• 설비공학논문집
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• 제12권4호
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• pp.422-429
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• 2000

Plate and shell heat exchanger(P&SHE) is widely applied as evaporators or condensers in the refrigeration and air conditioning systems for their high efficiency and compactness. In order to set up the database for the design of the P&SHE, heat transfer and pressure drop characteristics for single phase flow of water in a plate & shell heat exchanger are experimentally investigated in this study. Single phase heat transfer coefficients were measured for turbulent water flow in a plate and shell heat exchangers by Wilson plot method. The shell side heat transfer resistance was varied and the overall heat transfer coefficients were measured. The single-phase heat transfer coefficients in a plate side were obtained by Wilson plot method. Single-phase heat transfer correlations based on projected heat transfer area and friction factor correlations have been proposed for single phase flow in a plate and shell heat exchanger.

• 동력기계공학회지
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• 제3권4호
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• pp.22-27
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• 1999

Single phase heat transfer coefficients were measured for turbulent water flow in a plate & shell heat exchangers by using Wilson plot method. An experiment for counterflow heat exchange between the plate and shell was performed. The shell side heat transfer resistance was varied and the overall heat transfer coefficients were measured. The single-phase heat transfer coefficients in a plate side were obtained by Wilson plot method. Single-phase heat transfer correlations based on projected heat transfer area have been proposed for a plate & shell heat exchanger.

• 설비공학논문집
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• 제11권6호
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• pp.912-920
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• 1999

The forced convective boiling heat transfer coefficients of R-407C were measured inside a horizontal tube 6.0mm I.D. and 4.0m long. The heat transfer coefficients increased according to an increase in heat flux at constant mass flux. Because nucleation was completely suppressed in the two-phase flow region with high quality, heat transfer coefficients in forced convective evaporation were higher than those in nucleate boiling region. Average heat transfer coefficients of R-407C were about 30 percent lower than the pure refrigerant correlation, due to mass transfer resistance at the gas-liquid interface. However, the total experimental data shows an agreement with the predicted data for ternary refrigerant mixtures with a mean deviation of 30%.

• Progress in Superconductivity
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• 제8권1호
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• pp.81-86
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• 2006

We investigated resistance development in $Au/YBa_2Cu_3O_7(YBCO)$ thin film meander lines during high-power faults. The meander lines were fabricated by patterning 300 nm thick YBCO films coated with 200 nm thick gold layers into meander lines. A gold film grown on the back side of the substrate was also patterned into a meander line. The front meander line was connected to a high-power fault-test circuit and the back line to a DC power supply. Resistance of both lines was measured during the fault. They were immersed in liquid nitrogen during the experiment. Behavior of the resistance development prior to quench completion could be understood better by comparing resistance of the front meander lines with that of the back. Quench completion point could be determined clearly. Resistance and temperature at the quench completion point were not affected by applied field strength. The experimental results were analyzed quantitatively with the concept of heat transfer within the meander lines/substrate and to the surrounding liquid nitrogen. In analysis, the fault period was divided into three regions: flux-flow region, region prior to quench completion, and region after quench completion. Resistance was calculated for each region, reflecting the observation for quench completion. The calculated resistance in three regions was joined seamlessly and agreed well with data.

• 대한미생물학회지
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• 제22권3호
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• pp.295-300
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• 1987

Salmonella strains isolated from blood in the Dong-san hospital, Taegu during the period from 1971 to 1986 were studied for species distribution, drug resistance, and R plasmids. The number of strains was 2,527 and all of them were classified into S. typhi and S. paratyphi A. Approximately 300 strains were isolated in the period from 1974 to 1976 and 1978, 268 in 1982, and 204 in 1983, but the numbers isolated in the 1980's have a tendency to decrease as compared with those of the 1970's. S. typhi occupied 85% or more of strains isolated until 1976, but the isolation frequency decreased yearly with some variation, and S. paratyphi A increased gradually from 1974. Only 4 strains of S. paratyphi A were resistant to some drugs, and the resistance was not transferred to E. coli by conjugation. S. typhi resistant to drugs were 15 in 1971 through 1973, 24 in 1974, and 13 in 1975, but afterwards only few resistant strains were isolated. These strains were resistant to two or more drugs; chloramphenicol(Cm), tetracycline(Tc), streptomycin(Sm), sulfisomidine(Su), ampicillin(Ap), and kanamycin(Km) and no strain resistant to other drugs tested was found. Strains resistant to 3 or less drugs didn't transfer the resistance to E. coli by conjugation. There were 15 strains resistant to four or more drugs, and were isolated in years from 1972 to 1976. These strains transferred the resistance to E. coli, and the resistance was considered to be mediated by R plasmids. Transfer frequency was higher at $25^{\circ}C$ than at $37^{\circ}C$ and patterns of transferred resistance were Cm, Tc, Sm, Su; Ap, Km; Cm. R plasmids having markers of Cm, Tc, Sm and Su were classified into Inc H1.

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 2013년도 춘계학술대회 논문집
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• pp.1207-1208
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• 2013

• 한국지반공학회:학술대회논문집
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• 한국지반공학회 2006년도 추계 학술발표회
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• pp.409-429
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• 2006

In designing rock-socketed drilled shaft, bearing capacity evaluation is very important because the maximum values of base and side resistance are not generally mobilized at the same value of displacement, FHWA and AASHTO code suggest different ultimate bearing capacity formular according to rock type and shaft settlement. In domestic code suggest base resistance and side resistance can be added on condition that after confirming the result of field load test with axial load transfer test. This paper shows that static load test and hi-directional load test result analysis of deep rock-socketed drilled shaft in three different sites. Load-settlement curve, t-z, and q-w curve in rock-socketed part were calculated and compared. t-z curve in weathered and soft rock showed no deflection softening behavior in pretty large strain (about 2-3% of diameter). Ultimate resistance could be the summation of side resistance and base resistance in rock-socketed drilled shaft in domestic sites.

• 한국지반공학회논문집
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• 제21권5호
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• pp.187-196
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• 2005

풍화 및 절리가 발달한 암반에 근입된 말뚝의 허용지지력 결정에는 침하량이 매우 중요한 인자가 되며, 설계단계에서 말뚝두부의 침하량을 예측하기 위해서는 말뚝의 하중전이기구에 대한 이해가 필수적이다. 따라서 본 연구에서는 풍화된 암반에 근입된 현장타설말뚝의 하중전이기구에 대한 연구를 수행하였다. 이를 위해 직경 1m의 총 5본의 현장 타설말뚝을 풍화된 편마암 부지에 시공하구 재하시험 및 하중전이 계측을 수행하여 말뚝의 축방향 지지거동을 분석하였다. 암반상태를 정량적으로 파악하기 위하여 재하시험 부지의 암반에 대한 엄밀한 현장/실내시험을 수행하고, 이를 토대로 암반상태가 말뚝의 하중전이기구에 미치는 영향을 분석하였다. 하중전이 계측을 통해 얻은 주면하중전이 (f-w) 곡선은 풍화상태가 상대적으로 양호한(MW) 연암의 경우, 수 mm의 변위에서 항복에 도달하며, 이후 변위에 따른 지지하중의 증가율이 급격히 둔화되는 경향을 보였다. 반면 풍화암/풍화토에 근입된 말뚝의 f-w 곡선은 뚜렷한 항복점을 보이지 않으며, 상대적으로 큰(>15m) 변위까지 주면하중이 쌍곡선 형태로 증가하였다. 선단하중전이(q-w) 곡선은 암반상태에 관계없이 선단변위 (q-w)까지는 선형적인 거동을 보였다.

• 감성과학
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• 제25권4호
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• pp.119-128
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• 2022

본 연구의 목적은 웨어러블 에너지 하베스팅의 전도사를 통한 효율적인 전력 전달을 위해 전도사 자수 스트치 회로에서 각도와 굽힘의 개수가 저항에 미치는 영향을 분석하고 실제 태양광 패널과의 연결을 통해 손실 전력의 변화를 연구하는 것이다. 본 연구에서는 전도사 스티치 회로의 각도를 30˚부터 180˚까지 30˚단위로 설계하였으며 저항의 측정은 analog discovery2 장비를 활용하여 측정한다. 측정한 저항값을 분석하여 저항값이 급격히 변화하는 각도의 구간에서는 5˚단위로 다시 측정하여 분석한다. 이후 분석 결과를 토대로 전도사에 가해지는 장력이 수렴하는 각도를 분석하고 해당 각도에서 스티치의 굽힘 개수를 달리하여 다시 저항을 측정한다. 스티치의 각도가 줄어들수록, 굽힘의 개수가 늘어날수록 저항은 줄어듦을 확인하고 연구결과를 토대로 스티치로 인한 손실 전력을 계산한 결과 전도사 자수 스티치가 일반적인 자수에 비해 1.61배의 손실 전력을 줄일 수 있음을 고찰한다. 이러한 결과는 웨어러블 에너지 하베스팅의 전도사를 통한 전달에서 자수의 스티치가 전력 전달에 중요한 영향을 미치는 것을 시사한다. 본 연구결과를 기반으로 후속 연구에서는 곡선 형태의 스티치, 전도사의 개수 등 다양한 형태의 스티치를 비교 분석하여 웨어러블 에너지 하베스팅이 보다 효율적으로 생산 후 저장될 수 있도록 하는 전도사 회로 설계 기술을 개발하고자 한다.

• 한국전산유체공학회:학술대회논문집
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• 한국전산유체공학회 2004년도 춘계 학술대회논문집
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• pp.183-189
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• 2004

The flow and the heat transfer about the cross-flow fin-tube heat exchanger in an out-door unit of a heat pump system has been numerically Investigated. Using the general purpose analysis code, FLUENT, the Navier-Stokes equations and the energy equation are solved for the three dimensional computation domain that encompasses multiple rows of the fin-tube. The temperature on the fin and tube surface is assumed constant but compensated later through the fin efficiency when predicting the heat-transfer rate. The contact resistance is also taken into consideration. The flow and temperature fields for a wide range of inlet velocity and fin-tube arrangements are examined and the results are presented in the paper. The details of the flow are very well captured and the heat transfer rate for a range of inlet velocity is in excellent agreement with the measured data. The flow solution provides the effective permeability and the inertial resistance factor of the heat exchanger if the exchanger were to be approximated by the porous medium. This information is essential in carrying out the global flow field calculation which, in turn, provides the inlet velocity lot the microscopic temperature-field calculation of the heat exchanger unit.