US1784982A - Curing massecuite - Google Patents
Curing massecuite Download PDFInfo
- Publication number
- US1784982A US1784982A US167595A US16759527A US1784982A US 1784982 A US1784982 A US 1784982A US 167595 A US167595 A US 167595A US 16759527 A US16759527 A US 16759527A US 1784982 A US1784982 A US 1784982A
- Authority
- US
- United States
- Prior art keywords
- massecuite
- mass
- curing
- separated
- pasty
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
- C13B30/04—Separating crystals from mother liquor
- C13B30/06—Separating crystals from mother liquor by centrifugal force
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
- C13B30/04—Separating crystals from mother liquor
- C13B30/08—Washing residual mother liquor from crystals
- C13B30/10—Washing residual mother liquor from crystals in centrifuges
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B50/00—Sugar products, e.g. powdered, lump or liquid sugar; Working-up of sugar
- C13B50/02—Sugar products, e.g. powdered, lump or liquid sugar; Working-up of sugar formed by moulding sugar
Definitions
- Green sugar or massecuite was formerly boiled, so that it left the boiling apparatus in a more or less still liquid state. It was cooled in tubs, but only to the extent so that it left these tubs still in the liquid state. If the massecuite showed atendency to lose 'this state, syrup or even water was added in order to maintain the mass in a sufliciently liquid condition, so that the crystals could i be separated from the mother liquor in centrifuges of known construction in which the centrifugal force amounted to 800 times the weight of the mass to be separated.
- the yield can be still further increased if the a massecuite during or after cooling is deprived of a portion of its water content, for example by evaporation'or the like.
- a massecuite of pasty orlastio condition cannot be worked in centri uges of known construction. Experiments have now ployment of especially high centrifugal force (over 800 times the weight of the centrifuged mass) the pasty or plastic masses can be separated into sugar crystals and syrup more efiiciently and purer crystals are obtained than were possible with liquid massecuite and the use of centrifugal forces of usual amount.
- a process for increasing the yield of sugar crystals from any kind'of massecuite which comprises boiling the massecuite, cool ing to a pasty condition, removing a portion of its water content by evaporation, and then separating the mass into sugar crystals and syrup by means of a centrifuge in which the centrifugal force is considerably more than 800 times the weight of the mass to be separated.
- a process for increasing the yield of sugar crystals from massecuite which comprises increasing crystallization by bringing the massecuite to a pasty condition, and then separating the mass into sugar crystals and syrup by-means of a centrifuge, in which the centrifugal force is considerably more than 800 times the weight of the mass to be separated.
Description
Patented Dec. 16, 1930 UNITED" STATES PATENTOFFICE SOCIETE ANONYME, F TIRLEMONT,-BELGIUM, A
oonrona'rrou CURING MASSECUITE No Drawing. Application filed February 11, 1927, Serial No. 167,595, and in Germany July 24, 1926.
Green sugar or massecuite was formerly boiled, so that it left the boiling apparatus in a more or less still liquid state. It was cooled in tubs, but only to the extent so that it left these tubs still in the liquid state. If the massecuite showed atendency to lose 'this state, syrup or even water was added in order to maintain the mass in a sufliciently liquid condition, so that the crystals could i be separated from the mother liquor in centrifuges of known construction in which the centrifugal force amounted to 800 times the weight of the mass to be separated.
With the continued cooling in the cooling tubs, the yield of sugar increases; it is found by experience that this is also the case if the massecuite loses the liquid state and passes over into a pasty or plastic condition; Also,
the yield can be still further increased if the a massecuite during or after cooling is deprived of a portion of its water content, for example by evaporation'or the like. A massecuite of pasty orlastio condition cannot be worked in centri uges of known construction. Experiments have now ployment of especially high centrifugal force (over 800 times the weight of the centrifuged mass) the pasty or plastic masses can be separated into sugar crystals and syrup more efiiciently and purer crystals are obtained than were possible with liquid massecuite and the use of centrifugal forces of usual amount.
I claim: a 1. A process for increasing the yield of sugar crystals from any kind of massecuitewhich comprises boiling the massecuite, 0001-.
ing to a pasty condition, and then separating' the mass into sugar crystals and syrup b means of a-centrifuge, in which the centri ugal force is considerably more than 800 times the weight of the mass to be separated. 2. A process for increasing the yield of sugar crystals from any kind which comprises boiling the massecuite, cooling to a pasty condition, removing a portion of its water content, and then separating the mass into sugar crystals and syrup by means of a centrifuge operating under a high cenof the mass to be separated.
shown that by the .em-
trifugal force of atleast 800 times the weight g 3. A process for increasing the yield of sugar crystals from any kind'of massecuite which comprises boiling the massecuite, cool ing to a pasty condition, removing a portion of its water content by evaporation, and then separating the mass into sugar crystals and syrup by means of a centrifuge in which the centrifugal force is considerably more than 800 times the weight of the mass to be separated.
4. A process for increasing the yield of sugar crystals from massecuite which comprises increasing crystallization by bringing the massecuite to a pasty condition, and then separating the mass into sugar crystals and syrup by-means of a centrifuge, in which the centrifugal force is considerably more than 800 times the weight of the mass to be separated.
In testimony whereof I have aflixed my signature.
, JULIEN BERGE.
of massecuite
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1784982X | 1926-07-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
US1784982A true US1784982A (en) | 1930-12-16 |
Family
ID=7743198
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US167595A Expired - Lifetime US1784982A (en) | 1926-07-24 | 1927-02-11 | Curing massecuite |
Country Status (1)
Country | Link |
---|---|
US (1) | US1784982A (en) |
-
1927
- 1927-02-11 US US167595A patent/US1784982A/en not_active Expired - Lifetime
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1784982A (en) | Curing massecuite | |
CN107652156B (en) | Crystallization method and device of beta-methylnaphthalene | |
US2503695A (en) | Method for producing solids concentrate from fruit and vegetable juices as well as other solutions | |
GB610376A (en) | Method of centrifuging and washing sugar massecuites and similar mixtures | |
US2651665A (en) | Recovery of pure paraxylene | |
US1775385A (en) | Process for centrifugal separation | |
RU2511498C1 (en) | Crystalline white sugar production method | |
RU2815551C1 (en) | Method for separation of fillmass of first crystallisation of sugar production | |
Slavyansky et al. | Improvement of the technology of separation of utfel i crystallization in batch centrifuges | |
RU2544596C2 (en) | Crystalline white sugar production method | |
US2347157A (en) | Centrifugal purging and washing method for sugar mixtures and the like | |
US2175995A (en) | Method of centrifuging sugar | |
RU2652995C1 (en) | Crystalline white sugar production method | |
GB687405A (en) | Improvements in and relating to the separation of xylenes by crystallization | |
US2213710A (en) | Method of recovering sugar crystals from solution | |
RU2264471C1 (en) | Sugar production method | |
US1740693A (en) | Process of manufacturing sugar | |
GB274799A (en) | Improvements relating to curing massecuite | |
RU2158311C1 (en) | Sugar production process | |
US2129864A (en) | Process of crystallizing dextrose | |
US2217598A (en) | Process for refining sugar | |
RU2815554C1 (en) | Method of producing first crystallization fillmass | |
RU2360005C1 (en) | Sugar production method | |
US495614A (en) | Eugen | |
SU68332A1 (en) | Method of crystallization of the second product massecuite |