Method for preparing D-psicose crystal

US10246476B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10246476-B2
Application numberUS-201515520786-A
CountryUS
Kind codeB2
Filing dateAug 9, 2015
Priority dateOct 20, 2014
Publication dateApr 2, 2019
Grant dateApr 2, 2019

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Abstract

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A method for producing high purity D-psicose crystals having a purity of 98% (w/w) or more and a grain size of MA200 or more. The method includes: removing impurities from a D-psicose solution to obtain a purified D-psicose solution; concentrating the purified D-psicose solution; cooling the concentrated D-psicose solution to 30° C. to 40° C. through a heat exchanger; seed crystallizing the D-psicose solution at 30° C. to 40° C. to obtain a seed crystallized massecuite; and full-scale crystallizing the seed crystallized massecuite. The method can produce pure D-psicose crystals in a suitable form for industrial application through an economical crystallization process from the D-psicose solution without using organic solvents.

First claim

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What is claimed is: 1. A method for producing D-psicose crystals having a grain size of MA200 μm or larger, comprising: removing impurities from a D-psicose solution to obtain a purified D-psicose solution; concentrating the purified D-psicose solution to provide a concentrated D-psicose solution having a concentration of 80 Brix (%) to 85 Brix (%); performing rapid cooling of the concentrated D-psicose solution to 30° C. to 40° C. in a heat exchanger to provide a copied D-psicose solution having a temperature between 3° C. and 4° C., wherein the rapid cooling is performed at a cooling rate of 5° C. to 20° C. per hour; placing the cooled D-psicose solution at a temperature between 30° C. and 40° C. to a crystallizer and adding D-psicose seed crystals to the crystallizer; performing seeded crystallization of D-psicose in the crystallizer while controlling temperature to stay between 30° C. and 40° C., which provides a D-psicose massecuite having a temperature between 30° C. and 40° C.; and performing full-scale crystallization of D-psicose using the D-psicose massecuite while controlling temperature to stay between 30° C. and 40° C., which provides D-psicose crystals having a grain size of MA200 μm or larger. 2. The method according to claim 1 , wherein the step of removing impurities from a D-psicose solution to obtain a purified D-psicose solution comprises: decoloring the D-psicose solution by passing through a column packed with a decoloring agent; desalting the decolored D-psicose solution via ion exchange resin chromatography; and passing the desalted D-psicose solution through a continuous chromatography column packed with an ion exchange resin to which calcium activating groups are attached. 3. The method according to claim 2 , wherein the ion exchange resin used in the ion exchange resin chromatography is a 100% weak basic anion resin. 4. The method according to claim 2 , wherein the step of passing through a continuous chromatography column is a simulated moving bed (SMB) process. 5. The method according to claim 2 , wherein the D-psicose solution purified through the continuous chromatography column has a purity of 95% (w/w) or more. 6. The method for producing high purity D-psicose crystals according to claim 1 , wherein performing seeded crystallization comprises adding seeds of D-psicose to the cooled D-psicose solution at a temperature between 30° C. and 40° C.; and adding additional D-psicose solutions to the seeds-added D-psicose solution. 7. The method according to claim 6 , wherein the concentration of the additional D-psicose solutions is in a range of 80 Brix (%) to 85 Brix (%). 8. The method according to claim 6 , wherein the volume of the additional D-psicose solutions is in a range of 5 (v/v) % to 20 (v/v) % based on the volume of the seed-added D-psicose solution. 9. The method according to claim 1 , wherein the full-scale crystallization comprises: adding another D-psicose solution having a purity of 95% (w/w) or higher and a concentration of 80 Brix (%) to 85 Brix (%) to the seed crystallized massecuite, and subsequently, repeating heating and cooling the resulting solution within the range of 30° C. to 40° C. 10. The method according to claim 9 , wherein repeating heating and cooling the resulting solution comprises adding, to the resulting solution, an additional D-psicose solution at a temperature of 30° C. to 40° C. two times or more an interval of 10 hours to 20 hours. 11. The method according to claim 10 , wherein the additional D-psicose solution is added each time in an amount of 5 (v/v) % to 20 (v/v) % based on the volume of the resulting solution to which the additional D-psicose solution is added. 12. A method of crystallizing D-psicose, the method comprising: concentrating a D-psicose solution to provide a concentrated D-psicose solution having a concentration of 80 Brix (%) to 85 Brix (%); performing rapid cooling of the concentrated D-psicose solution to 30° C. to 40° C. to provide a cooled D-psicose solution having a temperature between 30° C. and 40° C., wherein the rapid cooling is performed by heat exchange at a cooling rate of 5° C. to 20° C. per hour; placing, in a first crystallizer, the cooled D-psicose solution having a temperature between 30° C. and 40° C. and adding D-psicose crystal seeds to the first crystallizer; performing seeded crystallization of D-psicose in the first crystallizer while controlling a temperature of the D-psicose solution in the first crystallizer to stay between 30° C. and 40° C., which provides a D-psicose massecuite; placing the D-psicose massecuite to a second crystallizer and adding thereto a processed D-psicose solution to provide a crystallization mixture in the second crystallizer, wherein the processed D-psicose has a concentration between 80 Brix (%) and 85 Brix (%) and a temperature between 30° C. and 40°; and performing crystallization of D-psicose in the second crystallizer while controlling a temperature of the crystallization mixture in the crystallizer to stay between 30° C. and 40° C., which provides D-psicose crystals having a grain size of MA200 μm or larger. 13. The method of claim 12 , wherein performing seeded crystallization in the first crystallizer comprises adding an additional D-psicose solution to the first crystallizer at least once, wherein the additional D-psicose solution is at a temperature between 30° C. and 40° C. when added. 14. The method of claim 12 , wherein performing crystallization in the second crystallizer comprises adding an additional D-psicose solution to the second crystallizer at least once, wherein the additional D-psicose solution is at a temperature between 30° C. and 40° C. when added.

Assignees

Inventors

Classifications

  • Crystallisation on to a bed of product crystals; Seeding · CPC title

  • by indirect heat exchange · CPC title

  • Monosaccharides · CPC title

  • C07H1/06Primary

    Separation; Purification · CPC title

  • Anion-exchange · CPC title

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What does patent US10246476B2 cover?
A method for producing high purity D-psicose crystals having a purity of 98% (w/w) or more and a grain size of MA200 or more. The method includes: removing impurities from a D-psicose solution to obtain a purified D-psicose solution; concentrating the purified D-psicose solution; cooling the concentrated D-psicose solution to 30° C. to 40° C. through a heat exchanger; seed crystallizing the D-p…
Who is the assignee on this patent?
Cj Cheiljedang Corp
What technology area does this patent fall under?
Primary CPC classification C07H1/06. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Apr 02 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).