시간에서도 템퍼링 시간의 길고 짧음에 따라 건조속도가 다르게 나타났으며, 각질화 진행 정도에 따라 템퍼링 시간의 조절이 필요한 것으로 판단된다. 3. 전자레인지를 이용한 녹용의 건조는 2분 건조 후 3분 템퍼링을 반복하는 것이 효과적인 것으로 나타났다. 4 본 실험결과 전자레인지의 마이크로파를 이용한 건조기술을 녹용 건조에 이용할 수 있을 것으로 생각된다. 5. 본 연구에서는 건조시간과 템퍼링 시간에 따른 건조만을 검토하였으나, 앞으로의 연구는 건조 후의 녹용의 성분변화 여부에 대한 검토가 필요한 것으로 사료된다.

• Journal of Biosystems Engineering
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• 제16권4호
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• pp.372-383
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• 1991

This study was performed to find out optimum drying conditions of red pepper to minimize energy consumption and drying time, respectively, under the quality constraint using Box's complex method. The results from this study are summarized as follows. 1. From the optimization results for the drying process, energy consumption was minimized at the drying condition to minimize drying time. 2. The optimization results according to drying method was found out to be greatly affected by the quality constraint of red pepper. Especially, the turning point to change drying stage was a very important factor in the drying method with two stages.

• 한국식품저장유통학회지
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• 제4권3호
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• pp.271-278
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• 1997

Drying of Shiitake mushroom was investigated to see the effect of temperature, relative humidity of drying air and diameter of the pileus on its rates. The drying rate was increased with the increase of the air temperature and the decrease of the relative humidity. The external color was dark brown at higher drying temperature and higher relative humidity. Exponential and Thompson nodel were found to describe well the raying process of the Shiitake mushroom.

• 펄프종이기술
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• 제31권5호
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• pp.31-46
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• 1999

A drying paper strives to shrink due to the shrinkage of the individual paper fibres. Laboratory results show that a reduction of the shrinkage or an imposed stretch leads to a large increase in tensile stiffness and a large decrease in strain at break. In c cylinder drying section the water in the web is repeatedly heated on the drying cylinder and evaporated in the free draw. To evaluate the drying process regarding influence on paper properties these sub-processes, or drying phases, have to be studied separately. The effect of the conditions on the drying cylinder and on the VacRoll is investigated in pilot trails. Both the fabric tension on the drying cylinder and on the VacRoll reduces the shrinkage of the paper. The laboratory results are used as input to a numerical simulation of the conditions in the free draw. If the web width is increased or the length of the free draw is reduced the mean shrinkage of the paper web is reduced . However, the difference in shrinkage between the middle and the edge of the web is increased.

• 수산해양기술연구
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• 제42권4호
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• pp.259-266
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• 2006

In this study, the 2-way condensation system was designed applying air-to-air heat pump to dry a marine product such as squid in the winter. And to be made the drying apparatuses by this system, there are two kinds of type, A type, was set a compressor outside of the drying apparatus, B type, was set a compressor in the drying room. And then the variations of temperature in drying room were measured to compare the heating performance of the drying apparatuses between A type and B type at $-6.5^{\circ}C$, outdoor temperature. The temperature of the drying room for B type was increased to $36^{\circ}C$ but the temperature of the drying room for A type was not increased to $36^{\circ}C$, to be increased to $20^{\circ}C$.