EP2009086A1 - Procédé de coloration de minéraux non-adsorbants et le produit ainsi obtenu - Google Patents

Procédé de coloration de minéraux non-adsorbants et le produit ainsi obtenu Download PDF

Info

Publication number
EP2009086A1
EP2009086A1 EP07012496A EP07012496A EP2009086A1 EP 2009086 A1 EP2009086 A1 EP 2009086A1 EP 07012496 A EP07012496 A EP 07012496A EP 07012496 A EP07012496 A EP 07012496A EP 2009086 A1 EP2009086 A1 EP 2009086A1
Authority
EP
European Patent Office
Prior art keywords
colouring
adsorbent
accordance
procedure
minerals
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP07012496A
Other languages
German (de)
English (en)
Other versions
EP2009086B1 (fr
Inventor
Francisco Javier Álvarez Iglesias
Antonio Quintilla Beroy
Constantino Toca Marguelles
Ignacio Banales Alonso
Miguel Angel Caballero López
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.)
Minera Catalano Aragonesa SA
Original Assignee
Minera Catalano Aragonesa 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 Minera Catalano Aragonesa SA filed Critical Minera Catalano Aragonesa SA
Priority to EP07012496A priority Critical patent/EP2009086B1/fr
Priority to PL07012496T priority patent/PL2009086T3/pl
Priority to ES07012496T priority patent/ES2416281T3/es
Priority to UAA200807710A priority patent/UA100110C2/ru
Priority to MX2008007645A priority patent/MX2008007645A/es
Publication of EP2009086A1 publication Critical patent/EP2009086A1/fr
Application granted granted Critical
Publication of EP2009086B1 publication Critical patent/EP2009086B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/40—Dyes ; Pigments
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00—Special methods for preparing compositions containing mixtures of detergents
    • C11D11/0082—Special methods for preparing compositions containing mixtures of detergents one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/06—Powder; Flakes; Free-flowing mixtures; Sheets
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02—Inorganic compounds ; Elemental compounds
    • C11D3/04—Water-soluble compounds
    • C11D3/046—Salts
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02—Inorganic compounds ; Elemental compounds
    • C11D3/04—Water-soluble compounds
    • C11D3/08—Silicates
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02—Inorganic compounds ; Elemental compounds
    • C11D3/12—Water-insoluble compounds
    • C11D3/122—Sulfur-containing, e.g. sulfates, sulfites or gypsum

Definitions

  • This descriptive report refers, as its title indicates, to a procedure for colouring granulated non-adsorbent minerals and the product thus obtained of the type used in the field of chemical products and processes leading to coloured speckles used in the detergent industry being obtained, characterised in that it allows coloured granules, also known by the English tem "speckles", to be obtained which are particularly used as coloured speckles present in powdered detergents.
  • These coloured granules are obtained from non-adsorbent mineral particles with a diameter of between 300 and 2,000 ⁇ m using a granular base of the same size, a binding agent and a colouring agent or pigment, all by means of a characteristic production procedure.
  • the process is based on a non-adsorbent salt, preferably a monocrystal inorganic salt with a grain size of between 300 and 2,000 ⁇ m, preferably between 600 and 1,500 ⁇ m, of a hygroscopic nature in order to be able to fix the colouring agent, so these are mainly inorganic salts, such as sodium carbonate, sodium tripolyphosphate, sodium chloride, sodium sulphate among others.
  • a non-adsorbent salt preferably a monocrystal inorganic salt with a grain size of between 300 and 2,000 ⁇ m, preferably between 600 and 1,500 ⁇ m, of a hygroscopic nature in order to be able to fix the colouring agent, so these are mainly inorganic salts, such as sodium carbonate, sodium tripolyphosphate, sodium chloride, sodium sulphate among others.
  • the colouring agent is responsible for providing the desired colour to the inorganic salt and any pigment or colouring agent allowed in the detergent industry or any preparation thereof, which must have a granulometry between 0.01 and 15 ⁇ m, preferably between 0.01 and and 5 ⁇ m] is used.
  • any pigment or colouring agent allowed in the detergent industry or any preparation thereof which must have a granulometry between 0.01 and 15 ⁇ m, preferably between 0.01 and and 5 ⁇ m] is used.
  • Pigment Blue 15 Pigment Green 7, Pigment Yellow 3, Pigment Red 57, Yellow Food Colouring 3, Food Blue 5, Acid Green 1, Acid Yellow 4, among others.
  • the binding agent is necessary to obtain a film, which fixes the colouring agent to the inorganic salt substrate, as it is a non-adsorbent material. This acts by generating a surface layer which fixes the colouring agent to the substrate and which is compatible with formulations in the detergent.
  • binding agents which may be used and which are found in literature, we may cite among others, sodium silicate, different types of polymers, carboxymethyl cellulose (CMC), etc.
  • the colouring procedure comprises a sequence of three main phases, which in their turn are divided into different intermediate steps.
  • This colouring procedure is carried out in a industrial rotary mixer of the endless screw or mixing blade variety, with a jacket or encasing double wall equipped with a peripheral water heating circuit and also equipped with a hot air injection system inside.
  • the appropriate temperature control and regulatory devices must be available both for water circulating in the jacket and for the hot air, to allow precise control of the working temperatures to prevent the formation and agglomeration of hydrated compounds.
  • Figure -2- gives a graphic example of the evolution of temperature inside the mixer.
  • Figure -3- shows a simplified view of the main elements, which the mixing device used in the invention must comprise.
  • the procedure for colouring granulated, non-adsorbent minerals and the product thus obtained which forms the object of this invention consists of a characteristic sequence of phases (1,2,3) in which a non-adsorbent mineral (4) or substrate is mixed with a colouring agent (9) and a binding agent (11).
  • the process is based on a non-adsorbent mineral (4), preferably a monocrystal inorganic salt with a grain size of between 300 and 2,000 ⁇ m, preferably between 600 and 1500 ⁇ m, so it is not necessary to carry out an agglomeration process for it to achieve the desired size and, given the monocrystalline nature of the product obtained, it is hard enough to withstand the effect of friction during mixing with the rest of the components.
  • a non-adsorbent mineral (4) preferably a monocrystal inorganic salt with a grain size of between 300 and 2,000 ⁇ m, preferably between 600 and 1500 ⁇ m, so it is not necessary to carry out an agglomeration process for it to achieve the desired size and, given the monocrystalline nature of the product obtained, it is hard enough to withstand the effect of friction during mixing with the rest of the components.
  • the colouring agent (9) can be fixed (9), so that sodium carbonate, sodium tripolysulphate, sodium chloride, sodium sulphate among others may be
  • the colouring agent (9) is responsible for providing the desired colour to the non-adsorbent mineral (4) and for this any pigment or colouring agent allowed in the detergent industry or any preparation thereof, which must have a granulometry of between 0.01 and 15 ⁇ m, preferably between 0.01 and 5 ⁇ m, is used, thus maintaining its visibility and facilitating the homogeneity of the colour in the subsequent process and avoiding stains in the product because of a larger size.
  • the commonest ones that may be used in the process we may cite: Pigment Blue 15, Pigment Green 7, Pigment Yellow 3, Pigment Red 57, Food yellow 3, Food Blue 5, Acid Green 1, Acid Yellow 4, among others.
  • the binding agent (11) is necessary to obtain a film, which fixes the colouring agent (9) to the inorganic salt substrate. Moreover, being non-adsorbent materials, the pigment or colouring agent must be fixed to the grain.
  • the binding agent (11) acts by generating a surface layer, which fixes the colouring agent (9) to the inorganic salt substrate (4), allowing it at the same time to be compatible with the formulations in the detergent.
  • binding agents (11) which may be used in this process, we may cite among others, sodium silicate, different types of polymers, carboxymethyl cellulose (CMC), etc ., preferably soluble sodium silicate because of its readiness to form vitreous layers with the above features when its diluting water dries up.
  • the colouring procedure characteristic of the invention comprises a sequence of three main phases, which in their turn are divided into different intermediate steps.
  • the phase starts with the initial step of loading (5) the mixer (17) with the non-adsorbent mineral (4), where the step of heating the product (6) above its hydration temperature is carried out, if it has one. To do this, the jacket (18) is heated at the same time above this temperature and hot air is introduced into the mixer (17).
  • the phase continues with the step of lowering the temperature (7) of the jacket (18) below the temperature of the product followed by the step of introducing (8) the colouring agent (9) in the form of a preparation.
  • the jacket (18) be below the temperature of the product in order to avoid incrustations. This may be achieved in two ways: by keeping it constant just above the hydration temperature or by maintaining a constant difference with the temperature of the product.
  • the colouring agent (9) will be added in suspension with water and, if necessary, with some kind of dispersant.
  • concentration of colouring agent (9) in the preparation will be preferably between 15 %, to avoid using a lot of water which will evaporate afterwards, and 60 %, to allow a good mix and close contact between the substrate (4) and the colouring agent (9), as the medium which puts them in contact and allows them to join is water, although they are fixed by the binding agent (11) in the subsequent drying process.
  • the addition to the mass will be made with sufficient time for mixing, preferably between 10 seconds and 5 minutes, depending on the mixing capacity of the equipment.
  • the proportion of colouring agent (9) to be used in relation to the non-adsorbent mineral (4) varies between 0.001% and 10%, preferably between 0.01% and 1%.
  • the introduction of the colouring agent (9) should be carried out preferably by means of spray nozzles or a shower to make mixing easier.
  • step of adding (10) the binding agent (11) is carried out several times (13) to facilitate homogeneity and avoid incrustations.
  • a drying step (12) is then carried out by introducing hot air into the mixer (17) to dry after each step of adding (10) a binding agent (11).
  • the method of introducing this hot air, its rate of flow and temperature will result in less time and, therefore, greater production capacity, resulting in fewer operational costs.
  • the temperature of the drying air must be preferably between 100 and 300° C, depending on the physical characteristics of the substrate (4), colouring agents (9) and binding agent (11) chosen.
  • the rate of flow of hot air to be introduced should be such that it is sufficient to dry and keep the bed spongy if necessary, but avoiding elutriates (solid product carried away by the air) being produced. As high granulometry is involved, excessive amounts of elutriates are not generated and this solved by installing a sleeve filter or an air washer at the outlet for the exhaust air.
  • the number of times (13) that the cycle of adding (10) and subsequent drying (12) steps is 5 by way of example, thus optimising the process in accordance with the type of mixer and product.
  • the temperatures on addition (10) depend on the equipment, the number (13) of additions intended, the substrate (4) load, the temperature of the cooling jacket (18) and the characteristics of the drying air.
  • the increase in temperatures between additions (10) should preferably be between 2 and 10° C. In this way a dry product will be obtained, preferably with humidity of less than 5% in weight.
  • the method of adding (10) the binding agent (11) should enhance uniform distribution throughout the product without generating any kind of agglomerate (either of product or dry residue of the binding agent itself) and avoid giving rise to incrustations.
  • adding is carried out over various steps emulating an on-going addition (10) and drying (12) process. That is to say, an addition (10) is made and we wait for this product to be dry enough for the next addition to be made.
  • the number of additions (13) simulates an on-going process of addition and depends on the percentage of binding agent (11) necessary for each size of grain and substrate (4).
  • the percentage addition of binding agent (11) may vary between 2 % and 10 %, the number of additions to fulfil the conditions of the first heading being a total of between 1 and infinity (exactly what an on-going addition process would be).
  • a suitable number of additions is between 2 and 10. Below this amount there is the risk of generating incrustations and agglomerations and above, the process is affected energy wise.
  • each one of the different additions (10) should be made in a way that allows a good mix.
  • the addition to the mass will be made with sufficient mixing time, preferably between 10 seconds and 5 minutes, depending on the mixing capacity of the equipment.
  • binding agent (11) should be by means of spray nozzles or a shower to make mixing easier.
  • binding agent (11) will be added continuously throughout the drying process (12).
  • a cooling process of the end product (16) must be carried out as otherwise the hygroscopic nature of the inorganic salts (4) being treated would cause condensation effects during storage.
  • a suitable temperature for finishing the process and considering the product as finished (and cold) would be around 30-60° C.
  • the cooling process is carried out by means of a step introducing cold air (14) and another simultaneous step introducing cold water (15) into the jacket (18). Cold is considered to be at a temperature around room temperature.
  • the rotating speed of the mixing element (17) may be varied by controlling the rotating motor (20) in order to improve each one. These revolutions should not be excessive in order to avoid stirring the granules too violently causing them to break and fine materials to be produced.
  • the following preferred values for each one of the above stages in a horizontal mixer (18) may be given:
  • revolutions during the process will fluctuate between 1 and 150 rpm in the mixing element, depending on the type of product, equipment and process.
  • the choice of the type of revolutions will directly influence the process time and, therefore the production capacity however, this will not have any great effect on the quality of the product.
  • the mixer (17), which may be used for this invention, may be any of those used in industry, preferably the horizontal type with flat blades and having the following components:
  • V/SA volume/surface area ratio of the jacket (18) should be optimised in order to avoid loss of energy and incrustations of the product.
  • This volume/surface area ratio should likewise optimise the contact surface of drying air with the product and therefore increase the production capacity for a given volume. This ratio will be different depending on the type of mixer (17).
  • the volume of product should be such that the formation of incrustations is prevented as, due to abrasion, they do not occur on the actual product bed.
  • the occupied volume should be such as to allow mixing and minimise incrustations. In most equipment this percentage fluctuates between 50 and 100 % of the total volume of the equipment, which allows movement of the mixture.
  • a production batch of coloured speckles of different colours is made, based on granular sodium sulphate with a constant jacket temperature, with the following mixer and process characteristics: Characteristics of the substrate.
  • Characteristic Value Compound Granular sodium sulphate Average size 900 ⁇ m Apparent density 1.6 Kg/l Initial humidity 0.03 % Characteristics of the binding agent Characteristic Value Compound Soluble sodium silicate Percentage of total addition to substrate (in N additions) 5 % Characteristics of the different colouring agents Characteristic Value Colouring agent 1 (Green) Pigment Green 7 (35 %) Colouring agent 2 (Blue) Pigment Blue 15 (35 %) Colouring agent 3 (Orange) Food Yellow 3 (35 %) Percentage addition of preparation 0.20 % Characteristics of the mixer Characteristic Value Type of mixer Horizontal with flat blades Volume of mixer 3,000 litres V / SA ratio 0.26 m 3 /m 2 Characteristics of process Characteristic Value Substrate load 3,000 Kg.
  • the sulphate thus obtained contains 97.4% pure sodium sulphate, higher than the methods currently used, since, as stated, the consumption of raw materials is less.
  • the remaining properties (granulometry, density, etc.) remain very similar to the starting product as practically no grains have been broken.

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)
  • Inorganic Chemistry (AREA)
  • Detergent Compositions (AREA)
  • Cosmetics (AREA)
EP07012496A 2007-06-26 2007-06-26 Procédé de coloration de minéraux non-adsorbants et le produit ainsi obtenu Active EP2009086B1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
EP07012496A EP2009086B1 (fr) 2007-06-26 2007-06-26 Procédé de coloration de minéraux non-adsorbants et le produit ainsi obtenu
PL07012496T PL2009086T3 (pl) 2007-06-26 2007-06-26 Sposób barwienia minerałów o słabych właściwościach adsorpcyjnych i produkt otrzymany tym sposobem
ES07012496T ES2416281T3 (es) 2007-06-26 2007-06-26 Procedimiento de coloreado de minerales no adsorbentes y producto así obtenido
UAA200807710A UA100110C2 (ru) 2007-06-26 2008-06-05 Способ окрашивания неадсорбирующих гранулированных минералов, продукт, полученный в результате его осуществления и применение
MX2008007645A MX2008007645A (es) 2007-06-26 2008-06-12 Procedimiento de coloreado de minerales no adsorbentes y producto asi obtenido.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP07012496A EP2009086B1 (fr) 2007-06-26 2007-06-26 Procédé de coloration de minéraux non-adsorbants et le produit ainsi obtenu

Publications (2)

Publication Number Publication Date
EP2009086A1 true EP2009086A1 (fr) 2008-12-31
EP2009086B1 EP2009086B1 (fr) 2013-03-27

Family

ID=38537723

Family Applications (1)

Application Number Title Priority Date Filing Date
EP07012496A Active EP2009086B1 (fr) 2007-06-26 2007-06-26 Procédé de coloration de minéraux non-adsorbants et le produit ainsi obtenu

Country Status (5)

Country Link
EP (1) EP2009086B1 (fr)
ES (1) ES2416281T3 (fr)
MX (1) MX2008007645A (fr)
PL (1) PL2009086T3 (fr)
UA (1) UA100110C2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3318622A1 (fr) * 2016-11-04 2018-05-09 Sociedad Anónima Minera Catalano-Aragonesa Particules colorées pour détergents et leur procédé de production

Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3850833A (en) 1971-01-25 1974-11-26 Colgate Palmolive Co Scouring cleanser composition
US4097418A (en) 1975-10-06 1978-06-27 The Procter & Gamble Company Granular colored speckles
US4162228A (en) 1977-05-31 1979-07-24 Lever Brothers Company Process for preparing colored detergent flakes
EP0060728A1 (fr) 1981-03-18 1982-09-22 Unilever Plc Procédé de fabrication de granules colorés pour détergents
EP0219328A2 (fr) 1985-10-14 1987-04-22 Unilever Plc Composition détergente et son procédé de préparation
US4671886A (en) 1985-11-25 1987-06-09 The Procter & Gamble Company Process for coloring granular product by admixing with pigment/diluent premix
GB2199338A (en) * 1986-12-30 1988-07-06 Unilever Plc Coloured detergent particles
EP0289311A2 (fr) 1987-04-30 1988-11-02 Unilever Plc Procédé de préparation d'une composition détergente granulaire
EP0344629A1 (fr) 1988-06-03 1989-12-06 Henkel Kommanditgesellschaft auf Aktien Composition adsorbente granulaire avec une capacité de dégagement ameliorée
US5065883A (en) 1990-09-17 1991-11-19 Container Corporation Of America Tamper evident closure
EP0556923A1 (fr) 1992-02-18 1993-08-25 Colorsil B.V. Pigment de silicate mixte au zirconium dopé, procédé de préparation et produits contenant le pigment ou un pigment ainsi préparé
EP0702055A2 (fr) 1994-09-14 1996-03-20 Ciba-Geigy Ag Pigments organiques prêts à être mélangés
US5605883A (en) 1993-02-24 1997-02-25 Iliff; Robert J. Agglomerated colorant speckle exhibiting reduced colorant spotting
WO1998016615A1 (fr) * 1996-10-15 1998-04-23 The Procter & Gamble Company Compositions particulaires colorees
EP0882125A1 (fr) 1996-02-14 1998-12-09 The Procter & Gamble Company Procede d'obtention d'une composition de detergent a faible densite par agglomeration avec un double sel inorganique
EP0935343A1 (fr) 1997-07-08 1999-08-11 MASUDA, Tatsuji Bascule rs
WO2000027980A1 (fr) * 1998-11-06 2000-05-18 The Procter & Gamble Company Grains colores et compositions les renfermant
EP1305387A1 (fr) 2000-07-31 2003-05-02 Unilever Plc Composition coloree a mouchetures et compositions particulaires de detergent de lessive contenant ladite composition
EP1627909A1 (fr) 2004-07-22 2006-02-22 The Procter & Gamble Company Compositions détergentes contenant des particules colorées
WO2007006357A1 (fr) * 2005-07-11 2007-01-18 Unilever Plc Granules delivrant un colorant

Patent Citations (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3850833A (en) 1971-01-25 1974-11-26 Colgate Palmolive Co Scouring cleanser composition
US4097418A (en) 1975-10-06 1978-06-27 The Procter & Gamble Company Granular colored speckles
US4162228A (en) 1977-05-31 1979-07-24 Lever Brothers Company Process for preparing colored detergent flakes
EP0060728A1 (fr) 1981-03-18 1982-09-22 Unilever Plc Procédé de fabrication de granules colorés pour détergents
EP0219328A2 (fr) 1985-10-14 1987-04-22 Unilever Plc Composition détergente et son procédé de préparation
US4671886A (en) 1985-11-25 1987-06-09 The Procter & Gamble Company Process for coloring granular product by admixing with pigment/diluent premix
GB2199338A (en) * 1986-12-30 1988-07-06 Unilever Plc Coloured detergent particles
EP0289311A2 (fr) 1987-04-30 1988-11-02 Unilever Plc Procédé de préparation d'une composition détergente granulaire
EP0344629A1 (fr) 1988-06-03 1989-12-06 Henkel Kommanditgesellschaft auf Aktien Composition adsorbente granulaire avec une capacité de dégagement ameliorée
US5065883A (en) 1990-09-17 1991-11-19 Container Corporation Of America Tamper evident closure
EP0556923A1 (fr) 1992-02-18 1993-08-25 Colorsil B.V. Pigment de silicate mixte au zirconium dopé, procédé de préparation et produits contenant le pigment ou un pigment ainsi préparé
US5605883A (en) 1993-02-24 1997-02-25 Iliff; Robert J. Agglomerated colorant speckle exhibiting reduced colorant spotting
EP0702055A2 (fr) 1994-09-14 1996-03-20 Ciba-Geigy Ag Pigments organiques prêts à être mélangés
EP0882125A1 (fr) 1996-02-14 1998-12-09 The Procter & Gamble Company Procede d'obtention d'une composition de detergent a faible densite par agglomeration avec un double sel inorganique
WO1998016615A1 (fr) * 1996-10-15 1998-04-23 The Procter & Gamble Company Compositions particulaires colorees
EP0935343A1 (fr) 1997-07-08 1999-08-11 MASUDA, Tatsuji Bascule rs
WO2000027980A1 (fr) * 1998-11-06 2000-05-18 The Procter & Gamble Company Grains colores et compositions les renfermant
EP1305387A1 (fr) 2000-07-31 2003-05-02 Unilever Plc Composition coloree a mouchetures et compositions particulaires de detergent de lessive contenant ladite composition
EP1305387B1 (fr) * 2000-07-31 2005-01-19 Unilever Plc Composition coloree a mouchetures et compositions particulaires de detergent de lessive contenant ladite composition
EP1627909A1 (fr) 2004-07-22 2006-02-22 The Procter & Gamble Company Compositions détergentes contenant des particules colorées
WO2007006357A1 (fr) * 2005-07-11 2007-01-18 Unilever Plc Granules delivrant un colorant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3318622A1 (fr) * 2016-11-04 2018-05-09 Sociedad Anónima Minera Catalano-Aragonesa Particules colorées pour détergents et leur procédé de production

Also Published As

Publication number Publication date
ES2416281T3 (es) 2013-07-31
UA100110C2 (ru) 2012-11-26
PL2009086T3 (pl) 2013-10-31
EP2009086B1 (fr) 2013-03-27
MX2008007645A (es) 2009-03-04

Similar Documents

Publication Publication Date Title
EP1547984B1 (fr) Procédé et dispositif pour la consolidation du plâtre
EP2531564B1 (fr) Procédé pour la préparation de granules de noir de charbon
ES2379855T3 (es) Granulados de pigmento que contienen coadyuvantes de filtración inorgánicos
CN101291885A (zh) 低热膨胀铸造介质
CN107488049A (zh) 一种Al2O3‑SiO2质球形轻质耐火材料骨料
JP2008531454A (ja) 泡ガラス粒状体を製造する方法
CN109942275B (zh) 一种利用煤矸石生产的陶粒砂及其加工工艺
EP2009086A1 (fr) Procédé de coloration de minéraux non-adsorbants et le produit ainsi obtenu
JPH0326795A (ja) ゼオライト集塊形成工程および生成物
KR20120016296A (ko) 분말재료로부터 과립을 생산하는 방법
PL116770B1 (en) Method of manufacture of pigment preparation for dyeingin the cake of linear polyesters
US5718755A (en) Preparation and use of iron oxide black pigment granules
CN108675779A (zh) 一种复合铝铬砖及其制备方法
CN204768344U (zh) 超微细硅树脂胶囊化磷系阻燃剂制备用加热搅拌装置
RU2103242C1 (ru) Пенобетон на магнезиальном вяжущем и способ его изготовления
US3096291A (en) Process of preparing dry granular compositions
CN107098681A (zh) 一种可相变控温的瓷砖及其制备方法
JPH06293576A (ja) 多孔性シリカ−炭素複合体及びその製造方法
CA2024800C (fr) Methode pour ameliorer la fluidite du chlorure de cyanuryle solide
RU2528814C2 (ru) Способ получения стеклокерамзита и порокерамики из трепелов и опок
JPH09241698A (ja) 高嵩密度粒状洗剤組成物の製造方法
JP4152150B2 (ja) ムライトウィスカーの製造方法
RU2244695C1 (ru) Способ получения легковесных высокопрочных керамических гранул
US3645004A (en) Drying of efflorescent material
WO2002032235A2 (fr) Methode de fabrication de produits sales de qualite alimentaire, mineral ou pharmaceutique

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC MT NL PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA HR MK RS

17P Request for examination filed

Effective date: 20090618

AKX Designation fees paid

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC MT NL PL PT RO SE SI SK TR

17Q First examination report despatched

Effective date: 20090917

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC MT NL PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 603433

Country of ref document: AT

Kind code of ref document: T

Effective date: 20130415

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602007029278

Country of ref document: DE

Effective date: 20130529

REG Reference to a national code

Ref country code: RO

Ref legal event code: EPE

REG Reference to a national code

Ref country code: DE

Ref legal event code: R082

Ref document number: 602007029278

Country of ref document: DE

Representative=s name: SCHAEFER, MATTHIAS, DIPL.-ING., DE

Ref country code: DE

Ref legal event code: R082

Ref document number: 602007029278

Country of ref document: DE

Representative=s name: SCHAEFER, MATTHIAS W., DIPL.-ING., DE

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

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: 20130327

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: 20130627

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: 20130327

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

Ref country code: GB

Payment date: 20130605

Year of fee payment: 7

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 603433

Country of ref document: AT

Kind code of ref document: T

Effective date: 20130327

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

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: 20130628

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: 20130327

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: 20130327

Ref country code: SI

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: 20130327

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20130327

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

Ref country code: BE

Payment date: 20130617

Year of fee payment: 7

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

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: 20130327

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: 20130327

Ref country code: IS

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: 20130727

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: 20130327

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: 20130729

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: 20130327

Ref country code: AT

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: 20130327

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

Ref country code: RO

Payment date: 20130618

Year of fee payment: 7

REG Reference to a national code

Ref country code: PL

Ref legal event code: T3

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

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: 20130327

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

Ref country code: IT

Payment date: 20130621

Year of fee payment: 7

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: 20130327

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: 20130327

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

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

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20140103

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20140228

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602007029278

Country of ref document: DE

Effective date: 20140103

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

Ref country code: CH

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

Effective date: 20130630

Ref country code: IE

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

Effective date: 20130626

Ref country code: LI

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

Effective date: 20130630

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

Ref country code: FR

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

Effective date: 20130701

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

Ref country code: PL

Payment date: 20140626

Year of fee payment: 8

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

Ref country code: RO

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

Effective date: 20140626

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20140626

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

Ref country code: MT

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: 20130327

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

Ref country code: IT

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

Effective date: 20140626

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

Ref country code: GB

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

Effective date: 20140626

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

Ref country code: TR

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: 20130327

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

Ref country code: HU

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

Effective date: 20070626

Ref country code: LU

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

Effective date: 20130626

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

Ref country code: PL

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

Effective date: 20150626

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: 20140630

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

Effective date: 20230530

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

Ref country code: ES

Payment date: 20230713

Year of fee payment: 17

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

Ref country code: DE

Payment date: 20240617

Year of fee payment: 18