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Open AccessJournal ArticleDOI

Pneumatic conveying of solids through straight pipes

Hirotaka Kqnno, +1 more
- 31 Jul 1969 - 
- Vol. 2, Iss: 2, pp 211-217
TLDR
In this paper, the pneumatic transport of solid particles in both horizontal and vertical pipes was studied using glass beads, copper spheres, millet and grass seeds, having diameters ranging from 0.1 to 1.0mm.
Abstract
The pneumatic transport of solid particles in both horizontal and vertical pipes was studied using glass beads, copper spheres, millet and grass seeds, having diameters ranging from 0.1 to 1.0mm. It was shown that the additional pressure drop and the particle velocity could be expressed by ΔPs/L=0.057 (ua/√gD)mρa, and us=ua-ut, respectively, in the case of vertical transport. In vertical transport, the copper spheres and glass beads were found to be densely distributed toward the wall of the pipe whereas higher concentration near the axis was observed for, polystyrene particles. The velocity profile of the air in the vertical pipe was symmetrical and was not appreciably affected by the addition of the particles. However, in the horizontal pipe, the velocity profile was asymmetric with respect to the pipe axis, and was found to be affected by the particle diameter, density, and the mass flow ratio of the air and the particles. A simple impulsive model was used to explain the additional pressure drop in horizontal conduits, which was thought to be caused mainly by the collision between the particles and the surface of the pipe wall.

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Journal ArticleDOI

Vertical pneumatic conveying: An experimental study with particles in the intermediate and turbulent flow regimes

TL;DR: In this article, a 3-inch diameter riser 30 feet in length using solids ranging in particle Reynolds number from 100 to 3500 was studied in vertical pneumatic conveying.
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Vertical pneumatic conveying: A theoretical study of uniform and annular particle flow models

TL;DR: Two models for vertical pneumatic conveying, a uniform flow model at high gas velocities and an annular flow model near the particle terminal velocity, have been examined theoretically.
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Pickup and saltation mechanisms of solid particles in horizontal pneumatic transport

TL;DR: In this paper, the authors examined pickup and saltation mechanisms of solid particles from an experimental viewpoint, in relation to the prediction of the minimum conveying velocity required in horizontal pneumatic transport systems that operate in dilute-phase.
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Flow behaviors in the downer of a large-scale triple-bed combined circulating fluidized bed system with high solids mass fluxes

TL;DR: In this paper, the authors investigated the flow behavior in the downer of a large-scale triple-bed circulating fluidized bed (TBCFB) gasifier cold model, which is composed of a downer (Φ 0.1m×6.5m), a bubbling fluidization bed (BFB, 0.27×3.4m3), a riser (∆ 0.6m×16.6
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An experimental study of vertical pneumatic conveying

TL;DR: In this article, the results from non-accelerating flow experiments conducted with a riser tube of bore 192 mm and height 16.2 m using spherical glass beads of average diameter 64 μm are presented.
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