Monoglycerides are important emulsifiers in food industry, cosmetics i
ndustry, chemistry and for the production of detergents. They are conv
entionally separated from mixtures of partial glycerides by molecular
distillation at temperatures above 200-degrees-C with a purity of max.
95%. The yield of monoglycerides is about 60%. An improved process fo
r the production of pure monoglycerides was developed. The partial gly
cerides are treated with propane as an extractant at 50 bar and temper
atures between 40 to 80-degrees-C in a countercurrent column. Due to t
he moderate extraction pressure, the process is called ''Low Pressure
Gas Extraction''. Monoglycerides are obtained with a purity above 99%
at a yield above 95%. Additionally pure diglycerides (above 92%) can b
e separated at high yields (above 90%). The process can be applied to
all kinds of glycerides as oleates, stearates, cocoates. Comparative d
iscussion of mass flow diagrams of conventional glyceride manufacturin
g and of the new extractive fractionation demonstrate the advantages o
f the new technology.