Enzyme-Assisted Soluble Coffee Production

• US 20080311245A1
• Filed: 07/07/2006
• Published: 12/18/2008
• Est. Priority Date: 07/18/2005
• Status: Abandoned Application

• Current Assignee: Intercontinental Great Brands LLC (Mondelez International, Inc.)
• Original Assignee: Intercontinental Great Brands LLC (Mondelez International, Inc.)
• Inventors: Perkins, Danielle E., Whalen-Pedersen, Erik, Silver, Richard S., Ceriali, Stefano, Plumb, Sian, Wragg, Anthony
• Application Number:
  US11/995,913
• Publication Number:
  US 20080311245A1
• Time in Patent Office: Days
• US Class Current: 426/52
• CPC Class Codes: A23F 5/246 Addition of, or treatment with, enzymes or microorganisms A23F5/163 and A23F5/204 take precedence
• CPC Class Codes: A23F 5/265 the solid substances are transported through the apparatus during the extraction cycle

Abstract

The invention relates to a coffee beverage composition being devoid of significant contents of oil and insoluble particulates, comprising

• (a) at least 15% based on the total weight of coffee solids of total mannose, wherein the free mannose content is less than 50% by weight of the total mannose content, and
• (b) less than 1,000 ppm on a total coffee solids basis of 5-hydroxymethyl furfural, and to a process for producing a soluble coffee extract, comprising the steps:
• (i) combining roast and ground coffee with water,
• (ii) adding hydrolase enzymes,
• (iii) wet-milling to a mean particle size of about 10 to about 250 μm,
• (iv) treating the reaction mixture by exposing it to a temperature in the range of about 20° C. to about 90° C., preferably about 50° C. to about 60° C., and
• (v) circulating the reaction mixture through a cross-flow semi-permeable membrane separation device where the soluble coffee extract is obtained as permeate.

Claims

1. A coffee beverage composition being devoid of significant contents of oil and insoluble particulates, comprising

(a) at least 15% based on the total weight of soluble coffee solids of total mannose;

wherein the free mannose content is less than 50% by weight of the total mannose content; and

(b) less than 1,000 ppm on a total soluble coffee solids basis of 5-hydroxymethyl furfural (5-HMF).

2. The coffee beverage composition according to claim 1, wherein the free mannose content is less than 30%, of the weight of total mannose.

3. The coffee beverage according to claim 1, wherein the 5-HMF level is less than 750 ppm, by weight of coffee solids.

4. The coffee beverage composition according to claim 1, further comprising cellooligosaccharides up to a content of 10% on a total soluble coffee solids basis.

5. The coffee beverage compositions according to claim 1, wherein the coffee beverage is dehydrated, a soluble coffee, a ready-to-drink coffee, a dry mix composition, a liquid mix composition, a frozen composition or a liquid concentrate composition.

6. The coffee beverage compositions according to claim 1, being essentially devoid of enzyme.

7. A process for producing a soluble coffee extract, comprising the steps:

(i) combining roast and ground coffee with water,

(ii) adding hydrolase enzymes,

(iii) wet-milling to a mean particle size of about 10 to about 250 μ

m to form a reaction mixture,

(iv) treating the reaction mixture by exposing it to a temperature in the range of about 20°

C. to about 90°

C., and

(v) circulating the reaction mixture through a cross-flow semi-permeable membrane separation device where the soluble coffee extract is obtained as permeate.

8. The process according to claim 7, wherein steps (ii) and (iii) can be carried out in any order.

9. The process according to claim 7, wherein the cumulative particle size distribution of the wet-milled roast and ground coffee comprises about 90% of the particles below 150 μ

m.

10. The process according to claim 7, wherein a multi-modal distribution is ground stage-wise or continuously to the desired particle size distribution.

11. The process according to claim 7, wherein the roast and ground coffee comprises roasted beans which were ground to an average particle size of between about 500 to about 5,000 μ

m.

12. The process according to claim 7, wherein the ground coffee is pre-treated to recover aroma compounds which are retained to be added back to later on obtained extracts or extracted solids.

13. The process according to claim 7, wherein the roast and ground coffee has been previously extracted with water and/or thermally hydrolysed.

14. The process according to claim 13, wherein the soluble coffee extract obtained from the spent grounds in step (v) is combined with the soluble coffee extract which was obtained in the extraction process of the fresh roast and ground coffee.

15. The process according to claim 13, wherein the extraction process is conducted at a temperature of less than 140°

C.

16. The process according to claim 7, wherein obtained soluble coffee extract is processed to make soluble coffee or liquid coffee.

17. The process according to claim 7, wherein the wet-milling is performed in two stages, the first stage leading to a mean particle size of about 100 to about 200 μ

m, and the second stage leading to a mean particle size of about 10 to about 150 μ

m.

18. The process according to claim 7, wherein carbohydrase and protease enzymes are used as hydrolase enzymes.

19. The process according to claim 18, wherein mannanases, or cellulases or a mixture thereof are used as carbohydrase enzymes.

20. The process according to claim 19, wherein a combination of at least one mannanase, at least one cellulase and at least one protease enzymes is used.

21. The process according to claim 20, wherein said combinations of enzymes act synergistically to reduce the physical volume of insoluble residue remaining after separation of the extract.

22. The process according to claim 20, wherein said enzymes are essentially devoid of dissaccharidases.

23. The process according to claim 7, wherein the process is operated in a batch mode.

24. The process according to claim 23, wherein the reaction mixture is separated into a liquid extract substantially reduced in insoluble matter and an insoluble matter stream after essential completion of the enzymatic reaction and before the membrane separation step.

25. The process according to claim 7, wherein the process is operated in a semi-continuous mode, wherein permeate is withdrawn until the mixture volume diminishes to a point that its viscosity or the pressure drop become high at which point some retentate is purged, and fresh coffee slurry fed and some fresh enzyme added.

26. The process according to claim 7, wherein the process is operated continuously by continuously adding fresh feed slurry and enzyme and continuously withdrawing a purge of retentate of equal volume from the recycle stream.

27. The process according to claim 7, wherein the membrane pore size is less than 0.8 μ

m.

28. The process according to claim 27, wherein said separation is performed with at least 1-10% of fine coffee solids being present in the feed to the membrane device.

29. The process according to claim 28, wherein the cross-flow semi-permeable membrane separation device comprises microfiltration or ultrafiltration membranes of molecular weight cut-off from about 20,000 to about 100,000.

30. The process according to claim 29, wherein the cross-flow semi-permeable membrane separation device comprises at least one of a hollow fibre filtration unit, a spiral wound unit and a flat plate unit.

31. The process according to claim 30, wherein the membrane separation occurs in two stages, wherein the permeate from the cross flow semi-permeable membrane microfiltration separation device is further processed in a second stage cross flow ultrafiltration cell of molecular weight cut-off from about 20,000 to about 100,000.

32. The process according to claim 31, wherein the grounds after the enzymatic extraction are post-treated by a second enzymatic reaction using galactanase and/or a thermal hydrolysis stage at a temperature between 100°

C. and 180°

C.

33. The process according to claim 32, wherein galactanase is added after about 75% of the mannan has been hydrolyzed.

34. The process according to claim 32, wherein the grounds are separated in a conventional separation step and/or in a membrane separation step.

35. The process according to claim 34, wherein the obtained extract is combined with other extracts.

36. A soluble coffee extract obtainable by the process according to claim 7.

37. The soluble coffee extract of claim 36 containing less than 1,000 ppm 5-HMF.

39. A coffee beverage or non-beverage composition comprising the soluble coffee extract of claim 36.

38. A coffee beverage or non-beverage composition being essentially devoid of enzyme residues.