ES2086219T3 - Procedimiento para la obtencion de granulados, que son adecuados como humectantes, agentes de lavado y/o agentes de limpieza. - Google Patents
Procedimiento para la obtencion de granulados, que son adecuados como humectantes, agentes de lavado y/o agentes de limpieza.Info
- Publication number
- ES2086219T3 ES2086219T3 ES93903908T ES93903908T ES2086219T3 ES 2086219 T3 ES2086219 T3 ES 2086219T3 ES 93903908 T ES93903908 T ES 93903908T ES 93903908 T ES93903908 T ES 93903908T ES 2086219 T3 ES2086219 T3 ES 2086219T3
- Authority
- ES
- Spain
- Prior art keywords
- granulation
- granulates
- agents
- capacity
- humidants
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
- B01D1/18—Evaporating by spraying to obtain dry solids
-
- 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
-
- 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
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents
- C11D11/04—Special methods for preparing compositions containing mixtures of detergents by chemical means, e.g. by sulfonating in the presence of other compounding ingredients followed by neutralising
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements for supplying or controlling air or other gases for drying solid materials or objects
- F26B21/20—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
- F26B21/25—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
- F26B3/10—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour carrying the materials or objects to be dried with it
- F26B3/12—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour carrying the materials or objects to be dried with it in the form of a spray, i.e. sprayed or dispersed emulsions or suspensions
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Microbiology (AREA)
- Detergent Compositions (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Drying Of Solid Materials (AREA)
- Glanulating (AREA)
Abstract
LOS GRANULADOS SE PRODUCEN A PARTIR DE SUS SOLUCIONES ACUOSAS Y/O SUSPENSIONES, MEDIANTE GRANULACION DE GRANULADO DE LECHO FLUIDIZADO EN UN GAS DE FLUIDIZACION CALIENTE EN LA ZONA DE PRESION NORMAL. SE UTILIZA VAPOR SOBRECALENTADO COMO AGENTE FLUIDIZANTE Y SE EVACUA EL GRANULADO A PARTIR DEL DISPOSITIVO DE GRANULACION ANTES DE QUE SE PRODUZCA EL RIESGO DE QUE SEA DAÑADO MEDIANTE EXPOSICION AL CALOR. SI SE REQUIERE, LA SOLTURA ESTABLE AL ALMACENAMIENTO Y LA CAPACIDAD DE FLUIR DE LA SUSTANCIA PARCIALMENTE SECADA SE ASEGURA MEDIANTE LA ADMINISTRACION DE COMPONENTES CON CAPACIDAD DE ENLACE DE CANTIDADES LIMITADAS DE AGUA Y/O MEDIANTE UN TRATAMIENTO SUBSECUENTE. EL SISTEMA ES UN SISTEMA CERRADO EN DONDE CIRCULA UNA CORRIENTE DE VAPOR, A PARTIR DEL CUAL EL AGUA EVAPORADA A PARTIR DE LA SUSTANCIA DEL PROCESO SE ARRASTRA COMO UNA CORRIENTE PARCIAL Y A LA QUE SE SUMINISTRA LA ENERGIA TERMICA LIBERADA. EL PROCESO ESTA LIBRE DE HUMOS DE EXHAUSTACION Y AGUAS RESIDUALES CONTAMINADAS, SIN QUE SE DISMINUYA LA CALIDAD DEL GRANULADO PRODUCIDO EN GRAN ESCALA.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4204035A DE4204035A1 (de) | 1992-02-12 | 1992-02-12 | Verbessertes verfahren zur trocknung von wertstoffen fuer wasch- und reinigungsmittel mit ueberhitztem wasserdampf |
| DE4204090A DE4204090A1 (de) | 1992-02-12 | 1992-02-12 | Vereinfachtes trocknungsverfahren fuer wertstoffe und wertstoffgemische aus dem bereich der wasch- und reinigungsmittel mit ueberhitztem wasserdampf |
| DE4206050A DE4206050A1 (de) | 1992-02-27 | 1992-02-27 | Neuartige staubarme aniontensidkonzentrate in pulver- beziehungsweise granulatform mit verbessertem aufloesevermoegen in waessrigen medien |
| DE4206521A DE4206521A1 (de) | 1992-03-02 | 1992-03-02 | Verfahren zur herstellung von granulaten, die als netz-, wasch- und/oder reinigungsmittel geeignet sind |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2086219T3 true ES2086219T3 (es) | 1996-06-16 |
Family
ID=27435391
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES93903908T Expired - Lifetime ES2086219T3 (es) | 1992-02-12 | 1993-02-04 | Procedimiento para la obtencion de granulados, que son adecuados como humectantes, agentes de lavado y/o agentes de limpieza. |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US5519948A (es) |
| EP (1) | EP0625921B1 (es) |
| JP (1) | JPH07503892A (es) |
| KR (1) | KR950700104A (es) |
| AT (1) | ATE135932T1 (es) |
| AU (1) | AU3494793A (es) |
| BR (1) | BR9305861A (es) |
| CA (1) | CA2130000A1 (es) |
| DE (1) | DE59302061D1 (es) |
| ES (1) | ES2086219T3 (es) |
| WO (1) | WO1993015813A1 (es) |
Families Citing this family (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1995014519A1 (de) * | 1993-11-24 | 1995-06-01 | Henkel Kommanditgesellschaft Auf Aktien | Verfahren zur herstellung wasserfreier, rieselfähiger zuckertensidpulver |
| DE4340015C2 (de) * | 1993-11-24 | 1996-07-04 | Henkel Kgaa | Verfahren zur Herstellung wasserfreier, rieselfähiger Zuckertensidpulver und deren Verwendung |
| GB9606913D0 (en) * | 1996-04-02 | 1996-06-05 | Unilever Plc | Surfactant blends processes for preparing them and particulate detergent compositions containing them |
| US6122841A (en) * | 1998-05-07 | 2000-09-26 | Asj Holding Aps | Apparatus for the drying of moist particulate material in superheated steam |
| DE19911040A1 (de) * | 1999-03-12 | 2000-09-21 | Cognis Deutschland Gmbh | Tensidgranulate |
| GB9913546D0 (en) | 1999-06-10 | 1999-08-11 | Unilever Plc | Granular detergent component containing zeolite map and laundry detergent compositions containing it |
| US20080000215A1 (en) * | 2000-03-02 | 2008-01-03 | Duncan Ronnie J | Engine systems and methods |
| DE10012949A1 (de) * | 2000-03-16 | 2001-09-27 | Henkel Kgaa | Kieselsäureester-Mischungen |
| US6837970B2 (en) * | 2001-12-18 | 2005-01-04 | Kimberly-Clark Worldwide, Inc. | Wood pulp fiber morphology modifications through thermal drying |
| DE10256530A1 (de) * | 2002-12-04 | 2004-06-24 | Degussa Ag | Verfahren zur Herstellung von wasserfreiem Alkalisulfid |
| US20040203308A1 (en) * | 2003-04-09 | 2004-10-14 | Ko Young Chan | Process for making absorbent material |
| DE102004019264B4 (de) | 2004-04-21 | 2008-04-10 | Stockhausen Gmbh | Verfahren zur Herstellung eines absorbierenden Polymers mittels Spreittrocknung |
| PT1793187E (pt) * | 2004-09-21 | 2012-03-05 | Joan Vives Iglesias | Processo e máquina destinados à sinterização e/ou secagem de materiais em pó utilizando uma radiação infravermelha |
| US20080005923A1 (en) * | 2006-07-07 | 2008-01-10 | Arthur Zwingenberger | Apparatus and method for drying instruments using superheated steam |
| WO2009065906A2 (de) * | 2007-11-20 | 2009-05-28 | Cognis Oleochemicals Gmbh | Verfahren zur herstellung einer organischen zusammensetzung beinhaltend einen n-nonylether |
| IL204790A (en) * | 2010-03-28 | 2014-07-31 | Airgreen Ltd | A method for processing and drying waste in a continuous circular process |
| AT514275B1 (de) * | 2013-05-07 | 2015-05-15 | Andritz Tech & Asset Man Gmbh | Verfahren zur Erzeugung von Salzen mit reduziertem Kristallwassergehalt |
| JP2017088426A (ja) * | 2015-11-04 | 2017-05-25 | 月島機械株式会社 | 塩化カルシウム水和物の造粒方法および塩化カルシウム水和物の造粒装置 |
| JP2019507671A (ja) * | 2015-12-11 | 2019-03-22 | ビーエーエスエフ ソシエタス・ヨーロピアBasf Se | 顆粒の製造方法 |
| JP6513299B2 (ja) * | 2017-02-09 | 2019-05-15 | 株式会社アルバック | 真空乾燥装置及び方法 |
| BR112022013825A2 (pt) * | 2020-01-13 | 2022-09-13 | Rio Tinto Alcan Int Ltd | Aparelho de calcinação e processo que usando hidrogênio |
| JP7836262B2 (ja) * | 2020-01-13 | 2026-03-26 | リオ ティント アルキャン インターナショナル リミテッド | 水素を使用する材料処理装置及びプロセス |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1787402A (en) * | 1927-02-25 | 1930-12-30 | Pilot Lab Inc | Bleaching agent and process of making the same |
| US2843942A (en) * | 1953-12-07 | 1958-07-22 | Phillips Petroleum Co | Process for drying wet carbon black pellets |
| US3212197A (en) * | 1961-06-08 | 1965-10-19 | James R Crawford | Drying method and apparatus |
| US3238634A (en) * | 1962-04-09 | 1966-03-08 | Phillips Petroleum Co | Process and apparatus for drying wet particulate solids |
| US4052794A (en) * | 1971-06-18 | 1977-10-11 | Struthers Scientific And International Corporation | Fluidized bed process |
| 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 |
| DE3565475D1 (en) * | 1984-04-07 | 1988-11-17 | Bayer Ag | Process and apparatus for the production of granules |
| JPS614795A (ja) * | 1984-06-18 | 1986-01-10 | Ebara Infilco Co Ltd | 有機性汚泥の固形燃料化方法 |
| US4793783A (en) * | 1987-01-20 | 1988-12-27 | The Dow Chemical Company | Apparatus for producing prills |
| DE3803109C2 (de) * | 1988-02-03 | 1998-10-08 | Eirich Maschf Gustav | Verfahren zum Trocknen von feuchtem Material |
| DE4030688A1 (de) * | 1990-09-28 | 1992-04-02 | Henkel Kgaa | Verfahren zur spruehtrocknung von wertstoffen und wertstoffgemischen unter verwendung von ueberhitztem wasserdampf |
-
1993
- 1993-02-04 KR KR1019940702787A patent/KR950700104A/ko not_active Withdrawn
- 1993-02-04 EP EP93903908A patent/EP0625921B1/de not_active Expired - Lifetime
- 1993-02-04 US US08/284,613 patent/US5519948A/en not_active Expired - Fee Related
- 1993-02-04 WO PCT/EP1993/000266 patent/WO1993015813A1/de not_active Ceased
- 1993-02-04 BR BR9305861A patent/BR9305861A/pt not_active Application Discontinuation
- 1993-02-04 CA CA002130000A patent/CA2130000A1/en not_active Abandoned
- 1993-02-04 DE DE59302061T patent/DE59302061D1/de not_active Expired - Fee Related
- 1993-02-04 AT AT93903908T patent/ATE135932T1/de not_active IP Right Cessation
- 1993-02-04 JP JP5513750A patent/JPH07503892A/ja active Pending
- 1993-02-04 AU AU34947/93A patent/AU3494793A/en not_active Abandoned
- 1993-02-04 ES ES93903908T patent/ES2086219T3/es not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07503892A (ja) | 1995-04-27 |
| CA2130000A1 (en) | 1993-08-19 |
| EP0625921B1 (de) | 1996-03-27 |
| US5519948A (en) | 1996-05-28 |
| KR950700104A (ko) | 1995-01-16 |
| DE59302061D1 (de) | 1996-05-02 |
| BR9305861A (pt) | 1997-02-18 |
| ATE135932T1 (de) | 1996-04-15 |
| WO1993015813A1 (de) | 1993-08-19 |
| AU3494793A (en) | 1993-09-03 |
| EP0625921A1 (de) | 1994-11-30 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG2A | Definitive protection |
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