EA200000026A1 - Способ получения гранулированных моющих продуктов - Google Patents
Способ получения гранулированных моющих продуктовInfo
- Publication number
- EA200000026A1 EA200000026A1 EA200000026A EA200000026A EA200000026A1 EA 200000026 A1 EA200000026 A1 EA 200000026A1 EA 200000026 A EA200000026 A EA 200000026A EA 200000026 A EA200000026 A EA 200000026A EA 200000026 A1 EA200000026 A1 EA 200000026A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- particles
- average diameter
- starting material
- solid starting
- microns
- Prior art date
Links
- 239000002245 particle Substances 0.000 abstract 6
- 239000007787 solid Substances 0.000 abstract 5
- 239000007858 starting material Substances 0.000 abstract 5
- 239000011230 binding agent Substances 0.000 abstract 1
- 239000003599 detergent Substances 0.000 abstract 1
- 239000012530 fluid Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000002994 raw material Substances 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
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
- C11D11/0082—Special methods for preparing compositions containing mixtures of detergents 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
- C11D11/0088—Special methods for preparing compositions containing mixtures of detergents 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 the liquefied ingredients being sprayed or adsorbed onto solid particles
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)
- Glanulating (AREA)
Abstract
Гранулированный моющий продукт получают распылением жидкого связующего для взаимодействия измельченного твердого исходного материала в грануляторе с малым сдвигающим усилием, таким как устройство с псевдоожиженным слоем. Средний диаметр dкапель не превышает в 10 раз средний диаметр dчастиц фракции твердого исходного материала, который имеет диаметр dчастиц от 20 до 200 мкм при условии, если свыше 90% по весу твердого исходного материала имеют средний диаметр dчастиц менее 20 мкм, то средний диаметр dчастиц совокупного твердого исходного материала составляет 20 мкм. Если свыше 90% по весу твердого исходного материала имеют средний диаметр dчастиц более 200 мкм, то средний диаметр dчастиц совокупного исходного твердого материала составляет 200 мкм.Международная заявка была опубликована вместе с отчетом о международном поиске.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GBGB9712583.5A GB9712583D0 (en) | 1997-06-16 | 1997-06-16 | Production of detergent granulates |
PCT/EP1998/003668 WO1998058047A1 (en) | 1997-06-16 | 1998-06-12 | Production of detergent granulates |
Publications (2)
Publication Number | Publication Date |
---|---|
EA200000026A1 true EA200000026A1 (ru) | 2000-08-28 |
EA001333B1 EA001333B1 (ru) | 2001-02-26 |
Family
ID=10814304
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA200000026A EA001333B1 (ru) | 1997-06-16 | 1998-06-12 | Способ получения гранулированных моющих продуктов |
Country Status (17)
Country | Link |
---|---|
US (2) | US6274544B1 (ru) |
EP (1) | EP0993503A1 (ru) |
CN (1) | CN1179029C (ru) |
AR (1) | AR013092A1 (ru) |
AU (1) | AU743892B2 (ru) |
BR (1) | BR9810168A (ru) |
CA (1) | CA2294594A1 (ru) |
EA (1) | EA001333B1 (ru) |
GB (1) | GB9712583D0 (ru) |
HU (1) | HUP0003318A3 (ru) |
ID (1) | ID23854A (ru) |
IN (1) | IN190658B (ru) |
PL (1) | PL189781B1 (ru) |
TR (1) | TR200000305T2 (ru) |
TW (1) | TW460578B (ru) |
WO (1) | WO1998058047A1 (ru) |
ZA (1) | ZA985192B (ru) |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9526097D0 (en) * | 1995-12-20 | 1996-02-21 | Unilever Plc | Process |
GB9712580D0 (en) * | 1997-06-16 | 1997-08-20 | Unilever Plc | Production of detergent granulates |
GB9712583D0 (en) | 1997-06-16 | 1997-08-20 | Unilever Plc | Production of detergent granulates |
GB9713748D0 (en) * | 1997-06-27 | 1997-09-03 | Unilever Plc | Production of detergent granulates |
WO1999003967A1 (en) | 1997-07-14 | 1999-01-28 | The Procter & Gamble Company | Process for making a low density detergent composition by controlling agglomeration via particle size |
CA2296320C (en) | 1997-07-14 | 2003-05-27 | The Procter & Gamble Company | Process for making a low density detergent composition by controlled agglomeration in a fluid bed dryer |
US6423679B1 (en) | 1997-07-15 | 2002-07-23 | The Procter & Gamble Company | Process for making high-active detergent agglomerates by multi-stage surfactant paste injection |
US6440342B1 (en) | 1998-07-08 | 2002-08-27 | The Procter & Gamble Company | Process for making a low density detergent composition by controlling nozzle height in a fluid bed dryer |
US6794354B1 (en) * | 1998-09-18 | 2004-09-21 | The Procter & Gamble Company | Continuous process for making detergent composition |
GB9913546D0 (en) | 1999-06-10 | 1999-08-11 | Unilever Plc | Granular detergent component containing zeolite map and laundry detergent compositions containing it |
US6790821B1 (en) | 1999-06-21 | 2004-09-14 | The Procter & Gamble Company | Process for coating detergent granules in a fluidized bed |
US6894018B1 (en) | 1999-06-21 | 2005-05-17 | The Procter & Gamble Company | Process for making granular detergent in a fluidized bed granulator having recycling of improperly sized particles |
GB9927653D0 (en) | 1999-11-22 | 2000-01-19 | Unilever Plc | Process for preparing granular detergent compositions |
GB0125653D0 (en) | 2001-10-25 | 2001-12-19 | Unilever Plc | Process for the production of detergent granules |
DE60217889T2 (de) | 2001-10-25 | 2007-05-31 | Unilever N.V. | Verfahren zur herstellung von waschmittelgranulaten |
DE10258006B4 (de) * | 2002-12-12 | 2006-05-04 | Henkel Kgaa | Trockenneutralisationsverfahren II |
US7198653B2 (en) | 2003-07-31 | 2007-04-03 | Delavau Llc | Calcium carbonate granulation |
US7459841B2 (en) * | 2004-01-22 | 2008-12-02 | Canon Kabushiki Kaisha | Electron beam apparatus, display apparatus, television apparatus, and spacer |
JP2008502746A (ja) * | 2004-06-16 | 2008-01-31 | ヘンケル コマンディットゲゼルシャフト アウフ アクチエン | コンポミックスマシーンにおいて中性化することにより得られるターゲット造粒 |
US9138414B1 (en) | 2006-09-15 | 2015-09-22 | Delavau Llc | Calcium supplement having enhanced absorption |
EP2123742A1 (en) | 2008-05-14 | 2009-11-25 | The Procter and Gamble Company | A solid laundry detergent composition comprising light density silicate salt |
CA3089557A1 (en) | 2018-01-26 | 2019-08-01 | Ecolab Usa Inc. | Solidifying liquid anionic surfactants |
MX2020007859A (es) | 2018-01-26 | 2020-09-18 | Ecolab Usa Inc | Solidificacion de tensioactivos de oxido de amina, betaina y/o sultaina liquidos con un aglutinante y un portador opcional. |
JP7485605B2 (ja) * | 2018-01-26 | 2024-05-16 | エコラボ ユーエスエー インコーポレイティド | 担体を用いる、液体アミンオキシド、ベタイン、および/またはスルタイン界面活性剤の固化 |
Family Cites Families (67)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE255833C (ru) | ||||
DE140987C (ru) | 1903-05-16 | |||
GB707994A (en) | 1950-02-13 | 1954-04-28 | Ruhrchemie Ag | Process for the neutralization of sulphonic acids |
GB748780A (en) * | 1952-05-30 | 1956-05-09 | Bataafsche Petroleum | Process for coating finely divided solid materials |
BE597383A (ru) * | 1959-11-24 | |||
AU413469B2 (en) | 1966-03-09 | 1971-05-24 | Knapsack Ag | Process forthe manufacture of detergent compositions |
US3650961A (en) * | 1969-07-18 | 1972-03-21 | Monsanto Co | Process for preparing particulate products having preferentially internally concentrated core components |
GB1341557A (ru) | 1970-06-02 | 1973-12-25 | ||
GB1437950A (en) | 1972-08-22 | 1976-06-03 | Unilever Ltd | Detergent compositions |
AT330930B (de) | 1973-04-13 | 1976-07-26 | Henkel & Cie Gmbh | Verfahren zur herstellung von festen, schuttfahigen wasch- oder reinigungsmitteln mit einem gehalt an calcium bindenden substanzen |
DE2433485A1 (de) | 1973-07-16 | 1975-02-06 | Procter & Gamble | Zur verwendung in waschmitteln geeignete aluminosilikat-ionenaustauscher |
US4153625A (en) | 1976-07-01 | 1979-05-08 | Barton Brandon H | Neutralization process |
US4666740A (en) * | 1976-12-02 | 1987-05-19 | The Colgate-Palmolive Co. | Phosphate-free concentrated particulate heavy duty laundry detergent |
GB1581761A (en) | 1977-06-09 | 1980-12-17 | Azote Sa Cie Neerlandaise | Urea granulation |
US4183763A (en) * | 1977-12-27 | 1980-01-15 | Oil-Dri Corporation Of America | Gypsum-based granules and method of production |
DD140987B1 (de) * | 1979-01-05 | 1982-06-30 | Manfred Mittelstrass | Kontinuierliches herstellungsverfahren granulierter wasch-und reinigungsmittel in wirbelschichtapparaten |
FR2471222A1 (fr) * | 1979-12-12 | 1981-06-19 | Interox | Procede pour la stabilisation de particules contenant des composes peroxygenes et compositions de blanchiment contenant des particules stabilisees selon ce procede |
US4664950A (en) * | 1980-09-02 | 1987-05-12 | The Colgate Palmolive Co. | Concentrated heavy duty particulate laundry detergent |
US4364750A (en) | 1981-02-09 | 1982-12-21 | Canadian Fine Color Company, Limited | Process and apparatus for purifying waste gases |
US4487710A (en) * | 1982-03-01 | 1984-12-11 | The Procter & Gamble Company | Granular detergents containing anionic surfactant and ethoxylated surfactant solubility aid |
US4473485A (en) * | 1982-11-05 | 1984-09-25 | Lever Brothers Company | Free-flowing detergent powders |
PH18527A (en) * | 1982-12-17 | 1985-08-02 | Unilever Nv | Detergent composition for washing fabric |
US4539135A (en) * | 1983-06-01 | 1985-09-03 | Colgate Palmolive Co. | Perfume-containing carrier for laundry compositions |
NL8302999A (nl) | 1983-08-27 | 1985-03-18 | Unie Van Kunstmestfab Bv | Werkwijze voor het bereiden van granules. |
NL8303000A (nl) | 1983-08-27 | 1985-03-18 | Unie Van Kunstmestfab Bv | Werkwijze voor het bereiden van granules. |
DE3413571A1 (de) | 1984-04-11 | 1985-10-24 | Hoechst Ag, 6230 Frankfurt | Verwendung von kristallinen schichtfoermigen natriumsilikaten zur wasserenthaertung und verfahren zur wasserenthaertung |
ES8607378A1 (es) * | 1984-08-06 | 1986-05-16 | Kao Corp | Una composicion detergente en polvo de gran densidad |
US4857223A (en) * | 1985-10-03 | 1989-08-15 | Colgate-Palmolive Company | Non-caking bleaching detergent composition containing a lower hydrate of sodium perborate |
US4734224A (en) | 1986-09-15 | 1988-03-29 | The Dial Corporation | Dry neutralization process for detergent slurries |
US4881940A (en) * | 1987-06-25 | 1989-11-21 | Colgate-Palmolive Co. | Granulated magnesium monoperoxyphthalate coated with fatty acid for prevention of dye damage of bleach sensitive fabrics |
JP2566146B2 (ja) | 1987-08-20 | 1996-12-25 | 株式会社大川原製作所 | 連続式流動層造粒装置 |
GB2209172A (en) * | 1987-08-28 | 1989-05-04 | Unilever Plc | Preparation of solid particulate components for detergents |
US4828721A (en) * | 1988-04-28 | 1989-05-09 | Colgate-Palmolive Co. | Particulate detergent compositions and manufacturing processes |
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 |
GB8818613D0 (en) | 1988-08-05 | 1988-09-07 | Paterson Zochonis Uk Ltd | Detergents |
US4845275A (en) | 1988-09-26 | 1989-07-04 | Amoco Corporation | Trimellitic acid process |
CA2001927C (en) | 1988-11-03 | 1999-12-21 | Graham Thomas Brown | Aluminosilicates and detergent compositions |
GB8907187D0 (en) | 1989-03-30 | 1989-05-10 | Unilever Plc | Detergent compositions and process for preparing them |
GB8922018D0 (en) | 1989-09-29 | 1989-11-15 | Unilever Plc | Detergent compositions and process for preparing them |
DE4127323A1 (de) | 1991-08-20 | 1993-02-25 | Henkel Kgaa | Verfahren zur herstellung von tensidgranulaten |
WO1993004154A1 (de) | 1991-08-20 | 1993-03-04 | Henkel Kommanditgesellschaft Auf Aktien | Verfahren zur herstellung carbonathaltiger granulate |
EP0555622B1 (en) | 1992-02-14 | 1997-07-09 | The Procter & Gamble Company | Process for making detergent granules by neutralisation of sulphonic acids |
DE4209435A1 (de) | 1992-03-24 | 1993-09-30 | Henkel Kgaa | Granulares, nichtionische Tenside enthaltendes, phosphatfreies Additiv für Wasch- und Reinigungsmittel |
DE4216629A1 (de) | 1992-05-20 | 1993-11-25 | Henkel Kgaa | Verfahren zur Herstellung aniontensidhaltiger Wasch- und Reinigungsmittel |
ES2091037T3 (es) | 1992-08-07 | 1996-10-16 | Hydro Agri Sluiskil Bv | Procedimiento para la produccion de granulos de urea. |
DE4232874A1 (de) | 1992-09-30 | 1994-03-31 | Henkel Kgaa | Verfahren zur Herstellung von Tensidgranulaten |
US5290603A (en) | 1992-12-18 | 1994-03-01 | Union Carbide Chemicals & Plastics Technology Corporation | Method for spraying polymeric compositions with reduced solvent emission and enhanced atomization |
US5739097A (en) | 1993-02-11 | 1998-04-14 | Henkel Kommanditgesellschaft Auf Aktien | Process for the production of surfactant granules |
DE4304015A1 (de) | 1993-02-11 | 1994-08-18 | Henkel Kgaa | Verfahren zur Herstellung von Granulaten |
DE4304062A1 (de) * | 1993-02-11 | 1994-08-18 | Henkel Kgaa | Verfahren zur Herstellung von Tensidgranulaten |
EP0695343B1 (en) | 1993-04-19 | 1997-05-14 | Akzo Nobel N.V. | Fluidized bed coated amidoperoxyacid bleach composition |
USH1604H (en) | 1993-06-25 | 1996-11-05 | Welch; Robert G. | Process for continuous production of high density detergent agglomerates in a single mixer/densifier |
DE4408360A1 (de) | 1994-03-14 | 1995-09-21 | Henkel Kgaa | Verfahren zur Herstellung schmutzlösender Granulate |
WO1996003485A1 (en) | 1994-07-21 | 1996-02-08 | The Procter & Gamble Company | Bleaching agents containing paraffin oil or wax in a particle separate from the bleach |
GB9415904D0 (en) * | 1994-08-05 | 1994-09-28 | Unilever Plc | Process for the production of detergent composition |
DE4443644A1 (de) * | 1994-12-08 | 1996-06-13 | Henkel Kgaa | Feste, rieselfähige Zubereitungen |
GB9526097D0 (en) | 1995-12-20 | 1996-02-21 | Unilever Plc | Process |
GB9601920D0 (en) | 1996-01-31 | 1996-04-03 | Unilever Plc | Process for the production of a detergent composition |
AU7661996A (en) | 1996-10-04 | 1998-04-24 | Procter & Gamble Company, The | Process for making a low density detergent composition |
CA2267291C (en) | 1996-10-04 | 2002-12-10 | The Procter & Gamble Company | Process for making a low density detergent composition by non-tower process |
GB9712583D0 (en) | 1997-06-16 | 1997-08-20 | Unilever Plc | Production of detergent granulates |
GB9712580D0 (en) | 1997-06-16 | 1997-08-20 | Unilever Plc | Production of detergent granulates |
GB9712587D0 (en) | 1997-06-16 | 1997-08-20 | Unilever Plc | Production of detergent granulates |
GB9713748D0 (en) | 1997-06-27 | 1997-09-03 | Unilever Plc | Production of detergent granulates |
WO1999003967A1 (en) | 1997-07-14 | 1999-01-28 | The Procter & Gamble Company | Process for making a low density detergent composition by controlling agglomeration via particle size |
CA2296320C (en) | 1997-07-14 | 2003-05-27 | The Procter & Gamble Company | Process for making a low density detergent composition by controlled agglomeration in a fluid bed dryer |
DE69826871T2 (de) | 1997-07-14 | 2006-03-09 | The Procter & Gamble Company, Cincinnati | Verfahren zur herstellung von waschmitteln mit niedriger schüttdichte durch kontrolle der düsenhöhe im fliessbett |
-
1997
- 1997-06-16 GB GBGB9712583.5A patent/GB9712583D0/en not_active Ceased
-
1998
- 1998-06-12 BR BR9810168-4A patent/BR9810168A/pt not_active IP Right Cessation
- 1998-06-12 TR TR2000/00305T patent/TR200000305T2/xx unknown
- 1998-06-12 EP EP98933628A patent/EP0993503A1/en not_active Withdrawn
- 1998-06-12 WO PCT/EP1998/003668 patent/WO1998058047A1/en active IP Right Grant
- 1998-06-12 CA CA002294594A patent/CA2294594A1/en not_active Abandoned
- 1998-06-12 HU HU0003318A patent/HUP0003318A3/hu unknown
- 1998-06-12 PL PL98337571A patent/PL189781B1/pl not_active IP Right Cessation
- 1998-06-12 AU AU83381/98A patent/AU743892B2/en not_active Ceased
- 1998-06-12 ID IDW991609A patent/ID23854A/id unknown
- 1998-06-12 CN CNB988079216A patent/CN1179029C/zh not_active Expired - Fee Related
- 1998-06-12 EA EA200000026A patent/EA001333B1/ru not_active IP Right Cessation
- 1998-06-15 ZA ZA9805192A patent/ZA985192B/xx unknown
- 1998-06-15 US US09/097,335 patent/US6274544B1/en not_active Expired - Fee Related
- 1998-06-16 AR ARP980102844A patent/AR013092A1/es active IP Right Grant
- 1998-06-16 IN IN375BO1998 patent/IN190658B/en unknown
- 1998-10-15 TW TW087117208A patent/TW460578B/zh not_active IP Right Cessation
-
2000
- 2000-09-11 US US09/659,715 patent/US6429184B1/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
US6274544B1 (en) | 2001-08-14 |
HUP0003318A3 (en) | 2003-02-28 |
US6429184B1 (en) | 2002-08-06 |
AU743892B2 (en) | 2002-02-07 |
CN1179029C (zh) | 2004-12-08 |
TR200000305T2 (tr) | 2000-12-21 |
ZA985192B (en) | 1999-12-20 |
AU8338198A (en) | 1999-01-04 |
EP0993503A1 (en) | 2000-04-19 |
ID23854A (id) | 2000-05-25 |
BR9810168A (pt) | 2000-10-17 |
PL337571A1 (en) | 2000-08-28 |
CN1265700A (zh) | 2000-09-06 |
EA001333B1 (ru) | 2001-02-26 |
IN190658B (ru) | 2003-08-16 |
GB9712583D0 (en) | 1997-08-20 |
CA2294594A1 (en) | 1998-12-23 |
HUP0003318A2 (hu) | 2001-02-28 |
PL189781B1 (pl) | 2005-09-30 |
TW460578B (en) | 2001-10-21 |
WO1998058047A1 (en) | 1998-12-23 |
AR013092A1 (es) | 2000-12-13 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s) |
Designated state(s): AM AZ BY KZ KG MD TJ TM |
|
MM4A | Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s) |
Designated state(s): RU |