The invention relates to the field of natural cheese and a method for making natural cheese with specific texture attributes.
Typical natural cheeses have well known texture attributes. Processed cheese, such as American cheese, is a food product made from natural cheese with the addition of other ingredients such as emulsifiers, sodium citrate, calcium phosphate, sorbic acid, enzymes, cheese culture, vitamin D3, milk fat, extra salt, saturated vegetable oils, whey and/or artificial food colorings. Processed cheese has several advantages over natural cheese including resistance to oiling offs when heated and a uniform look and physical behavior. Disadvantages include an elevated amount of sodium and artificial ingredients.
The present invention includes a method for accumulating streams from which to make natural cheese including the steps of adding concentrated acidified milk, adding cream, adding homogenized cream, adding water and adding raw milk.
The present invention includes a method for producing natural cheese including the steps of creating a first stream of raw milk, creating a second stream of concentrated acidified milk, creating a third stream of cream, creating a fourth stream of homogenized cream, creating a fifth stream of water, combining the five streams and making natural cheese from the combined streams.
The present invention includes a method for producing natural cheese with specific texture and flavor attributes including the steps of creating a first stream of raw milk, creating a second stream of concentrated acidified milk by adding an acidulant to skim milk to reduce the pH to 5.5 – 6.5 and concentrating the acidified milk 3-4 fold, creating a third stream of cream having 35-45% milk fat, creating a fourth stream of homogenized cream having 20-25% milk fat, creating a fifth stream of water, combining the five streams and making natural cheese from the combined streams.
Preferred exemplary embodiments of the invention are illustrated in the accompanying drawings in which like reference numerals represent like parts throughout.
Before any embodiments of the invention are explained in detail, it is to be understood that the invention is not limited in its application to the details of constructions and the arrangement of components set forth in the following description or illustrated in the drawings. The invention is capable of other embodiments and of being practiced or of being carried out in various ways.
The invention relates to natural cheese and the production of natural cheese with specific texture attributes. The invention utilizes processes within the boundaries of conventional cheese make technology which allow for the tuning of natural cheese texture while maintaining an ingredient statement as that of a Standard of Identity cheese.
With reference to
In stream 1, raw milk is separated and an acidulant, such as lactic acid, is added to reduce the skim milk pH. Other acidulants, such as using a CO2 injection, can also be utilized. The pH is reduced to between 5.5 and 6.5, more particularly reduced to between 5.7 to 5.9 and, more particularly reduced to 5.9. Following pH adjustment, the acidified skim milk is ultra-filtrated, as is known in the art, to concentrate the acidified skim milk to 3-5-fold, more particularly to 4-5 fold, and more particularly to 4.5.
In stream 2, a portion of the concentrated acidified milk is re-blended with water to produce a mineral reduced milk stream. The resultant stream will have reduced mineral contents such as calcium and phosphorus.
In stream 3, the raw milk is separated to produce cream with greater than 25% milk fat, more particularly in the range of 25-42%, and more particularly 35%.
Stream 4 includes raw milk.
In stream 5, raw milk is standardized to between with between 3-12% milk fat, more particularly to between 3-8% milk fat, and more particularly to 4% milk fat. After the desired milk fat is obtained, the stream is then homogenized, as is known in the art.
In
Turning now to
Streams 1, 2 and 3 are the same as described above with respect to
The streams can be combined in the same or differing percentages to form a unified stream that enters a pasteurization step. Examples of various percentages for the seven streams described in
The total amount demineralized protein prior to milk standardization is preferably in the range of 30-50%, and more particularly in the range of 45-47%, of total proteins in the vat. The total amount of homogenized fat is preferably in the range of 20-40%, and more particularly 35%, prior to milk standardization. The milk concentration factor is preferably approximately 1-1.5, and more particularly 1.15. The target protein:fat ratio in the final milk is preferably around 0.70-0.95, and more preferably 0.77-0.85. Preferably, these are the parameters that determine the ratios of each stream to the vat.
Unacidified skim milk concentrates can also be utilized to satisfy the standardization requirements such as amount of demineralized proteins, protein: fat ratio, and milk concentration factor as can be seen in example CT 7 (stream 8). Lactose powder (Stream 10) is added to compensate the lactose removal as a result of ultrafiltration as well to aid in acid development during the cheesemaking (CT5 V1 to V3). Portion of cream is added with lipolytic enzyme prior to homogenization to generate lipolytic flavor in the final cheese (Stream 9 in CT4 V4).
After pasteurization, the cheese make process proceeds as is known in the art. Additional lactic acid can be added after pasteurization to bring the pH of cheese milk down in the range of 6.1-6.5, and more specifically around 6.2-6.3.
The results of the method shown in
The natural cheese produced from the method disclosed herein preferably has the following compositional characteristics:
The cheese made according to
Examples CT1-CT5. An overview of five different example formulations for making a natural cheese is set forth in Table 1 and Table 2.
The mineral composition of Stream 2 in the examples is given in Table 3. The reduction of calcium and phosphorus achieved by ultrafiltration at pH 5.9 and dilution to starting volume with water is approximately 39% and 46% compared to the starting skim milk.
In Example CT1, the cheese make process was designed to achieve a composition and mimic processing for Monterey Jack type cheese as follows:
Processing times for Examples CT1-CT4 are set forth in Table 4.
In the Examples, calcium and phosphorus reduction in cheese is obtained when using at total of 47% of demineralized split stream 1 and 2 to raise the concentration factor of the milk to 1.15, reducing milk pH prior to milk-ripening to pH 6.35 with lactic acid and at a starter dosage of 25U/100 L. A pre-ripening time of 60 minutes and salting at pH of 5.22 contributed to the effective mineral reduction. In addition to the reduced mineral content in the split stream, the short make time and low pH in the final cheese contributed to additional calcium and phosphorus reduction. See Table 5.
Cheese firmness is measured instrumentally under cold conditions (refrigerator, shredding/slicing temperature) and melting properties were measured by two empirical tests, modified Schreiber test for melt area and the extent of oiling-off. The data is summarized in Table 6.
The calcium content of the in the final cheese influences the hot functionality of the cheese such as melt behavior. Despite higher extent of demineralization, cheeses spread less upon melting than the reference cheeses with normal calcium and phosphate content at near identical moisture content.
Partial homogenization is effective to reduce the extent of oiling-off, compared to the reference cheese and to other variants without homogenized cream. See for example
To assess cold functionality, the firmness (stress at fracture) and shortness (strain at fracture) is measured by uniaxial compression test. Data are given in Table 6. Fracture stress is translated to firmness and fracture strain to shortness. The firmness of the cheeses differed from around 50 kPa to 130 kPa and it appeared to be most strongly correlated with moisture contents. The level of calcium in cheese was not found to be related to firmness. Fracture strain, shortness (= opposite to long/elastic) appeared to be correlated with calcium content of the cheese while pH appeared not to influence the fracture strain.
With respect to cold functionality, the results of the instrumental compression-fracture measurement are in line with sensory perceived firmness of the cheeses.
With respect to hot functionality, with regard to melt area (modified Schreiber test), the amount of spread is comparable with that the targeted processed cheese counterparts.
With respect to oiling-off, the effect of emulsion properties is pronounced in the oiling-off behavior as shown in
In one example, the cheese milk standardized with the various streams according to the one process has the following characteristics: Protein:fat = 0.88, protein content = 4.16% (i.e., concentration factor 1.15 compared to normal milk with 3.6% protein), lactose content = 3.2% (CT5/vat 4), i.e., a dilution by 29% compared to starting milk (4.5% lactose), proportion of demineralized protein (retentate + diluted retentate) is 47% of total protein in the standardized cheese milk, and the proportion of homogenized fat is 35% of total fat in the standardized cheese milk.
The natural cheeses produced had the following approximate composition: moisture content 41 – 42%, NaCl content 1.8 %, fat content 30% and pH -5.30. The calcium and phosphorus content of these cheeses is reduced by approximately 30% and 40% respectively, compared to a reference cheese.
To evaluate the cheese melting properties analytically, temperature sweeps by oscillating small strain rheology were conducted. This methodology relates to the dynamic changes in the ratio between a system’s elastic/solid and viscous/liquid behavior (tan δ = G″/G′), as function of temperature. For comparison purpose, a commercially procured sample of Monterey Jack was also evaluated against the cheeses. Parameters used for the evaluations are described in Table 7.
The visco-elastic behavior upon heating to 80° C. and cooling was markedly different from a standard natural cheese (Monterey Jack), and approached that of processed cheese. As can be seen in Table 8, the Tan δmax (heat) was highest in the natural cheese sample whereas, the Tan δmax (heat) was comparatively low for the processed cheese sample. The Tan δmax (heat) for all the test cheeses ranged from 1.65 to 2.01. CT5 cheeses are less fluid-like and assumingly more cohesive than the natural cheese. The cross-over temperature was found to be typically higher for processed cheeses. The processed cheeses achieved liquid-like properties only at comparatively higher temperature, compared to the natural cheeses. See
With respect to
With respect to
The rheological analysis indicates differences in molecular assembly of the fat-filled protein matrix of the processed cheese and that of the texture-tuned cheeses of CT6. The processed cheese attains fluid-like character at higher temperatures (T crossover heating 12° C. higher) and maximum Tan δ remains approx. 35% lower (indicating a higher cohesivity).
The cheeses produced meets the desired chemical composition. Firmness and specific melting properties (e.g., oiling-off, spread, low/no stringiness, homogeneous melt) resembles those of the processed cheese benchmarks.
Turning now to
Stream 1 is raw milk as is known in the art.
Stream 2 is milk, such as skim milk, that has been separated from the raw milk, acidified, ultrafiltered and concentrated. More specifically, an acidulant, such as lactic acid, is added to reduce the pH. Other acidulants, such as a CO2 injection, can also be utilized. The pH is reduced to between 5.5 and 6.5, and more particularly reduced to between 5.7 to 6.0. Following pH adjustment, the acidified skim milk is ultra-filtrated, as is known in the art, to concentrate the acidified skim milk to 3-5-fold, more particularly to 3-4 fold, and more particularly to 3 fold.
Stream 3 is cream that has been separated from the raw milk. The fat content of the cream can be greater than 25%, however, other ranges can be utilized such as 20 - 50%, 35 - 45% and more particularly 40 - 45%.
Stream 4 is a homogenized cream stream. The fat content ranges that can be utilized include 15 - 30%, 20 - 25% and more particularly approximately 25%.
Stream 5 is water such as standard culinary type water.
The five streams can be combined in equal or differing percentages by weight or by volume to form a unified stream for pasteurization. For example, the following percentages by volume can be used:
In one example combination, the approximate percentages by volume are Stream 1 are 24-28%, Stream 2 are 27-28%, Stream 3 are 5 – 6%, Stream 4 are 7 – 9% and Stream 5 are 31-35%.
In another example combination, the percentages by volume are approximately Stream 1 25%, Stream 2 25%, Stream 3 5%, Stream 4 10% and Stream 5 35%.
After the accumulation and combination of the streams and pasteurization, the cheese make process proceeds as is known in the art. Additional lactic acid or CO2 can be added after pasteurization to bring the pH of cheese milk in the range of 5.8 – 6.35, and more specifically in the range of 5.95 – 6.10.
The results of the method shown in
Various features and advantages of the invention are set forth in the following claims.
The application claims the benefit of Provisional Application No. 63/056,821 filed Jul. 27, 2020, which is hereby incorporated by reference, and claims the benefit of Application No. 17/385,107 filed on Jul. 26, 2021, which is hereby incorporated by reference.
Number | Date | Country | |
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63056821 | Jul 2020 | US |
Number | Date | Country | |
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Parent | 17385107 | Jul 2021 | US |
Child | 18141032 | US |