EP1126017B1 - Verfahren zur Herstellung von Vollwaschmitteln und Vollwaschmittelkomponenten - Google Patents
Verfahren zur Herstellung von Vollwaschmitteln und Vollwaschmittelkomponenten Download PDFInfo
- Publication number
- EP1126017B1 EP1126017B1 EP00103515A EP00103515A EP1126017B1 EP 1126017 B1 EP1126017 B1 EP 1126017B1 EP 00103515 A EP00103515 A EP 00103515A EP 00103515 A EP00103515 A EP 00103515A EP 1126017 B1 EP1126017 B1 EP 1126017B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- fluidized bed
- product
- fluidised bed
- fluidising chamber
- components
- 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
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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
- C11D11/0082—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
- C11D11/0088—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 the liquefied ingredients being sprayed or adsorbed onto solid particles
-
- 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
- C11D11/02—Preparation in the form of powder by spray drying
Definitions
- the invention relates to a process for the preparation of heavy-duty detergents and heavy duty detergent components in granular or agglomerate form on a dry basis in a substantially horizontally oriented fluidized bed.
- the disadvantage is that, depending on the quality of the mixture of the individual components a more or less inhomogeneous distribution of different components takes place. During transport and at the Storage can easily cause segregation of the components within the packaging or the container come. Due to the high dust content and the tendency to segregate will increase the quality of the detergent or detergent components deteriorated considerably. This works are very disadvantageous because these dusts in the most common cases are classified as harmful to health. Furthermore, there is with decreasing particle size increases in tendency to Dust explosions.
- the object of the invention is to provide a method for Production of heavy-duty detergents and heavy-duty detergent components to develop in granular or agglomerated form on a dry matter basis, which is compared to the known granules by a homogeneous Composition of the granules or agglomerates of the individual Raw material components including the binder and the moisture characterized, a high resistance to mechanical stress has good water dispersibility and is low in dust are virtually dust-free.
- the product is produced by fluidized bed agglomeration / granulation in a substantially horizontal aligned fluidized bed.
- This is the solid in the Fluidized bed via a Bedüsungssystem a binder and / or Components in the form of solutions, suspensions or melts fed.
- the binder content in the product can be 1 to 35% by weight.
- Energy is a drying and solidification in the Bedüsungs Kunststoff the fluidized bed forming agglomerates / granules.
- the feed temperature of the process air is in between 20 ° C to the decomposition temperature of the substances involved.
- the process air from the fluidized bed entrained particles, in particular the fine dust, are in one in the Wirbe Anlagenapparat integrated with cross-sectional extensions provided expansion zone and in an adjoining Filter system separated from the air and into the fluidized bed returned and agglomerated there. This creates a low-dust or dust-free product with a grain size range of 0.2 to 2.00 mm.
- the process described above for the preparation of the final product is in different process stages, e.g. Heating up, agglomerating, Coating, drying and cooling in a row in a single or multistage fluidized bed performed.
- the advantage of the inventive method for the production of Heavy-duty detergents and heavy-duty detergent components in granules or Dry-based agglomerate form is that through the Fluidization of the material in the fluidized bed a uniform homogeneous composition of the individual granules or agglomerates from the individual raw material components including the binders and the corresponding moisture is created. A demixing of Components can no longer be done.
- the granules or agglomerate has a uniform quality.
- the production of granules or agglomerates by fluidized bed agglomeration / granulation has the further advantage that a firm, abriebarmes and low-dust end product is formed, the is readily dispersible in water.
- Another advantage of the method according to the invention is that by the perfect encapsulation of the process by process control a health hazard in a single apparatus Contact with the supplied dusts is avoided. In addition, will the area of dust explosion hazard on the interior of the Fluidized bed apparatus reduced.
- the process for the preparation of heavy duty detergents and heavy duty detergent components in granular or agglomerate form on a dry basis is done by Wirbarergesglomeration - / granulation one single- or multi-stage fluidized bed granulation plant, wherein the various process stages for the production of the final product such as Heating, agglomerating, coating, drying and cooling in a row be carried out in a fluidized bed 9.
- the powdery starting material is on the solids entry 2 and a rotary valve 12 as a pressure seal to the environment of first process stage in the field of the fluid space II of the fluidized bed fed.
- the supplied material goes through different process stages such as heating, agglomerating, coating, drying and cooling.
- process air 1 with different Temperatures over the Zu Kunststoffschn 10 and an air distribution floor 11 of the fluidized bed 9 fed.
- the supply air chambers form this 10 and the air distribution floor 11, as an upper limit, the Anströmteil 1, in which the process air 1 in the swirl space II introduced, distributed and evened out.
- the temperature of the process air 1 for the agglomeration of the product is dependent on the decomposition temperature of each introduced Substance components and lies according to the substance components between 20 to 300 ° C.
- the process air 1 for the cooling of the already granulated and dried material will be at the end of the process stages fed in front of the region of the product discharge 3.
- the temperature the process air 1 for cooling is between - 20 to + 30 ° C and also depends on the individual fabric components in the final product. This will give the process optimal conditions in the fluidized bed 9 by adjusting the respective layer temperature created.
- the vortex space II is in the lower area through the air distribution floor 11 with a substantially rectangular base and formed by vertical to slightly inclined side walls. there the side walls of the spinal space II can reach max. 10 ° from the Vertically inclined.
- the of the process air 1 is flowed through from bottom to top the fluidized solid forming the fluidized bed 9.
- the solid in the Fluidized bed 9 a binder, water and / or one or more Material components in the form of solutions, suspensions or melts fed.
- the dry matter content in the spray medium is 0 up to 100% while including the binder content in the final product Humidity is 1 to 35%.
- the spray system 8 consists of a known single or multi-fluid nozzle, where the injection direction from top to bottom or vice versa or can be inclined.
- the spray system 8 is a homogeneous solid mixture, wherein Granules with a homogeneous composition of the respective Individual components are formed.
- the expansion zone III closes on, in which the flow velocity of the process air 1 through Cross-sectional extensions is reduced.
- the side walls of the Expansion zone III show a strong inclination of 15-45 ° Vertical on, so that a cross-sectional widening to the subsequent filter system IV takes place.
- the expansion zone III is followed by an integrated filter system IV for dedusting the process air 1 and the simultaneous Return of the dust to the underlying fluidized bed 9 at.
- the filter system IV consists of filter elements 7, the mechanically through the filter cleaning 6 and / or by compressed air 5 can be cleaned impulsively. The use of other well-known Filter elements is possible. Due to the integrated filter system IV Contact with the dusts is avoided and the dust explosion hazard reduced to the interior of the fluidized bed apparatus.
- the purified process air leaves the system as exhaust 4 during the finished product also via a rotary valve 12 as Pressure completion via the product discharge 3 discharged from the system becomes.
- the system can be further equipment, such as Explosion Suppression / Relief or in Support of Solids movement e.g. by vibration devices, added become.
- detergent powder was ⁇ m agglomerated in a fluidized bed with two chambers in the upstream region and with a fluidization base area of 0.2 m 2 with a grain size smaller 200th 1.
- chamber agglomeration Supply air temperature 150 ° C
- Layer temperature 60 ° C
- Spraying medium 30% binder solution in the product 10% binder content 5% water content
- Second chamber cooling Cooling air temperature 25 ° C
- Outlet temperature of detergent agglomerate 35 ° C Distribution of the vortex area 75% agglomeration 25% cooling
- the invention relates to a process for the preparation of heavy-duty detergents and heavy duty detergent components in granular or agglomerate form on a dry basis in a substantially horizontally oriented fluidized bed.
- the object of the invention is to detergent granules or to produce agglomerates characterized by a homogeneous composition from the individual raw material components including the Binders and moisture are characterized by high strength have mechanical stress, good in water dispersible and low in dust to almost dust-free.
- this is achieved in that the production of the Product takes place in a fluidized bed.
- This is the solid in the fluidized bed via a Bedüsungssystem a binder and / or components in the form of solutions, suspensions or Melting supplied.
- Energy is a drying and solidification in the Bedüsungs Kunststoff the fluidized bed forming agglomerates / granules.
- the feed temperature of the process air is in between 20 ° C to the decomposition temperature of the substances involved.
- the entrained by the process air from the fluidized bed Particles are integrated in a fluidized bed apparatus Cross-sectional extensions provided expansion zone and in one subsequent filter system separated from the air and into the Fluidized bed returned and agglomerated there. This creates a dust-free or dust-free product with a grit area from 0.2 to 2.00 mm.
Description
1. | Kammer | Agglomeration |
Zulufttemperatur 150 °C | ||
Schichttemperatur 60 °C | ||
Sprühmedium 30 %ige Binderlösung | ||
im Produkt 10 % Binderanteil | ||
5 % Wasseranteil | ||
2. | Kammer | Kühlung |
Kühllufttemperatur 25° C | ||
Austrittstemperatur Waschmittelagglomerat 35 °C | ||
Aufteilung der Wirbelfläche | ||
75 % Agglomeration | ||
25 % Kühlung |
Claims (3)
- Verfahren zur Herstellung von Vollwaschmitteln und Vollwaschmittelkomponenten in Granulat- oder Agglomeratform auf Trockenstoffbasis in einer im wesentlichen horizontal ausgerichteten Wirbelschicht, dadurch gekennzeichnet,a) daß die verschiedenen Prozeßstufen zur Herstellung des Endproduktes wie z.B. Aufheizen, Agglomerieren, Coaten, Trocknen und Kühlen hintereinander in einer ein- oder mehrstufigen Wirbelschicht durchgeführt werden,b) daß das pulverförmige Ausgangsmaterial der ersten Prozeßstufe im Bereich des Wirbelraums der Wirbelschicht zugeführt wird,c) daß den verschiedenen Prozeßstufen unterhalb der Wirbelschicht die Prozeßluft zugeführt wird, wobei die Prozeß- bzw. Zulufttemperatur für die Agglomeration des Produktes abhängig von der Zersetzungstemperatur der einzelnen Stoffkomponenten des Endproduktes ist und 20 bis 300 °C und die Prozeßluft für die Kühlung - 20 bis + 30 °C beträgt,d) daß im Bereich des Wirbelraums über den gesamten Prozeßbereich mittels eines Sprüh- oder Bedüsungssystems dem Feststoff in der Wirbelschicht ein Bindemittel, Wasser und/oder ein oder mehrere Materialkomponenten in Form von Lösungen, Suspensionen oder Schmelzen zugeführt werden, wobei der Trockenstoffanteil im Sprühmedium 0 bis 100 % beträgt,e) daß im Bereich des Wirbelraums durch Fluidisierung eine Feststoffvermischung erfolgt und somit Granulate homogener Zusammensetzung aus den Einzelkomponenten gebildet werden,f) daß die Strömungsgeschwindigkeit der dem Wirbelraum von unten zugeführten Prozeßluft in der über dem Wirbelraum befindlichen Expansionszone durch Querschnittserweiterungen verringert wird, dabei eine Vorabscheidung von aus dem Wirbelraum mitgerissenen Partikeln und Rückführung der abgeschiedenen Partikel in den Wirbelraum erfolgt,g) daß die Abscheidung und Rückführung des Prozeßstaubes in den Wirbelraum in einem oberhalb der Expansionszone angrenzenden integrierten Filtersystem mit Abreinigungsmechanismus erfolgt.
- Verfahren nach Anspruch 1 dadurch gekennzeichnet, daß der Binderanteil im Produkt einschließlich Feuchte 1 bis 35 % beträgt.
- Verfahren nach Anspruch 1 und 2 dadurch gekennzeichnet, daß das Einbringen des Rohstoffes in die Wirbelschicht und der Austrag des Fertigproduktes aus der Wirbelschicht unter Druckabschluß zur Umgebung erfolgt.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK00103515T DK1126017T3 (da) | 2000-02-18 | 2000-02-18 | Fremgangsmåde til fremstilling af höjeffektive vaskemidler og komponenter i höjeffektive vaskemidler |
AT00103515T ATE307875T1 (de) | 2000-02-18 | 2000-02-18 | Verfahren zur herstellung von vollwaschmitteln und vollwaschmittelkomponenten |
EP00103515A EP1126017B1 (de) | 2000-02-18 | 2000-02-18 | Verfahren zur Herstellung von Vollwaschmitteln und Vollwaschmittelkomponenten |
DE50011442T DE50011442D1 (de) | 2000-02-18 | 2000-02-18 | Verfahren zur Herstellung von Vollwaschmitteln und Vollwaschmittelkomponenten |
US09/609,110 US6740632B1 (en) | 2000-02-18 | 2000-06-30 | Process for manufacturing industrial detergent and components thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP00103515A EP1126017B1 (de) | 2000-02-18 | 2000-02-18 | Verfahren zur Herstellung von Vollwaschmitteln und Vollwaschmittelkomponenten |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1126017A1 EP1126017A1 (de) | 2001-08-22 |
EP1126017B1 true EP1126017B1 (de) | 2005-10-26 |
Family
ID=8167894
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP00103515A Expired - Lifetime EP1126017B1 (de) | 2000-02-18 | 2000-02-18 | Verfahren zur Herstellung von Vollwaschmitteln und Vollwaschmittelkomponenten |
Country Status (5)
Country | Link |
---|---|
US (1) | US6740632B1 (de) |
EP (1) | EP1126017B1 (de) |
AT (1) | ATE307875T1 (de) |
DE (1) | DE50011442D1 (de) |
DK (1) | DK1126017T3 (de) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10221742A1 (de) * | 2002-05-16 | 2003-12-04 | Henkel Kgaa | Gerüststoffgranulate |
DE10322062A1 (de) * | 2003-05-15 | 2004-12-02 | Glatt Ingenieurtechnik Gmbh | Verfahren und Vorrichtung zum Aufbringen von Flüssigkeiten in eine Feststoffströmung eines Strahlschichtapparates |
DE10326231B4 (de) * | 2003-06-11 | 2016-04-07 | Glatt Ingenieurtechnik Gmbh | Verfahren zur Herstellung von Enzym-Granulaten |
PT1638678E (pt) * | 2003-06-11 | 2012-01-05 | Glatt Ingtech Gmbh | Método para produção de granulados enzimáticos e granulados enzimáticos assim obtidos |
US20080022940A1 (en) * | 2003-07-11 | 2008-01-31 | Bradley Kirsch | Composite Absorbent Particles with Superabsorbent Material |
US20080029039A1 (en) * | 2003-07-11 | 2008-02-07 | Dennis Jenkins | Dry Bed Agglomeration Process and Product Formed Thereby |
US20080251027A1 (en) * | 2003-07-11 | 2008-10-16 | Bradley Kirsch | Shaped Absorbent Particles |
US20090217882A1 (en) * | 2003-07-11 | 2009-09-03 | Dennis Jenkins | Dry Bed Agglomeration Process and Product Formed Thereby |
AU2005247060C1 (en) | 2004-05-24 | 2011-03-31 | Takeda As | Particulate comprising a calcium-containing compound and a sugar alcohol |
DE102004028883A1 (de) * | 2004-06-15 | 2006-01-05 | Glatt Ingenieurtechnik Gmbh | Verfahren zur Granulation von Malzextrakten |
CA2601755C (en) | 2005-02-03 | 2014-07-29 | Nycomed Pharma As | Melt granulation of a composition containing a calcium-containing compound |
CN103479582A (zh) | 2005-02-03 | 2014-01-01 | 武田奈科明有限公司 | 制备含钙组合物的快速湿聚结方法 |
MX2007010519A (es) * | 2005-03-04 | 2008-01-18 | Nycomed Pharma As | Proceso para la produccion de composiciones de calcio en un lecho fluido continuo. |
US8906411B2 (en) | 2005-12-07 | 2014-12-09 | Takeda Nycomed As | Pre-compacted calcium-containing compositions |
UA95093C2 (uk) | 2005-12-07 | 2011-07-11 | Нікомед Фарма Ас | Спосіб одержання кальцієвмісної сполуки |
US7776110B2 (en) | 2007-06-21 | 2010-08-17 | The Clorox Company | Agglomerated animal litter |
DE102007051093A1 (de) * | 2007-10-24 | 2009-04-30 | Henkel Ag & Co. Kgaa | Wasch- oder Reinigungsmittelcompounds und deren Herstellung |
US8277557B2 (en) * | 2009-08-07 | 2012-10-02 | Borregaard Industries Limited | Agglomerated particulate lignosulfonate |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1341557A (de) * | 1970-06-02 | 1973-12-25 | ||
US4323312A (en) * | 1977-08-26 | 1982-04-06 | Werner Glatt | Fluidized bed apparatus |
US4689297A (en) * | 1985-03-05 | 1987-08-25 | Miles Laboratories, Inc. | Dust free particulate enzyme formulation |
US4734290A (en) * | 1985-12-12 | 1988-03-29 | Mallinckrodt, Inc. | Process for preparing a coated-particle salt substitute composition |
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 |
EP0441092A1 (de) * | 1990-02-08 | 1991-08-14 | Niro Holding A/S | Verfahren und Vorrichtung zur Wärmebehandlung eines körnigen Produktes |
US5814501A (en) * | 1990-06-04 | 1998-09-29 | Genencor International, Inc. | Process for making dust-free enzyme-containing particles from an enzyme-containing fermentation broth |
DE4127323A1 (de) * | 1991-08-20 | 1993-02-25 | Henkel Kgaa | Verfahren zur herstellung von tensidgranulaten |
DE4304015A1 (de) | 1993-02-11 | 1994-08-18 | Henkel Kgaa | Verfahren zur Herstellung von Granulaten |
DK62994A (da) * | 1993-11-15 | 1995-05-16 | Niro Holding As | Apparat og fremgangsmåde til fremstilling af et agglomereret materiale |
DE4422607A1 (de) | 1994-06-28 | 1996-01-04 | Henkel Kgaa | Verfahren zum Herstellen von Granulaten in einer Wirbelschicht und Vorrichtung zum Durchführen des Verfahrens |
DE19524464C2 (de) * | 1995-07-10 | 2000-08-24 | Cognis Deutschland Gmbh | Verfahren zur Herstellung von Zuckertensidgranulaten |
DE19750424A1 (de) * | 1997-11-14 | 1999-05-20 | Henkel Kgaa | Verbessertes Verfahren zum Herstellen von Tensidgranulaten mit einem hohen Schüttgewicht |
-
2000
- 2000-02-18 DE DE50011442T patent/DE50011442D1/de not_active Expired - Lifetime
- 2000-02-18 AT AT00103515T patent/ATE307875T1/de active
- 2000-02-18 DK DK00103515T patent/DK1126017T3/da active
- 2000-02-18 EP EP00103515A patent/EP1126017B1/de not_active Expired - Lifetime
- 2000-06-30 US US09/609,110 patent/US6740632B1/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
EP1126017A1 (de) | 2001-08-22 |
DK1126017T3 (da) | 2006-02-06 |
US6740632B1 (en) | 2004-05-25 |
DE50011442D1 (de) | 2005-12-01 |
ATE307875T1 (de) | 2005-11-15 |
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