Sélection de la langue

Search

Sommaire du brevet 1061068 

Énoncé de désistement de responsabilité concernant l'information provenant de tiers

Une partie des informations de ce site Web a été fournie par des sources externes. Le gouvernement du Canada n'assume aucune responsabilité concernant la précision, l'actualité ou la fiabilité des informations fournies par les sources externes. Les utilisateurs qui désirent employer cette information devraient consulter directement la source des informations. Le contenu fourni par les sources externes n'est pas assujetti aux exigences sur les langues officielles, la protection des renseignements personnels et l'accessibilité.

Disponibilité de l'Abrégé et des Revendications

L'apparition de différences dans le texte et l'image des Revendications et de l'Abrégé dépend du moment auquel le document est publié. Les textes des Revendications et de l'Abrégé sont affichés :

  • lorsque la demande peut être examinée par le public;
  • lorsque le brevet est émis (délivrance).
(12) Brevet: (11) CA 1061068
(21) Numéro de la demande: 1061068
(54) Titre français: PROCEDE DE PRODUCTION DE FIBRES QUI GERMENT
(54) Titre anglais: PROCESS FOR PRODUCING PULLULAN FIBERS
Statut: Durée expirée - au-delà du délai suivant l'octroi
Données bibliographiques
(51) Classification internationale des brevets (CIB):
  • D01F 9/00 (2006.01)
  • C08L 5/00 (2006.01)
(72) Inventeurs :
  • NAKASHIO, SEIZO
  • TSUJI, KOZO
  • TOYOTA, NOBUHIRO
  • FUJITA, FUMIO
  • NOMURA, TATSUO
(73) Titulaires :
  • SUMITOMO CHEMICAL COMPANY
  • HAYASHIBARA BIOCHEMICAL LABORATORIES
(71) Demandeurs :
  • SUMITOMO CHEMICAL COMPANY
  • HAYASHIBARA BIOCHEMICAL LABORATORIES
(74) Agent:
(74) Co-agent:
(45) Délivré: 1979-08-28
(22) Date de dépôt:
Licence disponible: S.O.
Cédé au domaine public: S.O.
(25) Langue des documents déposés: Anglais

Traité de coopération en matière de brevets (PCT): Non

(30) Données de priorité de la demande: S.O.

Abrégés

Abrégé anglais


PROCESS FOR PRODUCING PULLULAN FIBERS
ABSTRACT OF THE DISCLOSURE
A pullulan-containing fiber is obtained by
using as a spinning solution an aqueous solution of
pullulan or a melt of pullulan plasticized with water,
and extruding the spinning solution at a temporary
up to 100°C through a nozzle into a gas phase.

Revendications

Note : Les revendications sont présentées dans la langue officielle dans laquelle elles ont été soumises.


THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A process for producing a pullulan-containing
fiber, characterized by using as a spinning solution an aqueous
solution of pullulan or a melt of pullulan plasticized with water,
and extruding the spinning solution at a temperature up to 100°C.
through a nozzle into a gas phase.
2. A process according to Claim 1, wherein the spinning
solution contains 5 to 99 wt% of water.
3. A process according to Claim 1, wherein in the
spinning solution is incorporated a plasticizer or a softener.
4. A process according to Claim 3, wherein the plasti-
dizer or softener is glycerin, sorbitol, maltitol, ethylene
glycol, propylene glycol, polyethylene glycol, polypropylene gly-
col or dimethyl sulfoxide.
5. A process according to Claim 1, wherein the
spinning solution is used in admixture with a water-soluble
polymer or an emulsion of water-insoluble polymer.
6. A process according to Claim 5, wherein the water-
soluble polymer is polyvinyl alcohol, polyethyleneimine, poly-
acrylamide, polyacrylic acid, sodium polyacrylate, polyvinyl
pyrrolidone, polyethylene oxide, sodium alginate, carboxymethyl
cellulose or hydroxyethyl cellulose.
7. A process according to Claim 5, wherein the water-
insoluble polymer is polyvinyl acetate, polyethylacrylate, poly-
propylacrylate, poly-n-butylacrylate, polymethacrylic acid, poly-
methylmethacrylate, polypropylmethacrylate, polybutylmethacrylate,
polystyrene, polyvinylchloride, polyvinylidenechloride, poly-
acrylonitrile or ethylene-vinylacetate copolymer.
8. A process according to Claim 1, wherein in spinning
solution is incorporated at least one member selected from the
group consisting of colorants, antioxidants, ultraviolet light
12

absorbers, fillers, and flame-retardants.
9. A process according to Claim 1, wherein in the
spinning solution is incorporated a monofunctional monomer, a
polyfunctional monomer and an initiator.
10. A process according to Claim 9, wherein the mono-
functional monomer is selected from the group consisting of
acrylamide, acrylic acid, methacrylic acid, 2-hydroxyethyl meth-
acrylate, and N-vinyl pyrrolidone.
11. A process according to Claim 9, wherein the poly-
functional monomer is ethylene glycol dimethacrylate, diethylene
glycol dimethacrylate, triethylene glycol dimethacrylate, non-
aethylene glycol dimethacrylate or methylene-bis-acrylamide.
12. A process according to Claim 9, wherein the initia-
tor is hydrogen peroxide, ammonium persulfate, potassium persul-
fate, cerium (IV) ammonium nitrate, cerium (IV) ommonium sulfate,
azobis-isobutyronitrile, t-butylperoxide, dicumylperoxide, cumene
hydroperoxide or t-butyl hydroperoxide.
13. A process as claimed in Claim 1, 2 or 3 in which
the temperature is from 70°C to 20°C.
14. A process as claimed in Claim 1, 2 or 3 in which
the temperature is from 50°C to 20°C.
15. A process as claimed in Claim 1, 2 or 3 in which
the pullulan has a molecular weight of from 10,000 to 5,000,000.
16. A process according to Claim 1 in which the fibre
is stretched at a temperature in the range of 60° to 120°C.
17. A process according to Claim 1 in which the fibre is
insolubilized by crosslinking with formaldehyde, acetaldehyde,
n-butylaldehyde, glyoxal, epoxy resin, diisocyanate, dimethyl-
olurea or dimethylolethyleneurea.
18. A process according to Claim 1 in which the fibre
is insolubilized with a bichromate and light.
13

19. A process as claimed in Claim 9 in which the fibre
is insolubilized by crosslinking, after spinning, with heat,
light or radiation.
14

Description

Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.


11~6~68
The present invention relates to a process for produc-
ing a novel fiber containing pullulan, which is a polymer having
repeated units of maltotriose.
Pullulan decomposes at about 2S0C when heated in an
absolutely dry state, but does not melt at temperatures between
room temperature and the thermal decomposition temperature there-
of. A process as been disclosed in which the melting temperature
of pullulan is lowered by addition of water as a plasticizer,
and is then subjected to molding. According to said process, -
it is known that a fiber can beobtained by subjecting pullulancontaining less than about 25% of water to extrusion at a temp-
erature of 110 to 120C under a pressure of 100 to 150 kg/cm2.
The pullulan referred to in the present invention is
a linear high poIymer in which units of maltotriose, which is
a trimer of glucose, are repeatedly bonded through ~-linkages
which are different from those of said trimer, and has the
molecular structure represented by the formula
CH20H CH20E~ CH20H '
~ ~
O ~ O ~ O 2 C 2 2
~ ~ ~ ~ t CH2 CH~OI CH~OH
~ O ~
wherein n is an integer of 20 to 10,000 which has the polymeri-
zation degree.
Heretofore, pullulan has been known merely as a water-
soluble tacky substance, but has remained a substance which is
entirely unknown in the field of fiber industry.
While the pullulan used in the present invention
-- 1 --

1061068
contains glucose units in its molecule, it is entirely different
in molecular structure and greatly different in properties from
starch, oxidized starch, enzymated starch, etherified starch,
cationized starch, aminated starch, cellulose, alkyl cellulose,
hydroxyalkyl cellulose, carboxymethyl cellulose and gum arabic
which are conventional glucose derivatives composed mainly of
glucose units, as in the case of pullulan.
Among the notewarthy properties of pullulan, those
which are particularly outstanding are its specific water solub-
ility and its excellent threading property.i.e. its ability toform filaments. The inventors have conducted extensive studies
to find a process for converting pullulan into fibers and to con-
firm that the resulting fibers possess excellent properties.
The present invention provides a novel fiber containing
pullulan which has a strength capable of practical use and a
specific water solubility.
The invention also provides a process for producing the
said fiber.
The present invention provides a process for producing
a fibrous substance, in which an aqueous solution containing
pullulan or a melt of pullulan plasticized with water is adjusted
to a temperature up to 100C. or less, preferably 70 to 20C,
more preferably 50 to 20C and is extruded through a nozzle into
a gas phase.
The present inventors have found that since pullulan
has a specific affinity for water, it can be easily spun at a
temperature lower than that disclosed inthe aforesaidknown process
taking advantage of the facts that pullulan and cold water are
homogeneously miscible with each other in any proportions, that
~0 an aqueous solution of pullulan has a high threading property,
and that an aqueous pullulan solution is stable over a long
period of time. A feature of the present invention is that a
-- 2

;1068
spinning solution comprising an aqueous pullulan solution or a
water-containing pullulan melt is spun at such a relatively low
temperature as up to 100C.
Pullulan has excellent water solubility, and particul-
arly the solubility of pullulan in the cold water is higher than
that of any other water-soluble polymer. A conventional water-
soluble polymer, e.g. polyvinyl alcohol, is sparingly soluble in
cold water, in general, though the extent of water solubility
varies depending on the degree of saponification of the polyvinyl
alcohol, and it is ordinary practice to prepare an aqueous poly-
vinyl alcohol solution by spraying steam maintained at above 110C.
into the system to dissolve the polyvinyl alcohol. Carboxymethyl
cellulose, which is also a water soluble polymer, has the disad-
vantage that when charged all at once into water, it exhibits
a so-called "undissolved state" making it difficult to obtain a L
homegeneous aqueous solution. In contrast to this, the pullulan E
used in the present invention is specific in water solubility ~t
as compared with polyvinyl alcohol or carboxymethyl cellulose,
and hence has the characteristic of quickly dissolving even in
cold water. Further, when compared with the viscosity of an
aqueous solution of another water-soluble polymer, which is
identical in molecular weight and concentration with pullulan,
the viscosity of an aqueous solution of pullulan is far lower
than that of an aqueous solution of not only carboxymethyl cellu-
lose but also polyvinyl alcohol, which is known to be relatively
low in viscosity. This low viscosity of aqueous pullulan solu-
tion, coupled with the specific water solubility of pullulan, has
made it possible that the aqueous pullulan solution, when used
as a spinning solution, is easily spun into fibres by extrusion
through a nozzle into air, nitrogen or other gas, while adjusting t
the aqueous pullulan solution to such a low temperature as up to
100C.
- 3 - ~t
'

1061068
No disclosure has yet been made as to the spinning of
starches, in general, except the disclosure in Ooya et al: "Sen-i
To Kogyo (Fibers and Industries)", Vol. 5, No. 9, page 441 (1972).
This literature teaches that corn starch, rice, millet flour,
wheat flour or the like starch is charged with 10 to 50% of
water, and the resulting mixture is subjected to a first heating
operation and is then cooled to homogeneously obtain a gel-like
spinning solution containing water, which is again heated to 90
to 120C and then extruded to obtain spun fibres. By contrast,
the pullulan used in the present invention can homogeneously
absorb a desired amount of water either in the form of steam or
by water spraying, and does not require any preliminary heating
operation for homogeneous dispersion of water. Starch is crystal-
line and hence must be dissolved by heating in a single operation,
whereas pullulan is non-crystalline and hence is easy in handling,
and this has marked advantages in the production of pullulan
fibers. Further, the crystallinity of starch and the non-crystal-
linity of pullulan result in a great difference in stability
between the two when converted into the form of aqueous solutions.
That is, an aqueous pullulan solution is stable over a long period
of time at any concentration, and does not exhibit any such gela-
tion or so-called "aging" phenomenon as observed in aqueous starch
stolutions. Consequently, an aqueous pullulan solution or a melt
of pullulan plasticized with water can easily be spun into fibres
by extrusion through a nozzle into a gas such as air or nitrogen
at relatively low temperature such as up to ~00C which cannot be
expected in the case of starches.
It is a characteristic of pullulan that even when an
aqueous pullulan solution or a pullulan melt has a relatively low
temperature at the time of spinning, as compared with a solution
of starch, the solution or melt is low in viscosity and

1061068
nence can be extruded under a relatively low extrusion pressure.
The spinnability of an aqueous pullulan solution or a pullulan
melt at a relatively low temperature ranging from 0 to 100C.
including room temperature is not only advantageous from the
standpoint of thermal efficiency, but also gives such great prac-
tical advantages that the temperature control of the spinning
solution and the maintenance of uniform temperature distribution
in the spinning solution can be facilitated to make the spun
filaments free from unevenness and to make possible the production
of fibers definite in quality.
The tensile strength of the starch fiber produced
according to the process disclosed in the previously cited lit-
erature is about 300 kg/cm2, whereas that of the pullulan fiber
produced according to the process of the present invention is
2,520 kg/cm2 and thus is more than 8 times the strength of said
starch fiber (refer to Example 1 as hereinafter described).
The water content of the pullulan spinning solution
used in the present invention is in the range of 5 to 99 wt%, t
preferably 30 to 80 wt% and spun fibres can be obtained by pro-
perly adjusting the temperature of the spinning solution to
the
molecular weight of pullulan, the shape and size of spinning
nozzle, and the extrusion pressure. For example, in case a
spinning solution of pullulan having a molecular weight of ~`
150,000 is extruded through a cylindrical noz~le of 0.3 mm. in
diameter and lmm. in length at room temperature under a pressure
of 1 to 10 kg/cm2, the water content of the pullulan spinning
solution is in the range of 30 to 80 wt%, preferably 50 to 70 wt~.
In the spinning according to the present invention, l~
pullulan may be mixed with, in addition tQ water, as a plasti- L
cizer or softener, a polyhydric alcohol such as glycerin, sor-
bitol, maltitol, ethylene glycol, propylene glycol, polyethylene
glycol or polypropylene glycol, or dimethyl sulfoxide.
-- 5 --
~ :, ,s
,~ .

~061068
If necessary, the spinning solution may be subjected,
in order to improve the physical properties of spun fibres and
fabrics obtained therefrom, to mixed-spinning in admixture with
other water-soluble polymer such as polyvinyl alcohol, polyethyl-
eneimine, polyacrylamide, polyacrylic acid, sodium polyacrylate, '
polyvinyl pyrrolidone, polyethylene oxide, sodium alginate, car- .
boxymethyl cellulose or hydroxyethyl cellulose, or an emulsion of
a water-insoluble polymer such as polyvinyl acetate, polyethyl
acrylate, polypropyl acrylate, poly n-butyl acrylate, polymeth-
acrylic acid, polymethyl methacrylate, polypropyl methacrylate,
polybutyl methacrylate, polystyrene, polyvinyl chloride, poly-
vinylidene chloride, polyacrylonitrile or ethylenevinyl acetate
copolymer.
Further, the spinning solution may properly include
inorganic and organic additives which include colorants such as ~.
pigments and dyes; antioxidants such as phenyl-~-naphthylamine,
phenyl-~-naphthylamine, N,N'-diphenyl-p-phenylenediamine, N,N'-
di-~-naphthyl-p-phenylenediamine, N,N'-diaryl-p-phenylenediamine,
N-isopropyl-N'-phenyl-p-phenylenediamine, aldol-~-naphthylamine,
6-ethoxy-2,2,4-trimethyl-1,2-dihydroquinoline, 1,1-bis(4-hydroxy-
phenyl) cyclohexane, 2,6-di-tert-butyl-p-cresol,2,2'-methylene- ,
bis-(4-methyl-6-tert-butylphenol),4,4'-thiobis-(6-tert-butyl-3-
methylphenol),styrenated phenol; ultraviolet light absorbers such
as phenylsalicylate, p-octylphenyl-salicylate, 4-tert-butylphenyl-
salicylate, 2,4-dihydroxybenzophenone, 2-hydroxy-4-methoxybenzo-
phenone, 2,2'-dihydroxy-4-methoxybenzophenone, 2-hydroxy-4-octoxy-
benzophenone, 2-hydroxy-4-methoxy-2'-carboxybenzophenone, 2,2'-
dihydroxy-4,4'-dimethoxy-benzophenone, resorcinol monobenzoate,
2-(2'-hydroxy-5'-methylphenyl)benzotriazole; fillers such as
calcium carbonate, clay, activated calcium fluoride, dolomite, '~`
talc, alumina white, mica powder, aluminum sulfate and barium F
sulfate; and flame retardants such as antimony oxide, antimony
~.
. ~

1061068
silico oxide, tris~ chloroethyl)-phosphate, tris(chloropropyl)
phosphate, tris(dichloropropyl)phosphate, tris(2-bromoethyl)
phosphate, triphenylphosphite, tris(2-chloroethyl)phosphite,
chlorinated paraffin and tetrabromoethane.
Fibers spun according to the present invention may be
stretched in steam at 60 to 120C., whereby they are further
enhanced in strength, Young's modulus and knot strength.
Pullulan fibers are useful in various fields. However,
they have high water solubility, so that it is necessary to control
the degree of water solubility or to insolubilize the pullulan
fibers according to the practical uses thereof. For this
purpose, the pullulan fibers can be insolubilized by crosslinking
with crosslinking agents for hydroxy group containing compounds
including aldehydes such as formaldehyde, acetaldehyde, n-butyl-
aldehyde and glyoxal, various epoxy resins, diisocyanates, and
methylol compounds such as dimethylol ureaand dimethylol ethylene
urea. Alternatively, the pullulan fibers can be insolubilized
by incorporating bichromates into the fibers and then crosslinking
the fibers with light.
It is also possible to insolubilize pullulan fibers by
previously incorporating into the pullulan spinning solution a
mixture comprising a monofunctional monomers such as acrylamide,
acrylic acid, methacrylic acid, 2-hydroxyethyl methacrylate or
N-vinyl pyrrolidone, and a polyfunctional monomers such as
ethylene glycol dimethacrylate and polyethylene glycol dimeth-
acrylate such as diethylene glycol dimethacrylate, triethylene
glycol dimethacrylate, nonaethylene glycol dimethacrylate, or
methylene-bis-acrylamide and an initiator such as hydrogen perox-
ide, ammonium persulfate, potassium persulfate, cerium (IV)
ammonium nitrate, cerium (IV) ammonium sulfate, azobis-isobutyron-

1061068
itrile, t-butyl-peroxide, di-t-butyl peroxide, dicumyl peroxide,
cumen hydroperoxide and t-butyl hydroperoxide, spinning the
resulting mixture to obtain pullulan fibers, and then cross-
linking the fibers by application of heat, light or radiation.
Further, in order to properly control the water solubility of
pullulan fibers, there may be used a modified pullulan prepared
by subjecting the pullulan to esterification, alkyl etherifica-
tion, hydroxyalkyl etherification, carboxyalkyl etherification,
phosphatization, oxidation, reduction or graft-copolymerization
with a vinyl monomer.
Characteristic features of a pullulan fiber obtained
by the spinning process of the present invention are as follows;
(1) The fiber dissolves quite quickly not only in hot water
but also in cold water.
(2) The strength and Young's modulus of a single fiber
have such values that the fiber can successfully be put into
practical use even when it has not been stretched. (refer to
Examples 1 and 2 as hereinafter described).
(3) The surface of the fiber has a beautiful silk-like
gloss.
(4) The fiber is colorless and transparent, and the sur-
face and interior thereof are excellent in dyeability.
(5) The fiber is hydrophilic and moisture-absorptive, so
that it generates no static electricity and thus is antistatic.
(6) The fiber is edible, non-toxic, tasteless and odorless,
and is of course non-irritative to the skin.
(7) Even when burned, the fiber does not generate any such
poisonous gases as nitrogen oxides and chlorides. Further, the
fiber, after use, can be discarded as is, since it spontaneously
decomposes in water and soil, without causing any such problem in
its disposal such as with other waste matter.
In view of such characteristic properties as mentioned
-- 8

106~068
above, pullulan fibers can be put into various uses. For example,
pullulan fibers can be made into paper by subjecting them to
paper-making, either singly or in admixture with wood pulp, hemp
or ramie fibers, using as a dispersant a hydrophilic low mole-
cular weight alcohol such as methanol, ethanol or isopropanol, or
a hydrophilic organic solvent such as acetone which does not
dissolve pullulan. The thus obtained paper is quickly soluble
ln water and excellent in printability, and hence can be used
as paper for secret documents. Further, they are water-soluble,
edible and indigestive, and hence can directly be used as inner
packings for medicines and as small bags for packing seasonings
for instantly-serviceable foodstuffs and for tea powder, coffee,
cocoa and the like foods. Furthermore, they are water-soluble
and non-irritative to the skin, and hence can be used as women's
sanitary cotton, toilet paper and tissue paper.
Alternatively, the pullulan fibers can be used as
binders for non-woven fabrics, taking advantage of their tacki-
ness. When fibers obtained from pullulan which has partly been
water-insolubilized, or pullulan fibers which have partly been
water-insolubilized, are spun either singly or in admixture with
other fibers, the resulting fibers can be used as underwear and
other clothes, taking advantage of the moisture-absorptivity,
antistatic properties and dyeability of the fibers.
The particular method of production of the pullulan
used in the present invention is not critical. At present, it
can be isolated and recovered as a tacky substance secreted in
a culture liquor of a strain belonging to the genus Pullularia
which is an incomplete microorganism. Thus, a strain of the
species Pullularia pullulans is subjected to a shaking culture
(i.e. culture is carried out in a manner in which the container
with the culture liquid is shaken to cause ready mixing of the
culture liquid with air), at 24C for 5 days in a medium contain-
~ _ g_

1~6~068
ing 10% of partially hydrolyzed starch, 0.5% of K2HPO4, 0.1% ofNaCl, 0.02% of MgSO4. 7H2O, 0.06% of (NH4)2SO4 and 0.04% of
yeast extract, whereby
- 9a -

1C~61068
p~llulan is obtained as a tacky subtance secreted from the cells
into the culture liquor. If necessary, the cells are removed by
centrifugation from the culture liquor, and the supernatant is
charged with methanol to deposit a pullulan precipitate. After
repeating water dissolution and methanol precipitation, purified
pullulan can be obtained. Pullulan somewhat varies in physical
properties depending on the kind of strain used. This, however,
is not greatly connected to the properties of pullulan as fiber.
The molecular weight of the pullulan used in the present
invention is not particularly limited, but is preferably in the
range of 10,000 to 5,000,000.
The present invention is illustrated in detail below
with reference to Examples.
Example 1
Pullulan having a molecular weight of about 150,000
was dissolved in water to prepare a s pinning solution containing
40 wt~ of said pullulan. The spinning solution was extruded at
room temperature (23C.) under a pressure of 2 kg/cm2 through a E
cylindrical nozzle of 0.3 mm. in diameter and 1 mrn. in length
into air at room temperature. The fibre from the nozzle was
wound up by means of a winding machine, whereby spun fibres were
obtained while evaporating water from the fibres into air. The
thus obtained fibres were about 20 microns in diameter, and the
unstretched fiber had a tensile strength of 2,520 kg/cm , an
elongation of 20~ and a Young's modulus of 15,000 kg/cm2. When
dipped into water at room temperature, the fiber dissolved there-
in instantaneously.
Example 2
A pullulan fiber spun under the same conditions as in
Example 1 was stretched in steam at 90C. to three times the
original length thereof. The thus stretched pullulan fiber had
a tensile strength of 2,900 kg/cm2, an elongation of 17~, and a
-- 1 0
~,; i

1061068
Young's modulus of 28,000 kg/cm2. When dipped into water at
room temperàture, the fiber dissolved therein instantaneously.
Example 3
Pullulan having a molecular weight of about 200,000 was
adjusted to a water content of 30 wt~ by spraying water thereto.
The pullulan thus treated was extruded at 70C. under a pressure
of 30 kg/cm2 through a cylindrical--nozzle of 0.5 mm. in diameter
and 1 mm. in length into air at room temperature, and the result-
ing fibres were wound up. The fibres were about 30 microns in
diameter, and the unstretched fiber had a tensile strength of
2,610 kg/cm2, an elongation of 18%, and a Young's modulus of -
16,500 kg/cm2. When dipped into water at room temperature, the
fiber dissolved therein instantaneously.
!
~.
~h
F
, ",

Dessin représentatif

Désolé, le dessin représentatif concernant le document de brevet no 1061068 est introuvable.

États administratifs

2024-08-01 : Dans le cadre de la transition vers les Brevets de nouvelle génération (BNG), la base de données sur les brevets canadiens (BDBC) contient désormais un Historique d'événement plus détaillé, qui reproduit le Journal des événements de notre nouvelle solution interne.

Veuillez noter que les événements débutant par « Inactive : » se réfèrent à des événements qui ne sont plus utilisés dans notre nouvelle solution interne.

Pour une meilleure compréhension de l'état de la demande ou brevet qui figure sur cette page, la rubrique Mise en garde , et les descriptions de Brevet , Historique d'événement , Taxes périodiques et Historique des paiements devraient être consultées.

Historique d'événement

Description Date
Inactive : CIB de MCD 2006-03-11
Inactive : Périmé (brevet sous l'ancienne loi) date de péremption possible la plus tardive 1996-08-28
Accordé par délivrance 1979-08-28

Historique d'abandonnement

Il n'y a pas d'historique d'abandonnement

Titulaires au dossier

Les titulaires actuels et antérieures au dossier sont affichés en ordre alphabétique.

Titulaires actuels au dossier
SUMITOMO CHEMICAL COMPANY
HAYASHIBARA BIOCHEMICAL LABORATORIES
Titulaires antérieures au dossier
FUMIO FUJITA
KOZO TSUJI
NOBUHIRO TOYOTA
SEIZO NAKASHIO
TATSUO NOMURA
Les propriétaires antérieurs qui ne figurent pas dans la liste des « Propriétaires au dossier » apparaîtront dans d'autres documents au dossier.
Documents

Pour visionner les fichiers sélectionnés, entrer le code reCAPTCHA :



Pour visualiser une image, cliquer sur un lien dans la colonne description du document. Pour télécharger l'image (les images), cliquer l'une ou plusieurs cases à cocher dans la première colonne et ensuite cliquer sur le bouton "Télécharger sélection en format PDF (archive Zip)" ou le bouton "Télécharger sélection (en un fichier PDF fusionné)".

Liste des documents de brevet publiés et non publiés sur la BDBC .

Si vous avez des difficultés à accéder au contenu, veuillez communiquer avec le Centre de services à la clientèle au 1-866-997-1936, ou envoyer un courriel au Centre de service à la clientèle de l'OPIC.


Description du
Document 
Date
(aaaa-mm-jj) 
Nombre de pages   Taille de l'image (Ko) 
Abrégé 1994-04-26 1 8
Revendications 1994-04-26 3 83
Page couverture 1994-04-26 1 16
Dessins 1994-04-26 1 5
Description 1994-04-26 12 422