produced dccording to the activated carbon process anti moreover Jpprecidbly cheaper, 4 . fj the protein content 01 hydrolyzed stdrch is reduced b y acitvated bentonite, the converter juice contains only 0,09-0,1 I n/e. APer passage through the cation exchangers all but 0,008-0,010 l i / ~j of the protein is extr.icted and finally amounts afier passing through the exchanger "Asmit" to only 0,004-0,006 yet. The limpid dilute juices may be vapor-concentrated from about 36' Bx up t o 86' Bx without intermediate processing. Wages in Australia being very high, works are mechanised to a maximum extent. i. The economical advantages of the described process Jre more limited or even questionable for wheat starch with La protein content of over 0,4 oio. 6. The great purity of the wheat starch syrups isnecessary, 3 s the demands made on confections for stability and storage properties Are particularly high in the humid sultry climate of the coastdl regions of Australia, and becmse of extremely long transport routes both within the continent and beyond its limits. Litcratrrrii~d~weis (1) : l d a m , G. -4.: Starch recovery and purification. Can. J. Technology 29 (M3y 1951), 217-231. (7) Horn)/, F. E.: Wheat Products for Industrial Uses.