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1. |
A. E. DUKLER - A LEGACY OF CONTRIBUTIONS TO CHEMICAL ENGINEERING |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 3-11
M. WICKS III,
F. K. WASDEN,
G. J. ZABARAS,
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ISSN:0098-6445
DOI:10.1080/00986449608936407
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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2. |
DYNAMIC SLUG TRACKING SIMULATIONS FOR GAS-LIQUID FLOW IN PIPELINES |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 13-39
O. J. NYDAL,
S. BANERJEE,
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摘要:
A Lagrangian slug tracking model for dynamic gas-liquid slug flow in pipelines of varying inclinations has been formulated and implemented in C + + using an object-oriented approach. Slugs and bubbles are discrete computational objects which are coupled by exchange of mass and momentum, and organized in linked lists
ISSN:0098-6445
DOI:10.1080/00986449608936408
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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3. |
SHEAR AND INTERFACIAL INSTABILITIES OF OIL-WATER FLOW IN AN INCLINED CHANNEL1 |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 41-49
B. S. TILLEY,
S. G. BANKOFF,
S. H. DAVIS,
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摘要:
A study of the linear stability of a laminar flow of an oil-water system in an inclined channel is presented. A novel shear-mode of instability, which is necessarily decaying in plane Poiseuille flow, is found to be the primary instability in certain situations. When the channel is sufficiently inclined, the long-wave mode can become unstable, regardless of the total volumetric flow rate of the fluids The consequences to oil transport are discussed.
ISSN:0098-6445
DOI:10.1080/00986449608936409
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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4. |
EXPERIMENTAL STUDY OF TURBULENT BUBBLY SHEAR FLOWS |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 51-70
GroupMultiphase Flows,
Group Interfaces,
M. LANCE,
J. L. MARIÉ,
E. MOURSALI,
J. BATAILLE,
C. SUZANNE,
V. ROIG,
R. BEL FDHILA,
L. MASBERNAT,
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摘要:
This paper in memory of Pr Dukler summarizes a set of experiments on bubbly shear flows carried out by two groups, in Toulouse and in Lyon. Homogeneous shear flows, plane mixing layer, boundary layer on a flat plate and sudden area expansion have been investigated, for low and moderate void fraction. Measurements of mean liquid velocity show that the main features of the corresponding single phase flow are conserved, in particular self-similarity of the mean velocity profiles. However, the turbulent field is strongly modified. The transverse interfacial momentum transfer has been evaluated, and proves to be dominated by instantaneous local forces, which are not usually taken into account in eulerian models.
ISSN:0098-6445
DOI:10.1080/00986449608936410
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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5. |
ON THE MODELLING OF SLUG FLOW |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 71-102
KJELLH. BENDIKSEN,
DAG MALNES,
OLEJØRGEN NYDAL,
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摘要:
A novel approach to modelling transient slug flow is presented. Aspects of current physical descriptions of slug flow, required as closure laws for the models are briefly reviewed. It is demonstrated how the dynamics of large scale changes in slug flow may be simulated, by incorporating a unit cell type of slug flow model into numerical transient two-fluid models.
ISSN:0098-6445
DOI:10.1080/00986449608936411
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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6. |
ANALYTICAL SOLUTION FOR LAMINAR-LAMINAR TWO-PHASE STRATIFIED FLOW IN CIRCULAR CONDUITS |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 103-143
N. BRAUNER,
J. ROVINSKY,
D. M. MARON,
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摘要:
Many attempts made in modelling stratified two-phase flow for predicting the operational flow characteristics (pressure drop, holdup, etc.) assume mostly plane interface between the phases. Obviously, the interaction between the stratified layers and the resulting flow characteristics may be significantly affected by the configuration of the interface. Moreover, complete analytical solutions for stratified flows in circular conduits a re not yet available even for laminar flows with plane interface and most of previous studies resort to average two-fluid modelling.
ISSN:0098-6445
DOI:10.1080/00986449608936412
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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7. |
THE METHOD OF VIRTUAL POWER APPLIED TO TWO-PHASE FLOW WITH PHASE CHANGE |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 145-153
N. COUTRIS,
J. M. DELHAYE,
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PDF (215KB)
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ISSN:0098-6445
DOI:10.1080/00986449608936413
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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8. |
BUBBLE AND SLUG FLOW AT MICROGRAVITY CONDITIONS: STATE OF KNOWLEDGE AND OPEN QUESTIONS |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 155-173
C. COLIN,
J. FABRE,
J. McQUILLEN,
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摘要:
Based on the experiments carried out over the past decade at microgravity conditions, an overview of our current knowledge of bubbly and slug flows is presented. The transition from bubble to slug flow, the void fraction and the pressure drop are discussed from the data collected in the literature. The transition from bubble to slug flow may be predicted by introducing a critical void fraction that depends on the fluid properties and the pipe diameter: however, the role of coalescence which controls this transition is not clearly understood. The void fraction may be accurately calculated using a drift-flux model: it is shown from local measurements that the drift of the gas with respect to the mixture is due to the non uniform radial distribution of void fraction. The pressuredrop happens to be controlled by the liquid flow for bubbly flow whereas for slug flow the experimental results show that pressure drops is larger than expected. From this study, the guidelines for future research in microgravity are given.
ISSN:0098-6445
DOI:10.1080/00986449608936414
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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9. |
TWO-PHASE FLOW PRESSURE CHANGE ACROSS SUDDEN EXPANSIONS IN DUCT AREAS |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 175-190
J. SCHMIDT,
L. FRIEDEL,
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摘要:
A new model to calculate the two-phase flow pressure change across a sudden expansion in a duct area was developed and checked against data measured with mixtures of air and water, aqueous glycerol, watery calcium nitrate and with refrigerant R 12. In the model all relevant physical parameters are included and, in contrast to equations in the literature, the entrainment of liquid in the gas stream is considered. The predictions are validated for a wide range of conditions, pipe diameters and physical properties typically encountered in industrial pipe line systems: Calculations based on the new approach are sufficiently accurate for engineering purposes.
ISSN:0098-6445
DOI:10.1080/00986449608936415
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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10. |
DRYOUT OF WATER FILM ON A HEATED TUBE SURFACE CAUSED BY AN OBSTRUCTION IN A BOILING TWO-PHASE VERTICAL UPWARD FLOW |
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Chemical Engineering Communications,
Volume 141-142,
Issue 1,
1996,
Page 191-206
T. FUKANO,
A. GOTO,
Y. TSURUSAKI,
S. MOROOKA,
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摘要:
Due to the increasing consumption of energy and the green house effect caused by C02nudear power stations have been playing more important role than ever in the electric power generation. And both the economy and the safety of the nuclear power station are strongly demanded. One of the restriction in the thermal design of the safe and economic nuclear reactor, especially in BWR is pointed out to be the heat removal from the fuel rods near the rods supporting spacer.
ISSN:0098-6445
DOI:10.1080/00986449608936416
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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