The present disclosure relates to the field of cheese making. In particular, the present disclosure relates to apparatuses and methods of fusing curd.
This section is intended to introduce various aspects of the art, which may be associated with the present disclosure. This discussion is believed to assist in providing a framework to facilitate a better understanding of aspects of the present disclosure. Accordingly, this section should be read in this light, and not necessarily as admissions of prior art.
Cheese curds can constitute a final product for the purpose of eating as a snack or as an ingredient in preparing dishes such as poutine or can be considered as an intermediary product to be used in a subsequent cheese making processes. The manufacturing of cheese curds requires that curd be fused, which involves intense manual labor and long time periods.
For example, when making cheddar cheese, curd may be fused by being manually formed into a thick layer that is cut into slabs of fused curd and the slabs are stacked atop each other to form fused curd stacks. The cutting and manipulation of the curd and the stacking of fused curd slabs promotes the syneresis process necessary to produce cheese. The stacking of the slabs of fused curd results in pressure being applied to the slabs, which causes whey to be expelled from the slabs. After ten minutes or so, the slabs are turned over and are again stacked atop each other and, in some instances, individual stacks are stacked atop one another. This can be repeated several times until the acidity of the fused curd stacks reaches a target pH value (e.g., a value comprised between 5.1 and 6.0) and proteins become aligned in the stack. When the target pH is reached, the fused curd stacks are milled into pieces of fused curd (cheese curds), which can then be either salted and packaged for consumer distribution or used in a subsequent cheese making process. For example, when the cheese curds are used in making cheddar cheese or other types of salted or unsalted cheeses, the cheese curds are provided to a pressing device where they are pressed against each other to form a continuum and are subsequently cut into blocks of cheese, packaged and aged.
The fused curd stacks prepared using the manual curd fusing process outlined above may still contain air pockets, water pockets and interstices such that when blocks of a fused curd stack is subjected to the milling process, the resulting cheese curds are unevenly sized and include multiple fines, which give the cheese curds a poor appearance. Further, because the cheese curds are unevenly sized, it can become challenging to automatically package the cheese curds into packages that have a precise target weight.
Therefore, improvements in the manufacturing of cheese curds are desirable.
In accordance with embodiments of the present invention, there is provided an apparatus for fusing curd. The apparatus comprises a container configured to receive curd therein to form a curd stack in the container, and a gas pressure system coupled to the container and configured to apply an overpressure on the curd stack when the container is sealed. There is also provided a method of producing cheese curds in batch. The method comprises obtaining curd in a container; stacking the curd to obtain a curd stack; sealing the container; subjecting the curd stack to an overpressure; maintaining the curd stack at the overpressure for a target duration; releasing the overpressure; and transforming a portion of the curd stack into cheese curds.
In accordance with another aspect, there is provided an apparatus for fusing curd. The apparatus comprises a container configured to receive curd to form a curd stack in the container. The curd stack has associated thereto a pressure parameter specifying a pressure required at the bottom of the curd stack to produce a curd block from a bottom portion of the curd stack. The apparatus also comprises a gas pressure system configured to apply a gas overpressure in the container. The gas pressure system being configured to apply the gas overpressure when a pressure value at the bottom of the curd stack is below the pressure parameter. The gas overpressure has a gas overpressure value equal to or greater than a difference between the pressure required at the bottom of the curd stack and the pressure value at the bottom of the curd stack.
The gas pressure system may comprise a cover configured to seal the container; and a gas source coupled to the container and configured to provide gas in the container to apply the overpressure.
The apparatus may further comprise a controller configured to obtain an indication that the pressure applied by the curd stack at the bottom of the curd stack is below the pressure parameter. The controller may be further configured to obtain the value of the gas overpressure to apply in the container. The apparatus may comprise a pressure sensor configured to measure the pressure at the bottom of the curd stack.
The apparatus may comprise a gas pressure sensing device configured to measure a gas pressure inside the container and to provide a signal to the controller to indicate that the pressure applied by the curd stack at the bottom of the curd stack is below the pressure parameter.
The controller may be configured to determine the pressure at the bottom of the curd stack in accordance with a height of the curd stack and with a predetermined pressure per unit length parameter of the curd stack.
The apparatus may comprise a conveyor unit that includes a conveyor mechanism that has a receiving portion and an emptying portion. The conveyor mechanism may be configured to convey a whey and curd mixture from the receiving portion toward the emptying portion. The emptying portion may be configured to provide the whey and curd mixture to the container. The conveyor unit may comprise an input unit configured to receive the whey and curd mixture and to provide the whey and curd mixture to the receiving portion of the conveyor mechanism. The conveyor unit may comprise a cover portion covering the conveyor mechanism and the cover portion may be configured to impede a loss of thermal energy from the whey and curd mixture to an outside of the conveyor unit to limit a drop in a temperature of the whey and curd mixture as the whey and curd mixture is conveyed from the receiving portion to the emptying portion.
The container may have an output portion configured to cut a block of curd from the curd stack. The apparatus may comprise a stretching device configured to receive the block of curd and to reduce a thickness and increase a length of the block of curd. The stretching device may comprise vertically spaced apart conveyors between which the block of curd is to be provided, and a curd cutter configured to receive the block of curd from the stretching device and to cut the block of curd into cheese curds.
The apparatus may comprise temperature control system configured to maintain a temperature of the container within a predetermined temperature range. The temperature control system may be configured to maintain the temperature within the predetermined temperature range with an accuracy of ±0.5° C.
The apparatus may comprise a pump system configured to pump the whey and curd mixture from a cheese cooking vat to the conveyor unit. The pump system may comprise a positive displacement pump.
The conveyor mechanism may be configured to drain whey from the whey and curd mixture as the whey and curd mixture is conveyed from the receiving portion to the emptying portion. The conveyor mechanism may include a perforated conveyor belt defining a plurality of draining apertures configured to allow whey from the whey and curd mixture to drip therefrom.
The conveyor mechanism may include a gutter configured to receive whey dripping through the plurality of apertures and to output the whey to a whey recovery container. The conveyor mechanism may be at an oblique angle.
In accordance with a further aspect, there is provided a method of producing cheese curds. The method comprises obtaining curd in a container, stacking the curd to obtain a curd stack, maintaining the curd stack within a predetermined temperature range for a predetermined time period, sealing the container from atmospheric pressure, providing a gas overpressure to an inside of the container to subject the curd stack to the gas overpressure, maintaining the curd stack at the overpressure for a target duration, releasing the overpressure, and transforming a portion of the curd stack into cheese curds.
The subjecting the curd to the overpressure may be to compensate for a pressure at the bottom of the curd stack being lower than a pressure required at the bottom of the curd stack. A value of the overpressure may be equal to or greater than a difference between the pressure required at the bottom of the curd stack and the pressure at the bottom of the curd stack. The method may further include obtaining a value of the pressure at the bottom of the curd stack.
Maintaining the curd stack at the overpressure for a target duration may include maintaining the curd stack at the overpressure for a duration comprised between about 1.5 hour and about 2.5 hours.
Embodiments have been described above in conjunctions with aspects of the present invention upon which they can be implemented. Those skilled in the art will appreciate that embodiments may be implemented in conjunction with the aspect with which they are described, but may also be implemented with other embodiments of that aspect. When embodiments are mutually exclusive, or are otherwise incompatible with each other, it will be apparent to those skilled in the art. Some embodiments may be described in relation to one aspect, but may also be applicable to other aspects, as will be apparent to those of skill in the art.
Further features and advantages of the present invention will become apparent from the following detailed description, taken in combination with the appended drawings, in which:
It will be noted that throughout the appended drawings, like features are identified by like reference numerals.
As used herein, the term “about” should be read as including variation from the nominal value, for example, a +/−10% variation from the nominal value. It is to be understood that such a variation is always included in a given value provided herein, whether or not it is specifically referred to.
The container 22 defines a top opening 30 and a bottom opening 32. The apparatus 20 may comprise a controllable closure device 28 configured to open and close the bottom opening of the container 22. As will described in more detail below, curd is placed in the container 22 through the top opening 28 and forms a curd stack in the container 22, when the controllable closure device 28 is closed.
The apparatus 20 also comprises a gas pressure system 34 coupled to the container 22 through a conduit 26 and configured to apply an overpressure on the curd stack formed in the container 22 when the top opening 30 is closed by the cover 24 and when the bottom opening 32 is closed by the controllable closure device 28. The gas pressure system 34 is configured to supply any suitable gas to the inside of the container at an overpressure. The overpressure may range from a few pounds per square inch (psi) above atmospheric pressure up to 8.8 psi or more above atmospheric pressure. Non-limiting examples of gases that can be provided to the inside of the container include food grade carbon dioxide, air and nitrogen. The overpressure produced by the gas pressure system 34 subjects the curd stack to the overpressure.
When there is an overpressure in the container 22, it is important for the cover 24 to be secured to the container 22 during operation such as to seal the top opening 30. Any suitable mechanisms for securing the cover 24 to the container 22 to seal the top opening 30 are considered within the scope of the present disclosure. Examples of such mechanisms include latching mechanisms that latch the cover 24 to the container 22. Other mechanisms include interference closures (presto cooker type of closure), sliding closures, etc. In some embodiments, a seal (not shown) may be installed on the cover 24 or the top of the container 22 such that the seal is between the cover 24 and the top of the container 22 when the cover 24 is closed.
The formation of the curd stack in the container 22 compresses the cheese curd in the curd stack, which causes the curd stack to express whey as the acidification of the curd takes place and as the syneresis process takes place. The overpressure in the container 22 subjects the curd stack to an additional pressure, which assists the syneresis process.
The controllable closure device 28 can be any device that allows the curd stack or part thereof to exit the container 22. As an example, the controllable closure device 28 can include a butterfly valve or more than one butterfly valve, a guillotine valve or two guillotine valves, or any other known controllable closure device or cutter device.
The container 22 shown in
The cover 24 shown in
Referring now to
As will be understood by the skilled worker, the apparatus 20 can include a temperature control system to subject the container 22 to any suitable temperature cycle or to maintain the container within a target temperature range. The apparatus 20 may also include any suitable type of pH measuring device to measure the pH of the curd stack. The apparatus 20 may also include any suitable type of whey draining mechanism to remove the whey expressed from the curd stack.
The conveyor unit 74 comprises a housing 75, a conveyor mechanism 77, and an input device 78 connected to the conduit 76 to receive a whey and curd mixture therefrom. The input device 78 may include a filter 80 configured to prevent curd clumps (clusters) having a size larger than a maximum allowable clump size from passing through and to allow whey and curd mixture or curd clumps having a size less than the maximum allowable clump size to pass. The curd clumps prevented from passing through the filter 80 may fall or slide toward a recovery conduit 82 connected to the input device 78 (to the conveyor unit 74). A portion of the whey present in the whey and curd mixture received at the input device 78 from the conduit 76 may flow toward, and be recovered by, the recovery conduit 82. In some embodiments, there may be no filter (80) present in the input device.
In some embodiments, such as in the embodiment shown at
The curd that traverses the filter 80 may reach the conveyor mechanism 77 at a receiving portion 86 of the conveyor mechanism. The curd that reaches the conveyor mechanism 77 will generally still include whey and may continue to be referred to as whey and curd mixture. The conveyor mechanism may include a conveyor belt 79 that may define a plurality of apertures (not shown). The apertures can be of any suitable size provided the size of the apertures allows whey to pass through the apertures while preventing most or the curd from passing through the apertures. For example, the apertures may have dimensions like those of draining cloth apertures or to those of whey/curd strainer apertures. In some embodiments, the dimensions of the apertures can range from 3 to 20 microns. As the whey and curd mixture 89 is conveyed away from the input device 78, whey may drain out of the whey and curd mixture 89 through the plurality of apertures and fall onto a whey collecting surface 84, which may be a bottom surface of the housing 75. The whey collecting surface 84 may be angled toward a conduit 83 connected to the recovery conduit 82. In some embodiments, there may be no apertures (draining apertures) defined by the conveyor belt 79.
The housing 75 may be configured to cover the conveyor mechanism 77. The housing 75 may act as a thermal barrier between the whey and curd mixture present in the conveyor mechanism 74 and the atmosphere surrounding the housing 75, as the whey and curd mixture 89 is conveyed away from the input device 75 toward an output portion 88 of the conveyor mechanism 77. The presence of a cover portion 90 of the housing 75 helps maintain the temperature of the whey and curd mixture within a target temperature range, which allows greater control over the acidity or acidity variation of the whey and curd mixture and of quality of the food product (e.g., cheese curds) to be produced with the curd. In some embodiments, for example, the whey and curd mixture at the input device 76 may contain 80% of whey and 20% of curd (or any other suitable ratio) and, due to the draining of whey, there may be, at the output portion 88 of the conveyor mechanism, 20% of whey and 80% of curd (or any other suitable ratio) in the whey and curd mixture. In some embodiments, the whey and curd mixture arriving at the input device 78 may be at a temperature comprised between 38° C. and 42° C. (or between any other suitable temperature limits). In some embodiments, the temperature at the output portion 88 may be at between 36° C. and 38° C. (or between any other suitable temperature limits). That is, in some embodiments, the housing 75 of the conveyor unit 74 may be configured to limit the temperature variation of the whey and curd mixture to about 2° C. to 6° C. In some embodiments, the temperature of the whey and curd mixture present in the conveyor unit 74 may be maintained within a temperature range that favors the fusion and aggregation of protein in the whey and curd mixture. In some embodiments, in addition to reducing heat loss and temperature decrease in the whey and curd mixture, the housing 75 (cover portion 90) may reduce a decrease in humidity of the whey and curd mixture.
As the whey and curd mixture 89 on the conveyor mechanism 77 reaches pass the output portion 88, the whey and curd mixture 89 may fall into the container 92. At this stage, the pH of the whey and curd mixture 89 may be between, FOR EXAMPLE, 5.8 and 6.3. The pH value at this stage may be selected in accordance with the desired cheese product and will affect the texture and the rheology of the cheese curds produced. The pH of the whey and curd mixture 89 as it traverses the conveyor unit 74 may vary by, for example, ±0.05 of a target value situated in the 5.8 to 6.3 pH range. The inventors have found that the housing 75 (cover 90) of the conveyor unit 74 allows to reduce temperature variations of the whey and curd mixture 89 conveying in the conveyor unit 74 and that in turn, reduces variations in the pH value of the whey and curd mixture. That is, the housing 75 allows the temperature of the conveyed whey and curd mixture to vary less than if there were no housing 75 (cover 90). As will be understood by the skilled worker, the ability to control the pH of the whey and curd mixture 89 allows some control over demineralisation of the whey and curd mixture 89 as it arrives at the container 92. The container 92 may have any suitable height and diameter and may be selected according to a cheesemaker's desired production. As an example, the container may have a height comprised between 2 and 5 meters and may have a diameter of 1.5 meter. Containers with heights outside the 2 to 5 meter range or diameters different than 1.5 meter are to be considered within the scope of the present disclosure. The apparatus 70 may be configured to produce between 500 and 3000 kg of fused curd daily (between 500 and 3000 kg of cheese curds).
The container 92 may have a cylindrical portion 94 and an extruder portion 96 coupled to the cylindrical portion 94. The extruder portion may be coupled to an output portion 98. The cylindrical portion 94 and the extruder portion 98 may be coupled to the recovery conduit 82, through a connecting conduit 100, to recover whey present in the cylindrical portion 94 or the extruder portion 96.
The cylindrical portion 94 or the extruder portion 96 or both the cylindrical portion 94 and the extruder portion 96 may have an interior wall 104, spaced apart from the exterior wall 93, and configured to drain whey from the whey and curd mixture received in the container 92 as the whey is expressed from the curd stack that is forming in the container 92. The interior wall may include any suitable type of filter material such as, for example, a stainless steel mesh. The curd passing through the extruder portion 96 may increase the mass density of the curd.
The cylindrical portion 94 and/or the extruder portion 96 may include or be thermally coupled to a heating device 91 configured to maintain the cylindrical portion 96 and/or the extruder portion 96 at a target temperature. Any suitable type of heating device may be used. For example, the cylindrical portion 94 and/or the extruder portion 96 may be thermally coupled to a heat exchanger or include a thermal jacket configured to have a warm fluid (e.g., warm water) circulating therein. A controller 113 may be connected to a thermometer device 115 coupled to the container 92 and also be coupled to the source (not shown) of the fluid to control a temperature of the fluid. The controller may be configured control to maintain the temperature of the container at a target temperature. The controller may also be coupled to a pump (not shown) configured to pump or circulate the warm fluid through the jacket. In some embodiments, the temperature of the container 92 may be controlled within about ±0.5° C.
As the whey and curd mixture 89 falls into the container 92, a curd stack 106 is formed in the container 92. As the curd stack 106 grows in height, pressure along the curd stack and at the bottom of the curd stack increases, which causes air-filled or whey-filled interstices in the curd stack 106 to collapse and to expel, out the curd stack, the whey or air that was in the interstices. That is, as the pressure increases with the addition of whey and curd mixture in the container 92, the curd stack 106 fuses into a continuous curd stack (i.e., a curd stack mostly free of interstices).
The desired pressure at the bottom of the curd stack 106 or at a bottom portion of the curd stack 106 may be comprised between, for example, about 0.2 kg/cm2 and about 0.42 kg/cm2 or more (about 2.85 psi to about 6 psi or more). For example, the desired pressure may be 0.45 kg/cm2, which is produced by a curd stack having a height of about 5 meters. However, any other suitable pressure at the bottom of the curd stack can be used without departing from the scope of the present disclosure. Curd stack taller than 5 m are within the scope of the present disclosure. As will be understood by the skilled worker, the curd stack 106 may have associated thereto a pressure per unit length parameter defining the pressure at the bottom of the curd stack 106 as a function of the height of the curd stack 106. The pressure per unit length parameter may be obtained in accordance with a known curd density and with the geometry of the curd stack.
The extruder portion 58 may be configured to funnel or extrude the curd stack 106 toward the output portion 98. The funnelling of the curd stack 106 may cause lateral compression of the curd stack 106 as well as longitudinal stretching of the curd stack 106. The lateral compression (compression in a plane that is perpendicular to the length of the curd stack) and longitudinal stretching (stretching along the axis defined by length of the curd stack) helps create a fibrous texture in the curd stack 106, which contributes to the continuousness of the curd stack 106.
In some embodiments, the cylindrical portion 94 may have a horizontal circular cross section and the extruder portion 96 may have a horizontal square or rectangular cross section Any other suitably shaped cylinder and extruder portion are to be considered within the scope of the present disclosure. In some embodiments, the cross-section of the cylindrical portion 94 and the output cross-section of the extruder portion may be selected to cause a reduction in surface area of about 50% or any other suitable reduction percentage. That is, the surface area the horizontal cross-section of a block of curd output from the extruder portion 96 or from the output portion 98 may be half of the horizontal cross-section of the curd stack in the cylinder portion 94. Any other suitable change in surface area is to be considered within the scope of the present disclosure. In some embodiments, the density of the curd may increase due to the curd passing through the extruder portion 96.
Having square or rectangular cross-section blocks of curd (114) allows for a more uniform milling of the blocks of curd to produce (e.g., a cutting process) uniformly sizes pieces of curd (i.e., pieces or curd having a substantially same weight, volume and surface area), which allows even seasoning (e.g., salting) of the pieces of curd and allows for automated packaging of the pieces of curds in packages having a substantially same weight.
The output portion 98 may include guillotine valves 102 configured to cut a block of the curd stack 106 and to release the block from the output portion 98. The guillotine valves 102 may be vertically spaced apart by any suitable distance. The vertical spacing of the guillotine valves determines the height of blocks of curd obtained from the curd stack 106.
The apparatus 70 may comprise a cover 108 configured to close off or seal a top opening 110 defined by the container 92. The apparatus 70 may also comprise a (food grade) gas pressure system 112 coupled to the cover 110 and/or the container 92 through a gas line 95. In some embodiments, when producing a batch of cheese curds of a size that does not require a full-height curd stack 106, and where the maximum height of the curd stack 106 for that batch is insufficient to produce, at the bottom portion of the curd stack, the pressure required to obtain or produce the desired fused curd stack, then the container may be sealed with the cover 108 and the gas pressure system 112 may be activated to provide an overpressure in the container to compensate for the shortness of the curd stack 106. The overpressure on the curd stack 106 may decrease the spacing between the casein micelles present in the curd stack 106 and contribute to the aggregation and fusion of the micelles. This contributes to regulating the humidity level of the cheese products obtained from the curd stack 106.
The overpressure may range from a few pounds per square inch (psi) over atmospheric pressure up to 8.8 psi or more above atmospheric pressure. The range of overpressure contemplated in embodiments of the present disclosure may be qualified as low overpressure range. Non-limiting examples of gases that can be provided to the inside of the container include food grade carbon dioxide, air and nitrogen. The overpressure produced by the gas pressure system 112 subjects the curd stack 106 to the overpressure. The container may include a pressure measuring device 111 configured to measure the overpressure in the container. The pressure measuring device 111 may be coupled to the cover 108, the cylindrical portion 94 or the extrusion portion 96. The inventors have discovered that when the curd stack 106 is not sufficiently tall to produce a target pressure at the bottom of the curd stack 106, an overpressure of gas may be introduced in the container to compensate for the insufficient height of the curd stack and to produce cheese curds of the same quality as those produce from a taller curd stack that generates the target pressure at the bottom of the curd stack. The overpressure of gas on the curd stack cause the casein micelle matrix to contract and, consequently, express whey that may be present in the casein micelle matrix.
When there is an overpressure in the container 92, it is important for the cover 108 to be secured to the container 92 during operation such as to seal the top opening 110. Any suitable mechanisms for securing the cover 108 to the container 92 to seal the top opening 110 are considered within the scope of the present disclosure. In some embodiments, a seal (not shown) may be installed such that the seal is between the cover 108 and the top of the container 92 when the cover 109 is closed.
The overpressure applied to the curd stack 106 subjects the curd stack to an additional pressure, which assists in the syneresis process. The syneresis process contributes to whey being expressed from the curd stack 106 as the acidification of the curd takes place.
The system 70 may also include a recovery pump 124 configured to pump recovered whey or cheese curd from the recovery conduits 82, 83 and 100 into a recovery vessel (not show) or a drain (not shown).
One or more shut-off valve (not shown) may be installed to prevent the overpressure in the container 92 to be felt at the recovery pump 124 or at the conveyor unit 74. For example, shut-off valves may be installed immediately before the recovery pump 124 and along the recovery conduit 82, below the connecting conduit 83.
The system 70 may include one or more acidity measuring device 107 (e.g., a pH meter) installed in the container 92 and configured to measure the acidity of the curd stack 106. The system 70 may include a controller 113 that may be coupled to the acidity measuring device 107, to the pressure measuring device 111, to the gas pressure system 112, to shut-off valves that may be present along the whey recovery conduits and to the conveyor unit 74. The controller 113 may be configured to control the gas pressure system according to a gas pressure signal received from the pressure measuring device. The controller may also be configured to control the butterfly valves 102 in accordance with a pH signal received from the acidity measuring device 107. The system may also include a curd stack pressure sensor 131 (or a force sensor) also coupled to the controller 113 and configured to measure a pressure or a force applied by the curd stack 106 on the topmost butterfly valve 102.
In operation, the controller 113 may continuously or periodically obtain signals from the acidity measuring device 107, the pressure monitoring device 111, and the pressure sensor 131 and the controller may control the gas pressure systems 112, the guillotine valves 102 and the conveyor unit 74. For example, if the controller 112 receives a signal that indicates the pH of the curd stack 106 has not yet reached a target value, the controller 112 may keep the butterfly valves 102 closed for longer than a predetermined period to allow the pH value of the curd stack 106 to decrease and attain the target value. In another scenario, if the controller 112 receives a signal from the pressure sensor 131 (or the force sensor) indicating the pressure is below a target value and, if the controller 113 obtains a signal the conveyor unit 74 is not in operation and that no additional whey and curd mixture is being added to the container 92, then the controller 113 may cause the cover 108 to be closed and the gas pressure system 112 to be activated to provide a gas overpressure in the container.
The flattening and stretching of the curd blocks 114 as they convey between the first conveyor device 116 and the second conveyor device 118 increases an alignment of the fibrous structure of the curd of curd blocks 114. This may result in increase shape and size uniformity of the cheese curds obtained when cutting the blocks of curd.
After conveying between the first conveyor device 116 and the second conveyor device 118, the curd blocks 114 are provided to a curd cutter (curd mill, cheese cutter, cheese mill) 120, which is configured to cut the curd blocks 114 into pieces of curds, which may be referred to as cheese curds. The cheese curds may exit the curd mill 120 onto a cheese curd conveyor 122, which may convey the cheese curds toward a salting process and then to a packaging process. Alternatively, the cheese curds may be conveyed to any other suitable processing step.
As the temperature increases from 20° C. to 50° C., G′ and G″ decrease due to fat liquefaction, but G′ is larger than G″, indicating the mechanical resistance of the protein network in the curd stack sample. The slope of G′ (plot 138) changes between 40° C. and 50° C., which suggests a change in the mechanical resistance of the protein network (cheese network) in relation to the thermal stability of the proteins. The change is observed in tan δ, which starts to increase rapidly. When the temperature reaches a value where G′ equals to G″ (tan δ=1), the melting point of curd stack sample occurs. This means the curd stack sample is undergoing a phase transition, where cheese changes from solid to semi-solid or liquid phase as a function of temperature. According to the plot 142, the melting point associated to the curd stack sample is between about 48° C. and 55° C. As the temperature increases beyond the melting point, the protein structure begins to collapse and the structural arrangement of the casein and the whey protein follows a complex process. The value of tan δ reaches a maximum at about 58° C., which is associated with colloidal calcium phosphate (CCP).
This indicates the tower cheese has the meltability function at same age as control cheese which does not have this property.
It will be appreciated that, although specific embodiments of the technology have been described herein for purposes of illustration, various modifications may be made without departing from the scope of the technology. The specification and drawings are, accordingly, to be regarded simply as an illustration of the invention as defined by the appended claims, and are contemplated to cover any and all modifications, variations, combinations or equivalents that fall within the scope of the present invention. In particular, it is within the scope of the technology to provide a computer program product or program element, or a program storage or memory device such as a magnetic or optical wire, tape or disc, or the like, for storing signals readable by a machine, for controlling the operation of a computer according to the method of the technology and/or to structure some or all of its components in accordance with the system of the technology.
Acts associated with the method described herein can be implemented as coded instructions in a computer program product. In other words, the computer program product is a computer-readable medium upon which software code is recorded to execute the method when the computer program product is loaded into memory and executed on the microprocessor of the wireless communication device.
Although the present invention has been described with reference to specific features and embodiments thereof, it is evident that various modifications and combinations can be made thereto without departing from the invention. The specification and drawings are, accordingly, to be regarded simply as an illustration of the invention as defined by the appended claims, and are contemplated to cover any and all modifications, variations, combinations or equivalents that fall within the scope of the present invention.
Number | Date | Country | |
---|---|---|---|
63330145 | Apr 2022 | US |