PROCESS FOR PRODUCING LACTOSE-FREE MILK WITH HIGH IN PROTEIN AND CALCIUM AND MILK WITHOUT SWEETNESS

Abstract

The present invention is related with the milk industry in general and with the processing industry of milk to produce for lactose-free milk and assessment of the subproduct in particular, and even more particularly in the milk processing industry through different separating means of the components such as micro- and nano filtration.

The function of the invention is to permit a lactose-free milk or a milk without lactose with a sensorial profile similar to that of normal pasteurized milk without lactose using the essential separation steps to reduce production costs, yet another objective was to determine the effect on the organoleptic characteristics of the concentration of natural milk components and concentrations which achieve the first objective, still another objective is to determine the ratio between retentate and permeate to obtain a sensorial profile equivalent to that of a normal pasteurized mil without lactose.

Claims

1. Process for the production of lactose-free milk with high in protein and calcium, and milk without sweetness which comprise a first step in which raw milk with standardized fat content is subjected to UF process which obtains an ultrafiltration retentate, milk concentrate (to a level of protein: from 7.9 to 8.7%, and a permeate ultrafiltration; the permeate of UF is subjected to nanofiltration NF where nanofiltration permeate comprising water and minerals and a nanofiltration retentate comprising water, lactose and mineral; The UF retentate is mixed with NF permeate to result in a reconstituted milk that ultrapasteurizara and packaged subsequently.

2. Process for the production of lactose-free milk with high-protein and calcium, and milk without sweetness, claim 1, wherein the protein concentration in the retentate of the UF is between 7.9 to 8.7%, preferably 8.0 to 8.6%, and even more preferably from 8.1 to 8.5% and even better from 8.2 to 8.4%.

3. Process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein the removal of lactose in the ultrafiltration is entre 29 and 36%.

4. Process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein the UF retentate is maintained the concentration of lactose between 9 and 10 Bx while the diafiltration process is performed.

5. Process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1 wherein the proportion to be use of the UF retentate is 64 to 71%, in combination with the portion of NF permeate of: 29 to 36%.

6. Process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein a value of 1 to 3%, is set in the final product of butterfat.

7. Process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein a protein value of 5.0 to 5.8% is established in the final product, with a content of 2.9 to 3.7% lactose.

8. The process for the production of lactose-free milk with high in protein and calcium, and milk without sweetness according to claim 1 which obtains an ultrafiltration retentate, milk concentrate to a level of protein: from 8.0 to 8.6%.

9. The process for the production of lactose-free milk with high in protein and calcium, and milk without sweetness according to claim 1 which obtains an ultrafiltration retentate, milk concentrate to a level of protein: from 8.2 to 8.4%.

10. The process for the production of lactose-free milk with high in protein and calcium, and milk without sweetness according to claim 1, wherein the protein concentration in the retentate of the UF is 8.0 to 8.6%.

11. The process for the production of lactose-free milk with high in protein and calcium, and milk without sweetness according to claim 1, wherein the protein concentration in the retentate of the UF is 8.1 to 8.5%.

12. The process for the production of lactose-free milk with high in protein and calcium, and milk without sweetness according to claim 1, wherein the protein concentration in the retentate of the UF is 8.2 to 8.4%.

13. The process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein_the removal of lactose in the ultrafiltration is from 30 to 35%.

14. The process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein the removal of lactose in the ultrafiltration is from 31 to 34%.

15. The process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein the removal of lactose in the ultrafiltration is from 32 to 33%.

16. The process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein in the UF retentate is maintained the concentration of lactose between 10 to 11 Bx while the diafiltration process is performed.

17. The process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein in the UF retentate is maintained the concentration of lactose between 11 to 12 Bx while the diafiltration process is performed.

18. The process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1, wherein in the UF retentate is maintained the concentration of lactose between 12 to 13 Bx while the diafiltration process is performed.

19. The process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1 wherein the proportion to be use of the UF retentate is 65 to 70% in combination with the portion of NF permeate of 30 to 35%.

20. The process for the production of lactose-free milk high in protein and calcium, and milk without sweetness, as claimed in claim 1 wherein the proportion to be use of the UF retentate is 67 to 68% in combination with the portion of NF permeate of 32 to 33%.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0056] FIG. 1 is a schematic of the process of the present disclosure, including all steps. In FIG. 1 we have the tank 1 of the standardized skim milk. This milk is fed into the computer ultrafiltration 2, outlining the broken line diagonal membrane. With this specification we can say that line 2a leads the retentate to the tank 5. On the other hand line 2b leads the permeate from the UF to the permeate tank 3.

[0057] The Line 3a leads the permeate to the tank NF 4. Meanwhile line 3b leading the permeate with the addition of water which stored in the tank 7, of mixing of retentate diafiltration. The tank 9 has water to inject to the NF retentate.

[0058] The part of the retentate that is not recirculated is sent to tank 8 where it is concentrated lactose solution.

[0059] The permeate from the NF is sent to the mixing tank 5 where it is mixed with the UF retentate, to result the product of delactosed milk sent to the tank 6, milk that subsequently receives the step of enzymatic cleavage of lactose.

[0060] The first step in the process of the present invention is the standardization of milk to be treated. This standardization is carried out playing with two components of milk, one is the fat concentration and protein concentration.

[0061] The raw milk is standardized to the required level of fat, i.e. a value of 1.4 to 2.2%, preferably 1.5 to 2.1, even more preferably from 1.6 to 2.0, even better 1.7 to 1.9% butterfat is established.

[0062] Meanwhile, the protein level after standardization as follows: A further preferred value of 2.9 to 3.7%, preferably 3.0 to 3.6, 3.1 to 3.5%, even better from 3.2 to 3.4%.

[0063] The next step is ultrafiltration, where you get a permeate of UF and a retentate of UF. The permeate is sent to the next step which is the step of nanofiltration NF. The retentate of the ultrafiltration is mixed with the permeate resulting from the NF. The UF permeate obtained is subjected to the process of NF to obtain a retentate (water, lactose and minerals) and a permeate (water and minerals).

EXAMPLES

Example 1

Set the Proportions Obtained of Retained and Permeate

[0064] The proportion of the retentate UF used is 64 to 71%, preferably 65 to 70%, even more preferably 66 to 69%, even better 67 to 68%; in combination with NF permeate ratio of: 29 to 36%, preferably 30 to 35%, even more preferably, 31 to 34%, even better from 32 to 33%. In the first instance I would like to emphasize that the optimal value of the UF retentate is 67.5% and the NF permeate is 32.5%. The use of higher proportion of UF retentate will result in a higher level of protein and lactose making the most expensive and sweeter product, sensory away from sweetness to a fresh milk at the moment of doing the hydrolysis of lactose and submit to treatment heat UHT; the use of a smaller proportion gives that the opposite case a less amount of protein and lactose losing sensory attributes to not recover the sweetness of milk after making the hydrolysis of lactose remaining. The different ranges described above are ideal for obtaining a good product with an optimal relationship.

Example 2

Establish the Level of Fat to Obtain the Final Product with Good Sensory Profile

[0065] Is established a value of 1 to 3%, preferably 1.3 to 2.7%, even more preferably from 1.6% to 2.4%, even better from 1.9 to 2.1% butterfat.

[0066] The optimum value set forth herein is 2%; lower amount of fat to 1% it will the product loss a sensory attributes, in addition to ascend the protein content as a matter of less added in the standardization in the cream. Amount greater to 3% we will have a product with better sensory performance, but the protein will be diluted and away from its optimum value, in addition to have an increase in calories.

Example 3

Determine the Optimal Range of Protein Concentration in the UF Retentate

[0067] Different final concentrations of protein in the retentate were tested. Finding those located between 7.9 to 8.7%, preferably 8.0 to 8.6%, and even more preferably from 8.1 to 8.5% and even better from 8.2 to 8.4% allowed to obtain the level of lactose, protein and desired reconstituted milk calcium.

Example 4

Establish the Protein Level to Obtain the Final Product with Good Sensory Profile

[0068] Is established a value of protein from 5.0 to 5.8%, preferably from 5.1 to 5.7, more preferably from 5.2 to 5.6%, even better from 5.3 to 5.5%.

[0069] The optimum value is 5.4%, a level greater than 5.8%, will make a product very expensive and not necessarily better sensory performance because it also increases the lactose and sweetness at the time of hydrolysis the same, a smaller amount will begin to have negative effects by decreasing sensory mouthfeel given by the protein and the amount of lactose not be sufficient to recover the sweetness of the original milk.

Example 5

The Implementation of the Diafiltration Process in Step NF

[0070] It was found that diafiltration could recover higher amount of minerals and aromatic compounds that give more flavor and milky notes.

Example 6

Defines the Optimal Range for Removal of Lactose

[0071] This range was between 29 and 36%, preferably between 30 and 35%, and most preferably from 31 to 34% and even better from 32 to 33%; reconstituted milk should be between 2.9 to 3.7% lactose, preferably between 3.0 to 3.6%, and most preferably from 3.1 to 3.5% and more preferably between 3.2 to 3.4% lactose) to generate a sweetness similar to normal pasteurized milk at the time of doing the enzymatic hydrolysis.

Example 8

Establish the Range for the Level Control of Lactose in the NF Retentate when Diafiltration is Used

[0072] The use of the UF permeate of a milk causes a limitation in the concentration of NF retentate (between lactose and calcium), as there is a risk of crystallization on the membrane (if solubilization of calcium are not undertaken), which is set to maintain a concentration of the retentate between 9 and 10 Bx, preferably 10 to 11 Bx, even more preferably 11 to 12, even better from 12 to 13 Bx while performing the process of diafiltration.

[0073] Higher level of lactose to 13 Brix is produced a crystallisation of calcium salts, clogging up the membranes and even damage them, make the diafiltration within 9 Brix will wash less of the retentate as a result of less flavor compounds be obtained and at the time of reconstitution of the final product with the UF retentate and permeate diafiltered to the NF the profile of the product would be less milk

[0074] Raw milk with contain of standardized fat is subjected to UF process wherein a retentate milk concentrate is obtained (to a level of protein: from 7.9 to 8.7%, preferably from 8.0 to 8.6%, and even more preferably between 8.1 to 8.5% and even better from 8.2 to 8.4%). Said retentate will be subsequently mixed with the permeate NF resulting with the use of diafiltration in a proportion from 64 to 71%, preferably 65 to 70%, even more preferably 66 to 69%, even better 67 to 68% of the retentate; in combination with NF permeate ratio of: 29 to 36%, preferably 30 to 35%, even more preferably, 31 to 34%, even better from 32 to 33%.

[0075] The permeate obtained of the UF is subjected to the NF process to obtain a retentate (water, lactose and minerals) and a permeate (water and minerals).

[0076] The filtration process is used primarily to make more efficient the recovery of mineral salts and aromatic compounds that give flavor, and it starts when the level of lactose and calcium is critical (insolubilization of calcium in membranes) in the NF retentate maintaining levels of lactose near to this point but without dilute more the retentate (see ranges). In the diafiltration only the water needed to maximize the recovery of mineral salts and flavor compounds needed to provide better sensory profile is used. The mixture obtained from retentate of UF and the permeate of NF reconstituted milk is then subjected to the UHT process for then adding the enzyme needed per container to hydrolyze lactose and recover the remaining sweetness level of a normal milk.

[0077] In diafiltration, water is added to the retentate during filtration, to maintain low solutes concentration and minimize saturation of the membrane. Thus, those solutes which are in the retentate, can still pass through the membrane for a longer period of time. The diafiltration can be developed in two different ways. In continuous, dilution water is added continuously during filtration, generally paying attention that the total volume of the feed remains constant. In Batch was allowed to proceed a certain filtration time without adding dilution water. After it has reduced the initial volume by a predefined value, it resets the spent volume with water and let continue the filtration. This process can be repeated several times to achieve the desired goal of separation (Zeman and Zydney, 1996).

[0078] It notes that the best method known to the applicant for carrying out the invention is that resulting from the present disclosure.

[0079] The invention has been sufficiently described so that a person of ordinary skill in the art can to reproduce and obtain the results mentioned herein. However, any skillful person that in the field of art to which the present invention may be able to make modifications not described in this application, however, if required for the implementation of these changes in a process of free-lactose milk, it is required the matter claimed in the following claims, such systems must be within the scope of the invention.