Lead Smelting and Refining, With Some Notes on Lead Mining
Science
Lead Smelting and Refining, With Some Notes on Lead Mining
Lead -- Metallurgy; Lead mines and mining
The drawing on page 190, Fig. 17, shows a side view of the apparatus
used in connection with the process, which will be readily understood
without special description. The dotted lines show the pot in its
emptying position. The series of operations is clearly illustrated in
Figs. 18-20, which are reproduced from photographs.
This process has now been in practical use at Ramsbeck for three years,
where it is employed for the desulphurization of galena of high grade
in lead, with which are mixed quartzose silver ore (or sand if no such
ore be available), and calcareous and ferruginous fluxes. A typical
charge is 100 parts of lead ore, 10 parts of quartzose silver ore,
10 parts of spathic iron ore, and 19 parts of limestone. A thorough
mixture of the components is essential; after the mixture has been
effected, the charge is thoroughly wetted with about 5 per cent.
of water, which is conceived to play a threefold function in the
desulphurizing operation, namely: (1) preservation of the homogeneity
of the mixture during the blowing; (2) reduction of temperature during
the process; and (3) formation of sulphuric acid in the process, which
promotes the desulphurization of the ore.
[Illustration: FIG. 17.—Savelsberg Converter.]
The moistened charge is conveyed to the converters, into which it
is fed in thin layers. The converters are hemispherical cast-iron
pots, supported by trunnions on a truck, as shown in the accompanying
engravings. Except for this method of support, which renders the
pot movable, the arrangement is quite similar to that which is
employed in the Huntington-Heberlein process. The pots which are now
in use at Ramsbeck have capacity for about 8000 kg. of charge, but
it is the intention of the management to increase the capacity to
10,000 or 12,000 kg. Previously, pots of only 5000 kg. capacity were
employed. Such a pot weighed 1300 kg., exclusive of the truck. The
air-blast was about 7 cu. m. (247.2 cu. ft.) per min., beginning at
a pressure of 10 to 20 cm. of water (2¾ to 4½ oz.) and rising to
50 to 60 cm. (11½ to 13½ oz.) when the pot was completely filled with
charge. The desulphurization of a charge is completed in 18 hours. A
pot is attended by one man per shift of 12 hours; this is only the
attention of the pot proper, the labor of conveying material to it and
breaking up the desulphurized product being extra. One man per shift
should be able to attend to two pots, which is the practice in the
Huntington-Heberlein plants.
[Illustration: Fig. 20.—Converter in Position for Blowing.]
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