Mcdowell-wellman Company

Dravo Corporation

William H Marlowe

Thomas E Ban

John C Sheppard

There is disclosed a method of reducing the swelling characteristics and bed characteristics of a pelletized fuel during a sintering operation. The method comprises the steps of pulverizing the coal to form a powdery mass, forming the mass into discrete pellets, providing a coating on the pellets with soluble salts, burnt lime, or hydrated lime, and heating the pellets to a temperature exceeding 800.degree. F.

Method for improving bed firing characteristics and inhibiting

A process is disclosed for gasifying pelletized coal to produce a low Btu gas containing large amounts of hydrogen and carbon monoxide. Advantageously, the process is carried out on a circular traveling grate machine on a continuous basis. A horizontally moving, quiescent, gas-permeable bed of coal is formed by depositing at least one layer of a sized recycle charge of coal and at least one layer of fresh coal. To initiate an oxidizing reaction zone, the surface of one of the layers is ignited and the zone travels as a wave downwardly into the layer and upwardly into any superposed layer. Air and steam or air and carbon dioxide are either updrafted or downdrafted through the bed to control combustion. The coal is reduced in zones ahead of the advancing zone or zones of oxidation, and the reactions are terminated before the oxidation zone reaches both outermost surfaces of the bed to minimize the formation of carbon dioxide. Unreacted coal is separated from fine ash and is used as the recycle feed.

Process for gasifying pelletized carbonaceous fuels

A method of educting oil from fine, high carbon oil shales is disclosed. The method includes the steps of providing a burden of oil bearing shale having a high fixed carbon content and charging the shale in the traveling grate machine, preferably a circular traveling grate machine. The burden is moved in a horizontal plane into a retorting zone, where the shale is heated to an oil-educating temperature of at least 800 degrees F. Oil and a medium BTU gas is educted from the burden, and the burden is then moved to a gasifying zone, where steam and air are downdrafted through the burden to raise the temperature of the burden to a temperature in excess of 1800 degrees F. Such a temperature converts substantial amounts of residual carbon in the burden to carbonaceous gases, and promotes substantial agglomeration or clinkering of the spent shale to enable a separation recyling process. The spent shale is cooled and the spent agglomerated shale is discharged from the machine.

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Euclid, OH, United States of America

William H Marlowe