NZ621519B2 - Frozen dessert and frozen dessert material - Google Patents
Frozen dessert and frozen dessert material Download PDFInfo
- Publication number
- NZ621519B2 NZ621519B2 NZ621519A NZ62151912A NZ621519B2 NZ 621519 B2 NZ621519 B2 NZ 621519B2 NZ 621519 A NZ621519 A NZ 621519A NZ 62151912 A NZ62151912 A NZ 62151912A NZ 621519 B2 NZ621519 B2 NZ 621519B2
- Authority
- NZ
- New Zealand
- Prior art keywords
- microfibrillated cellulose
- standard
- frozen dessert
- weight
- cream
- Prior art date
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- LPLVUJXQOOQHMX-QWBHMCJMSA-N glycyrrhizinic acid Chemical compound O([C@@H]1[C@@H](O)[C@H](O)[C@H](O[C@@H]1O[C@@H]1C([C@H]2[C@]([C@@H]3[C@@]([C@@]4(CC[C@@]5(C)CC[C@@](C)(C[C@H]5C4=CC3=O)C(O)=O)C)(C)CC2)(C)CC1)(C)C)C(O)=O)[C@@H]1O[C@H](C(O)=O)[C@@H](O)[C@H](O)[C@H]1O LPLVUJXQOOQHMX-QWBHMCJMSA-N 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 235000015110 jellies Nutrition 0.000 description 1
- 239000008274 jelly Substances 0.000 description 1
- 239000000832 lactitol Substances 0.000 description 1
- 235000010448 lactitol Nutrition 0.000 description 1
- VQHSOMBJVWLPSR-JVCRWLNRSA-N lactitol Chemical compound OC[C@H](O)[C@@H](O)[C@@H]([C@H](O)CO)O[C@@H]1O[C@H](CO)[C@H](O)[C@H](O)[C@H]1O VQHSOMBJVWLPSR-JVCRWLNRSA-N 0.000 description 1
- 229960003451 lactitol Drugs 0.000 description 1
- 239000008101 lactose Substances 0.000 description 1
- 235000010420 locust bean gum Nutrition 0.000 description 1
- 239000000711 locust bean gum Substances 0.000 description 1
- 235000010449 maltitol Nutrition 0.000 description 1
- 239000000845 maltitol Substances 0.000 description 1
- VQHSOMBJVWLPSR-WUJBLJFYSA-N maltitol Chemical compound OC[C@H](O)[C@@H](O)[C@@H]([C@H](O)CO)O[C@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O VQHSOMBJVWLPSR-WUJBLJFYSA-N 0.000 description 1
- 229940035436 maltitol Drugs 0.000 description 1
- 235000019988 mead Nutrition 0.000 description 1
- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 235000019865 palm kernel oil Nutrition 0.000 description 1
- 239000003346 palm kernel oil Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000009928 pasteurization Methods 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 235000019204 saccharin Nutrition 0.000 description 1
- CVHZOJJKTDOEJC-UHFFFAOYSA-N saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 1
- 229940081974 saccharin Drugs 0.000 description 1
- 239000000901 saccharin and its Na,K and Ca salt Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000010356 sorbitol Nutrition 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 229960002920 sorbitol Drugs 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 229940013618 stevioside Drugs 0.000 description 1
- OHHNJQXIOPOJSC-UHFFFAOYSA-N stevioside Natural products CC1(CCCC2(C)C3(C)CCC4(CC3(CCC12C)CC4=C)OC5OC(CO)C(O)C(O)C5OC6OC(CO)C(O)C(O)C6O)C(=O)OC7OC(CO)C(O)C(O)C7O OHHNJQXIOPOJSC-UHFFFAOYSA-N 0.000 description 1
- 235000019202 steviosides Nutrition 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000019408 sucralose Nutrition 0.000 description 1
- BAQAVOSOZGMPRM-QBMZZYIRSA-N sucralose Chemical compound O[C@@H]1[C@@H](O)[C@@H](Cl)[C@@H](CO)O[C@@H]1O[C@@]1(CCl)[C@@H](O)[C@H](O)[C@@H](CCl)O1 BAQAVOSOZGMPRM-QBMZZYIRSA-N 0.000 description 1
- 150000005846 sugar alcohols Chemical class 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000000892 thaumatin Substances 0.000 description 1
- 235000010436 thaumatin Nutrition 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000000811 xylitol Substances 0.000 description 1
- 235000010447 xylitol Nutrition 0.000 description 1
- HEBKCHPVOIAQTA-SCDXWVJYSA-N xylitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)CO HEBKCHPVOIAQTA-SCDXWVJYSA-N 0.000 description 1
- 229960002675 xylitol Drugs 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/04—Production of frozen sweets, e.g. ice-cream
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/32—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/32—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds
- A23G9/42—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds containing plants or parts thereof, e.g. fruits, seeds, extracts
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/44—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by shape, structure or physical form
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/52—Liquid products; Solid products in the form of powders, flakes or granules for making liquid products ; Finished or semi-finished solid products, frozen granules
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
- C08L1/02—Cellulose; Modified cellulose
Abstract
The disclosure relates to a frozen dessert containing plant-derived microfibrillated cellulose, wherein said plant-derived microfibrillated cellulose has at least a specific surface area of 150 m2/g or larger or water retention of 500% or more. Alternatively, the cellulose may have a rate of sedimentation of 1500 ml/g or more when in the form of a water dispersion having a microfibrillated cellulose content of 0.05% by weight or a light transmission of 40% or more at a wavelength of 600 nm when in the form of a water dispersion having a microfibrillated cellulose content of 0.02% by weight. ntation of 1500 ml/g or more when in the form of a water dispersion having a microfibrillated cellulose content of 0.05% by weight or a light transmission of 40% or more at a wavelength of 600 nm when in the form of a water dispersion having a microfibrillated cellulose content of 0.02% by weight.
Description
DESCRIPTION
FROZEN DESSERT AND FROZEN DESSERT MATERIAL
TECHNICAL FIELD
The present invention relates to a frozen dessert and a frozen
dessert material.
BACKGROUND ART
[0002]
In general, a “frozen dessert” is defined as “frozen or chilled
confectionery such as jelly, ice cream and sherbet” (Kojien, fourth edition,
Iwanami Shoten, 1991). In the present application, r, a ‘frozen
dessert’ is defined as follows.
That is, the ‘frozen dessert’ in the t application is broadly
classified into “hard ice cream” and “soft ice cream” as shown in Table l.
The “hard ice cream” is a frozen dessert which is in the form of an
end product ed through a ‘hardening process’ in a tion flow
to be described later and which is distributed while in a frozen state at
approximately —20°C, and placed in a freezing cabinet and sold as a
commodity at a store (commercial product). The “hard ice cream” is
categorized into “ice creams” and “ice confections”.
The “soft ice cream” is a frozen dessert which is commonly called
soft—serve ice cream and which is not distributed but is made with a frozen
dessert tion apparatus t a ‘hardening process’ in a store and
sold at the store face to face to consumers as a prepared food product at
imately —4 to —10°C directly taken out of the frozen dessert
production apparatus. The “soft ice cream” is also rized into “ice
creams” and “ice confections”.
Furthermore, under the hard ice cream and the soft ice cream
(hereinafter, abbreviated as soft cream), the “ice creams” are categorized
into an ice cream standard, an ice milk standard and a ce standard
based on the standards for ice creams specified under a erial
ordinance according to their compositions such as milk.
Likewise, under the hard ice cream and the soft cream, the “ice
confections” refer to frozen desserts containing less than 3% of milk solid.
The ice confections are further categorized into fat—containing ice
confections and fat-free ice confections as shown in Table 1.
It is noted that some products analogous to soft cream have been
recently offered to consumers, which are a frozen t put in
small-sized containers and distributed in the same manner as in the hard
ice cream, and then forcibly defrosted in a dedicated ting chamber in
a store until it is —8 to — 12°C, ed while each container is compressed
and deformed with a dedicated extruder and served in a well—known soft
cream form (twisted high). However, these products shall be categorized
into the hard ice cream since they are obtained through a hardening
process and they are distributed at —20°C.
[Table 1]
, Ice Cream Standard
i Milk Solid: 215.0%, Milk Fat: 28.0%
Ice Creams Ice Milk Standard
Hard
Milk Fat: 23.0%!
Ice Cream “Milk Solid: 210.0%,
Lact-ice Standard
Milk Solid: 23.0%
Ice Confections LFat—containing Ice tions
Frozen
(Milk Solid: Fat—free Ice Confections
Dessert
<3.0%)_
Ice Cream Standard
Milk Solid: 215.0% Milk Fat: 28.0%
Ice Creams Ice Milk Standard
Soft
(Milk Solid: 210.0%, Milk Fat: 23.0%)
Ice Cream
Lact—ice Standard
_[ (Milk Solid: 23.0%)
Ice Confections Fat—containing Ice Confections
(Milk SOlidi Fat—free ice tions
43.0%;
Consumers may eat the hard ice cream at the point of sale
immediately after the purchase, or may take it home by maintaining its
frozen state with dry ice or the like, keep it in a freezer and eat
it at an
riate time. Since the hard ice cream immediately after it is taken
out of the freezer is frozen
very hard, the hard ice cream is generally eaten
after the temperature of the product is approximately
—10°C, at which it is
soft enough to eat, and it thaws of its own accord by leaving
it at room
temperature.
However, the thawing time taken until the hard ice cream is soft
enough to eat varies y ing on the surrounding environment.
As time goes by, the surface of the hard ice
cream may start melting earlier
than the other part and impair a pleasant dry feeling,
or an edge portion of
the hard ice cream twisted high into
a sharp and beautiful shape may run
down and damage the shape, or the hard ice
cream may melt and fall like
a snowslide. Thus, consumers often miss the timing to eat the hard ice
cream while it is in an ideal state.
When a small child or an elderly person who cannot quickly eat up
a frozen dessert which is cold as being below zero encounters the
above—described situations, the frozen dessert starts melting completely
and dirties their hands or clothes, or melts and falls like a snowslide and
drips onto the floor. Such situations are often observed.
The same is true of soft cream which is made at the point of sale
Without a hardening process, served on an edible container such as a cone
cup and sold face to face while in a soft state at approximately —4 to -10°C.
Consumers eat the soft cream in or around the store while g the
container such as a cone cup. Then, the soft cream melts with time and
dirties hands and clothes of the consumers, or even worse the soft cream
melts and falls like a snowslide and drips onto the floor, necessitating
cleaning. Such situations occur more often when the ambient
temperature is high, in particular.
In these frozen desserts, which melt with time unless they are kept
in a frozen state as bed above, maintaining a pleasant dry feeling by
delaying start of melting as much as le, maintaining a beautiful
shape by delaying melting and falling as much as possible and
maintaining a beautiful ance perceptually appealing attractive taste
(reinforcing shape retention for holding a predetermined shape) lead to
ement of product's value (product's life) and thus are very
important objects as well as other properties such as flavor and texture.
As a conventional method for the reinforcement of the shape
retention of frozen desserts, addition of a izer and an emulsifier is
known. Examples of the stabilizer include hydrophilic polysaccharides
extracted from d, vegetable seeds, microorganisms or the like;
ble polysaccharides such as microcrystalline cellulose; and
synthetic stabilizers such as carboxymethylcellulose (CMC). Examples of
the emulsifier include low HLB emulsifiers such as unsaturated fatty
ester.
In addition, Patent Document 1 reports that use of microcrystalline
cellulose, carrageenan and waxy corn starch as stabilizers allows
enhancement of the liquid stability of a liquid soft cream mix before the
freezing and achievement of soft cream having good shape retention and
superior drip ance after the freezing for a long period of time. Here,
it should be noted that microcrystalline cellulose is clearly distinguished
from microfibrillated cellulose used in the present invention to be
bed later (see Patent Document 2, for example).
RELATED ART DOCUMENTS
PATENT DOCUMENTS
[0008]
Patent Document 1: Japanese Unexamined Patent Publication No.
HEI 5(1993)—276875
Patent Document 2: Japanese Unexamined Patent Publication No.
HEI 6(1994)—178659
Y OF THE INVENTION
PROBLEMS To BE SOLVED BY THE INVENTION
The t inventors have made intensive s for g the
time from when a consumer is about to eat a frozen dessert until when
melting, falling and loss of shape start, that is, extending the period of time
a frozen dessert can retain its shape (improvement of the shape retention).
As a result, the present inventors have reached the following findings.
The improvement of the shape ion of a frozen dessert with
stabilizers can be achieved by increasing the amount of the stabilizers to
add. However, addition of the stabilizers to the extent that an expected
effect is achieved makes the texture of the frozen dessert pasty,
significantly impairing the flavor of the frozen dessert.
[001 1]
The improvement of the shape ion of a frozen dessert with
low HLB emulsifiers can be also achieved by increasing the amount of the
emulsifiers to add. However, the emulsifiers have a distinctive taste and
odor, and addition of the emulsifiers to the extent that an expected effect is
achieved therefore reduces the flavor of the frozen dessert. Besides, the
low HLB emulsifiers induce demulsification, and churning is easily caused
during the freezing. Here, the churning refers to the situation Where a
plurality of fat globules are put together to grow to lumps and some of the
lumps r particles) are so large that they are visible. The churning
can be a cause of ion of melt—in-mouth characteristics and
roughness, significantly impairing the e of the frozen dessert.
MEANS FOR SOLVING THE PROBLEMS
The present inventors have found that it is possible to sufficiently
extend the shape holding time (shape retention) of a frozen dessert to the
ed extent without an adverse effect on the other properties by
including plant—derived microfibrillated ose having the following
parameters in a material mix of the frozen dessert to reach the present
invention.
The ‘microfibrillated cellulose’ in the present invention, which Will
be described later, refers to two types of microfibrillated cellulose distinctly
different in degree of lation according to each parameter described
later. The two types of microfibrillated cellulose are distinctively referred
to as “microfibrillated cellulose D standard”, which is less ated
“microfibrillated cellulose”, and “microfibrillated cellulose K standard”,
which is more fibrillated “microfibrillated cellulose”.
Thus, according to the present invention, there is provided a frozen
t containing plant-derived microfibrillated cellulose.
According to another aspect of the present invention, there is
provided a frozen dessert containing plant—derived microfibrillated
ose, wherein the microfibrillated cellulose has at least one of the
parameters:
(1) a specific surface area of 100 m2 /g or ; and
(2) a water retention of 300% or more.
[0015]
According to still another aspect of the present invention, there is
provided a frozen dessert containing plant—derived microfibrillated
ose, wherein the microfibrillated cellulose has at least one of the
parameters:
(A) a rate of sedimentation of 1000 ml/ g or more when in the form of a
water dispersion having a microfibrillated cellulose content of 0.05% by
weight; and
(B) a light transmission of 30% or more at a wavelength of 600 nm when in
the form of a water sion having a microfibrillated cellulose content of
0.02% by weight.
According to still another aspect of the present invention, there is
provided a frozen dessert containing plant—derived microfibrillated
cellulose, wherein more preferably, the microfibrillated cellulose has at
least one of the parameters:
(1) a specific surface area of 150 m2/ g or larger; and
(2) a water retention of 500% or more.
According to still another aspect of the present invention, there is
provided a frozen dessert containing plant—derived microfibrillated
ose, wherein still more preferably, a water dispersion containing the
microfibrillated ose has at least one of the parameters:
(A) a rate of ntation of 1500 m1/ g or more when in the form of a
water dispersion having a microfibrillated cellulose content of 0.05% by
; and
(B) a light transmission of 40% or more at a wavelength of 600 nm when in
the form of a water dispersion having a microfibrillated cellulose t of
0.02% by weight.
According to still another aspect of the present invention, there is
provided a frozen dessert material for the above-mentioned frozen dessert,
wherein the material contains the plant—derived microfibrillated cellulose.
According to still another aspect of the present invention, there is
provided a method for producing a frozen t, ing use of the
frozen dessert material.
EFFECTS OF THE INVENTION
The frozen dessert material of the present invention allows
production of a frozen dessert that has a shape holding (shape retention)
time sufficiently extended to the expected extent without an e effect
on the properties of the frozen dessert such as thermal physical property
change, viscosity, texture and flavor.
Of various frozen ts, in particular, a type of frozen dessert
which is served high on a cone cup, d upward into the shape of
so-called soft—serve ice cream and a type of frozen dessert which comes on
a stick (ice cream bar) (regardless of the categories of frozen desserts; hard
ice cream, soft cream or ice confection) melt, fall and loose shape with time,
and these problems are desired to be delayed as much as possible. Such
types of frozen dessert are therefore most suitable as embodiments of the
present invention
[0020]
According to the present invention, it is possible to obtain an
expected shape ion improvement effect by addition of a small
amount of plant—derived microfibrillated cellulose, and therefore it is not
necessary to change the ition of the material mix for a frozen
dessert which has been precisely adjusted so that good flavor and texture
can be achieved. As a result, liquid state deterioration such as separation,
thickening and coagulation of the material mix of the frozen dessert is less
likely to occur, and the properties of the frozen dessert are not adversely
affected besides the shape retention improvement.
BRIEF DESCRIPTION OF THE DRAWINGS
[002 1]
is a flow diagram showing processes of production,
distribution and sale of frozen desserts of the present invention.
is a photograph showing Example 1 while the time until
melting and g of a frozen dessert (soft cream) of the present invention
is being ed after production.
MODE FOR CARRYING OUT THE INVENTION
—derived microfibrillated cellulose>
In the present invention, a “frozen dessert” is defined as described
above (see Table 1).
The frozen dessert of the present invention is characterized by
containing plant—derived microfibrillated ose having the following
parameters so that the shape retention of the frozen dessert is ed
Without an adverse effect on the properties of the frozen dessert such as
Viscosity, texture and flavor, and on the properties of the frozen dessert
material such as thermal physical property change and long—term storage
stability. The microfibrillated ose is characterized by the following
parameters.
<Parameters for microfibrillated cellulose itself>
Specifically, the microfibrillated cellulose in the present invention
has at least one of the parameters:
(1) a specific surface area of 100 m2 /g or larger and preferably 150 In2 / g or
larger; and
(2) a water retention of 300% or more and preferably 500% or more.
ably, the brillated cellulose in the present invention has both
of the parameters ( 1) and (2).
The parameters (1) and (2) are for the brillated cellulose
itself and important factors for the improvement of the shape retention of
the frozen dessert.
In the present invention, the specific surface area is 100 m2/ g or
larger, preferably 150 m2/ g or larger, and more preferably 200 to 350 In2 / g.
In the present invention, the water retention is 300% or more, preferably
500% or more, and more ably 8500 to 36000%. It is difficult to
obtain a satisfactory shape retention improvement effect from the
microfibrillated ose if the c e area is smaller than 100
m2/g or the water retention is less than 800%.
In the present invention, the specific surface area is determined as
follows. A sample of a water dispersion of the microfibrillated cellulose is
collected, and the water in the sample is replaced with ethanol, and then
with tert—butyl alcohol. Thereafter, the sample is freeze—dried, and the
specific surface area of the microfibrillated cellulose is measured in
ance With the BET method with BELSORP—mini 11 produced by BEL
Japan, Inc. The determination of the specific surface area confirms that
the more the number of fibers of the microfibrillated cellulose per unit
weight is (the smaller the diameter of the fibers is), the larger the specific
surface area is.
[0026]
In the present invention, the water retention is a value ined
as follows. Into a metal cup filter provided with two sheets of qualitative
filter paper No. 101 produced by Advantech Toyo kabushiki , 50 g of
a water dispersion of microfibrillated cellulose obtained by dispersing
2O microfibrillated cellulose in water so as to have a microfibrillated cellulose
content of 0.5% by weight was poured, dehydrated using a centrifuge at a
centrifugal force of 1500 G and at a room temperature of 25°C for 15
minutes. The sample dehydrated is weighed, and then the sample is
dried and weighed to ate the water retention according to the
equation shown below. The determination of the water retention also
confirms that the more the number of fibers of the microfibrillated
cellulose per unit weight is, the larger the water retention is.
Water ion (%) = {(weight of sample dehydrated — weight of
sample dried) / weight of sample dried} X 100
<Parameters for water dispersion of microfibrillated cellulose>
The microfibrillated cellulose in the present invention may have at
least one of the parameters:
(A) a rate of sedimentation of 1000 ml/ g or more and preferably 1500 ml/ g
or more when in the form of a water dispersion having a brillated
cellulose content of 0.05% by weight; and
(B) a light ission of 30% or more and preferably 40% or more at a
wavelength of 600 nm when in the form of a water dispersion having a
microfibrillated cellulose content of 0.02% by weight. Preferably, the
microfibrillated ose in the present invention has both of the
parameters (A) and (B).
The parameters (A) and (B) are for the water dispersion of the
microfibrillated cellulose and important factors for the improvement of the
shape ion of the frozen dessert.
In the present invention, the rate of sedimentation is 1000 ml/ g or
more, preferably 1500 ml/ g or more, and more preferably 1800 to 2000
ml/ g. In the present ion, the light transmission is 30% or more,
preferably 40% or more, and more preferably 70% or more.
In the present invention, the rate of sedimentation is a value
determined as follows. In a measuring cylinder, 100 ml of a water
dispersion of microfibrillated cellulose ed by dispersing
microfibrillated cellulose in water so as to have a microfibrillated cellulose
t of 0.05% by weight is allowed to rest for 1 hour, and then the
volume of the suspended part is measured to calculate the rate of
sedimentation according to the on shown below. The
determination of the rate of sedimentation also confirms that the more the
number of fibers being measured per unit weight is, the larger the rate of
sedimentation is.
Rate of sedimentation (ml/ g) suspension volume (ml) / solid
content (g)
In the present invention, the light transmission is a value
determined as follows. A water dispersion of microfibrillated ose
obtained by dispersing microfibrillated cellulose in water so as to have a
microfibrillated cellulose content of 0.02% by weight is put in a standard
glass cell and measured for the light transmittance at a wavelength of 600
nm with a spectrophotometer using water as blank. The determination of
the light transmittance confirms that the more the number of fibers of the
microfibrillated ose per unit weight is, the larger the light
transmittance is.
In general, the more the number of fibers per unit weight is, the
finer and the more xly intertwined three—dimensional network
2O ure the fibers can form. Having at least one of the parameters (1)
and (2) or of the parameters (A) and (B) when in the form of a water
sion, the microfibrillated ose can form an extremely fine and
complexly intertwined three—dimensional network structure. A small
amount of microfibrillated cellulose uniformly contained in the frozen
dessert material can dramatically improve the shape retention of the
frozen dessert. Besides, the microfibrillated cellulose only has an effect of
improving the shape retention and does not have any adverse effect on the
properties of the frozen dessert.
The microfibrillated cellulose referred to is categorized into two
types of microfibrillated cellulose having a significant difference in the
melting and falling delaying effect according to the degree of fibrillation.
The two types of ibrillated cellulose are ctively referred to as
“microfibrillated cellulose D standard”, which is less fibrillated, and
fibrillated cellulose K standard”, which is more fibrillated.
They are defined as follows according to the parameters as defined
above.
— The “microfibrillated cellulose D standard” (hereinafter, may be ed
to as microfibrillated ose (D standard)) is defined as microfibrillated
cellulose having at least one of the parameters:
(1) a specific surface area of 100 m2 / g or larger and smaller than 150
m2 / g; and
(2) a water ion of 300% or more and less than 500%,
or as microfibrillated cellulose having, when in the form of a water
dispersion containing the microfibrillated cellulose, at least one of the
parameters:
(A) a rate of sedimentation of 1000 ml/ g or more and less than 1500 ml/ g
when in the form of a water dispersion having a microfibrillated cellulose
content of 0.05% by weight; and
(B) a light ission of 30% or more and less than 40% at a wavelength
of 600 nm when in the form of a water dispersion having a microfibrillated
cellulose content of 0.02% by weight.
- The fibrillated cellulose K standard” (hereinafter, may be referred
to as microfibrillated cellulose (K standard)) is defined as microfibrillated
cellulose having at least one of the parameters:
(1) a specific surface area of 150 m2/ g or larger; and
(2) a water retention of 500% or more,
or as microfibrillated cellulose having, when in the form of a water
dispersion containing the microfibrillated cellulose, at least one of the
parameters:
(A) a rate of sedimentation of 1500 ml/ g or more when in the form of a
water dispersion having a microfibrillated cellulose content of 0.05% by
weight; and
(B) a light transmission of 40% or more at a wavelength of 600 nm when in
the form of a water dispersion having a microfibrillated cellulose content of
0.02% by weight.
As described later, the effect of improving the shape ion of the
frozen dessert of the more fibrillated “microfibrillated ose K standard”
is greater than that of the less lated “microfibrillated cellulose D
rd”.
The microfibrillated cellulose is not limited as long as it has at least
one of the parameters (1) and (2) or of the parameters (A) and (B) when in
the form of a water dispersion of the microfibrillated cellulose. The plant
to be a material of the ibrillated cellulose is not particularly d,
and the method for the preparation of the microfibrillated cellulose is not
particularly limited, either.
As a representative method for the preparation of the
microfibrillated cellulose, a method by fibrillating a commonly known
never—dried pulp may be mentioned, for example.
Here, an example of the preparation of microfibrillated cellulose
derived from a never—dried pulp will be described. First, a raw wood
al such as a broadleaf tree and a coniferous tree is processed into
timber by removing its bark, the timber is pulverized into wood flour, and
the wood flour is classified to have a predetermined size (for example, 50
pm X 250 pm). Subsequently, the fied wood flour is immersed in an
organic solvent for defatting. The defatted wood flour is immersed in a
sodium chlorite solution to remove lignin. The wood flour after the lignin
removal is ally ed in an alkaline aqueous solution (for
example, a potassium hydroxide solution or a sodium hydroxide solution)
to remove a certain amount of hemicellulose. The fiber preparation after
the hemicellulose removal is washed with water. The fiber preparation
swelled after the washing with water is a never-dried pulp. In the present
invention, a ermined amount of hemicellulose may be contained in
the never—dried pulp, which will be described later in detail.
Then, the dried pulp is fibrillated with a fibrillation
apparatus (a grinder, for e) to give wet microfibrillated cellulose.
The fibrillation conditions of the fibrillation tus are set so that the
microfibrillated cellulose to be obtained will have at least one of the
parameters (1) and (2) or of the parameters (A) and (B) when in the form of
a water dispersion of the microfibrillated cellulose.
This preparation method is commonly known, which is useful in
preparation of microfibrillated cellulose derived from a never—dried pulp,
and disclosed in Japanese Unexamined Patent ation No. 2010-7010,
for example. The microfibrillated cellulose derived from a never—dried
pulp may be used as a water dispersion of the microfibrillated cellulose
obtained by dispersing the microfibrillated cellulose in water.
[0035]
Here, an example of the preparation of microfibrillated cellulose
derived from a dried pulp will be described. The above—mentioned fiber
ation is obtained in the same manner as in the example of the
preparation of microfibrillated cellulose derived from a dried pulp.
Thereafter, the fiber preparation is dried to give a dried pulp, and the dried
pulp is fibrillated to give microfibrillated cellulose. The microfibrillated
cellulose derived from a dried pulp may also be used as a water dispersion
of the microfibrillated cellulose obtained by dispersing the microfibrillated
ose in water.
In the frozen dessert of the present invention, the microfibrillated
cellulose may be prepared so as to satisfy (1) or (II), or a combination of (I)
and (11) described below. As a result, it is le to obtain a frozen
dessert further enhanced in shape retention. In particular, such an effect
of (II) is significant.
(I) The microfibrillated cellulose preferably has an OL-CCllUlOSG
content of 50% or more. The oc—cellulose t may be 100%. In this
case, r, the preparation time of the microfibrillated cellulose is
longer and the preparation cost is increased.
In the above—described examples of the preparation of the
brillated cellulose, hemicellulose is removed so that the oc—cellulose
content will be 50% or more. In this case, the oc—cellulose content
(hemicellulose content) in the brillated cellulose can be adjusted by
adjusting the period of time for immersing the wood flour after the lignin
removal in an alkaline aqueous solution or the tration of the
alkaline aqueous solution. The oc—cellulose content in the microfibrillated
cellulose can be determined using a commonly known method as a
component that does not dissolve in 17.5% by weight sodium hydroxide
solution.
(H) The microfibrillated cellulose may be chemically modified with a
substituent including -CH2COO—. That is, the microfibrillated cellulose
may be subjected to carboxymethylation (hereinafter abbreviated as CM).
In this case, the CM can be performed by a commonly known method
before the fibrillation in the above—described process. Here, the degree of
etherification (DS) may be 0.01 to 0.50, for example. The substituent
ing —CH2COO— can be confirmed by a commonly known , for
example, by analyzing the ed absorption um of the
microfibrillated cellulose.
The melting and falling delaying effect of the microfibrillated
cellulose subjected to the CM is increased by moderately increasing the
degree of etherification. However, if the degree of etherification is
increased too much, for example, if the degree of etherification exceeds 0.5,
the amount of chemicals such as sodium monochloroacetate and sodium
ide to be used in the reaction is increased, and therefore the
cellulose is damaged and the crystallinity thereof is impaired. As a result,
the solubility of the cellulose molecule will increase, and a ent
network structure cannot be formed. Accordingly, a sufficient melting
and falling delaying effect of the soft cream cannot be obtained.
[0039]
The brillated cellulose content in the frozen t is not
limited as long as the shape retention ement effect can be
sufficiently exerted on the frozen dessert Without an adverse effect on the
properties of the frozen dessert and on the physical properties of the frozen
dessert material s the shape retention improvement effect. In a soft
cream, for example, the most suitable microfibrillated cellulose content is
0.05 to 1.0% by weight in the case of microfibrillated cellulose not
subjected to the CM and 0.01 to 1.0% by weight in the case of
microfibrillated cellulose subjected to the CM.
<Frozen dessert material>
In the present ion, the raw materials other than the
microfibrillated cellulose included in the frozen dessert material are
selected from raw materials ly used for the frozen desserts such
as, for example, water, milk, dairy products, sweeteners, oils and fats,
stabilizers, fiers, flavorings, salt, fruit juices, and fruity flesh as
appropriate according to the type of the frozen dessert.
[0041]
The milk is not ularly d, and examples thereof include
cow milk and ed milk (skimmed milk). The dairy products are not
particularly limited, and examples thereof e skim milk powder,
modified milk powder, cream, condensed milk and fermented milk. The
milk and the dairy products may be used independently, or two or more
kinds may be used in combination.
The sweeteners are not particularly limited and examples thereof
include sugars such as sugar (sucrose, sucrose), grape sugar (glucose),
fruit sugar (fructose), malt sugar (maltose), milk sugar (lactose), trehalose,
starch syrup and isomerized glucose syrup; sugar alcohols such as
sorbitol, xylitol, maltitol, erythritol and lactitol; and non—sugar sweeteners
such as aspartame, sucralose, acesulfame K, stevioside, thaumatin,
glycyrrhizin, saccharin and dihydrochalcone. The sweeteners may be
used ndently, or two or more kinds may be used in combination.
The oils and fats are used as a skeletal component of the cream
according to the type of the frozen dessert to be eventually produced. The
oils and fats are not particularly limited and examples thereof e
vegetable oils such as palm tree oil, palm oil, palm kernel oil, soybean oil
and canola oil; and animal oils and fats such as lard, tallow and fish oil.
It is needless to say that milk fats such as butter and cream can be also
used. The oils and fats may be used independently, or two or more kinds
may be used in combination.
The stabilizers moderately increase the viscosity of the frozen
dessert material and prevent the oil and fat component from being
separated from the frozen dessert material during the production process,
storage or distribution. The stabilizers are used also for adjusting the size
of the ice ls of the cream and improving the texture of the cream.
The stabilizers are not ularly limited and es thereof e
plant—derived stabilizers such as carrageenan, guar gum, Locust bean
gum, rystalline cellulose, pectin, starch and Arabian gum;
animal—derived stabilizers such as gelatin, casein and casein Na; and
synthetic stabilizers such as carboxymethylcellulose (CMC) and
methylcellulose. The stabilizers may be used independently, or two or
more kinds may be used in combination.
[0045]
The emulsifiers have a function of dispersing fat. Insufficient
dispersion of fat makes it lt to perform a sterilization process and a
homogenization s well. The emulsifiers have an effect on the
overrun, dryness and texture. The emulsifiers are not particularly limited
and examples thereof include glycerin fatty acid ester, sorbitan fatty acid
ester, sucrose fatty acid ester and propylene glycol fatty acid ester. The
emulsifiers may be used independently, or two or more kinds may be used
in combination.
The flavorings (flavors) are not limited as long as they give desired
fragrance to the frozen dessert, and examples thereof include vanilla,
ate, coffee, strawberry, apple, orange, grape, cinnamon, sweet
melon, banana, peach, mango, mint and lemon. The flavorings may be
used independently, or two or more kinds may be used in combination.
<Preparation of frozen dessert material>
The frozen desserts of the t invention are produced,
distributed and sold in accordance with the processes shown in the flow
diagram of
<Blending process>
In the blending process, the raw als such as water, milk, a
dairy product, a sweetener, oil and fat, a stabilizer, an emulsifier, a
flavoring and a water dispersion of microfibrillated cellulose are placed in a
tank mixer as a blending apparatus, and uniformly stirred and mixed to
give a precursor mixture referred to as “premix”, which is a mix before heat
sterilization. The solids fraction of the water dispersion of microfibrillated
cellulose, that is, the microfibrillated cellulose content in the water
dispersion of microfibrillated cellulose is not particularly limited. In the
blending s, the amount of each al other than the water
dispersion of microfibrillated cellulose is calculated beforehand in View of
the , the solids fraction and the water amount of the water
dispersion of brillated cellulose. In the ng process, in
addition, inary heating may be performed in order to uniformly
dissolve and mix the raw materials. The temperature of the preliminary
heating is not particularly limited, but 50 to 80°C is appropriate, for
example.
<Sterilization process>
In the sterilization process (heating process), commonly known
continuous heating methods such as UHT sterilization and HTST
pasteurization can be employed. The sterilization method is not d
to these methods, and batch—wise or continuous ct heating methods
can be also ed, for example. The sterilization process may be
performed after a homogenization process.
[0050]
<Homogenization process>
In the homogenization process, the premix prepared in the
blending process is moved into a homogenizing apparatus, and milk fat,
and oil and fat in the premix are d with the homogenizing apparatus
to homogenize the premix. As the homogenizing apparatus,
conventionally—known homogenizers, homomixers, colloidal mills and the
like may be used. Some material mixes of frozen desserts that are free
from oils and fats are completely dispersed or dissolved in the blending
process. In the case of such material mixes, the homogenization process
2O may be omitted.
<Cooling process>
In the cooling process, the mix after the heat sterilization is cooled
rapidly. If the hot mix after the sterilization process is left as it is, the mix
may o degradation and demulsification. The degradation and the
demulsification of the mix are therefore d by rapidly cooling the mix
after the ization process.
Hereinafter, production ses of hard ice cream Will be
described first, and then production processes of soft cream Will be
bed.
<Ageing process>
In the case Where the frozen dessert material prepared is an ice
cream mix, the components in the mix will be stabilized, and satisfactory
ice cream will be obtained through the freezing by ageing the mix for
several hours to about two days (cooling temperature: 5 to 10°C) after the
cooling process.
ing process>
The mix after the ageing process is put in a frozen dessert
production apparatus er) and cooled to a predetermined temperature
While the mix and air are being stirred and mixed at a predetermined ratio
thereby to make creamed ice cream incorporating air.
<Filling s>
After the ng, a desired amount of the completed ice cream is
put in a desired container using a filling e.
Conventionally~known packaging containers in line with the
purpose may be used as the container being filled.
Examples of the container material include, but are not limited to,
cup containers, bulk containers, pillow containers and standing pouches
with the use of processed paper and plastic materials. As the filling
machine, commonly-known apparatuses may be used according to the
application.
The ice cream put in a container may be further packaged.
<Hardening process (hardening)>
Hardening is performed to freeze the ice cream after completion of
the filling s. The hardening may be performed using
commonly—known equipment to cool and harden the ice cream.
Examples of the method thereof include, but are not limited to, a method
by applying cold air at -30°C to —40°C and a method by using the
vaporization heat of liquid nitrogen. Rapid freezing is desirable since the
hardening speed has an effect on the growth of ice crystals of the ice cream
during the hardening process.
<Storage, distribution and sale>
The ice cream hardened is kept frozen, distributed, red to
each store, and then placed in a freezing cabinet and sold.
[0058]
In the words “Hard ice creams” indicate production of ice
creams under the category of hard ice cream, and the words “ice
confections” te production of ice confections under the category of
hard ice cream. They are produced in the substantially same manner.
In the case of raw als that are completely dispersed or dissolved in
the blending process, the homogenization process and the ageing process
can be omitted.
Next, production processes of the soft cream will be bed.
[0060]
<Fi11ing process>
In the case where the frozen dessert is soft cream, a desired
amount of a soft cream mix which has been cooled is put in a desired
container using a filling machine. Conventionally-known packaging
containers in line with the purpose may be used as the container being
filled. Examples of the container include, but are not limited to, Tetra Pak
cartons and Gable top cartons with the use of processed paper; and pillow
containers and bags for —boxes (BIBS) with the use of plastic
als. As the filling e, commonly~known apparatuses may be
used according to the application. The filling may be performed under
aseptic conditions or under non—aseptic conditions. In the case where
the filling is performed under aseptic conditions, long—term distribution
and storage under normal temperature are possible. Examples of the
filling machine to be used under aseptic conditions include, but are not
limited to, aseptic filling machines ble from Tetra Pak International
SA. The soft cream mix put in a container may be further packaged.
Examples of the packaging include, but are not d to, packing in a
ard box.
The soft cream mix packed in a box is stored with or without
refrigeration, distributed with or without refrigeration and delivered to
each store.
2O The production of ice confections under the category of soft cream
is substantially the same as the production of ice creams under the
category of soft cream as shown in In the case of raw materials
that are completely dispersed or ved in the blending process, the
homogenization process and the ageing process can be omitted.
[0062]
<Production of frozen dessert>
The soft cream mix prepared in a factory is packed in the factory
and delivered to each store. The soft cream mix is then put into a frozen
dessert production apparatus at a store, and cooled and prepared into a
creamed state incorporating air as described above. The soft cream mix
does not go through the hardening process and is sold face to face while in
a soft state.
EDUUMPLES
Hereinafter, examples of the t invention will be bed.
However, the present invention is not limited thereto.
(Preparation of mix base for soft cream of ice cream standard)
Sugars, dairy products, emulsifiers, stabilizers and the other
components, and water were used as raw materials at the ratios of the raw
materials shown in Table 2, and a mix base for soft cream of the ice cream
standard (hereinafter, may be referred to as soft cream mix base (ice cream
standard)) was ed. Sugar and starch syrup were used as the
sugars, butter and skim milk powder were used as the dairy products,
cellulose, casein Na and thickening polysaccharides were used as the
stabilizers, and vanilla flavoring and a noid pigment were used as
the other components.
[0065]
[Table 2]
water »
ration of mix base for soft cream of ice standard)
Sugars, a dairy product, oils and fats, emulsifiers, stabilizers and
the other components, and water were used as raw materials at the ratios
of the raw materials shown in Table 3, and a mix base for soft cream of the
lacto—ice standard (hereinafter, may be referred to as soft cream mix base
(lacto-ice standard)) was prepared. Sugar and starch syrup were used as
the sugars, skim milk powder was used as the dairy product, coconut oil
and palm oil were used as the oils and fats, cellulose, casein Na and
thickening polysaccharides were used as the stabilizers, and vanilla
flavoring and a carotenoid pigment were used as the other components.
[Table 3]
(Preparation of mix base for soft cream of fat—free ice confection standard)
Pureed strawberry, sugars, a dairy product, a stabilizer and the
other components, and water were used as raw materials at the ratios of
the raw materials shown in Table 4, and a mix base for soft cream of the
ee ice confection standard (hereinafter, may be referred to as soft
cream mix base (fat-free ice confection standard)) was prepared. Sugar
and starch syrup were used as the sugars, whey powder was used as the
dairy product, ning polysaccharides were used as the stabilizer, and
a flavoring and a coloring agent were used as the other components.
[Table 4]
(Preparation of mix base for hard ice cream of ice cream rd)
Sugars, dairy products, fiers, stabilizers and the other
components, and water were used as raw materials at the ratios of the raw
materials shown in Table 5, and a mix base for hard ice cream of the ice
cream standard (hereinafter, may be referred to hard ice cream (ice cream
standard)) was prepared. Sugar and starch syrup were used as the
sugars, butter and skim milk powder were used as the dairy products,
lO cellulose, casein Na and thickening polysaccharides were used as the
stabilizers, and a vanilla flavoring and a carotenoid pigment were used as
the other components.
[007 1]
[Table 5]
Water 65 6
Milk Fat
Milk Solid 18. 1
(Example 1)
In Example 1, microfibrillated ose of the microfibrillated
cellulose (D standard) was used and studied. As an example of the
brillated cellulose (D standard), commercially available CELISH
(registered trademark) FD—lOOG manufactured by Daicel Finechem Ltd.
was used, and as described later, soft cream of the ice cream standard
(hereinafter, may be referred to as soft cream (ice cream standard)) of
Example 1A, soft cream of the lacto—ice standard (hereinafter, may be
referred to as soft cream (lacto—ice standard)) of Example 1B, soft cream of
the fat—free ice tion standard (hereinafter, may be referred to as soft
cream (fat—free ice confection standard)) of Example 1C, and hard ice
cream of the ice cream standard (hereinafter, may be referred to as hard
ice cream (ice cream standard)) of e 1D were produced.
The solids fraction (microfibrillated cellulose content) of CELISH
FD—lOOG was measured to be 10% by weight. The specific surface area of
the microfibrillated cellulose in CELISH FD— 100G was measured to be 101
m2 / g, and the water retention thereof was measured to be 367%. The
viscosity of the water dispersion of microfibrillated cellulose when the
solids fraction of CELISH G was ed to 0.5% by weight was
measured at 52°C to be 170 CF. The rate of sedimentation when the
solids fraction was adjusted to 0.05% by weight was measured to be 1360
m1/g. The light transmission at a wavelength of 600 nm when the solids
fraction was adjusted to 0.02% by weight was measured to be 36.4%.
Table 6 shows the ement results.
[Table 6]
Microfibrillated Cellulose (D standard)
|SuracefArea (In)
Water ion (%)
Viscosity (CP)
Temperature
Rate of Sedimentation (ml/ g)
Light Transmission (0/0)
<Examp1e 1A>
A soft cream mix (ice cream standard) of Example 1A was
prepared by mixing the above—mentioned CELISH FD-lOOG with the soft
cream mix base (ice cream standard) shown in Table 2 so that the
microfibrillated cellulose t would be 0.1% by weight. The ratios of
the raw materials are shown in Table 7.
Subsequently, 1.7 L of the soft cream mix of Example 1A was put
into a frozen dessert tion apparatus (freezer NA6462WE, product
by Nissei Co., Ltd.) One hour after the start of freezing, approximately
1 10 g (approximately 140 ml) of soft cream was taken out and served on a
cone cup (No. 15 cone, product by Nissei Co., Ltd.) by twisting upward the
soft cream three and a half turns to give the soft cream (ice cream
standard) of Example 1A. The overrun of the ing soft cream was
43%, and the product temperature when the product was taken out of the
freezer was —5.2°C. Throughout the present specification, the “product
ature when the product was taken out of the freezer” refers to the
ature of the soft cream immediately after the serving.
Immediately after the production, the soft cream of Example 1A
was put in an incubator maintained at 35°C, and the cone cup was
ted in an upright position with a cup holder on a plate in the
tor as shown in The door was closed so that external air
would not enter, and the soft cream of Example 1A was observed as it
melted and fell. In doing so, the time from when the soft cream of
Example 1A was put in the incubator until when the soft cream on the
cone cup melted and fell onto the plate was measured.
In addition, the soft cream of Example 1A was eaten, and the
quality of the soft cream in terms of texture, mouth feel and flavor was
studied. The results are shown in Table 8.
<Example lB>
Soft cream of Example 1B was produced in the same manner as in
Example 1A by mixing the above-mentioned CELISH FD-lOOG with the
soft cream mix base (lacto-ice standard) shown in Table 3 so that the
microfibrillated cellulose content would be 0.1% by weight and preparing a
soft cream mix (lacto—ice standard) of Example 1B. The overrun of the
resulting soft cream was 42%, and the product temperature When the
product was taken out of the freezer was -5.1°C. The ratios of the raw
materials of the soft cream mix (lacto—ice standard) of Example 1B are
shown in Table 7.
The time until melting and falling of the soft cream of Example 1B
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 1B was eaten, and the texture, mouth feel and
flavor thereof were studied. The s are shown in Table 8.
<Examp1e 1C>
Soft cream (fat—free ice confection standard) of e 1C was
produced in the same manner as in Example 1A by mixing the
above—mentioned CELISH FD— 1000: with the soft cream mix base shown in
Table 4 so that the microfibrillated cellulose content would be 0.1% by
weight and preparing a soft cream mix (fat—free ice confection standard) of
Example 1C. The overrun of the ing soft cream was 50%, and the
product temperature when the product was taken out of the freezer was
—5.8°C. The ratios of the raw als of the soft cream mix of Example
1C are shown in Table 7.
2O The time until g and falling of the soft cream of e 1C
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 1C was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 8.
<Example 1D>
A hard ice cream mix (ice cream standard) of Example 1D was
prepared by mixing the above-mentioned CELISH FD—lOOG with the hard
ice cream mix base (ice cream standard) shown in Table 5 so that the
microfibrillated cellulose t would be 0.3% by weight.
The ratios of the raw materials of the mix for the hard ice cream of
Example 1D are shown in Table 7.
uently, the hard ice cream mix of Example ID was put in a
frozen dessert production apparatus (CARPIGIANI 243) and frozen so as to
have an overrun of 80% to give cream having an overrun of 72% and a
product temperature of —5.5°C when the product was taken out of the
freezer.
Approximately 86 g (approximately 140 m1) of the ice cream was
taken out and served on a cone cup (No. 15 cone, product by Nissei Co.,
Ltd.) by ng upward the ice cream three and a half turns, and then
soon put in a freezer at -20°C. The ice cream was left in the freezer for 24
hours or longer to be hardened. Thus, the hard ice cream (ice cream
standard) of Example ID was produced. The product temperature after
the hardening was approximately —20°C.
The time until melting and falling of the hard ice cream of Example
ID was ed in the same manner as in Example 1A. In addition, the
hard ice cream of Example ID was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 8.
[0079]
<Comparative Example 1A>
Soft cream (ice cream standard) of Comparative e 1A was
produced in the same manner as in Example 1A except that no
microfibrillated cellulose was added and only the soft cream mix base (ice
cream standard) shown in Table 2 was used. The overrun of the resulting
soft cream was 40%, and the product temperature when the product was
taken out of the freezer was —5.2°C. The ratios of the raw materials of the
soft cream mix of ative Example 1A are shown in Table 7.
The time until melting and falling of the soft cream of Comparative
Example 1A was measured in the same manner as in Example 1A. In
addition, the soft cream of Comparative Example 1A was eaten, and the
texture, mouth feel and flavor thereof were d. The results are
shown in Table 8.
<Cornparative Example 1B>
Soft cream (lacto—ice standard) of Comparative e 1B was
produced in the same manner as in Example 1B except that no
microfibrillated cellulose was added and only the soft cream mix base
(lacto-ice rd) shown in Table 3 was used. The overrun of the
resulting soft cream was 48%, and the product temperature when the
t was taken out of the freezer was —5.4°C. The ratios of the raw
materials of the soft cream mix of Comparative Example 1B are shown in
Table 7.
The time until melting and falling of the soft cream of Comparative
Example 1B was measured in the same manner as in Example 1B. In
on, the soft cream of Comparative Example 1B was eaten, and the
texture, mouth feel and flavor thereof were studied. The results are
2O shown in Table 8.
<Comparative Example 1C>
Soft cream (fat—free ice confection standard) of Comparative
Example 1C was produced in the same manner as in Example 1C except
that no microfibrillated cellulose was added and only the soft cream mix
base (fat-free ice confection standard) shown in Table 4 was used. The
overrun of the resulting soft cream was 46%, and the product temperature
when the product was taken out of the r was —8.0°C. The ratios of
the raw materials of the soft cream mix of Comparative Example 10 are
shown in Table 7.
The time until melting and falling of the soft cream of Comparative
Example 1C was measured in the same manner as in Example 1C. In
addition, the soft cream of Example 1C was eaten, and the texture, mouth
feel and flavor thereof were studied. The s are shown in Table 8.
<Comparative Example 1D>
Hard ice cream (ice cream standard) of Comparative Example 1D
was produced in the same manner as in Example 1D except that no
microfibrillated cellulose was added and only the hard ice cream mix base
(ice cream standard) shown in Table 5 was used. The overrun of the
resulting hard ice cream when it was taken out of the r was 80%, and
the product temperature when the product was taken out of the freezer
was —6.3°C. The product temperature after the hardening was
approximately —20°C. The ratios of the raw materials of the hard ice
cream mix (ice cream standard) of Comparative Example 1D are shown in
Table 7.
The time until melting and falling of the hard ice cream of
Comparative Example 1D was measured in the same manner as in
Example 1D. In addition, the hard ice cream of Comparative Example ID
was eaten, and the texture, mouth feel and flavor thereof were studied.
The results are shown in Table 8.
Comparison of the ed period of time with t to the time
until melting and falling between each e and each corresponding
ative Example is represented by a difference and a ratio between
the time until melting and falling (average) and the extended time until
melting and falling.
The extended period of time with respect to the time until melting
and falling was evaluated according to the difference between the time
until melting and falling of each Example (average) and that of each
corresponding Comparative Example. The difference of 30 s to 1
minute was evaluated as “1” (effective), the ence of 1 minute to 2
minutes was evaluated as “11” (significantly effective), and the difference of
2 minutes or more was evaluated as “111” kably effective).
The evaluation in the following Examples will also be made
according to the above—described criteria.
[Table 7]
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* Hard ice cream was hardened after taken out of the freezer and had an
end product temperature of approximately —20°C.
The results of Examples 1A to 1D have confirmed a significant
melting and falling delaying effect in the soft cream of any standard and in
the hard ice cream (ice cream standard) owing to the use of the material
mixes containing the microfibrillated cellulose (D standard).
(Example 2)
Frozen desserts of Examples 2A to 2C different in microfibrillated
cellulose (D standard) content were produced and tested in such manners
as described below.
In the water dispersion of microfibrillated cellulose of Example 2,
as in the case of Example 1, commercially available CELISH (registered
trademark) FD-lOOG manufactured by Daicel Finechem Ltd. was used as
an example of the “microfibrillated cellulose D rd”.
[0088]
<Example 2A>
Three types of mixes for soft cream of the ice cream standard which
are different in t of the microfibrillated cellulose (D standard) used
in Example 1 were prepared les 2A1 to 2A3).
The content of the microfibrillated cellulose (D standard) used in
e 1 was 0.1% by weight in e 2A1, 0.2% by weight in
Example 2A2, and 0.3% by weight in Example 2A3.
The ratios of the raw materials of the soft cream mixes (ice cream
rd) of Example 2A are shown in Table 9.
The time until melting and g of the soft cream of Example 2A
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 2A was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 10. Table 10
also shows the data of Comparative e 1A for comparison.
[Table 9]
Ice Cream Standard
Microfibrillated Cellulose
(D standard)
Example Example Example
2A1 2A2 2A3
Microfibrillated Cellulose Content 0. 1 0.2 0.3
Dairy Products 20.0 20.0
Stabilizers
Other Components
Water (Solid Content) —)(.0 (0.3)
Microfibrillated CM No No No
Cellulose -
Etherification
Water 62 .9
l l Total AmountiEi 100.0 1000 100.0
[Table 10]
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The results of Examples 2A1 to 2A3 indicate that the soft cream
(ice cream standard) having a microfibrillated cellulose (D standard)
t of 0.1% or more had a significant melting and falling delaying
effect. In practical use, it is most appropriate to add approximately 0.3%
by weight of the microfibrillated cellulose in terms of the costs and the
thickening of the material mix.
<Example 2B>
Three types of mixes for soft cream of the ice standard which
are different in content of CELISH FD—100G used in Example 1 were
prepared (Examples 2B1 to 2B3).
The content of the microfibrillated ose (D standard) used in
Example 1 was 0.07% by weight in Example 281, 0.1% by weight in
Example 2B2, and 0.2% by weight in Example 2B3.
The ratios of the raw materials of the soft cream mixes (lacto-ice
standard) of Example 2B are shown in Table 11.
The time until melting and falling of the soft cream (lacto-ice
standard) of Example 2B was measured in the same manner as in
e 1A.
In addition, the soft cream of Example 2B was eaten, and the
texture, mouth feel and flavor thereof were studied. The results are
shown in Table 12.
Table 12 also shows the data of Comparative Example 1B for
comparison.
[Table 1 1]
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The results of Examples 2B1 to 2B3 indicate that the soft cream
(lacto-ice standard) having a ibrillated cellulose (D standard)
content of 0.07% or more had a melting and g delaying effect on the
frozen desserts. In practical use, it is most appropriate to add
approximately 0. 1% by weight of the microfibrillated cellulose in terms of
the costs and the thickening of the material mix.
<Example 2C>
Two types of mixes for soft cream of the fat-free ice confection
standard which are different in content of CELISH FD—lOOG used in
Example 1 were prepared (Examples 2C1 and 2C2).
The content of the microfibrillated cellulose (D standard) used in
e 1 was 0.1% by weight in Example 2C1 and 0.2% by weight in
Example 2C2.
The ratios of the raw als of the soft cream mixes of Example
2C are shown in Table 13.
The time until melting and falling of the soft cream of Example 2C
was measured in the same manner as in Example 1A.
In addition, the soft cream of Example 2C was eaten, and the
texture, mouth feel and flavor thereof were studied. The results are
shown in Table 14.
Table 14 also shows the data of ative Example 1C for
comparison.
[0097]
[Table 13]
Fat—free Ice Confection
Microfibrillated Cellulose
D standard
2C1 2C2
Microfibrillated Cellulose Content O O . [O
1% by weight
W . 7
' I '7 s
Pureed Strawberry 23.1
Dairy Products NOOH .- Other Components . OIONOO
(Sohd Content)
Water (0.1) (0.2)
Dispersion of (Water Content) (0.9)
Microfibrillated l(1 8)
o No
Cellulose
Degree of Etherification —
Toalo _o.
[Table 14]]
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The s of Examples 2C1 and 2C2 indicate that the soft cream
(fat—free ice tion standard) having a microfibrillated cellulose (D
standard) content of 0.1% or more had a significant melting and falling
delaying effect on the frozen desserts. In practical use it is most
appropriate to add approximately 0.2% by weight of the microfibrillated
cellulose in terms of the costs and the thickening of the material mix.
[0 100]
(Example 3)
In Example 3, microfibrillated cellulose of the “microfibrillated
cellulose K standard” was used and the tests were performed.
As the microfibrillated cellulose (K standard), a water dispersion of
non—carboxymethylated brillated cellulose derived from a
never—dried pulp obtained using hinoki cypress wood flour as a raw
material h defatting, lignin removal, hemicellulose removal and
fibrillation steps was prepared under the following conditions.
[0 101]
[Defatting step]
Hinoki cypress wood flour was put in a filter paper e, and the
filter paper e was placed in a flask of a Soxhlet extractor containing
a mixed solution of toluene and ethanol (toluene : ethanol = 2 : 1). The
flask was placed in a hot water bath for 6 hours to extract and te fat
from the hinoki cypress wood flour. The defatted product was dried to
give defatted wood flour.
[0 102]
[Lignin removal step]
In a beaker containing 600 m1 of distilled water, 4 g of sodium
chlorite and 0.8 g of acetic acid, 10 g of the defatted wood flour was placed,
and the beaker was placed in a hot water bath at 70 to 80°C for 1 hour
under occasional stirring. Thereafter, without cooling, 4 g of sodium
chlorite and 0.8 g of acetic acid were added to further perform the heating
in the hot water bath, and this s was ed five times.
Thereafter, the resulting delignified pulp was collected by suction filtration
and washed with purified water repeatedly until the filtrate turned from
yellow to transparent and colorless.
[O 103]
[Hemicellulose removal step]
In a beaker, 300 ml of a mixture of 10g of the delignified pulp (in
solids content equivalents) and a 5% by weight sodium hydroxide aqueous
solution was prepared, and the beaker was placed in a hot water bath at
90°C for 2 hours. fter, the resulting pulp from which
hemicellulose was removed was collected by suction filtration and washed
with purified water repeatedly until the pH of the filtrate was confirmed to
be neutral to give a never—dried pulp.
[0 104]
llation step]
The never—dried pulp was fibrillated under the following conditions,
and a water sion of microfibrillated cellulose was obtained.
<Fibrillation conditions>
Fibrillating apparatus used: a stone mill type grinder (Serendipiter,
model: MKCA6—3) and grindstones (model: MKG—C) available from Masuko
Sangyo Co., Ltd
Rotation speed of grindstones: 1500 rpm
2O Other: Fibrillation was performed by further pressing the
tones by 620 um after they were in friction
[0 105]
<Example 3A>
The solids fraction (microfibrillated ose content) of the water
dispersion of the microfibrillated cellulose of Example 3A obtained as
described above was measured to be 0.97% by weight.
The specific surface area of the microfibrillated cellulose (K
standard) in the water dispersion of the brillated cellulose of
Example 3A was measured to be 168 m2/ g, and the water retention
thereof was measured to be 8196%.
The solids fraction of the water dispersion of the microfibrillated
cellulose of Example 3A was adjusted to 0.5% by weight, and the viscosity
thereof at a temperature of 53°C was measured to be 170 CF. The solids
fraction of the water dispersion was adjusted to 0.05% by , and the
rate of sedimentation was measured to be 2000 ml/ g. The solids fraction
of the water dispersion was adjusted to 0.02% by weight, and the light
transmission at a wavelength of 600 nm was measured to be 62.7%. The
parameters of the microfibrillated cellulose (K standard) in e 3A are
shown in Table 15. A soft cream mix (ice cream standard) of Example 3A
was prepared by mixing the water dispersion of the microfibrillated
cellulose of Example 3A with the soft cream mix base (ice cream rd)
shown in Table 2 so that the solids fraction of the microfibrillated cellulose
of Example 3A would be 0.1% by weight. The ratios of the raw materials
of the soft cream mix (ice cream rd) of Example 3A are shown in
Table 16.
[0 1 06]
Subsequently, soft cream (ice cream rd) of Example 3A was
produced in the same manner as in Example 1A.
The n of the resulting soft cream was 38%, and the product
temperature was —5.8°C.
[O 107]
Then, the time until melting and falling of the soft cream of
Example 3A was measured in the same manner as in Example 1A.
In addition, the soft cream of e 3A was eaten, and the
texture, mouth feel and flavor thereof were studied. The results are
shown in Table 17.
Table 17 also shows the data of Comparative Example 1A for
comparison with Example 3A.
<Example 38>
A water dispersion of microfibrillated cellulose of e 3B
having a solids fraction of 0.73% was prepared in the same manner as in
Example 3A.
The specific surface area of the microfibrillated cellulose (K
standard) of Example 3B was measured to be 232 m2 / g, and the water
retention f was measured to be 12057%.
[0 109]
The solids fraction of the water sion of microfibrillated
cellulose containing the microfibrillated ose (K standard) of Example
SB was ed to 0.5% by weight, and the viscosity thereof at a
temperature of 60°C was measured to be 3140 cP. The solids fraction of
the water dispersion was adjusted to 0.05% by weight, and the rate of
sedimentation was measured to be 2000 ml/ g. The solids fraction of the
water dispersion was adjusted to 0.02% by weight, and the light
transmission at a wavelength of 600 nm was measured to be 80.8%. The
parameters of the microfibrillated cellulose (K standard) in Example 3B are
shown in Table 15.
[01 10]
Soft cream —ice standard) of Example 3B was produced in the
same manner as in Example 3A by mixing the above—mentioned water
dispersion of microfibrillated cellulose with the soft cream mix base
(lacto-ice standard) shown in Table 3 so that the microfibrillated cellulose
content would be 0.1% by weight and preparing a soft cream mix (lacto—ice
standard) of Example 3B. The overrun of the resulting soft cream was
40%, and the product temperature when the product was taken out of the
freezer was -5.3°C. The ratios of the raw materials of the soft cream mix
(lacto—ice standard) of e 3B are shown in Table 16.
The time until melting and falling of the soft cream of Example 3B
was measured in the same manner as in e 3A. In addition, the
soft cream of Example 38 was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 17. Table 17
also shows the data of Comparative Example 18 for comparison with
Example 3B.
[O 1 1 1]
<Example 30>
Soft cream (fat—free ice confection standard) of Example BC was
produced in the same manner as in Example 3A by mixing the
microfibrillated cellulose (K rd) used in Example 3A with the soft
cream mix base (fat—free ice confection standard) shown in Table 4 so that
the microfibrillated cellulose (K standard) content would be 0.1% by
weight and ing a soft cream mix (fat-free ice confection standard) of
Example 3C. The overrun of the resulting soft cream was 48%, and the
t temperature was —7.5°C. The ratios of the raw materials of the
soft cream mix (fat—free ice confection standard) of Example 3C are shown
in Table 16. The time until melting and falling of the soft cream of
Example BC was measured in the same manner as in Example 3A.
In addition, the soft cream of Example 3C was eaten, and the
texture, mouth feel and flavor f were studied. The results are
shown in Table 17. Table 17 also shows the data of Comparative
Example 1C for comparison with Example 3C.
[01 12]
<Example 3D>
A hard ice cream mix (ice cream standard) of Example 3D was
prepared by mixing the water dispersion of microfibrillated cellulose used
in Example 3A with the hard ice cream mix base (ice cream standard)
shown in Table 5 so that the microfibrillated cellulose (K standard) content
would be 0.3% by weight.
The hard ice cream mix of Example 3D was frozen in the same
manner as in Example 1D to give ice cream (ice cream standard) having an
n of 71% and a product temperature of ~5.5°C when the product
was taken out of the freezer.
imately 86 g ximately 140 ml) of the ice cream was
taken out and served on a cone cup (No. 15 cone, product by Nissei Co.,
Ltd.) by twisting upward the ice cream three and a half turns, and then
soon put in a freezer at —20°C. The ice cream was left in the freezer for 24
hours to be hardened. Thus, the hard ice cream of Example 3D was
produced. The product temperature after the hardening was
approximately —20°C.
The ratios of the raw materials the hard ice cream mix of Example
3D are shown in Table 16.
The time until melting and falling of the hard ice cream of Example
SD was measured in the same manner as in Example 3A. In addition, the
hard ice cream of e SD was eaten, and the e, mouth feel and
flavor thereof were studied. The results are shown in Table 17 . Table 17
also shows the data of Comparative Example 1D for comparison with
Example 3D.
[01 13]
[Table 15]
Microfibrillated Cellulose (K standard)
Never—dried
Exampleié3A, 3C, 8D Example 3B
Water Retention (%) 8196 12057
Viscosity(()CPTemperature) 170 3140
. 3°C 60°C
Rate of ntation ml/g 2000 2000
Light Transmission (%) 62. 7 8-08
[O 1 14]
[Table 16]
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* Hard ice
cream was hardened after taken out of the freezer and had an en
d product temperature of approximately -20°C.
The results of Examples 3A to 3D have confirmed that a significant
effect of delaying g and falling of the frozen dessert was obtained in
the soft cream of any standard and the hard ice cream (ice cream
standard) that contain the microfibrillated cellulose (K standard) derived
from a never—dried pulp. In addition, comparison with the results of
Example 1 has ed that a better melting and falling delaying effect
was obtained in the soft cream of any standard and the hard ice cream (ice
cream standard) that contain the microfibrillated cellulose (K standard)
derived from a never-dried pulp than in those ning the
microfibrillated cellulose (D standard).
[01 17]
(Example 4)
Frozen desserts of Examples 481 to 484 different in content of
rboxymethylated microfibrillated cellulose (K standard) derived
from a never—dried pulp were produced and tested in such manners as
described below.
A water dispersion of microfibrillated cellulose containing
non-carboxymethylated microfibrillated cellulose (K standard) derived
from a never—dried pulp was prepared in the same manner as in e
3.
The solids fraction of the resulting water dispersion of the
non—carboxymethylated microfibrillated cellulose derived from a
never—dried pulp of Example 4 was measured to be 0.73% by weight.
The c surface area of the non—carboxymethylated
microfibrillated cellulose d from a never—dried pulp of Example 4 was
measured to be 260 m2/ g, and the water retention thereof was measured
to be 5338%.
The solids fraction of the water dispersion of the
non—carboxymethylated microfibrillated cellulose derived from a
never-dried pulp of e 4A was adjusted to 0.5% by weight, and the
viscosity thereof at a temperature of 50°C was measured to be 1330 CF.
The solids fraction of the water dispersion was adjusted to 0.05% by
weight, and the rate of sedimentation was measured to be 2000 ml/ g.
The solids fraction of the water dispersion was adjusted to 0.02% by
weight, and the light transmission at a wavelength of 600 nm was
measured to be 66.6%.
The parameters of the non—carboxymethylated microfibrillated
cellulose (K standard) derived from a dried pulp in Example 4 are
shown in Table 18.
[Table 18]
Microfibrillated Cellulose (K rd)
Neverd-drie
_SperfAw (mZ/g)
Water Retention (%)
Viscosity (cP) 1330
Temperature 50°C
Rate of Sedimentation (ml/ g) 1 2000
Light ission (%) 66.6
[0120]
Soft cream mixes —ice standard) each having a content of
non—carboxymethylated microfibrillated cellulose (K standard) derived
from a never—dried pulp of 0.05% by weight (Example 481), 0.07% by
weight le 4B2), 0.1% by weight (Example 4B3) or 0.2% by weight
2O (Example 4B4) were prepared in the same manner as in Example 2B
except that a water dispersion of the non-carboxymethylated
microfibrillated cellulose derived from a never—dried pulp of Example 4 was
used instead of the microfibrillated cellulose (D standard) used in Example
The ratios of the raw materials of the soft cream mixes (lacto—ice
standard) of Example 4B is shown in Table 19.
The time until melting and falling of the soft cream of Example 4B
was measured in the same manner as in Example 1A.
In on, the soft cream of Example 48 was eaten, and the
texture, mouth feel and flavor thereof were studied. The s are
shown in Table 20.
Table 20 also shows the data of Comparative Example 1B for
comparison.
[0 l 2 1]
[Table 19]
UoEU-.8>oZ I. odoH
Uhmfifiduw Unwfifiwuw 0.0045
MOMIOHOIQNH 803200 Odofi
UBEEQQESE cm.
9 Odofl
325:8 mafia
3 @5300 acoudoo 3:395 00.”on *3
3 § @8wa 30560.5 3mm Goflaoguofim
28 mEEwHSEm afififium wufivdomaoo «SEE 309 $33.
ofi “Vow
3855 «END IIIL 26 .550 Gomwhmmmwm vvpmawwmeowg Hagen?»
H983 H308
[Table 20]
oaawxm #9» H o. H
w @006 =oo~®H =Omrwfi =25 5 ad E
0% @090 tom~¢fi Evil” Emu: s‘mwum
EmuSBw 2&8me mm?
@3683 oEmem Hmv I
03339800 xm
083:8 ”Hammers: 3033 H90 98 Una Sfiofioafiwdoa firs
paw paw Eds wdfidm
2.33
gov 63 0E3 BENEQSB Guxms‘ mo 08$ mafia.“ paw
was» noNoofi 5505 82mm wagon“ wagon“, Aacofioaflwwofi wGEoE Aouggmv
usmchupaé 5535 poflom 05 paw povmofifi nowadago
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0E5 25% 08E; poommou 03mm 5a..»
on“ mfizfl M533 @250me
The results of Examples 4B1 to 4B4 have confirmed a significant
effect of ng melting and falling of the soft cream in the soft cream
(lacto—ice standard) containing 0.05% by weight or more of
non carboxymethylated microfibrillated ose (K standard) derived
from a never—dried pulp. In practical use, it is most appropriate to add
approximately 1.0% by weight of the ibrillated cellulose (K standard)
in terms of the costs and the thickening of the material mix.
In addition, comparison with the results of Example 2B has
confirmed that a better melting and g delaying effect was obtained in
the soft cream containing the microfibrillated cellulose (K standard)
derived from a never—dried pulp added at a certain concentration than in
the soft cream containing the microfibrillated cellulose (D standard) added
at the same concentration.
[0 124]
(Example 5)
ymethylated microfibrillated cellulose (K standard) d
from a never—dried pulp was prepared in such a manner as described
below, and frozen desserts of Examples 5A to SE were produced using the
cellulose and .
[0 125]
<Example 5A>
A never—dried pulp was obtained in the same manner as in
Example 3. Thereafter, an aqueous on was ed for the CM by
mixing 5.8 parts by weight of sodium monochloroacetate and 67.5 parts
by weight of purified water, 16.7 parts by weight of the never—dried pulp
(solid content: 1 1.9%) was put in the aqueous on under stirring, and
the stirring was carried out at room temperature for 30 minutes.
Thereafter, 10 parts by weight of a 30% sodium hydroxide aqueous
solution was added under continued stirring, and the stirring was carried
out at room temperature for 30 minutes. Then, the solution was heated
at 70°C for 1 hour and cooled to 30°C, and subsequently neutralized to pH
7.0 to 7.5 with acetic acid (the stirring was terminated at this point).
Thereafter, the carboxymethylated pulp was collected by suction filtration
and washed with purified water several times.
The resulting carboxymethylated pulp was fibrillated in the same
manner as in Example 3, and a water dispersion of the carboxymethylated
microfibrillated cellulose of Example 5A was ed.
[0 126]
The solids fraction of the resulting water sion of the
carboxymethylated microfibrillated cellulose of Example 5A was measured
to be 1.61% by .
The specific surface area of the carboxymethylated microfibrillated
cellulose (K standard) of Example 5A was measured to be 247 m2 / g, the
water retention thereof was measured to be 15632%, and the degree of
etherification was measured to be 0.06.
The solids fraction of the water dispersion of the
carboxymethylated microfibrillated cellulose of Example 5A was adjusted
to 0.5% by weight, and the viscosity thereof at a ature of 58°C was
ed to be 325 CF. The solids fraction of the water dispersion was
adjusted to 0.05% by weight, and the rate of sedimentation was measured
to be 2000 ml/ g. The solids fraction of the water dispersion was adjusted
to 0.02% by weight, and the light transmission at a wavelength of 600 nm
2O was measured to be 92.4%. The parameters of the ymethylated
microfibrillated cellulose (K standard) in Example 5A are shown in Table
A soft cream mix (ice cream standard) of Example 5A was prepared
by mixing the water dispersion of the carboxymethylated ibrillated
cellulose of Example 5 with the soft cream mix base (ice cream standard)
shown in Table 2 so that the content of the carboxymethylated
microfibrillated cellulose of e 5A would be 0.1% by weight. The
ratios of the raw materials of the soft cream mix of e 5A are shown
in Table 22.
[O 128]
Subsequently, soft cream (ice cream standard) of Example 5A was
produced in the same manner as in Example 1A using the soft cream mix
of Example 5A. The overrun of the resulting soft cream was 39%, and the
product temperature when the product was taken out of the freezer was
~5.0°C.
The time until melting and falling of the soft cream of Example 5A
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 5A was eaten, and the texture, mouth feel and
flavor f were studied. The results are shown in Table 23. Tables
22 and 23 also show the data of Comparative Example 1A for comparison
with Example 5A.
[0 1 29]
<Example 5B>
A water dispersion of carboxymethylated microfibrillated cellulose
of Example 5B was prepared in the same manner as in Example 5A.
The solids fraction of the resulting carboxymethylated
2O brillated cellulose (K rd) of Example 5B was 0.82% by
weight.
The specific surface area of the carboxymethylated microfibrillated
cellulose (K standard) of Example SB was measured to be 267 m2 / g, the
water retention thereof was measured to be 14209%, and the degree of
etherification was measured to be 0.06.
The solids fraction of the water dispersion of microfibrillated
ose containing the carboxymethylated microfibrillated cellulose (K
standard) of Example 5B was adjusted to 0.5% by weight, and the Viscosity
f at a temperature of 55°C was measured to be 2 170 CF. The solids
fraction of the water dispersion was adjusted to 0.05% by weight, and the
rate of ntation was measured to be 2000 ml/ g. The solids fraction
of the water dispersion was adjusted to 0.02% by weight, and the light
transmission at a wavelength of 600 nm was measured to be 85.8%. The
parameters of the carboxymethylated microfibrillated cellulose (K
standard) in Example 5B are shown in Table 21.
[0 1 3 1]
[Table 2 l]
Microfibrillated Cellulose (K standard)
Never—dried + Carboxymethylated
Example5A, 5C, SD, SE Example 5B
Water Retention (%) 15632 14209
Viscosity (cP) 325 2170
Temperature 58°C 5. 5°C
Rate of Sedimentation (ml/ g) 2000 2000
Light Transmission (%)
Degree of Etherification m
[o 132]
A soft cream mix (lacto—ice standard) of Example 5B was prepared
by mixing the water dispersion of the microfibrillated cellulose of e
5B with the soft cream mix base (lacto—ice rd) shown in Table 3 so
that the carboxymethylated microfibrillated cellulose content would be
0.1% by weight. The ratios of the raw materials of the soft cream mix of
Example SB are shown in Table 22.
[0 133]
Subsequently, soft cream (lacto—ice standard) of Example 5B was
produced in the same manner as in Example 5A using the soft cream mix
of Example 5B. The overrun of the resulting soft cream was 4 1%, and the
product temperature when the product was taken out of the freezer was
The time until g and falling of the soft cream of Example 5B
was measured in the same manner as in Example 5A. In on, the
soft cream of Example SB was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 23. Tables
22 and 23 also show the data of Comparative Example 18 for comparison
With e 5B.
<Examp1e 5C>
Soft cream (fat—free ice confection standard) of e SC was
produced by mixing the water dispersion of the carboxymethylated
microfibrillated cellulose used in Example 5A with the soft cream mix base
(fat—free ice confection standard) shown in Table 4 so that the
brillated cellulose (K standard) content would be 0.1% by weight.
The ratios of the raw materials of the soft cream mix of Example 5C are
2O shown in Table 22.
Subsequently, soft cream of Example 5C was produced in the same
manner as in Example 5A using the soft cream mix of Example 5C. The
overrun of the resulting soft cream (fat—free ice confection standard) was
45%, and the product temperature when the product was taken out of the
freezer was -6.3°C.
The time until melting and falling of the soft cream of Example BC
was measured in the same manner as in Example 5A. In addition, the
soft cream of Example SC was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 23. Tables
22 and 23 also show the data of Comparative Example 1C for comparison
with Example 5C.
[0 1 36]
<Examp1e 5D>
A hard ice cream mix (ice cream standard) of Example SD was
prepared by mixing the water dispersion of the microfibrillated cellulose
used in Example 5A with the hard ice cream mix base (ice cream standard)
shown in Table 5 so that the microfibrillated cellulose t would be
0.3% by weight. The ratios of the raw materials of the hard ice cream mix
of Example 5D are shown in Table 22.
The hard ice cream mix of Example SD was frozen in the same
manner as in Example 1D to give ice cream having an overrun of 78% and
a product temperature of -6.3°C when the product was taken out of the
freezer.
Approximately 86 g (approximately 140 ml) of the ice cream was
taken out and served on a cone cup (No. 15 cone, t by Nissei Co.,
Ltd.) by twisting upward the ice cream three and a half turns, and then
2O soon put in a freezer at —20°C. The ice cream was left in the freezer for 24
hours to be hardened. Thus, the hard ice cream (ice cream standard) of
Example SD was ed. The product temperature after the hardening
was approximately —20°C.
[0 1 37]
The time until melting and falling of the hard ice cream of Example
SD was measured in the same manner as in Example 5A. In addition, the
hard ice cream of Example SD was eaten, and the e, mouth feel and
flavor thereof were studied. The results are shown in Table 23. Tables
22 and 23 also show the data of Comparative Example 1D for comparison
with Example 5D.
[0 1 38]
<Example 5E>
A high overrun soft cream mix (ice cream standard) of Example SE
was prepared by mixing the water dispersion of the carboxymethylated
microfibrillated cellulose of Example 5A with the soft cream mix base (ice
cream standard) shown in Table 5 so that the carboxymethylated
microfibrillated ose (K rd) content would be 0.1% by weight.
The high overrun soft cream mix of Example SE was frozen in the
same manner as in Example 1D to give high overrun soft cream (ice cream
rd) having an overrun of 79% and a product temperature of —6. 1°C
when the product was taken out of the freezer.
The ratios of the raw materials of the high overrun soft cream mix
of Example 5E are shown in Table 22.
The time until melting and falling of the high overrun soft cream
(ice cream rd) of Example SE was measured in the same manner as
in Example 5A.
In addition, the soft cream of Example SE was eaten, and the
2O texture, mouth feel and flavor thereof were studied. The results are
shown in Table 23. Table 23 also shows the data of ative
e 5 for comparison with Example SE.
[0 139]
<Comparative Example 5>
A soft cream mix (ice cream standard) containing no
microfibrillated cellulose was prepared in the same manner as in
Comparative Example 1A.
The high overrun soft cream mix of Comparative Example 5 was
frozen in the same manner as in Example SE to give high overrun soft
cream (ice cream standard).
The overrun of the resulting soft cream of Comparative Example 5
was 80%, and the product ature when the product was taken out of
the freezer was —5.8°C. The time until melting and falling of the soft
cream of Comparative Example 5 was ed in the same manner as in
Example 5A. In addition, the soft cream of Comparative Example 5 was
eaten, and the texture, mouth feel and flavor thereof were studied. The
results are shown in Table 23.
[O 1 40]
[Table 22]
mango 38.5 :9 :9 OOH
#880 ammmtom 02 Edmucwum
9830
SH Sago on: cfivmmum
«dam
ombbmm uoo Emvufiw
038$me 0.9:
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03588” o.
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$830 Ubwvnwpm
viadummfioooEwam ‘
02 :3
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8 mo cams?
Ecozooumfi baonawbw $05on fig Eomv$8300 houseficfidoo 20
mammsw
«£50934 Bed oonoD 3
93 mavumwflsfim EoEESm mpnmaomaoo aoflumoaflofim §
~83an EEG 25 .850 333 «5659waUBMEuM—mwouo. 335200 3523
188‘
[Table 23]
. .
53:95 figvfifim ommamxm o- 5mm: RPM =0¢b
«5th H H
ammmflow 58.5
03 vfiuwbwmfiov
fl$30 Hmwcfim oafimxmam m.
o- HIKE
3mm Emcee okra—damage .mm
8H ofimfidxmOn =ofivm
ooaémm Gosoomnoo c.8355 oiambwmfio oEwam =OHKA onrmH =Ofimfi
038memm =oormm =oo.mm Eye: Wm
uofiofig mecqmym oiumhmmao 2&8me . =m§h
03am«m =09“. =o§m :om.w
02 ugenfiw
=mob
«Ogden we mo 8
333353 who Q emmhgfl
35695
G313 35% :% yoga mfifiofi mafia wnEoE mans SGoEeuSmwva—H wagon“ totem n Ens Manama uuuqofinv mfifloa
cam SvaE wage
05 3a.: 23 :35 EB 5G5 was .«0
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one waged:
3: wag tam 08S 25¢ 053
* Hard ice cream was hardened after taken out of the freezer and had an
end product temperature of approximately -20°C.
[O 142]
The results of Examples 5A to SE have confirmed that a significant
effect of ng melting and falling of the frozen dessert was obtained in
the soft cream of any standard and the hard ice cream (ice cream
rd) that contain the carboxymethylated microfibrillated cellulose (K
standard). The results of Example 5E has confirmed that a cant
melting and falling delaying effect was obtained also in the soft cream (ice
cream standard) having a high overrun (80%). Comparison with the
results of Examples 1 and 3 has confirmed that a still better melting and
falling delaying effect was obtained in the soft cream of any standard and
the hard ice cream (ice cream standard) that contain the
carboxymethylated microfibrillated cellulose (K standard) derived from a
never—dried pulp.
[O 143]
(Example 6)
Frozen desserts of Examples 6A to 6D different in content of
ymethylated microfibrillated cellulose (K standard) derived from a
dried pulp were produced and tested in such manners as described
below.
[0144]
<Example 6A>
Three types of mixes for soft cream of the ice cream standard which
are different in content of carboxymethylated microfibrillated cellulose (K
standard) derived from a never—dried pulp were prepared (Examples 6A1 to
6A3) in the same manner as in Example 2A except that the water
dispersion of the microfibrillated cellulose d from a never-dried pulp
of Example 5A was used instead of the ibrillated cellulose (D
standard) used in Example 1.
The content of the carboxymethylated microfibrillated cellulose (K
standard) derived from a dried pulp was 0.1% by weight in Example
6A1, 0.2% by weight in Example 6A2, and 0.3% by weight in Example 6A3.
The ratios of the raw als of the soft cream mixes (ice cream
standard) of Example 6A are shown in Table 24.
The time until melting and falling of the soft cream of Example 5A
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 5A was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 25.
Table 25 also shows the data of Comparative Example 1A for
comparison.
[0 145]
[Table 24]
Ice Cream Standard
Microfibrillated ose
Never—drie5K standard)+ ymethylated
Example Example Example
6A1 6A2 6A3
Microfibrillated Cellulose (K standard)
Content (0 by weight) -°‘°’
130 129
Dairy Products 20.0 20.0 20.0
Emulsifiers 0.7 0.7
Stabilizers 0.4
Other Components 0. 1 0.1
Amount to add 18.6 1
Water
(Solid Content). (0.3)
Dispersion
Of (Water Content) (122) (18 3)
Microfibrillated
clllllllose_
Degree of Etherification O06
Water 59.5
V W 7
_____
‘ Total Ainount
[0 146]
[Table 25]
2%?me =Omivfi =0m =O¢
agenda NH mH
panama
v:UBNTEonbnOQuMO oamfiwxm poow .iomimfi Emma =OH
08:58
G380 + oaamxm Ted
08 Efizuéegz >oZ
ofiugmmfioo ofimawxm 4:
Emeusw .,.
mo 3.2me mfiafl wfizfl MESS “common Mafia
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083:8 «taxpomaou Soxwu Do 98
Moi Una paw paw
983 paw
356380 was» 83on Bow
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fl 05 5G5 magma
uBflEnmeaz poSUOHm Ens $2 Ems ENV Ens @8qu 8pr
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The results of Examples 6A1 to 6A3 have confirmed a significant
g and falling delaying effect in the soft cream (ice cream standard)
containing 0. 1% by weight or more of the carboxymethylated
microfibrillated cellulose (K standard) derived from a never—dried pulp. In
practical use it is most appropriate to add approximately 0.3%
7 by weight
of the microfibrillated cellulose in terms of the costs and the thickening of
the material mix.
<Example 6B>
A water dispersion of carboxymethylated microfibrillated cellulose
d from a never—dried pulp of Example 6B was prepared in the same
manner as in Example 5A.
The solids fraction of the resulting carboxymethylated
microfibrillated cellulose (K standard) of Example 6B was 1.12% by
weight.
The specific surface area of the carboxymethylated microfibrillated
cellulose (K standard) of Example 6B was ed to be 263 m2 / g, the
water retention thereof was measured to be 12247%, and the degree of
etherification was measured to be 0.04.
[0 148]
The solids fraction of the water dispersion of microfibrillated
cellulose containing the carboxymethylated microfibrillated cellulose (K
standard) of e 6B was ed to 0.5% by weight, and the viscosity
thereof at a temperature of 5.100 was measured to be 970 CP. The solids
fraction of the water dispersion was ed to 0.05% by weight, and the
rate of sedimentation was measured to be 2000 m1/ g. The solids fraction
of the water dispersion was adjusted to 0.02% by weight, and the light
transmission at a ngth of 600 nm was measured to be 89.0%. The
parameters of the carboxymethylated microfibrillated cellulose (K
standard) in Example 6B are shown in Table 26.
[0 149]
Five types of mixes for soft cream of the lacto-ice standard which
are different in content of carboxymethylated microfibrillated cellulose (K
standard) were prepared (Examples 6B1 to 6B5) in the same manner as in
Example 2B except that the water dispersion of the microfibrillated
cellulose of Example 6B was used instead of the microfibrillated cellulose
(D standard) used in Example 1.
The content of the carboxymethylated microfibrillated cellulose (K
standard) derived from a never—dried pulp was 0.01% by weight in
e 6B1, 0.05% by weight in Example 682, 0.07% by weight in
Example 6B3, 0.1% by weight in Example 6B4, and 0.2% by weight in
Example 6B5.
The ratios of the raw materials of the soft cream mixes (lacto-ice
standard) of Example 6B are shown in Table 27.
The time until melting and falling of the soft cream (lacto—ice
standard) of Example 6B was measured in the same manner as in
Example 1A. In addition, the soft cream of Example 6B was eaten, and
the texture, mouth feel and flavor thereof were studied. The results are
shown in Table 28.
Table 28 also shows the data of Comparative Example 1B for
comparison.
[Table 26]
ibrillated ose
(K rd)
Neverdried + Carbo meth lated
Spemfic Surface Area In2 /g
Water Retention (%) 12247
Viscosity(()CP 970
Temperature 5 1 °C
Rate of Sedimentation ml/g 2000
[o 150]
[Table 27]
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Awaucfiw Ugflhfivfimxonamo 2993mm vmo 83 mm .
w bmdo
wawqfim v:
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02-303 usgfinmegz +33%-“:va 0389mm '5mod $0.9 :3; we» 3.0 Elmo odoH
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[Table 28]
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Bufiwxm wmm H =Ofiom =mo~wm 0m
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[o 152]
The results of Examples 6A1 to 6B5 have confirmed a significant
melting and g delaying effect in the soft cream (lacto-ice standard)
containing the carboxymethylated brillated cellulose (K rd)
derived from a never—dried pulp even in the case Where the microfibrillated
cellulose (K standard) content was 0.01% by .
The melting and falling delaying effect will be further improved by
increasing the amount of the carboxymethylated microfibrillated ose
(K standard) d from a never—dried pulp to add to 0.1% by weight. In
practical use, however, it is most appropriate that the content is
imately 0.2% by weight in terms of the costs and the thickening of
the material mix. In addition, comparison between Example 4B and
Example 6B indicates that a more significant effect of delaying melting and
falling of the soft cream was obtained in the case of the carboxymethylated
microfibrillated cellulose (K standard) added in a certain amount than in
the case of the non—carboxymethylated microfibrillated cellulose (K
standard) added in the same amount.
[0 1 53]
<Example 6C>
Two types of mixes for soft cream of the fat—free ice tion
2O standard which are different in content of carboxymethylated
microfibrillated cellulose derived from a never—dried pulp were prepared
(Examples 6C1 and 6C2) in the same manner as in Example 20 except
that the water dispersion of the carboxymethylated microfibrillated
cellulose derived from a never-dried pulp of Example 5A was used instead
of the microfibrillated cellulose (D standard) used in Example 1.
The content of the ymethylated microfibrillated cellulose
derived from a never—dried pulp was 0.1% by weight in Example 6C1 and
0.2% by weight in Example 6C2.
The ratios of the raw materials of the soft cream mixes (fat—free ice
confection standard) of Example 60 are shown in Table 29.
The time until melting and falling of the soft cream (fat—free ice
confection standard) of Example 6C was ed in the same manner as
in Example 1A. In addition, the soft cream of Example 6C was eaten, and
the texture, mouth feel and flavor thereof were studied. The results are
shown in Table 30.
Table 30 also shows the data of Comparative Example 1C for
comparison.
[0 1 54]
[Table 29]
Fat—free Ice tion Standard
Microfibrillated Cellulose
dried + Carbo meth lated
Microfibrillated Cellulose
M,“ w WW """'“"”‘“'3'1'”
Pureed Strwberry 23.1%
Stabilizers 0.2 0.2
Other Components 0.2
Water Dispersion
(O ' 1) (02)
Microfibrillated Cellulose (6- 1) (12-2)
(Never-dried + Carboxymethylated) Yes Yes
[Table 30]
639.3% Apouflhfiogofiwo ofimfiwxm moo IINo @000 =O.V.mN :omhm .imH 5
325:8 vm
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[0 156]
The results of Examples 6C1 and 602 have confirmed a cant
effect of delaying melting and falling of the soft cream in the soft cream
(fat-free ice confection standard) ning 0.1% by weight or more of the
carboxymethylated microfibrillated cellulose (K standard) derived from a
never—dried pulp. In practical use, it is considered most appropriate to
add imately 0.2% by weight of the microfibrillated cellulose in terms
of the costs and the thickening of the material mix.
[0 157]
<Example 6D>
Three types of mixes for hard ice cream of the ice cream standard
which are different in t of carboxymethylated microfibrillated
cellulose (K standard) derived from a never—dried pulp were prepared
(Examples 6D1 to 6D3) using the water dispersion of the
ymethylated microfibrillated cellulose derived from a never~dried
pulp of Example 5A.
The content of the carboxymethylated microfibrillated cellulose (K
standard) derived from a never—dried pulp was 0.1% by weight in Example
6D1, 0.2% by weight in Example 6D2, and 0.3% by weight in Example
6D3.
The ratios of the raw materials of the hard ice cream mixes (ice
cream standard) are shown in Table 3 1.
The hard ice cream mix (ice cream standard) of the ice cream
standard of Example 6D was frozen in the same manner as in Example 1D.
Approximately 86 g (approximately 140 ml) of the ice cream was taken out
and served on a cone cup (No. 15 cone, t by Nissei Co., Ltd.) by
twisting upward the ice cream three and a half turns, and then soon put in
a freezer at —20°C. The ice cream was left in the r for 24 hours to be
hardened. Thus, the hard ice cream (ice cream standard) of Example 6D
was produced.
The time until melting and falling of the hard ice cream of the ice
cream standard e 6D was measured in the same manner as in
Example 1A. In addition, the hard ice cream of the ice cream standard of
Example 6D was eaten, and the e, mouth feel and flavor thereof were
studied. The results are shown in Table 32.
Table 32 also shows the data of Comparative e 1D for
comparison.
[Table 31]
Hard Ice Cream
Ice Cream Standard
brillated Cellulose
(K standard)
(Never-dried + Carbo meth lated}
Example
Microfibrillated Cellulose 6OD11
Content (% by weight)
“7 77
Sugars 13.0
Dairy Products 200 _
Emulsifiers
Stabilizers
Other Components 0 1 —
Water
Microfibrillated
Cellulose
Degree of Etherification I 0.06
59. 5
’ “"' '
Total Anmou
[0 1 59]
[Table 32]
Bafimxfl mom I =NmbH
58.5 Empfimum 333200 oaamxm was o tbmhw swfima
ooH Apouflhfiomfiwonuwo
9mm 9820 + oafidxm So :wmrmm :mmflm
8H pouflmuflmouofig kyozv o>EmthSoo oaemxm DH
mo Seam
owofiszoo E33 #50 mafia mafia v “common mafia.“
AHJmBB 053
ohgmnomfioymommy AOL paw one MESS
Aoé ens Ea fits
Moo.“
mfizfl
wages manna fidefioufiwmofi 3 Awnofiohfimwofi 053 @6338 popnouxo paw
we? noflwflfiwkrm
nouflmnfimeowfi Houoob find
fix; Mo
o5 558wa
55an 5.505
En: @535 we wmflHoE
psoohoo 84695 53 fig: eamv poflom 5:5 Scum
“0.3“on 083 83%
ES; ES.»
93 vane 85
BEE Uopcouxm 2.3
* Hard ice cream was hardened after taken out of the freezer and had an
end product temperature of approximately ~20°C.
[o 160]
The results of Examples 6D1 t0 6D3 have confirmed a significant
melting and falling delaying effect in the hard ice cream (ice cream
rd) containing 0.1% by weight or more of the carboxymethylated
microfibrillated cellulose (K standard) derived from a never—dried pulp.
In cal use, it is considered most appropriate to add
approximately 0.2% by weight of the microfibrillated ose in terms of
the costs and the thickening of the material mix.
[0 16 1]
<Example 6E>
Two types of mixes for soft cream of the ice cream standard which
are different in content of carboxymethylated microfibrillated cellulose (K
standard) derived from a never—dried pulp were prepared (Examples 6E1
and 6E2) using the water dispersion of the carboxymethylated
microfibrillated cellulose derived from a never—dried pulp of Example 5A.
The content of the carboxymethylated microfibrillated cellulose (K
standard) derived from a never—dried pulp was 0.1% by weight in Example
6E1 and 0.3% by weight in Example 6E2.
The ratios of the raw materials of the soft cream mixes are shown in
Table 33.
The soft cream mix (ice cream standard) of e 6E was frozen
in the same manner as in Example SE to give high overrun soft cream (ice
cream standard).
The time until melting and falling of the high overrun soft cream of
2O Example 6E was measured in the same manner as in Example 1A.
In addition, the high overrun soft cream of Example 6E was eaten,
and the e, mouth feel and flavor thereof were studied. The results
are shown in Table 34.
Table 34 also shows the data of Comparative Example 5 for
comparison.
[0 162]
[Table 33]
High Overrun Soft Cream
Ice Cream Standard
Ingredients Microfibrillated Cellulose (K standard)
Never—dried + Carbo meth lated
Comparative Example Example
Exam-1e 5 6E1 6E2
Sugars 13.2 12.9
Dairy Products 20.0 20.0
Stabilizers 0.4 0.4
Other Components 0. 1 1 .09b—I-Po
Amount to add 6.2 18.6
Water
Dispersion (Solid Content) (0. 1) (0.3)
Microfigrillatedf (Water t) (6-1) (18-3)
Cellulose
Yes Yes
[Table 34]
High Overrun Soft Cream
Ice Cream Standard
Microfibrillated Cellulose
(K standard)
Never~dried + Carbo meth lated
Comparative Example Example
e 5 6E1 6E2
Microfibrillated Cellulose
Content _(:/o by weight )
Product temperature when -5.8 -61 _5.
the product was taken out of
the freezer (°C)
n (%)
Texture, mouth feel and flavor Good
Time until melting and falling 6’32" 1 1’35" 16'46”
1 st measurement
Time until melting and falling 5'21" 1 1’38” 14’23”
2nd measurement
Time until melting and falling 5‘57" 1 1’37" 15’35"
avera_e
Extended period of time with 9138!!
respect to the time until melting
and fallin;
Ratio of extended time 1.0
until melting and falling
Effect tion —
[o 164]
The results of es 6E1 and 6E2 have confirmed a significant
effect of delaying melting and falling of the soft cream in the high overrun
soft cream (ice cream standard) containing 0.1% by weight or more of
carboxymethylated microfibrillated cellulose (K rd) derived from a
never-dried pulp. In practical use, it is considered most appropriate to
add approximately 0.3% by weight of the microfibrillated cellulose in terms
of the costs and the thickening of the material mix.
[0 165]
(Example 7)
Soft cream of the lacto—ice rd of Examples 7B1 to 7B6
containing carboxymethylated microfibrillated cellulose (K standard)
derived from a never—dried pulp which were varied in degree of
etherification was produced and tested in such manners as described
below.
<Example 7Bl>
The carboxymethylated microfibrillated cellulose (K standard)
derived from a never—dried pulp used in Example 7B1 was ed as
follows.
A never-dried pulp was obtained in the same manner as in
Example 3. Thereafter, an aqueous solution was prepared for the CM by
mixing 1.9 parts by weight of sodium monochloroacetate and 82.6 parts
by weight of purified water, 12.2 parts by weight of the never—dried pulp
(solid content: 16.4%) was put in the aqueous solution under stirring, and
the ng was carried out at room temperature for 30 minutes.
Thereafter, 3.3 parts by weight of a 30% sodium hydroxide aqueous
solution was added under continued stirring, and the stirring was carried
out at room temperature for 30 minutes. Then, the solution was heated
at 70°C for 1 hour and cooled to 30°C, and subsequently neutralized to pH
7.0 to 7.5 with acetic acid (the ng was ated at this point).
fter, the carboxymethylated pulp was collected by suction filtration
and washed with purified water several times. The ing
carboxymethylated pulp was fibrillated in the same manner as in Example
3, and a water dispersion of the carboxymethylated microfibrillated
ose derived from a never—dried pulp of Example 7B1 was obtained.
The solids fraction of the resulting water dispersion of the
carboxymethylated brillated cellulose derived from a never-dried
pulp of Example 7B1 was measured to be 0.77% by weight.
The degree of etherification of the ymethylated
microfibrillated cellulose (K standard) derived from a never~dried pulp of
Example 7B1 obtained as described above was 0.02.
The specific surface area of the carboxymethylated microfibrillated
cellulose (K standard) of Example 7B1 was measured to be 288 m2/ g, and
the water retention thereof was measured to be 1 1612%.
[o 167]
The solids fraction of the water dispersion of the brillated
cellulose containing the carboxymethylated microfibrillated cellulose (K
standard) of Example 7B1 was ed to 0.5% by weight, and the
Viscosity thereof at a temperature of 52°C was measured to be 1020 CF.
The solids fraction of the water dispersion was adjusted to 0.05% by
, and the rate of sedimentation was measured to be 2000 ml/ g.
The solids fraction of the water dispersion was adjusted to 0.02% by
weight, and the light transmission at a wavelength of 600 nm was
measured to be 67.9%. The parameters of the carboxymethylated
microfibrillated cellulose in e 7B1 are shown in Table 35.
Soft cream (lacto~ice standard) of Example 7B1 was produced in
the same manner as in Example 1A by mixing the carboxymethylated
microfibrillated ose (K rd) of Example 7131 with the soft cream
mix base (lacto—ice standard) shown in Table 3 so that the content of the
carboxymethylated microfibrillated cellulose (K standard) derived from a
never-dried pulp would be 0.1% by weight and preparing a soft cream mix
(lacto—ice rd) of Example 7B1. The overrun of the resulting soft
cream was 43%, and the product temperature when the product was
taken out of the freezer was -5.4°C. The ratios of the raw materials of the
soft cream mix of Example 7B1 are shown in Table 36.
The time until melting and falling of the soft cream of Example 781
was measured in the same manner as in Example 1A. In addition, the
soft cream of e 7B1 was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 37.
<Example 7B2>
The carboxymethylated microfibrillated cellulose (K standard)
derived from a never—dried pulp used in e 7B2 was prepared as
follows.
A never—dried pulp was obtained in the same manner as in
Example 3. Thereafter, an aqueous solution was prepared for the CM by
mixing 3.9 parts by weight of sodium monochloroacetate and 77.2 parts
by weight of purified water, 12.2 parts by weight of the never—dried pulp
(solid content: 16.4%) was put in the aqueous solution under stirring, and
the stirring was carried out at room temperature for 30 minutes.
Thereafter, 6.7 parts by weight of a 30% sodium hydroxide aqueous
solution was added under continued ng, and the stirring was d
out at room ature for 30 s. The subsequent processes were
carried out in the same manner as in Example 7B 1. The solids fraction of
the resulting water dispersion of the carboxymethylated microfibrillated
2O cellulose derived from a never—dried pulp of Example 7B2 was measured to
be 0.78% by weight.
The degree of etherification of the carboxymethylated
microfibrillated cellulose (K standard) derived from a never-dried pulp of
Example 7B2 obtained as bed above was 0.04.
The specific surface area of the carboxymethylated microfibrillated
cellulose (K standard) of Example 7B2 was measured to be 300 m2/ g, and
the water retention thereof was measured to be 14032%.
[0 169]
The solids fraction of the water dispersion of microfibrillated
cellulose containing the carboxymethylated microfibrillated cellulose (K
standard) of Example 7B2 was adjusted to 0.5% by weight, and the
viscosity f at a temperature of 57°C was measured to be 1930 CF.
The solids fraction of the water dispersion was adjusted to 0.05% by
weight, and the rate of ntation was measured to be 2000 ml/ g.
The solids fraction of the water dispersion was adjusted to 0.02% by
weight, and the light transmission at a wavelength of 600 nm was
measured to be 79.9%. The parameters of the carboxymethylated
microfibrillated cellulose (K standard) in Example 7B2 are shown in Table
Soft cream (lacto—ice standard) of Example 7B2 was produced in
the same manner as in Example 1A by mixing the carboxymethylated
microfibrillated ose (K standard) of Example 7B2 with the soft cream
mix base —ice standard) shown in Table 3 so that the t of the
carboxymethylated microfibrillated cellulose (K standard) derived from a
never—dried pulp would be 0.1% by weight and preparing a soft cream mix
(lacto—ice rd) of Example 7B2. The overrun of the resulting soft
cream was 42%, and the product temperature when the product was
2O taken out of the freezer was —5.5°C. The ratios of the raw materials of the
soft cream mix of Example 7B2 are shown in Table 36.
The time until g and falling of the soft cream of Example 782
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 782 was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 37.
[017O]
<Example 7B3>
The carboxymethylated microfibrillated cellulose (K standard)
derived from a never-dried pulp used in e SB (degree of
etherification: 0.06) was used as carboxymethylated microfibrillated
cellulose derived from a dried pulp of Example 7B3.
Soft cream (lacto—ice standard) of Example 7B3 was produced in
the same manner as in Example 1A by mixing the carboxymethylated
microfibrillated cellulose (K rd) of Example 5B with the soft cream
mix base (lacto-ice standard) shown in Table 3 so that the content of the
ymethylated microfibrillated ose (K standard) derived from a
never—dried pulp would be 0.1% by weight and preparing a soft cream mix
-ice standard) of Example 7B3. The overrun of the resulting soft
cream was 41%, and the product temperature when the product was
taken out of the freezer was —5.3°C. The ratios of the raw als of the
soft cream mix of the lacto—ice standard of Example 783 are shown in
Table 36.
The time until melting and falling of the soft cream of e 783
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 7133 was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 37.
<Example 7B4>
The carboxymethylated microfibrillated cellulose (K standard)
derived from a never—dried pulp used in Example 7B4 was prepared as
follows.
A never-dried pulp was obtained in the same manner as in
Example 3. Thereafter, an aqueous solution was prepared for the CM by
mixing 9.7 parts by weight of sodium monochloroacetate and 61.4 parts
by weight of purified water, 12.2 parts by weight of the never—dried pulp
(solid content: 16.4%) was put in the aqueous solution under stirring, and
the stirring was carried out at room temperature for 30 minutes.
Thereafter, 16.7 parts by weight of a 30% sodium hydroxide aqueous
solution was added under ued stirring, and the stirring was carried
out at room temperature for 30 minutes. The uent processes were
carried out in the same manner as in Example 7B1. The resulting
carboxymethylated pulp was fibrillated in the same manner as in Example
3, and a water dispersion of the carboxymethylated microfibrillated
cellulose derived from a dried pulp of Example 7B4 was obtained.
The solids fraction of the resulting water dispersion of the
carboxymethylated microfibrillated cellulose derived from a never-dried
pulp of Example 784 was measured to be 1.13% by weight.
The degree of etherification of the carboxymethylated
brillated cellulose (K standard) derived from a never—dried pulp of
e 7B4 obtained as described above was 0.10.
The specific surface area of the carboxymethylated brillated
cellulose (K standard) of Example 7B4 was measured to be 273 m2 / g, and
the water retention thereof was ed to be 17486%.
The solids fraction of the water dispersion of microfibrillated
cellulose containing the carboxymethylated microfibrillated cellulose (K
standard) of Example 7B4 was adjusted to 0.5% by weight, and the
viscosity thereof at a temperature of 4.8°C was measured to be 1950 cP.
The solids fraction of the water dispersion was adjusted to 0.05% by
weight, and the rate of sedimentation was measured to be 2000 ml/ g.
The solids fraction of the water dispersion was adjusted to 0.02% by
, and the light transmission at a wavelength of 600 nm was
measured to be 78.0%. The parameters of the carboxymethylated
microfibrillated cellulose (K standard) in Example 7B4 are shown in Table
Soft cream (lacto-ice standard) of Example 7B4 was ed in
the same manner as in Example 1A by mixing the carboxymethylated
brillated cellulose (K standard) of Example 7B4 with the soft cream
mix base (lacto-ice standard) shown in Table 3 so that the content of the
carboxymethylated microfibrillated cellulose (K standard) derived from a
never—dried pulp would be 0.1% by weight and preparing a soft cream mix
(lacto~ice standard) of Example 7B4. The overrun of the resulting soft
cream was 40%, and the product temperature when the product was
taken out of the freezer was -5.2°C. The ratios of the raw als of the
soft cream mix of the lacto—ice standard of Example 784 are shown in
Table 36. The time until g and falling of the soft cream of Example
784 was measured in the same manner as in Example 1A. In addition,
the soft cream of Example 7B4 was eaten, and the texture, mouth feel and
flavor thereof were studied. The results are shown in Table 37.
<Example 7B5>
The carboxymethylated microfibrillated cellulose (K standard)
derived from a never—dried pulp used in Example 7B5 was prepared as
2O follows.
A never-dried pulp was obtained in the same manner as in
Example 3. Thereafter, an s solution was prepared for the CM by
mixing 11.7 parts by weight of sodium monochloroacetate and 56.1 parts
by weight of purified water, 12.2 parts by weight of the never—dried pulp
(solid t: 16.4%) was put in the aqueous solution under stirring, and
the stirring was carried out at room temperature for 30 minutes.
Thereafter, 20.0 parts by weight of a 30% sodium ide aqueous
solution was added under continued stirring, and the stirring was carried
out at room temperature for 30 minutes. The subsequent processes were
carried out in the same manner as in Example 781. The resulting
carboxymethylated pulp was fibrillated in the same manner as in Example
3, and a water dispersion of the carboxymethylated microfibrillated
ose derived from a never—dried pulp of Example 735 was ed.
The solids fraction of the resulting water dispersion of the
carboxymethylated microfibrillated cellulose derived from a never—dried
pulp of Example 7B5 was measured to be 1.03% by weight.
The degree of etherification of the carboxymethylated
microfibrillated cellulose (K standard) derived from a never—dried pulp of
Example 7B5 obtained as described above was 0.13.
The specific surface area of the carboxymethylated microfibrillated
cellulose (K standard) of Example 7B5 was ed to be 244 m2/ g, and
the water retention thereof was measured to be 16071%.
[0174]
The solids fraction of the water dispersion of microfibrillated
cellulose containing the carboxymethylated microfibrillated cellulose (K
standard) of Example 7B5 was adjusted to 0.5% by weight, and the
Viscosity thereof at a ature of 54°C was measured to be 1 140 CF.
2O The solids fraction of the water dispersion was adjusted to 0.05% by
weight, and the rate of ntation was measured to be 2000 ml/ g.
The solids fraction of the water dispersion was adjusted to 0.02% by
weight, and the light transmission at a wavelength of 600 nm was
ed to be 76.9%. The parameters of the ymethylated
brillated cellulose (K standard) in Example 7B5 are shown in Table
Soft cream (lacto—ice rd) of Example 7B5 was produced in
the same manner as in Example 1A by mixing the carboxymethylated
microfibrillated cellulose (K standard) of Example 785 with the soft cream
mix base (lacto-ice standard) shown in Table 3 so that the content of the
carboxymethylated microfibrillated cellulose derived from a never—dried
pulp would be 0.1% by weight and preparing a soft cream mix (lacto-ice
standard) of Example 7B5. The overrun of the resulting soft cream was
42%, and the product temperature when the t was taken out of the
freezer was —5. 1°C. The ratios of the raw materials of the soft cream mix
of e 7B5 are shown in Table 36.
The time until melting and falling of the soft cream of Example 7135
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 7B5 was eaten, and the texture, mouth feel and
flavor f were d. The results are shown in Table 37.
[O 1 75]
<Example 7B6>
The ymethylated microfibrillated cellulose (K standard)
derived from a never—dried pulp used in Example 786 was ed as
follows.
A never-dried pulp was obtained in the same manner as in
Example 3. Thereafter, an aqueous solution was prepared for the CM by
2O mixing 13.6 parts by weight of sodium monochloroacetate and 50.9 parts
by weight of purified water, 12.2 parts by weight of the never—dried pulp
(solid content: 16.4%) was put in the s solution under stirring, and
the stirring was carried out at room temperature for 30 minutes.
Thereafter, 23.3 parts by weight of a 30% sodium hydroxide aqueous
solution was added under continued stirring, and the stirring was carried
out at room temperature for 30 minutes. The subsequent processes were
carried out in the same manner as in Example 7B1. The resulting
carboxymethylated pulp was fibrillated in the same manner as in Example
3, and a water dispersion of the carboxymethylated microfibrillated
ose derived from a never-dried pulp of Example 7B6 was obtained.
The solids on of the resulting water dispersion of the
carboxymethylated microfibrillated cellulose derived from a never—dried
pulp of Example 7B6 was measured to be 0.78% by weight.
The degree of etherification of the carboxymethylated
microfibrillated cellulose (K standard) derived from a never—dried pulp of
Example 7B5 ed as described above was 0.17.
The specific surface area of the carboxymethylated microfibrillated
cellulose (K standard) of Example 786 was measured to be 336 m2/ g, and
the water ion thereof was measured to be 18174%.
The solids fraction of the water dispersion of microfibrillated
cellulose containing the carboxymethylated microfibrillated ose (K
standard) of Example 7B6 was adjusted to 0.5% by weight, and the
Viscosity thereof at a temperature of 54°C was measured to be 8600 CF.
The solids fraction of the water dispersion was adjusted to 0.05% by
, and the rate of ntation was measured to be 2000 ml/ g.
The solids fraction of the water dispersion was adjusted to 0.02% by
, and the light ission at a wavelength of 600 nm was
measured to be 98.2%. The parameters of the carboxymethylated
microfibrillated cellulose (K standard) in Example 786 are shown in Table
Soft cream (lacto—ice standard) of Example 7B6 was produced in
the same manner as in Example 1A by mixing the carboxymethylated
microfibrillated cellulose (K standard) of Example 786 with the soft cream
mix base (lacto—ice standard) shown in Table 3 so that the content of the
carboxymethylated microfibrillated cellulose derived from a never-dried
pulp would be 0.1% by weight and preparing a soft cream mix (lacto—ice
standard) of Example 7B6. The overrun of the resulting soft cream was
46%, and the t temperature when the product was taken out of the
freezer was —5.3°C. The ratios of the raw materials of the soft cream mix
of Example 7B6 are shown in Table 36.
The time until melting and falling of the soft cream of Example 7B6
was measured in the same manner as in e 1A. In addition, the
soft cream of Example 786 was eaten, and the texture, mouth feel and
flavor f were studied. The results are shown in Table 37.
1O [0 1 77]
<Comparative Example 7B>
Table 37 also shows the data of Comparative Example 1B
containing no microfibrillated cellulose for evaluation of the time until
melting and falling.
[O 178]
[Table 35]
Microfibrillated Cellulose (K standard) 1
~dried + Carbo meth lated
Example Example Example e Example Example
7B1 7B2 7B4 7B5 7B6
Etherlficatlon
6‘ (fl
Area m2/
Water Retention 1 1 6 1 2 1 4032 15632
Viscosity (cP)
Temperature
Rate of
Sedimentation
ml ;
Light
Transmission %
[O 1 79]
[Table 36]
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ogmfiwxm amp
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BoSvoE 3mm E
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.850 E382
p335 commuummmmmo Bumzunueofi $25sz 38.
[Table 37]
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mH ma Va o
maawxm mmh 55*; ..0m =8
ma 3
vafiamxm wmb 0H6 :OmbH tom =3
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The results of Examples 7E1 to 7E6 have confirmed a melting and
falling delaying effect in the soft cream of the lacto-ice standard containing
the carboxymethylated microfibrillated cellulose (K standard) derived from
a never—dried pulp having a degree of etherification of 0.02 or more. The
suitable degree of etherification is 0.04 to 0.10, and 0.06 is most suitable.
[0 1 8 1]
(Example 8)
Carboxymethylated microfibrillated cellulose (K rd) derived
from a dried pulp of Example 8 was prepared in such a manner as
described below, and frozen desserts of Examples 8A to 8D were produced
using the cellulose and tested in the same manner as in Example 1.
[0 1 82]
A carboxymethylated pulp was obtained in the same manner as in
Example 5A, and then dried by heating in an oven at 100°C until the
weight f no longer d.
The resulting dried pulp was fibrillated in the same manner as in
Example 3, and a water dispersion of the carboxymethylated
brillated cellulose derived from a dried pulp of Example 8 was
obtained.
[0 1 83]
The solids fraction of the resulting water dispersion of the
carboxymethylated microfibrillated cellulose derived from a dried pulp of
Example 8 was ed to be 0.92% by weight.
The specific surface area of the resulting carboxymethylated
microfibrillated cellulose (K standard) derived from a dried pulp of
Example 8 was ed to be 240 m2 / g, the water retention f was
measured to be 15605%, and the degree of etherification was measured to
be 0.04.
[0 1 84]
The solids fraction of the water dispersion of microfibrillated
ose containing the carboxymethylated microfibrillated cellulose (K
standard) derived from a dried pulp of Example 8 was adjusted to 0.5% by
weight, and the viscosity thereof at a temperature of 50°C was ed
to be 870 CP. The solids fraction of the water dispersion was adjusted to
0.05% by , and the rate of sedimentation was measured to be 2000
ml/ g. The solids fraction of the water dispersion was adjusted to 0.02%
by weight, and the light transmission at a wavelength of 600 nm was
measured to be 69.6%. The parameters of the carboxymethylated
microfibrillated cellulose (K standard) derived from a dried pulp in
Example 8 are shown in Table 38.
[O 1 85]
<Example 8A>
A soft cream mix (ice cream standard) of e 8 was prepared
by mixing the water dispersion of the carboxymethylated microfibrillated
cellulose derived from a dried pulp of Example 8 with the soft cream mix
base (ice cream standard) shown in Table 2 so that the solids fraction of
the carboxymethylated microfibrillated cellulose derived from a dried pulp
2O of Example 8 would be 0.1% by weight. The ratios of the raw materials of
the soft cream mix of e 8A are shown in Table 39.
[o 186]
Subsequently, soft cream (ice cream standard) of Example 8A was
produced in the same manner as in Example 1A. The overrun of the
ing soft cream was 41%, and the t temperature when the
product was taken out of the freezer was -5.8°C. Then, the time until
melting and falling of the soft cream of Example 8A was measured in the
same manner as in Example 1A.
In addition, the soft cream of e 8A was eaten, and the
texture, mouth feel and flavor f were studied. The results are
shown in Table 40.
Table 40 also shows the data of Comparative Example 1A for
comparison with Example 8A.
<Example 8B>
Soft cream (lacto—ice standard) of e 8B was produced in the
same manner as in Example 1A by mixing the water dispersion of the
carboxymethylated microfibrillated cellulose derived from a dried pulp of
Example 8 with the soft cream mix base (lacto—ice standard) shown in
Table 3 so that the content of the carboxymethylated microfibrillated
cellulose (K rd) derived from a dried pulp of Example 8 would be
0.1% by weight and preparing a soft cream mix (lacto-ice standard) of
Example 8B.
The overrun of the resulting soft cream was 46%, and the product
temperature when the product was taken out of the freezer was —5.8°C.
The ratios of the raw materials of the soft cream mix of Example 8B are
shown in Table 39.
The time until melting and falling of the soft cream of Example 8B
was measured in the same manner as in Example 1A. In addition, the
soft cream of Example 8B was eaten, and the texture, mouth feel and
flavor f were studied. The results are shown in Table 40. Table 40
also shows the data of Comparative Example 1B for comparison with
Example 88.
<Example 80>
Soft cream (fat—free ice confection standard) of Example 8C was
produced in the same manner as in Example 1A by mixing the water
dispersion of the carboxymethylated microfibrillated cellulose derived from
a dried pulp of e 8 with the soft cream mix base ree ice
confection standard) shown in Table 4 so that the content of the
carboxymethylated microfibrillated ose (K standard) derived from a
dried pulp of Example 8 would be 0.1% by weight and preparing a soft
cream mix (fat—free ice confection rd) of Example 8C.
The overrun of the ing soft cream was 48%, and the product
temperature when the product was taken out of the freezer was -7.8°C.
The ratios of the raw materials of the soft cream mix of Example 8C are
shown in Table 39.
The time until melting and falling of the soft cream of Example 8C
was ed in the same manner as in Example 1A.
In addition, the soft cream of Example SC was eaten, and the
texture, mouth feel and flavor thereof were studied. The results are
shown in Table 40. Table 40 also shows the data of ative
Example 1C for comparison with Example SC.
<Example 8D>
A hard ice cream mix (ice cream standard) of Example SD was
prepared by mixing the water dispersion of the carboxymethylated
microfibrillated cellulose derived from a dried pulp of Example 8 with the
hard ice cream mix base (ice cream standard) shown in Table 5 so that the
microfibrillated cellulose (K standard) content would be 0.3% by weight.
The hard ice cream mix (ice cream standard) of Example SD was
frozen in the same manner as in Example 1D to give ice cream having an
overrun of 79% and a product temperature of -6.2°C when the product
was taken out of the freezer.
imately 86 g (approximately 140 ml) of the ice cream was
taken out and served on a cone cup (No. 15 cone, product by Nissei Co.,
Ltd.) by twisting upward the ice cream three and a half turns, and then
soon put in a freezer at —20°C. The ice cream was left in the freezer for 24
hours to be hardened. Thus, the hard ice cream of e SD was
produced. The product temperature after the hardening was
approximately —20°C.
The ratios of the raw materials of the hard ice cream mix of
Example 8D are shown in Table 39. The time until melting and falling of
the hard ice cream of Example SD was measured in the same manner as in
Example 1A. In addition, the hard ice cream of Example SD was eaten,
and the texture, mouth feel and flavor thereof were studied. The results
are shown in Table 40. Table 40 also shows the data of Comparative
Example 1D for comparison with Example 8D.
[0 1 90]
[Table 38]
ibrillated Cellulose (K standard)
Am2/g
Water Retention (%)
Viscosity (cP)
Temperature
Rate of Sedimentation (ml/g)
Light Transmission (%)
Degree of Etherification (DS)
[O 1 9 1]
[Table 39]
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ENE 38.8 0.03
03 vuvaSBm 0.000
ovbfimm doflovmnoo IE. .0.
Nd N.o 00H.
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0 000
5080 wd H
.o 0.000
bpungmbm
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mhvEmHsfim wpoNHHHQSm wucvmomaoo ueogHal@8on QOHHHNOHMHHQH‘HHWN .3
U035 .850 02:080.
vonEHvO .38.
[Table 40]
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on: £830
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825:8 3%,»; avg? “30 98 pad
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* Hard ice cream was hardened after taken out of the freezer and
had an end product temperature of approximately -20°C.
[O 192]
The results of Examples 8A to 8D have confirmed that a significant
effect of delaying melting and falling of the frozen dessert was obtained in
the soft cream of any standard and the hard ice cream (ice cream
standard) that contain the ymethylated microfibrillated cellulose (K
standard) derived from a dried pulp. Comparison With the results of
Examples 5A to 513 indicates that a better and more significant melting
and falling delaying effect was obtained in the soft cream of any rd
and the hard ice cream (ice cream rd) that contain the
microfibrillated cellulose derived from a never—dried pulp than in those
that contain the microfibrillated cellulose derived from a dried pulp.
Claims (17)
1. A frozen dessert containing derived microfibrillated cellulose, wherein said plant—derived microfibrillated cellulose has at least one of the parameters: (1) a specific surface area of 150 m2/g or larger; and (2) a water retention of 500% or more.
2. A frozen dessert containing derived microfibrillated cellulose, wherein said plant-derived microfibrillated cellulose has at least one of the parameters: (A) a rate of sedimentation of 1500 1111/g or more when in the form of a water dispersion having a microfibrillated cellulose content of 0.05% by weight; (B) a light transmission of 40% or more at a wavelength of 600 nm when in the form of a water dispersion having a microfibrillated cellulose content of 0.02% by weight.
3. The frozen dessert according to claim 1, wherein said plant—derived microfibrillated cellulose has at least one of the ters: (1) a c surface area of 200 In2/g or larger; and (2) a water retention of 8500% or more.
4. The frozen dessert according to claim 2, wherein said plant-derived microfibrillated ose has at least one of the parameters: (A) a rate of sedimentation of 1800 ml/g or more when in the form of a water dispersion having a microfibrillated cellulose content of 0.05% by weight; (B) a light transmission of 70% or more at a wavelength of 600 run when in the form of a water sion having a microfibrillated cellulose content of 0.02% by weight.
5. The frozen dessert according to any one of claims 1 to 4, containing said microfibrillated cellulose and having a temperature of —4 to —40°C as a product.
6. The frozen dessert according to any one of claims 1 to 5, containing said microfibrillated cellulose and having a temperature of -4 to — 10°C as a product When the product is taken out of the r.
7. The frozen dessert according to any one of claims 1 to 6, ning said microfibrillated cellulose and having an n of 20% to 100% as a product.
8. The frozen dessert according to any one of claims 1 to 7, containing said microfibrillated cellulose and having an overrun of 20% to 80% as a product.
9. The frozen dessert according to any one of claims 1 to 8, wherein said microfibrillated cellulose is chemically modified with a substituent ing -CH2C00-.
10. The frozen dessert according to any one of claims 1 to 9, wherein said microfibrillated cellulose has a degree of etherification of 0.01 to 0.50.
1 1. The frozen dessert according to any one of claims 1 to 8, wherein said brillated cellulose comprises 0.05 to 1.0% by weight of microfibrillated cellulose which is not chemically modified with a tuent including —CH2C00-.
12. The frozen dessert according to any one of claims 1 to 10, wherein said microfibrillated cellulose comprises 0.01 to 1.0% by weight of microfibrillated ose chemically modified with a substituent including —CH2COO—.
13. The frozen dessert according to any one of claims 1 to 12, wherein said brillated cellulose has an a—cellulose content of 50% or more.
14. The frozen dessert ing to any one of claims 1 to 13, wherein said microfibrillated cellulose contains never-dried—pulp-derived or dried—pulp-derived microfibrillated cellulose.
15. A frozen dessert material for the frozen dessert according to any one of claims 2 to 4 or 9 t014, wherein the material contains said microfibrillated cellulose.
16. A method for producing a frozen dessert, comprising the steps of: a) stirring and mixing the plant—derived microfibrillated cellulose as defined in any one of claims 1 to 4 or 9 to 14 With a mix base to give a sor mixture; b) heating the precursor mixture; c) g the heated precursor mixture to give a frozen dessert mix; and d) freezing the frozen dessert mix to give a frozen dessert.
17. The frozen dessert according to claim 1, ntially as herein described With reference to any one of the Examples and/or
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2011200885 | 2011-09-14 | ||
JP2011-200885 | 2011-09-14 | ||
JP2012196178A JP5463397B2 (en) | 2011-09-14 | 2012-09-06 | Frozen desserts and frozen dessert ingredients |
JP2012-196178 | 2012-09-06 | ||
PCT/JP2012/073344 WO2013039110A1 (en) | 2011-09-14 | 2012-09-12 | Frozen dessert and frozen dessert raw material |
Publications (2)
Publication Number | Publication Date |
---|---|
NZ621519A NZ621519A (en) | 2016-02-26 |
NZ621519B2 true NZ621519B2 (en) | 2016-05-27 |
Family
ID=
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