DK1999157T3 - Fremgangsmåde til kogning af et stivelsesholdigt materiale med et højt tørstofindhold til fremstilling af en klæbende sammensætning - Google Patents
Fremgangsmåde til kogning af et stivelsesholdigt materiale med et højt tørstofindhold til fremstilling af en klæbende sammensætning Download PDFInfo
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- DK1999157T3 DK1999157T3 DK07731156.1T DK07731156T DK1999157T3 DK 1999157 T3 DK1999157 T3 DK 1999157T3 DK 07731156 T DK07731156 T DK 07731156T DK 1999157 T3 DK1999157 T3 DK 1999157T3
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- starch
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- 229920000856 Amylose Polymers 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
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- SOQBVABWOPYFQZ-UHFFFAOYSA-N oxygen(2-);titanium(4+) Chemical class [O-2].[O-2].[Ti+4] SOQBVABWOPYFQZ-UHFFFAOYSA-N 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
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Classifications
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J103/00—Adhesives based on starch, amylose or amylopectin or on their derivatives or degradation products
- C09J103/02—Starch; Degradation products thereof, e.g. dextrin
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
- C08B30/12—Degraded, destructured or non-chemically modified starch, e.g. mechanically, enzymatically or by irradiation; Bleaching of starch
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
- C08B30/12—Degraded, destructured or non-chemically modified starch, e.g. mechanically, enzymatically or by irradiation; Bleaching of starch
- C08B30/16—Apparatus therefor
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/28—Starch
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/10—Coatings without pigments
- D21H19/12—Coatings without pigments applied as a solution using water as the only solvent, e.g. in the presence of acid or alkaline compounds
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/36—Coatings with pigments
- D21H19/44—Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
- D21H19/54—Starch
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Grain Derivatives (AREA)
- Paints Or Removers (AREA)
Claims (20)
1. Fremgangsmåde til kogning afen stivelsesholdig sammensætning, hvilken fremgangsmåde omfatter: (a) et første trin, der omfatter blanding af mindst ét stivelsespulver med et vandigt stivelsesholdigt fluidum, der indeholder granuleret stivelse og/eller gelatineret stivelse, idet indholdet af stivelse i det vandige stivelsesholdige fluidum og blandingsforholdet mellem stivelsespulveret og det vandige stivelsesholdige fluidum er således, at det samlede indhold af stivelse i den opnåede blanding bliver større end 45 vægt-%, fortrinsvis mellem 50 og 82 vægt-% og navnlig mellem 52 vægt-% og 75 vægt-%, og idet det første trin udføres ved atmosfærisk tryk under omrøring i et kogekammer, der holdes ved en temperatur, som i det mindste er den samme som den højeste gelatineringstemperatur (TG) for alle de stivelser, der forefindes i blandingen, i et tidsrum på mellem 3 minutter og 2 timer, og (b) et andet trin, der omfatter opvarmning af den i trin (a) opnåede kolloide stivelsesopløsning ved et højere tryk end det atmosfæriske tryk og ved en temperatur på mellem 120 °C og 180 °C, fortrinsvis mellem 140 °C og 180° C, i et tidsrum på mellem 15 sekunder og 30 minutter.
2. Fremgangsmåde ifølge krav 1, kendetegnet ved, at det første trin (trin (a)) udføres ved en temperatur, der i det mindste er 5 °C og fortrinsvis i det mindste 10 °C højere end den højeste gelatineringstemperatur for alle de stivelser, der forefindes i blandingen.
3. Fremgangsmåde ifølge krav 1 eller 2, kendetegnet ved, at det første trin har en varighed på mellem 3 minutter og 2 timer, fortrinsvis mellem 5 minutter og 1 time og navnlig mellem 10 og 30 minutter.
4. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at opvarmningen i trin (b) har en tilstrækkelig varighed til at opnå stivelsesopløsninger, der i det væsentlige er frie for granuleret stivelse.
5. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at opvarmningen i trin (b) har en tilstrækkelig varighed til at opnå stivelsesopløsninger med en Brookfield-viskositet, målt ved 25 °C, på mindre end 6000 centipoise, fortrinsvis mindre end 5000 centipoise og navnlig mindre end 4000 centipoise.
6. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at opvarmningen i trin (b) har en varighed på mellem 15 sekunder og 30 minutter, fortrinsvis mellem 20 sekunder og 15 minutter og navnlig mellem 30 sekunder og 10 minutter.
7. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at opvarmningen i trin (b) finder sted ved indsprøjtning af vanddamp undertryk i den kolloide stivelsesopløsning, der opnås ved udgangen af trin (a).
8. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at det vandige stivelsesholdige fluidum, inden det indføres i kogekammeret som angivet i trin (a), opvarmes til en temperatur på mellem 100 °C og 180 °C.
9. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at det stivelsespulver, der indføres i kogekammeret som angivet i trin (a), har et fugtighedsindhold på mindre end 50 %, fortrinsvis mellem 3 og 30 % og navnlig mellem 7 og 22 %.
10. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at det vandige stivelsesholdige fluidum er en stivelsesmælk med et tørstofindhold på mindre end 52 vægt-%, fortrinsvis mellem 20 og 50 vægt-% og navnlig mellem 30 og 45 vægt-%.
11. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 8, kendetegnet ved, at det vandige stivelsesholdige fluidum er en kolloid stivelsesopløsning med et indhold af stivelse på mindre end 75 vægt-%, fortrinsvis mellem 35 og 70 vægt-% og navnlig mellem 38 og 65 vægt-%.
12. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at stivelsespulveret og stivelsen i det vandige stivelsesholdige fluidum uafhængigt er valgt blandt stivelse fra rodknolde, kornstivelse og stivelse fra bælgplanter, eventuelt modificerede.
13. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at stivelsespulveret og stivelsen i det vandige stivelsesholdige fluidum har den samme oprindelse.
14. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, kendetegnet ved, at en del af den stivelsesopløsning, der opnås ved udgangen af trin (b), recirkuleres til trin (a) for at tjene som vandigt stivelsesholdigt fluidum.
15. Sammensætning af stivelse, som kan opnås ved anvendelse afen fremgangsmåde ifølge et hvilket som helst af kravene 1 til 14.
16. Sammensætning af stivelse ifølge krav 15, kendetegnet ved, at den har et samlet indhold af stivelse på mindre end 75 vægt-%, fortrinsvis mellem 35 og 70 vægt-% og navnlig mellem 38 og 65 vægt-%.
17. Sammensætning af stivelse ifølge krav 15 eller 16, kendetegnet ved, at den har en Brookfield-viskositet, målt ved 25 °C, på mindre end 6000 centipoise, fortrinsvis mindre end 5000 centipoise og navnlig mindre end 4000 centipoise.
18. Sammensætning af stivelse ifølge et hvilket som helst af kravene 15 til 17, kendetegnet ved, at den i det væsentlige er fri for granuleret stivelse.
19. Anvendelse af en sammensætning ifølge et hvilket som helst af kravene 15 til 18 til færdigbehandling af cellulosematerialer, fortrinsvis papir og kartonark, fortrinsvis til fladebearbejdning, pigmenteret fladebearbejdning og coating af førnævnte materialer.
20. Anvendelse af en sammensætning ifølge et hvilket som helst af kravene 15 til 18 til limning, navnlig limning af celluloseholdige materialer, fortrinsvis bølgepap.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0602451A FR2898897B1 (fr) | 2006-03-21 | 2006-03-21 | Nouveaux procede et dispositif de cuisson d'une matiere amylacee a hautes matieres seches pour la preparation d'une composition adhesive |
| PCT/FR2007/000465 WO2007107648A1 (fr) | 2006-03-21 | 2007-03-19 | Procede de cuisson d'une matiere amylacee a hautes matieres seches pour la preparation d'une composition adhesive |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DK1999157T3 true DK1999157T3 (da) | 2017-03-20 |
Family
ID=37432239
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DK07731156.1T DK1999157T3 (da) | 2006-03-21 | 2007-03-19 | Fremgangsmåde til kogning af et stivelsesholdigt materiale med et højt tørstofindhold til fremstilling af en klæbende sammensætning |
Country Status (16)
| Country | Link |
|---|---|
| US (1) | US20100159104A1 (da) |
| EP (1) | EP1999157B1 (da) |
| JP (1) | JP2009530467A (da) |
| KR (1) | KR20080110639A (da) |
| CN (1) | CN101405302A (da) |
| CA (1) | CA2648016A1 (da) |
| DK (1) | DK1999157T3 (da) |
| ES (1) | ES2618362T3 (da) |
| FR (1) | FR2898897B1 (da) |
| LT (1) | LT1999157T (da) |
| MX (1) | MX2008011920A (da) |
| NO (1) | NO20084150L (da) |
| PL (1) | PL1999157T3 (da) |
| PT (1) | PT1999157T (da) |
| RU (1) | RU2434883C2 (da) |
| WO (1) | WO2007107648A1 (da) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2923832B1 (fr) | 2007-11-20 | 2011-01-07 | Roquette Freres | Composition anionique aqueuse contenant au moins un amidon anionique gelatinise, soluble et, de preference, un amidon anionique insoluble, non gelatinise ou partiellement gonfle. |
| CA2746484C (en) * | 2008-12-10 | 2017-03-14 | Cargill, Incorporated | Process using hydrocyclones |
| CN102933605B (zh) * | 2010-04-07 | 2017-10-13 | 卡吉尔公司 | 改性淀粉的方法 |
| SE536606C2 (sv) | 2012-06-26 | 2014-03-25 | Förfarande för framställning av en bestrykningssmet innehållande en starkt koncentrerad stärkelselösning för bestrykningav papper och kartong | |
| EP2719826A1 (en) * | 2012-10-09 | 2014-04-16 | Metso Paper Inc. | Process for producing a fiber web and arrangement for producing a fiber web |
| DE102012110282A1 (de) * | 2012-10-26 | 2014-04-30 | Bvg Bauer Verfahrenstechnik Gmbh | Vorrichtung und Verfahren zur Vermeidung von Abwasser bei kontinuierlichen enzymatischen Stärke-Abbauanlagen |
| KR101420371B1 (ko) * | 2013-12-26 | 2014-07-16 | 박종헌 | 골판지용 접착제 제조 시스템 및 제조 방법 |
| CN105801715B (zh) * | 2016-04-11 | 2018-07-27 | 海南金海浆纸业有限公司 | 一种淀粉蒸煮装置及其蒸煮淀粉的工艺 |
| EP3296666A1 (de) * | 2016-09-14 | 2018-03-21 | Siemens Aktiengesellschaft | Aufbereitung von stärke für eine hydrophobierung von papier |
| AT16656U3 (de) * | 2018-10-08 | 2020-07-15 | Pga Putz Granitzer Anlagenbau Ges M B H | Verfahren und Vorrichtung zum Aufschluss von Stärke |
| EP3921345A1 (en) * | 2019-02-08 | 2021-12-15 | Kemira Oyj | Method for dissolving starch |
| CN109619378B (zh) * | 2019-02-21 | 2022-06-21 | 桂林市顶寅食品有限责任公司 | 一种防止米粉粘连的方法 |
| KR102667489B1 (ko) * | 2021-12-09 | 2024-05-22 | 대상 주식회사 | 성형탄용 바인더, 이의 제조방법 및 이의 용도 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2593186B1 (fr) * | 1986-01-17 | 1988-01-22 | Roquette Freres | Procede de fabrication d'adhesifs a base d'amidon pour carton ondule |
| US5181959A (en) * | 1988-12-28 | 1993-01-26 | Honshu Paper Co., Ltd. | High-concentration starch adhesive |
| JPH05320597A (ja) * | 1991-04-09 | 1993-12-03 | Honshu Paper Co Ltd | 耐水性高濃度澱粉接着剤 |
| US5340405A (en) * | 1993-06-14 | 1994-08-23 | National Starch And Chemical Investment Holding Corporation | High solids liquid starch prepared by batch cooking |
| RU2280060C2 (ru) * | 2002-01-30 | 2006-07-20 | Тейт энд Лиль Юроп Н.В. | Клеи stein hall с высоким содержанием сухого вещества и способ получения клеев stein hall с высоким содержанием сухого вещества |
-
2006
- 2006-03-21 FR FR0602451A patent/FR2898897B1/fr not_active Expired - Fee Related
-
2007
- 2007-03-19 KR KR1020087025758A patent/KR20080110639A/ko not_active Withdrawn
- 2007-03-19 ES ES07731156.1T patent/ES2618362T3/es active Active
- 2007-03-19 MX MX2008011920A patent/MX2008011920A/es unknown
- 2007-03-19 RU RU2008141684/13A patent/RU2434883C2/ru not_active IP Right Cessation
- 2007-03-19 US US12/293,549 patent/US20100159104A1/en not_active Abandoned
- 2007-03-19 DK DK07731156.1T patent/DK1999157T3/da active
- 2007-03-19 CN CNA2007800101763A patent/CN101405302A/zh active Pending
- 2007-03-19 JP JP2009500888A patent/JP2009530467A/ja not_active Withdrawn
- 2007-03-19 PT PT77311561T patent/PT1999157T/pt unknown
- 2007-03-19 LT LTEP07731156.1T patent/LT1999157T/lt unknown
- 2007-03-19 CA CA002648016A patent/CA2648016A1/fr not_active Abandoned
- 2007-03-19 WO PCT/FR2007/000465 patent/WO2007107648A1/fr not_active Ceased
- 2007-03-19 PL PL07731156T patent/PL1999157T3/pl unknown
- 2007-03-19 EP EP07731156.1A patent/EP1999157B1/fr not_active Not-in-force
-
2008
- 2008-10-02 NO NO20084150A patent/NO20084150L/no not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| CN101405302A (zh) | 2009-04-08 |
| PT1999157T (pt) | 2017-03-16 |
| PL1999157T3 (pl) | 2017-06-30 |
| RU2008141684A (ru) | 2010-04-27 |
| EP1999157B1 (fr) | 2016-12-14 |
| JP2009530467A (ja) | 2009-08-27 |
| NO20084150L (no) | 2008-10-02 |
| CA2648016A1 (fr) | 2007-09-27 |
| EP1999157A1 (fr) | 2008-12-10 |
| MX2008011920A (es) | 2008-11-14 |
| ES2618362T3 (es) | 2017-06-21 |
| KR20080110639A (ko) | 2008-12-18 |
| LT1999157T (lt) | 2017-06-26 |
| WO2007107648A1 (fr) | 2007-09-27 |
| RU2434883C2 (ru) | 2011-11-27 |
| US20100159104A1 (en) | 2010-06-24 |
| FR2898897B1 (fr) | 2012-06-15 |
| FR2898897A1 (fr) | 2007-09-28 |
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