Swenson LogoSwenson Technology, Inc.

TOP FEED FILTER

Page 2

[previous pg] next page
If the magma is fed to the filter at a higher density, these openings can be considerably larger than the largest particles in the magma, even though very small particles are present in a graded mixture.

[graph]

Coarse crystalline solids form an exceedingly porous filter cake through which large volumes of air can be drawn, still maintaining a comparatively low vacuum in the system. Vacuums of 2 to 2-1/2 in. mercury, with exhauster capacities of 150 CFM of air at 70ºF per sq. ft. of filter area, are not uncommon. By preheating such large volumes of air, the material can be discharged in a completely dry state. For any given material, the temperature of the air to the filter varies with volume per square foot of filter area.

The vacuum depends on the size and characteristics of the crystals and increases as the porosity of the cake decreases. The curve chart shows the general relationship for exhauster displacement and air temperature for cakes of various porosities as indicated by the vacuum. It will be seen that as the vacuum increases, the temperature of the air increases and the displacement decreases. Therefore, each problem must be considered from several angles before the optimum operating conditions can be determined.

SOURCE HEAT - If the air to the filter is heated directly with gas or oil, the products of combustion will be mixed with the air. However, clean air can be delivered to the filter by using indirect heaters. Also, steam coils can be used if comparatively low-temperature air will accomplish the drying. Direct fired heaters are about 95% efficient, while indirect heaters have a thermal efficiency of only about 70%.

CAPACITY - The capacity of the top-feed filter depends on operating conditions and on the characteristics of the materials handled. Cake thickness ranges from 1/2 to 1-1/2 in. and normal drum speeds from 1/2 to 2-1/2 rpm. In general, when a bone-dry cake is to be delivered, capacities range between 100 and 900 lb. per sq. ft. of filter area per hour. Higher capacities are possible if only partial or no drying is required.

[installation]

EFFICIENCY - The overall thermal efficiency of the top-feed filter depends upon the uniformity of the aggregate in the cake, uniformity of cake formation on the filter, temperature of the air used for drying, and rate at which the hot air used for drying is drawn through the cake. All these factors are controlled in any well-engineered installation. A high thermal efficiency is obtained in the top-feed filter because much of the liquor is removed from the cake mechanically during the heating period.

FEED - The uniformity of the aggregate and of the cake itself and the tendency toward cloth blinding all are related to the feed density. Swenson top-feed filters definitely control the feed density by starting with a magma of maximum density and providing only sufficient dilution to cause the magma to flow.

[previous pg] next page

HOME

Copyright 2009 Swenson Technology, Inc.