EP3625321B2 - Method for producing gel-like preparations - Google Patents

Method for producing gel-like preparations Download PDF

Info

Publication number
EP3625321B2
EP3625321B2 EP18720246.0A EP18720246A EP3625321B2 EP 3625321 B2 EP3625321 B2 EP 3625321B2 EP 18720246 A EP18720246 A EP 18720246A EP 3625321 B2 EP3625321 B2 EP 3625321B2
Authority
EP
European Patent Office
Prior art keywords
production line
batch production
premixture
filling
line
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.)
Active
Application number
EP18720246.0A
Other languages
German (de)
French (fr)
Other versions
EP3625321B1 (en
EP3625321A1 (en
Inventor
Uwe Trebbe
Harald Müller
Thomas Holderbaum
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Henkel AG and Co KGaA
Original Assignee
Henkel AG and Co KGaA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=62063074&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP3625321(B2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Henkel AG and Co KGaA filed Critical Henkel AG and Co KGaA
Priority to PL18720246T priority Critical patent/PL3625321T3/en
Publication of EP3625321A1 publication Critical patent/EP3625321A1/en
Publication of EP3625321B1 publication Critical patent/EP3625321B1/en
Application granted granted Critical
Publication of EP3625321B2 publication Critical patent/EP3625321B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00Special methods for preparing compositions containing mixtures of detergents
    • C11D11/0094Process for making liquid detergent compositions, e.g. slurries, pastes or gels
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/0008Detergent materials or soaps characterised by their shape or physical properties aqueous liquid non soap compositions
    • C11D17/003Colloidal solutions, e.g. gels; Thixotropic solutions or pastes
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/20Organic compounds containing oxygen
    • C11D3/2003Alcohols; Phenols
    • C11D3/2065Polyhydric alcohols

Definitions

  • EP2746379A1 discloses the production of liquid detergent preparations by mixing a perfume-free solution with a solution containing surfactant and perfume.
  • From the EN 10 2010 055 770 A1 is a process for producing cosmetic and/or dermatological emulsions in which all ingredients are mixed in several stages in a batch production line. The finished emulsion is then pumped to a filling line and filled.
  • a method for producing gel-form washing or cleaning agents comprises providing a premix on a batch production line, wherein the premix contains at least water, glycerin and surfactants.
  • the method further comprises adding supplements to the premix, wherein the supplements comprise at least fragrances, on a filling line following the batch production line.
  • supplements in particular fragrances
  • a filling line is understood here and below to be the part of a production line from which the finished product is filled, for example, into individual quantity containers.
  • Upstream of the filling line is the batch production line, in which all ingredients apart from the supplements are mixed and on which the almost finished product is held in a collecting container if necessary to be fed to the filling line.
  • a first starting mixture containing water, glycerin and liquid non-ionic surfactants and a second starting mixture containing at least fatty alcohol ethoxylates (FAEO) are provided to prepare the premix.
  • the two starting mixtures are mixed in a mixer of the batch production line. This can in particular be a static mixer.
  • the premix is provided on the batch production line at a temperature of at least 60 °C, in particular at least 75 °C.
  • a temperature of at least 60 °C, in particular at least 75 °C Such high temperatures on the batch production line have the advantage that the premix has a relatively low viscosity and the individual components can be mixed well.
  • the supplements are mixed on the filling line at temperatures of no more than 40°C.
  • the supplements can be mixed on the filling line at room temperature.
  • At least one colorant can also be added on the filling line.
  • the premix is divided after the batch production line into at least two parts which are further processed on different filling lines, wherein different supplements are added to a first part of the premix than to a second part.
  • This approach has the advantage that different branches of filling lines provide different end products. Production can therefore be varied in some parameters in the final section of filling by adding different additives. This has the advantage that production is particularly economical and flexible. In particular, cleaning effort and waste are reduced because the same premix on the batch production line can be used for different end products on different filling lines.
  • Figure 1 shows a production line 1 for producing gel-form washing or cleaning agents.
  • the production line 1 is divided into a batch production line 2 and a subsequent filling line 3.
  • a batch is produced, ie a large quantity of the washing or cleaning agent by mixing different starting substances.
  • the filling line 3 the finished washing or cleaning agent is filled, for example, into a number of individual quantity containers.
  • supplementary agents are also added on the filling line 3.
  • the gel-form detergent or cleaning agent is not yet finished, but a premix is provided which still has to be supplemented with the additives in order to obtain the finished gel-form detergent or cleaning agent.
  • a first starting mixture 4 is first provided.
  • the first starting mixture 4 contains at least water, glycerin and liquid non-ionic surfactants. This first starting mixture 4 is typically provided at a temperature of about 80 °C.
  • the components of the first starting mixture can be mixed statically or dynamically, for example by means of a planetary mixer. After mixing, the first starting mixture 4 can be kept in a collection container 5 for further steps.
  • a second starting mixture 6 is then added to the first starting mixture 4, the second starting mixture 6 containing fatty alcohol ethoxylates (FAEO).
  • the second starting mixture 6 is also typically provided at a temperature of 80 °C.
  • the first starting mixture 4 and the second starting mixture 6 are mixed in a mixer 7, in particular a static mixer, to provide the premix.
  • the finished premix is thus available at the outlet of the batch production line 2 at a temperature of 80 °C.
  • the premix can be divided into different branches.
  • the premix is divided into a first branch 8 and a second branch 9 of the filling line 3.
  • a first supplementary agent 10 is added to the premix and mixed with it in a mixer 11, in particular a static mixer.
  • the first supplementary agent 10 contains in particular at least one first fragrance.
  • the first supplementary agent 10 in the embodiment shown contains a first dye. This produces the gel-like washing or cleaning agent. It can be kept in a collecting container 12 for filling and, if necessary, circulated until filling.
  • a second supplementary agent 13 is added to the premix instead of the first supplementary agent 10.
  • a second supplementary agent 13 is used which comprises at least a second fragrance and a second colorant.
  • the second supplementary agent 13 is added to the premix at a temperature of 25°C in order to obtain the finished gel-like washing or cleaning agent with a second fragrance and a second colorant.
  • a collecting container 15 can also be provided in the second branch 9, in which the finished gel-like washing or cleaning agent is kept ready for filling and, if necessary, circulated.
  • Figure 2 shows a flow chart of the Figure 1 described method.
  • a first starting mixture 4 and a second starting mixture 6 are provided at temperatures of about 80 °C on the batch production line 2.
  • a second step 200 the two starting mixtures 4, 6 are mixed together, in particular by means of a static mixer 7.
  • a third step 300 the premix thus obtained is fed to a filling line 3 of the production line 1.
  • a fourth step 400 at least one supplementary agent 10, 13 is added to the premix on the filling line 3.
  • a fifth step 500 the finished gel-like washing or cleaning agent is filled.

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)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • Dispersion Chemistry (AREA)
  • Cosmetics (AREA)
  • Detergent Compositions (AREA)

Description

Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung gelförmiger Wasch- oder Reinigungsmittel. EP 2746379 A1 offenbart die Herstellung flüssiger Waschmittelzubereitungen durch Vermischen einer parfümfreien Lösung mit einer Tensid und Parfüm enthaltenden Lösung.The present invention relates to a process for producing gel-form washing or cleaning agents. EP2746379A1 discloses the production of liquid detergent preparations by mixing a perfume-free solution with a solution containing surfactant and perfume.

Aus der DE 10 2010 055 770 A1 ist ein Verfahren zur Herstellung kosmetischer und oder dermatologischer Emulsionen bekannt, bei dem sämtliche Inhaltsstoffe in mehreren Stufen in einer Chargenproduktionslinie vermischt werden. Anschließend wird die fertige Emulsion zu einer Abfülllinie gepumpt und abgefüllt.From the EN 10 2010 055 770 A1 is a process for producing cosmetic and/or dermatological emulsions in which all ingredients are mixed in several stages in a batch production line. The finished emulsion is then pumped to a filling line and filled.

Ein derartiges Vorgehen hat den Nachteil, dass die Produktion verhältnismäßig unflexibel ist. Zudem sind verschiedene empfindliche Inhaltsstoffe, insbesondere Duft- und Farbstoffe, für längere Zeit sehr hohen Temperaturen ausgesetzt. Dies führt zu einem teilweisen Verlust dieser Stoffe in der Produktionslinie. Zudem ist es häufig schwierig, wegen der hohen Viskosität zu vermischender Stoffe blasenfrei zu arbeiten. Teilweise wird zur Beseitigung von Blasen unter Vakuum gearbeitet, was jedoch ebenfalls zum Verlust flüchtiger Inhaltsstoffe, insbesondere Duftstoffe, führt.Such a procedure has the disadvantage that production is relatively inflexible. In addition, various sensitive ingredients, particularly fragrances and dyes, are exposed to very high temperatures for long periods of time. This leads to a partial loss of these substances in the production line. In addition, it is often difficult to work without bubbles due to the high viscosity of the substances to be mixed. In some cases, vacuum is used to eliminate bubbles, but this also leads to the loss of volatile ingredients, particularly fragrances.

Es ist eine Aufgabe der vorliegenden Erfindung, ein verbessertes Verfahren zur Herstellung gelförmiger Wasch- oder Reinigungsmittel bereitzustellen, bei dem die genannten Nachteile nicht auftreten.It is an object of the present invention to provide an improved process for producing gel-form washing or cleaning agents in which the aforementioned disadvantages do not occur.

Diese Aufgabe wird gelöst durch den Gegenstand des unabhängigen Patentanspruchs. Weitere Ausführungsformen sind Gegenstand der Unteransprüche.This object is achieved by the subject matter of the independent patent claim. Further embodiments are the subject matter of the subclaims.

Gemäß einer Ausführungsform der Erfindung umfasst ein Verfahren zur Herstellung gelförmiger Wasch- oder Reinigungsmittel das Bereitstellen einer Vormischung auf einer Chargenproduktionslinie, wobei die Vormischung zumindest Wasser, Glycerin und Tenside enthält. Das Verfahren umfasst ferner das Zumischen von Ergänzungsmitteln zur Vormischung, wobei die Ergänzungsmittel zumindest Duftstoffe umfassen, auf einer der Chargenproduktionslinie nachfolgenden Abfülllinie.According to one embodiment of the invention, a method for producing gel-form washing or cleaning agents comprises providing a premix on a batch production line, wherein the premix contains at least water, glycerin and surfactants. The method further comprises adding supplements to the premix, wherein the supplements comprise at least fragrances, on a filling line following the batch production line.

Erfindungsgemäß werden somit Ergänzungsmittel, insbesondere Duftstoffe, zu einem späten Zeitpunkt in der Produktion zudosiert, und zwar erst auf einer Abfülllinie. Unter einer Abfülllinie wird hier und im Folgenden derjenige Teil einer Produktionslinie verstanden, aus dem die Abfüllung des fertigen Produktes beispielsweise in Einzelmengenbehälter erfolgt. Der Abfülllinie vorgelagert ist die Chargenproduktionslinie, in der die Vermischung sämtlicher Inhaltsstoffe abgesehen von den Ergänzungsmitteln erfolgt und auf der das nahezu fertig gestellte Produkt gegebenenfalls in einem Sammelbehälter vorgehalten wird, um der Abfülllinie zugeführt zu werden.According to the invention, supplements, in particular fragrances, are added at a late stage in production, namely on a filling line. A filling line is understood here and below to be the part of a production line from which the finished product is filled, for example, into individual quantity containers. Upstream of the filling line is the batch production line, in which all ingredients apart from the supplements are mixed and on which the almost finished product is held in a collecting container if necessary to be fed to the filling line.

Durch das Zumischen von Ergänzungsmitteln erst unmittelbar vor der Abfüllung wird eine kontinuierliche kostengünstige Produktion erreicht, bei der eine Blasenbildung vermindert werden kann und bei der eine sehr schonende Zugabe empfindlicher Duftstoffe ermöglicht ist. Zudem ist das Verfahren besonders flexibel und der Reinigungsaufwand wird minimiert, da eine Variation des fertigen Produktes noch in der Abfülllinie durch eine Variation der dort zugegebenen Ergänzungsmittel möglich ist.By adding supplements immediately before filling, continuous, cost-effective production is achieved, which reduces the formation of bubbles and allows for the very gentle addition of sensitive fragrances. In addition, the process is particularly flexible and cleaning effort is minimized, as the finished product can be varied in the filling line by varying the supplements added there.

Erfindungsgemäß wird zur Bereitstellung der Vormischung eine erste Ausgangsmischung enthaltend Wasser, Glycerin und flüssige nichtionische Tenside und eine zweite Ausgangsmischung enthaltend zumindest Fettalkoholethoxylate (FAEO) bereitgestellt. Die beiden Ausgangsmischungen werden in einem Mischer der Chargenproduktionslinie gemischt. Dabei kann es sich insbesondere um einen statischen Mischer handeln.According to the invention, a first starting mixture containing water, glycerin and liquid non-ionic surfactants and a second starting mixture containing at least fatty alcohol ethoxylates (FAEO) are provided to prepare the premix. The two starting mixtures are mixed in a mixer of the batch production line. This can in particular be a static mixer.

Auf diese Weise ist die Vormischung besonders leicht zu verarbeiten und eine Blasenbildung wird minimiert.This makes the premix particularly easy to process and minimises the formation of bubbles.

Gemäß einer Ausführungsform wird die Vormischung mit einer Temperatur von mindestens 60 °C, insbesondere von mindestens 75 °C auf der Chargenproduktionslinie bereitgestellt. Derart hohe Temperaturen auf der Chargenproduktionslinie haben den Vorteil, dass die Vormischung eine verhältnismäßig geringe Viskosität aufweist und sich die einzelnen Bestandteile gut vermischen lassen.According to one embodiment, the premix is provided on the batch production line at a temperature of at least 60 °C, in particular at least 75 °C. Such high temperatures on the batch production line have the advantage that the premix has a relatively low viscosity and the individual components can be mixed well.

Gemäß einer Ausführungsform werden die Ergänzungsmittel mit Temperaturen von höchstens 40 °C auf der Abfülllinie zugemischt. Insbesondere können die Ergänzungsmittel mit Raumtemperatur auf der Abfülllinie zugemischt werden.According to one embodiment, the supplements are mixed on the filling line at temperatures of no more than 40°C. In particular, the supplements can be mixed on the filling line at room temperature.

Diese verhältnismäßig niedrigen Temperaturen haben den Vorteil, dass temperaturempfindliche Stoffe, insbesondere Duftstoffe, aber auch Farbstoffe, nicht über längere Zeit hohen Temperaturen ausgesetzt werden, die diese zerstören könnten.These relatively low temperatures have the advantage that temperature-sensitive substances, especially fragrances, but also dyes, are not exposed to high temperatures for long periods of time, which could destroy them.

Neben Duftstoffen kann auf der Abfülllinie auch zumindest ein Farbstoff zugemischt werden.In addition to fragrances, at least one colorant can also be added on the filling line.

Gemäß einer Ausführungsform wird die Vormischung nach der Chargenproduktionslinie in zumindest zwei Teile geteilt, die auf unterschiedlichen Abfülllinien weiter behandelt werden, wobei einem ersten Teil der Vormischung andere Ergänzungsmittel zugemischt werden als einem zweiten Teil.According to one embodiment, the premix is divided after the batch production line into at least two parts which are further processed on different filling lines, wherein different supplements are added to a first part of the premix than to a second part.

Dieses Vorgehen hat den Vorteil, dass verschiedene Zweige von Abfülllinien unterschiedliche Endprodukte bereitstellen. Die Produktion kann somit noch in dem letzten Abschnitt der Abfüllung in einigen Parametern variiert werden, in dem unterschiedliche Ergänzungsmittel zugefügt werden. Dies hat den Vorteil, dass die Produktion besonders ökonomisch und flexibel erfolgt. Insbesondere ist der Reinigungsaufwand und der Abfall reduziert dadurch, dass dieselbe Vormischung auf der Chargenproduktionslinie für unterschiedliche Endprodukte auf unterschiedlichen Abfülllinien verwendet werden kann.This approach has the advantage that different branches of filling lines provide different end products. Production can therefore be varied in some parameters in the final section of filling by adding different additives. This has the advantage that production is particularly economical and flexible. In particular, cleaning effort and waste are reduced because the same premix on the batch production line can be used for different end products on different filling lines.

Ausführungsformen der Erfindung werden im Folgenden anhand von Figuren näher beschrieben. Darin zeigen

Figur 1
schematisch eine Produktionslinie für gelförmige Wasch- oder Reinigungsmittel gemäß einem Verfahren gemäß einer Ausführungsform der Erfindung und
Figur 2
ein Ablaufdiagramm eines Verfahrens gemäß einer Ausführungsform der Erfindung.
Embodiments of the invention are described in more detail below with reference to figures.
Figure 1
schematically a production line for gel-form washing or cleaning agents according to a method according to an embodiment of the invention and
Figure 2
a flow chart of a method according to an embodiment of the invention.

Figur 1 zeigt eine Produktionslinie 1 zur Herstellung gelförmiger Wasch- oder Reinigungsmittel. Die Produktionslinie 1 gliedert sich in eine Chargenproduktionslinie 2 und eine nachfolgende Abfülllinie 3. In der Chargenproduktionslinie 2 erfolgt die Produktion einer Charge, d.h. einer Großmenge des Wasch- oder Reinigungsmittel durch Vermischen verschiedener Ausgangssubstanzen. In der Abfülllinie 3 erfolgt die Abfüllung des fertigen Wasch- oder Reinigungsmittels beispielsweise in eine Anzahl von Einzelmengenbehältern. Erfindungsgemäß erfolgt auf der Abfülllinie 3 zudem die Zumischung von Ergänzungsmitteln. Figure 1 shows a production line 1 for producing gel-form washing or cleaning agents. The production line 1 is divided into a batch production line 2 and a subsequent filling line 3. In the batch production line 2, a batch is produced, ie a large quantity of the washing or cleaning agent by mixing different starting substances. In the filling line 3, the finished washing or cleaning agent is filled, for example, into a number of individual quantity containers. According to the invention, supplementary agents are also added on the filling line 3.

Auf der Chargenproduktionslinie 2 wird demnach das gelförmige Wasch- oder Reinigungsmittel noch nicht fertiggestellt, sondern es wird eine Vormischung bereitgestellt, die noch durch die Ergänzungsmittel ergänzt werden muss, um das fertige gelförmige Wasch- oder Reinigungsmittel zu erhalten.On batch production line 2, the gel-form detergent or cleaning agent is not yet finished, but a premix is provided which still has to be supplemented with the additives in order to obtain the finished gel-form detergent or cleaning agent.

Auf der Chargenproduktionslinie 2 erfolgt zunächst die Bereitstellung einer ersten Ausgangsmischung 4. Die erste Ausgangsmischung 4 enthält zumindest Wasser, Glycerin und flüssige nichtionische Tenside. Diese erste Ausgangsmischung 4 wird typischerweise bei einer Temperatur von etwa 80 °C bereitgestellt. Das Vermischen der Bestandteile der ersten Ausgangsmischung kann statisch oder dynamisch beispielsweise mittels eines Planetenmischers erfolgen. Nach dem Vermischen kann die erste Ausgangsmischung 4 in einem Sammelbehälter 5 für weitere Schritte vorgehalten werden.On the batch production line 2, a first starting mixture 4 is first provided. The first starting mixture 4 contains at least water, glycerin and liquid non-ionic surfactants. This first starting mixture 4 is typically provided at a temperature of about 80 °C. The components of the first starting mixture can be mixed statically or dynamically, for example by means of a planetary mixer. After mixing, the first starting mixture 4 can be kept in a collection container 5 for further steps.

Anschließend erfolgt die Zumischung einer zweiten Ausgangsmischung 6 zu der ersten Ausgangsmischung 4, wobei die zweite Ausgangsmischung 6 Fettalkoholethoxylate (FAEO) enthält. Auch die zweite Ausgangsmischung 6 wird typischerweise bei einer Temperatur von 80 °C bereitgestellt. Die erste Ausgangsmischung 4 und die zweite Ausgangsmischung 6 werden in einem Mischer 7, insbesondere einem statischen Mischer, zur Bereitstellung der Vormischung vermischt. Somit steht am Ausgang der Chargenproduktionslinie 2 die fertige Vormischung mit einer Temperatur von 80 °C bereit.A second starting mixture 6 is then added to the first starting mixture 4, the second starting mixture 6 containing fatty alcohol ethoxylates (FAEO). The second starting mixture 6 is also typically provided at a temperature of 80 °C. The first starting mixture 4 and the second starting mixture 6 are mixed in a mixer 7, in particular a static mixer, to provide the premix. The finished premix is thus available at the outlet of the batch production line 2 at a temperature of 80 °C.

Auf der nachfolgenden Abfülllinie 3 kann die Vormischung auf verschiedene Zweige aufgeteilt werden. In der in Figur 1 gezeigten Ausführungsform wird die Vormischung in einen ersten Zweig 8 und einen zweiten Zweig 9 der Abfülllinie 3 aufgeteilt. In dem ersten Zweig 8 der Abfülllinie 3 wird ein erstes Ergänzungsmittel 10 zu der Vormischung zudosiert und mit dieser in einem Mischer 11, insbesondere einem statischen Mischer, vermischt. Das erste Ergänzungsmittel 10 enthält insbesondere zumindest einen ersten Duftstoff. Ferner enthält das erste Ergänzungsmittel 10 in der gezeigten Ausführungsform einen ersten Farbstoff. Damit ist das gelförmige Wasch- oder Reinigungsmittel erhalten. Es kann für die Abfüllung in einem Sammelbehälter 12 vorgehalten und gegebenenfalls bis zur Abfüllung in einem Kreislauf geführt werden.On the subsequent filling line 3, the premix can be divided into different branches. In the Figure 1 In the embodiment shown, the premix is divided into a first branch 8 and a second branch 9 of the filling line 3. In the first branch 8 of the filling line 3, a first supplementary agent 10 is added to the premix and mixed with it in a mixer 11, in particular a static mixer. The first supplementary agent 10 contains in particular at least one first fragrance. Furthermore, the first supplementary agent 10 in the embodiment shown contains a first dye. This produces the gel-like washing or cleaning agent. It can be kept in a collecting container 12 for filling and, if necessary, circulated until filling.

Im zweiten Zweig 9 der Abfülllinie 3 wird zu der Vormischung anstelle des ersten Ergänzungsmittels 10 ein zweites Ergänzungsmittel 13 zudosiert. In dem in Figur 1 gezeigten Ausführungsbeispiel wird ein zweites Ergänzungsmittel 13 verwendet, das zumindest einen zweiten Duftstoff und einen zweiten Farbstoff aufweist. Das zweite Ergänzungsmittel 13 wird bei einer Temperatur von 25 °C zu der Vormischung zudosiert, um das fertige gelförmige Wasch- oder Reinigungsmittel mit einem zweiten Duft und einer zweiten Färbung zu erhalten.In the second branch 9 of the filling line 3, a second supplementary agent 13 is added to the premix instead of the first supplementary agent 10. In the Figure 1 In the embodiment shown, a second supplementary agent 13 is used which comprises at least a second fragrance and a second colorant. The second supplementary agent 13 is added to the premix at a temperature of 25°C in order to obtain the finished gel-like washing or cleaning agent with a second fragrance and a second colorant.

Wie im ersten Zweig kann auch im zweiten Zweig 9 ein Sammelbehälter 15 vorgesehen sein, in dem das fertige gelförmige Wasch- oder Reinigungsmittel zur Abfüllung bereitgehalten und gegebenenfalls im Kreislauf geführt wird.As in the first branch, a collecting container 15 can also be provided in the second branch 9, in which the finished gel-like washing or cleaning agent is kept ready for filling and, if necessary, circulated.

Figur 2 zeigt ein Ablaufdiagramm des anhand von Figur 1 beschriebenen Verfahrens. In einem ersten Schritt 100 werden eine erste Ausgangsmischung 4 und eine zweite Ausgangsmischung 6 bei Temperaturen von etwa 80 °C auf der Chargenproduktionslinie 2 bereitgestellt. Figure 2 shows a flow chart of the Figure 1 described method. In a first step 100, a first starting mixture 4 and a second starting mixture 6 are provided at temperatures of about 80 °C on the batch production line 2.

In einem zweiten Schritt 200 werden die beiden Ausgangsmischungen 4, 6 miteinander vermischt, insbesondere mithilfe eines statischen Mischers 7.In a second step 200, the two starting mixtures 4, 6 are mixed together, in particular by means of a static mixer 7.

In einem dritten Schritt 300 wird die dadurch erhaltene Vormischung einer Abfülllinie 3 der Produktionslinie 1 zugeführt.In a third step 300, the premix thus obtained is fed to a filling line 3 of the production line 1.

Auf der Abfülllinie 3 erfolgt in einem vierten Schritt 400 das Zumischen zumindest eines Ergänzungsmittels 10, 13 zu der Vormischung. In einem fünften Schritt 500 erfolgt die Abfüllung des fertigen gelförmigen Wasch- oder Reinigungsmittels.In a fourth step 400, at least one supplementary agent 10, 13 is added to the premix on the filling line 3. In a fifth step 500, the finished gel-like washing or cleaning agent is filled.

BezugszeichenlisteList of reference symbols

11
Produktionslinieproduction line
22
ChargenproduktionslinieBatch production line
33
AbfülllinieFilling line
44
erste Ausgangsmischungfirst starting mixture
55
SammelbehälterCollection container
66
zweite Ausgangsmischungsecond output mix
77
Mischermixer
88th
erster Zweigfirst branch
99
zweiter Zweigsecond branch
1010
erste Ergänzungsmittelfirst supplements
1111
Mischermixer
1212
SammelbehälterCollection container
1313
zweite Ergänzungsmittelsecond supplements
1414
Mischermixer
1515
SammelbehälterCollection container
100100
SchrittStep
200200
SchrittStep
300300
SchrittStep
400400
SchrittStep
500500
SchrittStep

Claims (7)

  1. A method for preparing gel-like washing or cleaning agents, wherein the method comprises:
    - providing a premixture on a batch production line (2), the premixture containing at least water, glycerol and surfactants, and
    - admixing additives (10, 13) with the premixture, the additives (10, 13) comprising at least fragrances, on a filling line (3) downstream of the batch production line (2)
    wherein a first starting mixture (4) containing water, glycerol and liquid non-ionic surfactants and a second starting mixture (6) containing at least fatty alcohol ethoxylates are provided for preparing the premixture, and the two starting mixtures (4, 6) are mixed in a mixer (7) of the batch production line (2).
  2. The method according to claim 1, wherein the premixture is provided on the batch production line (2) at a temperature of at least 60 °C.
  3. The method according to one of claims 1 or 2, wherein the premixture is provided on the batch production line (2) at a temperature of at least 75 °C.
  4. The method according to one of claims 1 to 3, wherein the additives (10, 13) are admixed at temperatures of at most 40 °C on the filling line (3).
  5. The method according to one of claims 1 to 4, wherein the additives (10, 13) are admixed at room temperature on the filling line (3).
  6. The method according to one of claims 1 to 5, wherein, in addition to fragrances, at least one dye is also admixed on the filling line (3).
  7. The method according to one of claims 1 to 6, wherein, after the batch production line (2), the premixture is divided into at least two parts which are further treated on different filling lines (3), wherein different additives (10, 13) are admixed with a first part of the premixture than with a second part.
EP18720246.0A 2017-05-19 2018-04-26 Method for producing gel-like preparations Active EP3625321B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL18720246T PL3625321T3 (en) 2017-05-19 2018-04-26 Method for producing gel-like preparations

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102017208559.2A DE102017208559A1 (en) 2017-05-19 2017-05-19 Process for the preparation of gel substances
PCT/EP2018/060659 WO2018210542A1 (en) 2017-05-19 2018-04-26 Method for producing gel-like preparations

Publications (3)

Publication Number Publication Date
EP3625321A1 EP3625321A1 (en) 2020-03-25
EP3625321B1 EP3625321B1 (en) 2021-06-09
EP3625321B2 true EP3625321B2 (en) 2024-05-01

Family

ID=62063074

Family Applications (1)

Application Number Title Priority Date Filing Date
EP18720246.0A Active EP3625321B2 (en) 2017-05-19 2018-04-26 Method for producing gel-like preparations

Country Status (5)

Country Link
EP (1) EP3625321B2 (en)
DE (1) DE102017208559A1 (en)
ES (1) ES2880777T3 (en)
PL (1) PL3625321T3 (en)
WO (1) WO2018210542A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102021200796A1 (en) 2021-01-28 2022-07-28 Psa Automobiles Sa Storage system for an electric vehicle charging cable

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2606393B1 (en) 1986-11-10 1989-03-10 Erca METHOD AND INSTALLATION FOR FILLING CONTAINERS WITH A MIXTURE OF AT LEAST TWO PASTY AND / OR LIQUID PRODUCTS
GB2217341A (en) 1988-02-04 1989-10-25 Colgate Palmolive Co Thixotropic aqueous automatic dishwashing detergent composition
US5296157A (en) 1991-03-05 1994-03-22 The Proctor & Gamble Company Liquid soap personal cleanser with critical heat cycle stabilizing system
US5518645A (en) 1992-05-19 1996-05-21 Henkel Kommanditgesellschaft Auf Aktien Process for the production of paste-form detergents
US20040116539A1 (en) 2002-12-16 2004-06-17 Unilever Home & Personal Care Usa, Division Of Conopco, Inc. Late variant addition process for personal care products
US20040247534A1 (en) 2003-06-06 2004-12-09 Sultan Dental Products, Ltd Foamable fluoride gel compositions and methods of treatment using the same
JP2008031115A (en) 2006-07-31 2008-02-14 Sunstar Inc Method and apparatus for producing liquid composition
WO2010034736A1 (en) 2008-09-25 2010-04-01 Unilever Plc Liquid detergents
WO2012061991A1 (en) 2010-11-11 2012-05-18 Unilever Plc Leave-on nonsolid skin conditioning compositions containing 12-hydroxystearic acid

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102010055770A1 (en) 2010-12-23 2012-06-28 Beiersdorf Ag Preparing cosmetic and/or dermatological emulsion comprises adding one or more glucosylglycerides to an aqueous phase and/or an oil phase at a specified temperature, and combining the oil and aqueous phases
EP2746379B1 (en) * 2012-12-20 2017-03-29 The Procter & Gamble Company Process for the production of a liquid composition
EP3031891B1 (en) * 2014-12-12 2019-03-20 The Procter and Gamble Company A multi-compartment laundry detergent water-soluble pouch
BR112017018719A2 (en) * 2015-03-02 2018-04-17 Unilever Nv viscous scented cleaning fluid for substrate cleaning and method of manufacturing a viscous fluid cleaning composition for cleaning a substrate with a high flow viscosity

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2606393B1 (en) 1986-11-10 1989-03-10 Erca METHOD AND INSTALLATION FOR FILLING CONTAINERS WITH A MIXTURE OF AT LEAST TWO PASTY AND / OR LIQUID PRODUCTS
GB2217341A (en) 1988-02-04 1989-10-25 Colgate Palmolive Co Thixotropic aqueous automatic dishwashing detergent composition
US5296157A (en) 1991-03-05 1994-03-22 The Proctor & Gamble Company Liquid soap personal cleanser with critical heat cycle stabilizing system
US5518645A (en) 1992-05-19 1996-05-21 Henkel Kommanditgesellschaft Auf Aktien Process for the production of paste-form detergents
US20040116539A1 (en) 2002-12-16 2004-06-17 Unilever Home & Personal Care Usa, Division Of Conopco, Inc. Late variant addition process for personal care products
US20040247534A1 (en) 2003-06-06 2004-12-09 Sultan Dental Products, Ltd Foamable fluoride gel compositions and methods of treatment using the same
JP2008031115A (en) 2006-07-31 2008-02-14 Sunstar Inc Method and apparatus for producing liquid composition
WO2010034736A1 (en) 2008-09-25 2010-04-01 Unilever Plc Liquid detergents
WO2012061991A1 (en) 2010-11-11 2012-05-18 Unilever Plc Leave-on nonsolid skin conditioning compositions containing 12-hydroxystearic acid

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
"Handbook of Detergents", 1 January 2009, CRC PRESS, article BAYLY A. E., D. J. SMITH, NIGEL S. ROBERTS, DAVID W. YORK, S. CAPECI, URI ZOLLER, SOSIS P.: "Detergent Processing", pages: 323 - 331
"Perfumes, Cosmetics and Soaps", 1 January 1974, article HOWARD G M., POUCHER W. A.: "CHAPTER TWELVE The Skin-Preparations for the Face and Hands", pages: 310 - 401
"Waschmittel. Chemie, Umwelt, Nachhaltigkeit", 1 January 2005, WILEY-VCH, article WAGNER GÜNTER: "Herstellung von flüssigen Waschmitteln", pages: 140 - 142

Also Published As

Publication number Publication date
DE102017208559A1 (en) 2018-11-22
EP3625321B1 (en) 2021-06-09
WO2018210542A1 (en) 2018-11-22
ES2880777T3 (en) 2021-11-25
PL3625321T3 (en) 2021-10-04
EP3625321A1 (en) 2020-03-25

Similar Documents

Publication Publication Date Title
DE1617208A1 (en) Liquid detergent
WO2000001474A1 (en) Method for producing aqueous emulsions or suspensions
DE3411328A1 (en) NON-IONIC, FLOWABLE PEARL DISPERSIONS
DE102011018646A1 (en) Method and device for adding hops in beer production, as well as hop product
DE3820630A1 (en) HAIR RINSE CONDITIONER
DE3602089C3 (en) A durable, aqueous, pourable and water-dispersible fabric softening composition
EP3625321B2 (en) Method for producing gel-like preparations
EP0569376B1 (en) Liquid washing agents
EP0002506B1 (en) Use of compositions for conditioning as well as washing hair
DE1644952B1 (en) Process for the production of aqueous emulsions of highly viscous, hydrophobic oils
DE1089514B (en) Thixotropic agent for cleaning the skin, preferably without the use of additional water
EP1009787B1 (en) Method for producing aqueous solutions of alkyl ether sulfates
DE102005048606A1 (en) Coloring agent, useful for oxidative hair coloring, comprises oxidative dye precursor, fatty acid polyethyleneglycolamide, fatty acid monoethanolamide ester, glyceryl mono/di stearate and emulsifying agent
DE2731059B2 (en) Hair conditioning agents and processes for their preparation
DE2258953A1 (en) HAIRWASHING METHODS AND SHAMPOOS TO ITS IMPLEMENTATION
DE639733C (en) Process for the production of soaps containing chlorinated hydrocarbons
DE2404607A1 (en) SHAMPOO COMPOSITION
DE102018222066A1 (en) Process for the preparation of cosmetic emulsions comprising cold-pressed oils
DE344529C (en) Process for the production of hair coloring agents in the form of oils, pomades, ointments, thickened solutions or emulsions
DE943271C (en) Process for the production of a liquid gluten product, in particular for food purposes
DE19926925A1 (en) Process for the preparation of liquid cleaning or detergent compositions
DE19523459A1 (en) Skin or hair care prods, esp shower gels
DE309890C (en)
DE1494395C3 (en) Process for the production of pasteable polyvinyl chloride powder
DE761664C (en) Process for the manufacture of shaving soaps and other hair softening and removing agents

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: UNKNOWN

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

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

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20191030

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

DAV Request for validation of the european patent (deleted)
DAX Request for extension of the european patent (deleted)
GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

INTG Intention to grant announced

Effective date: 20210115

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

Ref country code: AT

Ref legal event code: REF

Ref document number: 1400520

Country of ref document: AT

Kind code of ref document: T

Effective date: 20210615

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502018005650

Country of ref document: DE

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG9D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210909

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20210609

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2880777

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20211125

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210910

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210909

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: RS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20211011

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

REG Reference to a national code

Ref country code: DE

Ref legal event code: R026

Ref document number: 502018005650

Country of ref document: DE

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

PLAX Notice of opposition and request to file observation + time limit sent

Free format text: ORIGINAL CODE: EPIDOSNOBS2

26 Opposition filed

Opponent name: THE PROCTER & GAMBLE COMPANY

Effective date: 20220309

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

PLBB Reply of patent proprietor to notice(s) of opposition received

Free format text: ORIGINAL CODE: EPIDOSNOBS3

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20220430

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220426

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220430

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220430

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220430

R26 Opposition filed (corrected)

Opponent name: THE PROCTER & GAMBLE COMPANY

Effective date: 20220309

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220426

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20230426

Year of fee payment: 6

Ref country code: FR

Payment date: 20230424

Year of fee payment: 6

Ref country code: ES

Payment date: 20230627

Year of fee payment: 6

Ref country code: DE

Payment date: 20230420

Year of fee payment: 6

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230705

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: PL

Payment date: 20230414

Year of fee payment: 6

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20230419

Year of fee payment: 6

APBM Appeal reference recorded

Free format text: ORIGINAL CODE: EPIDOSNREFNO

APBP Date of receipt of notice of appeal recorded

Free format text: ORIGINAL CODE: EPIDOSNNOA2O

APAH Appeal reference modified

Free format text: ORIGINAL CODE: EPIDOSCREFNO

APBU Appeal procedure closed

Free format text: ORIGINAL CODE: EPIDOSNNOA9O

REG Reference to a national code

Ref country code: CH

Ref legal event code: PK

Free format text: BERICHTIGUNGEN

Ref country code: CH

Ref legal event code: PK

Free format text: TITEL

RIC2 Information provided on ipc code assigned after grant

Ipc: C11D 1/825 20060101ALI20240129BHEP

Ipc: C11D 1/72 20060101ALI20240129BHEP

Ipc: C11D 3/50 20060101ALI20240129BHEP

Ipc: C11D 3/20 20060101ALI20240129BHEP

Ipc: C11D 17/00 20060101ALI20240129BHEP

Ipc: C11D 11/00 20060101AFI20240129BHEP

PUAH Patent maintained in amended form

Free format text: ORIGINAL CODE: 0009272

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: PATENT MAINTAINED AS AMENDED

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210609

27A Patent maintained in amended form

Effective date: 20240501

AK Designated contracting states

Kind code of ref document: B2

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

REG Reference to a national code

Ref country code: DE

Ref legal event code: R102

Ref document number: 502018005650

Country of ref document: DE