<b>Siepermann's Process</b> (see English Patents 13,697 of 1889, 9,350 and 9,351 of 1900).
One part of sodium carbonate and two parts of charcoal (that is, sufficient charcoal to keep the mass from fusing during the process) is heated to
dark redness in the upper part of a vertical iron tube while a current of ammonia gas is sent through the mixture. Potassium cyanate, KCNO, is formed
thus :
K2CO3 + NH3 = KCNO + KOH + H2O.
The mixture is then allowed to fall to the bottom of the tube, where it is heated to bright redness. The cyanate is decomposed with formation of
cyanide:
KCNO + C = KCN + CO.
The final product is thrown into air-tight vessels, cooled, lixiviated with water, the solution being evaporated in vacuo until the KCN crystallises
out. <b>KCN is soluble with difficulty in the presence of much KOH or K2CO3, and crystallises out before these salts in the form of anhydrous
crystals.</b> As first made the KCN was a damp deliquescent mass, which had to be fused with the product of the ferrocyanide process. The
working of the process is difficult. It has been worked at Stassfurt since 1892.
<b>Bielby Process</b> (see English Patent, 4,820 of 1891). The principle is much the same as the Siepermann Process, but differs in
important details. Much less carbon is used, so that at the end only slight excess remains. The charcoal is added gradually during the operation, so
that the material is always present as a molten liquid through which the ammonia gas is forced under a slight pressure, when the following action
takes place:
K2CO3 + 4C + 2NH3 = 2KCN + 3CO + 3H2.
The final molten product is filtered from the small excess of unchanged charcoal, and thus a white saleable product is directly obtained without the
difficulties of lixiviation. However, since the melting point of the pure potassium carbonate is inconveniently high (about 890 C), ready-made cyanide
is added to it in order to reduce the temperature of fusion.
The Beilby process has been worked since 1892 by the Cassel Gold Extracting Co. at Glasgow, has achieved remarkable success. In 1899 Beilby's
process was estimated to supply fully 50 per cent of the world's output of high-strength cyanide. |