• Environmental engineer
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• s.182
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• pp.62-67
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• 2001

본 연구에서는 기존의 로터리 방식이나 플래시 방식 등의 직접열에 의한 건조방식이 2차 공해 유발 및 폭발이나 화재의 위험을 항상 내포하는 등 여러 가지 단점이 있으므로 이러한 문제점을 연속 감압식 간접열 방식의 건조장치를 개발하여 근원적으로 해결하고자 하였다. 본 연구의 목표는 50kg/hr용량의 연속 감압식 간접열 방식의 디스크 건조장치를 개발하여 건조효율을 70$\%$ 이상 향상시키며(기존의 제품은 50$\%$

• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 1999.12a
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• pp.436-443
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• 1999

• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 1999.07a
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• pp.301-306
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• 1999

현재까지 인삼건조에 관한 연구는 단편적이며 또한 열풍건조의 온도 조건에 따른 물리 화학적 품질 변화 등에 국한되고 있으며 최 등(1992)이 백삼과 태극삼의 평형함수율과 열풍 건조 방정식을 체계적으로 개발한 연구가 있었으나 건조 에너지와 품질의 관점에서 새로운 건조기의 개발 등에 관한 연구는 거의 없는 실정이다. (중략)

• Journal of Biosystems Engineering
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• v.25 no.2
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• pp.115-122
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• 2000

This study was performed to develop a prototype continuous flow ginseng dryer with which better product quality and lower drying energy consumption could be achieved compared with conventional ginseng dryers. A dryer having both far infrared ray (IR) and heated-air as the drying energy sources was designed and fabricated . Dryer performance was studied by examining energy efficiencies and dryer performance evaluation indices (DPEI) during the drying tests of medium-sized four year ginseng roots with IR radiating plate temperature and drying air temperature in the range of 80-12$0^{\circ}C$ and 22-5$0^{\circ}C$, respectively. The DPEI of IR /heated -air combined drying was 1/3 of that of the conventional heated-air drying when ginseng were dried to the same final moisture ratio. When ginsengs were dried for 12 hours in the prototype IR/heated-air combination dryer, a linear relationship was found to exist between final moisture ratio and ginseng temperature. As the drying progressed, drying air temperature inside the dryer was nearly constant but ginseng temperature was drastically increased during the first two hours and gradually increased thereafter until the end of drying. With the prototype Ir/heated-air combination dryer, the drying rate changed little but the energy efficiency increased proportionally when the amount of ginseng to be dried increased. Drying capacity, energy efficiency, and DPEI of the prototype IR/heated-air combination ginseng dryer were estimated to 1.500 roots, 65% and 3.800kJ/kg-water , respectively.

• Proceedings of the SAREK Conference
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• 2007.06a
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• pp.74-74
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• 2007

• Journal of Biosystems Engineering
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• v.22 no.3
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• pp.279-288
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• 1997

This study was worked out to obtain fundamental data needed for developing a continuous type dryer. The drying process in a cross-flow type continuous dryer was expressed as partial differential equations, and a drying simulation model for predicting rice moisture content, rice temperature, drying air absolute humidity, drying air temperature was developed by using the finite difference method. To validate the performance of the drying simulation model, a prototype continuous dryer was constructed in this study. The size of the test dryer was one-tenth to that of a commercial continuous dryer. The difference in the outlet rice moisture content between the predicted values and the measured values was within 0.5%, that of outlet rice temperature was below $3^{\circ}C$, that of drying air temperature in drying bed was within $8^{\circ}C$ and that of relative humidity of outlet drying air was big because of the different measuring point. In addition, a drying simulation model for a actual size continuous dryer with double flow was developed in this study. This drying simulation model included the rice mixing effect in the middle of drying length. The difference of outlet moisture content between the predicted and the measured values showed below 0.5% in this study.

• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 2003.02a
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• pp.112-117
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• 2003

우리나라의 미곡종합처리장(Rice Processing Complex, RPC)은 1991년 시범사업으로 2개소가 설치된 이래 2002년 말 현재 328개소가 설치 운영되고 있다. 현재 RPC는 벼의 수확 후 처리공정을 일관화 한 시설일 뿐만 아니라 쌀 유통의 중심시설로 성장하였다. RPC의 건조시설은 대부분이 열풍건조와 상온통풍건조를 조합하여 사용할 수 있도록 설계되어 있다. 열풍건조에는 순환식건조기와 연속식건조기가 이용되고 있으며, 상온통풍건조에는 원형철제빈(사일로)이 주로 이용되고 있으며 일부 사각빈이 이용된다. 원형철제빈은 벼의 건조와 저장을 겸용하고 있다. (중략)

• Resources Recycling
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• v.24 no.6
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• pp.54-60
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• 2015

The objective of this study is to develop a belt-type dryer with a capacity of 1 ton/day, thereby improving drying efficiency by more than 70% and reducing the size of dryers by more than 50%, and thus making dryers smaller and lighter to reduce the installation and operation costs by more than 20%. We identified structural improvements by analyzing existing dryers employing indirect heating and verified the superior drying performance of the proposed method through some basic experiments. Furthermore, we verified the improvements in the heat transfer and drying characteristics as we conducted the experiments at reduced pressure.

• Resources Recycling
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• v.9 no.4
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• pp.28-36
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• 2000

This study describes to analyze the characteristics for separation and recovery of both the dried particles and the purified solvent from the waste solvent through the vaporization process by the continuous and instantaneous vacuum drying system. The vacuum drying system for the waste solvents recovery consists of a feeding pump, a double pipe heat exchanger, a vacuum spray chamber, and a condenser. The vacuum drying system heats the waste solvent to the vapor in the double pipe heat exchanger and the expanded vapor is sprayed at the end of the tube. The vaporized solvent in the condenser are recovered. The particles in the waste solvent are separated and dried from the vapor in the vacuum spray chamber. Performance evaluation of the vacuum drying system was conducted using the mixture of the dried pigment particles and benzene or alkylbenzene as test samples. For the mixture of 10 wt% pigment particles an 90% benzene, the recovery efficiency of benzene was 88% with the purity of 99% and the recovery efficiency of dried particles was 94% with the moisture of 1.1 wt%. The size of pigment particles was decreased from $6.5\mu\textrm{m}$ to $5.6\mu\textrm{m}$ in diameter due to high speed spraying and dispersion in the vacuum drying system during drying process. Therefore, the vacuum drying system showed to be an effective method for separating particles and solvent in the waste solvent.

• Journal of the Korea Organic Resources Recycling Association
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• v.16 no.3
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• pp.29-37
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• 2008

The objective of this research is to evaluate the optimum treatment methods for disposal sludge cake at different temperatures and periods of time. The disposal dehydrated sewage cake used in this study was obtained from N wastewater treatment plant in the P City. This system consists of continuous conveyer thermal dryer and pyrolysis. The continual conveyer thermal dryer was operated to evaluate the optimum conditions with temperature settings, ranges from 130 to $180^{\circ}C$, loading rates of 650~750 kg/hr and operating times of 110~120 minutes. The continual pyrolysis was also operated to evaluate the optimum conditions with temperature settings, ranges from 650 to $750^{\circ}C$, loading rates of 100~158 kg/hr and operating times of 20~40 minutes. The sewage sludge cake has a moisture content of 78~80% (wt) which decreased up to 1~3%(wt) resulted in breaking of cell wall after operating the continuous conveyer thermal dryer and pyrolysis. Important parameters which were operating times, moisture contents, loading rates, conveyer velocities and rotary velocities effects on the thermal kinetics and dynamics were investigated to evaluate the optimum conditions for the continual thermal dryer and pyrolysis.