U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Direct production of a pure sugar product from cane juice

Patent 4332622 Issued on June 1, 1982. Estimated Expiration Date: Icon_subject August 25, 2000. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

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Inventors

Assignee

Application

No. 06/181234 filed on 08/25/1980

US Classes:

127/41, Inversion of sucrose127/46.1, Treatment of sacchariferous solutions127/48Chemical precipitation of impurities

Examiners

Primary: Schor, Kenneth M.

Attorney, Agent or Firm

International Class

C13K 3/00 (20060101)

Abstract

This invention provides a method for the purification of cane juice to produce a finished product of very high quality. This purification process and general concept differs from existing cane juice purification schemes in that traditional methods either produce crystalline raw sugar or a liquid product commonly referred to as high test or fancy molasses. The processing of the cane juice generally comprises the steps of:(a) pretreating the cane juice to remove any soil or foreign matter and substantially reducing the total cation concentration of the cane juice;(b) hydrolyzing the pretreated cane juice to a desired degree;(c) purifying the hydrolyzed juice without precipitation or crystallization of raw sugar by subjecting the solution obtained in step (b) to gross demineralization and decolorization; and(d) concentrating the purified solution obtained in step (c) to obtain a pure odorless finished sugar product which meets or exceeds existing standards for pure sugar.Preferably, these steps are carried out by:(e) acidifying fresh raw sugar cane juice to a pH lower than its naturally occurring pH (e.g. a pH of 2 to 5 or less) and heating the acidified juice at a temperature ranging from between about 40° and 95° C. (preferably 60° to about 80° C. for a period of time sufficient to convert the desired amount of cane juice to glucose and fructose;(f) adjusting the pH of the product of step (e) to about 5.2 to form a floc;(g) separating the floc from the juice and passing the juice through a filter aid to form a clear solution;(h) subjecting the clear solution to gross demineralization and decolorization by passing the solution sequentially through a decolorizer cation and anion exchange resin;(i) passing the solution obtained in step (h) through a carbon, bone char and/or carbonaceous adsorbant resins filter to remove cane flavors and odors;(j) passing the effluent obtained in step (i) over a cation and anion exchange resin; and(k) evaporating or concentrating the effluent of step (j) to the desired solids levelwhereby a clear, colorless and odorless liquid finished product is obtained which meets or exceeds standards for pure sugar solutions.

Other References

  • Meade-Chen; Cane Sugar Handbook; 10th Ed.; pp. 359-377; 1977; John Wiley & Sons Inc
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