KR890016160A - 분사 건조되고 포스페이트가 감소된 세재의 밀도를 상승시키는 방법 - Google Patents
분사 건조되고 포스페이트가 감소된 세재의 밀도를 상승시키는 방법 Download PDFInfo
- Publication number
- KR890016160A KR890016160A KR1019890005006A KR890005006A KR890016160A KR 890016160 A KR890016160 A KR 890016160A KR 1019890005006 A KR1019890005006 A KR 1019890005006A KR 890005006 A KR890005006 A KR 890005006A KR 890016160 A KR890016160 A KR 890016160A
- Authority
- KR
- South Korea
- Prior art keywords
- powder
- weight
- density
- phosphate
- reduced
- Prior art date
Links
- 239000003599 detergent Substances 0.000 title claims abstract 11
- 229910019142 PO4 Inorganic materials 0.000 title claims abstract 10
- 239000010452 phosphate Substances 0.000 title claims abstract 10
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 title claims abstract 10
- 239000000843 powder Substances 0.000 claims abstract 13
- 239000002736 nonionic surfactant Substances 0.000 claims abstract 6
- 238000001694 spray drying Methods 0.000 claims abstract 3
- 239000003945 anionic surfactant Substances 0.000 claims abstract 2
- 239000007788 liquid Substances 0.000 claims abstract 2
- 238000000034 method Methods 0.000 claims 8
- 239000007921 spray Substances 0.000 claims 8
- 230000014759 maintenance of location Effects 0.000 claims 2
- 229910021536 Zeolite Inorganic materials 0.000 claims 1
- 239000003513 alkali Substances 0.000 claims 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims 1
- 239000003979 granulating agent Substances 0.000 claims 1
- 239000010457 zeolite Substances 0.000 claims 1
- 238000010009 beating Methods 0.000 abstract 1
- 239000000126 substance Substances 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
-
- 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
- C11D11/02—Preparation in the form of powder by spray drying
-
- 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
- C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
- C11D1/66—Non-ionic compounds
- C11D1/83—Mixtures of non-ionic with anionic compounds
-
- 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
-
- 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
- C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
- C11D1/02—Anionic compounds
- C11D1/04—Carboxylic acids or salts thereof
-
- 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
- C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
- C11D1/02—Anionic compounds
- C11D1/12—Sulfonic acids or sulfuric acid esters; Salts thereof
- C11D1/22—Sulfonic acids or sulfuric acid esters; Salts thereof derived from aromatic compounds
-
- 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
- C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
- C11D1/66—Non-ionic compounds
- C11D1/72—Ethers of polyoxyalkylene glycols
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)
Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
Claims (8)
- 겉보기 밀도가 적어도 350g/리터인 분산 건조된 파우더는 샤프트가 길이(중심 축으로부터)는 드럼의 내부 반경의 80% 내지 98%인 방사상으로 배열된 충돌 기구로 장치되고 축 방향 회전용으로 장착되고, 샤프트의 회전 속도가 드럼내 파우더의 평균 보유시간이 10 내지 60초 이고 파우더 처리량을 균일하게 하기 위해 프로우드 지수가 50 내지 1000이고, 비이온 계면활성제의 반이하, 그러나 5% 이하(세제에 대해)가 분사 건조된 파우더내에 잔존하고 비이온 계면활성제의 잔류분이 혼합기에 액체형으로 도입되는 방식으로 조절되는 평형한 내부 벽면의 실린더형, 수평으로 배열되거나 약간 기울어진(수평에 대해) 혼합 드럼에 계속적으로 도입됨을 특징으로 하는A) 적어도 1종의 음이온 계면활성제 4 내지 20중량%B) 적어도 1종의 비이온 계면활성제 2 내지 20중량%C)적어도 1종의 조립제 20 내지 50중량%D)세척성 알칼리 3 내지 25중량%E)고온 분사 건조되는 다른 세제 구성성분 0 내지 30중량%를 함유하는 분사 건조되고, 포스페이트가 감소된 세제 성분의 밀도를 상승시키는 방법.
- 제 1 항에 있어서, 회전 기구의 길이가 드럼의 내부 반경의 85% 내지 96%인 분사 건조되고, 포스페이트가 감소된 세제 성분의 밀도를 상승시키는 방법.
- 제1 또는 2항에 있어서, 타워 파우더의 겉보기 밀도가 적어도 400g/1인 분사 건조되고, 포스페이트가 감소된 세제 성분의 밀도를 상승시키는 방법.
- 제1 내지 3항중 어느 한 항에 있어서, 파우더의 평균 보유 시간이 20 내지 50초인 분사 건조되고, 포스페이트가 감소된 세제 성분의 밀도를 상승시키는 방법.
- 제1 내지 4항중 어느 한 항에 있어서, 프로우드 지수가 100 내지 1000인 분사 건조되고, 포스페이트가 감소된 세제 성분의 밀도를 상승시키는 방법.
- 제1 내지 5항중 어느 한 항에 있어서, 파우더의 온도가 50℃를 상회하지 않는 분사 건조되고, 포스페이트가 감소된 세제 성분의 밀도를 상승시키는 방법.
- 제1 내지 6항중 어느 한 항에 있어서, 미세하게 절단된 건조 제올라이트의 0.5 내지 3중량%가 첨가되고 파우더와 혼합되는 분사 건조되고, 포스페이트가 감소된 세제 성분의 밀도를 상승시키는 방법.
- 제1 내지 6항중 어느 한 항에 있어서, 파우더 성분이 동시에 가공되는 분사 건조되고, 포스페이트가 감소된 세제 성분의 밀도를 상승시키는 방법.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3812530A DE3812530A1 (de) | 1988-04-15 | 1988-04-15 | Verfahren zur erhoehung der dichte spruehgetrockneter, phosphatreduzierter waschmittel |
DEP3812530.7 | 1988-04-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
KR890016160A true KR890016160A (ko) | 1989-11-28 |
Family
ID=6352038
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019890005006A KR890016160A (ko) | 1988-04-15 | 1989-04-15 | 분사 건조되고 포스페이트가 감소된 세재의 밀도를 상승시키는 방법 |
Country Status (8)
Country | Link |
---|---|
US (1) | US5149455A (ko) |
EP (1) | EP0337330B1 (ko) |
JP (1) | JPH01311200A (ko) |
KR (1) | KR890016160A (ko) |
AT (1) | ATE138096T1 (ko) |
DE (2) | DE3812530A1 (ko) |
DK (1) | DK182389A (ko) |
ES (1) | ES2086308T3 (ko) |
Families Citing this family (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3905671C2 (de) * | 1989-02-24 | 1999-02-04 | Henkel Kgaa | Zur Herstellung wäßriger Konzentrate geeignetes Waschmittelgranulat |
GB8924294D0 (en) * | 1989-10-27 | 1989-12-13 | Unilever Plc | Detergent compositions |
GB9008013D0 (en) * | 1990-04-09 | 1990-06-06 | Unilever Plc | High bulk density granular detergent compositions and process for preparing them |
JP3192469B2 (ja) * | 1991-05-17 | 2001-07-30 | 花王株式会社 | ノニオン洗剤粒子の製造方法 |
DE4123195A1 (de) * | 1991-07-12 | 1993-01-14 | Henkel Kgaa | Waschaktive zubereitung mit verzoegertem aufloeseverhalten und verfahren zu ihrer herstellung |
DE4124701A1 (de) * | 1991-07-25 | 1993-01-28 | Henkel Kgaa | Verfahren zur herstellung fester wasch- und reinigungsmittel mit hohem schuettgewicht und verbesserter loesegeschwindigkeit |
CA2083331C (en) * | 1991-11-26 | 1998-08-11 | Johannes H. M. Akkermans | Detergent compositions |
TW240243B (ko) * | 1992-03-12 | 1995-02-11 | Kao Corp | |
DE4211699A1 (de) * | 1992-04-08 | 1993-10-14 | Henkel Kgaa | Verfahren zur Erhöhung des Schüttgewichts sprühgetrockneter Waschmittel |
DE4221736A1 (de) * | 1992-07-02 | 1994-01-05 | Henkel Kgaa | Feste waschaktive Zubereitung mit verbessertem Einspülverhalten |
TR27586A (tr) * | 1992-09-01 | 1995-06-13 | Procter & Gamble | Yüksek yogunlukla zerre deterjanin yapilmasi icin islem ve islem ile yapilan bilesimler. |
DE69434056T2 (de) * | 1993-01-26 | 2006-02-23 | National Starch And Chemical Investment Holding Corp., Wilmington | Waschmittelzusammensetzung |
US5866012A (en) * | 1993-01-26 | 1999-02-02 | National Starch And Chemical Investment Holding Corporation | Multifunctional maleate polymers |
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 |
AU673926B2 (en) * | 1993-07-13 | 1996-11-28 | Colgate-Palmolive Company, The | Process for preparing detergent composition having high bulk density |
WO1995026394A1 (fr) * | 1994-03-28 | 1995-10-05 | Kao Corporation | Procede de production de particules detergentes a densite apparente elevee |
DE19500644B4 (de) * | 1995-01-12 | 2010-09-09 | Henkel Ag & Co. Kgaa | Sprühgetrocknetes Waschmittel oder Komponente hierfür |
US5757011A (en) * | 1995-02-10 | 1998-05-26 | Orbit Semiconductor, Inc. | X-ray onset detector and method |
US5547612A (en) | 1995-02-17 | 1996-08-20 | National Starch And Chemical Investment Holding Corporation | Compositions of water soluble polymers containing allyloxybenzenesulfonic acid monomer and methallyl sulfonic acid monomer and methods for use in aqueous systems |
US5565422A (en) * | 1995-06-23 | 1996-10-15 | The Procter & Gamble Company | Process for preparing a free-flowing particulate detergent composition having improved solubility |
US5739094A (en) * | 1997-01-17 | 1998-04-14 | The Procter & Gamble Company | Free-flowing particulate detergent admix composition containing nonionic surfactant |
US5733863A (en) * | 1997-01-17 | 1998-03-31 | The Procter & Gamble Company | Process for making a free-flowing particule detergent admix containing nonionic surfactant |
DE19757217A1 (de) * | 1997-12-22 | 1999-06-24 | Henkel Kgaa | Teilchenförmiges Wasch- und Reinigungsmittel |
EP1041139B1 (en) * | 1998-10-16 | 2004-12-22 | Kao Corporation | Process for producing detergent particles |
US20050203263A1 (en) * | 2004-03-15 | 2005-09-15 | Rodrigues Klein A. | Aqueous treatment compositions and polymers for use therein |
JP2007197662A (ja) * | 2005-12-28 | 2007-08-09 | Kao Corp | 洗剤粒子群の製造方法 |
BR112013001725A2 (pt) * | 2010-09-22 | 2016-05-31 | Dow Global Technologies Llc | processo para tratar de celulose e metodo para produzir agregados em um processo para dispersão e dissolução de éteres de celulose solúveis em água |
Family Cites Families (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3360865A (en) * | 1965-02-08 | 1968-01-02 | Pillsbury Co | Process and apparatus for agglomerating and drying flour |
US3886098A (en) * | 1971-03-15 | 1975-05-27 | Colgate Palmolive Co | Manufacture of free flowing particulate detergent composition containing nonionic detergent |
US4006110A (en) * | 1971-11-30 | 1977-02-01 | Colgate-Palmolive Company | Manufacture of free-flowing particulate heavy duty synthetic detergent composition |
DE2224837C3 (de) * | 1972-05-20 | 1986-05-07 | Agfa-Gevaert Ag, 5090 Leverkusen | Direktpositives photographisches Aufzeichnungsmaterial |
ZA734721B (en) * | 1972-07-14 | 1974-03-27 | Procter & Gamble | Detergent compositions |
GB1455873A (en) * | 1973-08-24 | 1976-11-17 | Procter & Gamble | Textile-softening detergent compositions |
GB1517713A (en) * | 1974-10-31 | 1978-07-12 | Unilever Ltd | Preparation of detergent formulations |
US4663194A (en) * | 1976-12-02 | 1987-05-05 | The Colgate-Palmolive Co. | Phosphate-free concentrated particulate heavy duty laundry detergent |
US4146495A (en) * | 1977-08-22 | 1979-03-27 | Monsanto Company | Detergent compositions comprising polyacetal carboxylates |
US4144226A (en) * | 1977-08-22 | 1979-03-13 | Monsanto Company | Polymeric acetal carboxylates |
EP0026529B2 (en) * | 1979-09-29 | 1992-08-19 | THE PROCTER & GAMBLE COMPANY | Detergent compositions |
US4320105A (en) * | 1980-10-20 | 1982-03-16 | Lithium Corporation Of America | Pellitizing method |
EP0120492B1 (de) * | 1983-03-25 | 1988-07-13 | Henkel Kommanditgesellschaft auf Aktien | Körnige, freifliessende Waschmittelkomponente und Verfahren zu ihrer Herstellung |
GB8329880D0 (en) * | 1983-11-09 | 1983-12-14 | Unilever Plc | Particulate adjuncts |
US4552681A (en) * | 1983-12-10 | 1985-11-12 | Henkel Kommanditgesellschaft Auf Aktien | Granular, free-flowing detergent component and method for its production |
DE3424987A1 (de) * | 1984-07-06 | 1986-02-06 | Unilever N.V., Rotterdam | Verfahren zur herstellung eines pulverfoermigen waschmittels mit erhoehtem schuettgewicht |
JPH07122079B2 (ja) * | 1984-09-14 | 1995-12-25 | 花王株式会社 | 流動性の改良された高密度の粒状洗剤の製法 |
JPS6169897A (ja) * | 1984-09-14 | 1986-04-10 | 花王株式会社 | 流動性の改良された高密度の粒状洗剤の製法 |
JPH0680160B2 (ja) * | 1984-09-14 | 1994-10-12 | 花王株式会社 | 流動性の改良された高密度の粒状洗剤の製法 |
JPH0672237B2 (ja) * | 1984-09-14 | 1994-09-14 | 花王株式会社 | 流動性の改良された高密度の粒状洗剤の製法 |
DE3514364A1 (de) * | 1985-04-20 | 1986-10-23 | Henkel KGaA, 4000 Düsseldorf | Koerniges waschmittel mit verbessertem reinigungsvermoegen |
US4970017A (en) * | 1985-04-25 | 1990-11-13 | Lion Corporation | Process for production of granular detergent composition having high bulk density |
DE3545947A1 (de) * | 1985-12-23 | 1987-07-02 | Henkel Kgaa | Phosphatfreies, granulares waschmittel |
ES2020949B3 (es) * | 1986-01-17 | 1991-10-16 | Kao Corp | Composicion detergente granular de alta densidad. |
US4931203A (en) * | 1987-06-05 | 1990-06-05 | Colgate-Palmolive Company | Method for making an automatic dishwashing detergent powder by spraying drying and post-adding nonionic detergent |
US4992198A (en) * | 1988-01-19 | 1991-02-12 | Kao Corporation | Detergent composition containing clathrate granules of a perfume-clathrate compound |
JPH0633439B2 (ja) * | 1988-07-28 | 1994-05-02 | 花王株式会社 | 高密度粒状濃縮洗剤組成物 |
-
1988
- 1988-04-15 DE DE3812530A patent/DE3812530A1/de not_active Withdrawn
-
1989
- 1989-04-08 EP EP89106222A patent/EP0337330B1/de not_active Expired - Lifetime
- 1989-04-08 ES ES89106222T patent/ES2086308T3/es not_active Expired - Lifetime
- 1989-04-08 AT AT89106222T patent/ATE138096T1/de active
- 1989-04-08 DE DE58909678T patent/DE58909678D1/de not_active Expired - Fee Related
- 1989-04-14 DK DK182389A patent/DK182389A/da not_active Application Discontinuation
- 1989-04-14 JP JP1096206A patent/JPH01311200A/ja active Pending
- 1989-04-15 KR KR1019890005006A patent/KR890016160A/ko not_active IP Right Cessation
-
1991
- 1991-01-18 US US07/644,469 patent/US5149455A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
DK182389D0 (da) | 1989-04-14 |
US5149455A (en) | 1992-09-22 |
EP0337330A3 (en) | 1990-04-11 |
DE3812530A1 (de) | 1989-10-26 |
DE58909678D1 (de) | 1996-06-20 |
ES2086308T3 (es) | 1996-07-01 |
DK182389A (da) | 1989-10-16 |
ATE138096T1 (de) | 1996-06-15 |
JPH01311200A (ja) | 1989-12-15 |
EP0337330B1 (de) | 1996-05-15 |
EP0337330A2 (de) | 1989-10-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR890016160A (ko) | 분사 건조되고 포스페이트가 감소된 세재의 밀도를 상승시키는 방법 | |
KR960702546A (ko) | 셀룰로우스 주제 프리믹스 형성방법 | |
US5238304A (en) | Process and device for mixing | |
DK409781A (da) | Dispergeringsblandemaskine | |
ATE85372T1 (de) | Maschinelles waschverfahren. | |
DE3469365D1 (en) | Suds suppressor compositions and their use in detergent compositions | |
KR920018204A (ko) | 세제 조성물 및 그 제조방법 | |
BR9915491A (pt) | Composição detergente particulada de lavagem de roupas e de livre escoamento, processo para a preparação de um componente detergente granular de livre escoamento, e, componente detergente granular e de livre escoamento | |
US3926827A (en) | Method for making detergent compositions | |
CN100491099C (zh) | 粉体复合改性方法及装置 | |
ES2133764T3 (es) | Procedimiento para producir una composicion detergente de alta densidad a partir de ingredientes detergentes de partida. | |
KR890013168A (ko) | 분무건조 세정제의 밀도 증가 방법 | |
GB2001252A (en) | A mixer for air entrained concrete or ordinary concrete | |
ES367854A1 (es) | Procedimiento para preparar un producto de lavanderia. | |
IE37041B1 (en) | Detergent compositions | |
CA2375488A1 (en) | Process for making a granular detergent composition | |
JPS6447432A (en) | Agitator | |
PL133394B2 (en) | Planetary mizer in particular for intensively mixing food products | |
JPH026104A (ja) | セラミック材料の混練方法 | |
KR20030058239A (ko) | 교반기 | |
KR970065824A (ko) | 세탁기 | |
BR9713167A (pt) | Processo para a fabricação de detergente de alta densidade. | |
JPS57149342A (en) | Production of crosslinkable polyolefin resin particle | |
KR20010017153A (ko) | 고밀도분말세제의 제조방법 | |
CN1093744A (zh) | 高效洁净剂及其生产方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
SUBM | Surrender of laid-open application requested |