• Transactions of the Korean Society of Mechanical Engineers
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• v.13 no.6
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• pp.1292-1300
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• 1989

본 연구에서는 비원형관의 평판길이의 변화가 평판과 원관사이의 상호작용 으로 나타나는 온도장, 유동장, 국소 Nusselt 수 및 평균 Nusselt 수에 미치는 영향 에 대하여 고찰하였다.

• Korean Journal of Mathematics
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• v.13 no.2
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• pp.183-191
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• 2005

In this paper we find the Laurent series expansions representing the reproducing kernels. Also we find the number of zeroes of the exact Bergman kernel via parallel slit domain in order to relate the exact Bergman kernel to an extremal problem.

• Proceedings of the SAREK Conference
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• 2005.06a
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• pp.135-135
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• 2005

• Proceedings of the Korean Nuclear Society Conference
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• 2004.05a
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• pp.118.2-118.2
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• 2004

• Proceedings of the Korean Nuclear Society Conference
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• 2005.05a
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• pp.757-758
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• 2005

• Proceedings of the Korean Nuclear Society Conference
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• 2005.05a
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• pp.623-624
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• 2005

• Proceedings of the Korean Society of Precision Engineering Conference
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• 2011.06a
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• pp.1505-1506
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• 2011

• Proceedings of the Korean Nuclear Society Conference
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• 1999.05a
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• pp.158-158
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• 1999

• Proceedings of the KSME Conference
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• 2001.06d
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• pp.201-207
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• 2001

We modeled the liquid film dryout(LFD) process for both tube and annulus which have uniformly heated vertical channels. We set phenomenological initial conditions in the model. The initial void fraction on the onset of the annular flow location is derived from the physical chum-to-annular flow criterion with the help of the drift-flux-model. The initial thermodynamic-equilibrium-quality is calculated by iteration with the flow quality to find the onset of the annular-flow location. Present model tends to predict very well at the lower exit quality but under-estimates at the higher exit quality. We found that the prediction error of the present model is gradually bigger as the inlet subcooling approaches near the saturation. We obtained excellent results for both tube and annulus channels as the mean of 0.97 and root-mean-square error of 11% for the number of 3883 experimental data on tubes, and of 0.96 and of 12% for 593 on annuli. The present model extended the applicable range to the relatively low exit quality region than previous LFD models.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.24 no.2
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• pp.306-315
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• 2000

An experimental study was conducted to examine the internal flow patterns inside the mixing chamber of effervescent atomizers. The mixing chamber has the rectangular cross section ($8mm{\times}2mm$) and made of transparent acrylic plate for flow visualization. The parameters tested were the air/liquid ratio (ALR), injection. pressure, and the nozzle orifice diameter. Three different flow regimes were observed; bubbly, annular, and intermittent flows. In the bubbly flow regime, the discharged mixture was disintegrated into drops through the bubble expansion and the ligament breakup. On the other hand, in the annular flow regime, the liquid annulus was disintegrated into small drops by the aerodynamic interaction between the phases due to the high relative velocities between the gas and the liquid. In the intermittent flow regime, the bubble-expansion/ligament-disintegration mode and the annulus-disintegration mode appeared alternatively. The correlations representing the transition criteria between the two-phase flow patterns within the mixing chamber were proposed based on the drift-flux models.