Natural water-insoluble encapsulation composition and process for preparing the same 机翻标题: 暂无翻译,请尝试点击翻译按钮。

源语言标题
(JP5744955) 天然​の​水−不溶性​カプセル​化​組成​物​及び​その​製造​法
公开号/公开日
JP5744955 B2 2015-07-08 [JP5744955]JP2013144714 A 2013-07-25 [JP2013144714] / 2015-07-082013-07-25
申请号/申请日
2013JP-0082858 / 2013-04-11
发明人
HUYNH KIM UYEN;CORMIER FRANCOIS;
申请人
COLAROME;
主分类号
IPC分类号
A23L-005/40A23L-005/41A61K-009/52A61K-047/42A61Q-090/00
摘要
(JP5744955) PROBLEM TO BE SOLVED: To provide an encapsulation composition and a process in which a material to be capsulated is encapsulated in a natural water-insoluble matrix.SOLUTION: The invention relates to a dry particulate encapsulation composition containing a water-insoluble matrix comprising at least 70 wt.% of proteins, based on the total weight of the matrix and a moisture content of about 5 to 10 wt.%, based on the total weight of the matrix and an encapsulate encapsulated in the matrix, wherein the matrix once wetted in a clear colorless aqueous solution or in mineral oil has a lightness value (L*) greater than about 40, a color vividness or chroma (C*) lower than about 33 and a hue angle between about 70° and 90°.  The encapsulation compositions are useful in encapsulating dyes, medications and vitamins.  Fine particulate encapsulation compositions comprising natural dyes can be used in lieu of artificial lakes in confectionery, cosmetics and caplets color coatings.
机翻摘要
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地址
代理人
代理机构
;
优先权号
2004US-60637730 2004-12-22
主权利要求
(JP5744955)  Claims machine translated from Japanese 1. The substance which is encapsulated inside the water insoluble plant protein concentrated matrix is included, being manufacturing method of dry particle condition extrusive ones, below: (i) The particular substance, the water insoluble plant protein concentrated blend, and the water are mixed in the extrusion molding machine;   (ii) (i) The blend, offering to the melting extrusion which in order to designate browning where the particular water insoluble plant protein concentrated matrix due to the May lard reaction is not desirable as minimum is done with low temperature and high humidity;   (iii) The particular extrusive blend, with gross weight standard of the dry extrusive blend the 5-10 weight % is dried to moisture content, in order to become grain size under 150 .micro.m with that, the extrusive blend which is the fragment which it dries pulverizes is produced;  And (iv) Pulverizing the particular dry extrusive blend, form particular particle condition extrusive ones Implication, Here, the water insoluble plant protein concentrated matrix in aforementioned dry particle condition extrusive ones with gross weight standard of the matrix, includes the plant protein which at least 70 weight % extrusion it is organized is converted, method. 2. The aforementioned water insoluble plant protein concentrated matrix, is the American protein concentrate, method of claim 1 statement. 3. The aforementioned American protein concentrate, with dry weight standard of the American protein concentrate, 77 weight % has the American protein mass which it exceeds, method of claim 2 statement. 4. The aforementioned extrusion, with the American protein concentrate and gross weight standard of the water, the 30-50 weight % is done at water content, claim method of 2 or 3 statements. 5. The aforementioned water insoluble plant protein concentrated blend, is soybean protein isolated ones, method of claim 1 statement. 6. Aforementioned soybean protein isolated ones, with dry standard of soybean protein isolated ones, 87 weight % have the soybean protein mass which it exceeds, method of claim 5 statement. 7. The aforementioned extrusion, the soybean protein densely with isolated ones and gross weight standard of the water, the 45-70 weight % is done at water content, claim method of 5 or 6 statements. 8. Temperature of the extrusion molding machine which does the aforementioned extrusion, is set to the 10.deg.C-35.deg.C, either of the claim 1-7 method of 1 section statements. 9. Aforementioned dry extrusive ones, are pulverized to the fine powder end when the particle has the average size under 150 .micro.m, under 50 .micro.m, under 20 .micro.m or under 10 .micro.m, either of the claim 1-8 method of 1 section statements. 10. The twin screw extrusion molding machine is used for the aforementioned extrusion, either of the claim 1-9 method of 1 section statements. 11. The substance where the description above is encapsulated, is the unstable substance, either of the claim 1-10 method of 1 section statements. 12. The aforementioned unstable substance is the thermal sensitivity substance, method of claim 11 statement. 13. The aforementioned unstable substance is the optical sensitivity substance, method of claim 11 statement. 14. The aforementioned substance is the colorant, either of the claim 1-13 method of 1 section statements. 15. The aforementioned substance, the natural pigment, nature rake of the pigment, the artificial pigment and the natural pigment which are equal, the synthetic pigment, is synthetic rake, or those combinations, method of claim 14 statement. 16. The aforementioned natural pigment, anthraquinone and the betta line, the caramel, the carotenoid, [kurukuminoido], the flavin, flavonol, porphyrin, [geniposhido] and the sandal wood, is sepia or vegetable black, method of claim 15 statement. 17. (A) The aforementioned flavonol, the red cabbage and the sweet potato, red or the [bu], the truth of [niwatoko] and at least from one of the groups which consist of the grape obtaining;   (B) The aforementioned betta line is the beat lead-lead;   (C) The aforementioned anthraquinone, is carmine acid or the carmine;   (D) The aforementioned carotenoid, the un nut, is [apokarotenaru], [apokarotenaruesuteru], [kantakisanchin], ***.beta.-karochin, the lycopene, the lutein, the paprika or the saffron;   (E) The aforementioned porphyrin, is the chlorophyll or the chlorphyllin;   (F) Aforementioned [kurukuminoido] is [tameritsuku];   (G) The aforementioned flavin is the riboflavin, Method of claim 16 statement. 18. The substance where the description above is encapsulated is the medicine or the vitamin, either of the claim 1-13 method of 1 section statements. 19. Dry particle condition extrusive ones which are produced either of the claim 1-18 by the method of 1 section statements. 20. Being dry particle condition extrusive ones which include the unstable substance which is encapsulated inside the water insoluble plant protein concentrated matrix, the plant protein which the aforementioned matrix, pushes out with gross weight standard of the matrix and is organized is converted at least 70 weight %, and with gross weight standard of the matrix the 5-10 weight % implication moisture content, When aforementioned dry particle condition extrusive ones, are produced by the melting extrusion which in order to designate browning where the aforementioned matrix due to the May lard reaction is not desirable as minimum is done with low temperature and high humidity, get wet to the transparent colorless aqueous solution or the mineral oil once with that, 40 super lightness (L*), color visibility or chroma under 33 (C*), and the matrix which possesses the hue angle of the 70.deg.-90.deg. is produced, dry particle condition extrusive ones. 21. The aforementioned matrix pushes out and includes, the American protein which it is organized is converted 70 weight % at least, dry particle condition extrusive ones of claim 20 statement. 22. The aforementioned matrix, with dry weight standard of the American protein concentrate, 77 weight % is produced from the melting extrusion of the American protein concentrate which possesses super American protein content, dry particle condition extrusive ones of claim 21 statement. 23. The aforementioned matrix pushes out and includes, the soybean protein which it is organized is converted 70 weight % at least, dry particle condition extrusive ones of claim 20 statement. 24. The aforementioned matrix, with dry weight standard of the soybean protein concentrate, 87 weight % is produced from the melting extrusion of soybean protein isolated ones which possess super soybean protein content, dry particle condition extrusive ones of claim 23 statement. 25. Temperature of the extrusion molding machine which does the aforementioned melting extrusion, is set to the temperature of the 10.deg.C-35.deg.C, either of the claim 20-24 dry particle condition extrusive ones of 1 section statements. 26. Aforementioned extrusive ones, include the particle which possesses the average size under 150 .micro.m, under 50 .micro.m, under 20 .micro.m or under 10 .micro.m, either of the claim 20-25 dry particle condition extrusive ones of 1 section statements. 27. The aforementioned unstable substance is the thermal sensitivity substance, either of the claim 20-26 dry particle condition extrusive ones of 1 section statements. 28. The aforementioned unstable substance is the optical sensitivity substance, either of the claim 20-26 dry particle condition extrusive ones of 1 section statements. 29. The aforementioned unstable substance is the colorant, either of the claim 20-28 dry particle condition extrusive ones of 1 section statements. 30. The aforementioned substance, the natural pigment, nature rake of the pigment, the artificial pigment and the natural pigment which are equal, the synthetic pigment, is synthetic rake, or those combinations, dry particle condition extrusive ones of claim 29 statement. 31. The aforementioned natural pigment, anthraquinone and the betta line, the caramel, the carotenoid, [kurukuminoido], the flavin, flavonol, porphyrin, [geniposhido] and the sandal wood, is sepia or vegetable black, dry particle condition extrusive ones of claim 30 statement. 32. (A) The aforementioned flavonol, the red cabbage and the sweet potato, red or the [bu], at least from one of the groups which consist of the truth or the grape of [niwatoko] obtaining;   (B) The aforementioned betta line is the beat lead-lead;   (C) The aforementioned anthraquinone, is carmine acid or the carmine;   (D) The aforementioned carotenoid, the un nut, is [apokarotenaru], [apokarotenaruesuteru], [kantakisanchin], ***.beta.-karochin, the lycopene, the lutein, the paprika or the saffron;   (E) The aforementioned porphyrin, is the chlorophyll or the chlorphyllin;   (F) Aforementioned [kurukuminoido] is [tameritsuku];   (G) The aforementioned flavin is the riboflavin, Dry particle condition extrusive ones of claim 31 statement. 33. The aforementioned colorant, the 5-15 weight % has the density of the range with the entire dry weight standard of aforementioned extrusive ones, either of the claim 29-31 dry particle condition extrusive ones of 1 section statements. 34. The unstable substance where the description above is encapsulated is the medicine or the vitamin, either of the claim 20-28 dry particle condition extrusive ones of 1 section statements. 35. The wax, the oil, the gum and the zein, coating it is done with the emulsifier or those blends, either of the claim 20-34 dry particle condition extrusive ones of 1 section statements. 36. (A) Organic acid or inorganic acid, tannin acid and [asukorubin] acid, calcium salt, zein, emulsifier, gum or those blends;   (B) ***.alpha.-tokohueroru, [asukorubin] acid, benzoic acid, [isoasukorubin] acid, butyl conversion hydroxy anisole and butyl conversion hydroxy toluene, the sodium citrate, sorbic acid and the kalium, heavily it is the sodium sulfate or those blends, the stabilizer or retention medicine;  And/or (C) The wax, the oil and the fat, the long chain fatty acid, the acacia, the gelatin, the lecithin, cholesterol, the sulfate or the sulfonate, the gum and the zein or they are those blends, fault - polarity coating Furthermore it includes, claim 20-35 in each case dry particle condition extrusive ones of 1 section statements. 37. The aluminum it is not included, either of the claim 20-36 dry particle condition extrusive ones of 1 section statements. 38. When aforementioned extrusive ones are dispersed in the aqueous solution, the aforementioned matrix, keeps discharges the aforementioned substance completely, or discharges completely, or or one part, either of the claim 20-37 dry particle condition extrusive ones of 1 section statements. 39. Being the method of encapsulating the thermal sensitivity colorant inside the water insoluble plant protein concentrated matrix, (i) In extrusive formation machine, The aforementioned colorant, Pro-Fam the water insoluble plant protein concentrated blend which is chosen from Remypro N80+ which is 974 which is soybean protein isolated ones, and the American protein concentrate, and Water It mixes;   (ii) In the melting extrusion which in order to designate browning where the aforementioned water insoluble plant protein concentrated matrix is not desirable with the May lard reaction as minimum is done with low temperature and high humidity offering the blend (i);   (iii) The 5-10 weight % it pushes out to moisture content with gross weight standard of the dry extrusive blend and dries the blend, in order to become grain size under 150 .micro.m with that, it produces the extrusive blend which is the fragment which it dries pulverizes;  And, (iv) Pulverizing aforementioned dry extrusive ones, form dry particle condition extrusive ones Implication, Here, the aforementioned water insoluble plant protein concentrated matrix in aforementioned dry particle condition extrusive ones includes the plant protein which at least 70 weight % extrusion it is organized is converted with gross weight standard of the aforementioned matrix, method. 40. Being the dry particle condition encapsulation composition, below: With the soybean or the American protein, and the gross weight standard of the matrix which include the thermal sensitivity colorant which is encapsulated inside the water insoluble plant protein concentrated matrix, as for the particular matrix, with gross weight standard of the matrix 70 weight % extrusion it is organized are converted at least the 5-10 weight % implication the moisture, When here, particular dry particle condition extrusive ones are produced by the melting extrusion which in order to designate browning where the particular matrix due to the May lard reaction is not desirable as minimum is done with low temperature and high humidity, get wet to the transparent colorless aqueous solution or the mineral oil once with that, 40 super lightness (L*), color visibility or chroma under 33 (C*), and the matrix which possesses the hue angle of the 70.deg.-90.deg. is produced, the composition.
法律状态
(JP5744955) LEGAL DETAILS FOR JP2013144714  Actual or expected expiration date=2025-12-06    Legal state=ALIVE    Status=GRANTED     Event publication date=2013-04-11  Event code=JP/APP  Event indicator=Pos  Event type=Examination events  Application details  Application country=JP JP2013082858  Application date=2013-04-11  Standardized application number=2013JP-0082858     Event publication date=2013-04-25  Event code=JP/A621  Event indicator=Pos  Event type=Examination events  Written request for application examination  Effective date of the event=2013-04-24  JAPANESE INTERMEDIATE CODE: A621     Event publication date=2013-04-25  Event code=JP/A521  Event type=Restitution or restoration  Written amendment  Effective date of the event=2013-04-24  JAPANESE INTERMEDIATE CODE: A523     Event publication date=2013-07-25  Event code=JP/A  Event indicator=Pos  Event type=Examination events  Published application  Publication country=JP  Publication number=JP2013144714  Publication stage Code=A  Publication date=2013-07-25  Standardized publication number=JP2013144714     Event publication date=2014-03-15  Event code=JP/A521  Event type=Restitution or restoration  Written amendment  Effective date of the event=2014-03-14  JAPANESE INTERMEDIATE CODE: A523     Event publication date=2014-03-19  Event code=JP/A131  Event indicator=Neg  Event type=Examination events  Notification of reasons for refusal  Effective date of the event=2014-03-18  JAPANESE INTERMEDIATE CODE: A131     Event publication date=2014-03-25  Event code=JP/A977  Event type=Examination events  Report on retrieval  Effective date of the event=2014-03-20  JAPANESE INTERMEDIATE CODE: A971007     Event publication date=2014-04-10  Event code=JP/AA91  Event indicator=Neg  Event type=Event indicating Not In Force  Notification of revocation by ex officio  Effective date of the event=2014-04-08  JAPANESE INTERMEDIATE CODE: A971091     Event publication date=2014-05-14  Event code=JP/A131  Event indicator=Neg  Event type=Examination events  Notification of reasons for refusal  Effective date of the event=2014-05-13  JAPANESE INTERMEDIATE CODE: A131     Event publication date=2014-08-12  Event code=JP/A601  Event type=Examination events  Written request for extension of term  Effective date of the event=2014-08-11  JAPANESE INTERMEDIATE CODE: A601     Event publication date=2014-08-15  Event code=JP/A602  Event type=Examination events  Written permission of extension of term  Effective date of the event=2014-08-14  JAPANESE INTERMEDIATE CODE: A602     Event publication date=2014-09-13  Event code=JP/A521  Event type=Restitution or restoration  Written amendment  Effective date of the event=2014-09-12  JAPANESE INTERMEDIATE CODE: A523     Event publication date=2015-03-24  Event code=JP/TRDD  Event indicator=Pos  Event type=Administrative notifications  Trial decision date    Event publication date=2015-04-01  Event code=JP/A01  Event indicator=Pos  Event type=Event indicating In Force  Written decision to grant a patent or to grant a registration (utility model)  Effective date of the event=2015-03-31  JAPANESE INTERMEDIATE CODE: A01     Event publication date=2015-05-07  Event code=JP/A61  Event indicator=Pos  Event type=Event indicating In Force  First payment of annual fees (during grant procedure)  Effective date of the event=2015-04-30  JAPANESE INTERMEDIATE CODE: A61     Event publication date=2015-05-15  Event code=JP/R150  Event indicator=Pos  Event type=Event indicating In Force   Certificate of patent (=grant) or registration of utility model JAPANESE INTERMEDIATE CODE: R150     Event publication date=2015-07-08  Event code=JP/B2  Event indicator=Pos  Event type=Event indicating In Force  Published granted patent (Second level)  from 01-03-1996 onwards (Published examined patent application (Second level) 1971-1996)  Publication country=JP  Publication number=JP5744955  Publication stage Code=B2  Publication date=2015-07-08  Standardized publication number=JP5744955
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