Process and apparatus for comminuting phytosterol particles
View Patent ↗A process and an apparatus for the comminution of foodstuff, especially phytosterol, particles to a particle size suitable for inclusion in liquid or solid foods.
1. An apparatus for comminuting foodstuff particles selected from the group consisting of phytosterol, neutraceutical, dietary mineral, food additives and food fortifiers particles to an average particle size suitable for inclusion in liquid or solid foods comprising:
controlled delivery means for delivering foodstuff particles having an average particle size in the range of between about 40 microns and about 200 microns, at a controlled mass velocity;
precooling means, in communication with said controlled delivery means, for precooling said foodstuff particles;
freezing means, in communication with said precooling means, for freezing said precooled foodstuff particles to below their glass transition temperature;
comminution means, in communication with said freezing means, for comminuting said frozen foodstuff particles;
particle size separating means, in communication with said comminution means, for separating foodstuff particles having an average particle size larger than about 25 microns from foodstuff particles having an average particle size smaller than about 25 microns;
packaging means, in communication with said particle size separating means, for packaging said foodstuff particles smaller than about 25 microns;
secondary freezing means, in communication with said particle size separating means, for freezing said foodstuff particles larger than about 25 microns to below their glass transition temperature;
secondary comminution means, in communication with said secondary freezing means, for comminuting said frozen foodstuff particles; and
said packaging means, in communication with said secondary comminuting means, for packaging said comminuted foodstuff particles having an average particle size smaller than about 25 microns.
2. An apparatus in accordance with claim 1 wherein said foodstuff particles are phytosterol particles.
3. An apparatus in accordance with claim 2 comprising bypassing means, in communication with said particle size separating means, for bypassing all or a portion of said phytosterol particles having an average particle size larger than about 25 microns from said secondary freezing means to said packaging means for packaging said phytosterol particles having an average particle size larger than about 25 microns.
4. An apparatus in accordance with claim 2 wherein said phytosterol particles are frozen in said freezing means and said secondary freezing means by contact with a cryogenic liquid.
5. An apparatus in accordance with claim 4 including recycle means for recycling a cryogenic gas, said cryogenic gas generated in said freezing means by the heating of said cryogenic liquid.
6. An apparatus in accordance with claim 5 wherein said cryogenic gas is recycled into said precooling means wherein it cools said phytosterol particles to below ambient temperature.
7. An apparatus in accordance with claim 5 wherein a cryogenic liquid is introduced into said comminution means concurrent with the introduction of said frozen phytosterol particles.
8. An apparatus in accordance with claim 7 comprising gas solid separating means, in communication with said particle size separating means, for separating said phytosterol particles from said cryogenic gas.
9. An apparatus in accordance with claim 1 wherein said comminuting means is an impact mill, said impact mill comprising a conically shaped stationary outer casing and an impact rotor, provided with a plurality of impact knives, having a complementary conical shape accommodated within said outer casing and providing a conically shaped gap there between.
10. An apparatus in accordance with claim 8 comprising a bag house in communication with said recycle means wherein said cryogenic gas is separated from entrained phytosterol particles and vented to the atmosphere.
11. An apparatus in accordance with claim 8 comprising a bag house in communication with said recycle means wherein said cryogenic gas is separated from entrained phytosterol particles and conveyed to a liquefaction plant for regeneration into a cryogenic liquid.
12. An apparatus in accordance with claim 2 wherein said packaging means includes means to package said phytosterol particles having an average particle size of less than about 25 microns in drums and disposing said drums on pallets.
13. An apparatus in accordance with claim 3 wherein said packaging means includes means for packaging said phytosterol particles having an average particle size of more than about 25 microns in drums and disposing said drums on pallets.
14. An apparatus in accordance with claim 1 wherein said secondary comminuting means comprises an impact mill and a jet mill, alternatively utilized as a function of the desired phytosterol particle size, wherein said jet mill is utilized to produce smaller sized particles than said impact mill.
15. An apparatus in accordance with claim 14 comprising a secondary particle size separating means, said secondary particle size separating means comprising an air classifier, said air classifier in communication with said impact mill and said jet mill for separating larger and smaller sized phytosterol particles.
16. An apparatus in accordance with claim 2 comprising phytosterol particle stream recycling means for recycling all or a portion of said phytosterol particles having an average particle size larger than about 25 microns to said freezing means.
17. A process of comminuting foodstuff particles selected from the group consisting of phytosterol, neutraceutical, dietary, mineral, food additives and food fortifier particles to a particle size suitable for inclusion in liquid or solid foods comprising the steps of:
delivering, under controlled mass velocity, foodstuff particles having an average particle size in the range of between about 40 microns and about 200 microns;
precooling said foodstuff particles having an average particle size in the range of between about 40 microns and about 200 microns;
freezing said precooled foodstuff particles to a temperature below the glass transition temperature;
comminuting said frozen foodstuff particles;
separating said comminuted foodstuff particles into a first foodstuff particle stream of foodstuff particles having an average particle size in the range of more than about 25 microns and a second foodstuff particle stream of foodstuff particles having an average particle size in the range of less than about 25 microns;
packaging said foodstuff particles of said second foodstuff particle stream;
freezing said foodstuff particles of said first foodstuff particle stream to a temperature below the glass transition temperature;
comminuting said frozen foodstuff particles of said first phytosterol particle stream; and
packaging said foodstuff particles of said first phytosterol particle stream.
18. A process in accordance with claim 17 wherein said foodstuff particles are phytosterol particles.
19. A process in accordance with claim 18 comprising bypassing all or a portion of said first phytosterol particle stream from said freezing stop to form a third phytosterol particle stream.
20. A process in accordance with claim 19 comprising packaging said third phytosterol particle stream.
21. A process in accordance with claim 18 comprising contacting said precooled phytosterol particles with a cryogenic liquid wherein said phytosterol particles are frozen.
22. A process in accordance with claim 21 comprising introducing a cryogenic liquid during said comminuting of said frozen phytosterol particles.
23. A process in accordance with claim 22 comprising separating a cryogenic gas, generated by vaporization of said cryogenic liquid during freezing and comminuting of said phytosterol particles, from said second phytosterol particle stream.
24. A process in accordance with claim 23 comprising recycling said cryogenic gas to said precooling step, wherein it contacts said phytosterol particles having an average particle size in the range of between about 40 microns and about 200 microns.
25. A process in accordance with claim 23 wherein said cryogenic liquid is liquid nitrogen and said cryogenic gas is gaseous nitrogen.
26. A process in accordance with claim 24 comprising filtering said cryogenic gas, subsequent to said contact with said phytosterol particles having an average particle size in the range of between about 40 microns and about 200 microns, whereby entrained phytosterol particles are removed and said filtered cryogenic gas in vented to the atmosphere.
27. A process in accordance with claim 24 comprising filtering said cryogenic gas, subsequent to said contact with said phytosterol particles having a average particle size in the range of between about 40 microns and about 200 microns, whereby entrained phytosterol particles are removed and said filtered cryogenic gas is recycled to a liquefaction plant where said cryogenic gas is converted into a cryogenic liquid.
28. A process in accordance with claim 18 wherein said freezing of said precooled phytosterol particles comprises showering said phytosterol particles with a cryogenic liquid.
29. A process in accordance with claim 18 wherein said comminuting of said frozen phytosterol particles of said first phytosterol particle stream comprises comminuting said phytosterol particles in alternate comminuting mills.
30. A process in accordance with claim 20 wherein said first, second and third phytosterol particle streams are packaged in drums and said drums are disposed on pallets.
31. A process in accordance with claim 18 comprising recycling all or a portion of said first phytosterol particle stream to said step of freezing said precooled phytosterol particles.