[go: up one dir, main page]

WO2011121157A1 - Peroxide-activating composition for cold washing, preparation method thereof and use of same - Google Patents

Peroxide-activating composition for cold washing, preparation method thereof and use of same Download PDF

Info

Publication number
WO2011121157A1
WO2011121157A1 PCT/ES2011/070185 ES2011070185W WO2011121157A1 WO 2011121157 A1 WO2011121157 A1 WO 2011121157A1 ES 2011070185 W ES2011070185 W ES 2011070185W WO 2011121157 A1 WO2011121157 A1 WO 2011121157A1
Authority
WO
WIPO (PCT)
Prior art keywords
transition metal
aluminosilicate support
impregnated
present
aluminosilicate
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.)
Ceased
Application number
PCT/ES2011/070185
Other languages
Spanish (es)
French (fr)
Inventor
Ramon Artigas Puerto
Manuel Cordero Sanchez
Miguel Angel Fernandez Fonseca
Hermenegildo Garcia Gomez
Esther Dominguez Torres
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.)
FMC Foret SA
Original Assignee
FMC Foret SA
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
Application filed by FMC Foret SA filed Critical FMC Foret SA
Publication of WO2011121157A1 publication Critical patent/WO2011121157A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/061Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing metallic elements added to the zeolite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/076Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/064Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing iron group metals, noble metals or copper
    • 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
    • C11D3/02Inorganic compounds ; Elemental compounds
    • C11D3/12Water-insoluble compounds
    • C11D3/124Silicon containing, e.g. silica, silex, quartz or glass beads
    • C11D3/1246Silicates, e.g. diatomaceous earth
    • C11D3/128Aluminium silicates, e.g. zeolites
    • 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
    • C11D3/39Organic or inorganic per-compounds
    • C11D3/3902Organic or inorganic per-compounds combined with specific additives
    • C11D3/3905Bleach activators or bleach catalysts
    • C11D3/3932Inorganic compounds or complexes

Definitions

  • the present invention relates to a activating composition of persalts in the cold washing process and an improved process for its preparation and use thereof. More particularly, the present invention relates to a process for preparing a catalyst composition comprising an insoluble solid support, in particular an aluminosilicate such as zeolite, which comprises in its structure one or more transition metals and which acts to enhance elimination. stains during the washing process in aqueous medium at room temperature by activating the peroxide contained in the detergent product, without affecting the dry stability of the detergent or damaging or deteriorating neither the color nor the fiber itself of the tissues subjected to washing.
  • the present invention relates to the use of the composition prepared according to the process of the present invention as activator of persales in the process of bleaching of tissues in the cold wash.
  • Bleaching is a process commonly used to remove stains on textile materials during the washing operation.
  • the most common types of bleaching are those that use chlorine or peroxides as bleaching agents.
  • the bleaching with chlorine although much cheaper, has many drawbacks such as that the chlorine cannot be mixed with the detergent in the same package, tends to attack various dyes and also degrades the fabrics.
  • Peroxide bleaching is much more effective and safer with colored textiles and can stored together with detergent and other components, to form a unique detergent-bleach package.
  • peroxide bleaching has several drawbacks, such that for the wash solution to be effective it must be at a temperature high enough to activate the peroxide compound.
  • sodium perborate requires a water temperature above 70 ° C, which is higher than the usual domestic washing temperatures.
  • bleach activators are compounds that do not themselves have bleaching action, but when used in combination with a bleaching peroxide compound it forms a new peroxide compound, which is more effective at low temperatures than the initial bleaching peroxide compound.
  • bleaching activators are tetraacetylethylenediamine (TAED), sodium p-acetoxybenzene sulfonate and sodium p-heptanoyloxybenzene sulfonate.
  • the objective of the present invention is to disclose a parakeet activating composition in the cold washing process.
  • the bleaching activator composition of the present invention comprises a solid and stable support, preferably a crystalline or pseudocrystalline aluminosilicate, more preferably a zeolite, and most preferably type A zeolite, which comprises in its structure transition metals integrated in its reticles, preferably selected from the group comprising Mn II, Co II and / or Fe II, most preferably Mn II, for the activation of persalts in tissue washing.
  • the persal activator composition of the present invention is characterized in that it produces a concentration of soluble manganese ions in a leaching test well below 0.2 ppm. This avoids incurring the well-known deterioration of the fibers, which is why other similar products have not prospered commercially.
  • Another objective of the present invention is to disclose an improved method of preparing the aforementioned activator composition.
  • the process of the present invention comprises two fundamental steps: dehydration of the aluminosilicate support and impregnation thereof with transition metal ions. This makes said procedure advantageously simple, economical and clean, since it does not generate waste or release to the environment water that needs to be processed.
  • type 4A zeolite is used as a support for the persal activator composition of the present invention, which generally contains between 18 and 21% by weight of crystallization water, it must be partially or totally dehydrated. The zeolite 4A is dehydrated in such a way that there is a loss of water of crystallization between 5 and 21% by weight.
  • the dehydration step of the process according to the present invention can be carried out continuously or discontinuously, both at atmospheric pressure and at reduced pressure, depending on the equipment used.
  • Dehydration is preferably carried out by calcination at a temperature between 105 and 750 ° C, preferably between 300 and 600 ° C and most preferably, between 400 and 500 ° C.
  • the dehydration process can be carried out in a calciner, for example, a rotary kiln.
  • a rotary kiln provided with atomizing nozzles, which allow the impregnation stage to be carried out.
  • the aluminosilicate or zeolite support is impregnated with an aqueous solution of a transition metal salt, preferably Mn II, Co II and / or Fe II, most preferably Mn II.
  • a transition metal salt preferably Mn II, Co II and / or Fe II, most preferably Mn II.
  • the amount of transition metal ion solution to be impregnated in the dehydrated aluminosilicate support should not exceed the amount of water removed in the dehydration stage.
  • washing solution which causes tissue damage.
  • carrying out the impregnation process as mentioned above prevents an additional drying step.
  • the concentration of transition metal ions in the solution to be impregnated in the aluminosilicate support can be adjusted to achieve the best results.
  • the impregnation must be carried out in such a way that a homogeneous product is obtained, that is, the transition metal ion solution is distributed equally. If this does not occur, local excesses may occur that result in poor anchoring of the transition metal ions to the support structure and that are subsequently leached into the wash solution.
  • the type of transition metal ion salt used in the process of the present invention should preferably be a water soluble salt and the anion is selected from the group comprising acetate, carbonate, chloride, nitrate and / or sulfate, or a mixture from the same.
  • the impregnation is compatible with the use of complexers such as ammonia, amines such as methylamines, ethylenediamine (EDA) and diethylenetriamine.
  • complexers such as ammonia, amines such as methylamines, ethylenediamine (EDA) and diethylenetriamine.
  • Other ligands such as organic carboxylates or compounds containing both amino groups and carboxylate groups can also be used.
  • the formation of these complexes can be carried out in two stages. In the first, the transition metal is introduced through the impregnation process described above and subsequently add the ligand that forms a complex.
  • the impregnation step of the transition metal salt solution can be carried out in a rotary kiln equipped with atomizing nozzles, as mentioned above for the dehydration stage. That is to say, that the entire process of the present invention can be carried out in a single device, provided that the homogeneity of the prepared activator composition is guaranteed, thus reducing the preparation costs of said composition.
  • the impregnation step can also be carried out in separate equipment, such as a solid-liquid mixer.
  • the cold scrubber activating composition prepared according to the process of the present invention, produces a concentration of soluble manganese ions in a leaching test well below 0.2 ppm, which is the upper limit allowed for these types of preparations, as shown below in the examples of embodiments.
  • the persal activator composition of the present invention can be incorporated into the detergent / bleach formulation alone or in combination with the persalt that will be activated in the wash solution, for example, such as sodium percarbonate.
  • Another objective of the present invention is to make known the use of the composition prepared according to the process of the present invention as activator of persales in the process of bleaching of tissues in cold washing.
  • Another additional objective of the present invention is the use of said composition for the preparation of a product having the combined action of detergent and bleaching agent.
  • Table 1 summarizes the main parameters used and the results obtained in relation to leaching of manganese ions.
  • the impregnated zeolite is gassed with CO 2 .

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Detergent Compositions (AREA)

Abstract

The present invention relates to a composition that activates persalts in the cold wash process, an improved method for the preparation thereof and the use of same. More particularly, the present invention relates to a method for preparing a catalyst composition comprising an insoluble solid support, in particular an aluminosilicate such as zeolite, which contains one or more transition metals in the structure thereof and which promotes the elimination of stains during the washing process in an aqueous medium at ambient temperature. Furthermore, the present invention relates to the use of the resulting composition as a persalt activator in the cold-wash fabric bleaching process.

Description

COMPOSICIÓN ACTIVADORA DE PERÓXIDOS PARA EL LAVADO EN FRÍO, PROCEDIMIENTO DE PREPARACIÓN Y USO DE LA MISMA  PEROXIDE ACTIVATING COMPOSITION FOR COLD WASHING, PREPARATION PROCEDURE AND USE OF THE SAME

DESCRIPCIÓN DESCRIPTION

La presente invención se refiere a una composición activadora de persales en el proceso de lavado en frió y a un procedimiento mejorado para su preparación y al uso de la misma. Más en particular, la presente invención se refiere a un procedimiento para preparar una composición catalizadora que comprende un soporte sólido insoluble, en particular un aluminosilicato tal como la zeolita, que comprende en su estructura uno o más metales de transición y que actúa potenciando la eliminación de manchas durante el proceso de lavado en medio acuoso a temperatura ambiente mediante la activación del peróxido que contiene el producto detergente, sin afectar la estabilidad en seco del detergente ni dañar o deteriorar ni el color ni la propia fibra de los tejidos sometidos a lavado. Además, la presente invención se refiere al uso de la composición preparada según el procedimiento de la presente invención como activadora de persales en el proceso de blanqueo de tejidos en el lavado en frió.  The present invention relates to a activating composition of persalts in the cold washing process and an improved process for its preparation and use thereof. More particularly, the present invention relates to a process for preparing a catalyst composition comprising an insoluble solid support, in particular an aluminosilicate such as zeolite, which comprises in its structure one or more transition metals and which acts to enhance elimination. stains during the washing process in aqueous medium at room temperature by activating the peroxide contained in the detergent product, without affecting the dry stability of the detergent or damaging or deteriorating neither the color nor the fiber itself of the tissues subjected to washing. In addition, the present invention relates to the use of the composition prepared according to the process of the present invention as activator of persales in the process of bleaching of tissues in the cold wash.

El blanqueo es un proceso utilizado comúnmente para eliminar manchas en materiales textiles durante la operación de lavado. Los tipos de blanqueo más comunes son los que utilizan cloro o peróxidos como agentes blanqueador. El blanqueo con cloro, aunque es mucho más económico, presenta muchos inconvenientes tales como que no se puede mezclar el cloro con el detergente en un mismo empaque, tiende a atacar diversos tintes y también degrada las telas. El blanqueo mediante peróxidos es mucho más eficaz y más seguro con los textiles coloreados y puede almacenarse junto con el detergente y otros componentes, para formar un empaque único de detergente-blanqueador. Bleaching is a process commonly used to remove stains on textile materials during the washing operation. The most common types of bleaching are those that use chlorine or peroxides as bleaching agents. The bleaching with chlorine, although much cheaper, has many drawbacks such as that the chlorine cannot be mixed with the detergent in the same package, tends to attack various dyes and also degrades the fabrics. Peroxide bleaching is much more effective and safer with colored textiles and can stored together with detergent and other components, to form a unique detergent-bleach package.

Sin embargo, el blanqueo con peróxidos presenta varios inconvenientes, tales como que para que la solución de lavado sea eficaz tiene que estar a una temperatura suficientemente alta para activar el compuesto de peróxido. Por ejemplo, el perborato sódico requiere una temperatura del agua por encima de 70°C, que es mayor que las temperaturas habituales de lavado doméstico.  However, peroxide bleaching has several drawbacks, such that for the wash solution to be effective it must be at a temperature high enough to activate the peroxide compound. For example, sodium perborate requires a water temperature above 70 ° C, which is higher than the usual domestic washing temperatures.

A efectos de disminuir la temperatura a la que se puede utilizar el lavado con peróxidos, se han utilizado como alternativa los denominados "activadores de blanqueo". Los activadores de blanqueo son compuestos que por si mismos no poseen acción blanqueadora, pero cuando se utilizan en combinación con un compuesto de peróxido blanqueador forma un nuevo compuesto de peróxido, que es más eficaz a bajas temperaturas que el compuesto de peróxido blanqueador inicial. Ejemplos de dichos activadores de blanqueo son tetraacetiletilendiamina (TAED) , sulfonato p-acetoxibenceno sódico y sulfonato p- heptanoiloxibenceno sódico.  In order to reduce the temperature at which peroxide washing can be used, so-called "bleach activators" have been used as an alternative. Bleaching activators are compounds that do not themselves have bleaching action, but when used in combination with a bleaching peroxide compound it forms a new peroxide compound, which is more effective at low temperatures than the initial bleaching peroxide compound. Examples of such bleaching activators are tetraacetylethylenediamine (TAED), sodium p-acetoxybenzene sulfonate and sodium p-heptanoyloxybenzene sulfonate.

También es conocido en la técnica que ciertos metales covalentes, en particular el manganeso (II), son excelentes activadores de los agentes de blanqueo de peróxidos tales como percarbonato sódico y perborato sódico. La patente estadounidense US 4.481.129 da a conocer que dichos activadores son más efectivos cuando se utilizan en combinación con un compuesto que libera aniones carbonato a la solución acuosa de lavado.  It is also known in the art that certain covalent metals, in particular manganese (II), are excellent activators of peroxide bleaching agents such as sodium percarbonate and sodium perborate. US Patent 4,481,129 discloses that such activators are more effective when used in combination with a compound that releases carbonate anions to the aqueous wash solution.

Sin embargo, recientemente se ha publicado que el uso de cationes manganeso (II) solubles como activadores de blanqueo puede teñir la ropa debido a la oxidación del manganeso a un estado de valencia superior (véase, patente estadounidense US 4.536.183). La presencia de un fuerte agente oxidante en la solución de lavado puede oxidar el Mn(II) a Mn(IV), que se puede adherir a la tela confiriéndole una apariencia de color pardo claro. However, it has recently been published that the use of soluble manganese (II) cations as bleach activators can dye clothes due to the oxidation of manganese to a higher valence state (see, US Patent 4,536,183). The presence of a strong oxidizing agent in the wash solution can oxidize the Mn (II) to Mn (IV), which can adhere to the fabric giving it a light brown appearance.

Este problema ha sido resuelto en la técnica incorporando el catión Mn(II) en el interior de soportes sólidos (por e emplo, zeolita) , que evita que el manganeso se deposite sobre la tela. Sin embargo, los procedimientos de obtención desarrollados hasta la fecha, que usualmente se basan en el intercambio iónico y/o la impregnación/ secado por pulverización, presentan numerosos inconvenientes y dificultades. Entre éstas se encuentran que comprenden numerosas y complejas etapas, por lo que resultan muy costosos y, además, producen desechos al medio ambiente altamente contaminantes. Por otra parte, en las composiciones conocidas en la técnica anterior no se hace referencia a la posibilidad de que los iones metálicos, por ejemplo el manganeso, se liberen nuevamente del soporte en que estaban absorbidos a la solución de lavado en un proceso conocido como lixiviación y se depositen en los tejidos lavados.  This problem has been solved in the art by incorporating the cation Mn (II) into solid supports (for example, zeolite), which prevents manganese from depositing on the fabric. However, the procurement procedures developed to date, which are usually based on ion exchange and / or impregnation / spray drying, present numerous drawbacks and difficulties. Among these are that they include numerous and complex stages, so they are very expensive and also produce highly polluting waste into the environment. On the other hand, in the compositions known in the prior art there is no reference to the possibility that metal ions, for example manganese, are released again from the support in which they were absorbed into the wash solution in a process known as leaching and are deposited in the washed tissues.

Además, en la práctica, existen muy pocos productos detergentes/blanqueadores comercialmente disponibles que comprendan agentes activadores de blanqueo basados en iones de metales covalentes sobre soportes sólidos, a pesar de que éstos son conocidos desde hace varias décadas.  In addition, in practice, there are very few commercially available detergent / bleach products comprising bleaching activating agents based on covalent metal ions on solid supports, although these have been known for several decades.

Por lo tanto, existe la necesidad de un procedimiento de preparación de un agente activador de blanqueo que sea simple, económico, amigable con el medio ambiente y que garantice que los iones metálicos no sean liberados en el proceso de lixiviación cuando dicho agente se pone en contacto con la solución de lavado, provocando de esta manera daños a los tejidos. Therefore, there is a need for a process for preparing a bleaching activating agent that is simple, economical, environmentally friendly and ensures that metal ions are not released in the leaching process when said agent comes into contact with the wash solution, thus causing tissue damage.

Por lo tanto, el objetivo de la presente invención es dar a conocer una composición activadora de persales en el proceso de lavado en frió. La composición activadora de blanqueo de la presente invención comprende un soporte sólido y estable, preferentemente un aluminosilicato cristalino o pseudocristalino, más preferentemente una zeolita, y lo más preferente zeolita tipo A, que comprende en su estructura metales de transición integrados en sus retículos, preferentemente seleccionados del grupo que comprende Mn II, Co II y/o Fe II, siendo lo más preferentemente Mn II, para la activación de persales en lavado de tejidos.  Therefore, the objective of the present invention is to disclose a parakeet activating composition in the cold washing process. The bleaching activator composition of the present invention comprises a solid and stable support, preferably a crystalline or pseudocrystalline aluminosilicate, more preferably a zeolite, and most preferably type A zeolite, which comprises in its structure transition metals integrated in its reticles, preferably selected from the group comprising Mn II, Co II and / or Fe II, most preferably Mn II, for the activation of persalts in tissue washing.

La composición activadora de persales de la presente invención está caracterizada porque produce una concentración de iones manganeso solubles en un ensayo de lixiviación muy inferiores a 0,2 ppm. Con ello se evita incurrir en el bien conocido deterioro de las fibras, razón por la cual otros productos similares no han prosperado comercialmente .  The persal activator composition of the present invention is characterized in that it produces a concentration of soluble manganese ions in a leaching test well below 0.2 ppm. This avoids incurring the well-known deterioration of the fibers, which is why other similar products have not prospered commercially.

Otro objetivo de la presente invención es dar a conocer un procedimiento mejorado de preparación de la composición activadora de persales mencionada anteriormente. El procedimiento de la presente invención comprende dos etapas fundamentales: deshidratación del soporte de aluminosilicato e impregnación del mismo con iones de metal de transición. Esto hace que dicho procedimiento sea ventajosamente simple, económico y limpio, ya que no genera residuos ni libera al ambiente aguas que necesiten ser procesadas. Si se utiliza zeolita del tipo 4A como soporte de la composición activadora de persales de la presente invención, que generalmente contiene entre un 18 y 21% en peso de agua de cristalización, ésta debe estar parcial o totalmente deshidratada. La zeolita 4A se deshidrata de tal manera que se produzca una pérdida de agua de cristalización entre 5 y 21% en peso. La etapa de deshidratación del procedimiento según la presente invención puede llevarse a cabo de forma continua o discontinua, tanto a presión atmosférica como a presión reducida, en dependencia del equipo que se utilice. La deshidratación se realiza preferentemente por calcinación a una temperatura entre 105 y 750°C, preferentemente entre 300 y 600°C y lo más preferente, entre 400 y 500°C. Another objective of the present invention is to disclose an improved method of preparing the aforementioned activator composition. The process of the present invention comprises two fundamental steps: dehydration of the aluminosilicate support and impregnation thereof with transition metal ions. This makes said procedure advantageously simple, economical and clean, since it does not generate waste or release to the environment water that needs to be processed. If type 4A zeolite is used as a support for the persal activator composition of the present invention, which generally contains between 18 and 21% by weight of crystallization water, it must be partially or totally dehydrated. The zeolite 4A is dehydrated in such a way that there is a loss of water of crystallization between 5 and 21% by weight. The dehydration step of the process according to the present invention can be carried out continuously or discontinuously, both at atmospheric pressure and at reduced pressure, depending on the equipment used. Dehydration is preferably carried out by calcination at a temperature between 105 and 750 ° C, preferably between 300 and 600 ° C and most preferably, between 400 and 500 ° C.

A escala industrial, el proceso de deshidratación se puede llevar a cabo en un calcinador, por ejemplo, un horno rotativo. De manera ventajosa, se puede llevar a cabo en una horno rotativo provisto de boquillas atomizadoras, que permitan realizar la etapa de impregnación.  On an industrial scale, the dehydration process can be carried out in a calciner, for example, a rotary kiln. Advantageously, it can be carried out in a rotary kiln provided with atomizing nozzles, which allow the impregnation stage to be carried out.

Una vez deshidratado, el soporte de aluminosilicato o zeolita es impregnado con una solución acuosa de una sal de metales de transición, preferentemente Mn II, Co II y/o Fe II, lo más preferente Mn II. Ventajosamente, la cantidad de solución de iones de metales de transición a impregnar en el soporte de aluminosilicato deshidratado no debe exceder la cantidad de agua eliminada en la etapa de deshidratación. Sorprendentemente, se ha encontrado que si la cantidad de solución de iones de metales de transición no excede la cantidad de agua eliminada no ocurre el proceso no deseado de lixiviación de los iones de metales de transición a la solución de lavado, que provoca daños a los tejidos. Además, llevar a cabo el proceso de impregnación tal como se ha mencionado anteriormente, evita que haya que realizar una etapa adicional de secado. Once dehydrated, the aluminosilicate or zeolite support is impregnated with an aqueous solution of a transition metal salt, preferably Mn II, Co II and / or Fe II, most preferably Mn II. Advantageously, the amount of transition metal ion solution to be impregnated in the dehydrated aluminosilicate support should not exceed the amount of water removed in the dehydration stage. Surprisingly, it has been found that if the amount of transition metal ion solution does not exceed the amount of water removed, the unwanted process of leaching the transition metal ions to the transition does not occur. washing solution, which causes tissue damage. In addition, carrying out the impregnation process as mentioned above prevents an additional drying step.

La concentración de iones de metal de transición en la solución a ser impregnada en el soporte de aluminosilicato se puede ajustar para lograr los mejores resultados. De manera ventajosa, es preferente preparar una solución saturada o cercana a la saturación de la sal de metal de transición utilizada.  The concentration of transition metal ions in the solution to be impregnated in the aluminosilicate support can be adjusted to achieve the best results. Advantageously, it is preferred to prepare a saturated or near saturation solution of the transition metal salt used.

La impregnación debe realizarse de modo que se obtenga un producto homogéneo, es decir que se reparta por igual la solución de iones de metal de transición. Si esto no ocurre pueden producirse excesos locales que traen como consecuencia un mal anclaje de los iones de metal de transición a la estructura del soporte y que sean lixiviados posteriormente en la solución de lavado.  The impregnation must be carried out in such a way that a homogeneous product is obtained, that is, the transition metal ion solution is distributed equally. If this does not occur, local excesses may occur that result in poor anchoring of the transition metal ions to the support structure and that are subsequently leached into the wash solution.

El tipo de sal de iones de metal de transición utilizada en el procedimiento de la presente invención debe ser preferentemente una sal soluble en agua y el anión se selecciona del grupo que comprende acetato, carbonato, cloruro, nitrato y/o sulfato, o una mezcla de las mismas.  The type of transition metal ion salt used in the process of the present invention should preferably be a water soluble salt and the anion is selected from the group comprising acetate, carbonate, chloride, nitrate and / or sulfate, or a mixture from the same.

Además, la impregnación es compatible con el uso de complejantes tales como amoniaco, aminas tales como metilaminas, etilendiamina (EDA) y dietilentriamina . También pueden utilizarse otros ligandos tales como carboxilatos orgánicos o compuestos que contienen tanto grupos amino como grupos carboxilatos. La formación de estos complejos puede llevarse a cabo en dos etapas. En la primera se introduce el metal de transición mediante el proceso de impregnación descrito anteriormente y posteriormente añadir el ligando que forma un complejo. In addition, the impregnation is compatible with the use of complexers such as ammonia, amines such as methylamines, ethylenediamine (EDA) and diethylenetriamine. Other ligands such as organic carboxylates or compounds containing both amino groups and carboxylate groups can also be used. The formation of these complexes can be carried out in two stages. In the first, the transition metal is introduced through the impregnation process described above and subsequently add the ligand that forms a complex.

La etapa de impregnación de la solución de la sal de metal de transición puede llevarse a cabo en un horno rotatorio equipado con boquillas atomizadoras, tal como se mencionó anteriormente para la etapa de deshidratación . Es decir, que venta osamente todo el procedimiento de la presente invención se puede llevar a cabo en un solo equipo, siempre que se garantice la homogeneidad de la composición activadora preparada, reduciendo de esta manera los costes de preparación de dicha composición. Sin embargo, la etapa de impregnación también se puede llevar a cabo en un equipo aparte, tal como por ejemplo un mezclador sólido-liquido.  The impregnation step of the transition metal salt solution can be carried out in a rotary kiln equipped with atomizing nozzles, as mentioned above for the dehydration stage. That is to say, that the entire process of the present invention can be carried out in a single device, provided that the homogeneity of the prepared activator composition is guaranteed, thus reducing the preparation costs of said composition. However, the impregnation step can also be carried out in separate equipment, such as a solid-liquid mixer.

Sorprendentemente, la composición activadora de persales para lavado en frió, preparada según el procedimiento de la presente invención, produce una concentración de iones manganeso solubles en un ensayo de lixiviación muy inferiores a 0,2 ppm, que es el limite superior permitido para estos tipos de preparaciones, tal como se muestra más adelante en los ejemplos de realizaciones .  Surprisingly, the cold scrubber activating composition, prepared according to the process of the present invention, produces a concentration of soluble manganese ions in a leaching test well below 0.2 ppm, which is the upper limit allowed for these types of preparations, as shown below in the examples of embodiments.

Sin pretender estar limitado a ninguna teoría científica específica, es posible que en los procedimientos de preparación de este tipo de composiciones basados en el intercambio iónico, en el que se produce una permuta entre un ión Mn2+ y 2 iones Na+, ocupando el Mn2+ una de las dos posiciones antes ocupadas por los iones Na+ . La estructura experimenta cierta distorsión y que los iones Mn2+ puedan ser fácilmente lixiviados por efecto de un nuevo intercambio iónico forzado por los iones Ca2+ presentes en exceso en la solución de lavado. Con el nuevo procedimiento se forma un compuesto distinto y más estable del que se obtendría por intercambio iónico en el que la sal de manganeso II queda atrapada en la estructura de la zeolita de modo que no lixivia de manera significativa. Without pretending to be limited to any specific scientific theory, it is possible that in the preparation procedures of this type of compositions based on ion exchange, in which a swap between an Mn 2+ ion and 2 Na + ions is produced, occupying the Mn 2+ one of the two positions previously occupied by Na + ions. The structure undergoes some distortion and that the Mn 2+ ions can be easily leached by the effect of a new ion exchange forced by the Ca 2+ ions present in excess in the wash solution With the new procedure a different and more stable compound is formed than would be obtained by ion exchange in which the manganese salt II is trapped in the zeolite structure so that it does not leach significantly.

La composición activadora de persales de la presente invención puede incorporarse a la formulación detergente/blanqueadora sola o en combinación con la persal que será activada en la solución de lavado, por ejemplo, tal como percarbonato sódico.  The persal activator composition of the present invention can be incorporated into the detergent / bleach formulation alone or in combination with the persalt that will be activated in the wash solution, for example, such as sodium percarbonate.

Otro objetivo de la presente invención es dar a conocer el uso de la composición preparada según el procedimiento de la presente invención como activadora de persales en el proceso de blanqueo de tejidos en el lavado en frío. Otro objetivo adicional de la presente invención es el uso de dicha composición para la preparación de un producto que presenta la acción combinada de detergente y agente blanqueador.  Another objective of the present invention is to make known the use of the composition prepared according to the process of the present invention as activator of persales in the process of bleaching of tissues in cold washing. Another additional objective of the present invention is the use of said composition for the preparation of a product having the combined action of detergent and bleaching agent.

En un ensayo de estabilidad en seco no se observó ningún cambio visible después de 12 días de inspección en cuando se mezcló la composición activadora de persales de la presente invención con una base de detergente comercialmente disponible. Tampoco hubo una pérdida significativa de oxígeno activo en dicha mezcla.  In a dry stability test, no visible change was observed after 12 days of inspection when the crib activator composition of the present invention was mixed with a commercially available detergent base. Nor was there a significant loss of active oxygen in said mixture.

Además, a una mezcla de la composición activadora de la presente invención y una base de detergente comercialmente disponible se le realizó una evaluación de conservación de la solidez del color y destrucción de tejidos, según la norma de la Asociación Internacional de Jabones, Detergentes y Productos de Limpieza (AISE) . Después de 20 ciclos de lavado a diferentes temperaturas (20°C, 60°C y 90°C) con diferentes tipos de tejidos (algodón, poliéster y poliamida) de diferentes colores (rojo, azul, naranja, fucsia y negro) y diferentes tipos de colorantes (directo, disperso y reactivo) no se observó pérdida del color, medido cuantitativamente según la Escala de Grises, ni se detectaron roturas atribuibles a la composición de la presente invención mediante Microscopía Electrónica (x800) . In addition, an evaluation of preservation of color fastness and tissue destruction was performed on a mixture of the activating composition of the present invention and a commercially available detergent base, according to the norm of the International Association of Soaps, Detergents and Products Cleaning (AISE). After 20 wash cycles at different temperatures (20 ° C, 60 ° C and 90 ° C) with different types of fabrics (cotton, polyester and polyamide) of different colors (red, blue, orange, fuchsia and black) and different types of dyes (direct, dispersed and reactive) no loss of color was observed, measured quantitatively according to the Grayscale , nor breakages attributable to the composition of the present invention were detected by Electron Microscopy (x800).

La presente invención es descrita a continuación con más detalles en referencia a varios ejemplos de realización. Estos ejemplos, sin embargo, no están destinados a limitar el alcance técnico de la presente invención .  The present invention is described in more detail below with reference to various embodiments. These examples, however, are not intended to limit the technical scope of the present invention.

Ejemplos  Examples

Ejemplo 1  Example 1

Se prepararon diferentes composiciones activadoras de persales. En la Tabla 1 se resumen los principales parámetros utilizados y los resultados obtenidos en relación con la lixiviación de iones manganeso. Different activating compositions of persales were prepared. Table 1 summarizes the main parameters used and the results obtained in relation to leaching of manganese ions.

Tabla 1. Parámetros del proceso de preparación composición activadora según la presente invención resultados obtenidos Table 1. Parameters of the preparation process activator composition according to the present invention results obtained

Figure imgf000011_0001
Figure imgf000011_0001

La zeolita impregnada se gasea con CO2. The impregnated zeolite is gassed with CO 2 .

2La muestra 6 se somete a reflujo en EDA.  2 Sample 6 is refluxed in EDA.

E emplo 2  E emplo 2

Ensayo de lixiviación  Leaching test

En un recipiente provisto de agitación mecánica y a una temperatura de 25°C se añaden 4,5 litros de agua del grifo. Se añaden 0,3 g de la composición según la presente invención impregnada con 0,4% de Mn, 2,8 g de percarbonato sódico, 15,3 g de una base de detergente comercialmente disponible. A continuación, se introduce en la solución una pieza de tela blanca (65% de poliéster, 35% de algodón) y se mantiene en agitación durante 1 hora a 25°C. Transcurrido este tiempo, se detiene la agitación, se retira la tela y se aclara con agua. Se determina la cantidad de iones de Mn II en las suspensión resultante. In a vessel equipped with mechanical agitation and at a temperature of 25 ° C, 4.5 liters of tap water are added. 0.3 g of the composition according to the present invention impregnated with 0.4% Mn, 2.8 g of sodium percarbonate, 15.3 g of a commercially available detergent base. A piece of white cloth (65% polyester, 35% cotton) is then introduced into the solution and kept under stirring for 1 hour at 25 ° C. After this time, stirring stops, the fabric is removed and rinsed with water. The amount of Mn II ions in the resulting suspension is determined.

Si bien la invención se ha descrito con respecto a ejemplos de realizaciones preferentes, éstos no se deben considerar limitativos de la invención, que se definirá por la interpretación más amplia de las siguientes reivindicaciones .  While the invention has been described with respect to examples of preferred embodiments, these should not be construed as limiting the invention, which will be defined by the broader interpretation of the following claims.

Claims

REIVINDICACIONES 1. Procedimiento para preparar una composición activadora de persales, en el proceso de blanqueo de tejidos en el lavado en frió, cuya composición activadora comprende un soporte de aluminosilicato impregnado con iones de metal de transición, caracterizado porque comprende las etapas de:  1. A method for preparing a activating composition of persalts, in the process of bleaching of tissues in cold washing, whose activating composition comprises an aluminosilicate support impregnated with transition metal ions, characterized in that it comprises the steps of: - deshidratación del soporte de aluminosilicato, e  - dehydration of aluminosilicate support, and -impregnación de iones de metales de transición en dicho soporte de aluminosilicato .  - impregnation of transition metal ions in said aluminosilicate support. 2. Procedimiento, según la reivindicación 1, en el que dicho soporte de aluminosilicato es cristalino o pseudocristalino .  2. A method according to claim 1, wherein said aluminosilicate support is crystalline or pseudocrystalline. 3. Procedimiento, según la reivindicación 1 ó 2, en el que dicho soporte de aluminosilicato es zeolita.  3. The method according to claim 1 or 2, wherein said aluminosilicate support is zeolite. 4. Procedimiento, según cualquiera de las reivindicaciones 1 a 3, en el que dicho soporte de aluminosilicato es zeolita tipo 4A.  4. A method according to any one of claims 1 to 3, wherein said aluminosilicate support is type 4A zeolite. 5. Procedimiento, según cualquiera de las reivindicaciones 1 a 4, en el que la etapa de deshidratación se realiza mediante calcinación.  5. A method according to any one of claims 1 to 4, wherein the dehydration step is carried out by calcination. 6. Procedimiento, según cualquiera de las reivindicaciones 1 a 5, en el que la etapa de deshidratación se realiza entre 105 y 750°C.  6. A method according to any one of claims 1 to 5, wherein the dehydration step is performed between 105 and 750 ° C. 7. Procedimiento, según cualquiera de las reivindicaciones 1 a 6, en el que la etapa de deshidratación se realiza entre 300 y 600°C. 7. Method according to any one of claims 1 to 6, wherein the dehydration step is performed between 300 and 600 ° C. 8. Procedimiento, según cualquiera de las reivindicaciones 1 a 7, en el que la etapa de deshidratación se realiza entre 400 y 500°C. 8. A method according to any one of claims 1 to 7, wherein the dehydration step is performed between 400 and 500 ° C. 9. Procedimiento, según cualquiera de las reivindicaciones 1 a 8, en el que en la etapa de deshidratación se produce una pérdida de agua de cristalización en el soporte de aluminosilicato entre 5 y 21% en peso.  9. A method according to any one of claims 1 to 8, wherein in the dehydration step a loss of crystallization water occurs in the aluminosilicate support between 5 and 21% by weight. 10. Procedimiento, según cualquiera de las reivindicaciones 1 a 9, en el que el metal de transición a impregnar en el soporte de aluminosilicato se selecciona entre el grupo que comprende Mn II, Co II ylo Fe II.  Method according to any one of claims 1 to 9, in which the transition metal to be impregnated in the aluminosilicate support is selected from the group comprising Mn II, Co II and Fe II. 11. Procedimiento, según cualquiera de las reivindicaciones 1 a 10, en el que el metal de transición es Mn II.  11. A method according to any one of claims 1 to 10, wherein the transition metal is Mn II. 12. Procedimiento, según cualquiera de las reivindicaciones 1 a 11, en el que la solución a impregnar en dicho soporte de aluminosilicato es una solución saturada o cercana a la saturación de una sal de metal de transición.  12. A method according to any one of claims 1 to 11, wherein the solution to be impregnated in said aluminosilicate support is a saturated or near saturation solution of a transition metal salt. 13. Procedimiento, según cualquiera de las reivindicaciones 1 a 12, en el que dicha sal de iones de metal de transición es una sal soluble en agua.  13. A method according to any one of claims 1 to 12, wherein said transition metal ion salt is a water soluble salt. 14. Procedimiento, según cualquiera de las reivindicaciones 1 a 13, en el que el anión de dicha sal de metal de transición se selecciona del grupo que comprende acetato, carbonato, cloruro, nitrato y/o sulfato, o una mezcla de los mismos.  14. A method according to any one of claims 1 to 13, wherein the anion of said transition metal salt is selected from the group comprising acetate, carbonate, chloride, nitrate and / or sulfate, or a mixture thereof. 15. Procedimiento, según cualquiera de las reivindicaciones 1 a 14, en el que la cantidad de solución de iones de metales de transición a impregnar en el soporte de aluminosilicato deshidratado no excede la cantidad de agua eliminada en la etapa de deshidratación . 15. A method according to any one of claims 1 to 14, wherein the amount of transition metal ion solution to be impregnated in the Dehydrated aluminosilicate support does not exceed the amount of water removed in the dehydration stage. 16. Procedimiento, según cualquiera de las reivindicaciones 1 a 15, en el que la solución a ser impregnada comprende además un agente comple ante.  16. A method according to any one of claims 1 to 15, wherein the solution to be impregnated further comprises a complete agent. 17. Procedimiento, según la reivindicación 16, en el que el agente complejante se selecciona del grupo que comprende amoniaco, metilamina, etilendiamina (EDA), dietilentriamina, carboxilatos orgánicos y/o compuestos que contienen tanto grupos amino como grupos carboxilatos o una mezcla de los mismos.  17. The method of claim 16, wherein the complexing agent is selected from the group comprising ammonia, methylamine, ethylenediamine (EDA), diethylenetriamine, organic carboxylates and / or compounds containing both amino groups and carboxylate groups or a mixture of the same.
PCT/ES2011/070185 2010-03-31 2011-03-18 Peroxide-activating composition for cold washing, preparation method thereof and use of same Ceased WO2011121157A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ESP201030495 2010-03-31
ES201030495A ES2343727B1 (en) 2010-03-31 2010-03-31 PEROXIDE ACTIVATING COMPOSITION FOR COLD WASHING, PREPARATION PROCEDURE AND USE OF THE SAME.

Publications (1)

Publication Number Publication Date
WO2011121157A1 true WO2011121157A1 (en) 2011-10-06

Family

ID=42352360

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/ES2011/070185 Ceased WO2011121157A1 (en) 2010-03-31 2011-03-18 Peroxide-activating composition for cold washing, preparation method thereof and use of same

Country Status (2)

Country Link
ES (1) ES2343727B1 (en)
WO (1) WO2011121157A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3444323A1 (en) * 2017-08-18 2019-02-20 The Procter & Gamble Company Cleaning kit

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES8706809A1 (en) * 1985-04-02 1987-06-16 Unilever Nv Bleach compositions.
ES8706478A1 (en) * 1985-04-02 1987-06-16 Unilever Nv Bleaching compositions.
EP0225663A2 (en) * 1985-12-06 1987-06-16 Unilever N.V. Preparation of bleach catalyst aggregates of manganese cation impregnated aluminosilicates
ES2216128T3 (en) * 1996-03-22 2004-10-16 THE PROCTER & GAMBLE COMPANY LIBERATION SYSTEM THAT HAS A ZEOLITE LOADED WITH A LIBERATION BAR.
WO2008132456A1 (en) * 2007-04-25 2008-11-06 Reckitt Benckiser N.V. Composition

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES8706809A1 (en) * 1985-04-02 1987-06-16 Unilever Nv Bleach compositions.
ES8706478A1 (en) * 1985-04-02 1987-06-16 Unilever Nv Bleaching compositions.
EP0225663A2 (en) * 1985-12-06 1987-06-16 Unilever N.V. Preparation of bleach catalyst aggregates of manganese cation impregnated aluminosilicates
ES2216128T3 (en) * 1996-03-22 2004-10-16 THE PROCTER & GAMBLE COMPANY LIBERATION SYSTEM THAT HAS A ZEOLITE LOADED WITH A LIBERATION BAR.
WO2008132456A1 (en) * 2007-04-25 2008-11-06 Reckitt Benckiser N.V. Composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3444323A1 (en) * 2017-08-18 2019-02-20 The Procter & Gamble Company Cleaning kit
WO2019035037A1 (en) * 2017-08-18 2019-02-21 The Procter & Gamble Company Cleaning kit

Also Published As

Publication number Publication date
ES2343727A1 (en) 2010-08-06
ES2343727B1 (en) 2011-03-17

Similar Documents

Publication Publication Date Title
ES2215411T3 (en) WHITENING WITH POLYOXOMETALATES AND AIR OR MOLECULAR OXYGEN.
ES2219438T5 (en) METHOD FOR WHITENING A SUBSTRATE.
ES2265041T3 (en) USE OF METAL COMPLEX COMPOUNDS AS OXIDATION CATALYSTS.
ES2320735T3 (en) METHOD FOR TREATING FIBER MATERIALS.
JPS608040B2 (en) Bleach composition that does not change color or pattern or cause fading
US4279769A (en) Bleaching composition
CN107488531A (en) A kind of neutral Instant detergent bar composition and preparation method thereof
BRPI0706638A2 (en) process for treating fiber materials
ES2343727B1 (en) PEROXIDE ACTIVATING COMPOSITION FOR COLD WASHING, PREPARATION PROCEDURE AND USE OF THE SAME.
ES2223838T3 (en) PROTECTION SYSTEMS FOR SULFUR DYES AND COMPOSITIONS AND METHODS THAT USE THE SAME.
ES2643483T3 (en) Whitening and oxidation catalyst
KR101287127B1 (en) Oxygen bleach composition improving solubility and bleaching ability
JPH1150095A (en) Bleaching activator and bleaching detergent composition
JP4527771B2 (en) Method for synthesizing macrocyclic ligands and bleach and bleach detergent compositions containing manganese complexes prepared thereby
ES2746314T3 (en) Manganese carboxylates for peroxygen activation
ES2314874T3 (en) WHITENING COMPOSITIONS.
JP4011215B2 (en) Bleach activator
KR100889652B1 (en) Uses of Macrocyclic Manganese Complexes and Bleach Detergent Compositions Containing them
JPS62252500A (en) Bleaching composition
GB2073268A (en) Bleaching Composition
JPH0781159B2 (en) Bleach composition
JPH01245099A (en) Bleaching agent composition
JPH0832916B2 (en) Bleachable detergent composition
JPH05339874A (en) Fade suppressing agent for oxygen-type bleaching agent
JPS5851998B2 (en) bleach composition

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 11762057

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 11762057

Country of ref document: EP

Kind code of ref document: A1