Process for preparing low-calorie nuts

• US 5,290,578 A
• Filed: 03/30/1992
• Issued: 03/01/1994
• Est. Priority Date: 09/29/1989
• Status: Expired due to Term

• Current Assignee: Her Majesty The Queen In Right of Canada As Represented By The Minister of National Defence
• Original Assignee: Chand A. Passey, Narayan D. Patil
• Inventors: Passey, Chand A., Patil, Narayan D.
• Primary Examiner(s): HEGGESTAD, HELEN F
• Application Number:
  US07/856,149
• Time in Patent Office: 701 Days
• Field of Search: 426/417, 426/425, 426/429, 426/430, 426/632, 554/9, 554/11, 554/15, 554/16, 554/17
• US Class Current: 426/417
• CPC Class Codes: A23L 25/20 consisting of whole seeds or seed fragments
• CPC Class Codes: B01D 11/0203 with a supercritical fluid
• CPC Class Codes: C11B 1/104 using super critical gases or vapours
• CPC Class Codes: Y02P 20/54 using solvents, e.g. supercritical solvents or ionic liquids

Abstract

A process for preparing nuts, particularly peanuts, of reduced calorific value by partially extracting oil from the nut kernels by extraction with supercritical carbon dioxide. The process involves pretreatment of the kernels, including their humidification and optional microwaving. The pretreatment and the extraction steps are optimized with a view to removing maximum amounts of high-calorie substances without losing the organoleptic qualities of the nuts. The process produces virtually unbroken peanut kernels.

Claims

1. A process capable of preparing unbroken nut kernels of significantly reduced calorific value suitable for use as a snack food, comprising the steps of:

a) humidifying shelled non-roasted nut kernels by contact with water vapor, in a manner substantially avoiding the presence of free moisture on the kernels, to bring the moisture content to a level sufficient to prevent the kernels from breaking during subsequent extraction;

b) placing the humidified kernels in an extraction vessel and exposing the kernels to carbon dioxide under supercritical fluid conditions of temperature and pressure to extract oils from the kernels, said extraction being performed in one or more hold and extract stages with removal and replenishment of carbon dioxide occurring during the extract stage or stages; and

c) removing the calorie reduced kernels.

2. The process according to claim 1, wherein the nuts are selected from the group consisting of almonds, cashews, pistacchios, Brazil nuts and hazel nuts.

3. The process according to claim 1 wherein the carbon dioxide atmosphere in the holding periods is maintained under supercritical conditions.

4. The process according to claim 1 wherein the carbon dioxide in at least some of the holding periods is liquid carbon dioxide.

5. The process according to claim 1 wherein the extraction step is followed by a partial reduction of the carbon dioxide pressure.

6. A process according to claim 1, wherein the nuts are peanuts, and the humidifying step is such as to bring the moisture content to between 7 and 14 weight % on the wet basis.

7. The process according to claim 6 wherein the peanut kernels are humidified at a temperature in the range 30°

-80°

C. for a time sufficient to bring the moisture content of the kernels to from 8 to 11 wt %.

8. The process according to claim 6 wherein following the humidification step, the kernels are subjected to microwave energy for a time sufficient to enhance the permeability of the cell walls without causing the moisture content to drop below about 7%.

9. A process according to claim 1, wherein the nuts are peanuts, and wherein the extraction is carried out at a temperature in the range 31.05°

-90°

C. and under a pressure in the range 25-50 MPa for a time effective to extract a desired amount of oil from the kernels.

10. The process according to claim 9 wherein the temperature is 50°

-65°

C. and the pressure is 35-50 MPa.

11. The process according to claim 9 wherein the extraction is carried out in stages preceded, and separated by, periods of holding the peanuts in the atmosphere of supercritical CO₂ under the prevailing extraction temperature and pressure.

12. A process according to claim 1, wherein the pressure in the extraction vessel is held at supercritical conditions for the hold stages.

13. A process according to claim 1, wherein the humidifying step is carried out with a mixture of water vapor and an inert gas selected from the group consisting of nitrogen and carbon dioxide.

14. A process according to claim 1, wherein the humidifying step is carried out with water vapor produced by a humidifier vessel heated by a water bath.

15. A process according to claim 1, wherein the pressure in the extraction vessel is varied in a controlled manner during as the extraction progresses.

16. A process for preparing peanuts of reduced calorific value, comprising a humidification step involving contacting non-roasted unbroken nut kernels with water vapor in a manner substantially avoiding the presence of free moisture on the kernels, and so as to bring the moisture content of the kernels to from about 7 to about 14 weight % on the wet basis, and subjecting the kernels to microwave energy for a time sufficient to enhance permeability of the cell walls without causing the moisture content to drop below about 7%, the humidification and exposure to microwave energy being effected in alternate stages, and subsequently extracting the nut kernels with carbon dioxide under supercritical conditions of temperature and pressure.

17. A process for preparing unbroken nuts of reduced calorific value, comprising providing unbroken non-roasted nut kernels with a moisture content sufficient to prevent the kernels from breaking during a subsequent extraction stage, said extraction stage involving extracting the kernels with carbon dioxide under supercritical fluid conditions of temperature and pressure in an extraction vessel, wherein the pressure in the extraction vessel is varied in a controlled manner as the extraction progresses.