• 출판저널
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• 통권85호
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• pp.19-19
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• 1991

• 월간 기계설비
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• 통권113호
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• pp.53-62
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• 1999

• 한국영양학회:학술대회논문집
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• 한국영양학회 2002년도 추계학술대회 및 총회
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• pp.132-132
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• 2002

• 대한방사선협회지
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• 제28권1호
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• pp.345-345
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• 2002

• 대한방사선협회지
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• 제29권1호
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• pp.226-226
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• 2003

• 대한기계학회논문집
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• 제19권6호
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• pp.1501-1509
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• 1995

It is known that the heat and mass transfer characteristics in the absorber are most sensitive of the temperature boost of all the heat exchangers and the development of a more efficient absorber should be highly important. This paper describes absorption experiments made with different inside tube diameters, tube length and tube shapes. The purpose of this study is to acquire basic knowledge about heat and mass transfer in a falling film type absorber with vertical inner tubes. Heat and mass transfer were measured for water vapor absorption into a Lithium Bromide-water solution flowing down an absorber of vertical inner tubes. As a result, insert spring tube compares bare tube and heat transfer improved by order of insert spring tube P2(pitch 20 mm) and P1(pitch 10 mm).

• 대한기계학회논문집B
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• 제21권2호
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• pp.294-302
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• 1997

Falling-film evaporation experiments for aqueous solution of lithium bromide (LiBr) were performed on a horizontal smooth 19.05-mm-dia copper tube. Average heat transfer coefficients were obtained with varied film Reynolds numbers, system pressures, LiBr concentrations and degrees of wall superheat. Heat transfer coefficients increase with increasing system pressure and decreasing concentration. For degrees of wall superheat, the heat transfer coefficient did not't show the distinct trend. For this experimental ranges, heat transfer coefficients showed maximum values at an optimal film Reynolds number. The results of this work were compared with pool boiling data reported previously, and it was shown that the heat transfer performance is superior to the pool boiling.

• 한국수자원학회:학술대회논문집
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• 한국수자원학회 2007년도 학술발표회 논문집
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• pp.1184-1188
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• 2007

하수관거는 장기간 사용에 의해 오염물질 퇴적 현상이 발생하여 관거 유하능력의 기능을 상실하게 되는 문제점이 발생한다. 관내 오염물질 제거 방법 중 관거 Flushing 방법을 적용하였을 경우, 유입유량, 유입시간, 관경사 변화에 따른 유속 및 수위 변화를 분석하여 하수관거 내 부유물질의 퇴적을 방지하기 위한 최소유속기준을 만족하는 관거 유하 길이를 분석하고자 한다. 관거 내의 수리학적 거동을 분석하기 위해서 SWMM 및 FLOW-3D 모형을 이용하여 관거 내 수리학적 거동 현상을 분석하였다. 또한 모형의 적용성을 검증하기 위해서 수리모형실험 자료를 이용하였다. $5\;{\textperthousand}$ 관경사에 대하여 유입유량 $0.16\;m^3/min$을 3 분 동안 Flushing 하였을 경우 최대유속은 0.58 m/s로 최소유속 0.6 m/s를 만족하는 관의 누가거리는 확보할 수 없는 것으로 모의되었다. 또한 관경사가 증가함에 따라서 최대유속 및 최대유량도 증가함을 보여주고 있다. 이와 같은 분석을 통해 관 내 부유물질의 퇴적을 방지하기 위해 Flushing 방법을 수행하였을 경우, 보다 효과적이며 경제적으로 Flushing 방법을 수행할 수는 설계 자료를 제공할 수 있을 것으로 기대된다.

• 설비공학논문집
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• 제13권5호
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• pp.422-430
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• 2001

In the present study, an evaporative generation process of ammonia-water solution film on the vertical plate was analysed. For the utilization of waste heat, hot water of low temperature was used as the heat source. The continuity, momentum, energy and diffusion equations for the solution film and vapor mixture were formulated in integral forms and solved numerically. Counter-current solution-vapor flow resulted in the refrigerant vapor of the higher ammonia concentration than that of co-current flow. Eve the rectification of refrigerant vapor was observed near the inlet of solution film in counter-current flow. For the optimum operation of generator using hot water, numerical experiments, based on the heat exchange and generation efficiencies. revealed the inter-relationships among the Reynolds number of the solution film and hot water, and the length of generator. Enhancement of heat and mass transport in the solution film was found to be very effective for the improvement of generation performance, especially at high solution flow rate.

• 설비공학논문집
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• 제13권8호
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• pp.720-729
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• 2001

The effect of vapor flow direction on falling film heat transfer was experimentally investigated by using water. Parallel flow (both water and vapor downwards) showed higher heat exchange performance than counterflow(downward water and upward vapor). The difference became significant as the vapor flow rate was increased. It is supposed that the uprising vapor disturbs the solution film flow and heat transfer is reduced by uneven distribution or detachment of water film.