Principles Of Flow Of Solids In Bins - Introduction

Society for Mining, Metallurgy & Exploration
Andrew W. Jenike
Organization:
Society for Mining, Metallurgy & Exploration
Pages:
14
File Size:
2483 KB
Publication Date:
Jan 1, 1968

Abstract

There used to be a time when bins were designed for total volume and placed in any available place of the plant. Poke holes were provided and feed was maintained by manual prodding, lancing, hammering, and by various mechanical flow-profiting devices. Little thought was given to what occurred inside the bins and why materials did not flow. Indeed, such mental effort was hard to justify while low-cost manual labor was plentiful, quality standards low, and rates of feed moderate. The past fifteen years have seen a drastic change in these conditions. We all know that labor for hard manual work is becoming unavailable at any wage, level. Standards of product uniformity are continuously rising. This uniformity is just as important in a fine ore feed to ball mills as it is in a cattle feed or in a flour mix. Rates of feed now frequently exceed 2,000 tons per hour per feeder. At that rate there is no time for, lancing or prodding. An efficient storage, plant contains a known available volume of bulk solid, and feeds it at the required time, at the prescribed rate, and without degradation of the product. A storage bin may also perform other functions such as blending of different grades, degasification of aerated, powders, isolation of different gaseous media. A contact bed of particles flowing by gravity in counter-current with a gas or liquid may be used as a continuous reactor. Gas or liquid pressures can be simply contained by, a sufficient head of flowing solid.
Citation

APA: Andrew W. Jenike  (1968)  Principles Of Flow Of Solids In Bins - Introduction

MLA: Andrew W. Jenike Principles Of Flow Of Solids In Bins - Introduction. Society for Mining, Metallurgy & Exploration, 1968.

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