Process for hard panning of chewable cores and cores produced by the process

• US 6,821,535 B2
• Filed: 02/02/2001
• Issued: 11/23/2004
• Est. Priority Date: 02/03/2000
• Status: Expired due to Fees

• Current Assignee: Xyrofin Oy
• Original Assignee: Xyrofin Oy
• Inventors: Bond, Mike, Fairs, Ian, Oravainen, Juha, Pepper, Tammy, Nurmi, Juha
• Primary Examiner(s): HENDRICKS, KEITH D
• Application Number:
  US09/776,075
• Publication Number:
  US 20010018084A1
• Time in Patent Office: 1,390 Days
• Field of Search: 426/5, 426/89, 426/103, 426/285, 426/302, 426/303, 426/304, 426/305, 426/306, 426/658, 426/660, 426/273
• US Class Current: 426/5
• CPC Class Codes: A23G 3/2092 Apparatus for coating with atomised liquid, droplet bed, liquid spray
• CPC Class Codes: A23G 4/025 for coating or surface-finishing
• CPC Class Codes: A23G 4/10 characterised by the carbohydrates used, e.g. polysaccharides containing dairy products A23G4/16
• CPC Class Codes: A23G 4/20 Composite products, e.g. centre-filled , multi-layer, laminated

Abstract

The invention relates to a process for the hard panning of chewable cores in a pan or drum wherein a syrup of a crystallizable sugar or polyol is intermittently sprayed over a bed of the cores and the cores are dried between sprayings with a flow of air. The speed and efficiency of the panning process is increased by controlling the drying of the cores between sprayings by controlling parameters of the drying air in such a way as to intentionally leave a substantial residual moisture in the drying coating layer at the start of a subsequent spraying phase. The chewable products are preferably xylitol coated chewing gums.

Claims

1. A process for the production of chewable coated cores comprising the hard panning of chewable cores in a coating pan or drum wherein a syrup containing at least one of a crystallizable polyol, a crystallizable sugar or mixtures thereof is intermittently sprayed over a rotating bed of the cores and said cores are dried between sprayings with a flow of air, said cores being dried between sprayings by controlling effective parameters of said drying air selected from the group consisting of air humidity, air temperature, air flow speed, air flow time, air flow direction and any combination thereof and stopping said drying before the relative humidity of the outlet flow of drying air has reached its basic level at which its gradient has flattened to a plateau, so as to cause a substantial residual moisture to remain in the drying coating layer at the start of a subsequent spraying phase.

2. A process according to claim 1, wherein said parameters comprise the relative humidity of said drying air at an outlet of said pan or drum.

3. A process according to claim 1 or 2, wherein said parameters comprise the temperature of said drying air at an inlet of said pan or drum.

4. A process according to claim 2, wherein the relative humidity of the outlet air when starting said subsequent spraying is higher than the basic relative humidity level.

5. A process according to claim 1, wherein a number of coating cycles is performed, each coating cycle comprises a syrup application phase, an optional pause phase and a drying phase.

6. A process according to claim 2, wherein the flow of drying air to said bed is stopped before the drying is completed and the relative humidity of the outlet air is 1-10 percentages higher than its basic level.

7. A process according to claim 5, wherein the direction of the air during at least a part of said drying phases is direct with the air flowing from above the bed through the product.

8. A process according to claim 1, wherein the coating syrup contains about 40 to 80% of the total weight of a polyol selected from the group consisting of xylitol, sorbitol, maltitol, isomalt and mixtures thereof.

9. A process according to claim 8, wherein the polyol is xylitol.

10. A process according to claim 9, wherein the temperature of the bed of chewable cores is adjusted to a temperature of 25 to 45°

C. for at least a part of the total coating procedure, and the drying during said part of the procedure is performed with air having an inlet temperature of 25 to 75°

C.

11. A process according to claim 10, wherein the bed temperature is 33 to 40°

C.

12. A process according to claim 10, wherein the inlet temperature is 40 to 50°

C.

13. A process according to claim 10, wherein the coating syrup temperature is 40 to 80°

C.

14. A process according to claim 1, wherein the coating syrup contains about 40 to 80% of the total weight of a sugar selected from the group consisting of saccharose, fructose and glucose.

15. A process according to claim 1, wherein the coating syrup contains 1 to 20% of gum of the total weight.

16. A process according to claim 8, wherein the coating syrup comprises other polyols, flavors, pigments, special sweeteners, insoluble additives or mixtures thereof.

17. A process according to claim 1, wherein the coating syrup contains dissolved, suspended or dissolved and suspended xylitol, sorbitol, lacitol maltitol, isomalt, mannitol or mixtures thereof.

18. A process according to claim 1, wherein the coating of the chewable cores is started by an initial sequence having a bed temperature lower than the bed temperature during the residual moisture retaining drying procedure.

19. A process according to claim 1, wherein the coating of the chewable cores is finished by an end coating sequence having a bed temperature lower than the bed temperature during said residual moisture retaining drying procedure.

20. A process according to claim 18 or 19, wherein the direction of the flow of air during the initial coating, the end coating or both coatings is reversed such that the air flows from below the bed through the product.

21. A process according to claim 1, wherein the direction of the air flow, the air flow speed, the air flow time, the temperature of the air or any combination thereof is changed during the coating procedure.

22. A process according to claim 1, wherein the cores are coated with syrup until a desired coating thickness is provided and the coated cores are tempered after the coating for a time sufficient to allow crystallization of the polyol or sugar in said coating to provide a crunchy hard coating.

23. A process according to claim 1, wherein said core comprises chewing gum.

24. A process according to claim 6, wherein the relative humidity of the outlet air is more than 3 percentages higher than its basic level.

25. A process according to claim 6, wherein the relative humidity of the outlet air is 4-8 percentages higher than its basic level.

26. A process according to claim 10, wherein the temperature of the bed is adjusted to a temperature of from 30 to 40°

C. and said inlet temperature is from 30 to 65°

C.

27. A process according to claim 15 wherein the gum is Gum Arabic.

28. A process for the production of chewable coated cores by hard panning comprising:

spraying a syrup containing at least one of a crystallizable polyol, a crystallizable sugar and combinations thereof over a rotating bed of chewable cores in a coating pan or drum;

stopping said spraying of said rotating cores while continuing rotation;

starting to dry said cores with an inlet flow of air;

controlling the drying of said rotating cores by controlling effective parameters of the drying air selected from the group consisting of air humidity, air temperature, air flow speed, air flow time, air flow direction and any combination thereof;

stopping said flow of drying air at a point before the relative humidity of the outlet flow of said drying air has reached its basic level at which its gradient has flattened to a plateau indicating that a substantial residual moisture remains in the drying coating layer;

starting a subsequent spraying phase by spraying said syrup onto the moisture containing layer of the previous spraying phase; and

repeating the spraying and drying of said rotating cores until a predetermined coating has been provided.