ULTRA-HIGH TEMPERATURE PASTEURIZED MILK CONCENTRATE, PACKAGE. DISPENSER AND METHOD OF PRODUCING SAME
RELATED APPLICATIONS
This application is a continuation-in-part application of U.S.
Application Serial No. 09/850,983, filed May 8, 2001 , which in turn is
a continuation of U.S. Application Serial No. 09/433,365, filed
November 3, 1 999, now abandoned. The entire disclosures of these
applications are incorporated herein by reference.
FIELD OF THE INVENTION
This invention relates to producing and packaging an ultra-
high temperature pasteurized milk concentrate for dilution with water and
dispensing as reconstituted milk having a fresh taste and having a
flavored, sweetened or juice note.
BACKGROUND OF THE INVENTION
The cost of transporting and storing fresh milk is significant
because of its short shelf life and weight. Because fresh milk is used
extensively by America's military and is one of its largest export
commodities, there is a long-felt need for a milk concentrate that has a
longer shelf life, a product package with a lesser weight for transportation
and storage, and that provides the same physical and taste characteristics
of fresh milk when reconstituted.
The prior art addresses various aspects of the UHT
pasteurization of milk, the production of condensed milk products, and
the reconstituting of concentrated liquid beverages. No known prior art,
however, discloses an ultra-high temperature pasteurized liquid milk
concentrate which may be packaged for dispensing as a reconstituted
milk beverage in existing beverage dispensers or for transporting large
amounts of UHT pasteurized milk concentrate worldwide to provide a
reconstituted milk at the destination that has the same physical
characteristics of and tastes like fresh milk.
U.S. Patent 2,860,057 discloses a known preparation of a
sterilized evaporated or condensed milk having a final desired
concentration of from about 1 6% to 35% total solids compared to the
standard concentration of about 8.0-8.5% total solids. The different
processes each involve forewarming and pasteurizing steps including
high-temperature-short-term sterilization after the milk is first
concentrated by conventional means. The disclosed processing avoids
age thickening or gelation of the milk during high-temperature sterilization
effected either before or after packaging in a can. If an aseptic canning
method is used, the sterilized concentrate is subsequently homogenized
under sterile conditions. Reconstitution involves a complicated dilution,
mixing, and color comparison procedure with disclosed mixing volume
ratio of water to evaporated milk of 1 : 1 .
U.S. Patent 4,921 ,71 7 describes a process for producing
UHT sterilized concentrated milk including first sterilizing a partially
concentrated milk product and then effecting further concentration of the
milk product under sterile conditions. U.S. Patent 4,842,884 describes
a formulated milk concentrate made with a mixture of nonfat dry milk
solids, water, edible oil and sugar. The concentrate can either be frozen
for later use or immediately blended with water to produce a beverage.
Once reconstituted, it may be stored for up to about 5 days.
U.S. Patents 2,570,231 ; 3, 108,875; 4,362,756; and
5,766,666 respectively disclose a sweetened condensed skim milk,
condensed cream, condensed milk having at least 8% milk fat, and a
reduced fat and/or fat-free condensed milk each processed differently to
produce a novel sweetened condensed dairy product in each instance.
The condensed cream is used for a source of fat in ice cream. The other
three condensed milk products are used in the baking and confectionary
industries and by retail consumers to produce baked goods. U.S. Patent
4,091 , 1 1 8 describes a vegetable-based sweetened condensed milk used
as a coffee creamer.
U.S. Patent 2,565,085 discloses the customary forewarming
of whole milk to destroy bacteria, molds, yeasts, and the like. The
forewarming also helps to maintain the texture of the milk product. Such
forewarming of the milk is usually effected at a temperature in the range
of 145°F to 1 75°F. U.S. Patent 5,260,079 describes a method of and
equipment for controlling the content of fat in milk using specified
process parameters for mixing skim milk with cream. U.S. Patents
5,223,299 and 5,229, 1 59 disclose sterilizing milk without stabilizers and
a packaged resultant milk concentrate product for use as coffee
creamers. U.S. Patent 4,282,262 discloses a milk blend fraction used as
an ingredient component for a two-packet frozen dessert. The milk blend
includes sodium hexametaphosphate and carrageenan used together as
stabilizers.
In brief, in prior practice ultra-high temperature pasteurized
(UHT) milk often had a "scor ched" or "burnt" milk taste as a result of
the extremely high temperature to which the milk is heated in the UHT
process. Milk is an extremely heat-sensitive product, in part, because it
contains proteins which become denatured at higher temperatures. Such
denaturing of the milk results in the scorched milk flavor whereby it loses
its fresh milk taste. While improvements have been made in UHT
processing for regular strength solids UHT milk products prior to this
invention, it was commonly believed in the dairy industry that the
problem of scorching would increase as the solids level in milk increases
because, in such a concentrated environment, milk proteins would be
more susceptible to denaturing at higher temperatures. Known
concentrated milk with high milk solids also has a natural tendency
to separate or granulate and turn to gel upon aging. Moreover,
reconstitution of such a concentrated milk also may lead to granulation
and product separation, thus destroying the taste and mouth feel of
regular fresh milk.
SUMMARY OF THE INVENTION
This invention is directed to ultra-high temperature
pasteurized (UHT) liquid milk concentrates and methods for producing
them. The invention also provides an aseptic UHT milk concentrate
package and dispenser for reconstitution with water and dispensing as a
fresh milk product.
The objectives and benefits of this invention are achieved by
providing a condensed liquid milk blend which includes a stabilizer and a
pasteurized liquid milk concentrate having an amount of nonfat milk solids
sufficient to produce the UHT liquid milk concentrate having a nonfat milk
solids content of at least about 29.9% (i.e., about 30%) by weight when
the UHT milk concentrate is reconstituted with water. It has been found
that such a high solids liquid milk concentrate may be converted into a
UHT milk concentrate by directing a continuous flow of a condensed milk
blend into direct contact with steam. The steam is injected directly into
the continuous flow of the milk blend at an effective ultrapasteurizing
temperature sufficient to form the UHT milk concentrate having a nonfat
milk solids content of at least about 30% by weight.
The UHT liquid milk concentrate upon reconstitution with
water, at water to concentrate volume ratios in the range of about 3: 1 to
4: 1 , tastes like regular fresh milk. The UHT liquid milk concentrate has
(a) an extended shelf stability of at least about 30 days without
granulation and/or separation, (b) milk solids which do not separate upon
dilution with water, and (c) upon dilution provides a drinkable product
which tastes like fresh milk.
Among the other advantages achieved by this invention, the
UHT concentrated milk is packaged under aseptic conditions and used in
currently available dispensing machines. Other benefits in transportation,
military use, commercial and other food service programs are achieved.
Other advantages and objectives of this invention will be further
understood with reference to the following detailed description.
DETAILED DESCRIPTION OF THE INVENTION
A primary purpose of this invention is to provide an ultra-
high temperature pasteurized concentrated liquid milk that has a shelf life
of at least about 30 days and, upon dilution with about 3 to 4 volumes
of water, the milk solids do not separate and the diluted concentrate has
an acceptable taste profile like fresh milk. The stability is obtained
without granulation and/or separation of solids, i.e., a lack of
sedimentation or crystallization of solids. Hereinafter the ultra-high
temperature concentrated liquid milk is sometimes simply referred to as
"ultrapasteurized milk concentrate" or "UHT milk concentrate".
The term "fresh" as applied to milk herein means
characteristics normally associated with fresh, pasteurized milk, whether
it is in the categories of Fat Free, or skim (less than 0.21 % fat), Low Fat
(1 % fat), Reduced Fat (2% fat), or Full Fat (3.25% fat). These milk
products are purchased at a store by a consumer who recognizes them
as fresh. Consumers have recognition of the inventive products as fresh,
as compared to, for example, products such as canned or condensed
milk, reconstituted powdered milk, UHT milk, and the like. A consumer
would recognize these latter-mentioned products as not fresh. In addition
to the consumer test for freshness presently employed in this invention,
other sensory tests may be employed to give a sensory description of the
inventive milk product. Such other tests usually evaluate the major
sensory characteristics of fresh milk which include (a) the presence or
absence of visual defects, whether it has visibly separated or coagulated,
or changed in color, (b) the aroma and taste, which together contribute
to the flavor, and (c) the texture and mouth feel, i.e., free of milk defects
which may be described as watery, thin, coagulated, sandy, gritty, or
separated.
An extended shelf stability or life of at least about 30 days
means that the milk has an acceptable taste profile of fresh milk when
either (a) it is held or stored at a temperature of less than about 45°F
according to the Public Health Service/Food and Drug Administration
Publication No. 229, entitled, "Grade A Pasteurized Milk Ordinance,
Section 7, pages 1 8-1 9 (1 999 revision) standard for milk (sometimes
referred to herein after as "ESL" milk) or (b) it is aseptically packaged and
does not require refrigeration for storage at a temperature less than about
85°F, sometimes referred to hereinafter as "aseptic" or aseptically
packaged" milk.
Another object of the invention is to provide a packaged
concentrated milk product for use in currently available dispensing
machines used for reconstituting and dispensing juices.
A further object is to provide a concentrated liquid milk
product package that produces substantial cost savings for export,
military uses such as for naval ships and submarines, and for commercial
and government food service programs.
Still another object of the invention is to provide milk
concentrate packages in standard retail pint and quart packages for the
general population that yield about V_ gallon for the pint and about one
gallon for the quart when reconstituted. In general, concentrate packages
having from about 2 to 64 ounces are provided for use.
A still further object of the invention is to provide milk
concentrate that is enriched with vitamins and other nutritive ingredients
that address special dietetic needs of special groups with dietary
restrictions.
Another object is to provide a UHT pasteurized liquid milk
concentrate packaged in an amount of up to 300 gallons while gaining
shelf-life and economic benefits heretofore unknown in the dairy industry
and enabling the on-site destination reconstituting of the concentrate
using existing dispensing equipment and otherwise using uncomplicated,
simple water to milk concentrate mixing techniques in water to
concentrate volume ratios in the range of about 3: 1 to 4: 1 .
In one embodiment, the package comprises a container for
a preselected amount of the ultrapasteurized liquid milk concentrate with
a structural configuration effective for use with dispensing means which
includes means for mixing the ultrapasteurized milk concentrate with
water to create a reconstituted milk beverage that tastes like fresh milk.
To preferably produce a 1 % reconstituted product at a mix ratio of about
3 to 3.7 of water to concentrate, the ultrapasteurized milk concentrate
includes a high-solids condensed skim milk (HSCS) in the range of about
87.4% to about 89.4% by weight (more generally about 80% to about
90% by weight) a cream content in the range of from about 8.5% to
1 0.5% by weight, and a stabilizer content of about 0.7% by weight
(based on solids content of stabilizer) . To preferably produce a skim milk
product at a mix ratio of about 3.25 to 4 of water to concentrate, the
ultrapasteurized milk concentrate includes a high solids condensed skim
milk (HSCS) in the range of about 96.5% to about 99% by weight, a
cream content in the range of about 0 to about 2.5% by weight, and a
stabilizer solids content of about 0.75 % by weight. To preferably
produce 2% and 3.25% resonstituted whole milk products at a mix ratio
of about 3 to 3.5 of water to concentrate, the ultrapasteurized milk
concentrate includes high solids condensed skim milk (HSCS) range of
about 67.5% by weight to about 81 % by weight, cream content in the
range of about 1 8% to 31 .5% by weight, and a stabilizer content of
about 0.6 to about 0.65% by weight. More broadly, in order to produce
a spectrum of products of no fat to full fat milk products, mix ratios of
about 3 to 4, the high solids condensed skim milk is in the range of about
67 to about 99% by weight, cream is in the range of from about 0 to
about 31 .5% by weight, and the stabilizer is in the range of about 0.6 to
0.75% by weight. The initially pasteurized condensed skim milk has a
total milk solids nonfat (MSNF) content of at least about 30% by weight
or more, preferably about 35% to 45% by weight, and cream has a milk
fat content of from about 36% to 45% by weight. The stabilizer solids
content preferably consists essentially of sodium hexametaphosphate in
the range of about 97.0%^ to 99.0% and carrageenan (kappa type) in the
range of about 1 .0% to 3.0%. Other stabilizers may be employed to
achieve the benefits of this invention in view of this detailed description.
In a specific embodiment, the milk concentrate package has a structural
configuration effective for disposition of a liquid dispensing means
including discharge nozzle means for mixing said ultrapasteurized
concentrate with water to dispense the reconstituted liquid milk
beverage.
The method for producing the ultrapasteurized liquid milk
concentrate of the invention comprises heating a milk starting product to
an elevated pasteurizing temperature under reduced pressure for an
amount of time sufficient to evaporate liquid from the milk starting
product to form a pasteurized, high-solids intermediate liquid milk
concentrate. An amount of cream is mixed with the intermediate milk
concentrate to form a condensed liquid blend having a preselected
amount of fat content to produce the reconstituted milk beverage having
the desired taste characteristics.
A final liquid milk concentrate is produced by mixing a
sufficient amount of a stabilizer material with a predetermined amount of
the condensed liquid blend. The stabilizer material is effective to ensure
uniform distribution of and prohibit separation and settling of milk solids
in the ultrapasteurized liquid milk concentrate during storage. The
stabilizer material is effective to produce a protein complex for forming
a stable dispersion of colloidal constituents and to substantially uniformly
distribute the colloidal constituents in the final liquid milk concentrate.
The stabilizer material maintains the preselected pH of the final liquid milk
concentrate in the range of about 6 to 8 during the ultrapasteurizing step.
The stabilizer material is further effective for inhibiting thermal
coagulation of milk proteins at the preselected pH of the final milk
concentrated. The total MSNF content in the final liquid milk concentrate
is at least about 30% by weight of the concentrate to produce a
reconstituted milk beverage having a MSNF content of at least about
8.25% by weight.
The final liquid milk concentrate is ultrapasteurized to form
the ultrapasteurized liquid milk concentrate of the invention. The final
homogenizing and packaging of the ultrapasteurized milk concentrate
forms the ultrapasteurized liquid milk concentrate package of the
invention for subsequent mixing of the ultrapasteurized milk with water
to form the desired reconstituted milk beverage.
A feature of the invention is directed to a heating step that
includes foreheating the initial liquid milk to an elevated foreheating
temperature for a selected time period to produce the milk starting
product, which is then heated to the elevated pasteurizing temperature
that is higher than the foreheating temperature to produce the desired
intermediate liquid milk concentrate. When the initial liquid milk is a skim
milk, the elevated foreheating temperature is in a range of about 144°F
to about 1 52°F and the elevated pasteurizing temperature is maintained
in the range of about 1 78°F to 1 82°F for a time period in the range from
about 1 6-22 seconds to pasteurize the intermediate milk concentrate.
Another feature is directed to the manner of preparing the
stabilizer material for mixing with the condensed liquid blend. In a
specific embodiment, the stabilizer material is first solubilized in water
under high shear conditions and at an elevated temperature to form a
stabilizer slurry that is mixed with the condensed liquid blend to form the
final liquid milk concentrate. In the preferred form, the stabilizer slurry
includes sodium hexametaphosphate and carrageenan so that when the
slurry is mixed with the condensed liquid blend, the carrageenan forms
a protein carrageenate complex with milk protein to provide the stable
dispersion of colloidal constituents. The sodium hexametaphosphate is
effective to aid in substantially uniformly distributing the colloidal
constituents and inhibiting thermal coagulation in the concentrate. The
stabilizer slurry includes a stabilizer material solids content in the range
of about about 33 to 35% by weight of the stabilizer slurry to produce
a stabilizer material solids content of less than about 1 .0% by weight of
the final liquid milk concentrate. The stabilizer material includes sodium
hexametaphosphate in the range of about 32 to 34.5% of the stabilizer
slurry and carrageenan (kappa type) in the range of about 0.3 to about
1 % by weight. Other stabilizers may be used as long as they provide the
benefits of this invention.
Another feature of the invention is directed to the particular
viscosity of the concentrates at different times during the processing.
The viscosity of the intermediate liquid milk concentrate is in the range
of about 300 to 400 centipoises at 40° to 45°F and the viscosity of the
ultrapasteurized (UHT) milk concentrate is in the range of about 1 ,000 to
1 ,500 centipoises at the same temperature range. The pasteurized
intermediate liquid milk concentrate includes a milk solids nonfat (MSNF)
content preferably in the range of from 35.0% to 36.5% by weight up
to about 45% by weight. The pasteurized intermediate liquid milk
concentrate thus includes a MSNF content in an amount preferably of at
least about 35% to produce a reconstituted low fat milk product upon
mixing the ultrapasteurized milk concentrate with water. Moreover, the
upper limit of the milk solids nonfat content of about 45% precludes burn
damage of the final liquid milk concentrate during the ultrapasteurizing
step. Water is mixed with the ultrapasteurized milk concentrate to form
the reconstituted milk product in a water/concentrate volume ratio of
parts of water to parts of ultrapasteurized milk concentrate in the range
of about 3: 1 to about 4: 1 .
Another feature of the invention is directed to the
composition of the intermediate liquid milk concentrate that includes
intermediate high-solids milk concentrate in the range of from about 67%
to about 99% by weight, cream in the range of from about 0 to about
32% by weight, and stabilizer material in the amount of about 0.6 to
about 0.75% by weight of the concentrate. The reconstituted milk
beverage over the range of non fat to fat milk products includes a milk fat
content in the range of less than about 0.21 % to 3.25 % and a milk
solids nonfat content of at least about 8.25% by weight of the milk
beverage.
A further feature of the invention is directed to the ultra
pasteurizing step that includes heating the intermediate liquid milk
concentrate to an elevated ultra pasteurizing temperature by direct
contact with steam for a period of time sufficient to form the
ultrapasteurized liquid milk concentrate. In particular, it has been found
that injecting steam directly into a continuous stream in flow of the
intermediate liquid milk concentrate at UHT conditions provides the
desired product of this invention. In a specific embodiment, the ultra
pasteurizing step includes heating the intermediate liquid milk concentrate
to a temperature in the range of about 288°F to 295°F for a period of
time sufficient to produce an ultrapasteurized liquid milk concentrate of
the invention. More specifically, the ultra pasteurizing heating step
includes first heating the intermediate liquid milk concentrate to a first
elevated temperature of about 1 80°F for a period from 30 to 36 seconds
and then directing the heated liquid milk concentrate to a direct steam
injection zone to be heated to about 290°F to 295°F for a period of
about 2 to 5 seconds.
The homogenizing step comprises homogenizing the
ultrapasteurized milk concentrate in the range of about 3000 psi to about
5000 psi. The packaging step for the ESL milk feature after
homogenizing includes the step of cooling the ultrapasteurized milk
concentrate to a temperature of less than about 45°F and filling
packaging means with the ultrapasteurized milk concentrate for
disposition in a liquid beverage dispenser. In this packaging step, the
ultrapasteurized milk concentrate is disposed in a package for use in a
beverage dispenser that includes discharge nozzle means for mixing the
ultrapasteurized milk concentrate with water to form the desired
reconstituted milk beverage. For the aseptically packaged milk, it is at
temperatures of about 70°to 90°F, or about 80°F, during packaging. In
a further specific embodiment, the packaging step includes disposing up
to 300 gallons of the ultrapasteurized milk concentrate in a package
container.
In another embodiment of the invention, a preselected
amount of liquid skim milk is heated to a temperature in the range of
about 1 44° to 1 52°F for an amount of time sufficient to produce a
preheated milk starting product. The preheated milk starting product is
then pasteurized in the range of about 1 78°F to 1 82°F in a time period
in the range of about 1 6-22 seconds. The pasteurizing step is effected
under a vacuum to evaporate liquid from the milk starting product to
produce an intermediate condensed liquid milk including milk solids nonfat
in the range of about 35.0% to 36.5% by weight. Cream and stabilizing
material are mixed with the intermediate condensed liquid milk to produce
a final liquid milk concentrate including a cream content in the range of
8.5% to 1 0.5% by weight thereof and a stabilizing material content of
less than 1 .0% thereof. The final liquid milk concentrate is then
ultrapasteurized and homogenized to form the ultrapasteurized milk
concentrate, which is then disposed in the package container for
subsequent reconstitution with water at a water/milk concentrate volume
ratio in the range from about 3: 1 to 4: 1 .
In another feature of the method of the invention, a liquid
milk starting product is heated under vacuum to an elevate temperature
for an amount of time sufficient to pasteurize the milk starting product
and evaporate liquid from the milk starting product to form a pasteurized,
high-solids condensed liquid skim milk including milk nonfat solids in the
range of about 35.0% to 36.5%. An amount of cream is mixed with the
pasteurized condensed skim milk to form a final skim milk concentrate.
The stabilizer slurry contains sodium hexametaphosphate and carrageenan
(kappa type) in amounts sufficient to prohibit separation, settling, and
crystallization of milk constituents in the final liquid milk concentrate
during storage. The final liquid skim milk concentrate is ultrapasteurized,
homogenized and packaged to form an ultrapasteurized milk concentrate
package for disposing in a liquid dispensing means including discharge
nozzle means for mixing the ultrapasteurized milk concentrate with water
to dispense a reconstituted milk beverage.
PROCEDURES AND OPERATING EXAMPLES
The ultrapasteurized concentrated milk product of the
invention is produced using a direct steam injection process to achieve
new and unexpected results. As will be described in more detail
hereinafter, the process of the invention is effected using a UHT direct
steam injection apparatus as used in the dairy industry. For example, one
type of such apparatus used for ultrapasteurization is the direct heating
plant in which high pressure potable steam is mixed with the liquid milk
product by injecting the steam into the liquid milk product. More
specifically, a Tetra Pak VTIS direct steam injection system for UHT
pasteurization is used, as described hereinafter. See Tetra Therm Aseptic
VTIS Direct UHT treatment module based on steam injection, ®1 996,
Tetra Pak Processing Systems AB, Lund, Sweden. The water added to
the liquid milk product is then removed by evaporation, usually under
reduced pressure, which also cools the product. The direct steam
injection apparatus provides a continuous ultrapasteurization process.
In a specific embodiment of the invention, the
ultrapasteurized milk concentrate is produced in a series of process steps.
First, a high solids condensed skim milk (HSCS) is prepared by
pasteurizing under vacuum conditions. HSCS and cream are mixed to
form about 1 ,000 to 4000 gallons in a batch tank of a condensed liquid
blend having a preselected fat content. A special stabilizer mixture is
mixed with warm water under high shear mixing conditions to form a
unique stabilizer slurry which is added to the condensed liquid blend to
ensure production of a final liquid milk concentrate that will provide a
reconstituted milk beverage having the desired taste and milk
characteristics. Vitamin A Palmitate and Vitamin D3 are added to the
batch, which is then ultrapasteurized and homogenized. The resultant
ultrapasteurized milk concentrate is then held in sterile tanks until
packaging in an aseptic filler. The ESL milk concentrate of the invention
has a refrigerated shelf-life of below about 45°F for at least about 30
days or preferably about 4 months. The aseptic milk concentrate has a
shelf life of at least about 30 days, or preferably about 4 to 6 months,
when stored at a temperature of less than about 85°F. The HSCS milk
and cream are sources of milk-derived carbohydrates, proteins, and
minerals. In addition, the cream brings the desired milk fat content to the
UHT pasteurized milk concentrate of the invention.
The process parameters are controlled to maintain the milk
solids nonfat content in the HSCS within a critical range and the novel
stabilizer system under ultrapasteurization conditions to produce an
ultrapasteurized milk concentrate having substantially uniformly
distributed milk constituents of at least about 30% by weight MSFN,
preferably about 35 to about 45% by weight MSNF that do not separate.
And for the first time such a milk concentrate can be reconstituted with
water within an available juice or other beverage dispensing system to
yield a reconstituted milk product that has the same characteristics of and
tastes like fresh milk.
The starting pasteurized skim milk may be acquired in the
market place. Alternatively, the initial pasteurization process in a specific
embodiment of the invention is continuous and treats a skim milk (less
than 0.5% fat content) at a flow rate of 3000 gal/hr. The milk is first
preheated for 10 minutes + /- 30 seconds at a temperature of about
1 50°F within a temperature range of 1 44°F to 1 52°F. The preheated
milk is then pasteurized at about 1 80° + /- 2°F for 1 6-22 seconds and
held for 1 0 minutes + /- 30 seconds under a vacuum of 23 + /-
0.5 inches of mercury with an air temperature of about 1 45°F. After
pasteurization, the HSCS is directed through a plate cooler for 3 minutes
at a flow rate of 800 to 1 ,000 gal/hr where it is cooled to a temperature
of less than 40°F.
Heating the milk under vacuum evaporates liquid and thus
produces the desired high solids intermediate condensed skim milk, which
includes preferably about 35.0 to 45.0% milk solids nonfat (MSNF), or
more, by weight as required for further processing. A lower MSNF
content of less than about 30% will not produce an ultrapasteurized milk
concentrate required to produce the novel milk beverage of the invention
when reconstituted with water. A higher MSNF greater than about 45%
may produce excessive viscosity of and "burn-on" in the final liquid milk
concentrate as it moves through the ultrapasteurizing equipment.
After the initial pasteurization, the intermediate HSCS milk
concentrate is mixed with cream having a fat content in the range of from
about 36% to about 45% to form a condensed liquid blend in a batch
tank having a capacity of at least 750 gallons. Stabilizer material is then
added to the batch of condensed liquid blend to form a final liquid milk
concentrate to be subsequently ultrapasteurized. The stabilizers are first
mixed under high shear conditions with warm water having a temperature
of 95 + /- 5°F (90° to 1 00°F), preferably about 75°F ± 5°F. The
resultant stabilizer slurry includes a stabilizer content as stated above.
The initial stabilizer mixture composition used in forming the
slurry of the invention consists essentially of sodium hexametaphosphate
in the range of 97.0-99.0% and carrageenan (kappa type) in the range of
1 .0-3.0%. The stabilizer slurry is formed by metering the stabilizer
mixture and water into a high shear liquefier blender and mixing it for
about 1 5 minutes to get the stabilizer material into solution. If the
stabilizer is not solubilized, it will not be evenly distributed in the slurry
and as required in the final ultrapasteurized milk concentrate of the
invention. The desired amounts of Vitamins A Palmitate (250 ml) and D3
(1 00 ml) are added to the stabilizer slurry during the blending step. The
slurry mixture is then pumped into the batch tank and intermixed with the
condensed liquid blend of HSCS milk and cream. The viscosity of the
final liquid milk concentrate before ultrapasteurization is 300 to 400
centipoises at about 40° to 45°F. After UHT treatment, the viscosity of
the UHT milk concentrate is about 1 000 to 1 500 centipoises at about
40° to 45°F.
Four milk classifications exist in the industry as designated
by the government in terms of the percentage of the milk solids fat
content as Full Fat (3.25% Fat); Reduced Fat (2.00% Fat); Low Fat
(1 .00% Fat); and Fat Free (Skim,) ( < .21 % Fat). The composition of the
final liquid milk concentrate of the invention varies depending on the
percentage of fat content desired in the reconstituted milk beverage. The
percentage of milk solids, nonfat in each final liquid milk concentrate is
at least about 30% to attain at least 8.25% milk solids nonfat content in
the reconstituted milk beverage made with the UHT milk concentrate of
the invention. The percentage of stabilizer solids in the milk concentrate
of the invention in each instance is less than one percent. The following
Table I shows the total solids calculated for the UHT pasteurized milk
concentrate of the invention based on the concentrate being reconstituted
with water in a water to concentrate volume ratio of 3 parts of water to
one part milk concentrate.
TABLE
The following Table II shows the percentage of fat, MSNF,
and total solids in reconstituted milk beverages with the characteristics
and tastes like any of the four types of fresh milk made by mixing water
with the liquid milk concentrate of Table I in a water to concentrate
volume ratio of 3: 1 .
TABLE
A beverage dispenser manufactured by Wilshire bearing the
trademark QUANTUM 4000 operates with a plastic bag package
containing the liquid milk concentrate of the invention. A peristaltic pump
draws the concentrate from the package and discharges it through a
dispensing nozzle to mix it with water flowing at a rate effective to
reconstitute the concentrate at a mixing ratio of parts of water to parts
of concentrate in a volume ratio range of from about 3: 1 to about 4: 1 .
The reconstituted milk beverage has the characteristics of and tastes like
fresh milk.
In another specific embodiment, for example, the
concentrated milk is loaded into a 300 gallon tri-wall aseptic bag-in-box
using an INTASEPT bulk bag-in-box to connect to a steam sterilized
connector that pierces the exit port on the aseptic 300 gallons in the box.
This allows the concentrated milk to retain its aseptic atmosphere when
penetrated by the sterile connector. The concentrated sterile milk is then
unloaded into a sterile blending tank that holds a combination of 2,000
gallons of both sterile water and concentrated milk. The sterile
concentrated milk and water are mixed together in the blending tank at
the proper mix ratio to reconstitute the milk to regular strength milk. The
milk is still in a sterile atmosphere. The regular strength milk is then
pumped into a sterile surge holding tank until being pumped to a dairy
packaging machine where the product still remains in a sterile
atmosphere. It is then packaged in paper milk cartons.
The 300 gallon bag-in-box has at least a 30 day shelf life,
and more preferably at least 4 months, from the date of manufacturing.
The paper retail package would have the remaining shelf life of at least
about the 90 days minus the time from date of manufacturing to the date
the 300 gallon bag-in-box is processed for retail packaging. Since the
concentrated aseptic milk has remained in a USDA approved aseptic
system, the product does not have to be re-pasteurized. As a new and
unexpected result, this system allows for a dairy to be established
anywhere in the world that local laws permit at a minimum expenditure
compared to regular dairies.
Another embodiment of this process to produce an aseptic
shelf stable UHT milk concentrate of the invention starts with a liquid
milk concentrate having a nonfat milk solids content in the range of from
about 30% to about 45% by weight with an optimum content range of
about 36% to 40% by weight to ultimately produce a reconstituted milk
beverage by mixing about 3 to 4 parts water to one part of the UHT milk
concentrate. The industry-wide fat content classification of the different
types of milk is from less than 0.21 % up to 3.25% by weight of
butterfat thus including fat free ( < .21 % fat content) milk, low fat ( 1 %
fat content) skim, reduced fat (2% fat content) milk and full fat (3.25%
fat content) milk. So, depending on the particular classification desired
in the reconstituted milk beverage of the invention, a sufficient amount
of cream may be mixed with the starting liquid milk concentrate to
provide a condensed liquid milk blend having a sufficient amount of fat
content effective to form a reconstituted milk beverage having a fat
content of from less than 0.21 % up to 3.25% by weight of the
reconstituted milk beverage when the ultrapasteurized liquid milk
concentrate is reconstituted with water. If a no fat product is desired, no
cream or fat is needed in the mixture. The following Examples 1 -5
further illustrate the practice of the invention. Vitamin A and D
concentrate is added in a minor amount to the ingredients.
EXAMPLE 1
Skim white Milk (mix ratio 4. Ox)
1 % White Milk (mix ratio 3.7x)
EXAMPLE 3
2% White Milk (mix ratio 3.25x)
EXAMPLE 4
Whole White Milk (mix ratio 3. Ox)
In the Examples 1 -5, a stabilizer is first prepared for adding
to the liquid milk concentrate to form the condensed liquid milk blend that
is to be ultrapasteurized. In these examples, one (1 ) pound of stabilizer
consisting of sodium hexametaphosphate and carrageenan (kappa type)
is mixed with two (2) pounds of warm water (70° F minimum). The
resultant mixture is then blended together in a high shear blender for 1 5
minutes to form a stabilizer slurry, which is then mixed with the initial
liquid milk concentrate for at least 15 minutes to produce the condensed
liquid milk blend that is to be UHT pasteurized. The stabilizer in the
examples is a slurry in water of about 1 -2% of the total weight of the
condensed liquid milk blend which may include cream, flavor, juice
concentrate, sweetener, etc. Up to about 10% by weight of the UHT
milk concentrate product may contain a flavor, sweetening agent or juice
concentrate. In the case of these products the fresh milk taste still
dominates the product upon reconstitution with a flavored, sweetened or
juice note added to the product. Such flavors or sweetening agents are
selected from the group consisting of caramel, vanilla, hazelnut, cocoa,
coffee extract, peach, strawberry, chai tea, vanilla chai, sucralose,
aspartame, corn syrup and fructose. Fruit or juice concentrates are
selected from the group consisting of peach, orange, strawberry and
grape.
The condensed liquid milk blend, with stabilizer and other
ingredients, of Examples 1 -5 is then continuously run through a Tetra Pak
VTIS direct steam injection UHT pasteurization system that uses a
prewarming step of about 1 80°F for about 30-36 seconds and then heats
the milk to a temperature range of from about 288°F to about 294°F for
2.5 to 5 seconds. In these examples, the ultrapasteurizing temperature
is about 294°F. The UHT milk concentrate is then sent to a cooling
condenser, which cools the concentrate to a temperature of from about
80°F to 90°F within about 2 to 5 seconds. The UHT milk concentrate
is then run through a high-pressure homogenizer, preferably at about
3500 to 5000 psi, or as low as 1 500 psi and sent to an aseptic bag filler
machine that sterilizes the bag with steam before it is filled with the
sterilized UHT milk concentrate. The nozzle and inside lip of the bag is
sprayed with H2O2. The final product is checked for proper milk solids
and fat content as well as the proper pH level of about 6-8. The milk
concentrate of these examples includes a total milk solids content of from
about 40% to about 46% by weight when it is running through the direct
steam injection system, homogenizer, and cooling condenser.
The milk products of Examples 1 -5, after dilution with water
at the mix ratios, when tested for sensory characteristics by consumers,
all satisfy the requirements of a fresh milk product. The UHT milk
concentrate and the reconstituted product do not exhibit any visible
separation or coagulation or change in color. The aroma and taste satisfy
the further characteristics of fresh milk without the negative attributes of
"cooked", "scorched", "burnt", etc., as described above. Furthermore,
the products have the texture and mouth feel of fresh milk without the
defects for milk products which may be described as watery, thin,
coagulated, sandy, gritty or separated.
While the ULTRA-HIGH TEMPERATURE MILK
CONCENTRATE, PACKAGE, DISPENSER AND METHOD OF PRODUCING
SAME have been shown and described in detail, it is obvious that this
invention is not to be considered as limited to the exact form disclosed,
and that changes in detail and construction may be made therein within
the scope of the invention without departing from the spirit thereof.
WHAT IS CLAIMED IS: