CHAPTER VIII

MILD ALKALI

Caustic and Mild. There are two classes of alkalis distinguished by the

terms caustic and mild. If a piece of all-wool material is boiled with a

solution of caustic soda or potash, it dissolves completely, giving a

yellow solution. Mild alkali will not dissolve flannel, though it may

have some slight chemical action causing shrinkage. Partly for this

reason, and partly because commercial washing soda often contains a

little caustic soda, woollen garments must not be boiled or even washed

in hot soda water.

The disintegrating action of the caustic alkalis is also illustrated by

the use of caustic soda in the preparation of wood pulp for paper

making. Tree trunks are first torn up and shredded by machinery; but

notwithstanding the power of modern machinery, the fibre is not nearly

fine enough for the purpose until it has been “beaten” with a solution

of caustic soda, whereby the pulp is brought to a smooth and uniform

consistency like that of thin cream.

Mild Soda and Potash. Until the middle of the eighteenth century, it was

thought that the soluble matter extracted from the ashes of all plants

was the same. In 1752 it was shown that the substance obtained in this

way from plants which grew in or near the sea differed from that from

land vegetation by producing a golden yellow colour when introduced into

the non-luminous flame of a spirit lamp, while that from land plants

gave to the flame a pale lilac tinge. The former substance is now known

as mild soda, and the latter as mild potash.

At this point it is well to make it clear to the reader that there are

two bodies commonly called soda, and two called potash. One of each pair

is caustic and one mild.

By a simple chemical test it is easy to distinguish a mild from a

caustic alkali. When a little dilute acid is added to the former, there

is a vigorous effervescence caused by the escape of carbon dioxide, but

no gas is given off when a caustic alkali is treated in the same way.

The liberation of carbon dioxide on the addition of acids shows that the

mild alkalis are carbonates.

Washing Soda is so well known, that very little description of its

external characteristics is necessary. It is a crystalline substance,

easily soluble in water. The crystals, when freshly prepared, are

semi-transparent; but after exposure to air for some time, they are

found to lose their transparency and to become coated with an opaque

white solid which crumbles easily. This change in appearance is

accompanied by a loss in weight.

Crystals of soda melt very easily on the application of heat and, on

continued heating, the liquid seems to boil. When this operation is

carried out in a vessel attached to a condenser, the vapour that is

given off from the melted soda condenses to a clear colourless liquid

which, on examination, proves to be water. When no more water collects

in the receiver, the vessel contains a dry, white solid, which by any

chemical test that may be applied is shown to be the same as washing

soda, but it contains no water of crystallization and has a different

crystalline form. This substance is anhydrous sodium carbonate, or soda

ash as it is called in commerce. When soda ash is mixed with water, it

combines with about twice its own weight of that liquid, forming soda

crystals again.

Washing soda, then, contains nearly two-thirds of its weight of water.

Some of this water is given off spontaneously when the soda is exposed

to air; the water may even be said to evaporate. This accounts for the

loss of weight observed and also for the formation of the white layer of

partially dehydrated soda over the surface of the crystal. The property

of losing water in this way is common to most crystals containing a high

percentage of water of crystallization. The phenomenon is known as

“efflorescence.” It may here be observed that crystals of washing soda

which have become coated over in this way contain relatively more soda

than those which are transparent.

Natural Soda. In Egypt, Thibet, and Utah, there are tracts of country

where the soil is so impregnated with soda that the land is desert. The

separation of the soda from the earth is a simple operation, for it is

only necessary to agitate the soil with water and, after the insoluble

matter has settled down, to evaporate the clear solution until the soda

crystallizes out.

In addition to alkali deserts, there are also alkali lakes. Those in

Egypt are small, nevertheless, about 30,000 tons of soda per annum are

exported from Alexandria. Owens Lake in California is said to contain

sufficient soda to supply the needs of North America; while in the East

African Protectorate, beneath the shallow waters of Lake Magadi

(discovered in 1910), there is a deposit of soda estimated at

200,000,000 tons.

The Leblanc Process. At the present time, the greater part of the

world’s supply of soda is made from common salt by two processes. The

older of these, which is known as the Leblanc process, was introduced in

France towards the end of the eighteenth century. In those days soda was

very dear, for the main supply came from the ashes of seaweeds;

wherefore the French Academy of Sciences, in 1775, offered a prize for

the most suitable method of converting salt into soda on a manufacturing

scale. The prize was won by Nicholas Leblanc, who in 1791 started the

first soda factory near Paris. These were the days of the French

Revolution; the “Comité de Sûreté Général” abolished monopolies and

ordered citizen Leblanc to publish the details of his process.

[Illustration: Fig. 12. SALT CAKE FURNACE]

The first alkali works were established in Great Britain in 1814. The

total amount of soda now made in this country every year is about

1,000,000 tons, of which nearly one-half is still made by the Leblanc

process.

Salt Cake. The first stage of the Leblanc process consists in mixing a

charge of salt weighing some hundredweights with the requisite amount of

“chamber” sulphuric acid. The operation is carried out in a circular

cast-iron pan (D, Fig. 12) about 9 ft. in diameter and 2 ft. deep. The

pan is covered over with a dome of brickwork, leaving a central flue (E)

for the escape of hydrochloric acid gas which is produced. At first, the

reaction takes place without the application of heat, but towards the

end the mass is heated for about one hour. The contents of the pan are

then raked out on to the hearth of a reverberatory furnace (_a_, _b_)

and more strongly heated. More hydrochloric acid gas is given off, and

the reaction is completed. The solid product which remains is impure

Glauber’s salt (sodium sulphate), and is known in the trade as “salt

cake.”

Black Ash. In the second stage of the Leblanc process, salt cake is

converted into black ash. The salt cake is crushed and mixed with an

equal weight of powdered limestone or chalk and half its weight of coal

dust. This mixture is introduced into a reverberatory furnace (Fig. 13)

by the hopper K, and heated to about 1000° C. by flames and hot gases

from a fire at _a_. During this operation, the mass is kept well mixed,

and after some time it is transferred to _h_ where the temperature is

higher. The mixture then becomes semi-fluid and carbon monoxide gas is

given off.

[Illustration: Fig. 13. BLACK ASH FURNACE]

The formation of carbon monoxide within the semi-solid mass renders it

porous. This is an advantage, because it greatly facilitates the

subsequent operation of dissolving out the soluble sodium carbonate. The

appearance of the flames of carbon monoxide at the surface of the black

ash indicates the end of the process. The product is then worked up into

balls and removed from the furnace.

The chemical changes which take place in making black ash are probably

as follows: Carbon (coal dust) removes oxygen from sodium sulphate,

which is thus changed to sodium sulphide. This substance then reacts

with the limestone (calcium carbonate), forming sodium carbonate (soda)

and calcium sulphide.

Extraction of Soda. It now only remains to dissolve out the soda from

the insoluble impurities with which it is mixed in the black ash. It is

evident that the smaller the amount of water used for this purpose the

better, because the water has subsequently to be got rid of by

evaporation. The process of extraction is, therefore, carried out

systematically. The black ash is treated with water in a series of tanks

which are fitted with perforated false bottoms. The soda solution, which

is heavier than water, tends to sink to the bottom and, after passing

through the perforations, is carried away by a pipe to the second tank,

and so on throughout the series. The fresh water is brought first into

contact with the black ash from which nearly all the soda has been

extracted.

The method of finishing off the black ash liquor differs according to

the final product which the manufacturer desires to obtain, for the

liquor contains caustic soda as well as mild soda. For the present, we

will suppose that the end product is to be washing soda. In this case,

carbon dioxide is passed into the liquor to convert what caustic soda

there is into mild soda.

The clarified soda liquor is then evaporated until crystals of soda

separate out. The first part of this process is carried out in large

shallow pans (P. Fig. 13), using the waste heat of the black ash

furnace, and finally in vats containing steam-heated coils. As the

crystals separate out, they are removed, drained, and dried.

Alkali Waste. Black ash contains less than half its weight of soda, so

that for every ton of soda produced there is from a ton and a half to

two tons of an insoluble residue which collects in the lixiviating and

settling tanks. This residue is known as alkali waste.

Alkali waste is of no particular value. It is not even suitable as a

dressing for the land, and since it is not soluble in water there is no

convenient means of disposing of it. Consequently, it is just

accumulated at the works and, as the heap grows at an alarming rate, it

cumbers much valuable ground. Moreover, it contains sulphides from

which, under the influence of air and moisture, sulphuretted hydrogen is

liberated. Alkali waste, therefore, has a very unpleasant odour.

The whole of the sulphur which was contained in the sulphuric acid used

in the first stage of the process remains in the alkali waste, mainly as

calcium sulphide. A plant for the recovery of this sulphur is

established in some of the larger works. The alkali waste is mixed with

water to the consistency of a thin cream, in tall, vertical cylinders.

Carbon dioxide under pressure is forced into the mixture, and this

converts the calcium sulphide into calcium carbonate and sets free

hydrogen sulphide, which, when burnt with a limited supply of air,

yields sulphur.

By this process, the most unpleasant feature of alkali waste, namely,

the smell, is removed. The calcium carbonate which remains is of very

little value. Some of it is used in making up fresh charges for the

black ash process and some for preparing Portland cement, for which

finely-ground calcium carbonate is required; the remainder is thrown on

a heap.

Bicarbonate of Soda. Bicarbonate of soda can be easily distinguished

from washing soda. It is a fine, white powder similar in appearance to

the efflorescence on soda crystals. It does not contain any water of

crystallization.

When bicarbonate of soda is heated, it does not melt, and, as far as its

external appearance is concerned, it does not seem to undergo any

change. If, however, suitable arrangements are made, water and carbon

dioxide gas can be collected, and the sodium bicarbonate will be found

to have lost 36·9 per cent. of its weight. The substance which remains

is identical with that obtained by heating soda crystals, that is,

anhydrous sodium carbonate. Sodium bicarbonate is, therefore, a compound

of sodium carbonate and carbonic acid.

The most familiar use of this compound is indicated by its common names

“baking-soda” and “bread-soda.” It is mixed with dough or other similar

material in order to keep this from settling down to a hard solid mass

in baking. The way in which bicarbonate of soda prevents this will be

readily understood when it is remembered that an ounce of this substance

liberates more than 2,300 cu. in. of carbon dioxide when it is heated.

When the bicarbonate of soda is well mixed with the ingredients of the

cake or loaf and disseminated throughout the mass, each particle will

furnish (let us say) its bubble of gas. Since these cannot escape, a

honey-combed structure is produced.

[Illustration: Fig. 14. THE SOLVAY PROCESS]

Baking powder is a mixture of bicarbonate of soda and ground rice; the

latter substance is merely a solid diluent.

The Solvay Process. Soda ash is one of the principal forms of mild

alkali used in commerce. Large quantities of this substance are made by

heating bicarbonate of soda. We shall now consider another alkali

process in which this substance is the primary product.

For the greater part of the first century of its existence, the Leblanc

soda process had no rival, although another method, known as the

ammonia-soda process, was patented as early as 1838. In this case,

however, as in many others, expectations based on the experiments

carried out in the laboratory were not realized when the method came to

be tried under manufacturing conditions. It was not until 1872 that

Ernest Solvay, a Belgian chemist, had so far solved the difficulties,

that a new start could be made. In that year, about 3,000 tons of soda

were produced by the ammonia-soda or Solvay process, as it has now come

to be known. Since then, however, the quantity produced annually has

been steadily increasing, until at the present time it amounts to more

than half of the world’s supply.

The Solvay process is very simple in theory. Purified brine is saturated

first with ammonia gas and then with carbon dioxide. Water, ammonia, and

carbon dioxide combine, forming ammonium bicarbonate, which reacts with

salt (sodium chloride), producing sodium bicarbonate and ammonium

chloride.

The principal reaction is carried out in a tower (Fig. 14 (1), _a_, _a_)

from 50 to 65 ft. in height and about 6 ft. in diameter. At intervals of

about 3½ ft. throughout its length, the tower is divided into sections

by pairs of transverse discs, one flat with a large central hole, and

one hemispherical and perforated with small holes (Fig. 14 (2)). The

discs are kept in position by a guide rod G. Fig. 14 (3) shows a better

arrangement of the guide rods. In modern works, the space between the

discs is kept cool by pipes conveying running water. The ammoniated

brine is led into the tower near its middle point. The carbon dioxide is

forced in at E in the lowest segment, and as it passes up the tower it

is broken up into small bubbles by the sieve plates. Sodium bicarbonate

separates out as a fine powder, which makes its way to the bottom of the

tower suspended in the liquid.

The perforated plates are necessary for the proper distribution of

carbon dioxide through the brine. They are, however, a source of

trouble, because the holes quickly become blocked up with sodium

bicarbonate, and every ten days or so it is necessary to empty the tower

and clean it out with steam or boiling water.

Recovery of Ammonia. The production of 1 ton of soda ash by the Solvay

process involves the use of a quantity of ammonia which costs about

eight times as much as the price realized by selling the soda. It is

evident that the success of the process as a commercial venture depends

largely on the completeness with which the ammonia can be recovered.

During the process, ammonia is converted into ammonium chloride, which

remains dissolved in the residual liquor. From this ammonia gas is set

free by adding quicklime and by blowing steam through the mixture. It is

now claimed that 99 per cent. of the ammonia used in one operation is

recovered.

Soda Ash. The bicarbonate of soda produced by the Solvay process is

moderately pure. For all ordinary purposes, it is only necessary to wash

it with cold water to remove unchanged salt, and after drying, it is

ready to be placed on the market if it is to be sold as bicarbonate. The

greater part of the Solvay product, however, is converted into soda ash

by the application of heat. If soda crystals are required, the soda ash

is dissolved in water and crystallized.

In many ways, the Solvay process compares very favourably with the older

method. It is an advantage to start with brine, for that is the form in

which salt is very often raised from the mines. The end product is

relatively pure; moreover, it is quite free from caustic soda, which for

some purposes for which soda ash is used is a great recommendation.

There is no unpleasant smelling alkali waste. On the other hand, the

efficiency of the Solvay process is not high, for only about one-third

of the salt used is converted into soda. This would make the process

impossible from the commercial point of view were it not for the

cheapness of salt.

The Leblanc process, too, has its advantages. In the next chapter we

shall see that it is adaptable for the production of caustic as well as

mild alkali. The chlorine which is recovered in the Leblanc process is a

very valuable by-product. In the Solvay process, chlorine is lost, for

hitherto no practicable method has been found for its recovery from

calcium chloride.

The position with regard to the future supply of alkali is very

interesting. The competition between the Leblanc and the Solvay

processes for supremacy in the market is very keen. At the same time,

both processes are in some degree of danger of being supplanted by the

newer electrical methods, which will be mentioned in the last chapter.

The following table shows very clearly the rapid progress made by the

Solvay process in ten years. The quantities are given in _tonnes_ (1

tonne = 0·9842 ton).

1884. 1894.

_Leblanc _Solvay _Leblanc _Solvay

soda._ soda._ soda._ soda._

Great Britain 380,000 52,000 340,000 181,000

Germany 56,500 44,000 40,000 210,000

France 70,000 57,000 20,000 150,000

United States — 1,100 20,000 80,000

Austria-Hungary 39,000 1,000 20,000 75,000

Russia — — 10,000 50,000

Belgium — 8,000 6,000 30,000

545,500 163,100 456,000 776,000

Mild Potash. Potassium carbonate (mild potash) was formerly obtained

from wood ashes. The clear aqueous extract was evaporated to dryness in

iron pots, and the substance was on this account called _potashes_;

later, potash. A whiter product was obtained by calcining the residue,

and this was distinguished as _pearl-ash_. Chemically pure potassium

carbonate was formerly obtained by igniting cream of tartar (potassium

hydrogen tartrate) with an equal weight of nitre. It is for this reason

that potassium carbonate is sometimes called “salt of tartar.”

About the middle of last century, natural deposits of potassium chloride

were discovered in Germany. The beds of rock salt near Stassfurt are

covered over with a layer of other salts, and for many years these were

removed and cast aside as “waste salts” (_abraumsalze_). When at a later

date they were examined more carefully, they were found to contain

valuable potassium compounds, notably the chloride. After that

discovery, mild potash was made by the Leblanc process., and Germany

controlled the world’s markets for all potassium compounds.

At the outbreak of war, the German supplies of potassium compounds

ceased as far as the allied nations were concerned, and an older method

of making potassium chloride from _orthoclase_ or potash-felspar was

revived. This involves the heating of the powdered mineral to a high

temperature after mixing it with calcium chloride, lime, and a little

fluorspar. The potassium chloride is then extracted from the fused mass

with water. This method has been worked with great success in America,

and it is claimed that potassium chloride can be made in that country at

a cost which is lower than that formerly paid for the imported article.

Mild potash and soda are so very similar in chemical properties that in

most cases it is immaterial which compound is used. In all cases in

which there is this choice, soda is employed, both because it is cheaper

and because it is more economical, for 106 parts of soda ash are

equivalent to 138 parts of potash. There are, however, some occasions

when soda cannot be substituted, notably for the manufacture of hard

glass and soft soap, and for the preparation of caustic potash,

potassium dichromate, and other potassium salts.

Potassium Bicarbonate. This resembles the corresponding sodium salt in

nearly every respect. It is, however, much more readily soluble in

water, so much so, that it is not possible to obtain this substance by

the Solvay method. It is made from potassium carbonate by saturating a

strong aqueous solution of that substance with carbon dioxide.

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