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Title: Sensitive substance
encapsulation
United States Patent: RE40,059
Issued: February 12, 2008
Inventors: Pacifico; Carl
J. (West Milford, NJ), Wu; Wen-Hsin (Middletown, NY), Fraley; Marta (Parksville,
NY)
Assignee: Balchem Corporation
(New Hampton, NY)
Appl. No.: 09/996,636
Filed: November 29, 2001
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Training Courses -- Pharm/Biotech/etc.
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Abstract
A process for stabilizing a sensitive
substance; (a) plating a sensitive substance onto a solid carrier under a
controlled atmosphere to reduce loss of the sensitive substance; (b)
encapsulating the plated material under controlled atmosphere and airflow
to reduce volatilization during the process and stabilize the sensitive
substance.
Description of the
Invention
More than one reissue application has
been filed for U.S. Pat. No. 6,251,478. The reissue applications are U.S.
Ser. No. 09/996,636 (the present application) and U.S. Ser. No.
10/776,035, both of which are divisional reissues of U.S. Pat. No.
6,251,478..Iaddend.
FIELD OF THE INVENTION
The present invention relates to the encapsulation and stabilization of
volatile, and temperature and oxygen sensitive substances.
BACKGROUND OF THE INVENTION
Three are many materials that exist in nature, or are synthesized, that
have low stability under ambient conditions. These materials may
decompose, disassociate, lose viability, etc. through reaction with oxygen
present in the atmosphere, or losing essential components by
volatilization at ambient and elevated temperatures. Examples include
flavors, flavor compounds, aromas, fragrances, vitamins, nutrients (such
as omega 3 oils, carotenoids, vitamin A and E), alcohols, acetones,
ketones, aldehydes, organic acids, antioxidants, biologically active
substances etc., hereinafter referred to as sensitive materials.
Sensitive materials may have single or multiple components that can be
categorized based on their level of volatility. Components that reach the
boiling point at low temperatures are categorized as having high
volatility, high notes or top notes. An example of a low boiling point
component is diacetyl (2,3-Butanedione) with a boiling point of 88.degree.
F. (water has a boiling point of 212.degree. F.) Diacetyl is used to bring
the characteristic dairy flavor in butter, coffee, and vinegar.
Volatile materials may comprise a single low boiling point component or
may comprise a mixture of low, medium and/or high boiling components. The
medium and low notes are not volatile at ambient or elevated temperatures
(250.degree. F. and above), and are therefore generally unaffected by
atmospheric conditions or elevated processing temperatures. Loss of the
high notes in volatile materials very often results in a finished product
that is out of balance.
The high notes of volatile materials are the most sensitive portions of
the product. High notes can be lost through volatilization which is
accelerated at temperature above 40.degree. F. Loss of high notes can also
occur during storage, incorporation in a food product, processing of a
food product, and storage of that food product even under frozen
conditions.
There have been attempts to overcome the problems associated with
maintaining high notes in a formulation. For instance, over formulation is
used to supply the high notes (high volatiles) in greater quantities to
compensate for the losses. However, this solution does not address the
relative concentrations of differing volatile compounds in the original
product versus the resulting product. Furthermore, it is difficult to
anticipate how much of the high notes will be lost. In addition, high
notes are lost over a period time and the amount of loss can depend on
temperature, so that the composition of the volatile material is
constantly changing.
Another approach to delivering a balanced composition of high, medium, and
low notes has been through encapsulation technology. Early attempts used
spray drying and spray chilling technologies to stabilize the flavor and
fragrance compositions. With spray drying, a volatile substance is first
emulsified in an aqueous solution of a water-soluble protective colloid,
such as gelatin, and carbohydrates (e.g. gum arabic, starch, dextrin. The
emulsion is then sprayed into a column of heated air or gases to evaporate
the water. The resulting dry particles have a water-soluble shell or
capsule of the water-soluble colloid in which the volatile substance, such
as a flavor, is embedded or encapsulated in the form of minute droplets.
Spray chilling is differentiated from spray drying by having the emulsion
being sprayed into a column of ambient or chilled air.
U.S. Pat. No. 3,857,964 teaches controlled release flavor compositions
which comprise flavor particles having an outer coating of a
physiologically inert, water-softenable and swellable material. Flavor
particles may be formed by adding and stirring volatile agents, such as
cyclic acetal compounds, into a polymeric material. The resulting flavor
particles are then coated by stirring them into a sodium alginate
solution, passing them through a size-limiting orifice into a room
temperature bath of calcium lactate solution.
U.S. Pat. No. 5,607,708 relates to an encapsulated flavoring material
formed of an edible, oil-insoluble, water-soluble outer shell surrounding
an edible, water-insoluble inner core that is liquid at a temperature of
about 45.degree. C. and contains a volatile, oil-soluble flavoring
material dissolved or dispersed in the inner core. Materials suitable for
the outer shell include gelatin, water soluble gums, starches or dextrins.
The cover material may be an unsaturated vegetable oil, fat and/or
partially hydrogenated oil or fat. It is important during the manufacture
of the core materials that the material have a relatively low melting
point so that the volatile components may be mixed with this material at
low temperatures, thereby minimizing the loss of the volatile component.
Coannular centrifugal extrusion methods may be used to form particles of
the core material and simultaneously to coat them with the shell material.
Coannular extrusion means are used in U.S. Pat. No. 5,399,368 to produce
coated materials in which volatile materials, such as coffee oil, are
entrained.
U.S. Pat. No. 5,874,102 teaches encapsulated fatty acid salt products
comprising a core material coated with continuous film that serves as a
barrier to volatile compounds contained in the core matrix. The particles
may then be coated by direct spraying means. Direct spraying of a
volatile-containing core material by an aqueous solution of first and
second coagulating agents is also shown in U.S. Pat. No. 5,558,889. U.S.
Pat. No. 5,004,595 teaches the production of similar coated particles
using a fluidized bed process.
U.S. Pat. No. 4,689,235 discloses an encapsulating matrix composition that
is extrudable at a pressure in the range of 1 to 10 atm and having an
improved loading capacity up to 40% comprising maltodextrin and hydrogen
octenylbutanedioate amylodextrin. The matrix may contain from 5 to 40 wt.
% of a normally liquid or volatile active ingredient which is added in a
tank having heating and agitating means.
U.S. Pat. No. 4,576,826 relates to a method for producing flavorant
capsules by forming a stable emulsion of an edible oil and an aqueous
essence. The emulsion is directly sprayed or dropped in a dropwise manner
onto an agitated powdered edible protein, carbohydrate or mixture thereof
to form capsule shells thereon. Frozen essences may be utilized in the
form of frozen particles which are added to the coating material prior to
curing.
While spray drying and spray chilling were able to transform a liquid
flavor into a solid particle, they also had inherent limitations such as
the use of large volumes of air. Compounds sensitive to oxygen in air will
begin to oxidize and decompose. For example, materials with multiple
double bonds such as conjugated linoleic acid, omega 3 oils, fish oils, as
well as anaerobes and facultative anaerobes such as, but not limited to,
Bifidobacterium sp., and Lactobacillus sp., will lose potency or activity
after exposure to oxygen. Additionally, heat is involved in both processes
that will cause almost complete volatilization and/or oxidation of the low
boilers or sensitive materials even with over formulation.
SUMMARY OF THE INVENTION
An object of the present invention is to provide a method for the
encapsulation of temperature/oxygen sensitive materials including flavors,
fragrances, nutrients, colors, anaerobic bacteria, and products with
similar characteristics without the loss of volatile portions due to
reaction with oxygen or elevated temperatures.
A further object of the present invention is to provide protection and
prevent undesirable oxidation of alcohols, acetones, ketones, aldehydes,
organic acids, and antioxidants.
A further object of the present invention is to provide improved stability
of biologically active compounds which include Lactobacilli,
Bifidobacterium, Enterococci, phytase, amylases, lipases, invertases,
transglutaminases, proteases, lipoxygenases and pentosanases.
The present invention is directed to an encapsulation technique whereby "topnotes"
or sensitive substances, which do not typically survive current
encapsulation process such as spray drying, spray chilling, and fluid bed
technologies, are captured and stabilized.
The invention is directed to a method of encapsulating a sensitive
substances some of which require: plating the volatile material onto a
solid carrier, in an atmosphere inert to the volatile material, to form a
plated material; and encapsulating the plated material.
DETAILED DESCRIPTION OF THE INVENTION
A sensitive substance such as a volatile liquid material is first plated
onto a solid carrier in a sealed reactor. The reactor is then filled with
nitrogen, carbon dioxide, or any other suitable gas inert to the sensitive
substance to displace any unconditioned air. Then the plated material is
encapsulated either in the same vessel in which the plating occurred or in
another vessel.
The carrier is placed in a vessel capable of being sealed and supporting
mechanical mixing. Preferably the mechanical mixing creates a fluidized
bed. The vessel is then sealed and then oxygen is displaced through the
introduction of an inert gas. Suitable gases include, but are not limited
to, carbon dioxide, nitrogen, and helium. The inert gas also acts as a
blanket. The inert gas is selected so that it will not react with the
volatile material or the carrier. The carrier material is then agitated.
A liquid material (oxygen sensitive liquid material) is then agitated to
ensure a fully homogenized mire. Without exposing the liquid material to
air or oxygen, the liquid material is then supplied, e.g. pumped, into the
sealed vessel and introduced into the vessel by a nozzle. The nozzle is
used to form small droplets that are more easily absorbed onto the carrier
material. The time involved in spraying is dependent upon the addition
level of the liquid onto the solid and the time required to ensure
complete absorption to form a free flowing powder. While the volatile
liquid material is being added, the carrier is agitated or mixed to ensure
even distribution of the liquid material onto the solid carrier.
A typical volatile liquid material has a boiling point between about
40.degree. F. and about 250.degree. F., preferably about 50.degree. to
about 100.degree. F., and more preferably about 60.degree. to about
80.degree. F. Examples of volatile materials also include, but are not
limited to, flavors, flavor compounds, aromas, fragrances, vitamins,
nutrients (such as omega 3 oils, carotenoids, vitamin A and E), alcohols,
acetones, ketones, aldehydes, organic acids, antioxidants, and essential
oils. Examples of volatile materials are: lemon oil, spearmint oil,
vanilla extract, garlic oil, cinnamon extract and other essential oils
derived from botanical origins.
Other sensitive materials include biologically active compounds which
include, but are not limited to, Lactobacilli, Bifidobacterium,
Enterococci, phytase, amylases, lipases, invertases, transglutaminases,
proteases, lipoxygenases and pentosanases.
The carrier may be any porous or semi porous material such as, but not
limited to, maltodextrin, dextrins silicon dioxide, starches, gums or
hydrocolloids. The carrier is selected based upon its ability to entrap
the liquid material. Suitable carriers include, but are not limited to,
the following. N-ZORBIT M which is a tapioca maltodextrin derived from
tapioca and K-4484 which is a tapioca dextrin with high solubility, good
clarity, and bland flavoring. N-ZORBIT M and K-4484 are products of
National Starch and Chemical Company.
The particle size of the carrier is preferably between about 50 microns
and about 2,000 microns, preferably between about 100 microns and about
1000 microns, and more preferably between about 200 and about 500 microns.
Both the volatile liquid material and solid carrier may be edible.
Loading levels of the liquid onto the solid carrier are between about 1%
and about 70% by weight, preferably 5% to 40%, more preferably between
about 10% and about 30%, and most preferably between about 15% and about
25%. One skilled in the art would understand the amount of volatile
material needed for a particular end product. For example, garlic is very
strong and thus would require a lower loading concentration as would
cinnamon. Apple juice would likely require a higher concentration.
Prior to adding the liquid material, the carrier may be chilled by, for
example, the addition of liquid nitrogen which has a temperature between
minus 198.degree. and minus 208.degree. C. The liquid material may also be
chilled to below about 40.degree. F., and kept chilled while it is added
to the carrier. If desired, the vessel may also have a cooling jacket to
cool the vessel during the plating process.
Any suitable mixer vessel, such as a paddle mixer, ribbon blender, or
V-blender, may be used in the present invention to plate the solid onto
the carrier.
After the volatile liquid material is plated onto a solid carrier to form
a plated material, the plated material is encapsulated either in the same
vessel in which the plating occurred or in another vessel. In a preferred
embodiment, the plated material is removed from the sealed mixer and
placed in a reactor designed to encapsulate solid particles. In either
case, the encapsulation reactor must be capable of being sealed. The
reactor is then filled with nitrogen, carbon dioxide, or any other
suitable gas inert to the volatile material to displace any unconditioned
air. Preferably, the vessel has means to agitate and heat the contents of
the vessel.
Any suitable encapsulant material may be used. Preferably the
encapsulating material is a lipid material such as, but not limited to,
mono-, di-, and triacylglycerols, waxes, and organic esters derived from
animals, vegetables, minerals, and modifications. Examples include
glyceryl triesterates such as soybean oil, cotton seed oil, canola oil,
tallow and palm kernal oil, and esters of long chain fatty acids, and
alcohols, such as carnauba wax, beeswax, bran wax, tallow and palm kernal
oil. The lipid material preferably has a melting point between about
60.degree. and about 200.degree. F.
Specific encapsulants include, but are not limited to, the following.
NATIONAL 46 which is a low viscosity product designed for the
encapsulation of citrus flavors, such as orange and lemon, and other
delicate flavor oils. CAPSUL which is a modified food starch derived from
waxy maize designed for encapsulation of flavors, clouds, vitamins, and
spices. N-LOK which is a low viscosity product designed for the
encapsulation of flavors, fats, oils, and vitamins. NATIONAL, CAPSUL, and
N-LOK are all products of National Starch and Chemical Company.
In a preferred embodiment, the encapsulant material is melted and the
liquefied material is then pumped into the encapsulation reactor. The flow
rate is dependent upon the type of encapsulation reactor used in the
procedure and is well within the skill of the art. The carrier containing
volatile material is fluidized in the reactor by methods known to those
who are skilled in the art such as by forcing an inert gas upward through
a bed of particles so that the particles undergo a continuous circular,
tumbling action. As the particles are fluidized, the liquefied material is
sprayed onto the fluidized particles.
The final percentage of encapsulant (coating) in the resulting
encapsulated particles is between about 10 to about 90%, preferably about
20 to about 80% and more preferably between about 30 and about 50% by
weight.
Claim 1 of 33 Claims
1. A method of encapsulating a sensitive
material comprising: .Iadd.(a) .Iaddend.plating the sensitive material
onto a solid carrier, in an atmosphere inert to the sensitive material, to
form a plated material; and .Iadd.(b) .Iaddend.encapsulating the plated
material.Iadd., wherein encapsulating comprises spraying a melted
encapsulant onto the plated material.Iaddend.. ____________________________________________
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Patent and Trademark Office Web site to access the full
patent.
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