FR2657354A1 - Composite pigment containing titanium oxide and process for obtaining it - Google Patents
Composite pigment containing titanium oxide and process for obtaining it Download PDFInfo
- Publication number
- FR2657354A1 FR2657354A1 FR9001019A FR9001019A FR2657354A1 FR 2657354 A1 FR2657354 A1 FR 2657354A1 FR 9001019 A FR9001019 A FR 9001019A FR 9001019 A FR9001019 A FR 9001019A FR 2657354 A1 FR2657354 A1 FR 2657354A1
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- adjuvant
- powder
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Classifications
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/0081—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound
- C09C1/0084—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound containing titanium dioxide
- C09C1/0087—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound containing titanium dioxide only containing titanium dioxide and silica or silicate
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/0081—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound
- C09C1/0084—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound containing titanium dioxide
Abstract
Description
PIGMENT COMPOSITE CONTENANT DE L'OXYDE DE TITANE ET PROCEDE D'OBTENTION
L'invention concerne des pigments composites contenant de l'oxyde de titane, un (ou plusieurs) autre(s) minéral(aux) et un procédé d'obtention des pigments composites considérés.COMPOSITE PIGMENT CONTAINING TITANIUM OXIDE AND PROCESS FOR OBTAINING
The invention relates to composite pigments containing titanium oxide, one (or more) other mineral (s) and a process for obtaining the composite pigments under consideration.
Les produits de ce type sont connus et sont généralement obtenus par co-broyage intense de TiO2 et d'un (ou plusieurs) autre(s) minéral(aux) tels que feldspath, mica, talc, etc... Un tel procédé est décrit par exemple dans la demande de brevet français FR-A-2575170.Products of this type are known and are generally obtained by intense co-grinding of TiO2 and of one (or more) other mineral (s) such as feldspar, mica, talc, etc. Such a process is described for example in French patent application FR-A-2575170.
Cependant, ce procédé conduit à des produits pulvérulents ayant une prise d'huile trop élevée ( > 30 g/100 g suivant la norme AFNOR NF T30-022) et/ou une blancheur insuffisante ( < 90 suivant le norme NF Q-003-038).However, this process leads to powdery products having too high an oil uptake (> 30 g / 100 g according to the AFNOR standard NF T30-022) and / or insufficient whiteness (<90 according to the standard NF Q-003- 038).
Les produits selon l'invention possèdent une prise d'huile < 30 g/100 g et une blancheur }90. The products according to the invention have an oil uptake <30 g / 100 g and a whiteness} 90.
Les produits selon l'invention sont les pigments composites essentiellement constitués de Ti02 et d'un autre adjuvant minéral obtenu sous forme de poudre, dont la granulométrie moyenne est supérieure ou égale à 1 gm et de préférence k 2 Mm. The products according to the invention are the composite pigments essentially consisting of TiO 2 and of another mineral adjuvant obtained in the form of powder, the average particle size of which is greater than or equal to 1 gm and preferably k 2 Mm.
Par la granulométrie moyenne (D50) on entend la taille des particules pour laquelle 50% en volume possède une taille supérieure ou égale à cette dimension D50.By average particle size (D50) is meant the particle size for which 50% by volume has a size greater than or equal to this dimension D50.
La taille maximale (100% passant) sera désigné par D100.The maximum size (100% passing) will be designated by D100.
De façon plus précise, la granulométrie est telle qu' au plus 10% (en volume) des grains sont de taille inférieure à 1 gm et au plus 10% (en volume) sont de taille supérieure à 30 Mm. More precisely, the particle size is such that at most 10% (by volume) of the grains are of size less than 1 gm and at most 10% (by volume) are of size greater than 30 mm.
Ce produit est constitué de grains d'adjuvant minéral ayant leur surface tapissée de particules de Ti02 et agglomérés en particules individuelles dont la taille moyenne est k 1 Mm et de préférence k 2 Um. This product consists of grains of mineral additive having their surface lined with TiO 2 particles and agglomerated into individual particles whose average size is k 1 Mm and preferably k 2 Um.
Par "TiO2,, on entend le Ti02 pur, le TiO2 pour peintures (par ex. les références RL60 ou RL68 de THANN et MULHOUSE) et/ou le TiO2 pour plastiques (par ex. la référence RL90 de la même société). By "TiO2 ,, we mean pure Ti02, TiO2 for paints (eg the references RL60 or RL68 from THANN and MULHOUSE) and / or TiO2 for plastics (eg the reference RL90 from the same company).
Les adjuvants appartiennent au groupe des produits siliceux, de la famille des silicates, des carbonates ou de sulfates.Adjuvants belong to the group of siliceous products, of the family of silicates, carbonates or sulfates.
Les principaux représentants en sont le feldspath, le mica, le talc, la wollastonite, le silicate de Ca, la barytine, le calcin, utilisés seuls ou en mélange.The main representatives are feldspar, mica, talc, wollastonite, Ca silicate, barite, cullet, used alone or as a mixture.
Le rapport pondéral adjuvant/ "tu02" est compris entre 40/60 et 90/10.The adjuvant / "tu02" weight ratio is between 40/60 and 90/10.
Au-dessous de 40/60, le prix du pigment composite est trop élevé; en-dessous de 90/10, la blancheur obtenue est insuffisante.Below 40/60, the price of the composite pigment is too high; below 90/10, the whiteness obtained is insufficient.
La liaison entre les grains TiO2 et ceux de l'adjuvant est une liaison forte de type chimique.The bond between the TiO2 grains and those of the adjuvant is a strong bond of chemical type.
Le procédé consiste: a à mélanger des poudres de "tu02" (submicronique) et d'adjuvant(s) avec un rapport pondéral adjuvant/"TiO2" compris entre 60/40 et 90/10.The method consists in: a mixing powders of "tu02" (submicron) and of adjuvant (s) with an adjuvant / "TiO2" weight ratio of between 60/40 and 90/10.
2 . à mettre l'ensemble en suspension aqueuse, contenant jusqu'à 75% de matière sèche. 2. to put the whole in aqueous suspension, containing up to 75% of dry matter.
- à atomiser cette suspension de manière à obtenir une poudre finale dont la granulométrie moyenne D50 k 1 gm (et de préférence k 2 pm) est telle qu au plus 10% en volume soit inférieure 1 gm et au plus 10% > 30 Mm. - To atomize this suspension so as to obtain a final powder whose average particle size D50 k 1 gm (and preferably k 2 pm) is such that at most 10% by volume is less than 1 gm and at most 10%> 30 Mm.
On peut éventuellement ajouter au mélange initial un (ou des) agent(s) mouillant(s), dispersant(s) ou défloculant(s), de 0,1 à 1% (en poids) % par rapport à la matière sèche et/ou une huile de silicone ou un silane de préférence entre 1 et 10% en poids/matière sèche.It is optionally possible to add to the initial mixture a wetting agent (s), dispersant (s) or deflocculant (s), from 0.1 to 1% (by weight)% relative to the dry matter and / or a silicone oil or a silane preferably between 1 and 10% by weight / dry matter.
Au-delà des valeurs limites de 0,1% à 1%, la viscosité à fort taux de cisaillement (1000s .1) de la suspension est trop importante, ce qui interdit l'atomisation de suspension contenant plus de 75% de matières sèches.Beyond the limit values of 0.1% to 1%, the viscosity at high shear rate (1000s .1) of the suspension is too high, which prohibits the atomization of suspension containing more than 75% of dry matter .
Au-dessous de 1% d'huile de silicone ou silane, la tenue de TiO2 sur l'adjuvant est limitée.Below 1% of silicone or silane oil, the resistance of TiO2 on the adjuvant is limited.
Au-dessus de 10% d'huile de silicone ou silane, la blancheur n'est pas atteinte.Above 10% silicone or silane oil, the whiteness is not reached.
La granulométrie moyenne de l'adjuvant entrant dans le mélange (D50) est inférieure ou égale à 5 Mm; il comprend au plus 10% en volume de particules k 5 Mm. The average particle size of the adjuvant entering the mixture (D50) is less than or equal to 5 mm; it comprises at most 10% by volume of particles k 5 Mm.
L'invention sera mieux comprise à l'aide des exemples suivants:
EXEMPLE 1
Des échantillons ont été préparés dans les conditions suivantes: - mélange de:
feldspath EAL (SOGEREM) prébroyé mécaniquement et possédant la granulométrie suivante:
D50 = 3,20 Mm D100 = 20 Mm
50 . TiO2 "Rectapur" de PROLABO possédant la granulométrie suivante
D50 = 0,48 Mm D100 = 6 gm dans les proportions pondérales respectives 70/30.The invention will be better understood using the following examples:
EXAMPLE 1
Samples were prepared under the following conditions: - mixture of:
feldspar EAL (SOGEREM) mechanically pre-ground and having the following particle size:
D50 = 3.20 Mm D100 = 20 Mm
50. PROLABO TiO2 "Rectapur" with the following particle size
D50 = 0.48 Mm D100 = 6 gm in the respective weight proportions 70/30.
On a ajouté à ce mélange 0,2% en poids d'un agent dispersant nO 6768 de
STEPAN (polycarboxylate d'ammonium), ainsi que 5,5% en poids d'huile de silicone "RHODORSIL 10646" de RHONE-POULENC. 0.2% by weight of a dispersing agent No. 6768 of
STEPAN (ammonium polycarboxylate), as well as 5.5% by weight of silicone oil "RHODORSIL 10646" from RHONE-POULENC.
L'atomisation a été conduite sur atomiseur de laboratoire Mini Spray Dryer 5-90 de BUCHI dans les conditions suivantes:
Suspension à 60% en matière sèche
Température d'entrée: 2200C
Température de sortie: 1300C
Débit d'alimentation de la suspension : 0,8 1/h
Les résultats obtenus concernant la granulométrie finale (déterminée avec l'appareil Horiba Kappa 700) et les propriétés de prise d'huile et de blancheur selon les normes citées, sont les suivantes - D50 = 16,15 M m - D100= 40 gm - prise d'huile: 20g/lOOg - blancheur : 91
EXEMPLE 2
Mêmes caractéristiques que pour l'Exemple 1 sauf - EAL prébroyé mécaniquement et possédant la granulométrie D50=0,28 Mm
D100=2 gm - 1% par rapport à la matrice sèche d'huile de S; Rhodersil 10646.The atomization was carried out on a BUCHI Mini Spray Dryer 5-90 laboratory atomizer under the following conditions:
60% solids suspension
Inlet temperature: 2200C
Outlet temperature: 1300C
Suspension feed rate: 0.8 1 / h
The results obtained concerning the final particle size (determined with the Horiba Kappa 700 device) and the properties of oil setting and whiteness according to the standards cited, are as follows - D50 = 16.15 M m - D100 = 40 gm - oil intake: 20g / lOOg - whiteness: 91
EXAMPLE 2
Same characteristics as for Example 1 except - EAL mechanically pre-ground and having the particle size D50 = 0.28 mm
D100 = 2 gm - 1% relative to the dry matrix of S oil; Rhodersil 10646.
L'atomisation a été conduite dans les mêmes conditions que dans l'Exemple 1.The atomization was carried out under the same conditions as in Example 1.
Les caractéristiques de la poudre composite obtenue sont les suivantes - blancheur : 92 - prise d'huile : 34g/100 g - D50 = 3,5 gm - D100 = 10 Mn. The characteristics of the composite powder obtained are as follows - whiteness: 92 - oil setting: 34 g / 100 g - D50 = 3.5 gm - D100 = 10 Mn.
Claims (16)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9001019A FR2657354A1 (en) | 1990-01-19 | 1990-01-19 | Composite pigment containing titanium oxide and process for obtaining it |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9001019A FR2657354A1 (en) | 1990-01-19 | 1990-01-19 | Composite pigment containing titanium oxide and process for obtaining it |
Publications (1)
Publication Number | Publication Date |
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FR2657354A1 true FR2657354A1 (en) | 1991-07-26 |
Family
ID=9393193
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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FR9001019A Withdrawn FR2657354A1 (en) | 1990-01-19 | 1990-01-19 | Composite pigment containing titanium oxide and process for obtaining it |
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FR (1) | FR2657354A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2678630A1 (en) * | 1991-07-03 | 1993-01-08 | Rech Expl Minieres Ste Gle | Composite pigment containing titanium oxide and process of preparation |
US5562763A (en) * | 1992-04-07 | 1996-10-08 | Merck Patent Gesellschaft Mit Beschrankter Haftung | Process for the preparation of composite pigments |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
LU40959A1 (en) * | 1961-12-14 | 1962-03-07 | ||
US3253939A (en) * | 1962-02-19 | 1966-05-31 | Laporte Titanium Ltd | Titanium dioxide pigments |
US3453131A (en) * | 1966-01-05 | 1969-07-01 | Oxford Paper Co | Composite colloidal pigment particles,their formation and suspensions thereof |
US3459574A (en) * | 1964-11-20 | 1969-08-05 | Du Pont | Opacifying pigment glass composition |
FR2386590A1 (en) * | 1977-04-04 | 1978-11-03 | Noranda Mines Ltd | NEW CORROSION INHIBITOR PIGMENTS BASED ON ZINC MOLYBDATE COMPOUNDS |
-
1990
- 1990-01-19 FR FR9001019A patent/FR2657354A1/en not_active Withdrawn
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
LU40959A1 (en) * | 1961-12-14 | 1962-03-07 | ||
US3253939A (en) * | 1962-02-19 | 1966-05-31 | Laporte Titanium Ltd | Titanium dioxide pigments |
US3459574A (en) * | 1964-11-20 | 1969-08-05 | Du Pont | Opacifying pigment glass composition |
US3453131A (en) * | 1966-01-05 | 1969-07-01 | Oxford Paper Co | Composite colloidal pigment particles,their formation and suspensions thereof |
FR2386590A1 (en) * | 1977-04-04 | 1978-11-03 | Noranda Mines Ltd | NEW CORROSION INHIBITOR PIGMENTS BASED ON ZINC MOLYBDATE COMPOUNDS |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2678630A1 (en) * | 1991-07-03 | 1993-01-08 | Rech Expl Minieres Ste Gle | Composite pigment containing titanium oxide and process of preparation |
US5562763A (en) * | 1992-04-07 | 1996-10-08 | Merck Patent Gesellschaft Mit Beschrankter Haftung | Process for the preparation of composite pigments |
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