Ice cream of desired taste and good mouthfeel is produced by employing
specially designed formulation and a contrived production method. On
production, it is important to control a fat de-emulsification rate an
d distribution of fat globules, ice crystal size, air cells and unfroz
en matrix. We have investigated the relationship between fat de-emulsi
fication, and a type and the revolution number of a dasher. Ice cream
consisting of vegetable fat 9.0%, M.S.N.F. 9.5% and total solids 38.0%
was prepared by freezing the mix in a CREPACO continuous freezer. Con
ditions were varied as follows. The dasher type was 15 dasher, or 80 d
asher, the mix flow rate was 65 l/h and the revolution number of the d
asher was 110 rpm and 220 rpm. The particle size distribution of fat g
lobules was measured by a Laser diffraction particle size analyzer. Th
e fat de-emulsification rate was determined from the difference betwee
n the particle size distribution of fat globules measured in ice cream
mix and an ice cream solution prepared by diluting ice cream at 5 sim
ilar to 10 degrees C with 5 volumes of ion exchange water. Melting res
istance was examined by the meltdown method. The fat de-emulsification
rate increased when a dasher of larger was employed and this resulted
improved melting resistance. Also, the fat de-emulsification rate inc
reased using a higher revolution number and this resulted in improved
melting resistance. Dryness of ice cream increased when a dasher of la
rger volume and higher revolution number were used. The particle size
distribution of fat globules changed when the fat de-emulsification ra
te increased i.e. fat globules of below 1.2 mu m in diameter decreased
and, un-expectedly, the proportion of fat globules of ranging from 7
to 15 mu m in diameter increased.