Technical Field
[0001] The present invention relates to a method for producing a tobacco material, a tobacco
material for oral use, and a tobacco product for oral use.
Background Art
[0002] Conventionally, a method comprising adding water to a tobacco starting material,
heating based on tube heat, heating based on steam spraying, and drying with hot air
in order to modify the tobacco material is known. In the modifying process, a saccharide
or the like is added, if necessary.
[0003] However, in the method, it is not expected to modify the tobacco starting material
so as to exceed the characteristics of the tobacco starting material itself. When
sensory characteristics need to be largely improved, it is necessary to change the
mixing ratio of the tobacco starting material and an additive.
[0004] U.S. Patent Application Publication No. 1757477 discloses a method for directly bringing a tobacco starting material into contact
with an ozone gas. However, the permeability of ozone into an object to be treated
is very low. Thus, even if the tobacco starting material is directly exposed to the
ozone, the reaction in the tobacco starting material is not expected or a long treatment
time is required. As a result, the treatment efficiency is low. This is inefficient
and the treatment cost is high.
[0005] On the other hand, a tobacco product for oral use has attracted attention in recent
years. The tobacco product for oral use is produced by putting a tobacco material
for oral use containing moist tobacco powder in a water-permeable pouch. The tobacco
product for oral use is inserted between the lip and the gum of the mouth to enjoy
the taste and fragrance of the tobacco. A pH regulator is added to the moist tobacco
powder so as to adjust a nearly neutral region of the pH to an alkaline region. Thus,
preferable flavor and taste are provided. In the tobacco product for oral use, it
is desired that the pH adjusted during the storage period is substantially maintained
from the viewpoint of quality maintenance.
[0006] Jpn. PCT National Publication No.
2009-082331 discloses a tobacco product which contains magnesium carbonate as a pH regulator
to make a tobacco material alkaline. The article also discloses that an additional
pH regulator may be used, in addition to magnesium carbonate. As examples thereof,
sodium carbonate, phosphate or the like are described. The additional pH regulator
is used to rapidly adjust the pH of the tobacco material to a desired pH value (neutral
or alkaline).
[0007] However, the amount of the alkaline substance to be uniquely determined is an amount
required to adjust the pH of the moist tobacco powder to a desired neutral or alkaline
pH value. Further, as the amount of the alkaline substance to adjust the pH of the
tobacco powder to a desired pH value is relatively small, it is not possible to maintain
the adjusted pH value over a long period of time. As a result, it is necessary to
store the tobacco product for oral use containing the tobacco powder whose initial
pH is adjusted using only the alkaline substance not at room temperature but at a
low temperature (-20°C to 10°C).
[0008] If a large amount of the alkaline substance is added to the tobacco material for
oral use in order to maintain the storage stability over a long period of time, the
pH value increases largely. Thus, the mucous membrane of the mouth may be injured
upon insertion into the mouth. The tobacco product for oral use containing the moist
tobacco powder that is used in the mouth desirably has a pH of 9.0 or less.
[0009] Among tobacco products for oral use, particularly, a tobacco product for oral use
in the form such that a tobacco material is wrapped with a bag-shaped pouch of non-woven
fabric and the whole pouch is put into the mouth for use is known. When the pigment
component as an ingredient in the tobacco product for oral use is eluted into the
water content and attached to the pouch, color stains such as spots may be formed
on the pouch. Further, in the pouch taken out from the mouth after use, the pigment
component as an ingredient seeps into the pouch through the saliva and the pouch is
colored. Such color staining of the pouch easily gives an unpleasant impression. Color
stains derived from the pigment component as an ingredient impair an aesthetic appearance
of the product.
[0010] A method comprising allowing only the pigment component in the tobacco starting material
to be eluted to the extent that color staining of the pouch is not caused and removing
it has been attempted. However, the method impairs a taste component of the tobacco
starting material, and thus it has been technically difficult.
[0011] In view of such circumstances, there has been a demand for a method for removing
the pigment component without impairing the flavor of tobacco.
Summary of Invention
[0012] An object of the present invention is to provide a method for producing a tobacco
material in which bad habits are removed and the bleaching or the like is modified
and which has a excellent storage stability over a long period of time.
[0013] Another object of the present invention is to provide a tobacco material for oral
use having a high brightness by Hunter.
[0014] Still another object of the present invention is to provide a tobacco product for
oral use which contains a tobacco material for oral use having a high brightness by
Hunter and exhibits an aesthetic appearance during storage and after use.
[0015] In order to solve the above problem, according to a first aspect of the present invention,
there is provided a method for producing a tobacco material which comprises:
- a) preparing a mixed suspension of a tobacco starting material residue and an extract
of a water-soluble component by immersing a tobacco starting material in water to
allow the water-soluble component in the tobacco starting material to be dissolved
in water;
- b) supplying ozone to the mixed suspension to be dissolved in it and bringing the
dissolved ozone into contact with the mixed suspension.
[0016] According to a second aspect of the present invention, there is provided a method
for producing a tobacco material which comprises:
- a) immersing a tobacco starting material in water to allow the water-soluble component
in the tobacco starting material to be dissolved in water;
- b) separating the tobacco starting material residue after the extraction from the
extract of the water-soluble component;
- c) mixing the separated tobacco starting material residue with water again to prepare
a suspension; and
- d) supplying ozone to the suspension to be dissolved in it, and bringing the dissolved
ozone into contact with the suspension.
[0017] According to a third aspect of the present invention, there is provided a method
for producing a tobacco material which comprises:
- a) immersing a tobacco starting material in water to allow the water-soluble component
in the tobacco starting material to be dissolved in water;
- b) separating the tobacco starting material residue after the extraction from the
extract of the water-soluble component;
- c) supplying ozone to the separated extract to be dissolved in it, and bringing the
dissolved ozone into contact with the extract; and
- d) drying the tobacco starting material residue and applying the extract after the
ozone treatment to the tobacco starting material residue during the drying process.
[0018] According to a fourth aspect of the present invention, there is provided a tobacco
material for oral use produced by the method according to any of the first to third
aspects.
[0019] According to a fifth aspect of the present invention, there is provided a tobacco
product for oral use which contains a tobacco material for oral use having a brightness
by Hunter of 35 or more.
Brief Description of Drawings
[0020]
FIG. 1 is a flow chart showing a method for producing a tobacco material according
to a first embodiment.
FIG. 2 is a flow chart showing a method for producing a tobacco material according
to a second embodiment.
FIG. 3 is a flow chart showing a method for producing a tobacco material according
to a third embodiment.
FIG. 4 is a flow chart showing another embodiment of the method for producing a tobacco
material according to the third embodiment.
FIG. 5 is a characteristic diagram showing the storage periods and changes in pH of
tobacco materials obtained in Examples 1 to 3 and Comparative Example 1.
Description of Embodiments
[0021] Hereinafter, the method for producing a tobacco material, the tobacco material for
oral use, and the tobacco product for oral use according to the embodiments will be
described in detail.
(First embodiment)
[0022] The method for producing a tobacco material according to the first embodiment includes
the following steps.
<Step a>
[0023] A mixed suspension of a tobacco starting material residue and an extract of a water-soluble
component is prepared by immersing a tobacco starting material in water to allow the
water-soluble component in the tobacco starting material to be dissolved in water.
<Step b>
[0024] Ozone is supplied to the mixed suspension to be dissolved in it. The dissolved ozone
is brought into contact with the mixed suspension.
[0025] According to the first embodiment, ozone is supplied to the mixed suspension of the
tobacco starting material residue and the extract of the water-soluble component to
be dissolved in it, and the dissolved ozone is brought into contact with the mixed
suspension so that the reaction of the mixed suspension with the ozone can efficiently
proceed.
[0026] When the water-soluble component in the tobacco starting material, which is eluted
in water in the reaction of the mixed suspension and the ozone, is a substance which
decomposes to release an acidic component (e.g., saccharide), the substance can be
oxidized by efficiently bringing it into contact with the ozone. Here, the "substance
which decomposes to release an acidic component" is also referred to as "a substance
decomposable to release an acidic component". Further, when the substance decomposable
to release an acidic component (e.g., polysaccharide) is contained in the tobacco
starting material residue, the substance can be oxidized by effectively bringing it
into contact with ozone. In other words, the substance decomposable to release an
acidic component may be pre-oxidized before the storage of the tobacco material and
released as an acidic component.
[0027] As a result, it is possible to prevent the substance decomposable to release an acidic
component from being decomposed by aging and releasing the acidic component during
the storage of the resulting tobacco material. This allows a decrease in the pH of
the tobacco product by the acidic component to be avoided. Therefore, the pH adjusted
during the storage can be substantially maintained. Thus, a tobacco material excellent
in storage stability can be produced.
[0028] Further, the amount of the dissolved ozone to be brought into contact with the mixed
suspension is adjusted, namely, the level of treatment for the tobacco starting material
residue and the extract of the water-soluble component is selected so that it is possible
to produce a tobacco material from which undesirable characteristics have been removed
without impairing the flavor of tobacco, and the color tone resulting from the pigment
component is adjusted (the whiteness is increased).
[0029] Particularly, a tobacco material the whiteness of which is increased, for example,
to a Hunter brightness of 35 or more, may be used as a tobacco material for oral use.
For the tobacco product including the tobacco material for oral use, for example,
a tobacco product for oral use in the form such that a tobacco material is wrapped
with a bag-shaped pouch of non-woven fabric and the whole pouch is put into the mouth
for use, color staining of the pouch due to the pigment component during storage and
after use is reduced. Accordingly, there can be provided a tobacco product having
an improved aesthetic appearance.
[0030] Examples of the tobacco starting material used in Step a may include tobacco leaves
and stems separated from the tobacco leaves. The stems are rolled with a rolling mill
and finely cut. The resulting products may be used as stem shreds.
[0031] The type of water-soluble component in the tobacco starting material is not particularly
limited. In general, examples thereof may include carbohydrates (saccharides), alkaloids,
proteins, and amino acids.
[0032] When the tobacco starting material is immersed in water in Step a, the amount of
water is preferably 5 to 20 times the amount of the tobacco starting material. Water
may be at normal temperature and it is preferably heated to 20 to 60°C. Preferably,
the time for immersing the tobacco starting material in water is, for example, 10
minutes to 2 hours. In immersing the tobacco starting material in water, it is preferable
that both the materials are stirred to facilitate the water-soluble component in the
tobacco starting material dissolving in water.
[0033] In the step of supplying ozone (Step b), the ozone is preferably dissolved in an
amount of 0.5 to 500 g per 1 L of the extract in the mixed suspension. The degree
of reaction of the ozone with an extract of a tobacco starting material residue and
a water-soluble component, that is, the degree of treatment may be selected by changing
the ozone dissolution amount.
[0034] The step of supplying ozone (Step b) is preferably performed by exposing the mixed
suspension to ozone. The ozone exposure allows the tobacco starting material residue
and the extract in the mixed suspension to be in contact with not only the dissolved
ozone but also the bubble ozone. As a result, it is possible to effectively react
the water-soluble component in the tobacco starting material residue and the extract
with the ozone.
[0035] In the ozone exposure, it is desired that the ozone bubbles have a diameter of 0.5
to 1000 µm, more preferably a diameter of 0.5 to 100 µm.
[0036] In the process of bringing the dissolved ozone into contact with the mixed suspension,
it is preferable that the mixed suspension is stirred, circulated with a pump or both
the stirring and circulating processes are performed. The stirring and circulating
processes allow the contact efficiency of the tobacco starting material residue and
the extract in the mixed suspension with the ozone to be increased.
[0037] It is preferable that the step of supplying ozone is continuously performed so that
the ozone dissolved in the mixed suspension as a reaction field is always present.
[0038] After Steps a and b, the mixed suspension after the ozone treatment may be dried.
In this case, the mixed suspension after the ozone treatment is subjected to solid
liquid separation and the tobacco starting material residue as a solid is dried. In
the drying, the separated extract may be applied by spraying so that the component
of the extract is incorporated into the dry product.
[0039] The pH and water content of the resulting dry product are adjusted with a pH regulator
to produce a target tobacco material. As the pH regulator, for example, sodium carbonate
or potassium carbonate may be used. The tobacco material after adjustment of the pH
and the water content preferably has a pH of 7.0 to 9.0 and a water content of 10.0
to 50.0% by mass.
[0040] FIG. 1 shows a flow in the method for producing a tobacco material according to the
first embodiment.
[0041] As shown in FIG. 1, a tobacco starting material is prepared in Step S1.
[0042] Water is added to the tobacco starting material in Step S2. The tobacco starting
material is stirred in a state immersed in water at Step S3. The water-soluble component
in the tobacco starting material is eluted to form an extract.
[0043] The mixed suspension of the tobacco starting material residue and the extract obtained
in Step S4 is exposed to ozone (O
3) in Step S5, the ozone is dissolved, and the process of bringing the aforementioned
into contact with the ozone dissolved in the mixed suspension is performed.
[0044] The mixed suspension is dried in Step S6. Thereafter, in Step S7, the pH and water
content of the dry product are adjusted to produce a tobacco material.
(Second embodiment)
[0045] The method for producing a tobacco material according to the second embodiment includes
the following steps.
<Step a>
[0046] A tobacco starting material is immersed in water to allow a water-soluble component
in the tobacco starting material to be dissolved in water.
<Step b>
[0047] The tobacco starting material residue after the extraction is separated from the
extract of the water-soluble component.
<Step c>
[0048] The separated tobacco starting material residue is again mixed with water to prepare
a suspension.
<Step d>
[0049] Ozone is supplied to the suspension to be dissolved in it, and the dissolved ozone
is brought into contact with the suspension.
[0050] According to the second embodiment, the water-soluble component of the tobacco starting
material is extracted, the tobacco starting material residue is separated from the
extract, the tobacco starting material residue is again mixed with water to prepare
a suspension, ozone is supplied to the suspension to be dissolved in it, and the dissolved
ozone is brought into contact with the tobacco starting material residue of the suspension
so that the reaction of the tobacco starting material residue (including a large amount
of the substance decomposable to release an acidic component) with the ozone can efficiently
proceed.
[0051] In the reaction of the tobacco starting material residue with the ozone, the substance
decomposable to release an acidic component (e.g., polysaccharide) in the tobacco
starting material residue can be oxidized by effectively bringing it into contact
with the ozone. In other words, the substance decomposable to release an acidic component
may be pre-oxidized before the storage of the tobacco material and released as an
acidic component.
[0052] As a result, it is possible to prevent the substance decomposable to release an acidic
component from being decomposed by aging and releasing the acidic component during
the storage of the resulting tobacco material. Thus, it is possible to avoid a decrease
in the pH of the tobacco product by the acidic component. Therefore, the pH adjusted
during the storage can be substantially maintained. Thus, a tobacco material excellent
in storage stability can be produced.
[0053] Further, the amount of the dissolved ozone is adjusted, namely, the level of treatment
for the tobacco starting material residue is selected so that it is possible to produce
a tobacco material from which undesirable characteristics have been removed without
impairing the flavor and the color tone resulting from the pigment component is adjusted
(the whiteness is increased).
[0054] Particularly, a tobacco material the whiteness of which is increased, for example,
to a Hunter brightness of 35 or more, may be used as a tobacco material for oral use.
In the tobacco product including the tobacco material for oral use, for example, a
tobacco product for oral use in the form such that a tobacco material is wrapped with
a bag-shaped pouch of non-woven fabric and the whole pouch is put into the mouth for
use, color staining of the pouch due to the pigment component during storage and after
use is reduced. Accordingly, there can be provided a tobacco product having an aesthetic
appearance.
[0055] Examples of the tobacco starting material used in Step a may include tobacco leaves
and stems separated from the tobacco leaves. The stems are rolled with a rolling mill
and finely cut. The resulting products may be used as stem shreds. However, in the
second embodiment, since a target to be subjected to the ozone treatment is the tobacco
starting material residue after the separation of the extract, one containing the
substance decomposable to release an acidic component (e.g., polysaccharide) in the
residue after the extraction of water may be selected as the tobacco starting material.
[0056] The conditions of immersing the tobacco starting material in water (in Step a) are
preferably set to the same conditions as the first embodiment.
The separation step (in Step b) may be performed using, for example, a barrier filter.
[0057] In the step of supplying ozone (Step d), the ozone is preferably dissolved in an
amount of 0.5 to 500 g per 1 L of the water in the mixed suspension. The degree of
reaction of the ozone with a tobacco starting material residue, that is, the degree
of treatment, may be selected by varying the amount of ozone dissolution.
[0058] The step of supplying ozone (Step d) is preferably performed by exposing the mixed
suspension to ozone. The ozone exposure allows the tobacco starting material residue
in the suspension to be in contact with not only the dissolved ozone but also the
bubble ozone. Thus, it is possible to effectively react the tobacco starting material
residue with the ozone.
[0059] In the ozone exposure, it is desired that the ozone bubbles have a diameter of 0.5
to 1000 µm, more preferably a diameter of 0.5 to 100 µm.
[0060] In the process of bringing the dissolved ozone into contact with the suspension,
it is preferable that the suspension is stirred, circulated with a pump or both the
stirring and circulating processes are performed. The stirring and circulating processes
allow the contact efficiency of the tobacco starting material residue and the extract
in the mixed suspension with the ozone to be increased.
[0061] It is preferable that the step of supplying ozone is continuously performed so that
the ozone dissolved in the suspension as a reaction field is always present.
[0062] After Steps a and d, the suspension after the ozone treatment is dried. Preferably,
the drying process is performed at 40 to 100°C so that the moisture content of the
dry product is from 5.0 to 50.0% by mass.
[0063] The pH and water content of the resulting dry product are adjusted with a pH regulator
to produce a target tobacco material. As the pH regulator, for example, sodium carbonate
or potassium carbonate may be used. The tobacco material after adjustment of the pH
and the water content preferably has a pH of 7.0 to 9.0 and a water content of 10.0
to 50.0% by mass.
[0064] In this regard, the extract separated after the extraction may not be used depending
on the purpose or may be sprayed to the suspension during drying so as to return it
to an original state.
[0065] FIG. 2 shows a flow in the method for producing a tobacco material according to the
second embodiment.
[0066] As shown in FIG. 2, a tobacco starting material is prepared in Step S1.
[0067] Water is added to the tobacco starting material in Step S2. The tobacco starting
material is stirred in a state immersed in water at Step S3. The water-soluble component
in the tobacco starting material is eluted to form an extract.
[0068] The suspension after the extraction of the water-soluble component in Step S4 is
subjected to solid liquid separation to obtain a tobacco starting material residue
shown in Step S5 and an extract shown in Step S6.
[0069] Water is added to the tobacco starting material residue in Step S7 and a suspension
is prepared in Step S8. The suspension is exposed to ozone (O
3) in Step S9, the ozone is dissolved in water, and the process of bringing the dissolved
ozone into contact with the suspension is performed.
[0070] The suspension is dried in Step S10. Thereafter, the pH and water content of the
dry product are adjusted in Step S11 to produce a tobacco material.
[0071] In this regard, the extract obtained in Step S6 may be returned by the spraying process
during drying of the suspension of Step S10.
(Third embodiment)
[0072] The method for producing a tobacco material according to the third embodiment includes
the following steps.
<Step a>
[0073] A tobacco starting material is immersed in water to allow a water-soluble component
in the tobacco starting material to be dissolved in water.
<Step b>
[0074] The tobacco starting material residue after the extraction is separated from the
extract of the water-soluble component.
<Step c>
[0075] Ozone is supplied to the separated extract to be dissolved in it, and the dissolved
ozone is brought into contact with the extract.
<Step d>
[0076] The tobacco starting material residue separated in Step b is dried, and the extract
after the ozone treatment is applied to the tobacco starting material residue during
the drying process by, for example, spraying.
[0077] According to the third embodiment, ozone is supplied to the extract of the water-soluble
component extracted from the tobacco starting material to be dissolved in it, and
the dissolved ozone is brought into contact with the extract so that the reaction
of the extract with the ozone can efficiently proceed.
[0078] In the reaction, the substance decomposable to release an acidic component (e.g.,
saccharide) contained in the water-soluble component of the extract is brought into
contact with the dissolved ozone so that it can be efficiently oxidized. In other
words, the substance decomposable to release an acidic component may be pre-oxidized
before the storage of the tobacco material and released as an acidic component.
[0079] As a result, during drying of the separated tobacco starting material residue, the
extract after the ozone treatment (including the substance decomposable to release
an acidic component which has been already oxidized) is applied so as to return it
to the residue. Thus, it is possible to prevent the substance decomposable to release
an acidic component from being decomposed by aging and releasing the acidic component
during the storage of the resulting tobacco material. Thus, it is possible to avoid
a decrease in the pH of the tobacco product by the acidic component. Therefore, the
pH adjusted during the storage can be substantially maintained. Thus, a tobacco material
excellent in storage stability can be produced.
[0080] Further, the amount of the dissolved ozone is adjusted, namely, the level of treatment
for the extract of the water-soluble component is selected so that undesirable characteristics
can be removed without impairing the flavor and the color tone resulting from the
pigment component of the extract can be adjusted (the whiteness is increased). As
a result, during drying of the tobacco starting material residue after the separation,
the extract after the ozone treatment is returned to the residue by the spraying process
so that it is possible to produce a tobacco material in which the flavor is maintained,
there are no undesirable characteristics, and the whiteness is increased.
[0081] Particularly, a tobacco material of which the whiteness is increased, to for example,
a Hunter brightness of 35 or more may be used as a tobacco material for oral use.
In the tobacco product including the tobacco material for oral use, for example, a
tobacco product for oral use in the form such that a tobacco material is wrapped with
a bag-shaped pouch of non-woven fabric and the whole pouch is put into the mouth for
use, color staining of the pouch due to the pigment component during storage and after
use is reduced. Accordingly, there can be provided a tobacco product having a good
aesthetic appearance.
[0082] Examples of the tobacco starting material used in Step a may include tobacco leaves
and stems separated from the tobacco leaves. The stems are rolled with a rolling mill
and finely cut. The resulting products may be used as stem shreds. However, in the
third embodiment, since a target to be subjected to the ozone treatment is the extract,
one containing the substance decomposable to release an acidic component (e.g., saccharide)
in the extract may be selected as the tobacco starting material to be subjected to
the treatment.
[0083] The conditions in immersing the tobacco starting material in water (in Step a) are
preferably set to the same conditions as the first embodiment.
[0084] The separation step (in Step b) may be performed using, for example, a barrier filter.
[0085] In the step of supplying ozone (Step c), the ozone is preferably dissolved in an
amount of 0.5 to 500 g per 1 L of the extract. The degree of reaction of the ozone
with a starting material, that is, the degree of treatment may be selected by varying
the amount of ozone dissolution.
[0086] The step of supplying ozone (Step c) is preferably performed by exposing the extract
to ozone. The ozone exposure allows the extract to be in contact with not only the
dissolved ozone but also the bubble ozone. Thus, it is possible to effectively react
the extract with the ozone. In the ozone exposure, it is desired that the ozone bubbles
have a diameter of 0.5 to 1000 µm, more preferably a diameter of 0.5 to 100 µm.
[0087] In the process of bringing the dissolved ozone into contact with the extract, it
is preferable that the extract is stirred, circulated with a pump or both the stirring
and circulating processes are performed. The stirring and circulating processes allow
the contact efficiency of the extract with the ozone to be increased.
[0088] It is preferable that the step of supplying ozone is continuously performed so that
the ozone dissolved in the extract as a reaction field is always present.
[0089] The process of drying the separated tobacco starting material residue in Step d is
preferably performed at 40 to 100°C because the extract treated with the ozone during
the drying process is returned by the spraying process. Preferably, the drying process
is performed so that the moisture content of the resulting dry product is from 5.0
to 25.0% by mass.
[0090] In Step d, a partial or total amount of the extract (the extract treated with the
ozone) may be applied to the tobacco starting material residue during the drying process.
[0091] The pH and water content of the dry product obtained in Steps a to d are adjusted
with a pH regulator to produce a target tobacco material. As the pH regulator, for
example, sodium carbonate or potassium carbonate may be used. The tobacco material
after adjustment of the pH and the water content preferably has a pH of 7.0 to 9.0
and a water content of 10.0 to 50.0% by mass.
[0092] FIG. 3 shows a flow in the method for producing a tobacco material according to the
third embodiment.
[0093] As shown in FIG. 3, a tobacco starting material is prepared in Step S1.
[0094] Water is added to the tobacco starting material in Step S2. The tobacco starting
material is stirred in a state immersed in water at Step S3. The water-soluble component
in the tobacco starting material is eluted to form an extract.
[0095] The suspension after the extraction of the water-soluble component in Step S4 is
subjected to solid liquid separation to obtain a tobacco starting material residue
shown in Step S5 and an extract shown in Step S6.
[0096] The extract is exposed to ozone (O
3) in Step S7, the ozone is dissolved in water, and the process of bringing the dissolved
ozone into contact with the extract is performed.
[0097] The tobacco starting material residue after solid liquid separation in Step S8 is
dried, and the extract after the ozone treatment is returned to the tobacco starting
material residue during the drying process by the spraying process. Thereafter, in
Step S9, the pH and water content of the dry product are adjusted to produce a tobacco
material.
[0098] In the third embodiment, the following steps may be added.
[0099] The separated tobacco starting material residue is again mixed with water to prepare
a suspension. Ozone is supplied to the suspension to be dissolved in it, and the dissolved
ozone is brought into contact with the suspension. The suspension after the ozone
treatment is dried, and the extract after the ozone treatment is, for example, returned
to the tobacco starting material residue dry product during drying, by, for example,
the spraying process.
[0100] FIG. 4 shows a flow in the method for producing a tobacco starting material.
[0101] As shown in FIG. 4, a tobacco starting material is prepared in Step S1.
[0102] Water is added to the tobacco starting material in Step S2. The tobacco starting
material is stirred in a state immersed in water at Step S3. The water-soluble component
in the tobacco starting material is eluted to form an extract.
[0103] The suspension after the extraction of the water-soluble component in Step S4 is
subjected to solid liquid separation to obtain a tobacco starting material residue
shown in Step S5 and an extract shown in Step S6.
[0104] Water is added to the tobacco starting material residue in Step S7 and a suspension
is prepared in Step S8. The suspension is exposed to ozone (O
3) in Step S9, the ozone is dissolved in water, and the process of bringing the dissolved
ozone into contact with the suspension is performed.
[0105] The suspension is dried in Step S10.
[0106] The extract obtained by solid liquid separation in Step S4 is exposed to ozone (O
3) in Step S11, the ozone is dissolved in water, and the process of bringing the dissolved
ozone into contact with the extract is performed.
[0107] During drying of the suspension in Step S10, the extract after the ozone treatment
is returned by the spraying process. Thereafter, the pH and water content of the dry
product are adjusted in Step S12 to produce a tobacco material.
[0108] According to another embodiment of the third embodiment, appropriate ozone treatment
may be performed depending on the properties of the tobacco starting material residue
after the extraction and the properties of the extract.
[0109] That is, in the first embodiment, the ozone treatment is performed on the mixed suspension
of the tobacco starting material residue and the extract after the extraction. The
ozone effect is uniformly applied to the tobacco starting material residue and the
extract.
[0110] However, a large amount of the substance decomposable to release an acidic component
may be contained in the tobacco starting material residue after the extraction, depending
on the kind of the tobacco starting material. In contrast, a large amount of the substance
decomposable to release an acidic component may be contained in the extract. Further,
the flavor, undesirable characteristics, and the pigment component may be
weighted in either the tobacco starting material residue or the extract.
[0111] As described above, the tobacco starting material residue and the extract are respectively
treated with the ozone so that the degree of the reaction of the tobacco starting
material residue and the extract with the ozone, namely, the treatment degree can
be independently and arbitrarily adjusted according to their properties. Thus, it
is possible to produce a tobacco material of which the storage stability is excellent,
the flavor is maintained, there are no undesirable characteristics, and the whiteness
is increased.
(Fourth embodiment)
[0112] The tobacco product for oral use according to the fourth embodiment includes a tobacco
material for oral use having a Hunter brightness of 35 or more. A more preferred tobacco
material for oral use has a Hunter brightness of 37 or more.
[0113] The tobacco product for oral use has, for example, a structure in which a tobacco
material is wrapped with a bag-shaped pouch of non-woven fabric. As for the tobacco
product for oral use, the whole pouch is put into the mouth for use.
[0114] The tobacco material for oral use may be obtained by the method for producing a tobacco
material described in the first to third embodiments.
[0115] Also, the tobacco material for oral use may be obtained by treating the tobacco starting
material with an oxidant except for the ozone. As the oxidant, for example, hydrogen
peroxide may be used.
[0116] Since the tobacco product for oral use according to the fourth embodiment includes
a tobacco material for oral use having a Hunter brightness of 35 or more, color staining
of the pouch due to the pigment component during storage and after use is reduced
and an aesthetic appearance is exhibited.
[0117] Hereinafter, examples and comparative examples of the present invention will be described.
In this regard, the moisture content of the tobacco materials according to Comparative
Examples 1 and 2 and Examples 1 to 4 was measured by the following method.
<Measurement method of moisture content>
[0118] The moisture content of 3.0 g of a powdered tobacco material was measured using a
heat drying type moisture meter (HB 43-S: manufactured by METTLER TOLEDO International
Inc.).
(Comparative Example 1)
[0119] First, a tobacco starting material in which ground powders of rustica leaves, burley
leaves, and tobacco stems were mixed at a proportion of 35% by mass, 15% by mass,
and 50% by mass, respectively, was prepared.
[0120] Subsequently, 4 kg of the tobacco starting material was heated at 110°C for 30 minutes,
and heated and dried at 80°C for 3 hours. Further, the dry product was cooled. The
moisture content of the resulting tobacco starting material was then measured. As
a result, the moisture content of the tobacco starting material was 18% by mass.
[0121] Subsequently, water (in an amount required to adjust the final moisture content of
the tobacco material to 25.0% by mass) was prepared. Sodium carbonate was added to
the water in an amount of 3.0% by mass based on the dry weight of the tobacco material.
The total amount of the resulting sodium carbonate solution was sprayed to the tobacco
starting material to produce a tobacco material having a moisture content of 25% by
mass and a pH (initial value) of 8.43.
(Example 1)
[0122] Four kg of a tobacco starting material with the same composition as that of Comparative
Example 1 and 80 L of water were stirred and mixed for 30 minutes so as to allow the
component in the tobacco starting material to be eluted (dissolved) in water.
[0123] Subsequently, the stirring was continued and the exposure to ozone fine bubbles was
continued for 3 hours while circulating the mixed suspension of the tobacco starting
material residue and the extract with a pump. At this time, the average diameter of
the ozone fine bubbles was 10 µm and the exposure to ozone was carried out at 25°C
and 38.0 g/hr.
[0124] Subsequently, the mixed suspension after the ozone treatment was subjected to solid-liquid
separation. In the drying process, the extract as a liquid was sprayed to the tobacco
starting material residue while heating the tobacco starting material residue as a
solid to 80°C. The moisture content of the resulting dry product was measured. As
a result, the moisture content of the dry product was 8.8% by mass.
[0125] Subsequently, water (in an amount required to adjust the final moisture content of
the tobacco material to 25.0% by mass) was prepared. Sodium carbonate was added to
the water in an amount of 2.3% by mass based on the dry weight of the tobacco material.
The total amount of the resulting sodium carbonate solution was sprayed to the dry
product to produce a tobacco material having a moisture content of 25% by mass and
a pH (initial value) of 8.50.
(Example 2)
[0126] First, a tobacco starting material in which ground powders of rustica leaves burley
leaves were mixed at a proportion of 70% by mass and 30% by mass, respectively, was
prepared.
[0127] Then, 4 kg of a tobacco starting material and 80 L of water were stirred and mixed
for 30 minutes so as to allow the component in the tobacco starting material to be
eluted (dissolved) in water. Subsequently, the stirring was continued and the exposure
to ozone fine bubbles was continued for 3 hours while circulating the mixed suspension
of the tobacco starting material residue and the extract with a pump. At this time,
the average diameter of the ozone fine bubbles was 10 µm and the exposure to ozone
was carried out at 25°C and 38.0 g/hr.
[0128] Subsequently, the mixed suspension after the ozone treatment was subjected to solid-liquid
separation. In the drying process, the extract as a liquid was sprayed to the tobacco
starting material residue while heating the tobacco starting material residue as a
solid to 80°C. The moisture content of the resulting dry product was measured. As
a result, the moisture content of the dry product was 8.5% by mass.
[0129] Subsequently, water (in an amount required to adjust the final moisture content of
the tobacco material to 25.0% by mass) was prepared. Sodium carbonate was added to
the water in an amount of 2.8% by mass based on the dry weight of the tobacco material.
The total amount of the resulting sodium carbonate solution was sprayed to the dry
product to produce a tobacco material having a moisture content of 25% by mass and
a pH (initial value) of 8.25.
(Example 3)
[0130] Four kg of a tobacco starting material with the same composition as that of Example
2 and 80 L of water were stirred and mixed for 30 minutes so as to allow the component
in the tobacco starting material to be eluted (dissolved) in water. Subsequently,
the stirring was continued and the exposure to ozone fine bubbles was continued for
3 hours while circulating the mixed suspension of the tobacco starting material residue
and the extract with a pump. At this time, the average diameter of the ozone fine
bubbles was 10 µm and the exposure to ozone was carried out at 25°C and 38.0 g/hr.
[0131] Subsequently, the mixed suspension after the ozone treatment was subjected to solid-liquid
separation. In the drying process, the extract as a liquid was sprayed to the tobacco
starting material residue while heating the tobacco starting material residue as a
solid to 80°C. The moisture content of the resulting dry product was measured. As
a result, the moisture content of the dry product was 8.5% by mass.
[0132] Subsequently, water (in an amount required to adjust the final moisture content of
the tobacco material to 50.0% by mass) was prepared. Sodium carbonate was added to
the water in an amount of 2.8% by mass based on the dry weight of the tobacco material.
The total amount of the resulting sodium carbonate solution was sprayed to the dry
product to produce a tobacco material having a moisture content of 25% by mass and
a pH (initial value) of 8.48.
[0133] The smell of the resulting tobacco materials of Comparative Example 1 and Example
1 was measured by the following method. The results are shown in Table 1 below.
<Method for measuring smell>
1) Analytical laboratories: Japan Food Research Laboratories
2) Preparation of sample gas
[0134] Ten g of a sample was placed in a sample bag of polyethylene terephthalate (volume:
about 2 L), and the inside of the bag was substituted with a nitrogen gas. Thereafter,
it was allowed to stand at room temperature for about 3 hours and used as a sample
gas.
3) Measurement method
[0135] The smell of the sample gas was measured under the following conditions using a smell
identification testing device.
4) Measurement conditions
[0136]
Model: Smell identification device: FF-2A (Shimadzu Corporation.)
Autosampler for sample bags: FAS-1 (Shimadzu Corporation.)
Dilution mixing device: FDL-1 (Shimadzu Corporation.)
Sampling tube: usually used
Software for data analyses: Smell P (Shimadzu Corporation.)
[Table 1]
System and kind of smell (Standard gas component) |
Odor contribution |
Comparative Example 1 |
Example 1 |
Ammonia |
2.3 |
-5.3 |
Note) the odor contribution is a value obtained by representing the strength of the
smell of the system as an odor index equivalent value. |
[0137] When the calculated value is the set threshold or less, it is represented by a minus
(-) value (the lowest value: - 30).
[0138] As is clear from Table 1 above, undesirable characteristics in the tobacco material
obtained in Example 1 can be significantly reduced as compared to those in the tobacco
material of Comparative Example 1.
[0139] In this regard, undesirable characteristics in the tobacco materials obtained in
Examples 2 and 3 were significantly reduced, similarly to Example 1.
[0140] Regarding the tobacco materials obtained in Examples 1 to 3 and Comparative Example
1, the pH during the production, the pH after storage for two months, and the pH after
storage for four months were measured by the following method. The results are shown
in FIG. 5. In the storage process, the tobacco material was placed in an atmosphere
where the temperature went up and down every day (25 to 30°C).
<pH measurement method>
[0141] Three g of a tobacco material was weighed and put into a vial, and 30 mL of water
was added thereto. The mixture was subjected to shaking at 200 rpm for 10 minutes
(extraction treatment). The resulting mixture was allowed to stand for 5 minutes,
and then the pH of the extract was measured using a pH meter (IQ 240, manufactured
by IQ Scientific Instruments Inc.).
[0142] As is clear from FIG. 5, the pH during storage in the tobacco materials obtained
in Examples 1 to 3 can be significantly controlled as compared to that of the tobacco
material obtained in Comparative Example 1. In other words, changes in the pH during
storage are small.
(Examples 4 to 9)
[0143] Five kg of a tobacco starting material with the same composition as that of Comparative
Example 1 and 400 mL of water were stirred and mixed for 30 minutes so as to allow
the component in the tobacco starting material to be eluted (dissolved) in water.
[0144] Subsequently, the stirring was continued and the exposure to ozone fine bubbles was
continued for 10 minutes, for 20 minutes, for 30 minutes, for 40 minutes, for 80 minutes,
and 120 minutes while circulating the mixed suspension of the tobacco starting material
residue and the extract with a pump. At this time, the average diameter of the ozone
fine bubbles was 45 µm and the exposure to ozone was carried out at 25°C and 6.0 g/hr.
[0145] Subsequently, the mixed suspension after the ozone treatment was subjected to solid-liquid
separation. The extract after the separation was concentrated. The concentrated extract
was sprayed to the tobacco starting material residue after the separation so as to
make it return to the original state while keeping the residue at 40°C, and thus six
kinds of tobacco materials were produced.
(Comparative Example 2)
[0146] A tobacco material was produced in the same manner as Examples 4 to 9 except that
the circulation of the mixed suspension of the tobacco starting material residue and
the extract with a pump and the exposure to ozone fine bubbles were not performed.
[0147] Regarding the resulting tobacco materials of Examples 4 to 9 and Comparative Example
2, the Hunter brightness was measured by the following method. The results are shown
in Table 2 below.
<Method for measuring Hunter brightness>
[0148] A powdered tobacco material was collected and placed in a petri dish having a diameter
of 12 cm until the thickness was about 2 cm. The brightness, hue, and saturation were
measured with a hue color difference meter (Hue color difference meter CR410, manufactured
by Konica Minolta, Inc.).
[0149] Based on the resulting data, the Hunter brightness was calculated using the following
equation.

[0150] Here, L represents brightness, and a and b represent chromaticity showing hue and
saturation.
[Table 2]
|
Circulation time of mixed suspension (time for exposure to ozone) (min.) |
Hunter brightness |
Comparative Example 2 |
0 |
34.7 |
Example 4 |
10 |
37 |
Example 5 |
20 |
40.0 |
Example 6 |
30 |
40.7 |
Example 7 |
40 |
42.5 |
Example 8 |
80 |
45.1 |
Example 9 |
120 |
45.4 |
[0151] As is clear from Examples 4 to 9 of Table 2 above, the longer the circulation time
of the mixed suspension (the time for exposure to ozone),the higher Hunter brightness
of the resulting tobacco material is.
(Examples 10 to 12)
[0152] Five g of a tobacco starting material with the same composition as that of Comparative
Example 1 and 400 mL of water were stirred and mixed for 30 minutes so as to allow
the component in the tobacco starting material to be eluted (dissolved) in water.
[0153] Subsequently, while the stirring was continued, the temperature of the mixed suspension
of the tobacco starting material residue and the extract was set to 5°C, 25°C, and
80°C. The exposure to ozone fine bubbles was continued for 5 hours while circulating
the mixed suspension with a pump. At this time, the average diameter of the ozone
fine bubbles was 45 µm and the exposure to ozone was carried out at 6.0 g/hr.
[0154] Subsequently, the mixed suspension after the ozone treatment was subjected to solid-liquid
separation. The extract after the separation was concentrated. The concentrated extract
was sprayed to the tobacco starting material residue after the separation so as to
make it return to the original state while keeping the residue at 40°C, and thus three
kinds of tobacco materials were produced.
[0155] Regarding the resulting tobacco materials of Examples 10 to 12, the pH and the Hunter
brightness were measured by the above method. The results are shown in Table 3 below.
[Table 3]
|
Temperature of circulation treatment of mixed suspension (°C) |
pH of tobacco material |
Hunter brightness |
Example 10 |
5 |
4.7 |
51.3 |
Example 11 |
25 |
5 |
51.8 |
Example 12 |
80 |
5.2 |
46.3 |
[0156] As is clear from Table 3 above, the tobacco materials of Examples 9 and 10 in which
the temperature of the mixed suspension was set to 5°C and 25°C showed a high Hunter
brightness as compared to that of the tobacco material of Example 11 in which the
temperature of the mixed suspension was set to 80°C. This is because the solubility
of ozone is higher at the low temperature side.
(Comparative Example 3)
[0157] A tobacco starting material in which ground powders of rustica leaves, burley leaves,
and tobacco stems were mixed at a proportion of 35% by mass, 15% by mass, and 50%
by mass, respectively, was prepared.
[0158] Then, 4 kg of a tobacco starting material and 80 L of water were stirred and mixed
for 30 minutes so as to allow the component in the tobacco starting material to be
eluted (dissolved) in water. Subsequently, the suspension was subjected to solid-liquid
separation and only the tobacco starting material residue as a solid was heated and
dried at 80°C. The moisture content of the dry product was measured. As a result,
the moisture content of the dry product was 9.8% by mass.
[0159] Subsequently, water (in an amount required to adjust the final moisture content of
the tobacco material to 25.0% by mass) was prepared. The water was sprayed to the
dry product to produce a tobacco material having a moisture content of 25.2% by mass.
(Example 13)
[0160] Four kg of a tobacco starting material with the same composition as that of Comparative
Example 3 and 80 L of water were stirred and mixed for 30 minutes so as to allow the
component in the tobacco starting material to be eluted (dissolved) in water. Subsequently,
the suspension was separated and only the tobacco starting material residue as a solid
was collected. Eighty L of water was added to the tobacco starting material residue
again and the stirring was continued. The exposure to ozone fine bubbles was continued
for 3 hours while circulating the suspension of the tobacco starting material residue
and the water with a pump. At this time, the average diameter of the ozone fine bubbles
was 10 µm and the exposure to ozone was carried out at 25°C and 38.0 g/hr.
[0161] Subsequently, the suspension after the ozone treatment was subjected to solid-liquid
separation and only the tobacco starting material residue as a solid was collected.
The residue was heated and dried at 80°C. The moisture content of the dry product
was measured. As a result, the moisture content of the dry product was 9.4% by mass.
[0162] Subsequently, water (in an amount required to adjust the final moisture content of
the tobacco material to 25.0% by mass) was prepared. The water was sprayed to the
dry product to produce a tobacco material having a moisture content of 24.7% by mass.
[0163] Regarding the resulting tobacco materials of Comparative Example 3 and Example 13,
the Hunter brightness was measured by the above method. The results are shown in Table
4 below.
[Table 4]
|
Hunter brightness |
Comparative Example 3 |
35 |
Example 13 |
47 |
[0164] As is clear from Table 4 above, the tobacco material obtained in Example 13 shows
a high Hunter brightness as compared to that of the tobacco material obtained in Comparative
Example 3.
(Example 14)
[0165] First, a tobacco starting material consisting of 60% by mass of laminae (18% by mass
of burley and 42% by mass of rustica) and 40% by mass of stems was prepared.
[0166] 5 g of the tobacco starting material and 400 mL of water were stirred and mixed for
30 minutes so as to allow the component in the tobacco starting material to be eluted
or dissolved in water. Subsequently, the mixed suspension was filtered to be separated
into an extract and a tobacco starting material residue.
[0167] The exposure to ozone fine bubbles was continued for 120 minutes while circulating
the extract with a pump. At this time, the average diameter of the ozone fine bubbles
was 45 µm and the exposure to ozone was carried out at 25°C and 6.0 g/hr. After the
treatment, the ozone was concentrated to a volume of 10% or less under reduced pressure
at 60°C.
[0168] Subsequently, the total amount of the extract after the ozone treatment was sprayed
for drying while heating the tobacco starting material residue at 40°C (RH 60%). The
resulting product was allowed to stand at 22°C and 60% RH for 12 hours to produce
a tobacco material having a moisture content of 14.6% by mass and a pH of 3.726.
(Example 15)
[0169] 5 g of the tobacco starting material having the same composition as that of Example
14 and 400 mL of water were stirred and mixed for 30 minutes so as to allow the component
in the tobacco starting material to be eluted or dissolved in water. Subsequently,
the mixed suspension was filtered to be separated into an extract and a tobacco starting
material residue.
[0170] The exposure to ozone fine bubbles was continued for 120 minutes while circulating
the extract with a pump. At this time, the average diameter of the ozone fine bubbles
was 45 µm and the exposure to ozone was carried out at 25°C and 6.0 g/hr. After the
treatment, the ozone was concentrated to a volume of 10% or less under reduced pressure
at 60°C.
[0171] On the other hand, 400 mL of water was newly added to the tobacco starting material
residue to prepare a suspension. The exposure to ozone fine bubbles was continued
for 120 minutes while circulating the suspension with a pump. At this time, the average
diameter of the ozone fine bubbles was 45 µm and the exposure to ozone was carried
out at 25°C and 6.0 g/hr. Thereafter, it was dried to obtain a treated residue.
[0172] Subsequently, the total amount of the extract after the ozone treatment was sprayed
for drying while heating the treated residue at 40°C (RH 60%). The resulting product
was allowed to stand at 22°C and 60% RH for 12 hours to produce a tobacco material
having a moisture content of 12.2% by mass and a pH of 3.227.
[0173] Regarding the resulting tobacco materials of Examples 14 and 15, the Hunter brightness
was measured by the above method. The results are shown in Table 5 below.
[Table 5]
|
Hunter brightness |
Example 14 |
41.5 |
Example 15 |
47.7 |
[0174] As is clear from Table 5 above, the tobacco material of Example 14 obtained by spraying
the extract after the ozone treatment to the tobacco starting material residue after
the extraction exhibits a high Hunter brightness. Further, the tobacco material of
Example 15 obtained by spraying the extract after the ozone treatment to the tobacco
starting material residue treated with the ozone after the extraction and drying it
exhibits a high Hunter brightness as compared to that of the tobacco material of Example
14.
(Example 16)
[0175] One g of the tobacco starting material having the same composition as that of Example
14 was mixed with 5% of hydrogen peroxide water to prepare a mixed suspension. The
suspension was allowed to stand for 12 hours, followed by filtration of the mixed
suspension to obtain a residue. Subsequently, the treated residue was dried while
heating the residue at 40°C (RH 60%). Thereafter, the resulting product was allowed
to stand at 22°C and 60% RH for 12 hours to produce a tobacco material. The Hunter
brightness of the resulting tobacco material was measured, and it was 47.1.
[0176] As is clear from this result, even if hydrogen peroxide is used as an oxidant except
for the ozone, a high Hunter brightness can be similarly obtained.
Industrial Applicability
[0177] According to the present invention, there can be provided a method for producing
a tobacco material in which undesirable characteristics are removed and the bleaching
or the like is modified and which has a excellent storage stability over a long period
of time as well as a tobacco material for oral use having a high Hunter brightness.
[0178] According to the present invention, there can be provided a tobacco product for oral
use which contains a tobacco material for oral use having a high Hunter brightness,
and exhibits an aesthetic appearance during storage and after use.