LACTOSE-REMOVING MILK PROCESS FOR LACTOSE-FREE MILK PRODUCTION AND BYPRODUCT USE

Abstract

The present invention relates to dairy and milk treatment industries for obtaining lactose-free milk and assessment of byproduct in particular, particularly to milk treatment industry through different separation means such as micro and nanofiltration equipment. One of the purposes of this invention is to provide a delactosed or lactose-free milk with sensory profile equivalent to a normal pasteurized milk using essential separation steps to reduce product costs. Another purpose of this invention is to determine the effect of milk natural components concentration on organoleptic properties to achieve the first purpose of this invention. Another purpose is to determine percentage between retentate and permeate to get a sensory profile equivalent to a normal pasteurized milk.

Description

FIELD OF THE INVENTION

The present invention relates to dairy and milk treatment industries for obtaining lactose-free milk and assessment of byproduct in particular, particularly to milk treatment industry through different separation means such as micro and nanofiltration equipment.

BACKGROUND OF THE INVENTION

After some time, it has been observed men and women who have trouble digesting lactose, disaccharide consisting of glucose and galactose. This situation can cause mild digestive problems, but also stronger problems. It has been attempted to solve this problem in several ways.

Furthermore, it is a high percentage tendency of the population, as can be seen in soft drinks by reducing carbohydrate intake in general and sugars in particular.

An alternative is to provide the person who has lactose intolerance a non-bender lactose enzyme, externally and by oral ingestion prior to the consumption of any dairy product. This solution is cumbersome and requires some planning and discipline by consumer. These features are not in target audience of a product to be marketed massively.

Other option is to apply lactase enzyme into milk fluid as a process for obtaining a product for direct consumption or for preparation of various milk derivatives to ensure low-lactose content.

These processes using lactase into the product provides a sweetness increased by the amount of galactose obtained, resulting an undesirable product by consumer.

U.S. Pat. No. 5,334,399 refers a solution to solve the problem adding potassium chloride to the product where enzymatic hydrolysis was performed. It is a practical solution, but often not allowed for breach of official standards in some countries.

Moreover, said procedure does not allow the assessment of an unwanted component which remains in said product and a process to remove said component to contain more advantages.

Some of said processes use equipment with membranes (filters) of different size (pore size) for different filtration processes such as ultrafiltration. Depending on the pore size, filter becomes more selective as follows:

1. Microfiltration. Used to retain particles according to their size such as bacteria and spores. Let through proteins, fat, sugars, amino acids, minerals and water.

2. Ultrafiltration. Used to retain particles according to their size such as proteins and fat. Let through sugars, amino acids, minerals and water.

3. Nanofiltration. Used to retain particles according to their size such as sacarose or granulated sugar. Let through minerals and water.

4. Reverse osmosis. Let through water and simple minerals.

Thus, it is not possible to determine a milk treatment process for lactose-free milk with similar organoleptic properties such as ultrapasteurized milk without lactose-free process.

A process known currently comprising the steps of:

Equipment use membranes capable to perform microfiltration, ultrafiltration, nanofiltration and reverse osmosis processes to separate milk components.

The process for producing lactose-free or low-lactose milk is as follows:

• • Subjecting skim or low-fat milk through ultrafiltration process to obtain a retentate and permeate.
  • UF permeate is then subjected to nanofiltration process to obtain equally said retentate and permeate.
  • A mixed UF retentate and NF permeate is performed.

UF and NF processes can perform a partial or even near elimination of lactose content where also part of minerals are lost. This mixture then is subjected to an enzymatic hydrolysis process using β-galactosidase enzyme to reduce lactose content generating glucose and galactose.

Also can perform reconstitution of milk using UF retentate adding water to protein desired level or including reverse osmosis process to concentrate minerals of NF permeate and used for milk reconstitution.

This process provides milk with strange organoleptic characteristics for a normal milk without considering this situation, besides de possibility of using operations which increase the production process.

Any invention that refers the necessary steps (micro, ultra or nano filtration and reverse osmosis) to achieve a lactose-free process for a delactosed or lactose-free milk with a sensory profile equivalent to a pasteurized milk (lactose milk), a partial removal of lactose by physical means and then removing the remaining lactose using lactase enzyme (β-galactosidase enzyme) and obtaining a fully lactose as byproduct, it contributes a non-existent technical knowledge to the state of the art for its protection by a patent.

Patent No. CA2701066, Vernazza, Francesco, refers to a method to obtain low-fat milk comprising at least two steps: first step milk is subjected to an ultrafiltration process to produce an ultrafiltration permeate and retentate after said process and; a second step wherein said ultrafiltration permeate is subjected to a nanofiltration process to produce a nanofiltration permeate and a nanofiltration concentrate after said process. Nanofiltration permeate is continuously recycled directly to the nanofiltration operation to dilute retentate from ultrafiltration and to obtain low-fat milk therefrom. This method does not consider physicochemical conditions to achieve milk with specific organoleptic characteristics.

Mexican patent No. PA/a/2004/011243, Janne Sahlstein, refers to a procedure for producing lactose-free milk products. Process of said invention is characterized by subjecting whole milk to ultrafiltration (UF), nanofiltration (NF) and reverse osmosis concentration, followed by the addition of salt to the UF retentate. Disadvantages of said method is the addition of salt to ultrafiltration retentate adding concentration by reverse osmosis becoming said method more expensive.

Mexican patent No. PA/a/2005/002049 refers to a method for separating milk components, comprising the steps of: passing milk in one-direction-flow through a filtration apparatus; a first step of milk filtration by ultrafiltration means for producing a first liquid filtered and a first concentrated, wherein lactose content of first filtered does not exceed 5.5% by weight; a second step of milk filtration by nanofiltration of first liquid filtered by nanofiltration means for producing a second liquid filtered and a second concentrated, wherein lactose content of second filtered does not exceed 0.15% by weight; a third step of milk filtration by reverse osmosis of second liquid filtered for producing a third liquid filtered and a third concentrated, wherein lactose content of third concentrated does not exceed 0.06% by weight; and wherein first filtered, second filtered and third filtered are removed from filtration apparatus through a first output, a second output and a third output respectively. Said patent contains reverse osmosis.

U.S. Pat. No. 8,445,052, Holst et. al., refers to a process for producing lactose-free or substantially lactose-free milk, preferably without adding water, and the resultant product. Said process comprising the steps of: a) ultrafiltration of original milk for obtaining a first permeate and a first retentate; b) nanofiltration of said first permeate for obtaining a second permeate and a second retentate; mixing first retentate with second permeate for obtaining a mixture; and d) hydrolyze remaining lactose in said mixture for obtaining a hydrolyzed milk. Process provides a lactose-free product with original milk flavor. Said process does not consider the composition of fats, proteins and carbohydrates of original milk.

Processes present in state of the art have the following disadvantages: only used UF retentate and mixing directly retentate with soft water to achieve desired fat and protein levels, making these levels higher to obtain products with good sensory profile.

Also is a complicated and higher cost of operation process due to the application of 3 filtration steps: UF, NF and reverse osmosis.

Also adding flavor to achieve a product that according to Mexican standards, said product not categorized as milk but as flavored milk.

Also incorporate the use of more proteins, up from 3.5% being unaffordable for Mexican market.

Also are methods or processes with lower yields due to the water removal in product and does not return said water in filtration process.

Also said methods or processes use external salts for recovering of lost minerals which increases cost of product.

Also not considered recovery of mineral salts and possible aromatic compound total or partially responsible of milk flavor.

OBJECT OF THE INVENTION

One of the purposes of this invention is to provide a delactosed or lactose-free milk with sensory profile equivalent to a normal pasteurized milk.

Another purpose of this invention is to provide the above quality using essential separation steps to reduce product costs.

Another purpose of this invention is to determine the effect of milk natural components concentration on organoleptic properties to achieve the first purpose of this invention.

Another purpose is to determine percentage between retentate and permeate to get a sensory profile equivalent to a normal pasteurized milk.

Further purposes and qualities will be detailed through the present invention.

BRIEF DESCRIPTION OF THE INVENTION

In other words, the process object of this invention begins with standardization of milk to be treated.

Raw milk is standardized to the required fat level, setting a value from 1.4 to 2.2%, preferably from 1.5 to 2.1, even more preferably from 1.6 to 2.0%, even more preferably from 1.7 to 1.9% of butterfat. Meanwhile, protein level after standardization is as follows: a value from 2.9 to 3.7%, preferably from 3.0 to 3.6%, even more preferably from 3.1 to 3.5%, even more preferably from 3.2 to 3.4%.

Later, milk is subjected to UF process wherein a “milk-concentrate” retentate is obtained (from 4.7 to 5.3%, preferably from 4.8 to 5.2%, even more preferably from 4.9 to 5.1%), said retentate subsequently will be mixed with the permeate resulting from NF process. This concentration must be reached in retentate in ultrafiltration step to obtain level of lactose in reconstituted milk.

In the process of this invention, proportions in UF step are: 55 to 63%, preferably from 56 to 62%, even more preferably from 57 to 61%, even more preferably from 58 to 60% of retentate and; from 37 to 45%, preferably from 38 to 44%, even more preferably from 39 to 43%, even more preferably from 40 to 42% of permeate.

Permeate obtained in UF is subjected to NF process to obtain a retentate (water, lactose and minerals) and a permeate (water and minerals).

For NF step, process of this invention stablishes the following proportions: from 30 to 38%, preferably from 31 to 37%, even more preferably from 32 to 36%, even more preferably from 33 to 35% of retentate and; from 62 to 70%, preferably from 63 to 69%, even more preferably from 64 to 68%, even more preferably from 65 to 67% of permeate.

Diafiltration process is used primarily to streamline the recovery of minerals salts and aromatic compounds that provide flavor, it begins when lactose level is critical (lactose crystallization in membranes) in NF retentate, keeping lactose levels closed to said level avoiding diluted over the retentate.

In diafiltration only enough water is used to restore water lost during the process, such that by mixing UF retentate and NF permeate is obtained the same milk volume which it started only by obtaining a lower yield for protein adjustment necessary to provide better sensory profile. Mixing obtained from UF retentate and NF reconstituted milk permeate is then subjected to UHT process and then adding thereto enzyme needed by container to hydrolyze remaining lactose.

The use of UF permeate of milk causes a limitation in NF retentate concentration (between lactose and calcium), due to risk of crystallization on membrane, therefore it is recommended maintain a retentate concentration between 9 and 10° Bx, preferably from 10 to 11° Bx, even more preferably from 11 to 12° Bx, even more preferably from 12 to 13° Bx while diafiltration process is performed.

To generate a similar sweetness such as pasteurized milk during enzymatic hydrolysis, such step also part of process of this invention, in UF and NF steps should be removed from 35 to 40%, preferably from 36 to 39%, even more preferably from 37 to 38%; reconstituted milk should be from 2.7 to 3.5%, preferably from 2.8 to 3.4%, even more preferably from 2.9 to 3.3% and even more preferably from 3.0 to 3.2% of lactose.

Another parameter defining process of this invention is the proportion obtained from retentate and permeate in UF and NF processes. Said process has the following proportions: proportions in UF process are: from 55 to 63%, preferably from 56 to 62%, even more preferably from 57 to 61%, even more preferably from 58 to 60% of retentate; from 37 to 45%, preferably from 38 to 44%, even more preferably from 39 to 43%, even more preferably from 40 to 42% of permeate. For NF process: from 32 to 36%, preferably from 33 to 35% of retentate; from 62 to 70%, preferably from 63 to 69%, even more preferably from 64 to 68%, even more preferably from 65 to 67% of permeate.

BRIEF DESCRIPTION OF DRAWINGS

FIG. 1 shows process scheme of the present description, all the steps including.

A detailed description of the invention is next, relying on examples for this purpose is carried out.

DETAILED DESCRIPTION OF THE INVENTION

FIG. 1 shows a process scheme of the present invention, all the steps including. FIG. 1 shows standardized fat milk tank (1). Said milk is fed into ultrafiltration equipment (2), through broken line outlining the membrane. Line (2a) connecting retentate to tank (5). Line (2b) connects UF permeate to permeate tank (3).

Line (3a) carries permeate of permeate tank to NF equipment (4). Line (3b) carries permeate with addition of water stored into retentate-diafiltration water mixture tank (7). Tank (9) contains water that is injected to NF retentate.

A portion of the non-recirculated retentate is carried to the tank (8) wherein concentrated solution is concentrated.

NF permeate is carried to mixing tank (5) wherein UF retentate is mixing with said NF permeate to get delactosed milk which is carried to tank (6), said delactosed milk receives enzymatic cleavage of lactose step.

The first step in the process of this invention is to standardization of milk to be treated. Said standardization is accomplished with two milk components, fat concentration and protein concentration.

Raw milk is standardized to required fat level, i.e., setting a value from 1.4 to 2.2%, preferably from 1.5 to 2.1, even more preferably from 1.6 to 2.0%, even more preferably from 1.7 to 1.9% of butterfat.

Protein level after standardization is as follows: a value from 2.9 to 3.7%, preferably from 3.0 to 3.6, eve more preferably from 3.1 to 3.5%, even more preferably from 3.2 to 3.4%.

Next step is ultrafiltration to get a UF permeate and a UF retentate. Permeate is carried to nanofiltration (NF) step. UF retentate is mixing with NF permeate. UF permeate is subjected to NF process to get a retentate (water, lactose and minerals) and permeate (water and minerals).

EXAMPLES

Example I

	Test
Date	no.	Activities
Apr-	P1	Methodology:
21th-14		Use of skim milk (2 g/L).
		Total solids concentration (SC) up to 12.8% (8.26%
		protein) using ultrafiltration process (UF).
		Reconstitution of milk using retentate and soft water
		to initial protein values of milk (3.1%), using
		only 2.12% of lactose.
		Heat treatment of milk-UHT Process-
		Enzymatic hydrolysis (using β-galactosidase) of
		lactose remaining less than 1%.
		Results:
		Product obtained has a milky and sweet diluted profile
		Next steps:
		Raise the profile increasing fat level to 1.6%.

In this example, skim milk has a butterfat content of 2 g/L. No nanofiltration has used and enzymatic hydrolysis of lactose remaining was less than 1%.

The result was undesirable because the product was very sweet and diluted.

Example II

May	P2	Methodology:
9th-14		Use of skim milk (2 g/L).
		Concentration (SC) up to 12.98% (8.14% protein)
		using UF process.
		Reconstitution of milk using retentate and soft water
		to initial protein values of milk (3.1%), using
		only 2.2% of lactose.
		Standardization up to 1.6% of butterfat (BF)
		Heat treatment of milk-UHT Process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5%.
		Results:
		Product obtained has a dairy profile, more tan P1
		but still less sweet diluted profile.
		Next steps:
		Explore the possibility of reducing the use of soft
		water and reinstate salts and possible flavor compounds
		that are lost in UF permeate through the inclusion
		of nanofiltration (NF) process.

In this example, skim milk had the same butterfat content on treated milk of 2 g/L. concentration through UF has noticeably same concentrations of milk compounds.

Product is less sweet than example 1, and has a dairy profile, however, has a thin consistency.

Example III

May	P3	Exploratory test process
21st-14		To evaluate the feasibility of processing UF permeate
		with NF process, in order to improve the dairy
		product profile retrieving salts and possible flavor
		compounds, thus decreasing the use of soft water.
		Methodology:
		Use of skim milk (2 g/L).
		Concentration (SC) up to 9.51% (4.2% protein) using
		UF process.
		Using UF permeate for processing by NF.
		Concentration of NF retentate up to 13.5°Bx max
		(the process stops at this point).
		Results:
		It is feasible to perform NF process using UF permeate
		and decreasing use of soft water for reconstitution
		of milk without adding lactose to reconstituted
		product.
		Next steps:
		To perform test using UF and NF processes.

In this example, butterfat content on treated milk is the same, but concentration on final solids and protein is lower such that is less water with ultrafiltration step, because a nanofiltration step is applied to permeate.

It is feasible performed NF process using UF permeate and using less soft water for reconstitution of milk.

Example IV

May	P4	Methodology:
28th-14		Use of skim milk (2 g/L).
		Concentration (SC) up to 14.32% (8.58% protein)
		using UF process.
		Using UF permeate for processing by NF.
		Concentration of NF retentate up to 12% of lactose.
		Reconstitution of milk using UF retentate, NF permeate
		and soft water to initial protein values of
		milk (3.2%), using only 1.7% of lactose.
		NO standardization is performed at a level of 1.6%
		of butterfat for the purpose of comparing the product
		obtained against only UF (P1).
		Heat treatment of milk-UHT process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5%.
		Results:
		Product obtained improves dairy profile using these
		two processes versus P1, but still less sweet and
		diluted.
		Next steps:
		Establish minimum amount of remaining lactose in
		reconstituted milk having the same sweetness as
		initial milk.
		To identify the feasibility of using skim milk of
		16 g/L.
		To determine whether additional homogenization
		and pasteurization processes retain more flavor
		compounds into fat globules.

The result is still not acceptable, the product is diluted and sweetness is poor.

Example V

Jun	P5	Methodology:
18th-14		Use of skim milk (16 g/L).
		Pasteurization and homogenization of milk
		(72° C./16 s to 170 bar)
		Concentration up to 16.11% SC (8.7% protein) using
		UF process (see text in result section*).
		UF permeate processing through NF.
		NF retentate concentration up to 9.18% of lactose.
		Reconstitution of milk using UF retentate, NF permeate
		and soft water to initial protein values of
		milk (3.2%), with 2.525 of lactose (it had to standardize
		at this level of lactose*).
		PH adjustment using lactic acid, because acidity is
		lost during all filtration process.
		Heat treatment of milk-UHT process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5%.
		Results:
		Product obtained has a better dairy profile, however
		sweetness is perceived slightly below to a pasteurized
		milk.
		Pasteurization and homogenization process does
		not contribute to the improvement of profile but also
		complicates operation and cost.
		There are major benefits using skim milk but:
		*Using skim milk, curve use on rapid methods equipment
		(Milkoscan) are not suitable due outliers observed
		during UF process monitoring, because of this,
		the product was more concentrated in UF step obtaining
		values above.
		Next steps:
		Develop a specific curve on Milkoscan to obtain reliable
		data during concentration process by opening
		with semi-skim milk.
		Explore the possibility of incorporating diafiltration
		process in NF step for improving mineral salts recovery
		and aromatic compounds, thereby eliminating
		the direct use of soft water.

Example VI

Jun	P6	Exploratoriy testing process
25th-14		Validate the curve drawn in Milkoscan equipment,
		monitoring data obtained with protein titration process.
		Explore diafiltration process during NF step to improve
		dairy profile of product and streamline the recovery
		of salts and possible aromatic compounds,
		thereby eliminate use of soft water directly in the
		reconstitution to get the same UF permeate volume.
		Methodology:
		Use of skim milk (2 g/L).
		Concentration up to 10.54% SC (4.69% protein) using
		UF process.
		Processing UF permeate through NF and diafiltration.
		Concentration of NF retentate using diafiltration
		process when indicates 12-13°Bx in retentate
		avoiding exceed these values until recovering the
		same volume of UF permeate. The final NF permeate
		concentration is up to 7.26% of lactose.
		Reconstitution of milk using UF retentate and NF
		permeate diafiltered to initial protein values of milk
		(3.07%), using only 3.26% of lactose.
		Standardization performed a level of 1.6% of butter-
		fat.
		Heat treatment of milk-UHT process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5%
		Results:
		Product obtained has a better dairy profile with a
		noticeable decrease when diluted and sweetness is
		similar to a raw milk.
		Proper functioning of generated curve for this
		concentration process is shown.
		Feasible and beneficial the use of diafiltration process
		is shown.
		Next steps:
		To perform the process using semiskim milk.
		To use curve generated in Milkoscan for raw milk.
		To use diafiltration process in NF step.

Product obtained has a better dairy profile, however, sweetness is lower than a pasteurized milk.

Example VII

Jun	P7	Methodology:
26th-14		Use of skim milk (16 g/L).
		Retentate concentration up to 14.96% SC (6.23%
		protein) using UF process and working pressure to
		35 psi.
		UF permeate processing using NF and diafiltration.
		Final concentration of NF retentate using diafiltration
		to 9.32% of lactose (12.67% SC), up to 12°Bx
		during diafiltration (°Bx vary from 8 to 12). Working
		pressure on NF is up to 560 psi.
		Reconstitution of milk using UF retentate plus NF
		diafiltered permeate (soft water is removed) to initial
		protein values of milk (3.29%), remaining only
		2.75% of lactose.
		Heat treatment of milk-UHT process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5%.
		Results:
		Product obtained has better texture, dairy profile
		and same sweetness as pasteurized milk versus P6,
		but still has opportunity to optimize texture and
		sweetness.
		Next steps:
		To improve sweetness level through optimize lactose
		level from 3.1 +/− 1% in reconstituted milk.
		To achieve lower °Bx width variation during diafiltration
		process keeping values in upper limit, that
		is, between 12 and 13°Bx.

Following was obtained:

Product obtained has better texture, dairy profile and same sweetness as pasteurized milk versus P6, but still has opportunity to optimize texture and sweetness.

Example VIII

Jul 1st-	P8	Methodology:
14		Use of semi skim milk (16 g/L).
		Retentate concentration up to 13.05% SC (5.02%
		protein) using UF process.
		UF permeate processing using NF and diafiltration.
		Final concentration of NF retentate using diafiltration
		to 7.66% of lactose (10.13% SC), up to 13°Bx
		during diafiltration (°Bx vary from 10 to 12.5).
		Reconstitution of milk using UF retentate plus NF
		diafiltered permeate to initial protein values of milk
		(3.26%), remaining only 3.27% of lactose.
		Heat treatment of milk-UHT process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5
		Results:
		Product obtained has better dairy profile and same
		sweetness as pasteurized milk, optimizing texture
		but still has opportunity to optimize versus pasteurized
		milk.
		To achieve lower °Bx width variation and close variation.
		Next steps:
		To decrease °Bx width variation during diafiltration
		process.
		Explore a reconstitution of milk to higher protein
		levels to optimize texture.

Results obtained as follows:

Product obtained has better dairy profile and same sweetness as pasteurized milk, optimizing texture but still has opportunity to optimize versus pasteurized milk.

To decrease ° Bx width variation during diafiltration process but still close said variation.

Example IX

Jul	P9	Methodology:
16th-14		Use 1.4% of fat milk because fat is increased in
		reconstituted milk depending on the desired concentration
		level in UF retentate.
		Retentate concentration up to 14.14% SC (5.81%
		protein) using UF process.
		UF permeate processing using NF and diafiltration.
		Final concentration of NF retentate using diafiltration
		to 9.59% of lactose (12.94% SC), up to 13°Bx
		during diafiltration (°Bx vary from 10.5 to 12.5).
		Two reconstitutions of at different levels of protein
		(3.2 and 3.5%) using UF retentate plus NF diafiltered
		permeate are performed, remaining only
		2.91% of lactose in 3.2% of protein and 3.03% of
		lactose in 3.5% of protein, both with 1.6% fat.
		Heat treatment of milk-UHT process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5%.
		Results:
		Products obtained have better dairy profile, better
		than 3.5% of protein and slight lack of texture.
		It is a better control of °Bx amplitude.
		Next steps:
		To perform reconstitutions of milk at different protein
		and fat levels (up to 1.8% keeping as low-fat
		milk)

Products obtained have better dairy profile, better than 3.5% of protein and slight lack of texture.

Example X

Jul	P10	Methodology:
24th-14		Use 1.4% of fat milk.
		Retentate concentration up to 14.07% SC (5.63%
		protein).
		UF permeate processing using NF and diafiltration.
		Final concentration of NF retentate using diafiltration
		to 9.08% of lactose (12.29% SC), up to 13°Bx
		during diafiltration (°Bx vary from 10.5 to 12.5).
		Three reconstitutions of at different levels of protein
		(3.2 protein and 1.6% fat, 3.2% protein and
		1.8% fat, 3.5% protein and 1.8 fat) are performed,
		remaining only 2.97%, 2.97% and 3.11% of lactose
		respectively using UF retentate plus NF diafiltered
		permeate.
		Heat treatment of milk-UHT process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5%.
		Results:
		Product obtained has better dairy profile due to the
		difference in fat level.
		Difference in protein is low between 3.2 and 3.5%
		compared with fat from 1.6 to 1.8%.
		Best products are from 3.2 to 3.5% of protein with
		1.8% fat.
		Profiles of these products are similar sweetness
		and texture to pasteurized milk, whiter presentation
		and non-overcooked.
		Next steps:
		To perform product with 3.3% of protein and 1.8%
		fat as final proposal.

Protein difference is not as marked between 3.2 and 3.5% comparing fat between 1.6 and 1.8% found.

Example XI

Aug	P11	Methodology:
14th-14		Use 1.4% of fat.
		Retentate concentration up to 14.66% SC (5.7%
		protein).
		UF permeate processing using NF and diafiltration.
		Final concentration of NF retentate using diafiltration
		to 9.68% of lactose (13.24% SC), up to 13°Bx
		during diafiltration (°Bx vary from 11 to 12.5).
		Two reconstitutions of at different levels of protein
		(3.3 and 3.5% of protein) with 1.8% fat are performed,
		remaining only 3.13% and 3.14%% of lactose
		using UF retentate plus NF diafiltered permeate.
		Heat treatment of milk - UHT process-
		Enzymatic hydrolysis of lactose remaining less than
		0.5%.
		Results:
		Both products are similar sensory to a pasteurized
		milk, whiter presentation and non-overcooked. It is
		recommended 3.3% protein and 1.8% fat.

Best method known for applicant for carrying out the invention is that resulting from the present description.

This invention has been sufficiently described so that a person with ordinary skills in present state of the art can reproduce and obtain results mentioned in said invention. If any person may be able to make modifications not described in said invention, said modifications in a lactose-removing milk process for lactose-free milk production and byproduct use, said modifications must be within scope of invention.

Claims

1. A lactose-removing milk process for lactose-free milk production and byproduct use, comprising a standardization of milk to be treated, applying an ultrafiltration UF step, permeate obtained in UF is subjected to NF process to obtain a nanofiltration retentate, obtaining diafiltered step between UF and NF, characterized in, that standardization is carried out to provide milk to be delactosed a fat value from 1.4 to 2.2%, preferably from 1.5 to 2.1, even more preferably from 1.6 to 2.0%, even more preferably from 1.7 to 1.9% of butterfat and a protein value from 2.9 to 3.7%, preferably from 3.0 to 3.6%, even more preferably from 3.1 to 3.5%, even more preferably from 3.2 to 3.4%; UF step is designed to achieve a retentate from 55 to 63%, preferably from 56 to 62%, even more preferably from 57 to 61%, even more preferably from 58 to 60% and a permeate from 37 to 45%, preferably from 38 to 44%, even more preferably from 39 to 43%, even more preferably from 40 to 42%.

2. A lactose-removing milk process for lactose-free milk production and byproduct use according to claim 1, characterized in, that nanofiltration step stablishes the following proportions: retentate from 30 to 38%, preferably from 31 to 37%, even more preferably from 32 to 36%, even more preferably from 33 to 35% and; permeate from 62 to 70%, preferably from 63 to 69%, even more preferably from 64 to 68%, even more preferably from 65 to 67%.

3. A lactose-removing milk process for lactose-free milk production and byproduct use according to claim 1, characterized in, that diafiltration step begins when lactose level is critical (lactose crystallization in membranes) in NF retentate, keeping lactose levels closed to said level avoiding diluted over the retentate to streamline the recovery of minerals salts and aromatic compounds that provide flavor, only enough water is used to restore water lost during the process, such that by mixing UF retentate and NF permeate is obtained the same milk volume which it started only by obtaining a lower yield for protein adjustment necessary to provide better sensory profile.

4. A lactose-removing milk process for lactose-free milk production and byproduct use according to claim 3, characterized in, that nanofiltration retentate maintain a retentate concentration between 9 and 10° Bx, preferably from 10 to 11° Bx, even more preferably from 11 to 12° Bx, even more preferably from 12 to 13° Bx while diafiltration process is performed.

5. A lactose-removing milk process for lactose-free milk production and byproduct use according to claim 1, characterized in, that UF and NF steps should be removed from 35 to 40%, preferably from 36 to 39%, even more preferably from 37 to 38%; reconstituted milk should be from 2.7 to 3.5%, preferably from 2.8 to 3.4%, even more preferably from 2.9 to 3.3% and even more preferably from 3.0 to 3.2% of lactose.

6. A lactose-removing milk process for lactose-free milk production and byproduct use according to claim 1, characterized in, that proportions in UF process are: from 55 to 63%, preferably from 56 to 62%, even more preferably from 57 to 61%, even more preferably from 58 to 60% of retentate and; from 37 to 45%, preferably from 38 to 44%, even more preferably from 39 to 43%, even more preferably from 40 to 42% of permeate.

7. A lactose-removing milk process for lactose-free milk production and byproduct use according to claim 1, characterized in, that proportions in NF process are from 30 to 38%, preferably from 31 to 37%, even more preferably 32 to 36%, preferably from 33 to 35% of retentate and; from 62 to 70%, preferably from 63 to 69%, even more preferably from 64 to 68%, even more preferably from 65 to 67% of permeate.