Book ChapterDOI
Properties of Cocurrent Gas-Liquid Flow
TLDR
The problem of two-phase flow classification is complicated by the inevitable differences because of individual interpretations of visual observations and also by differences in terminology as mentioned in this paper, and a number of definite flow patterns are investigated.Abstract:
Publisher Summary Two-phase gas–liquid glow is encountered in an increasing number of important situations, and a clear understanding of the rates of transfer of momentum, heat, and material are required for logical and careful design and operation of a very wide variety of chemical engineering equipment and processes. In the production and transport of crude petroleum and petroleum products, two-phase flow is finding increasing use. Two-phase flow systems may be classified initially by composition, as containing a single component, or two or more components with any one component present in both phases or only essentially in one or the other phase. Varieties of flow patterns include bubble flow, plug flow, stratified flow, wavy flow, snug flow, annular flow, mist or spray flow. The problem of two-phase-flow classification is complicated by the inevitable differences because of individual interpretations of visual observations and also by differences in terminology. This chapter investigates a number of definite flow patterns. In the case of single-component two-phase flow—such as in vaporizing water—physical equilibrium is commonly assumed and seems to yield reasonable results, even though it might seem that supersaturation could occur. The rate of mass transfer among phases, therefore, is not a limiting process for single component flow.read more
Citations
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Book ChapterDOI
The Flow of Liquids in Thin Films
TL;DR: In this article, the Kapitsa theory for wavy film flow appears to apply over only a very limited part of the total wavy flow regime, and it is shown that it is possible to predict quite accurately the flow behavior in the smooth laminar flow regime of the film; unfortunately, this flow regime is not of great practical importance.
Journal ArticleDOI
Effect of tube diameter on boiling heat transfer of R-134a in horizontal small-diameter tubes
TL;DR: In this article, the boiling heat transfer of R-134a flow in horizontal small-diameter tubes with inner diameter of 0.51, 1.12, and 3.1mm was experimentally investigated.
Journal ArticleDOI
Flow regimes in two-phase gas-liquid flow
P.L. Spedding,D.R. Spence +1 more
TL;DR: In this paper, experimental data were determined for co-current air-water horizontal flow in a 00935 m id pipe and flow patterns were identified by a combination of visual/video observations, the pressure fluctuation characteristics and a detailed examination of the pressure loss and holdup data.
Journal ArticleDOI
Condensation heat transfer and flow pattern inside a herringbone-type micro-fin tube
TL;DR: In this paper, the authors measured the heat transfer and pressure drop of a newly proposed herringbone-type micro-fin tube and compared them with those of a helical micro- fin and a smooth tube.
Journal ArticleDOI
Experimental study on condensation heat transfer and pressure drop in horizontal smooth tube for R1234ze(E), R32 and R410A
TL;DR: In this article, the effects of mass flux and saturation temperature on heat transfer and pressure drop have been analyzed and compared with R32 and nearly azeotropic HFC refrigerant blend R410A.
References
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Journal Article
Proposed Correlation of Data for Isothermal Two-Phase, Two-Component Flow in Pipes
Journal ArticleDOI
Two-phase bubble flow
TL;DR: In this article, a theory is presented which shows that the velocity of the bubbles consists of a component equal to the superficial liquid velocity, a component equivalent to the gas velocity and a component due to buoyancy.
Journal ArticleDOI
Two-phase (gas—liquid) flow phenomena—I Pressure drop and hold-up for two-phase flow in vertical tubes
G.H. Anderson,B.G. Mantzouranis +1 more
TL;DR: In this paper, the authors developed a theory for two-phase flow in a vertical tube when the liquid flow is annular, and they examined data on liquid hold-up and pressure gradient together with original data obtained on airwater mixtures in a 1 2 in. diameter glass tube.
Journal ArticleDOI
Gas-liquid flow in horizontal pipes
TL;DR: In this article, an investigation was made of the flow of air-water and air-oil mixtures in horizotal smooth pipes with inner diameters ranging from 24 mm to 140 mm, and rough pipes with an inner diameter of 50 mm.
Journal ArticleDOI
Initiation of roll waves
TL;DR: In this paper, the theory proposed by Jeffreys to explain roll-wave transition on a liquid surface is applied to the concurrent flow of a gas and liquid and data are presented for concurrent flow with water-glycerine solutions, water-butanol solutions, and water-sodium lauryl sulfate solutions.
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