Elongated bubble velocity estimation in vertical liquid-gas flows using flow-induced vibration

Author(s):  
Felipe de Castro Teixeira Carvalho ◽  
Maurício de Melo Freire Figueiredo ◽  
Alberto Luiz Serpa
2020 ◽  
Vol 112 ◽  
pp. 109950
Author(s):  
Felipe de Castro Teixeira Carvalho ◽  
Maurício de Melo Freire Figueiredo ◽  
Alberto Luiz Serpa

2008 ◽  
Vol 2008.13 (0) ◽  
pp. 439-440
Author(s):  
Daisuke ITO ◽  
Hiroshige KIKURA ◽  
Masanori ARITOMI ◽  
Horst Michael PRASSER

1960 ◽  
Vol 7 (2) ◽  
pp. 161-176 ◽  
Author(s):  
George Rudinger ◽  
Lowell M. Somers

Small regions in a flow where the density is different from that of the surrounding gas do not exactly follow accelerated motions of the latter, but move faster or slower depending on whether their density is smaller or larger than that of the main flow. This behaviour cannot be quantitatively explained by treating a gas ‘bubble’ as a hypothetical solid particle of the same density, because a gas bubble cannot move relative to the surrounding gas without being transformed into a vortex which absorbs part of the energy of the relative motion.To illustrate the acceleration effect, the flow velocity behind known pressure waves in a shock tube is compared with the observed velocity of a bubble produced by a spark discharge. The displacement of such a bubble by a wave exceeds that of a flow element by more than 20%, but the bubble density is not known. If the spark discharge is replaced by a small jet of another gas, a pressure wave cuts off a section of this jet which then represents a bubble of known density.A theory is developed which permits computing the response of such bubbles to accelerations. The ratio of the bubble velocity to the velocity of the surrounding gas depends on the density ratio for the two gases and on the shape of the bubble, but not on the acceleration. Experimental results with H2, He, and SF6bubbles in air, accelerated by shock waves of various strength, are presented and agree well with the theoretical predictions. The results apply regardless of whether accelerations are produced by pressure waves in a non-steady flow or by curvature of streamlines in a steady flow. Various aspects of the experimental observations are discussed.


Author(s):  
Chiwoong Choi ◽  
DongIn Yu ◽  
Moohwan Kim

Most correlations of pressure drop in microchannel have been developed based on modifying of C-value in Lockhart and Martinelli’s correlation for various flow regimes. However, the pressure drop is highly related with flow pattern. And the elongated bubble flow is major flow regime in microchannel. To study behaviors and pressure drop of bubble flow regime in microchannel, a glass rectangular microchannel was fabricated using a photosensitive glass. Experiments of adiabatic two-phase flow in rectangular microchannels were conducted with hydraulic diameters of 503 and 322 μm. Moreover, the visualization of bubble flow patterns was achieved with a high-speed camera and a long-distance microscope. The bubble velocity, lengths of liquid slug and bubble and void fraction were evaluated based on a unit cell model using image processing. The pressure drop of single bubble in a rectangular microchannel was extracted from measured total pressure drop. Especially, pressure drop correlation of a single elongated bubble was achieved for Capillary number and diameter.


Author(s):  
R. T. K. Baker ◽  
R. D. Sherwood

The catalytic gasification of carbon at high temperature by microscopic size metal particles is of fundamental importance to removal of coke deposits and conversion of refractory hydrocarbons into fuels and chemicals. The reaction of metal/carbon/gas systems can be observed by controlled atmosphere electron microscopy (CAEM) in an 100 KV conventional transmission microscope. In the JEOL gas reaction stage model AGl (Fig. 1) the specimen is positioned over a hole, 200μm diameter, in a platinum heater strip, and is interposed between two apertures, 75μm diameter. The control gas flows across the specimen and exits through these apertures into the specimen chamber. The gas is further confined by two apertures, one in the condenser and one in the objective lens pole pieces, and removed by an auxiliary vacuum pump. The reaction zone is <1 mm thick and is maintained at gas pressure up to 400 Torr and temperature up to 1300<C as measured by a Pt-Pt/Rh 13% thermocouple. Reaction events are observed and recorded on videotape by using a Philips phosphor-television camera located below a hole in the center of the viewing screen. The overall resolution is greater than 2.5 nm.


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