EP0508543B1 - Structuration chimique de pâtes tensio-actives pour former des granulés tensio-actifs avec haute activité - Google Patents
Structuration chimique de pâtes tensio-actives pour former des granulés tensio-actifs avec haute activité Download PDFInfo
- Publication number
- EP0508543B1 EP0508543B1 EP92200994A EP92200994A EP0508543B1 EP 0508543 B1 EP0508543 B1 EP 0508543B1 EP 92200994 A EP92200994 A EP 92200994A EP 92200994 A EP92200994 A EP 92200994A EP 0508543 B1 EP0508543 B1 EP 0508543B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- paste
- surfactant
- extruder
- process according
- alkyl
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions
- C11D11/0082—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions
- C11D11/04—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions by chemical means, e.g. by sulfonating in the presence of other compounding ingredients followed by neutralising
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
- C11D17/06—Powder; Flakes; Free-flowing mixtures; Sheets
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
- C11D17/06—Powder; Flakes; Free-flowing mixtures; Sheets
- C11D17/065—High-density particulate detergent compositions
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Detergent Compositions (AREA)
Claims (7)
- Procédé de préparation d'une composition détergente granulaire, comprenant les étapes suivantes:(i) on neutralise un ou des acides tensioactifs anioniques dans un excès de matière alcaline pour obtenir une pâte tensioactive qui comprend au moins 40 % en poids d'agent tensioactif anionique, ladite pâte ayant une viscosité d'au moins 10 Pa.s lorsqu'elle est mesurée à 70°C et à un taux de cisaillement de 25 s-1 de telle sorte que la pâte tensioactive reste pompable à des températures auxquelles l'agent tensioactif est stable;(ii) on conditionne ladite pâte; et ensuite(iii) on granule ladite pâte dans un mélangeur/granulateur à haut taux de cisaillement après mélange avec une poudre détergente sèche;caractérisé en ce que ladite étape de conditionnement (ii) est effectuée en ajoutant des structurants chimiques à ladite pâte, élevant de la sorte la viscosité apparente de ladite pâte,
et caractérisé par ailleurs en ce que ladite pâte est maintenue à une température d'au moins 20°C, mais à l'exclusion de 20°C, tout au long de l'étape de granulation (iii). - Procédé selon la revendication 1, dans lequel ledit structurant chimique est sélectionné dans le groupe comprenant l'hydroxyde de sodium en solution aqueuse, l'hydroxyde de potassium en solution aqueuse, le chlorure de sodium, les phosphonates, les silicates, la silice, l'amidon, des polymères et des copolymères, des agents tensioactifs non ioniques, l'urée et leurs mélanges.
- Procédé selon l'une quelconque des revendications 1 et 2, caractérisé en ce que ledit structurant chimique se présente sous la forme de poudre et est sélectionné dans le groupe comprenant les phosphonates, les silicates, la silice, les copolymères d'acide maléique et d'acide acrylique.
- Procédé selon l'une quelconque des revendications 2 et 3, caractérisé en ce que ladite étape de conditionnement est réalisée au moyen d'une extrudeuse, ladite extrudeuse ayant un ou plusieurs orifices d'entrée dans le cylindre de l'extrudeuse pour permettre l'addition de poudres et/ou de pâtes supplémentaires qui sont mélangées dans l'extrudeuse.
- Procédé selon la revendication 4, caractérisé en ce que la pâte pénètre dans l'orifice d'entrée de l'extrudeuse à une température comprise entre 40 et 80°C et sous un vide de 0 à 7,3 kPa en dessous de la pression atmosphérique.
- Procédé selon l'une quelconque des revendications 4 et 5, caractérisé en ce que le cylindre de la section de mélange de l'extrudeuse est refroidi par n'importe quels moyens appropriés, notamment par addition d'une quantité allant jusqu'à 30 %, en poids de la pâte, d'anhydride carbonique solide ou d'azote liquide directement dans le cylindre de l'extrudeuse, pourvu que ladite pâte soit maintenue à une température entre 20 et 90°C, mais à l'exclusion de 20°C, tout au long de l'étape de granulation (iii).
- Procédé selon l'une quelconque des revendications 4 à 6, caractérisé en ce que l'extrudeuse est une extrudeuse à vis jumelées.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP91870060 | 1991-04-12 | ||
EP91870060 | 1991-04-12 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0508543A1 EP0508543A1 (fr) | 1992-10-14 |
EP0508543B1 true EP0508543B1 (fr) | 1997-08-06 |
Family
ID=8209015
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP92200994A Expired - Lifetime EP0508543B1 (fr) | 1991-04-12 | 1992-04-07 | Structuration chimique de pâtes tensio-actives pour former des granulés tensio-actifs avec haute activité |
Country Status (20)
Country | Link |
---|---|
EP (1) | EP0508543B1 (fr) |
JP (1) | JP3225041B2 (fr) |
CN (1) | CN1042746C (fr) |
AU (1) | AU1870092A (fr) |
BR (1) | BR9205890A (fr) |
CA (1) | CA2108166C (fr) |
CZ (1) | CZ213793A3 (fr) |
DE (1) | DE69221357T2 (fr) |
EG (1) | EG20046A (fr) |
ES (1) | ES2104809T3 (fr) |
FI (1) | FI934463A (fr) |
HU (1) | HUT66724A (fr) |
IE (1) | IE921162A1 (fr) |
MX (1) | MX9201721A (fr) |
NO (1) | NO933641L (fr) |
PT (1) | PT100371A (fr) |
SK (1) | SK108493A3 (fr) |
TR (1) | TR26814A (fr) |
TW (1) | TW200524B (fr) |
WO (1) | WO1992018602A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7186677B2 (en) | 2001-12-21 | 2007-03-06 | Henkel Kommanditgesellschaft Auf Aktien (Henkel Kgaa) | Method for the production of surfactant granulates containing builders |
Families Citing this family (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE69227311T2 (de) * | 1992-07-15 | 1999-06-02 | Procter & Gamble | Waschmittelzusammensetzungen |
EP0618289B1 (fr) * | 1993-03-30 | 1998-08-19 | The Procter & Gamble Company | Détergents granulaires à haute activité comprenant des agents de chelation et polymères et leur procédés de préparation |
US5486303A (en) * | 1993-08-27 | 1996-01-23 | The Procter & Gamble Company | Process for making high density detergent agglomerates using an anhydrous powder additive |
US5723433A (en) * | 1993-09-24 | 1998-03-03 | The Chemithon Corporation | Sovent removal process |
US6058623A (en) * | 1993-09-24 | 2000-05-09 | The Chemithon Corporation | Apparatus and process for removing volatile components from a composition |
DK0663439T3 (da) * | 1994-01-17 | 2000-09-18 | Procter & Gamble | Fremgangsmåde til fremstilling af detergentgranulat |
US5703037A (en) * | 1994-04-20 | 1997-12-30 | The Procter & Gamble Company | Process for the manufacture of free-flowing detergent granules |
EP0678573B1 (fr) * | 1994-04-20 | 2000-11-29 | The Procter & Gamble Company | Procédé de préparation de granules s'écoulant librement |
US5565137A (en) * | 1994-05-20 | 1996-10-15 | The Proctor & Gamble Co. | Process for making a high density detergent composition from starting detergent ingredients |
EP0688862A1 (fr) * | 1994-06-24 | 1995-12-27 | The Procter & Gamble Company | Pâtes détergents structurés et un procédé de fabrication de particules de détergent |
GB9417354D0 (en) * | 1994-08-26 | 1994-10-19 | Unilever Plc | Detergent particles and process for their production |
GB9417356D0 (en) * | 1994-08-26 | 1994-10-19 | Unilever Plc | Detergent particles and process for their production |
US5489392A (en) * | 1994-09-20 | 1996-02-06 | The Procter & Gamble Company | Process for making a high density detergent composition in a single mixer/densifier with selected recycle streams for improved agglomerate properties |
US5516448A (en) * | 1994-09-20 | 1996-05-14 | The Procter & Gamble Company | Process for making a high density detergent composition which includes selected recycle streams for improved agglomerate |
WO1996025482A1 (fr) * | 1995-02-13 | 1996-08-22 | The Procter & Gamble Company | Procede pour produire des agglomerats detergents a classe granulometrique controlee |
US5574005A (en) * | 1995-03-07 | 1996-11-12 | The Procter & Gamble Company | Process for producing detergent agglomerates from high active surfactant pastes having non-linear viscoelastic properties |
AUPN535095A0 (en) * | 1995-09-12 | 1995-10-05 | Procter & Gamble Company, The | Compositions comprising hydrophilic silica particulates |
US6159927A (en) * | 1995-09-12 | 2000-12-12 | The Procter & Gamble Company | Compositions comprising hydrophilic silica particulates |
US6172033B1 (en) | 1996-07-04 | 2001-01-09 | The Procter & Gamble Company | Process for conditioning of surfactant pastes to form high active surfactant agglomerates |
EP0816486B1 (fr) * | 1996-07-04 | 2004-04-14 | The Procter & Gamble Company | Procédé pour conditionner des pâtes tensio-actives pour obtenir des agglomérats tensio-actifs à haute activité |
GB9618876D0 (en) * | 1996-09-10 | 1996-10-23 | Unilever Plc | Process for preparing high bulk density detergent compositions |
GB9618875D0 (en) * | 1996-09-10 | 1996-10-23 | Unilever Plc | Process for preparing high bulk density detergent compositions |
GB9618877D0 (en) * | 1996-09-10 | 1996-10-23 | Unilever Plc | Process for preparing high bulk density detergent compositions |
US6281188B1 (en) * | 1996-10-04 | 2001-08-28 | The Procter & Gamble Company | Process for making a low density detergent composition |
GB9726824D0 (en) * | 1997-12-19 | 1998-02-18 | Manro Performance Chemicals Lt | Method of manufacturing particles |
DE19822942A1 (de) * | 1998-05-22 | 1999-11-25 | Henkel Kgaa | Granulation von Aniontensidsäuren |
DE19822943A1 (de) * | 1998-05-22 | 1999-11-25 | Henkel Kgaa | Verfahren zur Herstellung von Wasch- und Reinigungsmitteln |
DE19844523A1 (de) | 1998-09-29 | 2000-03-30 | Henkel Kgaa | Granulationsverfahren |
DE19844522A1 (de) | 1998-09-29 | 2000-03-30 | Henkel Kgaa | Granulationsverfahren |
DE10232304B4 (de) * | 2002-07-17 | 2005-10-27 | Henkel Kgaa | Neutralisation im Mischer |
GB0323273D0 (en) * | 2003-10-04 | 2003-11-05 | Unilever Plc | Process for making a detergent composition |
WO2014009101A1 (fr) * | 2012-07-09 | 2014-01-16 | Unilever N.V. | Procédé de production d'un granulé de détergent, granulé de détergent et composition détergente comprenant ledit granulé |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6072999A (ja) * | 1983-09-30 | 1985-04-25 | 花王株式会社 | 超濃縮粉末洗剤の製法 |
JPS61118500A (ja) * | 1984-11-14 | 1986-06-05 | ライオン株式会社 | 濃縮型洗剤組成物の製造方法 |
US4933100A (en) * | 1988-01-19 | 1990-06-12 | Colgate-Palmolive Co. | Built synthetic organic detergent composition patties and processes for washing laundry therewith |
US4919847A (en) * | 1988-06-03 | 1990-04-24 | Colgate Palmolive Co. | Process for manufacturing particulate detergent composition directly from in situ produced anionic detergent salt |
US4925585A (en) * | 1988-06-29 | 1990-05-15 | The Procter & Gamble Company | Detergent granules from cold dough using fine dispersion granulation |
GB8907187D0 (en) * | 1989-03-30 | 1989-05-10 | Unilever Plc | Detergent compositions and process for preparing them |
US5045238A (en) * | 1989-06-09 | 1991-09-03 | The Procter & Gamble Company | High active detergent particles which are dispersible in cold water |
CA2017922C (fr) * | 1989-06-09 | 1995-07-11 | Frank Joseph Mueller | Preparation de granules detergentes a haut pouvoir nettoyant au moyen d'un systeme de neutralisation continue |
-
1992
- 1992-04-07 ES ES92200994T patent/ES2104809T3/es not_active Expired - Lifetime
- 1992-04-07 EP EP92200994A patent/EP0508543B1/fr not_active Expired - Lifetime
- 1992-04-07 DE DE69221357T patent/DE69221357T2/de not_active Expired - Fee Related
- 1992-04-09 AU AU18700/92A patent/AU1870092A/en not_active Abandoned
- 1992-04-09 JP JP51026592A patent/JP3225041B2/ja not_active Expired - Fee Related
- 1992-04-09 CA CA002108166A patent/CA2108166C/fr not_active Expired - Fee Related
- 1992-04-09 WO PCT/US1992/002879 patent/WO1992018602A1/fr not_active Application Discontinuation
- 1992-04-09 CZ CS932137A patent/CZ213793A3/cs unknown
- 1992-04-09 BR BR9205890A patent/BR9205890A/pt not_active Application Discontinuation
- 1992-04-09 SK SK1084-93A patent/SK108493A3/sk unknown
- 1992-04-09 HU HU9302874A patent/HUT66724A/hu unknown
- 1992-04-10 PT PT100371A patent/PT100371A/pt not_active Application Discontinuation
- 1992-04-10 TR TR00344/92A patent/TR26814A/xx unknown
- 1992-04-10 IE IE116292A patent/IE921162A1/en not_active Application Discontinuation
- 1992-04-11 CN CN92103408A patent/CN1042746C/zh not_active Expired - Fee Related
- 1992-04-11 EG EG18692A patent/EG20046A/xx active
- 1992-04-13 MX MX9201721A patent/MX9201721A/es unknown
- 1992-05-06 TW TW081103529A patent/TW200524B/zh active
-
1993
- 1993-10-11 FI FI934463A patent/FI934463A/fi not_active Application Discontinuation
- 1993-10-11 NO NO933641A patent/NO933641L/no unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7186677B2 (en) | 2001-12-21 | 2007-03-06 | Henkel Kommanditgesellschaft Auf Aktien (Henkel Kgaa) | Method for the production of surfactant granulates containing builders |
Also Published As
Publication number | Publication date |
---|---|
ES2104809T3 (es) | 1997-10-16 |
CZ213793A3 (en) | 1994-10-19 |
HUT66724A (en) | 1994-12-28 |
CN1042746C (zh) | 1999-03-31 |
JPH06506719A (ja) | 1994-07-28 |
TW200524B (fr) | 1993-02-21 |
BR9205890A (pt) | 1994-09-27 |
CA2108166A1 (fr) | 1992-10-13 |
EG20046A (en) | 1997-08-31 |
SK108493A3 (en) | 1994-12-07 |
IE921162A1 (en) | 1992-10-21 |
EP0508543A1 (fr) | 1992-10-14 |
DE69221357T2 (de) | 1998-03-12 |
HU9302874D0 (en) | 1994-01-28 |
PT100371A (pt) | 1993-07-30 |
FI934463A0 (fi) | 1993-10-11 |
TR26814A (tr) | 1994-08-09 |
JP3225041B2 (ja) | 2001-11-05 |
NO933641D0 (no) | 1993-10-11 |
WO1992018602A1 (fr) | 1992-10-29 |
FI934463A (fi) | 1993-10-11 |
CA2108166C (fr) | 1998-08-04 |
MX9201721A (es) | 1992-10-01 |
NO933641L (no) | 1993-12-13 |
AU1870092A (en) | 1992-11-17 |
CN1066881A (zh) | 1992-12-09 |
DE69221357D1 (de) | 1997-09-11 |
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