IE920086A1 - Process for making a vegetable fat cream and cheese product therefrom - Google Patents
Process for making a vegetable fat cream and cheese product therefromInfo
- Publication number
- IE920086A1 IE920086A1 IE920086A IE920086A IE920086A1 IE 920086 A1 IE920086 A1 IE 920086A1 IE 920086 A IE920086 A IE 920086A IE 920086 A IE920086 A IE 920086A IE 920086 A1 IE920086 A1 IE 920086A1
- Authority
- IE
- Ireland
- Prior art keywords
- curd
- vegetable fat
- fatty acids
- milk
- fat
- Prior art date
Links
- 235000019871 vegetable fat Nutrition 0.000 title claims abstract description 73
- 235000013351 cheese Nutrition 0.000 title claims abstract description 68
- 238000000034 method Methods 0.000 title claims abstract description 56
- 239000006071 cream Substances 0.000 title claims abstract description 55
- 235000013336 milk Nutrition 0.000 claims abstract description 50
- 239000008267 milk Substances 0.000 claims abstract description 50
- 210000004080 milk Anatomy 0.000 claims abstract description 50
- 239000005862 Whey Substances 0.000 claims abstract description 31
- 102000007544 Whey Proteins Human genes 0.000 claims abstract description 31
- 108010046377 Whey Proteins Proteins 0.000 claims abstract description 31
- 239000000203 mixture Substances 0.000 claims abstract description 17
- 235000021122 unsaturated fatty acids Nutrition 0.000 claims abstract description 11
- 150000004670 unsaturated fatty acids Chemical class 0.000 claims abstract description 11
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 34
- 150000004671 saturated fatty acids Chemical class 0.000 claims description 26
- 239000003925 fat Substances 0.000 claims description 21
- 235000019197 fats Nutrition 0.000 claims description 21
- 235000003441 saturated fatty acids Nutrition 0.000 claims description 21
- 235000021281 monounsaturated fatty acids Nutrition 0.000 claims description 20
- 235000021243 milk fat Nutrition 0.000 claims description 19
- 239000003921 oil Substances 0.000 claims description 19
- 235000019198 oils Nutrition 0.000 claims description 19
- 239000004310 lactic acid Substances 0.000 claims description 17
- 235000014655 lactic acid Nutrition 0.000 claims description 17
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 claims description 17
- 235000020183 skimmed milk Nutrition 0.000 claims description 17
- 239000007858 starting material Substances 0.000 claims description 12
- 235000020238 sunflower seed Nutrition 0.000 claims description 11
- 235000019484 Rapeseed oil Nutrition 0.000 claims description 9
- 238000003825 pressing Methods 0.000 claims description 8
- 238000010411 cooking Methods 0.000 claims description 7
- 230000005070 ripening Effects 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 6
- 235000008939 whole milk Nutrition 0.000 claims description 6
- 239000004006 olive oil Substances 0.000 claims description 5
- 235000008390 olive oil Nutrition 0.000 claims description 5
- 238000009938 salting Methods 0.000 claims description 5
- 108090000790 Enzymes Proteins 0.000 claims description 4
- 102000004190 Enzymes Human genes 0.000 claims description 4
- 230000001112 coagulating effect Effects 0.000 claims description 4
- 238000005520 cutting process Methods 0.000 claims description 3
- 235000010469 Glycine max Nutrition 0.000 claims description 2
- 244000068988 Glycine max Species 0.000 claims description 2
- 235000012343 cottonseed oil Nutrition 0.000 claims description 2
- 239000002385 cottonseed oil Substances 0.000 claims description 2
- 238000003801 milling Methods 0.000 claims description 2
- 239000003813 safflower oil Substances 0.000 claims description 2
- 235000019483 Peanut oil Nutrition 0.000 claims 1
- 235000019486 Sunflower oil Nutrition 0.000 claims 1
- 235000005687 corn oil Nutrition 0.000 claims 1
- 239000000312 peanut oil Substances 0.000 claims 1
- 239000002600 sunflower oil Substances 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 235000011617 hard cheese Nutrition 0.000 abstract description 8
- 235000021081 unsaturated fats Nutrition 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 239000000796 flavoring agent Substances 0.000 description 7
- 235000019634 flavors Nutrition 0.000 description 7
- 229940108461 rennet Drugs 0.000 description 7
- 108010058314 rennet Proteins 0.000 description 7
- 235000013311 vegetables Nutrition 0.000 description 7
- OENHQHLEOONYIE-UKMVMLAPSA-N all-trans beta-carotene Natural products CC=1CCCC(C)(C)C=1/C=C/C(/C)=C/C=C/C(/C)=C/C=C/C=C(C)C=CC=C(C)C=CC1=C(C)CCCC1(C)C OENHQHLEOONYIE-UKMVMLAPSA-N 0.000 description 6
- 235000013734 beta-carotene Nutrition 0.000 description 6
- TUPZEYHYWIEDIH-WAIFQNFQSA-N beta-carotene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1=C(C)CCCC1(C)C)C=CC=C(/C)C=CC2=CCCCC2(C)C TUPZEYHYWIEDIH-WAIFQNFQSA-N 0.000 description 6
- 239000011648 beta-carotene Substances 0.000 description 6
- 229960002747 betacarotene Drugs 0.000 description 6
- 244000309466 calf Species 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- OENHQHLEOONYIE-JLTXGRSLSA-N β-Carotene Chemical compound CC=1CCCC(C)(C)C=1\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C OENHQHLEOONYIE-JLTXGRSLSA-N 0.000 description 6
- 235000009508 confectionery Nutrition 0.000 description 5
- 235000005911 diet Nutrition 0.000 description 4
- 230000037213 diet Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 244000105624 Arachis hypogaea Species 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 3
- 235000013365 dairy product Nutrition 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 235000010777 Arachis hypogaea Nutrition 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- 108091005804 Peptidases Proteins 0.000 description 2
- 102000035195 Peptidases Human genes 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 208000029078 coronary artery disease Diseases 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- 229940088598 enzyme Drugs 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 229940024999 proteolytic enzymes for treatment of wounds and ulcers Drugs 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 1
- 235000003276 Apios tuberosa Nutrition 0.000 description 1
- 235000003911 Arachis Nutrition 0.000 description 1
- 235000017060 Arachis glabrata Nutrition 0.000 description 1
- 235000018262 Arachis monticola Nutrition 0.000 description 1
- 235000010744 Arachis villosulicarpa Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 description 1
- 235000019463 artificial additive Nutrition 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000416 hydrocolloid Substances 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 235000009973 maize Nutrition 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 235000020200 pasteurised milk Nutrition 0.000 description 1
- 235000020232 peanut Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C21/00—Whey; Whey preparations
- A23C21/04—Whey; Whey preparations containing non-milk components as source of fats or proteins
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C11/00—Milk substitutes, e.g. coffee whitener compositions
- A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
- A23C11/04—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing non-milk fats but no non-milk proteins
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C19/00—Cheese; Cheese preparations; Making thereof
- A23C19/02—Making cheese curd
- A23C19/055—Addition of non-milk fats or non-milk proteins, polyol fatty acid polyesters or mineral oils
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Dairy Products (AREA)
Abstract
A process is provided for producing a vegetable fat cream and a cheese product therefrom. The process comprises forming a mixture of vegetable fat and whey in a weight ratio of 1:1.5 to 1:9, wherein the vegetable fat comprises by weight at least 70% unsaturated fatty acids. The mixture is blended to form an artificial cream and the artificial cream is homogenised at a pressure of 500 to 1500 psi and at a temperature of 50 to 55 DEG C. The vegetable fat cream thus produced may be mixed with milk to form a filled milk and a cheese product prepared therefrom. Hard cheese products resembling Cheddar Cheese may be thus produced having a high unsaturated fat content and relatively low total fat content.
Description
This invention relates to a process for preparing a vegetable fat cream which is high in unsaturated fatty acids, and the vegetable fat cream prepared by such a process. The invention further relates to a process for using this vegetable fat cream to prepare a hard cheese product resembling Cheddar Cheese, but which contains vegetable fat which is high in unsaturated fatty acids, wholly or partially in place of milk fat, and which may also contain a lower total fat content than a traditional Cheddar Cheese, and the cheese product made by such a process.
Throughout this specification the term vegetable fat is used to include both solid vegetable fats and liquid vegetable oils.
One reason for wishing to substituting vegetable fat for milk fat in cheese is that milk fat is high in saturated fatty acids. Medical experts have for many years warned that a diet high in fat, and particularly a diet high in saturated fatty acids, is a risk factor for coronary heart disease, and that fat intake, and particularly saturated fatty acid intake, should be reduced. One way to do this is to reduce the total fat content of foods that contain a high proportion of saturated fatty acids. Another way is to substitute vegetable fats low in saturated fatty acids for fats high in saturated fatty acids, such as milk fat . Many medical experts believe that the polyunsaturated fatty acid content of the diet should be increased, as this might have a protective effect against coronary heart disease. More recently the view has been put forward that an increase in the monounsaturated fatty acid content of the diet might have a similar or even better protective effect.
Substituting the milk fat in dairy products such as cheese by vegetable fats high in unsaturated fatty acids (polyunsaturated or monounsaturated or both) thus has the double effect of reducing saturated fatty acid intake and raising unsaturated fatty acid intake, whereas reducing the total fat content of dairy products such as cheese only has the single effect of lowering saturated fatty acid intake.
A process for preparing a semi-hard to hard cheese product is disclosed in GB 2214776A. This process inherently suffers from a disadvantage that replacement of milk fat by fat rich in unsaturated fatty acids results in a cheese product having a poor cheese flavour. In order to overcome this disadvantage, GB 2214776A uses cheese flavour concentrates which are added during the cheese making process. Only with the use of these added cheese flavour concentrates is an acceptable favour produced in the cheese product.
In other known processes preparation of a vegetable fat cream or a filled milk from skimmed milk and vegetable fat is disclosed for use in making a cheese product. However, in these processes it is often necessary to use an emulsifier such as a lecithin or mono- and diglycerides and/or a stabiliser such as a hydrocolloid as part of the processes (e.g. GB 2223927A). Clearly, the need to use these additives is undesirable because it results in additional processing steps and expense. Furthermore, owing to the consumers' trend away from products containing additives, dairy products containing few additives are more commercially acceptable.
The present invention provides a process for producing a vegetable fat cream, which process comprises:
forming a mixture of vegetable fat and whey in a weight ratio of 1:1.5 to 1:9, wherein the vegetable fat comprises by weight at least 70% unsaturated fatty acids;
blending the mixture to form an artificial cream; and homogenising the artificial cream.
There is also provided a process for producing a cheese product, which process comprises:
making a vegetable fat cream as described above; mixing the vegetable fat cream with milk to form a filled milk;
and preparing a cheese product therefrom.
Thus, the cheese product produced in accordance with the present invention has a good flavour resembling that of a normal mild Cheddar cheese without the use of undesirable cheese flavour concentrates or artificial additives such as emulsifiers and stabilisers.
In the process of producing the vegetable fat cream, the whey used may be natural whey or a reconstituted whey solution. Typically, the whey is sweet cheese whey or a reconstituted solution of 7 - 10% by weight of whey powder or of demineralised whey powder. Preferably, the weight ratio of vegetable fat to whey is in the range 1:2 to 1:2.5, more preferably 1:2.33.
The artificial cream formed by blending the mixture of vegetable fat and whey typically has a 10 - 40% fat content. Preferably, the fat content is in the range 28.5 to 33.3%, more preferably about 30%.
The step of homogenising the artificial cream is preferably effected at a pressure of 500 - 1500 psi and at a temperature of 50 to 55°C. More preferably, the pressure is about 750 psi.
Typically, the vegetable fat is selected from fats which are high in monounsaturated fatty acids, fats which are high in polyunsaturated fatty acids or mixtures thereof. The vegetable fat may therefore be selected according to the type of cheese product required to be produced from the vegetable fat cream.
The vegetable fat cream may be used in the process of making a cheese product as described above. The process does not use a conventional method of Cheddar cheese making but uses instead, either a method resembling that used for the manufacture of American Washed Curd Cheese or a modified method of Cheddar Cheese manufacture.
Nevertheless, the cheese product made according to the present invention resembles a mild Cheddar cheese in both taste and texture.
A hard cheese product may be produced in which the milk fat is replaced by one or more vegetable fats and which comprises by weight at least 70% of the fat as unsaturated fatty acids. Alternatively, a hard cheese product may be produced in which the milk fat is partially replaced by one or more vegetable fats and which comprises by weight at least 60% of the fat as unsaturated fatty acids.
The milk mixed with the vegetable fat cream is preferably pasteurised milk and may be skimmed milk or a mixture of skimmed milk and whole milk depending on the amount of milk fat required in the filled milk. Typically, a filled milk of 1 - 4% fat content is formed, preferably 2.3 - 2.5 % fat content. The skimmed milk used is typically a normal skimmed milk containing less than 0.1% milk fat.
Preferably the process for making the cheese product further comprises ripening the filled milk in the presence of a starter culture; and adding a coagulating enzyme to form a coagulum.
The starter culture used to ripen the filled milk may be of the mesophilic or thermophilic type as generally used in cheese making. The coagulating enzyme is typically added in the form of rennet and may be of animal, vegetable or microbial origin. Optionally, at the stage of coagulation or ripening, colouring matter suitable for use in cheese making may be added to the filled milk in order to impart an acceptable colouring to the cheese product. Proteolytic enzymes commonly used for enhancing cheese flavour may also be added at the stage of ripening.
Once a coagulum has formed, the coagulated curd is preferably cut into pieces of curd. The pieces of curd are preferably cut over 5 to 10 minutes and are approximately 1/2 inch cubes. Optionally, calcium chloride may be added before cutting the coagulum in amounts normally used in cheese making in order to aid the coagulation process.
Preferably, the curd is scalded to 35 - 48°C over 15 minutes, more preferably to 40°C over 30 minutes. The scalded curd is then cooked at 35 - 48°C for 15 to 19 minutes. The time and temperature chosen for the scalding and cooking of the curd generally depends on the type of starter culture used for the cheese making. A high temperature and longer time for scalding and cooking would generally only be used with a thermophilic starter culture.
After cooking the curd, typically one of two processes may be used to separate the curd. The curd may be drained after cooking and allowed to Cheddar, followed by milling and salting to an acidity of 0.42 to 0.65% lactic acid. Alternatively, the curd may be washed in water to bring the temperature to 28 - 32°C, preferably to 30°C, followed by pitching the curd. The curd is then left, with or without dry stirring, until the acidity reaches 0.2 - 0.6% lactic acid, preferably 0.3% lactic acid, followed by salting. At this stage, proteolytic enzymes may also be added.
Once the curd has been brought to the correct acidity, it is filled into moulds, pressed and then ripened to form a final cheese product at 7 - 12°C, preferably about 8°C.
To make a cheese product high in monounsaturated fatty acids, a vegetable fat preferably containing at least 55% by weight of monounsaturated fatty acids and 5-25% by weight of saturated fatty acids is used. Examples of such vegetable fats are olive oil, rapeseed oil, peanut (groundnut or arachis) oil, high monounsaturated fatty acid sunflowerseed oil (Trisun) and hydrogenated non-lauric vegetable fat. Preferably the vegetable fat is a hydrogenated rapeseed oil containing 77.5 - 82.5% by weight of monounsaturated fatty acids and 15 - 20% by weight of saturated fatty acids.
To make a cheese product high in polyunsaturated fatty acids, a vegetable fat preferably containing at least 45% by weight of polyunsaturated fatty acids and 7.5 - 25% by weight of saturated fatty acids is used. Examples of such vegetable fats are sunflowerseed oil, safflowerseed oil, soyabean oil, cottonseed oil, and maize (corn) oil. Preferably the vegetable fat is a sunflowerseed oil containing at least 55% by weight of polyunsaturated fatty acids and less than 15% by weight of saturated fatty acids.
Alternatively, the vegetable fat cream may be used to make a cheese product containing raised levels of both polyunsaturated and monounsaturated fatty acids but a low level of saturated fatty acids. In this case the vegetable fat cream is made from a mixture of one or more vegetable fats high in polyunsaturated fatty acids and one or more vegetable fats high in monounsaturated fatty acids, the ratios of the different vegetable fats used depending on the desired ratio of polyunsaturated fatty acids to monounsaturated fatty acids in the vegetable fat cream.
The saturated fatty acid content of the mixture of vegetable fats will remain at less than 25%.
As a further alternative, the vegetable fat cream may be used to make a cheese product in which only part of the milk fat is replaced by the vegetable fat cream, for example a cheese product in which the fat content consists of 75% of vegetable fat and 25% of milkfat, or of 50% of vegetable fat and 50% of milkfat. Preferably the fat content of the cheese product consists of 45-55% sunflowerseed oil and 45-55% milk fat. The inclusion of the milk fat in the cheese product means that the proportion of saturated fatty acids in the fat content of the cheese product will be raised and that of unsaturated fatty acids will be lowered. In this case the vegetable fat cream is made as above, but it is blended with a mixture of pasteurised skimmed milk and pasteurised whole milk, the ratios of the amounts of vegetable fat cream, skimmed milk and whole milk being such that a partially filled milk of 1.0 - 4.0% fat content, preferably 2.3 2.5% fat content, is obtained containing the required ratio of vegetable fat to milk fat.
The hard cheese product made according to the invention does not have to resemble a conventional hard cheese, but may be one containing a lower fat content than normal, for example one containing a fat content of around 15%. In this case the fat content of the filled or partially filled milk formed preferably has a fat content of 1.2 - 1.4% fat. Such a reduced fat hard cheese product may have any one of the fat compositions outlined above.
In an alternative embodiment, the vegetable fat cream may be diluted in two stages, firstly to form an intermediate artificial cream and secondly to form the filled milk. The intermediate artificial cream may have a fat content of 5 - 20%, preferably 8 - 16.5%, and more preferably 12%.
The invention will now be described further by way of example only with reference to the following Examples.
EXAMPLES A : PREPARATION OF VEGETABLE FAT CREAM
Example Al
239kg of a hydrogenated rapeseed oil (CONFAO 5 ex-Aarhus Olie) were placed in a melting tank and heated to 60°C. 37kg of sweet edible spray dried whey powder were added to 470L of water at a minimum temperature of 60°C in a heating tank and mixed for 10 minutes. The heated oil was added to the whey powder solution and mixed for a further 10 minutes to form an artificial cream of 32% fat content.
This artificial cream was homogenized at 750psi at a temperature of 55°C using a single stage homogenizer.
Example A2
50kg of Trisun high monounsaturated fatty acid sunflowerseed oil were placed in a melting tank and heated to 60°C. 30kg of sweet edible spray dried whey powder were added to 410L of water to a minimum temperature of 60°C in a heating tank and mixed for 10 minutes using a Silverson high speed mixer. The heated oil was added to the whey powder solution and mixed for 10 minutes using the Silverson mixer, to form an artificial cream of 12% fat content.
The artificial cream was homogenized at 750psi at a temperature of 50°C using a single stage homogenizer.
Example A3
90kg of olive oil were placed in a melting tank and heated to 60°C. 30kg of sweet edible spray dried whey powder were added to 410L of water at a minimum temperature of 60°C in a heating tank and mixed for 10 minutes using a Silverson high speed mixer. The heated oil was added to the whey powder solution and mixed for 10 minutes using the Silverson mixer, to form an artificial cream of 17% fat content.
The artificial cream was homogenized at 750psi at a temperature of 55°C using a single stage homogenizer.
Example A4
The procedure and ingredients of Example Al were used except that 239 kg of olive oil were used in place of the hydrogenated rapeseed oil.
Example A5
The procedure and ingredients of Example Al were used except that 239 kg of Trisun high monounsaturated fatty acid sunflowerseed oil were used in place of the hydrogenated rapeseed oil.
Example A6
239kg of a hydrogenated rapeseed oil (CONFAO 5 ex-Aarhus Olie) were placed in a melting tank and heated to 60°C. 37kg of sweet edible spray dried whey powder were added to 470L of water at a minimum temperature of 60°C in a heating tank and mixed for 10 minutes using a
Silverson high speed mixer. The heated oil was added to the whey powder solution and mixed for 10 minutes using the Silverson mixer, to form an artificial cream of 32% fat content.
This artificial cream was homogenized at 750psi at a temperature of 55°C using a single stage homogenizer and was pumped into a mixing tank containing 1322L of pasteurised skimmed milk at 50°C. The artificial cream and the skimmed milk were mixed for 10 minutes using a Silverson mixer to form an intermediate artificial cream of 11.5% fat content.
Example A7
The procedure and ingredients of Example Al were used except that 239 kg of sunflowerseed oil were used in place of the hydrogenated rapeseed oil.
EXAMPLES B : PREPARATION OF VEGETABLE FAT CHEESE PRODUCT
Example BI
746L of the artificial cream of Example Al were added to 9253L of pasteurised skimmed milk in a cheese vat and stirred for 5 minutes to make a filled milk of 2.4% fat content. The temperature of the filled milk was maintained at 33°C. 0.58kg of β-carotene powder was dissolved in
10kg of hot water and added to the vat and stirred for 5 minutes, then 1.7L of calcium chloride solution was added. 200 units of Eurozyme DVI mesophilic starter were added to the filled milk, which was allowed to ripen for 60 minutes.
When acidity reached 0.19% lactic acid, 2.48L of calf rennet were added, and the ripened filled milk was stirred for 5 minutes and allowed to coagulate for 60 minutes.
When ready the curd was cut to a size of half an inch over a period of 8 minutes. The curd was then scalded to 38°C over 30 minutes, and stirred for 50 minutes. Pasteurized cold water was added to the vat until the temperature reached 30°C, when it was stirred for 10 minutes.
The curd was then pitched onto the DMC belt and the whey was drained. When the acidity of the curd reached 0.3% lactic acid, it was salted with 25kg salt. The curd was then filled into cheese moulds and pressed at low pressure (3psi) for 25 minutes, at medium pressure (9psi) for 25 minutes, and at high pressure (18psi) for 30 minutes, under an 80% absolute vacuum. After pressing the 20kg blocks were bagged, vacuum packed, slatted and stored at 8°C for 4 weeks, when the cheese product was graded.
The cheese product made by this method had a fat content of 24.8%, comprising monosaturated fatty acids 19.4%, saturated fatty acids 4.4% and polyunsaturated fatty acids 0.3%. All the fat was of vegetable origin.
Example B2
490L of the artificial cream of Example A2 were added to 8000L of pasteurised skimmed milk and 1510L of pasteurised whole milk in a cheese vat and stirred for 5 minutes to make a filled milk of 1.25% fat content. The temperature of the filled milk was maintained at 33°C. 0.58kg of beta-carotene powder was dissolved in 10kg of hot water and added to the fat and stirred for 5 minutes. 200 units of Eurozyme DVI mesophilic starter were added to the filled milk, which was allowed to ripen for 85 minutes.
When the acidity reached 0.18% lactic acid, 2.48L of calf rennet were added, and the ripened filled milk was stirred for 5 minutes and allowed to coagulate for 70 minutes. When ready the curd was cut into a size of 1/2 inch and allowed to stand for a period of 10 minutes. The curd was then scalded to 35°C over 15 minutes, and stirred for 10 minutes.
The curd was then pitched to the Tebel Crockatt apparatus, the whey was drained and the curd was channeled and milled as in Cheddar manufacture. When the acidity of the curd reached 0.42% lactic acid, it was salted with 25kg salt. The curd was fed into a large hoop press and pressed at low pressure (700psi) for 10 minutes under a vacuum of 25 inches Hg and for 10 minutes without vacuum, then at high pressure (1200psi) for 4 hours. After pressing the curd was cut into 20kg blocks, bagged and stored at 8°C for 4 weeks, when it was graded.
The cheese product made by this method had a fat content of 15%, comprising monounsaturated fatty acids 8.2%, saturated fatty acids 5.3% and polyunsaturated fatty acids 1.0%. 50% of the fat was of vegetable origin (Trisun sunflowerseed oil) and 50% was milk fat. The cheese had a very good mild Cheddar flavour.
Example B3
530L of the artificial cream of Example A3 were added to 8660L of pasteurised skimmed milk and 820L of pasteurised whole milk in a cheese vat and stirred for 5 minutes to make a filled milk of 1.3% fat content. The temperature of the filled milk was maintained at 33°C. 0.58kg of beta-carotene powder was dissolved in 10kg of hot water and added to the vat and stirred for 5 minutes. 200 units of Eurozyme DVI mesophilic starter were added to the filled milk, which was allowed to ripen for 85 minutes.
When the acidity reached 0.18% lactic acid, 2.48L of calf rennet were added, and the ripened filled milk was stirred for 5 minutes and allowed to coagulate for 70 minutes.
When ready the curd was cut to a size of 1/2 inch and allowed to stand for 5 minutes. The curd was then scalded to 35°C over 15 minutes, and stirred until the acidity had risen by 0.02%. The whey was then drained until the curd showed, when it was stirred until the acidity reached 0.16 - 0.18%. Pasteurised cold water at 12°C was added to the vat until the temperature reached 30°C, when it was stirred for 5 minutes.
The curd was then pitched, the whey was drained and the curd was cheddared. When the acidity of the curd reached 0.3% lactic acid, it was salted with 25kg salt.
The curd was fed into a large hoop press and pressed at low pressure (700psi) for 10 minutes under a vacuum of 25 inches Hg and for 10 minutes without vacuum, then at high pressure (1200psi) for 4 hours. After pressing the curd was cut into 20kg blocks, bagged and stored at 8°C for 4 weeks, when it was graded.
The cheese product made by this method had a fat content of 15%, comprising monounsaturated fatty acids 8.8%, saturated fatty acids 3.9% and polyunsaturated fatty acids 1.8%. 75% of the fat was of vegetable origin (olive oil) and 25% was milk fat.
Example B4
2069L of the intermediate artificial cream of Example A6 were added to 7931L of pasteurised skimmed milk in a cheese vat and stirred for 5 minutes to make a filled milk of 2.4% fat content. The temperature of the filled milk was maintained at 33°C. 0.58kg of beta-carotene powder was dissolved in 10kg of hot water and added to the vat and stirred for 5 minutes. 200 units of Eurozyme DVS thermophilic starter were added to the filled milk, which was allowed to ripen for 60 minutes.
When the acidity reached 0.19% lactic acid, 2.48L of calf rennet were added, and the ripened filled milk was stirred for 5 minutes and allowed to coagulate for 60 minutes. When ready the curd was cut to a size of 1/2 inch over a period of 8 minutes. The curd was then scalded to 47°C over 60 minutes, and stirred to 30 minutes after which it was allowed to settle for 15 minutes. The whey was then drained to the top of the curd, which was stirred for 5 minutes before the remainder of the whey was drained. The curd was then allowed to Cheddar. After cheddaring, the curd was milled, followed by salting with 25kg salt when the acidity reached 0.5 -0.6% lactic acid. The curd was then fed into a large hoop press and pressed at low pressure (700psi) for 10 minutes under a vacuum of 25 inches Hg and for 10 minutes without vacuum, then at high pressure (1200psi) for 4 hours. After pressing the curd was cut into 25kg blocks, bagged and stored at 8°C for 4 weeks, when it was graded.
The cheese product made by this method had a fat content of 24.8%, comprising polyunsaturated fatty acids 16.6%, monounsaturated fatty acids 4.9% and saturated fatty acids 2.6%. All the fat was of vegetable origin.
Example B5
1241L of the intermediate artificial cream of Example A5 were added to 8759L of pasteurised skimmed milk in a cheese vat and stirred for 5 minutes to make a filled milk of 1.36% fat content. The temperature of the filled milk was maintained at 33°C. 0.58kg of beta-carotene powder was dissolved in 10kg of hot water and added to the vat and stirred for 5 minutes. 200 units of Eurozyme DVI mesophilic starter were added to the filled milk, which was allowed to ripen for 85 minutes.
When the acidity reached 0.18% lactic acid, 2.48L of calf rennet were added, and the ripened filled milk was stirred for 5 minutes and allowed to coagulate for 70 minutes. When ready the curd was cut to a size of 1/2 inch and allowed to stand for 10 minutes. The curd was then scalded to 35°C over 15 minutes and stirred for 10 minutes. The whey was then drained until the curd showed, when pasteurised water at 25°C was added to the vat up to the original level of the whey.
After stirring for 20 minutes, the curd was pitched, the whey was drained and the curd was channeled. When the acidity of the curd reached 0.4% lactic acid, it was salted with 25kg salt. The curd was fed into a large hoop press and pressed at low pressure (700psi) for 10 minutes under a vacuum of 25 inches Hg and for 10 minutes without vacuum, then at high pressure (1200psi) for 4 hours. After pressing the curd was cut into 25kg blocks, bagged and stored at 8°C for 4 weeks, when it was graded.
The cheese product made by this method had a fat content of 16%, comprising monounsaturated fatty acids 12.4%, polyunsaturated fatty acids 1.6% and saturated fatty acids 1.6%. All of the fat was of vegetable origin.
Example B6
2069L of the intermediate artificial cream of Example A6 were added to 7931L of pasteurised skimmed milk in a cheese vat and stirred for 5 minutes to make a filled milk of 2.4% fat content. The temperature of the filled milk was maintained at 33°C. 0.58kg of beta-carotene powder was dissolved in 10kg of hot water and added to the vat and stirred for 5 minutes. 200 units of Eurozyme DVI mesophilic starter were added to the filled milk, which was allowed to ripen for 60 minutes.
When the acidity reached 0.19% lactic acid, 2.48L of calf rennet were added, and the ripened filled milk was stirred for 5 minutes and allowed to coagulate for 70 minutes. When ready the curd was cut into a size of 1/2 inch over a period of 8 minutes. The curd was then scalded to 39.9°C over 30 minutes, and stirred for 60 minutes. Pasteurised cold water was added to the vat until the temperature reached 30°C, when it was stirred for 10 minutes.
The curd was then pitched to the Tebel Crockatt apparatus, the whey was drained and the curd was stirred as in Cheddar manufacture. When the acidity of the curd reached 0.3% lactic acid, it was salted with 25kg salt.
The curd was fed into a large hoop press and pressed at low pressure (700psi) for 10 minutes under a vacuum of 25 inches Hg and for 10 minutes without vacuum, then at high pressure (1200psi) for 4 hours. After pressing the curd was cut into 20kg blocks, bagged and stored at 8°C for 4 weeks, when it was graded.
The cheese product made by this method had a fat content of 24.8%, comprising monounsaturated fatty acids 19.4%, saturated fatty acids 4.4% and polyunsaturated fatty acids 0.3%. All the fat was of vegetable origin.
Claims (22)
1. A process for producing a vegetable fat cream, which process comprises: forming a mixture of vegetable fat and whey in a weight ratio of 1:1.5 to 1:9, wherein the vegetable fat comprises by weight at least 70% unsaturated fatty acids; blending the mixture to form an artificial cream; and homogenising the artificial cream at a pressure of 500 to 1500 psi and at a temperature of 50 to 55°C.
2. A process a claimed in claim 1, wherein the weight ratio of vegetable fat to whey is 1:2 to 1:2.5.
3. A process as claimed in claim 1 or claim 2, wherein the vegetable fat comprises by weight at least 55% monounsaturated fatty acids and 5 to 25% saturated fatty acids.
4. A process as claimed in claim 3, wherein the vegetable fat is selected from olive oil, rapeseed oil, peanut oil, high monounsaturated fatty acid sunflower oil and hydrogenated non-lauric vegetable fat, or a mixture thereof
5. A process as claimed in claim 4, wherein the vegetable fat is a hydrogenated rapeseed oil comprising by weight 77.5 to 82.5% monounsaturated fatty acids and 15 to 20% saturated fatty acids.
6. A process as claimed in claim 1 of claim 2, wherein the vegetable fat comprises by weight at least 45% polyunsaturated fatty acids and 7.5 to 25% saturated fatty acids.
7. A process as claimed in claim 6, wherein the vegetable fat is selected from sunflowerseed oil, safflowerseed oil, soyabean oil, cottonseed oil and maize oil, or a mixture thereof.
8. A process as claimed in claim 7, wherein the vegetable fat is a sunflowerseed oil comprising by weight at least 55% polyunsaturated fatty acids and less than 15% saturated fatty acids.
9. A process as claimed in claim 1 or claim 2, wherein the vegetable fat comprises a mixture of fats high in monounsaturated fatty acids and of fats high in polyunsaturated fatty acids, whereby the saturated fatty acid content of the mixture is less than 25%.
10. A process for producing a cheese product, which process comprises: making a vegetable fat cream as claimed in any one of the preceding claims; and mixing the vegetable fat cream with milk to form a filled milk; and preparing a cheese product therefrom.
11. A process as claimed in claim 10, which further comprises; ripening the filled milk in the presence of a starter culture; adding a coagulating enzyme to form a coagulum; cutting the coagulum into pieces of curd; scalding the curd to 35 to 48°C over 15 to 60 minutes; cooking the curd at 35 to 48°C for 15 to 90 minutes; draining the curd after cooking; allowing the curd to Cheddar; milling the curd; salting the curd at an acidity of 0.42 to 0.65% lactic acid; pressing the curd; and ripening the curd to form the cheese product.
12. A process as claimed in claim 10, which further comprises; ripening the filled milk in the presence of a starter culture; adding a coagulating enzyme to form a coagulum; cutting the coagulum into pieces of curd; scalding the curd to 35 to 48°C over 15 to 60 minutes; cooking the curd at 35 to 48°C for 15 to 90 minutes; washing the curd to bring the temperature to 28 to 32°C; pitching the curd; allowing the curd to reach an acidity of 0.2 to 0.6% lactic acid; salting the curd; pressing the curd; and ripening the curd to form the cheese product.
13. A process as claimed in in any one of claims 10 to 12, wherein the filled milk has a fat content of 1 to 4%.
14. A process as claimed in claim 13, wherein the filled milk has a fat content of 2.3 to 2.5%.
15. A process as claimed in claim 13, wherein the filled milk has a fat content of 1.2 to 1.4% and the cheese product is a reduced fat cheese product.
16. A process as claimed in claim 13 or claim 14, wherein the milk mixed with the vegetable fat cream to form the filled milk is skimmed milk.
17. A process as claimed in claim 13 or claim 14, wherein the milk mixed with the vegetable fat cream to form the filled milk is a mixutre of skimmed milk and whole milk.
18. A process as claimed in claim 17, wherein the fat content of the filled milk consists of 45-55% of sunflowerseed oil and 45-55% of milkfat.
19. A process for producing a vegetable fat cream substantially as hereinbefore described in any one of the Examples A.
20. A vegetable fat cream whenever prepared by a process as claimed in any of claims 1 to 9 or 19.
21. A process for producing a cheese product substantially as hereinbefore described in any of the Examples B.
22. A cheese product whenever prepared by a process as claimed in any one of claims 10 to 18 or 21.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB919100761A GB9100761D0 (en) | 1991-01-14 | 1991-01-14 | Process for making a vegetable fat cream and cheese product therefrom |
Publications (2)
Publication Number | Publication Date |
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IE920086A1 true IE920086A1 (en) | 1992-07-15 |
IE64863B1 IE64863B1 (en) | 1995-09-06 |
Family
ID=10688410
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
IE920086A IE64863B1 (en) | 1991-01-14 | 1992-01-10 | Process for making a vegetable fat cream and cheese product therefrom |
Country Status (2)
Country | Link |
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GB (2) | GB9100761D0 (en) |
IE (1) | IE64863B1 (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE69223784T2 (en) * | 1991-06-14 | 1998-05-07 | Associated Food Technology Pty. Ltd., Carinbah, Neusuedwales | MONO UNSATURATED DAIRY PRODUCTS |
US5580600A (en) * | 1991-06-14 | 1996-12-03 | Associated Food Technology Pty, Ltd. | Monounsaturated dairy products |
GB2324236B (en) * | 1997-04-17 | 2001-10-24 | Univ North London | A cheesy comestible and a process of making same |
GB0229750D0 (en) * | 2002-12-20 | 2003-01-29 | Angel Technology Ltd | Cheese alternative product and process for preparing a cheese alternative product |
DE102005001666A1 (en) * | 2005-01-13 | 2006-05-04 | Milchwerke Mainfranken Eg | Use of rapeseed oil for preparing milk protein containing foodstuffs e.g. fat free farm cheese |
EP1880613B1 (en) * | 2006-05-19 | 2009-09-30 | Ilia Eduardowitsch Singer | Composition for producing artificial cheese |
ES2316275B1 (en) * | 2007-03-16 | 2010-03-22 | Universidad Politecnica De Madrid | PROCESS OF REPLACEMENT OF MILK SATURATED FATS WITH NON-HYDROGEN VEGETABLE OILS. |
NL2003984C2 (en) * | 2009-12-18 | 2011-06-21 | Friesland Brands Bv | Cheese low in saturated fatty acids and method of making same. |
EP2926670A1 (en) | 2012-10-29 | 2015-10-07 | Maria Diet S.L. | Cheese substitute and method for the production thereof |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ATE12338T1 (en) * | 1981-10-07 | 1985-04-15 | Unilever Nv | LOW-FAT BREAD SPREAD AND METHOD OF MAKING THE SAME. |
-
1991
- 1991-01-14 GB GB919100761A patent/GB9100761D0/en active Pending
-
1992
- 1992-01-08 GB GB9200320A patent/GB2255489B/en not_active Expired - Fee Related
- 1992-01-10 IE IE920086A patent/IE64863B1/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
IE64863B1 (en) | 1995-09-06 |
GB9200320D0 (en) | 1992-02-26 |
GB2255489A (en) | 1992-11-11 |
GB2255489B (en) | 1994-10-19 |
GB9100761D0 (en) | 1991-02-27 |
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