IE56072B1 - A process for making portioned cheese - Google Patents

Description

The present invention relates to a process for making portioned cheese, in particular fresh unripe cheeses, such as White Cheese, Feta, Cream Cheese, Cheddar and cottage cheese.

When cheese is manufactured according to the classic method the starting material is usually cow's milk or goat’s milk, which may be homogenized. The milk may be used as whole milk, i.e. with its total solids content, or a major or minor portion of the cream may be centri10 fuged off.

The milk is coagulated by addition of rennet, and the coagulum is processed into cheese in several processing steps, comprising filtration of the separated whey, pressing in moulds end ripening or storage of the pressed cheeses. Sometimes the coagulum is also cooked and washed Instead of coagulating the milk by addition of rennet it is known to effect acidification, either by addition of a lactic acid forming bacterial culture or an inorgani acid, such as phosphoric acid, or an organic acid, e.g. lactic acid or gluconic acid. Also a neutral acidogen may be added, such as glucono-delta-lactone which releases gluconic acid by hydrolysis, cf. the US Patent Specifications 2 982 654 and 3 620 768.

Addition of acid to a pH below about 5.0 usually causes instantaneous coagulation of the proteins in the milk.

It is known to replace the whole milk or skim milk starting material in the cheese making by a milk concentrate formed by ultrafiltration or diafiltration of the milk. Such a method is disclosed in DE-A-2734825. Whole milk has a solids content of about 12%, of which about 3.5IS is protein, about 3.5« is fat and the balance is lactose, minerals and Small amounts of other substances, such as vitamins, etc. Ultrafiltration causes removal of a large portion of the water and the low-molecular substances, in particular the lactose and minerals, dissolved in the water. The retentate with a concentration of 35 to 40* solids constitutes a liquid cheese milk, which is processed into cheese in the usual manner by coagulation of the protein, recovery of the coagulum, pressing and subsequent treatment in the usual marine r .

The described method of making cheese is very timeconsuming and laborious. It is moreover uneconomical in that a considerable portion of the solids of the milk is lost, e.g. by low fermentation processes,'or occurs in by-products of low commercial value.

The object of the present invention is to provide a more rational and labour-saving process for'making portioned cheese .

Another object of the invention is to make cheeses with an improved yield, i.e. with a greater content of the original solids content of the milk.

According, the invention provides a process for making portioned cheese which comprises providing pasteurized or sterilized concentrated cheese milk having a solid content of 35-40¾ and in the form of an ultrafiltrated or diafiltrated fluid retentate, adding to said concentrated milk an adjusted amount of glucona-delta-lactona or an equivalent chemically welldefined acidogen and conventional auxiliary substances and/or additives, intimately mixing the acidogen and said substances and/or additives with oaid concentrated milk in a closed container or pipe system, introducing the mixture into individual packages the temperature and the flow conditions of the mixture in said closed container or pipe system being adjusted such that the mixture Introduced into the packages is in fluid state and the coagulation of the milk containing said acidogen and substances and/or additives begins only during or immediately after said introduction into the packages, hermetically sealing said individual packages containing the mixture and allowing the packages to stand at a suitable temperature for the contents thereof to curdle and ripen.

The making of cheese by the process of the invention is preferably continuous, there being used concentrated cheese milk, which has got the composition the finished cheese is to have by addition of common auxiliary substances and additives, such as rennet, lipase, organic acids, calcium chloride, stabilizers, emulsifiers, phosphates, citrates, salts and acidogens. While liquid, the mixture is distributed in small containers, which are closed hermetically and stored under conditions which, because of the presence of acidogen, result in coagulation and cheese formation and also ripening. However, it is possible to mix the concentrated cheese milk with the auxiliary substances and the additives portionwise, but the amount of the acidogen and the conditions of mixing are then to be so adapted that the mixture is liquid, non-coagulated or only partly coagulated when it is distributed in the individual packages .

The DE 27 34 825 and the French Patent Specification 2 '360 258 disclose a continuous process for making cheese, wherein a concentrated cheese milk is first produced, containing the usual auxiliary substances and additives and having the same composition as the finished cheese is to have. To convert this liquid product tu cheese, a particularly adapted acid-forming bacterial culture is added immediately after the liquid product is pasteurized and while it is still hot, viz. 55 to 60°C, and the product is then transferred to a container which is closed hermetically and left to stand under suitable conditions for cheese formation and ripening.

However, in this known method it is difficult to control the process and to obtain uniTorm end products because bacterial cultures often have a varying composition and activity, and because the mixing has to take place at a high temperature involving a risk of uncontrollable deterioration of the bacterial culture.

In the process of the invention, the cheese milk containing auxiliary substances and additives is expediently pumped through a closed pipe system in which the mixing with io acidogen takes place and from where the mixture is dispensed directly into the indivicusl packages.

As all additives have a well-defined composition, the process can be controlled with great accuracy. Thus, temperatures and treatment periods can be adjusted more favourably so that no coagulation or only partial coagulation will taka place before the mixture has been transferred to the individual packages. Also the fermentation reactions and ripening processes characteristic of the cheese formation take place in the package after it has been closed hermetically.

The process is very labour-saving and can be carried out without any risk of contamination. It is not necessary to add bacteriel cultures, which do not have a welldefined composition and euhose effect is difficult to control. The use of a chemically well-defined acidogen permits a precise pH adjustment to be maintained so that the curdling and ripening processes proceed uniformly and at a constant rate during the continuous process.

The preferred acidogen is glucono-delta-lactone, but it is also possible to use another chemical compound with corresponding properties, such as those described in the US Patent Specification 3 620 768.

$ The finished cheese product has retained the original composition of the milk solids essentially unchanged. There is no conversion of the lactose contained in the milk. The yield is therefore high in relation to milk solids.

The cheese milk used as the starting material is expediently formed by ultrafiltration or diafiltration Hhich gives a liquid concentrate with a high content of protein.

The additives, including the acidogen, are expediently introduced continuously by metering means in the pipe system for mixing with the cheese milk. Thus, the acidogen can be introduced in the concentrated cheese milk in the form of a dry powder by means of a screw or a worm metering device, from which the atmospheric air has been expelled by means of gaseous carbon dioxide. This obviates the necessity of suspending or dissolving the acidogen in water with consequent dilution of the cheese milk and of introducing air into the cheese, which 2o might cause bubbles or holes.

The process of the invention mill be explained more fully bel otia by means of some working examples.

EXAMPLE 1 Milk faith a pH of 6.7 and about 12% solids, about 3.4% protein and about 3.5% fat is heated to 98°C for 15 seconds. Then it is cooled to 60°C and homogenized at a pressure of 18.6 x 10& Pa, cooled to 8°C and mixed with an 0.15% starter distillate through a static in-line mixer for immediate reduction of pH to 6.10.

The mixture is allowed to rest for 0.5 to 8 hours.

The acidified milk io heated to 51°C and ultrafiltrated to provide a retentate with 38% solids.

The retentate is mixed with an 0.1% emulsifier stabilizer and is homogenized at 5.88 x 10θ Pa and heated to 9S°C for seconds and cooled to 28°C.

An 0,1% cold water mixture containing 40 parts of water, 1/2 part of rennet and 1/2 part of citrate (1:40), a 4% cold tester mixture containing 1 part of water, 1 pert of glucono-delta-lactone (1:1) and a 7% hot faster mixture with 1 part of water, 1 part of salt (1:1) are added to the retentate in a static in-line mixer.

The mixture in liquid shape is immediately dispensed into individual plastics cups or other Individual packages The package is sealed hermetically and left to stand at room temperature until the cheese hss developed into a cuttabla or spreadable type by renneting, acidification, coagulation and ripening.

EXAMPLE 2 Hilk with a pH of 6.7, about 12% solids, about 3.4% protein and about 3.5% fat is mixed with 13% butter and/or vegetable fat and 13% caseinate, is heated to $8°C for 15 seconds, cooled to 60°C and homogenized at a pressure of 18.6 x 10b Pa and cooled to 12°C, and 0.25% organic nutritional acid is added through a static in-line mixer for immediate reduction of pH to 5.2Q.

The mixture is allowed to rest for 0.5 to 8 hours. The acidified concentrate is heated to 31°C. A 4% cold weter mixture containing 1 part of tiater, 1 part of gluconodelta-lectone, an 0.1% cold water mixture containing 40 parts of water, 1/2 part of rennet and 1/2 part of lipase and a 3% cold water mixture containing 1 part of I water end 1 part of salt are added to the concentrate through a static in-line mixer. lhe mixture is immediately dispensed in a liquid or partially coagulated form into plastics cups or other packages and is closed hermetically. The packaged product is left to stand until renneting, acidification, coagulation and ripening of the cheese is completed in the package.

EXAMPLE 3 10 Example 1 is repeated with the change that the starting material is reconstituted milk, made of 12 parts of milk solids which are dissolved in 68 parts of water and emulsified together with 13% butter, based on the weight of the finished mixture. This gives a spreadable cream cheese.

EXAMPLE 4 Example 1 is repeated ftith the change that the additives, i.e. rennet, citrate, glucono-delta-lactone and salt, are mixed-in a dry state and introduced into the pipe system for mixing with the cheese milk by means of a worm metering device, from which the atmospheric air has been removed by flushing with gaseous carbon dioxide.

EXAMPLE 5 The procedure described in example 1 is repeated with the change that the starting material is skim milk which is subjected to diafiltration.

The cheese product obtained is of the same type as a cottage cheese.

EXAMPLE 6 Milk with a pH of about 6.5 and about 12% solids, about 3,4% protein and about 3,5% fat is heated to about 98°C for 15 seconds. Then it is cooled to about 60°C and homogenized at a pressure of about 18.6 x 10® Pa, cooled to about 55°C and ultrafiltrated to provide a retentate with about 38% solids.

The retentate is homogenized at about 5.88 x 10θ Pa and is heated to 90°C for about 15 seconds and cooled to about 28°C. Salt in a dry state is mixed with the retentate» and 40 parts of water, 1/2 part of rennet and 20 parts of glucono-delta-lactone are added to the retentate.

The mixture is immediately dispensed in a liquid form into individual packages which are closed hermetically.

The packaged product is left to stand until renneting, acidification and coagulation is completed, end is then left for curing at ebout 5°C.

The produced cheese is of the Feta type and has the composition: Component Content in g Content in g per Method of per kg of cheese kg of solids analysis Mater/solids 625/375 0/1000 AOAC Fat 160 427 AOAC Protein (Nx6.37) 119 317 AACC Salt 36,9 98.4 AOAC Glucono-deltalactone (GDL) 20,5 54.4 SLT Ashes (excl. salt) 9,2 24.5 AOAC Phosphor 2.4 6.4 NMK Carbohydrate 29 77

Claims (6)

CIAIMSs

1. a process for making portioned cheese which comprises providing pasteurised or sterilised concentrated cheese milk having a solid content of 35-40% and in the form of an ultrafiltrated or diafiltrated fluid retentate, adding to said concentrated milk an adjusted amount of glucona^deltalactone or an equivalent chemically well-defined acidogen and conventional auxiliary substances and/or additives, intimately mixing the acidogen and said substances and/or additives with said concentrated milk in a closed container or pipe system, introducing the mixture into individual packages the temperature and the flow conditions of the mixture in said closed container or pipe system being adjusted such that the mixture introduced into the packages is in fluid state and the coagulation of the milk containing said acidogen and substances and/or additives begins only during or immediately after said introduction into the packages, hermetically sealing said individual packages containing the mixture and allowing the packages to stand at a suitable temperature for the contents thereof to curdle and ripen.

2. A process according to claim 1, wherein the acidogen and the auxiliary substances and/or additives are introduced into the concentrated cheese milk in the pipe system in the form of an aqueous suspension.

3. A process according to claim 1, wherein the acidogen and the other additives are introduced into the concentrated cheese milk in the pipe system in the form of a dry powder. .11 4. «,

4. A process for staking portioned cheese, substantially as hereinbefore described with particular reference to the Examples 1, 3, 3, 5 and 6, and Example

5. 5. Portioned cheese whenever made by a process claimed in a preceding claim. F. R« KELLY

6. CO., AGENTS FOR THE APPLICANTS