U.S. patent application number 16/535703 was filed with the patent office on 2021-02-11 for low sodium salt composition.
This patent application is currently assigned to Salarius Ltd.. The applicant listed for this patent is Salarius Ltd.. Invention is credited to Javier Contreras, Victor Hugo Manzanilla.
Application Number | 20210037865 16/535703 |
Document ID | / |
Family ID | 1000004286546 |
Filed Date | 2021-02-11 |
United States Patent
Application |
20210037865 |
Kind Code |
A1 |
Contreras; Javier ; et
al. |
February 11, 2021 |
LOW SODIUM SALT COMPOSITION
Abstract
Salt particles adhered to a bulk carrier of the present
invention are improved over prior alternative salts by having
smaller salt particles adhered to a bulk carrier are achieved
through modifications of variables for production of salt adhered
to carrier particles, including starting solid composition,
salt-carrier slurry composition, inlet and outlet drying
temperature, slurry temperature, and moisture content control. The
resulting salt-carrier product of salt adhered to carrier particles
can be produced with much smaller salt particles of about 100
nanometers to less than 2 microns adhered to a carrier, which in
turn improves electrostatic forces that help the salt-carrier
product better adhere to and coat a food product than salts not
adhered to a carrier particle.
Inventors: |
Contreras; Javier;
(Alpharetta, GA) ; Manzanilla; Victor Hugo; (Boca
Raton, FL) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Salarius Ltd. |
London |
|
GB |
|
|
Assignee: |
Salarius Ltd.
London
GB
|
Family ID: |
1000004286546 |
Appl. No.: |
16/535703 |
Filed: |
August 8, 2019 |
Current U.S.
Class: |
1/1 |
Current CPC
Class: |
A23L 19/18 20160801;
A23L 27/40 20160801; A23L 25/25 20160801; A23L 7/122 20160801; A23V
2002/00 20130101; A23L 3/46 20130101 |
International
Class: |
A23L 27/40 20060101
A23L027/40; A23L 3/46 20060101 A23L003/46; A23L 19/18 20060101
A23L019/18; A23L 25/00 20060101 A23L025/00; A23L 7/122 20060101
A23L007/122 |
Claims
1. An improved method of making a low-sodium, salt-carrier product
having less sodium per unit volume than an equivalent unit volume
of sodium chloride, comprising: providing an aqueous salt-carrier
slurry comprising an aqueous solvent and a selected percent by
weight of a solids mixture, wherein the solids mixture comprises
salt and a carrier medium, and wherein the carrier medium is
present in an amount between about 2.77% by weight and less than
25% by weight of the aqueous solvent, and wherein the salt is
present in an amount between about 3.9% by weight and less than 25%
by weight of the aqueous solvent; and exposing the slurry to a
drying process to both: A) form a carrier particle comprised of the
carrier medium; and B) form a plurality of salt particles of less
than about 100 nanometers to less than 2 microns on the surface of
the carrier particle.
2. The method of claim 1, wherein the drying process is spray
drying, spray cooking, freeze drying or roll drying.
3. The method of claim 1, wherein the unit volume of sodium
chloride and the unit volume of the salt alternative composition
produce an approximately equivalent salt taste.
4. The method of claim 1, wherein the carrier medium is a bulking
agent, carbohydrate or its derivative, starch, maltodextrin,
hydrocolloid, protein, protein derivative, yeast extract, flavor
enhancer, or lipid.
5. The method of claim 4, wherein the protein derivative is a
protein derived from soy, wheat, or whey.
6. The method of claim 4, wherein the carbohydrate or its
derivative is one or more of maltodextrin, starch, pre-gelatinized
starch, modified starch, pyrodextrin, gum, cereal flour, or tuber
flour.
7. The method of claim 1, wherein the salt is one or more of sodium
chloride, potassium chloride, magnesium chloride, ammonium
chloride, or magnesium sulfate.
8. The method of claim 4, wherein the drying process comprises
spray-drying using a spray drier inlet temperature between about
360.degree. F..+-.25.degree. F. and a spray dryer outlet
temperature of 200.degree. F..+-.25.degree. F.
9. The method of claim 8, wherein: the aqueous slurry comprises the
salt plus the carrier in an amount of about 10% to 36% by weight of
the aqueous salt-carrier slurry and salt in an amount about 2.5% to
less than 25% by weight of the aqueous salt-carrier slurry, wherein
the aqueous salt-carrier slurry is prepared by heating the salt,
the carrier, and water to a temperature of about 176.degree.
F..+-.10.degree. F. until the water, salt, and carrier are
substantially dissolved to a moisture content of about 1.2% to
5%.
10. The method of claim 9, further comprising pumping the aqueous
slurry through a nozzle to control moisture content to 1.2% to
5%.
11. An improved salt-carrier product formed by a process
comprising: providing an aqueous salt-carrier slurry comprising an
aqueous solvent and a selected percent by weight of a solids
mixture, wherein the solids mixture comprises salt and a carrier
medium, and wherein the carrier medium is present in an amount
between about 2.77% by weight and less than 25% by weight of the
aqueous solvent, and wherein the salt is present in an amount
between about 3.9% by weight and about 42% by weight of the aqueous
solvent; and exposing the aqueous salt-carrier slurry to a drying
process to both: A) form a carrier particle comprised of the
carrier medium; and B) form a plurality of salt particles of an
average size of less than about 100 nanometers to less than 2
microns on the surface of the carrier particle.
11. The salt-carrier product of claim 10, wherein the carrier
medium is maltodextrin and the drying process is a freeze drying,
spray drying, spray cooking, or roll drying process.
12. The salt-carrier product of claim 11, wherein the salt is a
salt of sodium, chloride, potassium, or sulfate ion.
13. The salt-carrier product of claim 12, wherein the carrier
medium is a bulking agent, carbohydrate or its derivative,
hydrocolloid, protein, protein derivative, yeast extract, flavor
enhancer, lipid, mineral, or salt.
14. The product of claim 13, wherein the carrier media comprises
two or more different medium materials.
15. The product of claim 13, wherein the interior portion of the
carrier particle is substantially devoid of the salt crystals.
16. The salt-carrier product of claim 11, the aqueous salt-carrier
slurry comprises the salt plus the carrier in an amount of about
10% to 36% by weight of the aqueous salt-carrier slurry and salt in
an amount about 2.5% to less than 25% by weight of the aqueous
salt-carrier slurry, wherein the aqueous salt-carrier slurry is
prepared by heating the salt, the carrier, and water to a
temperature of about 176.degree. F..+-.10.degree. F. until the
water, salt, and carrier are substantially dissolved to a moisture
content of about 1.2% to 5%.
17. The salt-carrier product of claim 16, wherein the salt carrier
product adheres better adheres to foods than salt that is not
adhered to a carrier particle.
18. The salt-carrier product of claim 17, wherein the foods are
potato chips.
19. The salt-carrier product of claim 17, wherein the foods are
corn chips.
20. The salt-carrier product of claim 17, wherein the foods are
nuts.
Description
FIELD OF THE INVENTION
[0001] This invention relates to food ingredients. In particular,
this invention relates to food additives and ingredients that
provide a low-sodium alternative to salt, e.g., sodium chloride, or
"table salt." More specifically, this invention provides for salt
particles adhered to a bulk carrier that provides a desired salt
flavor using a reduced amount of sodium chloride as compared to
conventional table salt. The salt particles adhered to a bulk
carrier of the present invention are improved over prior
alternative salts by having smaller salt particles adhered to a
bulk carrier, which in turn, results in increased electrostatic
forces that enable the alternative salt particles to adhere better
to food. This disclosure also relates to improved methods for
making the improved low-sodium salt alternatives having salt
particles adhered to bulk carriers.
BACKGROUND
[0002] Table salt (sodium chloride) provides a taste that humans
and other animals generally enjoy. Too much sodium, however, is
known to cause certain adverse health effects such as high blood
pressure and heart disease. Salt is a common ingredient used in
food preparation and is also used as a condiment for finished foods
such as cooked meats, vegetables, and snacks, e.g., popcorn.
Processed and "fast food" items often contain high levels of salt
to provide a desirable taste to the consumer; however, the short
term benefit of so-called convenience foods can come with
long-term, increased risk of heart attack or stroke. While the
human body may require a salt for electrolyte balance and other
physiological processes, in many cases people ingest sodium at
levels that can be deleterious to their health.
[0003] Too much salt in the diet can give rise to adverse health
consequences, e.g., high blood pressure which is a risk factor for
stroke. As U.S. Pat. No. 9,491,961, noted, UK Government figures
indicate that the average intake of salt per person is
approximately 6.0-9.0 grams per day. However, the UK Government
recommended maximum is 3 grams per day. Currently in the U.S.,
according to the FDA, the average adult consumption of sodium is
3,400 mg per day. As a result, according to the Centers for Disease
Control, about 90% of Americans consume too much sodium. According
to a 2019 study by the National Academy of Engineering, Sciences
and Medicine, for individuals ages 14 and older, they recommend
that individuals reduce sodium intakes if above 2,300 mg per
day.
[0004] According to the World Health Organization, cardiovascular
disease takes the lives of 17.9 million people per year and is
responsible for 31% of global deaths. According to the Centers for
Disease Control, "About 610,000 people die of heart disease in the
United States every year--that's 1 in every 4 deaths." In the U.K.,
there are about 160,000 deaths from heart disease each year
accounting for 26% of all deaths.
[0005] Clearly, a significant reduction by approximate 50% of
current sodium consumption would be beneficial to human health and
would save lives.
[0006] In principle, one way of reducing the amount of salt in a
food product would be to mill the salt to give a very large surface
area which should mean that the same "seasoning level" may be
achieved using a lower amount of salt. However, as noted in U.S.
Pat. No. 9,491,961, salt is hygroscopic and the finely milled salt
quickly re-agglomerates unless protected using expensive or complex
storage systems which would add additional cost to what is
otherwise a commodity product.
[0007] U.S. Pat. No. 9,491,961 noted that another possibility is to
replace at least a portion of the salt with a substitute.
Alternatives to sodium chloride include the use of magnesium and
potassium chlorides but these impart a bitter or metallic taste
which is not generally acceptable to consumers. Furthermore the use
of potassium and magnesium ions also affects neurons and can lead
to changes in blood pressure. Other substitutes include organic
molecules, such as monosodium glutamate (MSG), peptides and nucleic
acid based substitutes. However these have their own problems.
Thus, for example, there is a reported cancer risk associated with
MSG. Additionally the substitutes may affect texture of the final
finished food product and may have a potential to induce allergic
responses. As a consequence, salt substitutes have replaced one
"problem" with other issues and as a consequence found resistance
within the food manufacturer sector and among public driven
pressure groups.
[0008] Other solutions to this problem include producing
alternative salt products comprising salt adhered to carrier
particles. These salt-carrier products result in lower-sodium salt
compositions that impart a salty taste with less sodium content
than an equivalent volume of sodium chloride itself.
[0009] For example, U.S. Pat. No. 9,491,961 describes a method of
preparing a salt product that comprises the steps of: (i) providing
a mixture which comprises salt dissolved in a solvent, the mixture
further containing an organic material that is solid under ambient
temperature conditions; and (ii) atomizing the mixture and
evaporating the solvent to produce a salt product comprised of
individual crystallites of salt attached to hollow particles of
organic material. The organic material may be a polymer such as a
carbohydrate (e.g., maltodextrin or Gum Arabic). More than 95% of
the resulting salt-carrier product particles produced using the
methods described in U.S. Pat. No. 9,491,961 had a size of less
than 50 microns.
[0010] U.S. Pat. No. 8,900,650 describes a salt composition
including a carrier particle having disposed thereon a plurality of
salt crystallites. The methods include providing an aqueous slurry
comprising an aqueous solvent and a selected percent by weight of a
solids mixture, wherein the solids mixture comprises salt and a
carrier medium, and wherein the carrier medium is present in an
amount between about 25% by weight and about 75% by weight of the
aqueous solvent; and exposing the slurry to a drying process to
both: a) form a carrier particle comprised of the carrier medium;
and b) form a plurality of salt particles of an average size of
less than about 20 microns on the surface of the carrier particle,
with the salt particles on the surface of the carrier particle
having an average size ranging from 100 nanometers to less than 2
microns.
[0011] The salt-carrier product described in U.S. Pat. No.
8,900,650 can be a bulking agent, carbohydrate or its derivative,
starch, maltodextrin, hydrocolloid, protein, protein derivative,
starch, pre-gelatinized starch, modified starch, pyrodextrin, gum,
cereal flour, or tuber flour yeast extract, flavor enhancer, or
lipid. The drying process can include freeze drying, spray drying,
spray cooking, or roll drying process.
[0012] When applying these salt-carrier products to food, it is
important that they coat the food well. As explained below, the
inventors have determined that by altering the variables for
production of salt adhered to carrier particles, including starting
solid composition, salt-carrier slurry composition, inlet and
outlet air drying temperature, slurry temperature, and moisture
content control, the resulting salt-carrier product of salt adhered
to carrier particles can be produced with much smaller salt
particles of about 100 nanometers to less than 2 microns adhered to
a carrier, which in turn improves electrostatic forces that help
the salt-carrier product better coat a food product.
SUMMARY OF THE INVENTION
[0013] In a first aspect, an improved method of making a
low-sodium, salt-carrier product having less sodium per unit volume
than an equivalent unit volume of sodium chloride, is provided
comprising an aqueous salt-carrier slurry comprising an aqueous
solvent and a selected percent by weight of a solids mixture,
wherein the solids mixture comprises salt and a carrier medium, and
wherein the carrier medium is present in an amount between about
2.77% by weight and less than 25% by weight of the aqueous solvent,
and wherein the salt is present in an amount between about 3.9% by
weight and less than 25% by weight of the aqueous solvent; and
exposing the slurry to a drying process to both: A) form a carrier
particle comprised of the carrier medium; and B) form a plurality
of salt particles of less than about 100 nanometers to less than 2
microns on the surface of the carrier particle.
[0014] In another embodiment, the drying process is spray drying,
spray cooking, freeze drying or roll drying.
[0015] In another embodiment, the unit volume of sodium chloride
and the unit volume of the salt alternative composition produce an
approximately equivalent salt taste.
[0016] In another embodiment, the carrier medium is a bulking
agent, carbohydrate or its derivative, starch, maltodextrin,
hydrocolloid, protein, protein derivative, yeast extract, flavor
enhancer, or lipid.
[0017] In another embodiment, the protein derivative is a protein
derived from soy, wheat, or whey.
[0018] In another embodiment, the carbohydrate or its derivative is
one or more of maltodextrin, starch, pre-gelatinized starch,
modified starch, pyrodextrin, gum, cereal flour, or tuber
flour.
[0019] In another embodiment, the salt is one or more of sodium
chloride, potassium chloride, magnesium chloride, ammonium
chloride, or magnesium sulfate.
[0020] In another embodiment, the drying process comprises
spray-drying using a spray drier inlet temperature between about
360.degree. F..+-.25.degree. F. and a spray dryer outlet
temperature of 200.degree. F..+-.25.degree. F.
[0021] In another embodiment, the aqueous slurry comprises the salt
plus the carrier in an amount of about 10% to 36% by weight of the
aqueous salt-carrier slurry and salt in an amount about 2.5% to
less than 25% by weight of the aqueous salt-carrier slurry, wherein
the aqueous salt-carrier slurry is prepared by heating the salt,
the carrier, and water to a temperature of about 176.degree.
F..+-.10.degree. F. until the water, salt, and carrier are
substantially dissolved to a moisture content of about 1.2% to
5%.
[0022] In another embodiment, the method further comprises pumping
the aqueous slurry through a nozzle to control moisture content to
1.2% to 5%.
[0023] In a second aspect, an improved salt-carrier product is
formed by a process comprising providing an aqueous salt-carrier
slurry comprising an aqueous solvent and a selected percent by
weight of a solids mixture, wherein the solids mixture comprises
salt and a carrier medium, and wherein the carrier medium is
present in an amount between about 2.77% by weight and less than
25% by weight of the aqueous solvent, and wherein the salt is
present in an amount between about 3.9% by weight and about 42% by
weight of the aqueous solvent; and exposing the aqueous
salt-carrier slurry to a drying process to both: A) form a carrier
particle comprised of the carrier medium; and B) form a plurality
of salt particles of an average size of less than about 100
nanometers to less than 2 microns on the surface of the carrier
particle.
[0024] In another embodiment, the carrier medium is maltodextrin
and the drying process is a freeze drying, spray drying, spray
cooking, or roll drying process.
[0025] In another embodiment, the salt is a salt of sodium,
chloride, potassium, or sulfate ion.
[0026] In another embodiment, the carrier medium is a bulking
agent, carbohydrate or its derivative, hydrocolloid, protein,
protein derivative, yeast extract, flavor enhancer, lipid, mineral,
or salt.
[0027] In another embodiment, the carrier media comprises two or
more different medium materials.
[0028] In another embodiment, the interior portion of the carrier
particle is substantially devoid of the salt crystals.
[0029] In another embodiment, the aqueous salt-carrier slurry
comprises the salt plus the carrier in an amount of about 10% to
36% by weight of the aqueous salt-carrier slurry and salt in an
amount about 2.5% to less than 25% by weight of the aqueous
salt-carrier slurry, wherein the aqueous salt-carrier slurry is
prepared by heating the salt, the carrier, and water to a
temperature of about 176.degree. F..+-.10.degree. F. until the
water, salt, and carrier are substantially dissolved to a moisture
content of about 1.2% to 5%.
[0030] In another embodiment, the salt carrier product adheres
better to foods than salt that is not adhered to a carrier
particle.
[0031] In another embodiment, the foods are potato chips. In
another embodiment, the foods are corn chips.
[0032] In another embodiment, the foods are nuts.
[0033] Unless otherwise defined, all technical and scientific terms
used herein have the same meaning as commonly understood by one of
ordinary skill in the art. Although methods and materials similar
or equivalent to those described herein can be used in the practice
or testing of any described embodiment, suitable methods and
materials are described below. The materials, methods, and examples
are illustrative only and not intended to be limiting. In case of
conflict with terms used in the art, the present specification,
including definitions, will control.
[0034] The details of one or more embodiments are set forth in the
accompanying drawings and the description below. Other features,
objects, and advantages will be apparent from the drawings and
detailed description, and from the claims.
BRIEF DESCRIPTION OF THE DRAWINGS
[0035] FIG. 1 is a schematic flow diagram depicting the process for
making the improved salt-carrier product described herein.
[0036] FIG. 2 is a scanning electron micrograph (SEM) of the
improved salt-carrier product that depicts the size of the salt
particles on an example of the improved salt-carrier product
described herein.
DETAILED DESCRIPTION
[0037] For table-top or surface (sprinkle-on) applications, most
commercially available salt is not immediately soluble in saliva
because of its high density and relatively large particle size.
When these particles are sprinkled on foods for immediate
consumption or during further processing, they provide low
intensity, long lasting, spotty salty taste. Most prepared foods
are only briefly chewed and swallowed; thus, salt is sometimes
added in a relatively high concentration to compensate for
incomplete dissolution and the short mouth residence time. As a
result, a consumer may ingest salt that is still in granule form
and thereby consume far greater quantities of sodium than necessary
to achieve a desired "salty" taste.
[0038] In general, a desired level of salty flavor can be achieved,
while reducing sodium consumption, by providing small consumable
salt particles having a large surface area-to-volume ratio. In
general, the surface area-to-volume ratio of a particle increases
as the size of the particle decreases. Thus, small salt particles
provide increased interaction with saliva and sensory physiology in
the mouth, e.g., tongue, cheeks, gums, etc., which can lead to an
increased sensation of a salty taste. Because more of the salt
particle surface is exposed to saliva, the dissolution rate of salt
particles is greater as compared to regular, commercial-grade salt
particles that one may find, e.g., at a restaurant. Because the
residence time of food is relatively short in the mouth, increasing
the dissolution rate of salt particles can have a pronounced effect
on the sensation of salty taste.
[0039] As used herein, the phrases "nanometer- to micron-sized" or
"nanometer- to micron-scale" and similar phrases carry their
ordinary meaning, that is, they refer to objects having at least
one dimension of nanometer or micron scale.
[0040] As used herein, the phrases "nanometer- to micron-sized" or
"nanometer- to micron-scale" and similar phrases carry their
ordinary meaning, that is, they refer to objects having at least
one dimension of nanometer or micron scale. "Salt particles" can
refer to a specific size, e.g., a narrow size distribution of
particles, or a collection of particles of different sizes, e.g., a
mean size for a population of salt particles.
[0041] Nanometer- to micron-sized salt particles are provided for
direct application on prepared foods or in preparation of foods. In
this and other embodiments, other ingredients can be added to the
salt particles to achieve certain storage or use parameters, e.g.,
bulk density, flow, anti-caking, hydrophobicity, and other
parameters. In some embodiments, a coagulating or wetting agent may
be used to reduce the likelihood of producing an excess amount of
dust when salt particles are applied to, or used in the preparation
of foods.
[0042] In general, nanometer- to micron-sized salt particles can be
adhered to a carrier to deliver the ultra-small salt particles to
the consumer's mouth. The term "adhered" as used herein carries its
ordinary meaning: to be joined or united, or attached. The
processes involved in adhering salt particles to carriers can
include chemical ionic and covalent bonding, surface tension,
adhesion, and any other physical process that joins the two
entities.
[0043] The term "adhered" as used herein carries its ordinary
meaning: to be joined or united, or attached. The processes
involved in adhering salt particles to carriers can include
chemical ionic and covalent bonding, surface tension, adhesion, and
any other physical process that joins the two entities.
[0044] "Salt" can be any type of salt, e.g., potassium chloride or
a combination of salts. In certain preferred embodiments, "salt"
refers to salts of sodium, chloride, potassium or sulfate ions.
While the context of this disclosure focuses on providing
low-sodium products for foodstuffs, the disclosed technology can be
used for other purposes, including methods for introducing salts
into living systems for medical or veterinary applications. In
certain embodiments, the methods and products described herein can
be used in applications where rapid introduction of sodium may be
advantageous, e.g., in certain medical applications. Salts may
include certain additives, e.g., minerals or other chemical
elements; in some cases, the additives may provide certain health
benefits.
[0045] Carriers can include, without limitation, bulking agents,
cereal and tuber starches, maltodextrins, cereal and tuber flours,
hydrocolloids, proteins, protein powders, including those from any
plant or animal source, including, but not limited to cereals,
tuber, dairy and whey powders; flavors, and seasonings, among
others. Proteins can be any protein source from plant or animal,
including dairy, meat, corn, etc. Carriers can vary in size and
shape and can be processed from their original form (e.g., protein
powders can be further refined or milled to a desired size) to
provide a desired functionality, such as bulk flow or bulk density.
In some embodiments, utilizing a carrier to deliver salt particles
can provide certain packing, storage, and use benefits. For
example, a carrier can be chosen to provide a desired bulk density
for a particular salt-carrier product. In another example, a
carrier may be chosen for its bulk flow characteristics in
large-scale foods processing, or for its hydrophobic or hygroscopic
properties. Maltodextrin has been determined to be a preferred
carrier. A "salt-carrier product" refers to nanometer- or
micron-scale salt particles adhered to a carrier.
[0046] In general, salt particles can be adhered to the surface of
a carrier. The degree of salt coverage on the particle can be
varied to produce various taste effects, including adjusting the
intensity of a salty flavor. In addition, the bulk density of the
salt, e.g., sodium chloride, in a salt-carrier product can be
adjusted by controlling the salt coverage on the particle.
[0047] In general, the salt-carrier products described herein can
be agglomerated to provide desirable properties related to use,
storage, handling, and other considerations. For example, to reduce
dust, salt-carrier products can include wetting agents or other
additives to promote agglomeration of particles. Other additives
can be used for obtaining a desired bulk density, product flow,
antimicrobial, or other material handling parameter.
[0048] FIG. 1 is a schematic flow diagram of an exemplary process
for making the improved salt-carrier product. A salt-carrier
product can be made, according to one of many methods, by carrying
out the following steps, which need not necessarily be performed in
the order presented.
[0049] At step 100, a solid composition of salt and a carrier is
prepared to create a salt-carrier slurry by adding a selected
carrier, preferably maltodextrin, to water in a tank with good
agitation and heating the tank to a temperature of 176.degree.
F..+-.10.degree. F. to dissolve the carrier and then add the salt
to the tank and continuing to heat the aqueous salt-carrier
solution at a temperature of 176.degree. F..+-.10.degree. F. and
agitating it for sufficient time to ensure the salt is dissolved
and it becomes an aqueous salt-carrier slurry at step 300.
Alternatively, the salt and carrier could be combined with the
water and heated at different temperatures for different times, so
long as the salt, carrier, and water are substantially dissolved to
become an aqueous salt-carrier slurry.
[0050] The concentration of salt in the salt solution can be
adjusted to provide a desired coverage of salt on the resulting
salt-carrier product. The salt can include single salts (e.g.,
sodium chloride) or a mixture of salts (e.g., sodium chloride,
potassium chloride, ammonium chloride, etc.). The carrier can be
any bulking agent, e.g., a powdered bulking agent, including but
not limited to proteins, carbohydrates or their derivative(s)
(maltodextrin, pre-gelatinized starch, gums, cereal flours and the
like), hydrocolloids, hydrolyzed proteins, yeast extracts, and
flavorings. In some embodiments, a combination of different types
of carriers can be used, e.g., a combination of a carbohydrate, a
starch, and potassium salt can be used. The proportion of carrier
to salt can be chosen to obtain a desired working density or other
characteristic of the salt-carrier product. The salt-carrier
mixture can then be mixed until homogeneous.
[0051] Examples of solid compositions used to create the
salt-carrier slurry of the improved salt-carrier product include a
salt plus carrier percent by weight of 11% to 39.9% of aqueous
solvent (water); a salt percentage by weight of aqueous solvent
(water) of 3.9% to less than 25%; a carrier percentage of 2.77% to
24.9% by weight aqueous solvent (water); a salt plus carrier
percentage by weight of aqueous salt-carrier slurry of 10 to 39.9%;
a salt percentage by weight of aqueous salt-carrier slurry of 2.5%
to 14.9%.
[0052] At step 400, the an aqueous salt-carrier slurry fed into a
nozzle of a drying chamber that has several orifices to spray out
the slurry at different angles and drop sizes that can affect
particle sizes into a drying chamber at step 500 with particle
sizes inversely proportional to the angle aperture and directly
proportional to the orifice aperture. The inlet temperature of the
drying chamber is preferably 360.degree. F..+-.25.degree. F.
Changing the amount of slurry that is pumped through the nozzle at
step 400 can control the moisture content to 1.2% to 5%. Moisture
content is the water content of the resulting product. The amount
of slurry pumped through the nozzle into the drying chamber is
controlled through the pump and compressor while slowed by the
nozzle resistance (pressure drop).
[0053] The slurry should remain in the drying chamber until desired
moisture content is reached and either precipitates to the
collection hopper or is pulled by the cyclone as per regular Spray
Drying practices, when they exit the outlet of the drying chamber
at a temperature of 200.degree. F..+-.25.degree. F., followed by a
cyclone at step 700 that collects the smaller particles that are
too light to gravitate on the drying chambers hopper, a step
particularly important as particle sizes of this process generates
more smaller particles than typical spray drying processes. There
is a suction blower/scrubber process at step 750 and a bagger
process at step 800 that bags the resulting salt-carrier
particles.
[0054] The salt-carrier mixture can then be subjected to a process
to drive off (evaporate) water. In general, it can be advantageous
to drive off water quickly, so as to reduce the growth time of salt
nuclei that form on the surface of the carrier during the drying
process. Exemplary processes for removing water from the
carrier-slurry mixture include spray drying, spray cooking, freeze
drying, and drum drying, among others.
[0055] In one approach, the average size of the salt particles can
be controlled by adjusting parameters during the drying process,
e.g., a spray-drying process, including one or more of (not by way
of limitation): the ratio of salt-to-carrier in the slurry as
described in the examples above, and spray drying parameters,
including one or more of the inlet temperature, pump speed, air
flow, and compressor pressure. It will be understood that various
other means can be used to achieve similar results. Drying
temperatures and times may vary particularly when methods other
than spray drying are used in the drying process.
[0056] The improved process produces salt particles of an average
size of 100 nanometers to less than 2 microns adhered to or on the
surface of the carrier particles. FIG. 2 depicts an example of a
salt-carrier product described herein with a salt particle size of
100 nm to less than 2 microns. Specifically, FIG. 2 is a SEM image
of the improved salt-carrier product, demonstrating that the salt
particles adhered to or on the surface of an exemplary carrier
particle were measured to be 1.3 microns and 1.5 microns.
[0057] A number of illustrative embodiments have been described.
Nevertheless, it will be understood that various modifications may
be made without departing from the spirit and scope of the
inventive concepts presented herein. For example, suitable carriers
can include any material capable of providing a nucleation site for
salt crystals. Examples include non-organic materials such as
certain plastics and synthetic fillers known in the art.
[0058] In general, the methods provided herein can extend to other
foods and food additives as well. For example, using similar
processes as those described above, sugar particles can be grown on
a suitable carrier to provide an analogous sugar-carrier product.
Such an embodiment may provide a more intense sugar flavor than can
be obtained with commercially-available sugar granules commonly
found in restaurants, and may assist in lowering overall sugar
intake. Those with certain adverse health conditions, such as
diabetes or obesity may find such a sugar-carrier product
beneficial to their health.
[0059] In general, the salt-carrier products (and their
equivalents) described herein may be packaged for retail sale or
for bulk shipments. The products described herein may be used for
sprinkle-on applications, e.g., used in salt shakers and the like,
and in bulk applications such as large-scale food processing. The
salt-carrier products described herein may be used as flavorings,
tenderizers, flavor enhancers, additives, fillers, and other
ingredients generally known to those who prepare and consume foods,
e.g., chefs, those in the food preparation industry, and consumers.
Accordingly, other embodiments are within the scope of the
following claims.
[0060] To gain consumer loyalty in a competitive snack food market,
companies need to consistently produce well-coated potato chip
products. Toward this end, it is important to understand how
seasoning adheres to food surfaces so that we can improve the
process involved in coating snacks. The adhesion of salt onto
potato chips affects the product's flavor and impacts whether
consumers will purchase the product.
[0061] Scientists at The Ohio State University examined a number of
factors that could impact how salt adheres to potato chips: surface
oil content (SOC), chip temperature, the time between frying and
coating the product, oil composition, salt particle size, salt
crystal shape and the use of electrostatics. It appears that the
best adhesion conditions would involve applying small salt
particles to an oily surface. "Optimize the adhesion of salt onto
potato chips," The Free Library. 2008 Food Technology Intelligence,
Inc. 30 Jun. 2019.
[0062] Investigators produced chips with three different SOC
levels--high, low and no SOC. Patting fried chips with a paper
towel reduced SOC levels. Extracting fried chips with hexane
removed SOC. Baking fried chips increased chip temperature.
[0063] The researchers fried chips in soybean, olive, corn, peanut
and coconut oils to study the effects of oil composition. The
non-electrostatically coated NaCl crystals of five different
particle sizes and three different shapes onto the chips. Using a
powder applicator, five different sizes of salt were
electrostatically applied onto all SOC chips. A feeder, which
simulates a moving conveyor belt used in commercial settings,
removed the salt.
[0064] Chips with high SOC had the highest adhesion of salt, making
SOC the most dominant factor. Increasing chip temperature increased
SOC and adhesion activity. Increasing the time between frying and
coating the chip reduced the extent of adhesion for low-SOC level
chips, but did not affect high- and non-SOC chips. Changing oil
composition did not change adhesion values.
[0065] Increasing the size of the salt particles decreased the
extent of adhesion on all SOC chips. The effect of salt size was
most evident in lower SOC chips. The larger-shaped crystals adhered
less extensively than smaller-shaped crystals on all SOC chips,
except for large cubic-shaped crystals on low-SOC chips. For chips
with low SOC levels or none at all, cubic-shaped crystals gave the
best adhesion properties. Electrostatic coating improved adhesion
values for all salt sizes.
[0066] The relationship between salt particle size and adhesion has
also been noted by Amos Nussinovitch, Adhesion in Foods (2017).
Ertran Ermiss in his Ph.D. thesis at Greenwich University of
Greenwich, entitled Establishment of a Repeatable Test Procedure
for Measuring Adhesion Strength of Particles In Contact With
Surfaces (2011), noted that the electrostatic force between a
seasoning particle and a crisp substrate could be calculated as
follows:
[0067] Calculation of Electrostatic Force (F.sub.el)
[0068] The electrostatic interaction between the seasoning particle
and the crisp substrate can be considered as coulombic interaction
between two oppositely charged particles situated on both side of
the surface and is given by (Bowling, 1988)
F el = q 2 4 8 .pi. r ( R p + h ) 2 ##EQU00001##
[0069] Where q is the net change of the seasoning particle,
.epsilon..sub.0 is permittivity of vacuum (electric constant).
.epsilon..sub.r is the dielectric constant of the intervening
medium (oip in this case). R.sub.p is equivalent radius of particle
and h is the surface-to-surface distance of separation. Finally,
the language used in the specification has been principally
selected for readability and instructional purposes, and it may not
have been selected to delineate or circumscribe the inventive
subject matter. It is therefore intended that the scope of the
invention be limited not by this detailed description, but rather
by any claims that issue on this application based hereon.
Accordingly, the disclosure of the embodiments of the invention is
intended to be illustrative, but not limiting, of the scope of the
invention.
[0070] The improved salt-carrier product adheres better to foods
and coats foods, including potato chips, corn chips, nuts, and
other snack chips, better than salt that is not adhered to a
carrier particle. Adhering better to foods means that there is less
salt-carrier product by volume that does not adhere to the foods
than salt not adhered to a carrier particle when an approximately
equal volume of salt not adhered to a carrier product and the
improved salt-carrier product are applied to the same foods.
[0071] The invention has been described in terms of particular
embodiments. The alternatives described herein are examples for
illustration only and not to limit the alternatives in any way. The
steps of the invention can be performed in a different order and
still achieve desirable results. It will be obvious to persons
skilled in the art to make various changes and modifications to the
invention described herein. To the extent that these variations
depart from the scope and spirit of what is described herein, they
are intended to be encompassed therein. It will be understood by
those skilled in the art that various changes in form and details
may be made therein without departing from the scope of the
invention encompassed by the appended claims.
* * * * *