A new bed-collapsing technique for measuring the dense phase properties of gas-fluidized beds

Park, J.J.; Park, J.H.; Chang, Ilhan; Kim, S.D.; Choi, Cheong Song

doi:10.1016/0032-5910(91)80038-k

Cited by 13 publications

(17 citation statements)

References 13 publications

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“…The gas supply was then cut by closing valve V1 and simultaneously opening valve V2. In this so-called 'dual-drainage' configuration the gas escaped through the base of the windbox as well as upwards through the bed (Park et al 1991;Cherntongchai and Brandani 2005). Bed height during collapse was measured as a function of time from the X-ray images and corrected for perspective effects and minor camera distortion.…”

Section: Methodsmentioning

confidence: 99%

Gas retention in fine-grained pyroclastic flow materials at high temperatures

et al. 2007

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International audienceThe ability of a dense pyroclastic flow to maintain high gas pore pressure, and hence low friction, during runout is determined by (1) the strengths and longevities of gas sources, and (2) the ability of the material to retain residual gas once those sources become ineffective. The latter is termed the gas retention capacity. Gas retention capacity in a defluidizing granular material is governed by three timescales: one for the evacuation of bubbles (t be ; brief and not considered in this paper), one for hindered settling from the expanded state (t sett), and one for diffusive release of residual pore pressure from the non-expanded state (t diff). The relative magnitides of t sett and t diff depend on bed thickness, t sett dominating in thin systems and t diff in thick ones. Three pyroclastic flow materials, two ignimbrites and a block-and-ash flow sample, were studied experimentally to investigate expansion behaviour under gas flow and to determine gas retention times. Effects of particle size were evaluated by using two size cuts (<4 mm and <250 μm) from each sample. Careful drying of the materials was necessary to avoid effects of humidity-related cohesion. Two sets of experiments were carried out: (1) expansion in the non-bubbling regime at 50–200°C, (2) bed collapse tests from the initially bubbling state at 50–550°C. Provided that gas channelling was avoided by gentle stirring, all the samples exhibited a regime of uniform expansion prior to the onset of bubbling. Fine particle size (in particular high fines content), low particle density and high temperature all favoured smoother fluidization by increasing the maximum expansion possible in the non-bubbling state. An empirical equation describing the uniform expansion of the materials was determined. High temperature also favoured greater gas partitioning into the dense phase of the bubbling bed, as well (in finer-grained samples) as higher voidage in the settled bed. Large values of t sett and t diff were favoured by fine particle size. Temperature had less influence, suggesting that experimental results at low temperatures (50–200°C) can be extrapolated to higher temperatures. Gas retention times provide insight into the ability of pyroclastic flows in expanded (t sett) or non-expanded (t diff) flow states to retain gas once air ingestion or gas production have become ineffective. Finer-grained pyroclastic flows are expected to retain gas longer, and hence to have higher apparent ‘mobilities', than coarser-grained ones of comparable volume, as has been observed on Montserrat

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Section: Methodsmentioning

confidence: 99%

Gas retention in fine-grained pyroclastic flow materials at high temperatures

et al. 2007

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“…Many other researchers applied this assumption for their analysis (Barreto, 1984;Barreto et al, 1988;Nie and Lui, 1998;Xie, 1997). Park et al (1991) were among the first to use of a venting valve and suggested that the aperture of this valve should be adjusted to optimize the gas discharge. Recent measurements were carried out using this system (Lettieri et al, 2000;Lorences et al, 2003).…”

Section: Introductionmentioning

confidence: 97%

Mathematical description of pressure drop profile for the 1-valve and 2-valve bed collapse experiment

Cherntongchai¹,

Innan²,

Brandani³

2011

Chemical Engineering Science

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“…It has been shown that the effect of the residual gas exiting from the windbox through the bed cannot be neglected, and improvements of the bed collapse technique have been proposed. They consist either in modifying the equations for the voidage and gas velocity of the dense phase [10] or in performing the dual-drainage bed collapse technique [15]. The previous studies focused on the effects of the (i) physical properties of the powders (diameter, density, percentage of fines), (ii) the bed height, (iii) the distributor (porous or perforated plate), (iv) windbox volume, (v) operating pressure, (vi) fluidising velocity before defluidisation.…”

Section: Introductionmentioning

confidence: 99%