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Patent 2148678 Summary

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(12) Patent Application: (11) CA 2148678
(54) English Title: SOLID FEED AND PROCESS FOR PRODUCING SAME
(54) French Title: ALIMENTATION SOLIDE ET METHODE DE PREPARATION
Status: Dead
Bibliographic Data
(51) International Patent Classification (IPC):
  • A23K 20/163 (2016.01)
  • A23K 50/80 (2016.01)
(72) Inventors :
  • UCHIDA, KIICHI (Japan)
(73) Owners :
  • SAPPORO BREWERIES LIMITED (Japan)
(71) Applicants :
(74) Agent: RICHES, MCKENZIE & HERBERT LLP
(74) Associate agent:
(45) Issued:
(22) Filed Date: 1995-05-04
(41) Open to Public Inspection: 1995-11-18
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
125918/1994 Japan 1994-05-17
132456/1994 Japan 1994-05-24

Abstracts

English Abstract






Provided is a solid feed and a process for producing the solid feed
for culture fishes and shellfishes or animals characterized in that the
solid feed contains a specific polysaccharide.
The polysaccharide is used as a binder, and is also effective as an
agent for treating or preventing diseases. Further. the polysaccharide
is decomposed and absorbed into the fishes and shells or animals as an
energy source and nutrient, making it possible to increase a feed
effect.


Claims

Note: Claims are shown in the official language in which they were submitted.






WHAT IS CLAIMED IS:
1. A solid feed comprises containing a polysaccharide having the
following properties:
(1) White, tasteless, odorless, non-crystalline powder
(2) Solubility: soluble in water, formamide and dimethyl
sulfoxide but insoluble in alcohol, acetone, benzene,
ethyl acetate, hexane, chloroform and carbon tetrachloride
(3) pH of an aqueous solution: neutral or weakly acidic
(4) Constituent sugar: only glucose
(5) Elemental analysis: C: 43.0-45.0 %. H: 6.0-6.3 %
(6) Structure: .alpha. -glucan in which a main bond is an .alpha. -1.6 bond
(7) Protein: not detected by a Lowry method
(8) Molecular weight: approximately 10,000 or more without
Passing through a dialysis membrane
(9) Color reaction: positive in an anthrone-sulfuric acid reaction
and phenol-sulfuric acid reaction, and passive in a biuret
reaction, Lowry-Folin reaction, Elson-Morgan reaction and
iodine reaction
(10) Melting point: not showing a clear melting point
(11) UV absorption spectrum: showing no characteristic absorption
(12) IR absorption spectrum: showing characteristic absorption
ascribable to .alpha. -glucan
(13) l3C-NMR spectrum: showing characteristic absorption ascribable
to .alpha. -1.6 glucan
(14) Antitumor activity
2. A process for producing a solid feed characterized in that the


-17-


solid feed contains a polysaccharide having the following properties:
(1) White, tasteless, odorless, non-crystalline powder
(2) Solubility: soluble in water, formamide and dimethyl
sulfoxide but insoluble in alcohol, acetone, benzene,
ethyl acetate, hexane, chloroform and carbon tetrachloride
(3) pH of an aqueous solution: neutral or weakly acidic
(4) Constituent sugar: only glucose
(5) Elemental analysis: C: 43.0-45.0 %, H: 6.0-6.3 %
(6) Structure: .alpha.-glucan in which a main bond is an .alpha.-1,6 bond
(7) Protein: not detected by a Lowry method
(8) Molecular weight: approximately 10,000 or more without
passing through a dialysis membrane
(9) Color reaction: positive in an anthrone-sulfuric acid reaction
and phenol-sulfuric acid reaction, and passive in a biuret
reaction, Lowry-Folin reaction, Elson-Morgan reaction and
iodine reaction
(10) Melting point: not showing a clear melting point
(11) UV absorption spectrum: showing no characteristic absorption
(12) IR absroption spectrum: showing characteristic absorption
ascribable to .alpha.-glucan
(13) 13C-NMR spectrum: showing characteristic absorption ascribable
to .alpha.-1,6 glucan
(14) Antitumor activity
3. The process of claim 2 wherein the polysaccharide is used as a
binder when producing the solid feed and as an agent for treating or
preventing diseases of fishes and shellfishes or animals.
4. The process of claim 1 wherein the polysaccharide is produced



- 1 8 -


from one or more microorganisms selected from the group consisting of
Leuconostoc mesenteroides subspecies dextranicum BL-75 (FERM BP-2242),
L. mesenteroides subspecies dextranicum NCFB 517 (FERM BP-2711), L.
mesenteroides subspecies dextranicum NCFB 531 (FERM PB-2712), L.
mesenteroides subspecies dextranicum NCFB 861 (FERM BP-2713), L.
mesenteroides subspecies dextranicum NCFB 864 (FERM BP-2714), L.
mesenteroides subspecies dextranicum NCFB 880 (FERM BP-2715), L.
mesenteroides subspecies dextranicum 46-1 (FERM BP-2670), L.
mesenteroides subspecies dextranicum ATCC 1956, L. mesenteroides
subspecies dextranicum IF0 3349, Lactobacillus confusus 40-1 (FERM BP-
2865). L. confusus 40-3 (FERM BP-2866). L. confusus 77-1 (FERM BP-2867),
L. confusus 78-1 (FERM BP-2868), L. confusus 80-I (FERM BP-2869), and
mutants thereof.
5. The process of claim 2 wherein the feed is a feed for culturing
fishes, shells and crustacea or animals.




- 1 9 -

Description

Note: Descriptions are shown in the official language in which they were submitted.


214~78


SOLID FEED AND PROCESS FOR PRODUCINC SAME

FIEED OF THE INVENTION
The present invention relates to a solid feed and a process for
producing a solid feed. More specifically, the present invention
relates to a solid feed and a process for producing a solid feed for
culture fishes and shellfishes as well as for animals such as dogs,
cats, domestic animals and domestic fowls, characterized in that the
solid feed contains a specific polysaccharide.
BACKGROUND OF THE INVENTION
In recent years, cultivation of fishes and shellfishes has been
increasing in an attempt to utilize marine resources at a high level.
However, fishes and shellfishes suffer from bacterial or viral diseases
in a farm owing to degradation of a breeding environment such as
congested cultivation, water pollution or the like, inviting serious
damages to fishing industries.
- It has been indicated that one cause of this fact is that a
biological preventability of fishes and shellfishes is decreased in the
farm and the fishes and shellfishes tend to be infected with virus or
bacteria.
To cope with the fish diseases, antibiotics and vaccines have been
developed and used. However, the antibiotics are less effective because
of resistant bacteria, and when persons eat the fishes and shellfishes
to which the antibiotics are applied, the antibiotics are incorporated
into their bodies. For these reasons, the use of the antibiotics tends
to be limited. Further, kinds of fishes and shellfishes and diseases



- 1 -

214g~7~
-



thereof to which the vaccines can be applied are also limited.
Further, bacterial or viral diseases have often occurred owing to
congested breeding, degradation of a breeding environment and the like,
inviting serious damages to breeding industries. Breeding of pets such
as dogs, cats and the like has been recently increased. However, the
pets have not been bred with appropriate feeds, and they have been
infected with bacteria or virus, and have suffered from diseases.
It has been indicated that one cause of this fact is that a
biological preventability of the pets and domestic animals is decreased
in the breeding environment and the pets and domestic animals tend to
be infected with virus or bacteria.
To cope with the diseases, antibiotics and vaccines have been
developed and used. However, the antibiotics are less effective
because of resistant bacteria, and there is a possibility that the
antibiotics are incorporated into human bodies. For these reasons, the
use of the antibiotics tends to be limited. Further, kinds of animals
and diseases to which the vaccines can be applied are also limited.
Under these circumstances, development of a new agent for
preventing diseases which is safe and effective has been in demand.
On the other hand, when producing a solid feed for culture fishes
and shelIfishes or animals, a binder is required. Typical examples of
the binder which has been used so far include starch, dextrin, gluten,
agar, gelatin, casein. carrageenan,- sodium alginate, sodium
polyacrylate, carboxYmethYlcellulose (CMC), hydroxypropylcellulose
(HPC), sodium lignin sulfonate, sodium salt of casein and sodium
cellulosic glycolate. The starch and gluten are used in relatively
large amounts of from 5 to 20 %, but the binder is commonly added in an

2148~7g

amount of from approximately 1 to 10 %, preferably 0.5 to 5 %. It is
preferable that the binder is effective in as small an amount as
possible. Thus, development of a new substance has been expected.
SUMMARY OP THE INVENTION
The present inventors established a process for producing a
tasteless, odorless, water-soluble polysaccharide having physiological
activities such as an antitumor activity, activity of adiusting
immunity, activity of preventing infection and the like, and made
studies with respect to the develoPment of the usage of such a
polysaccharide (for example, Japanese Laid-Open Patent Application
(Kokai) Nos. 35,791/1991 and 224,494/1991).
During the development of the usage of this polysaccharide, they
have focused on the physiological activity such as the activity of
preventing infection by the immunological activity of the
polysaccharide, and have assiduouslY made extensive investigations.
Consequently, they have found that the polysaccharide gives fishes,
shellfishes and animals such a physiological activity, and it can,
therefore, be used as an agent for treating or preventing diseases due
to such microorganisms as bacteria, virus, etc.
It has been further found that the Polysaccharide is produced as a
highly viscous solution, that when the polysaccharide is mixed in the
form of a solution, it can firmly bind a powdery raw material because of
the high viscosity and when the polysaccharide is dried, it is
solidified, for which reason it can be used as a binder in the
production of a solid feed.
Consequently, various solid feeds can be produced by directly
incorporating the viscous polysaccharide solution into the powdery raw

21~867~

material of the feed for culture fishes and shellfishes or animals
without using another binder.
The use of water-soluble glucan as an agent for preventing fish
diseases is described in Japanese Laid-Open Patent Application (Kokai)
Nos. 218.615/1990 and 256,620/1990. However. a knowledge of using the
water-soluble glucan as the binder has not been gained yet.
Moreover, since the feed for culture fishes and shellfishes is
supplied in water. there are serious problems of cultivation fishery
such as water pollution and decrease in the intake efficiency owing to
collapse of the solid feed in water.
There have been examples in which the polysaccharide is used as an
agent for preventing or treating diseases of animals. However. a
knowledge of utilizing the polysaccharide as a binder has not been
gained yet. Also. when using a feed for animals in solid form,
collapse of the solid feed and a decrease in the intake efficiency
thereof are serious problems. AccordinglY. the binder of the solid feed
is the important factor.
However. it has been clarified that non-digestive high polymers
such as CMC. sodium polyacrylate and the like which have been currentlY
used in many cases are not only lacking in the immunological activity
but also adversely affect growth and digestion of fishes and
shellfishes or animals.
On the other hand. since the sPecific polysaccharide used in the
present invention is digestive. it is digested and absorbed into fishes.
shellfishes and animals as a nutrient and is utilized in vivo.
The polysaccharide used in the present invention is characterized
in that it can be used not only as a binder but also as an agent for



- 4 -

2148fi78

preventing infectious diseases having an immunological activitY and
further as a nutrient.
It is advisable that the form of the feed and the stability of the
feed in water are secured sufficiently such that the feed in the form of
pellets or the like is neither too hard, nor is it collapsed to form a
powder. The polysaccharide is extremely suitable as the binder of the
feed.
Besides, since the polysaccharide used in the present invention is
advantageous in that when solidifying the feed, the polysaccharide
exhibits both of a bindability and an ability of forming a surface
coating, it is also suitable for the production of a finely divided feed
such as a microbinding feed for use in, for example, larvae of
crustacea, Iarvae of shells and spawns.
Based on the above-mentioned findings, the present inventors have
completed a novel process in which a specific polysaccharide to be
described later is used as an agent for preventing diseases and as a
binder when producing a solid feed for culture fishes and shellfishes
or anlmals.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is to provide a solid feed for culture fishes
and shellfishes or animals and a process for producing the solid feed
characterized in that the solid feed contains a polysaccharide having
specific properties.
That is. the present invention is to provide a solid feed for
culture fishes and shellfishes or animals and a process for producing a
solid feed for culture fishes and shellfishes or animals characterized
in that the solid feed contains a polysaccharide having the following

21~8fi7~

properties:
(1) White, tasteless, odorless, non-crystalline powder
(2) Solubility: soluble in water, formamide and dimethyl sulfoxide
but insoluble in alcohol, acetone, benzene, ethyl acetate,
hexane, chloroform and carbon tetrachloride
(3) pH of an aqueous solution: neutral or weakly acidic
(4) Constituent sugar: only glucose
(5) Elemental analysis: C: 43.0-45.0 %, H: 6.0-6.3 %
(6) Structure: a -glucan in which a main bond is an a -1,6 bond
(7) Protein: not detected by a Lowry method
(8) Molecular weight: approximately 10,000 or more without passing
through a dialysis membrane
(9) Color reaction: positive in an anthrone-sulfuric acid reaction
and phenol-sulfuric acid reaction, and passive in a biuret
reaction. Lowry-Folin reaction, Elson-Morgan reaction and
iodine reaction
(10) Melting point: not showing a clear melting point
(11) UV absorption spectrum: showing no characteristic absorpotion
(12) IR absorption spectrum: showing characteristic absorption
ascribable to a -glucan
(13) l3C-NMR spectrum: showing characteristic absorption ascribable
to a -1, 6 glucan
(14) Antitumor activity
The polysaccharide used in the present invention is a -glucan in
which a main bond is a water-soluble a -1,6 bond. This polysaccharide
can be obtained by various methods. It is practically advisable that
the polysaccharide be obtained as a fermentation product formed by

21~7~

cultivating a specific microorganism using sucrose as a substrate. For
example, an intended polysaccharide is obtained as a viscous solution
by cultivating one or more microorganisms with sucrose-containing
solution or sucrose-containing medium (for example, Japanese Laid-Open
Patent Application (Kokai) No. 35,791/1991). The microorganisms are
selected from the group consisting of Leuconostoc mesenteroides
subspecies dextranicum BL-75 (FERM BP-2242), L. mesenteroides subspecies
dextranicum NCFB 517 (FERM BP-2711), L. mesenteroides subspecies
dextranicum NCFB 531 (FERM PB-2712), L. mesenteroides subspecies
dextranicum NCFB 861 (FERM BP-2713), L. mesenteroides subspecies
dextranicum NCFB 864 (FERM BP-2714), L. mesenteroides subspecies
dextranicum NCFB 880 (FERM BP-2715), L. mesenteroides subspecies
dextranicum 46-1 (FERM BP-2670), L. mesenteroides subspecies dextranicum
ATCC 1956 and L. mesenteroides subspecies dextranicum IFO 3349;
Lactobacillus confusus 40-1 (FERM BP-2865), L. confusus 40-3 (FERM BP-
2866), L. confusus 77-1 (FERM BP-2867), L. confusus 78-1 (FERM BP-2868)
and L. confusus 80-1 (FERM BP-2869); and mutants thereof.
The polysaccharide may be separated from the culture solution in a
usual manner. For example, the polysaccharide can be easily separated
by filtration or centrifugal separation to remove the microbial cells.
As the crude polysaccharide, the microbial cell-containing culture
solution itself or the culture solution being subiected to heat-
sterilization can be used. If required, the culture solution may be
purified by removing the microbial cells through a procedure such as
filtration, centrifugal separation or the like and then applYing
appropriate purifying procedure.
Purther, a cell-free polysaccharide having a high purity can be

21~78

produced as a viscous solution directly easilY by reacting sucrose
solution with a polysaccharide synthetase extracted from the above-
mentioned microorganism (refer to Japanese Laid-Open Patent Application
(Kokai) No. 224,494/1991).
Starting materials used to produce the solid feed for culture
fishes and shellfishes or animals in the present invention are a fish
meal, skim milk, oil meal, corn flour. wheat flour, dry yeast, egg
powder, rice bran, wheat bran, meat powder and molasses, alfalfa meal,
trace amounts of additives. The starting (raw) materials may be
properly selected in consideration of the composition of the feed, kinds
of fishes and shellfishes or animals and the like. For example, a
composition of a feed for cultivating an ayu (sweetfish) is shown below.
Table 1
Composition of a feed for an ayu (a suitable form of a solid
feed is crumbles):
Fish meal 30 %
Meat powder 20 %
Wheat flour 15 %
Soybean flour 5 %
Soybean oil cake 10 X
Wheat bran 5 %
Germ 5 X
Dry beer yeast 5 X
Whole egg powder 3 X
Additives 1 X
Polysaccharide 1 X




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2148fi78

Further. a composition of a feed for dog is shown below.
Table 2
Composition of a feed for a dog (pellet type. calculated as
anhydrous product):
Fish meal 30 %
Meat powder 20 %
Corn flour 15 %
Soybean oil cake 10 %
Rice bran 5 %
Alfalfa meal 5 %
Germ 5 %
Dry beer yeast 5 %
Whole egg powder 3 %
Additives 1 %
Polysaccharide 1 %

In the production of the solid feed for culture fishes and
shellfishes or animals. the amount of the polysaccharide used is usually
from 0.01 to 5.0 X by weight, preferably from 0.05 to 2.0 % by wei8ht~
calculated as an anhydrous product. based on the total weight of the
feed ingredients. The feed is produced under ordinary conditions
except that the polysaccharide is used instead of a conventional
binder. In a typical process for producing the feed, a mixture of
various feed ingredients corresPonding to kinds of fishes and
shellfishes or animals and dry raw materials is kneaded with the
polysaccharide (liquid) at a predetermined concentration. and the
reaction mixture is formed into fine particles. granules. pellets. or



_ g _

2`~ ~67~

spiral bars which are then dried. Crumbles are obtained by drying and
pulverizing the pellets and screening the resulting particles.
When using a powdery polysaccharide, a liquid polysaccharide is
powdered by spraY-drying or the like. The powdery polysaccharide is
mixed with the powdery feed starting materials, and water is suitably
added to the resulting substance. The mixture can be formed into
pellets or the like. The powdery polysaccharide is indeed advantageous
in storage, transportation and the like, but the powdering takes much
cost. Thus, the powdery polysaccharide is not economical.
The fishes and shellfishes which are cultivated with the feed
provided by the present invention include fishes, shells and crustacea.
Examples thereof include those cultivated in fresh water, such as a
carp, eel, ayu, rainbow trout, loach, goldfish, tilapia, kokanece and
catfish; and those cultivated in seawater, such as a young Yellowtai
yellowtail, red sea bream, black porgy, horse mackerel, hardtail,
silver salmon, trout, flatfish, bluefin, rabbitfish, crimson sea bream,
parrot fish, prawn, lobster, scallop and oyster.
The animals which are cultivated with the feed provided bY the
present invention include PetS~ domestic animals, domestic fowls, etc.
Examples thereof include mammalia such as dog, cat, etc.; birds such as
parakeet, Java sparrow, etc.; domestic animals such as cow, pig, horse,
sheep, goat, etc.; domestic fowls such as chicken, duck, etc.
The present invention is characterized in that when producing a
solid feed for culture fishes and shellfishes or animals in the form of
pellets, crumbles, spiral bars, fine particles, granules or the like, a
specific polysaccharide is incorporated into the solid feed. The
Polysaccharide is used as a binder, and is also effective as an agent



-1 O-

21~8~78

for treating or preventing diseases. Further, the polysaccharide is
decomposed and absorbed into the fishes and shellfishes or animals as
an energy source and nutrient, making it possible to increase a feed
effect.
Examples
The present invention is illustrated more specifically by referring
to the following Examples.
Example 1
Production of a polysaccharide:
Leuconostoc mesenteroides subspecies dextranicum BL-75 (FERM BP-
2242) was subiected to stab-culture. The cultured cells were
inoculated in a test tube filled with 8 ml of a culture medium
(comprising 4.0 % sucrose, 0.05 % dry beer yeast, 0.5 % dipotassium
hydrogenphosphate and 0.1 % sodium chloride) and having a diameter of 15
mm, and the mixture was statically cultured at 26C for 24 hours.
Subsequently, 20 ml of the above-obtained cells at a concentration of 1
x 107/cm2 were inoculated in a 3-liter conical flask filled with 1 liter
of a culture medium having the above-mentioned composition, and were
statically cultured at 28C for 20 hours.
Water was added to the thus-obtained viscous culture solution to
adiust the concentration of the polysaccharide to 1 %. Then, the
culture solution was centrifuged to remove the cells and insoluble
matters and to obtain 1.8 liters of the 1 % polysaccharide solution.
This process for producing the polysaccharide is described in detail in
Japanese Laid-Open Patent Application (Kokai) No. 35,791/1991.
Production of a feed:
One hundred grams of a fish meal, 70 8 of a skim milk, 10 8 of an

2148~7~

oyster shell powder, 200 g of a chicken meal. 200 g of an oil meal, 250
g of a corn flour, 10 g of a wheat germ. 80 g of a rice bran and 10 g
of dry beer yeast and other additives were uniformly mixed, and further
mixed with 150 g of the above-obtained lX polysaccharide solution. The
resulting mixture was formed into pellets having a diameter of 5 mm by
means of a pelleter. The pellets were steam-sterilized, and then dried
to yield 1 kg of the pelletized feed for trouts. This feed was not
collapsed in water, and was taken in by trouts at good efficiency
without water pollution.
Example 2
Production of a polysaccharide:
One hundred milliliters of a sterilized 1 % polysaccharide solution
(crude enzymatic solution) obtained in the same manner as in Example 1
were added to 1 liter of a heat-sterilized culture medium comprising 28
% sucrose, 0.1 % yeast extract, 0.5 % potassium hydrogenphosphate and
0.1 % sodium chloride. The mixture was statically reacted at 30C for
24 hours. Water was then added thereto to obtain 2 liters of a 10 %
polysaccharide solution. This process for producing the polysaccharide
is disclosed in detail in Japanese Laid-Open Patent Application (Kokai)
No. 224,494/1991.
Production of a feed:
A fish meal (450 g), 200 g of a skim milk, 150 g of a wheat flour,
50 g of a bread crumb, 50 g of an oil meal and 40 g of dry beer yeast
and other additives were uniformlY mixed, and further mixed with 150 g
of the above-obtained polysaccharide solution. The mixture was then
formed into pellets having a diameter of 6 mm by means of a pelleter.
The pellets were steam-sterilized, and dried with hot air to yield l kg



- 1 2 -

21~78

of a pelletized feed for eels. The feed was applied to eels in a farm.
It was found that the feed was not collapsed in water and was taken in
by eels at good efficiency without water pollution.
Example 3
Production of a polysaccharide:
Lactobacillus confusus 40-1 (FERM BP-2865) was subiected to stab-
culture. The cultured cells were inoculated in a test tube filled with
5 ml of a culture medium (comprising 2.0 % sucrose, 0.5 % yeast extract
and 2.0 % dipotassium hydrogenphosphate, pH 7.4) and having a diameter
of 15 mm, and the mixture was statically cultured at 26C for 24 hours.
Subsequently, 10 ml of the culture solution were added to a 1-liter
conical flask filled with 500 ml of a culture medium having the above-
mentioned composition, and were statically cultured at 26C for 24
hours.
The thus-obtained culture solution was heat-sterilized, and then
centrifuged to remove the cells and to obtain 470 ml of a 1 %
polysaccharie solution. This process for producing the polysaccharide
is detailed in Japanese Laid-Open Patent Application (Kokai) No.
36,187/1992.
Production of a feed:
Five-hundred grams of a fish meal, 200 g of a wheat flour, 100 8 of
a meat bone meal, 50 8 of an oil meal, 50 g of a rice bran and 50 g of
dry beer yeast and other additives were uniformly mixed, and further
mixed with 180 g of the above-obtained lX polysaccharide solution. The
mixture was formed into pellets having a diameter of 5 mm by means of a
pelleter. The pellets were steam-sterilized, and then dried to yield 1
kg of a pelletized feed for red sea breams. This feed was not

2i~8~7a

collapsed in water and was taken in by red sea breams at good efficiency
without water pollution.
Example 4
Production of a polysaccharide:
Leuconostoc mesenteroides subspecies dextranicum BL-75 (FERM BP-
2242) was subiected to stab-culture. The cultured cells were
inoculated in a test tube filled with 8 ml of a culture medium
(comprising 5.0 X sucrose, 0.05 X dry beer yeast, 0.5 % dipotassium
hydrogenphosphate and 0.1 % sodium chloride) and having a diameter of 15
mm, and the mixture was statically cultured at 30C for 18 hours.
Subsequently, 20 ml of the above-obtained cells at a concentration of 1
x 107/cm2 were inoculated in a 3-liter conical flask filled with 1 liter
of a culture medium having the above-mentioned composition, and were
statically cultured at 28C for 20 hours.
Water was added to the thus-obtained viscous culture solution to
adiust the concentration of the polysaccharide to 2 %. Then, the
culture solution was centrifuged to remove the cells and insoluble
matters and to obtain 1.0 Iiter of the 2% polysaccharide solution.
This process for producing the polysaccharide is described in detail in
Japanese Laid-Opn Patent Application (Kokai) No. 35,791/1991.
Production of a feed:
One hundred grams of a fish meal, 70 g of a skim milk, 60 g of a
meat bone meal, 150 g of a chicken meal, 50 g of an alfalfa meal, 200 g
of an oil meal, 250 g of a corn flour, 10 g of a wheat germ, 80 g of a
rice bran and 10 g of dry beer yeast and other additives were uniformlY
mixed, and further mixed with 200 g of the above-obtained
polysaccharide solution. The resulting mixture was formed into pellets



- 1 4 -

- 21~8~i7~

having a diameter of 10 mm by means of a pelleter. The pellets were
steam-sterilized. and then dried to yield 1 kg of the pelletized feed
for puppies.
Example 5
Production of a polysaccharide:
One hundred milliliters of a sterilized 1 X polysaccharide solution
(crude enzymatic solution) obtained in the same manner as in Example 4
were added to 1 liter of a heat-sterilized culture medium comprising 26
% sucrose. 0.1 % yeast extract. 0.5 % potassium hydrogenphosphate and
0.1 % sodium chloride. The mixture was statically reacted at 30C for
20 hours. Water was then added thereto to obtain 2 liters of a 10%
polysaccharide solution. This process for producing the polysaccharide
is detailed in Japanese Laid-Open Patent Application (Kokai) No.
224.494/1991.
Production of a feed:
A fish meal (550 g). 100 g of a skim milk. 150 g of a wheat bran.
30 g of a meat bone meal. 70 g of an oil meal and 40 8 of dry beer
yeast and other additives were uniformly mixed. and further mixed with
180 g of the above-obtained polysaccharide solution. The mixture was
then formed into pellets having a diameter of 7 mm by means of a
pelleter. The pellets were steam-sterilized. and dried ~ith hot air to
yield 1 kg of a pelletized feed for cats.
Example 6
Production of a polysaccharide:
Lactobacillus confusus 40-1 (FERM BP-2865) was subiected to stab-
culture. The cultured cells were inoculated in a test tube filled with
15 ml of a culture medium (comprising 3.0 X sucrose. 0.5 % yeast extract



- 1 5 -

2148~78

and 2.0 % dipotassium hydrogenphosphate. pH 7.4) and having a diameter
of 15 mm, and the mixture was staticallY cultured at 26C for 24 hours.
Subsequently. 10 ml of the culture solution was added to a 1-liter
conical flask filled with 500 ml of a culture medium having the above-
mentioned composition. and statically cultured at 26 C for 24 hours.
The thus-obtained culture solution was heat-sterilized, and then
centrifuged to remove the cells and to obtain 450 ml of a 1.3X
polysaccharide solution. This process for producing the polysaccharide
is detailed in Japanese Laid-Open Patent Application (Kokai) No.
36.187/1992.
Production of a feed:
Five-hundred grams of a fish meal. 200 g of a wheat bran. 50 g of
an oyster shell powder. 50 g of an oil meal. 50 g of a rice bran. 50 g
of a dry vegetable and 50 g of dry beer yeast and other additives were
uniformly mixed. and further mixed with 170 g of the above-obtained 1.3
% polysaccharide solution. The mixture was formed into pellets having
a diameter of 3 mm by means of a pelleter. The pellets were steam-
sterilized, and then dried to yield 1 kg of a pelletized feed for
chickens.




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Administrative Status

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Administrative Status

Title Date
Forecasted Issue Date Unavailable
(22) Filed 1995-05-04
(41) Open to Public Inspection 1995-11-18
Dead Application 1998-05-04

Abandonment History

Abandonment Date Reason Reinstatement Date
1997-05-05 FAILURE TO PAY APPLICATION MAINTENANCE FEE

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $0.00 1995-05-04
Registration of a document - section 124 $0.00 1996-01-18
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
SAPPORO BREWERIES LIMITED
Past Owners on Record
UCHIDA, KIICHI
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Cover Page 1996-07-04 1 16
Abstract 1995-11-18 1 12
Description 1995-11-18 16 525
Claims 1995-11-18 3 82