FIELD: food industry. SUBSTANCE: method involves the boiling down fillmass up to 91.0-91.5% CB and the following its crystallization by cooling to the required temperature by a few stages in mixers. Cooling rate in the first mixer is maintained to be 4.0-3.0 C/hr and fillmass is cooled to 62.0-57 C; in the second mixer - 3.0-2.5 C/hr and cooled to 48.0-43.0 C, and in the third mixer - at the rate 2.5-1.7 C/hr and cooled to 40.0-35 C. In the next mixer cooling rate is decreased by 1.0-0.5 C/hr as compared with former one. The cooling rate in the last mixer is 0.5-0.3 C/hr. EFFECT: increased sugar yield and accelerated crystallization process.
Title | Year | Author | Number |
---|---|---|---|
METHOD OF PRODUCING LAST-CRYSTALLIZATION MASSEQUITE | 0 |
|
SU1604855A1 |
METHOD FOR PRODUCTION OF LAST CRYSTALLIZATION MASSECUITE | 2003 |
|
RU2251573C1 |
METHOD OF CRYSTALLIZING SUGAR FROM RAW CLARIFICATION PRODUCT | 2000 |
|
RU2171844C1 |
METHOD OF PREPARING LAST-CRYSTALLIZATION STRIKE | 2000 |
|
RU2170766C1 |
METHOD FOR PRODUCING OF FINAL-PRODUCT SUGAR | 2004 |
|
RU2267540C1 |
METHOD FOR PRODUCTION OF FIRST CRYSTALLISATION FILLMASS | 2011 |
|
RU2479632C1 |
CRYSTALLINE WHITE SUGAR PRODUCTION METHOD | 2012 |
|
RU2511498C1 |
METHOD OF SUGAR PRODUCTION FROM RAW CANE SUGAR AT BEET SUGAR FACILITY | 2006 |
|
RU2335544C1 |
METHOD FOR PREPARING SUGAR OF LAST CRYSTALLIZATION | 2005 |
|
RU2293120C1 |
SUGAR PRODUCTION METHOD | 2007 |
|
RU2360005C1 |
Authors
Dates
1996-02-20—Published
1993-07-15—Filed