Flow structure and distribution effects in gas-liquid mixture flows

Air-water mixtures which are assumed to flow homogeneously in a pipe are usually described by a one-dimensional momentum balance. This allows definition of a friction factor in a manner similar to single phase flows. By defining a momentum flux distribution parameter, the momentum balance has been modified to correctly include the etfects of phase and velocity distributions and the effect of these on calculated friction factors has been investigated. Resistivity probes were used to measure void fraction and gas phase velocity distributions for selected vertical and horizontal flow conditions, and these were combined with static pressure measurements to calculate friction factors. For bubbly flows, the inclusion of these distribution effects did not substantially alter friction factor estimates which are approximately 10% above single phase values (for Reynolds numbers based on liquid viscosity).

Friction factor values are shown to be related to flow development with higher values associated with deveioping flows. In particular, high friction factors are associated with the need to break-up bubbles to an “equilibrium” size. In order to experimentally simulate fully developed vertical flows, the highly turbulent nozzle mixer is most suitable while the less turbulent wall-injection type seems appropriate for horizontal flows.     

Large scale planar laser induced fluorescence in turbulent density-stratified flows

Planar Laser Induced Fluorescence (PLIF) is used to obtain a series of two-dimensional concentration distributions in large scale (order of 5 m) time-varying thermally stratified flows. Density gradients due to turbulent fluctuations within the image area were found to cause reflection and refraction of the laser light sheet, reducing the usual simplicity of the PLIF method. To compensate for these effects, a variable local attenuation coefficient has been introduced to relate the attenuation of the laser sheet due to the concentration of the fluorescent dye and its spatial gradient. A mathematical algorithm for image restoration has been developed and applied to produce two-dimensional surface temperature mappings using fluorescent dye as an indicator. The algorithm has been verified using a set of temperature probes placed in the flow. It is found that this method provides both powerful flow visualization and adequate non-intrusive concentration measurements for large scale investigations of density stratified flows.     

Local characteristics of upward gas-liquid flows

The results of two-phase flow structure measurements in an upward gas-liquid flow in a 86.4 mm i.d. tube by the electrochemical and conductivity techniques are presented. Measurements were made in bubble and slug flow regimes at liquid flow rates ranging from 0.2 to 2 m/s.The flow instability and ambiguity in a bubble regime at low velocities is shown to exist. Great discrepancy between measured wall shear stress values and those predicted by the Lockhart-Martinelli model are due to the nonuniform distribution of gas over the tube cross section. Measurements of intensity of wall shear stress and liquid velocity fluctuations in a two-phase flow are presented.     

Nonequilibrium degassing of a single-component gas-liquid mixture

At the present time the calculation of the separation of gas-liquid mixtures is carried out according to methods based on the assumption of the existence of phase equilibrium between the liquid and separated gas [1, 2]. However, the validity of this assumption is violated with a decrease of the separation time. In the present work a model and a method of calculating non equilibrium degassing are proposed for the special case of a single-component gas-liquid mixture.Translated from Izvestiya Akademii Nauk SSSR, Mekhanika Zhidkosti i Gaza, No. 5, pp. 110–117, September–October, 1976.     

Non equilibrium gas-liquid flows in variable cross section ducts

The behaviour of two-phase high velocity flows in variable cross section ducts was investigated using a one-dimensional numerical model developed for the study of the annular flow configuration. Heat, mass, and momentum transfer between the phases during the flow were considered. The validation of the calculation procedure was made with some experimental data for the air-water couple, while the main application concerned the evaluation of momentum transfer from an expanding gas to an entrained liquid stream in droplet form. A liquid metal-gas flow was considered to simulate the process taking place in a plant where electrical power is generated by a liquid metal flowing in a magnetic field (MHD). The effectiveness of energy and momentum transfer between the liquid and the gas phase during the expansion was evaluated and the influence of nozzles with different convergence angles was investigated.     

Thermal mechanism of wave damping in a gas-liquid mixture

The effect of interphase heat transfer on the process of propagation of a wave in a monodisperse gas-liquid mixture is investigated. A three-wave equation of the Boussinesq type is derived and formulas for the dependence of the thermal components of the dissipative coefficients on the thermophysical parameters of the mixture are obtained. The limits of applicability of the short-wave method are determined. The theoretical and experimental values of the phase wave velocity are compared and found to be in good agreement.Yerevan. Translated from Izvestiya Rossiiskoi Akademii Nauk, Mekhanika Zhidkosti i Gaza, No. 6, pp. 75–83, November–December, 1994.     

A theory of hydroshock in a two-phase gas-liquid mixture

A hydroshock in a two-phase gas-liquid mixture is usually calculated by an analog of the Zhukovskii formula for a mixture (see, for example, [1, 2]) which establishes the relation of the hydro-shock intensity to the velocity of sound in the mixture. However, as the experimental data [1] show, the hydroshock intensity in the mixture can significantly exceed the calculated values, a fact which is explained by the increase in the propagation velocity of the perturbation wave in comparison to the velocity of sound in the mixture [3, 4]. In the present paper, an equilibrium model of shock transition, similar to [5, 6], is used to calculate the attenuation of the hydroshock as the gas content of the mixture increases in a bubble flow regime. It is shown that owing to the high compressibility of the mixture the effect of the elasticity of the pipe-line walls is small, and the dependence of the propagation velocity of the perturbation wave on the intensity and gas content becomes the main effect. A simple dependence of the hydroshock intensity on the gas content and two similarity parameters is obtained.Translated from Izvestiya Akademii Nauk SSSR, Mekhanika Zhidkosti i Gaza, No. 5, pp. 202–204, September–October, 1984.     

Large eddy simulation of homogeneous shear flows with several subgrid‐scale models

In this article, large eddy simulation is used to simulate homogeneous shear flows. The spatial discretization is accomplished by the spectral collocation method and a third‐order Runge–Kutta method is used to integrate the time‐dependent terms. For the estimation of the subgrid‐scale stress tensor, the Smagorinsky model, the dynamic model, the scale‐similarity model and the mixed model are used. Their predicting performance for homogeneous shear flow is compared accordingly. The initial Reynolds number varies from 33 to 99 and the initial shear number is 2. Evolution of the turbulent kinetic energy, the growth rate, the anisotropy component and the subgrid‐scale dissipation rate is presented. In addition, the performance of several filters is examined. Copyright © 2005 John Wiley & Sons, Ltd.     

Compressible gas-liquid mixture flow at abrupt pipe enlargements

A detailed investigation was made of the flow of compressible gas-liquid mixtures through sudden enlargements in diameter of circular pipes. One-dimensional analysis shows that the dimensionless pressure rise varies with mixture void fraction and mixture momentum, while the establishment of choking conditions at the enlargement is controlled by the length of pipe downstream in which frictional pipe flow occurs. The flows were found to exhibit two characteristic modes, jet flow and submerged flow, with intermediate flows displaying unsteady oscillation between these modes. The distance to the downstream position of maximum pressure increased steadily with mixture void fraction when the upstream pipe outlet was choked, varying from 5 to 50 times the downstream pipe diameter. If the flow was not choked, this distance was much smaller and showed discrete fixed values associated with the mode of flow.

One-dimensional analysis accurately predicted maximum pressure, but when flow was choked at the enlargement the calculation was sensitive to the pressure in the region of separated flow surrounding the central jet in the enlargement. Although analysis of maximum pressure in terms of flow expansion and normal shock gave a general indication of the maximum pressure (which was thus concluded to depend on the general flow processes expected in the enlargement), accurate prediction of maximum pressures will depend on empirical knowledge of the separated flow region pressures. The maximum pressure rise was found to be in the range extending down to 0.3 of the upstream pipe outlet pressure and reduced with void fraction; it was also influenced by the enlargement area ratio. Flows in the approach and outlet pipes were found to be compressible, frictional pipe flows of the Fanno type, with somewhat reduced friction factors occurring in the outlet pipe.     

Propagation of modulated nonlinear waves in a relaxing gas-liquid mixture

The propagation of nonstationary weak shock waves in a chemically active medium is essentially dispersive and dissipative. The equations for short-wavelength waves for such media were obtained and investigated in [1–4]. It is of interest to study quasimonochromatic waves with slowly varying amplitude and phase. A general method for obtaining the equations for modulated oscillations in nonlinear dispersive media without dissipation was proposed in [5–8]. In the present paper, for a dispersive, weakly nonlinear and weakly dissipative medium we derive in the three-dimensional formulation equations for waves of short wavelength and a Schrödinger equation, which describes slow modulations of the amplitude and phase of an arbitrary wave. The coefficients of the equations are particularized for the considered gas-liquid mixture. Solutions are obtained for narrow beams in a given defocusing medium as well as linear and nonlinear solutions in the neighborhood of a diffraction beam. A solution near a caustic for quasimonochromatic waves was found in [9].Translated from Izvestiya Akademii Nauk SSSR, Mekhanika Zhidkosti i Gaza, No. 1, pp. 133–143, January–February, 1980.     

Hydroshock theory in a two-phase gas-liquid mixture in a slug flow regime

A study is made of the intensity of a hydroshock in a two-phase gas-liquid mixture in a slug flow regime in the case when a pipeline is shut off by a liquid slug. The intensity is studied as a function of the length of the shut-off section of the liquid slug, the content of gas bubbles in the liquid slugs, and the pipeline shut-off law, and with allowance for the shock-wave character of the process [1, 2]. The calculated data using the shock-wave theory agree well with the experimental data of [3] and, unlike the results of the linear theory of [3], make it possible to determine the intensity of the hydroshock not only in the case of weak waves, but also in the case of waves of moderate intensity.Translated from Izvestiya Akademii Nauk SSSR, Mekhanika Zhidkosti i Gaza, No. 5, pp. 188–190, September–October, 1985.     

油气分离器内气液两相流的数值模拟

用DPM模型对油气分离器内的气液两相流流场进行了数值模拟。对计算结果分析发现,除了离心力作用可以增强分离效果外,气流在壁面上的碰撞过程对提高分离效果也具有重要作用。据此提出的改型设计方案在工程试验中获得了更高的分离效率,证明本文数值模拟所用的计算模型能够满足此类计算的要求,计算后的机理分析也反映了流动的本质。     

Shock structure in separated nozzle flows

In the case of high overexpansion, the exhaust jet of the supersonic nozzle of rocket engines separates from nozzle wall because of the large adverse pressure gradient. Correspondingly, to match the pressure of the separated flow region, an oblique shock is generated which evolves through the supersonic jet starting approximately at the separation point. This shock reflects on the nozzle axis with a Mach reflection. Thus, a peculiar Mach reflection takes place whose features depend on the upstream flow conditions, which are usually not uniform. The expected features of Mach reflection may become much difficult to predict, depending on the nozzle shape and the position of the separation point along the divergent section of the nozzle.      

Large scale grain dust explosions-research in Poland

For the last five years grain dust explosion research was carried out in surface and underground facilities of Experimental Mine “Barbara” Research was focused on problems of evaluation critical dust parameters influencing explosion course, explosion development and suppression by both passive and active means. The main conclusions are as follows: nominal dust concentration needed to obtain flame propagation must be higher than 50 g/m³, for nominal concentrations higher than 100 g/m³ flame acceleration is observed and detonation is possible; strong grain dust explosions can be effectively suppressed with passive water barriers whereas for weak ones active barries must be used.     

Laminar boundary layers of co-current gas-liquid stratified flows—I. Theory

The flow in the developing laminar boundary layers on a flat moving gas-liquid interface is studied theoretically. Analysis of the equations shows that flows depend on two parameters, each less than unity. Using a perturbation method, an analytical solution with accuracy to the third power of the small parameters is obtained and is in close agreement with the exact solution of the problem.