The requirements for a satisfactory slag are that it shall be—

(_a_) Fusible at the temperature of furnace working.

(_b_) Fluid and run easily.

(_c_) Of sufficiently low specific gravity as will allow

of good settling and separation of the matte or

metallic products.

It is well known that within certain broad limits of silica content,

slags will fulfil these conditions to a greater or less extent, whilst

the most suitable and economic slag under any particular circumstances

is decided, as stated above, by the composition of the charge, the

quantity and character of the available fluxes, and the previous

experience with the furnace. The limits of the silica content for

suitable slags as just indicated are fixed by several well-known

general properties of the silicates.

Speaking broadly, and from the point of view of the more or less

ferruginous silicates constituting copper-smelting slags, the

more basic silicates—such as the subsilicate class (oxygen in

acid : oxygen in base < 1 : 1)—are generally characterised by high

formation-temperature, and by being very fluid, thin and fiery, dense

and corrosive. On the other hand, the more acid silicates, such as

those of the multi-silicate class (oxygen in acid : oxygen in base >

2 : 1) are characterised by lower formation-temperature and low density,

and by being thick and viscous.

As the silica content within this range of silicates increases, the

melting point is lowered and the specific gravity is reduced, features

which are very advantageous from the point of view of the production

of clean slags. Their fluidity, however, decreases, and a very high

temperature is thus required in order to render them sufficiently

limpid to run freely from the furnace. On this account the highest

proportions of silica usually considered feasible in a slag, correspond

to the bisilicates of the representative composition, MO. SiO_{2}.

With high temperature conditions in the furnace and rapid working,

such slags can be dealt with successfully, and if the charges are

necessarily highly siliceous, it may be advantageous from the economic

point of view to work with this class of slag.

In proportion as the silica content gradually decreases and as they

become more basic, the silicates are more and more corrosive and fiery,

and especially in the case of the iron silicates, they gradually attain

such a high specific gravity that efficient settling of the matte is

not possible. In addition, the more basic the silicate the greater is

its dissolving power for sulphides, hence high copper losses in the

slags result from these combined causes. Such basic silicates possess,

however, the advantage of marked liquidity, and of flowing from the

furnace in a thin limpid stream. The high density and the solvent power

of basic slags thus fix a limit to the composition which is considered

economically suitable, and the lowest proportions of silica usually

worked with correspond to the mono-silicates represented by the formula

2MO. SiO_{2}. Slags containing a greater proportion of base (usually

iron) possess too high a density to permit of clean settling. In

practice, therefore, the majority of slags are mixed silicates of a

composition ranging between the limpid but somewhat dense mono-silicate

and the lighter but more viscous bisilicate, corresponding to silica

contents of from 30 to 48 per cent. of silica, and within the limits of

35 to 45 per cent. of silica most copper blast-furnace slags will be

found. The composition roughly corresponds in a large number of cases

to that of the sesqui-silicates of the general formula 4MO. 3SiO_{2}

(oxygen in base : oxygen in acid :: 4 : 6 :: 1 : 1½).

As is well known, mixed silicates—_i.e._, silicates of two or more

bases—are generally characterised by the properties of increased

fusibility, and often of increased fluidity, and their employment is

usual and generally advantageous in smelting practice. The relative

proportion between the various bases in such mixed silicates is largely

a matter depending upon the prevailing conditions at the smelter.

In modern smelting, particularly where partial pyritic work is

conducted, and where fairly siliceous charges are worked, a slag

running about 40 per cent. SiO_{2} is aimed for, iron and earth oxides

constituting the remaining 60 per cent. or so. In cases where this

quantity of iron is present in the charge, the slag may be constituted

chiefly of iron silicate, but even in such instances the advantages of

lime additions are marked. When iron is not available in sufficient

quantity, the extra fuel costs and working difficulties of running

with more siliceous slags would render their production undesirable,

and the purchase of limestone or similar earthy flux is particularly

advantageous. The purely iron silicates are usually dense, and thus

tend to hold up copper values both in mechanical suspension as well

as in solution; the addition of lime, which has a marked effect in

reducing the specific gravity, permits of more basic slags being worked

with, where necessary, without such heavy losses in the slag.

The presence of lime silicate with the iron silicates has a marked

influence on the fluidity of the slags, even when they are more highly

siliceous, whilst on account of the lower atomic weight of calcium,

lime will, weight for weight, flux off a greater quantity of silica

than will ferrous oxide. In forming a slag of similar oxygen ratio,

thus—

Mono-silicate of lime, 2CaO . SiO_{2},

Lime : silica :: 112 to 60, or 1 part to 0·54 part.

Mono-silicate of iron, 2FeO . SiO_{2},

Iron oxide : silica :: 144 to 60, or 1 part to 0·42 part;

hence for the production of a slag of the same oxygen ratio, less

weight of lime would be required to flux off the same weight of silica;

in other words, the replacing values of the two oxides are as 112 to

144, or 7 to 9.

Of the other bases which are occasionally present in slags, the

proportions of the oxides of magnesium and zinc are sometimes

considerable, the calculations being analogous to the previous

cases. The case of alumina is anomalous, and its behaviour in slag

production is not definitely understood. Many experienced workers

hold the view that it tends to act either as acid or base, according

to the proportions of silica. Thus, in a very siliceous slag, alumina

in moderate quantity behaves as a basic oxide, forming aluminium

silicates, and in very basic or low silica slags the alumina appears

either to neutralise some of the excess base, acting as an acidic

oxide, or to dissolve as such in the slag, whilst in intermediate cases

it possibly behaves partly as an acid and partly as base. This view

has recently been questioned, and it has been suggested by Shelby that

alumina always acts as an acid in the formation of slags. The matter is

thus one which requires further considerable investigation.

Usually neither alumina nor zinc oxide behave very satisfactorily in

the furnace when present in large quantities, tending to thicken the

slags and to promote viscosity.

=Anaconda Practice in Charge Calculations.=—An example of some of the

practical considerations which enter into the calculation and making up

of charges is well illustrated in certain particulars of the practice

as conducted at Anaconda. Details of the materials charged over a

period of one month are indicated in Table X. The important charge

constituents available in large quantity include:—

Cu. SiO_{2}. Fe(O). S.

% % % %

First-class smelting ore, 8·6 54·0 13·6 14·0

Concentrates, 10·9 26·0 32·0 32·0

Briquettes, 5·0 50·0 13·0 13·0

Lime-rock (flux), .. .. .. ..

Old converter slags and residues, .. .. .. ..

Modern Copper Smelting being lectures delivered at Birmingham University, greatly extended and adapted and with and introduction on the history, uses and properties of copper. · 第 48 / 71 题