Sweet particulate fat-containing powder, its preparation and its use
The present invention relates to powders comprising, based on dry weight: (a) 25-75 wt. % carbohydrates, including at least 50% sucrose by weight of said carbohydrates; (b) 10-70 wt. % fat; and (c) 0.4-20 wt % protein; wherein the powder comprise an amorphous matrix of fat, protein and carbohydrates as well as sucrose crystallites embedded therein; and wherein at least 40% of the sucrose is present in crystalline form. Processes of preparing the powders are also provided, comprising: (a) providing a dispersion comprising fat, carbohydrate, protein and water, and having a dry solids content of 50-75 wt. %; (b) providing a finely divided particulate sucrose; and (c) spray drying the dispersion into a spray drier while continuously introducing the finely divided particulate sucrose into the spray drier in an amount of at least between 40 and 80 wt. % based on the total weight of carbohydrates in the final spray dried product.
1. A process of preparing a powder, comprising, based on dry weight:
(i) 25-75 wt. % carbohydrates, wherein at least 50% by weight of the carbohydrates is sucrose, and wherein at least 40% of the sucrose is in crystalline form;
(ii) 10-70 wt. % fat;
(iii) 0.4-20 wt. % protein;
wherein at least 80 wt. % of the powder particles comprises 40-75 wt. % of an amorphous matrix and 25-60 wt. % of one or more sucrose crystallites embedded in the amorphous matrix, the process comprising:
(a) providing a dispersion comprising fat, carbohydrate, protein and water, and having a dry solids content of 50-75 wt. %;
(b) providing a finely divided particulate sucrose; and
(c) introducing the dispersion and the finely divided particulate sucrose into a spray dryer through a dry powder injection unit consisting of at least two concentric tubes having a central tube equipped with a spray nozzle through which the dispersion is pumped and a mantle or outer tube surrounding the central tube, through which outer tube the finely divided particulate sucrose is pneumatically transported towards the nozzle to insure instantaneous mixing with the dispersion emerging from the nozzle, and wherein the particulate sucrose is provided in an amount of at least 40 wt. % based on the total weight of carbohydrates in the final spray dried product.
2. The process according to claim 1 , wherein the dispersion comprises 60-75 wt. % dry solids.
3. The process according to claim 2 , wherein the dispersion comprises 65-75 wt. % dry solids.
4. The process according to claim 1 , wherein sucrose is provided in an amount of at least 50 wt. % by weight of the carbohydrates.
5. The process according to claim 1 , wherein sucrose is provided in an amount of at least 50 wt. % by weight of the sucrose contained in the final spray dried product.
6. The process according to claim 1 , wherein the finely divided particulate sucrose is continuously introduced into the spray drier in an amount of 50-75 wt. % based on the total weight of carbohydrates in the final spray dried product.
7. The process according to claim 1 , wherein the dispersion comprises, by weight of dry matter:
(a) in an amount of up to 50 wt. % carbohydrates;
(b) 20-75 wt. % fat;
(c) 1-40 wt. % protein; and
(d) 0-20 wt. % other edible ingredients.
8. The process according to claim 1 , wherein the finely divided sucrose particulate has a d10 between 140 and 180 μm, a d50 between 300 and 380 μm, and a d90 between 500 and 600 μm.