EP0758374A1 - Heterogene tensidgranulate - Google Patents
Heterogene tensidgranulateInfo
- Publication number
- EP0758374A1 EP0758374A1 EP95918598A EP95918598A EP0758374A1 EP 0758374 A1 EP0758374 A1 EP 0758374A1 EP 95918598 A EP95918598 A EP 95918598A EP 95918598 A EP95918598 A EP 95918598A EP 0758374 A1 EP0758374 A1 EP 0758374A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- alkyl
- formula
- weight
- sulfates
- carbon atoms
- 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.)
- Granted
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
- 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
- C11D1/14—Sulfonic acids or sulfuric acid esters; Salts thereof derived from aliphatic hydrocarbons or mono-alcohols
- C11D1/146—Sulfuric acid esters
-
- 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
- C11D1/37—Mixtures of compounds all of which are anionic
-
- 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
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
- C11D17/0039—Coated compositions or coated components in the compositions, (micro)capsules
-
- 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
- C11D1/14—Sulfonic acids or sulfuric acid esters; Salts thereof derived from aliphatic hydrocarbons or mono-alcohols
-
- 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
- C11D1/29—Sulfates of polyoxyalkylene ethers
Definitions
- the invention relates to heterogeneous surfactant granules with an inner grain consisting of longer-chain alkyl sulfates or their mixtures with shorter-chain homologs or alkyl ether sulfates and a coating of shorter-chain alkyl sulfates.
- Another object of the invention is directed to a method for producing the heterogeneous surfactant granules.
- Anionic surfactants especially alkyl sulfates or fatty alcohol sulfates, are important components of detergents, dishwashing detergents and cleaning agents.
- anionic surfactants behave conventionally , ie their solubility increases more or less linearly with temperature until the solubility product is reached.
- anionic surfactants that have sufficient solubility, especially in cold water.
- the best-known hydrotropes undoubtedly include the short-chain alkylarylsulfonates, such as, for example, toluene, xylene or cumene sulfonate. They are suitable, for example, as solubilizers for anionic and nonionic surfactants in the production of liquid detergents.
- solubilizers for anionic and nonionic surfactants in the production of liquid detergents The improved solubility is probably due to advantageous mixed micelle formation.
- solubility in cold water in particular of fatty alcohol sulfates
- hydrotrope surfactants with high HLB values, for example highly ethoxylated polyglycol ethers (tallow alcohol 40 EO adduct) or the like.
- HLB values for example highly ethoxylated polyglycol ethers (tallow alcohol 40 EO adduct) or the like.
- German patent application DE-Al 4030688 (Henkel). It is proposed here to dry aqueous surfactant pastes using hot steam. Condensation of the superheated steam on the cooler feed and release of the heat of condensation to the material to be dried results in the surfactant droplets heating up spontaneously to the boiling point of the water. As a result, a multitude of fine channels form in the tenside grain when the water escapes. The resulting high internal surface area - for example compared to conventional spray-dried products - leads to a significantly improved dissolution rate. Nevertheless, there is the disadvantage that the method described is associated with a high level of technical complexity.
- solid detergents with high apparent density and improved solubility are obtained by adding mixtures of anionic and nonionic surfactants to polyethylene glycol ethers with a molecular weight in the range from 200 to 12,000, preferably 200 to 600, and then drying and / or in solid form.
- a detergent preparation containing C 12/18 fatty alcohol sulfate is
- spray-dried detergent compositions are disclosed in general form which, in addition to anionic surfactants, contain nonionic surfactants, polyacrylates and polyethylene glycol ethers with an average molecular weight in the range from 1,000 to 20,000.
- the teaching of this document is that the dispersibility of anionic surfactants can be improved by adding nonionic surfactants, polyethylene glycol ethers and polyacrylates to them.
- DE-OS 2124526 relates to detergent and cleaning agent mixtures with controlled foam behavior. According to Example 6, compositions are disclosed which contain tallow alcohol sulfate, alkylbenzenesulfonate and polyethylene glycol with a molecular weight of approximately 20,000.
- solid detergents are known from international patent application WO 92/09676 (Henkel), which are obtained by treating aqueous alkyl sulfate pastes with soda and zeolites and then extruding them. The document does not reveal anything about the dissolution rate of the solids.
- the object of the invention was to provide new forms of alkyl sulfate, which are light-colored even after mechanical compression and show improved solubility in cold water.
- the invention relates to heterogeneous surfactant granules consisting of an inner grain containing a) alkyl sulfates of the formula (I)
- R 1 is an alkyl radical having 16 to 18 carbon atoms and X is an alkali or alkaline earth metal, ammonium, alkylammonium, alkanolammonium or glucammonium, and b1) alkyl sulfates of the formula (II),
- the new teaching now consists in the surprising finding that a structured, ie heterogeneous, alkyl sulfate grain with further improved solubility can be obtained by granulating with an inner grain which contains the longer-chain alkyl sulfate, optionally in admixture with shorter-chain homologues or selected alkyl ether sulfates coated with a short-chain alkyl sulfate of a defined layer thickness.
- the invention further relates to a process for the preparation of heterogeneous surfactant granules, in which a dry anionic surfactant powder containing a) 30 to 100, preferably 70 to 90,% by weight of alkyl sulfates of the formula (I)
- R 1 O-SO 3 X in which R 1 represents an alkyl radical having 16 to 18 carbon atoms and X represents an alkali or alkaline earth metal, ammonium, alkylammonium, alkanolammonium or glucammonium, and bl) 0 to 70, preferably 10 to 30% by weight of alkyl sulfates of the formula (II),
- Alkyl sulfates and alkyl ether sulfates are to be understood as meaning the sulfation products of primary alcohols or their ethylene oxide adducts.
- alkyl sulfates with 16 to 18 carbon atoms, which have particularly advantageous washing properties, are suitable as component a).
- Typical examples of this are cetyl sulfate and steryl sulfate and preferably tallow alkyl sulfate or technical mixtures of comparable composition.
- component a) can make up 100% by weight of the inner grain.
- a mixture is preferably used which, in addition to component a), either has shorter-chain alkyl sulfates with 12 to 14 carbon atoms (component b1) and / or alkyl ether sulfates with 16 to 18 carbon atoms and 1 to 3, preferably about 2, ethylene oxide units (component b2).
- the weight ratio between components a) and b) is usually in the range from 70:30 to 98: 2 and is preferably 80:20 to 90:10.
- the coating of the inner grain again consists of shorter-chain alkyl sulfates with 12 to 14 carbon atoms.
- Typical examples are lauryl sulfate, myristyl sulfate or technical mixtures based, for example, on a coconut fatty alcohol cut.
- the granulation is carried out in such a way that a coating with a layer thickness corresponding to 0.5 to 10, preferably 1 to 5 and in particular 1.5 to 2% by weight, based on the granulate, results.
- alkyl sulfates of component a) and in particular of component b1) are used which have a degree of sulfonation of 60 to 80 and preferably of about 70% by weight and thus still contain a noticeable proportion of unsulfated starting materials.
- the invention includes the knowledge that such undersulfurized alkyl sulfates as coatings for the inner surfactant grain lead to a particularly light color.
- the substances that make up component a), ie the inner grain, alone or as a mixture, are used as dry powders.
- a dry tallow alkyl sulfate powder for example, an aqueous sulfuric acid half ester of a corresponding tallow alcohol can be subjected to spray neutralization following sulfation. It is also possible to dry a neutralized aqueous paste in a conventional spray tower or using superheated steam (cf. DE-Al 4124701, Henkel). If a mixture of the C 16/18 alkyl sulfates with the If components b1) and / or b2) are desired, these can be prepared either mechanically by mixing the ingredients or by cosulfating the corresponding hydroxyl compounds.
- the sulfates are usually present as alkali metal salts and preferably as sodium salts.
- the granulation can be carried out continuously or batchwise in a conventional manner in a mixer with a drying device such as, for example, a Lödige mixer, Drais mixer, Schugi mixer or Fukai mixer or else a fluidized bed.
- a drying device such as, for example, a Lödige mixer, Drais mixer, Schugi mixer or Fukai mixer or else a fluidized bed.
- the heterogeneous surfactant granulate is produced by coating a C 16/18 tallow alkyl sulfate powder with C 12/14 coconut alkyl sulfate using water as the granulating liquid.
- tallow alkyl sulfate powder or a powdery mixture of tallow alkyl sulfate and lauryl sulfate or tallow alkyl 2EO sulfate (weight ratio 90:10) is coated with a 35 or 65% strength by weight aqueous paste of lauryl sulfate.
- the surfactant granules according to the invention have rapid solubility in both cold and warm water and improved washing-up behavior in the washing machine. Another advantage is that in the course of their mechanical compression there is no adverse effect on their color quality.
- the surfactant granules according to the invention can be mixed with other detergent constituents or can also be agglomerated or extruded and are accordingly suitable as raw materials for the production of solid detergents.
- Example 2 An acidic sulfuric acid half ester based on C 16/18 tallow alcohol and C 12/14 coconut fatty alcohol (weight ratio 90:10) was subjected to spray neutralization. The dried powdered C 12/18 fatty alkanol sulfate sodium salt was then processed with the addition of water in a Lödige mixer to form a granulate.
- Example 2 An acidic sulfuric acid half ester based on C 16/18 tallow alcohol and C 12/14 coconut fatty alcohol (weight ratio 90:10) was subjected to spray neutralization. The dried powdered C 12/18 fatty alkanol sulfate sodium salt was then processed with the addition of water in a Lödige mixer to form a granulate.
- Example 2 An acidic sulfuric acid half ester based on C 16/18 tallow alcohol and C 12/14 coconut fatty alcohol (weight ratio 90:10) was subjected to spray neutralization. The dried powdered C 12/18 fatty alkanol sulfate sodium salt was then processed with
- Comparative example V1 was repeated. Instead of water, an aqueous paste of lauryl sulfate sodium salt with a solids content of 35% by weight (Texapon (R) LS35, Henkel KGaA, Duesseldorf / FRG) was used. The weight ratio between the inner grain and the coating was 1.5% by weight, based on the solids content of the granulating liquid.
- Texapon (R) LS35 Henkel KGaA, Duesseldorf / FRG
- Comparative example V1 was repeated. Instead of water, an aqueous paste of lauryl sulfate sodium salt with a solids content of 35% by weight (Texapon (R) LS35, Henkel KGaA, Duesseldorf / FRG) was used. The weight ratio between the inner grain and the coating was 2.5% by weight, based on the solids content of the granulating liquid.
- Texapon (R) LS35 Henkel KGaA, Duesseldorf / FRG
- Comparative example V1 was repeated. Instead of water, an aqueous paste of lauryl sulfate sodium salt with a solids content of 65% by weight (Texapon (R) LS65, Henkel KGaA, Düsseldorf / FRG) was used. The weight ratio between the inner grain and the coating was 1.5% by weight, based on the solids content of the granulating liquid.
- Example 5
- aqueous paste of C 16/18 tallow alkyl sulfate sodium salt with a solids content of about 50% by weight was subjected to conventional spray drying.
- the water-free powder was mixed in a weight ratio of 90:10 with a spray-neutralized powder of C 12/14 coconut alkyl sulfate sodium salt and then with the addition of an aqueous paste of lauryl sulfate sodium salt with a solids content of 35% by weight (Texapon (R) LS35, Henkel KGaA, Düsseldorf / FRG) granulated in a Lödige mixer.
- the weight ratio between the inner grain and the coating was 1.5% by weight, based on the solids content of the granulating liquid.
- Example 5 was repeated, but instead of the coconut alkyl sulfate, C 16/18 tallow alcohol 2EO sulfate sodium salt was used.
- a jump-dried mixed powder consisting of C 16/18 tallow alkyl sulfate, C 12/14 coconut alkyl sulfate and C 16/18 tallow alcohol 1EO sulfate (in each case in the form of the sodium salts, weight ratio 35:25:40) was added to a Lödige mixer Granulated addition of an aqueous paste of lauryl sulfate sodium salt with a solids content of 35% by weight. The weight ratio between the inner grain and the coating was 2% by weight, based on the solids content of the granulating liquid.
- Example 8 Example 8:
- Example 5 was repeated, but steam-dried material was used instead of the spray-dried tallow alkyl sulfate.
- the particle size of all the granules examined was at least 90% by weight in the range from 0.2 to 1.4 mm.
- Example 5 was repeated, but granules of different particle size distribution were produced by varying the mixer speed, mass flow and mixing time. The results are summarized in Table 2:
Abstract
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4415369A DE4415369C1 (de) | 1994-05-02 | 1994-05-02 | Heterogene Tensidgranulate |
DE4415369 | 1994-05-02 | ||
PCT/EP1995/001544 WO1995029981A1 (de) | 1994-05-02 | 1995-04-24 | Heterogene tensidgranulate |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0758374A1 true EP0758374A1 (de) | 1997-02-19 |
EP0758374B1 EP0758374B1 (de) | 1999-08-11 |
Family
ID=6517038
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP95918598A Expired - Lifetime EP0758374B1 (de) | 1994-05-02 | 1995-04-24 | Heterogene tensidgranulate |
Country Status (5)
Country | Link |
---|---|
US (1) | US5824633A (de) |
EP (1) | EP0758374B1 (de) |
DE (2) | DE4415369C1 (de) |
ES (1) | ES2136851T3 (de) |
WO (1) | WO1995029981A1 (de) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4432365A1 (de) * | 1994-09-12 | 1996-03-14 | Henkel Kgaa | Wasserfreie Tensidgemische |
US6174849B1 (en) * | 1996-10-30 | 2001-01-16 | Henkel Kommanditgesellschaft Auf Aktien | Water-free surfactant mixtures containing alcohol sulfates |
DE19648014C2 (de) * | 1996-11-20 | 2002-09-19 | Cognis Deutschland Gmbh | Wasserfreie Tensidgemische |
DE19820943A1 (de) * | 1998-05-11 | 1999-11-18 | Henkel Kgaa | Alkylsulfat-Granulate |
DE19941934A1 (de) * | 1999-09-03 | 2001-03-15 | Cognis Deutschland Gmbh | Detergentien in fester Form |
DE10120263A1 (de) * | 2001-04-25 | 2002-10-31 | Cognis Deutschland Gmbh | Feste Tensidzusammensetzungen, deren Herstellung und Verwendung |
EP1788071B1 (de) * | 2004-08-06 | 2013-06-12 | Kao Corporation | Herstellungsverfahren für einkernige waschmittelteilchen |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
LU60943A1 (de) * | 1970-05-20 | 1972-02-23 | ||
DE2558593C2 (de) * | 1975-12-24 | 1985-07-25 | Henkel KGaA, 4000 Düsseldorf | Pulverförmige, in ihrem Benetzungsverhalten verbesserte Wasch- und Reinigungsmittel, sowie Verfahren zu deren Herstellung |
CA1293421C (en) * | 1985-07-09 | 1991-12-24 | Mark Edward Cushman | Spray-dried granular detergent compositions containing nonionicsurfactant, polyethylene glycol, and polyacrylate |
US4657784A (en) * | 1986-03-10 | 1987-04-14 | Ecolab Inc. | Process for encapsulating particles with at least two coating layers having different melting points |
GB8625104D0 (en) * | 1986-10-20 | 1986-11-26 | Unilever Plc | Detergent compositions |
GB8811672D0 (en) * | 1988-05-17 | 1988-06-22 | Unilever Plc | Detergent composition |
GB8818613D0 (en) * | 1988-08-05 | 1988-09-07 | Paterson Zochonis Uk Ltd | Detergents |
US5215683A (en) * | 1989-04-26 | 1993-06-01 | Shell Oil Company | Highly concentrated liquid surface active compositions containing alcohol ethoxylate and alcohol ethoxysulfate |
DE4030688A1 (de) * | 1990-09-28 | 1992-04-02 | Henkel Kgaa | Verfahren zur spruehtrocknung von wertstoffen und wertstoffgemischen unter verwendung von ueberhitztem wasserdampf |
DE4038476A1 (de) * | 1990-12-03 | 1992-06-04 | Henkel Kgaa | Feste waschmittel |
DE4124701A1 (de) * | 1991-07-25 | 1993-01-28 | Henkel Kgaa | Verfahren zur herstellung fester wasch- und reinigungsmittel mit hohem schuettgewicht und verbesserter loesegeschwindigkeit |
DE4203031A1 (de) * | 1992-02-04 | 1993-08-05 | Henkel Kgaa | Verfahren zur herstellung fester wasch- und reinigungsmittel mit hohem schuettgewicht und verbesserter loesegeschwindigkeit |
DE4242185A1 (de) * | 1992-12-15 | 1994-06-16 | Henkel Kgaa | Granulare Wasch- und Reinigungsmittel mit hohem Tensidgehalt |
US5443751A (en) * | 1993-03-05 | 1995-08-22 | Church & Dwight Co. Inc. | Powder detergent composition for cold water washing of fabrics |
US5482646A (en) * | 1993-03-05 | 1996-01-09 | Church & Dwight Co., Inc. | Powder detergent composition for cold water laundering of fabrics |
WO1995002390A1 (en) * | 1993-07-12 | 1995-01-26 | The Procter & Gamble Company | Surfactant system |
DE4403323A1 (de) * | 1993-09-23 | 1995-08-10 | Henkel Kgaa | Extrudierte Wasch- oder Reinigungsmittel mit verbesserten Löseeigenschaften |
-
1994
- 1994-05-02 DE DE4415369A patent/DE4415369C1/de not_active Expired - Fee Related
-
1995
- 1995-04-24 EP EP95918598A patent/EP0758374B1/de not_active Expired - Lifetime
- 1995-04-24 ES ES95918598T patent/ES2136851T3/es not_active Expired - Lifetime
- 1995-04-24 US US08/732,422 patent/US5824633A/en not_active Expired - Fee Related
- 1995-04-24 DE DE59506594T patent/DE59506594D1/de not_active Expired - Fee Related
- 1995-04-24 WO PCT/EP1995/001544 patent/WO1995029981A1/de active IP Right Grant
Non-Patent Citations (1)
Title |
---|
See references of WO9529981A1 * |
Also Published As
Publication number | Publication date |
---|---|
WO1995029981A1 (de) | 1995-11-09 |
EP0758374B1 (de) | 1999-08-11 |
US5824633A (en) | 1998-10-20 |
DE4415369C1 (de) | 1995-08-31 |
ES2136851T3 (es) | 1999-12-01 |
DE59506594D1 (de) | 1999-09-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0541608B1 (de) | Verfahren zur herstellung wasch- und reinigungsaktiver granulate | |
WO1995007975A1 (de) | Stückseifen | |
EP0538294B1 (de) | Verfahren zur herstellung wasch- und reinigungsaktiver tensidgranulate | |
WO2011117079A1 (de) | Wasch-, reinigungs- oder vorbehandlungsmittel mit erhöhter fettlösekraft | |
DE2810703A1 (de) | Nichtiogenes tensid | |
DE2551111A1 (de) | Granulierte oder pulverige reinigungsmittelmischung | |
WO1992015660A1 (de) | Flüssige reinigungsmittel mit einem gehalt an sulfoölsauren disalzen | |
EP0758374B1 (de) | Heterogene tensidgranulate | |
DE2204568B2 (de) | ||
DE4332373C2 (de) | Wasserfreie Detergensgemische | |
EP0682690B1 (de) | Anionische tenside mit verbesserter löslichkeit | |
EP0682691B1 (de) | Feste, wasserfreie waschmittel | |
EP0863972A1 (de) | Wässrige tensidmischung | |
DE19543990C2 (de) | Flüssige Vorprodukte für Wasch-, Spül- und Reinigungsmittel | |
DE60117815T2 (de) | Schmelzmischverfahren zur herstellung von syndetseifenriegeln | |
DE69729964T2 (de) | Verfahren zur herstellung einer waschmittelzusammensetzung durch zugabe von cotensiden | |
DE19520105A1 (de) | Verfahren zur Herstellung wasserfreier, rieselfähiger Tensidpulver | |
DE19806496C2 (de) | Syndetseifen | |
WO1998015606A2 (de) | Syndetseifen | |
WO1994014943A1 (de) | Neutrales wischpflegemittel (ii) | |
WO1998018889A2 (de) | Wasserfreie tensidgemische | |
WO1996008550A1 (de) | Wasserfreie tensidgemische | |
EP1157087A1 (de) | Reinigungsmittel für harte oberflächen |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19961024 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): DE ES FR GB IT NL |
|
17Q | First examination report despatched |
Effective date: 19971210 |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE ES FR GB IT NL |
|
REF | Corresponds to: |
Ref document number: 59506594 Country of ref document: DE Date of ref document: 19990916 |
|
ET | Fr: translation filed | ||
ITF | It: translation for a ep patent filed |
Owner name: STUDIO JAUMANN P. & C. S.N.C. |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2136851 Country of ref document: ES Kind code of ref document: T3 |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 19991112 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
REG | Reference to a national code |
Ref country code: GB Ref legal event code: IF02 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: 732E |
|
NLS | Nl: assignments of ep-patents |
Owner name: COGNIS DEUTSCHLAND GMBH & CO. KG |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: TP |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 20070403 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20070419 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20070521 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20070418 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20070601 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20070411 Year of fee payment: 13 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20080424 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 20081101 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20081101 Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20081101 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20081231 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20080430 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20080425 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20080424 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20080425 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20080424 |