This paper is concerned with a remedy for interface smearing,which is usable when fixed (i.e. non moving and so non conforming) grids are employed. It is simple to employ and has been found to be rather effective. T...This paper is concerned with a remedy for interface smearing,which is usable when fixed (i.e. non moving and so non conforming) grids are employed. It is simple to employ and has been found to be rather effective. The paper explains its principle, describes how it has been implemented and presents some results obtained with its assistance. The results are compared both with those of earlier methods of interface motion calculation and with experimental data.展开更多
Aim To develop a hydrodynamic model on the void fraction in liquid slugs for gas liquid slug flow in vertical tubes. Methods Developing the model by considering the gas exchange between the Taylor bubble and the fo...Aim To develop a hydrodynamic model on the void fraction in liquid slugs for gas liquid slug flow in vertical tubes. Methods Developing the model by considering the gas exchange between the Taylor bubble and the following liquid slug. Results Some experimental data are obtained to check the model. In comparison with previous published results, the predictions from this model are better and in good agreement with the experimental data. The error is within ±20%. Conclusion The proposed model can correctly predict the void fraction in liquid slugs for gas liquid two phase slug flow in vertical tubes.展开更多
This paper deal with the frictional resistance characteristics of gas liquid two phase flow in vertical upward helical coiled tubes under the system pressure 0.1 0.6MPa. By means of dimension analysis and π theo...This paper deal with the frictional resistance characteristics of gas liquid two phase flow in vertical upward helical coiled tubes under the system pressure 0.1 0.6MPa. By means of dimension analysis and π theorem, the correlation formulas were obtained for calculating the frictional resistance coefficients of gas liquid two phase flow in helical coiled tubes. The calculated results agree well with the experimental results.展开更多
In the present work, an experimental research was carried out on the air-water two phase flow patterns and their transition characteristics in the shell-side of a segmentally baffled horizontal shell -tube heat exchan...In the present work, an experimental research was carried out on the air-water two phase flow patterns and their transition characteristics in the shell-side of a segmentally baffled horizontal shell -tube heat exchanger model of horizontally-cut baffles. In the inlet crossflow zone, the two -phase flow was in vertical downflow across an in-line (square) horizontal tube bundle with a pitch to diameter ratio. p/D of 1. 28. The flow pattern sketch was obtained by visual observation. The flow pattern transition characteristics and their criteria were presented and dimensionless correlations for determining flow patterns were established.展开更多
文摘This paper is concerned with a remedy for interface smearing,which is usable when fixed (i.e. non moving and so non conforming) grids are employed. It is simple to employ and has been found to be rather effective. The paper explains its principle, describes how it has been implemented and presents some results obtained with its assistance. The results are compared both with those of earlier methods of interface motion calculation and with experimental data.
文摘Aim To develop a hydrodynamic model on the void fraction in liquid slugs for gas liquid slug flow in vertical tubes. Methods Developing the model by considering the gas exchange between the Taylor bubble and the following liquid slug. Results Some experimental data are obtained to check the model. In comparison with previous published results, the predictions from this model are better and in good agreement with the experimental data. The error is within ±20%. Conclusion The proposed model can correctly predict the void fraction in liquid slugs for gas liquid two phase slug flow in vertical tubes.
文摘This paper deal with the frictional resistance characteristics of gas liquid two phase flow in vertical upward helical coiled tubes under the system pressure 0.1 0.6MPa. By means of dimension analysis and π theorem, the correlation formulas were obtained for calculating the frictional resistance coefficients of gas liquid two phase flow in helical coiled tubes. The calculated results agree well with the experimental results.
文摘In the present work, an experimental research was carried out on the air-water two phase flow patterns and their transition characteristics in the shell-side of a segmentally baffled horizontal shell -tube heat exchanger model of horizontally-cut baffles. In the inlet crossflow zone, the two -phase flow was in vertical downflow across an in-line (square) horizontal tube bundle with a pitch to diameter ratio. p/D of 1. 28. The flow pattern sketch was obtained by visual observation. The flow pattern transition characteristics and their criteria were presented and dimensionless correlations for determining flow patterns were established.
