• 산업식품공학
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• 제14권2호
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• pp.106-111
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• 2010

본 연구는 일정한 실험조건 하에서 골심지 시료에 따른 골 성형 실험을 행하여 골심지에 의한 하이로골의 발생과 골판지상자의 압축강도의 관계에 대하여 조사하였다. 골판지의 골 높이가 낮은 골(low corrugation)의 비율이 많은 골심지 그레이드는 장력 변동의 저항에도 약하며 골심지의 이탈력에 의한 강탈(stealing)이 일어나기 쉽고, 결과적으로 낮은 골 비율이 높아졌으며, 골심지 두께 편차가 큰 골심지는 골 성형 시에 슬립현상을 발생하기 쉽기 때문에 불규칙한 골을 연속 형성하는 경향이 있었다. 또한 골심지의 그레이드에 따른 하이로골 분포비율의 실험결과 일반적 경향으로는 그레이드가 높은 골심지 일수록 낮은 골비율이 적었다. 골 성형된 골판지 시트의 두께의 경우는 원지 평량과의 상관성은 적고 골심지 두께와 상관하며 y=3.9732x+4.2712, $R^{2}=0.8142$), 골심지의 밀도에 역상관한다((y=-3.1213x+6.8736, $R^{2}=0.9919$). 하이로골 중에서 낮은 골 분포를 크게 나타낸 골심지 재료의 골판지로 만든 골판지상자의 압축강도가 현저히 낮고 골심지 시료의 그레이드에 따라 13%의 차이가 있었으며 압축강도의 편차도 골심지의 시료에 따라 21%로 크며, 골심지 골은 원지의 두께 및 밀도 등 물리적 특성치의 변동과 관계한다.

• 설비공학논문집
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• 제13권7호
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• pp.588-594
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• 2001

The purpose of this study is to investigate the thermal and hydrodynamic characteristics of the channel in corrugated plate type heat exchangers numerically. Numerical work has been conducted using the Reynolds Stress Model(RSM) by utilizing the commercial finite-volume code, FLUENT. Based on this model, the dependence of heat transfer and friction factor on geometrical parameters have been investigated. It is found that larger corrugation angle give higher values of heat transfer coefficients and friction factors. As the reynolds number increases, the heat transfer coefficient also increases. It is also observed that the heat transfer coefficient reaches maximum while the friction factor stays relatively low at same corrugation angle. Through the analysis, it is found that the optimum corrugation angle for the heat exchanger performance exists. It is noted that the flow repulsions at the contact point of the two fluid streams make the low mixing more active for larger corrugation angle and high reynolds number.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2003년도 추계학술대회
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• pp.97-102
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• 2003

An experimental study is conducted to investigate the effects of duct corrugation angle on heat/mass transfer characteristics in wavy ducts by using a naphthalene sublimation technique. The corrugation angles of the wavy ducts are $145^{\circ}$ , $130^{\circ}$ and $115^{\circ}$ . and the Reynolds numbers based on the duct hydraulic diameter vary from 300 to 3,000. At the low $Re(Re{\leq}1000)$, high heat/mass transfer regions are formed by the secondary vortex flows called Taylor-Gortler vortices on both pressure-side and suction-side walls. At the high $Re(Re{\geq}1000)$, the effects of these secondary flows are vanished. As corrugation angle decreases, the local peak Sh induced by Taylor-Gertler vortices are increased and average Sh also enhanced. More pumping power (pressure loss) is required with the smaller corrugation angle due to the stronger secondary vortex flows.

• 대한기계학회논문집B
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• 제28권7호
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• pp.789-799
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• 2004

An experimental study is conducted to investigate the effects of duct corrugation angle on heat/mass transfer characteristics in wavy ducts of a primary surface heat exchanger application. Local heat/mass transfer coefficients on the wavy duct sidewalls are determined by using a naphthalene sublimation technique. The corrugation angles(${\alpha}$) of the wavy ducts are 145$^{\circ}$, 130$^{\circ}$, 115$^{\circ}$ and 100$^{\circ}$. And the Reynolds numbers based on the duct hydraulic diameter vary from 300 to 3,000. The results show that at the low Re(Re $\leq$1000), the secondary vortices called Taylor-Gortler vortices perpendicular to the main flow direction are generated due to effect of duct curvature. By these secondary vortices, high heat/mass transfer regions are formed on both pressure-side and suction-side walls. At the high Re(Re $\geq$ 1000), these secondary flows are vanished with helping flow transition to turbulent flow and the regions which show high heat/mass coefficients by flow reattachment are formed on suction side. As corrugation angle decreases, the local peak Sh induced by Taylor-Gortler vortices increase at Re $\leq$1000. At high Re(Re $\geq$ 1000), by the existence of different kind of secondary flows called Dean vortices, non-uniform Sh distribution appears along spanwise direction at the narrow corrugation angle (${\alpha}$=100$^{\circ}$). Average Sh also increase by the enhanced effect of secondary vortices and flow reattachment. More pumping power (pressure loss) is required with the smaller corrugation angle due to the enhancement of flow instability.

• 한국음향학회지
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• 제23권3호
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• pp.192-196
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• 2004

스피커 댐퍼의 재질에 따른 휨강도와 기하학적 요소인 주름의 반경 및 각 주름의 곡률반경으로 탄성계수를 결정하여 실험치와 비교하였다. 그 결과 댐퍼의 탄성은 휨강도에 비례하고 원형주름의 반경에는 반비례하며 주름의 곡률반경의 제곱에 반비례함을 알 수 있었다. 또, 댐퍼의 안쪽은 주름을 작게 만들고 바깥쪽은 주름을 크게 만든 변형 댐퍼로 스피커를 제작함으로서 고음부의 감도가 증가하면서도 저음부가 강화되는 소형 스피커를 만들 수 있었다.

• 한국초전도ㆍ저온공학회논문지
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• 제25권2호
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• pp.19-24
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• 2023

Recently, interest in renewable energy such as solar and wind power has increased as an alternative to fossil fuels. Renewable energy sources such as large wind farms require long-distance power transmission because they are located inland or offshore, far from the city where power is required. High-Temperature Superconducting (HTS) power cables have more than 5 times the transmission capacity and less than one-tenth the transmission loss compared to the existing cables of the same size, enabling large-capacity transmission at low voltage. For commercialization of HTS power cables, unmanned operation and long-distance cooling technology of several kilometers is essential, and pressure drop characteristic is important. The cryostat's spiral corrugation tube is easier to bend, but unlike the round tube, the pressure drop cannot be calculated using the Moody chart. In addition, it is more difficult to predict the pressure drop characteristics due to the irregular surface roughness of the binder wound around the cable core. In this paper, a CFD model of a spiral corrugation tube with a core was designed by referring to the water experiments from previous studies. In the four cases geometry, when the surface roughness of the core was 10mm, most errors were 15% and the maximum errors were 23%. These results will be used as a reference for the design of long-distance HTS power cables.

• 한국전자파학회논문지
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• 제27권5호
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• pp.486-489
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• 2016

논문에서는 corrugation 구조의 적용과 PTFE 테플론(비유전율=2.1) 유전체 렌즈의 삽입을 통하여 우수한 임피던스 매칭 특성과 고이득 성능을 가지는 corrugated 혼 안테나가 제안되었다. 제안된 안테나는 X 밴드(8~12 GHz)에서 -25 dB 이하의 측정 반사손실 성능을 가지고, 중심 주파수인 10 GHz에서 최대 이득이 22.3 dBi이며, 안테나의 전체 크기는 $110mm{\times}110mm{\times}135mm$이다. 제안된 안테나의 성능을 고려하였을 때, 레이더식 레벨 트랜스미터 시스템에 삽입되기에 적합하며, 특히 LNG 및 LPG와 같이 낮은 비유전율 및 반사율을 가지는 물질이 저장된 선박 혹은 해양플랜트 내부의 가스탱크에 적용될 수 있을 것으로 사료된다.

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 1997년도 춘계학술대회 논문집
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• pp.620-624
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• 1997

Corrugated membranes which are used as a means of liquid- and gas-sealing for a LNG storage tank and provide one of the most reliable primary barrier are the main component of in-ground membrane types for the assurance of high safety. It absorbs large thermal and mechanical deformations caused by ultra low temperature of LNG, -162 .deg.c, the cryogenic liquid and mechanical deformations caused by was carried out on crossing corrugation by commercial F.E code, ANSYS. This paper presents some of results in stress analysis of membranes performed for the purpose to investigate the strength of existing membrane for LNG storage tank designed by IHI,MHI, KHI and KGC expect for Technigaz eariy published. Based on these analytical studies,design criteria were estabilished and SHI original membranes having a high level of safety and fitting to larger capacities were developed.

• 한국전자파학회논문지
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• 제19권8호
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• pp.913-919
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• 2008

본 논문에서는 밀리미터파 시스템에 응용이 가능한, 마이크로스트립으로 급전되는 초광대역 테이퍼 슬롯 안테나의 새로운 설계법을 제시하고 그 실험결과를 보여주고 있다. 초광대역 특성을 가지는 마이크로스트립-CPS 전이 구조 혹은 발룬을 적용하여 테이퍼 슬롯 안테나 고유의 초광대역 특성을 얻었고, 안테나와 발룬의 연결은 임피던스 정합의 방법을 이용함으로 테이퍼 슬롯 안테나 설계를 간단하게 하였다. 테이퍼 슬롯 안테나 설계에는 페르미-디락(Fermi-Dirac) 테이퍼 함수와 corrugation을 적용하였다. 제안된 안테나는 23 GHz에서 58 GHz까지의 초광대역 주파수 특성을 가졌으며, 12에서 14 dBi의 비교적 높고 평탄한 이득과 낮은 부엽 레벨을 가졌다. 또한, 4개의 소자로 이루어진 간단한 선형 배열 안테나를 통하여 광대역 위상 배열 및 밀리미터파 센서에 응용될 수 있음을 보였다.

• 설비공학논문집
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• 제15권10호
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• pp.809-820
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• 2003

The present study investigates effects of flow velocity on the convective heat/mass transfer characteristics in wavy ducts of a primary surface heat exchanger application. Local heat/mass transfer coefficients on the wavy duct sidewall are determined by using a naphthalene sublimation technique. The flow visualization technique is used to understand the overall flow structures inside the duct. The aspect ratio and corrugation angle of the wavy duct is fixed at 7.3 and 145$^{\circ}$ respectively, and the Reynolds numbers, based on the duct hydraulic diameter, vary from 100 to 5,000. The results show that there exist complex secondary flows and transfer processes resulting in non-uniform distributions of the heat/mass transfer coefficients on the duct side walls. At low Re (Re<1000), relatively high heat/mass transfer regions like cell shape appear on both pressure and suction side wall due to the secondary vortex flows called Taylor-Gortler vortices perpendicular to the main flow direction. However, at high Re (Re>1000), these secondary flow cells disappear and boundary layer type flow characteristics are observed on pressure side wall and high heat/mass transfer region by the flow reattachment appears on the suction side wall. The average heat/mass transfer coefficients are higher than those of the smooth circular duct due to the secondary flows inside wavy duct. And also friction factors are about two times greater than those of the smooth circular duct.