Manufacture of Chloroform from Acetone and Bleaching-powder.
-This is the process most generally employed. The method differs in minor detail with the various manufactures, but the following may be taken as
representatives. The reaction is carried out in a cast-iron still of about 800 gallons capacity, which is provided with stirring gear, steam-coils,
and cooling-coils, and is connected with a condenser; 300 gallons of water are run into the still, and 800 lbs of bleaching powder are added through a
manhole, which is then securely bolted down. During addition of the bleaching powder the mixture is very thoroughly stirred. (In some processes the
mixing is carried out in a separate vessel, and the suspension is strained from the larger unbroken lumps of bleaching powder before being allowed to
run into the still.) The container (A in the diagram shown on p. 78) is charged with 70 lb of acetone, which is then slowly run into the bottom of the
still by means of a valve B. The introduction of the acetone is accompanied by a rise in the temperature which is not allowed to exceed 110 F.,
cooling being effected if necessary by stopping the flow of acetone and circulating cold water though the cooling coil in the still. When all the
acetone has been introduced the contents of the still are raised to 134 F. At this temperature chloroform begins to distill over. The temperature is
then very gradually raised to 150 F., so as to keep the chloroform readily distilling. Towards the end of the reaction the mixture is stirred and the
temperature raised until no more chloroform distills over.
The crude chloroform obtained is separated and purified first by agitation with concentrated sulfuric acid. This operation is carried out in the
vessel shown in the diagram ; 1,500 lb. of crude chloroform are introduced into the vessel and thoroughly stirred, by means of the agitation gear
shown, with 600 lb. of sulfuric acid. The stirring is continued until a sample of the chloroform when thoroughly shaken with pure concentrated
sulfuric acid does not impart the slightest color on the latter. The time required for complete purification is usually about 3 hours. The chloroform
is next separated from the sulfuric acid and finally distilled over lime. The yield obtained from the above quantities averaged from over 2,000
batches was 124 lb., the highest yield in any one case being 131 lb. Variation in yield is attributed to the varying composition of bleaching powder,
though doubtless other factors influence the result. Bleaching powder containing less then 33% of available chlorine gives unsatisfactory results,
while samples containing more then 35% of chlorine are also unsatisfactory. The best results appear to be obtained with bleaching powder containing
34% of available chlorine. |