KR20140100984A - Pigment dispersion - Google Patents

Abstract

The present invention relates to a process for preparing aqueous pigment dispersions substantially free of organic binders, comprising mixing at least one water-soluble or water-dispersible silane compound with colloidal silica particles To form silanized colloidal silica particles in an aqueous dispersion wherein the at least one silane compound is mixed with the colloidal silica particles such that the weight ratio of silane to silica is from about 0.2 to about 1.5 ); And mixing the silanized colloidal silica particles with an organic and / or inorganic pigment to form a substantially aqueous pigment dispersion wherein the weight ratio of silica to pigment is from about 0.001 to about 0.8. The present invention also relates to an aqueous pigment dispersion according to the method defined herein and to a pigment dispersion substantially free of organic coupling agent, wherein the weight ratio of silane to silica is from about 0.2 to about 1.5, and the silanized colloidal silica particles And organic and / or inorganic pigments wherein the weight ratio of silica to pigment is from about 0.001 to about 0.8.

Description

PIGMENT DISPERSION [0002]

The present invention relates to an aqueous pigment dispersion, a process for producing the dispersion, and uses thereof.

Inorganic pigments are often incorporated into various polymers as whiteners, tinting agents or opacifiers. A pigment such as TiO ₂ is particularly useful for this purpose, which is due to very effectively scatter light. The pigments for example, can be present in the pigment dispersion known in distinct US 5,886,069 which describes a TiO ₂ particles having inorganic particles dispersed in the TiO ₂ particle surfaces. However, such dispersions are not always sufficiently stable, and are difficult to store for long periods of time without destabilization or gelation leading to significantly lower light scattering efficiency. The dispersion may also have the problem of TiO ₂ particles coming into close contact with one another and optically crowding the TiO ₂ particles. As a result of this, the hiding power and tinting strength can be considerably reduced. Extenders are added to the paint formulation to place the TiO ₂ particles at regular intervals to preserve the scattering efficiency. However, the distribution of the extender is difficult and affects hiding power. It is desirable to provide an aqueous pigment dispersion in which no dispersing agent such as a surfactant is present. Surfactants can impart foaming problems to the dispersion and reduce the resistance to water and chemicals.

WO 2004/035474 A1 describes silanized colloidal silica particles combined with an organic binder. However, organic binders can interfere with the stability of the pigment dispersion. Additional energy input may also be required since the method of dispersing the pigment in the presence of an organic binder requires a higher shear force. In addition, the presence of the organic binder reduces the amount of dispersible pigment and reduces the light scattering efficiency obtained.

The present invention relates to a process for providing an aqueous pigment dispersion having improved stability. It is a further object of the present invention to provide a method of making storage and shelf life longer and to provide acceptable pigment properties such as light scattering efficiency when mixed with a formulation comprising paint.

The present invention relates to a process for preparing a substantially aqueous pigment dispersion substantially free of organic binders, comprising at least one water-soluble or water-dispersible silane compound and a colloidal silica Mixing the particles to form silanized colloidal silica particles in an aqueous dispersion, wherein the weight ratio of silane to silica is from about 0.2 to about 1.5; and mixing the at least one silane compound with colloidal silica Mixed with the particles); And mixing the silanized colloidal silica particles with an organic and / or inorganic pigment to form the substantially aqueous pigment dispersion wherein the weight ratio of silica to pigment is from about 0.001 to about 0.8.

The term "essentially or substantially free from organic binder" means that the organic binder content in the aqueous pigment dispersion is less than or equal to about 15 wt%, such as less than or equal to about 10 wt% By weight or less, for example, about 3% by weight or less, or about 1% by weight or less, or about 0.1% by weight or less. Therefore, according to one embodiment, the dispersion is prepared such that the resulting dispersion contains an organic binder in an amount below the limits disclosed above.

According to one embodiment, the silane and colloidal silica particles have a weight ratio of silane to silica ranging from about 0.25 to about 1.5, such as from about 0.3 to about 1.5, or from about 0.35 to about 0.8, or from about 0.4 to about 0.8 .

The silane compound may form a stable siloxane covalent bond (Si-O-Si) with the silanol group or may be connected to the silanol group by, for example, hydrogen bonding at the surface of the colloidal silica particle.

According to one embodiment, the mixing of silane and colloidal silica particles is carried out continuously at a temperature of, for example, from about 20 캜 to about 95 캜, or from about 50 캜 to about 75 캜, such as from about 60 캜 to about 70 캜 . The silane can be slowly added to the silica particles under controlled agitation at a controlled rate, the rate being such that the colloidal silica surface area (on the colloidal silica particles) is 1 nm ² and the silane molecule per hour (h) For example from about 0.1 to about 10, or from about 0.5 to about 5, such as from about 1 to about 2. The addition of the silane can be continued for a suitable time depending on the rate of addition, the amount of silane to be added and the degree of silanization desired. However, the addition of the silane can continue for about 5 hours or less, for example about 2 hours or less, until an appropriate amount of silane is added. The amount of silane added to the colloidal silica particles is suitably from about 0.1 to about 6, such as from about 0.3 to about 3, or from about 1 to about 2, silane molecules per 1 nm ² of the surface area of the colloidal silica particles.

The mixing of the silane and silica may be carried out at a pH of from about 1 to about 13, for example from about 6 to about 12, or from about 7.5 to about 11, or from about 9 to about 10.5.

The colloidal silica particles referred to herein as silica sols are, for example, precipitated silica, micro silica, silica fume, pyrogenic silica, fumed silica, silica) or a silica gel having sufficient purity, and mixtures thereof.

The colloidal silica particles and the silica sol may be modified and may contain other elements such as amine, aluminum and / or boron, and may be present in the particles and / or in the continuous phase. Boron-modified silica sols are disclosed, for example, in US 2,630,410. The aluminum modified silica particles suitably have an Al ₂ O ₃ content of from about 0.05 wt% to about 3 wt%, such as from about 0.1 wt% to about 2 wt%. Methods for making aluminum-modified silica sols are further disclosed, for example, in Iler, K. Ralph, "The Chemistry of Silica", pages 407-409, John Wiley & Sons (1979) and US 5 368 833.

The colloidal silica particles used are suitably from about 2 nm to about 150 nm, such as from about 2 nm to about 100 nm, or from about 3 nm to about 50 nm, or from about 4 nm to about 40 nm, or from about 4 nm to about 15 nm, or from about 5 nm to about 12 nm. Suitably, the colloidal silica particles have a particle size of from about 20 m ² / g to about 1500 m ² / g, such as from about 50 m ² / g to about 900 m ² / g, or from about 70 m ² / g to about 600 m ² / g, or from about 200 m ² / g to about 500 m ² / g.

The colloidal silica particles may have a narrow particle size distribution, for example, a low relative standard deviation of the particle size. The relative standard deviation of the particle size distribution is the ratio of the standard deviation of the particle size distribution to the average particle size by numbers. The relative standard deviation of the particle size distribution may be less than about 60% (by numbers), such as about 30% or less, or about 15% or less.

The colloidal silica particles are suitably dispersed in an aqueous solvent to form an aqueous silica sol and are suitably selected from the group consisting of K ⁺ , Na ⁺ , Li ⁺ , NH ₄ ⁺ , organic cations, primary, secondary, tertiary and quaternary amines , Or a mixture thereof. However, colloidal silica dispersed in, for example, a partial organic dispersion comprising a lower alcohol, acetone or a mixture thereof may be used, and the volume of the organic portion may suitably be in the range of about 1 volume % To about 20% by volume, such as from about 1% by volume to about 10% by volume, or from about 1% by volume to about 5% by volume. According to one embodiment, the colloidal silica particles have a negative charge. Suitably, the stoichiometric silica content is from about 1% to about 80%, such as from about 5% to about 80%, or from about 10% to about 80%, such as from about 20% About 80 wt%, such as about 25 wt% to about 70 wt%, or about 30 wt% to about 60 wt%. The pH of the silica sol is suitably from about 1 to about 13, for example from about 6 to about 12, or from about 7.5 to about 11. However, for aluminum-modified silica sols, the pH is suitably from about 1 to about 12, or from about 3.5 to about 11.

The silica sol may have an S-value of from about 20 to about 100, for example from about 30 to about 90, or from about 60 to about 90.

The S-value is characterized by the extent of aggregation of the colloidal silica particles, for example, the degree of aggregate or microgel formation. The S-value was calculated using the method described in J. Phys. Chem. 60 (1956), 955-957 by Iler, R.K. &Amp; Dalton, R.L.

The S-value depends on the silica content, the viscosity and the density of the colloidal silica particles. High S-values indicate low microgel content. The S-value is expressed, for example, by weight percent of SiO ₂ present in the dispersed phase of the silica sol. The degree of microgel can be adjusted, for example, in a manufacturing process as described further in US 5368833.

According to one embodiment, a silicate, such as an alkali metal silicate, such as sodium silicate, potassium silicate or lithium silicate, may be mixed with silanized colloidal silica particles to further increase stability. According to one embodiment, the molar ratio of silica to M ₂ O (where M is an alkali metal) is from about 4 to about 20, such as from about 5 to about 15, such as from about 6 to about 11 to be.

According to one embodiment, suitable silane compounds to be mixed with the colloidal silica particles are epoxysilane and silane compounds comprising glycidoxy or glycidoxypropyl groups; Tris- (trimethoxy) silane, octyltriethoxysilane, methyltriethoxysilane, methyltrimethoxysilane; Isocyanate silanes, such as tris- [3- (trimethoxysilyl) propyl] isocyanurate; Gamma-mercaptopropyltrimethoxysilane, bis- (3- [triethoxysilyl] propyl) polysulfide, and beta - (3,4-epoxycyclohexyl) -ethyltrimethoxysilane; Glycidoxypropyltrimethoxysilane, gamma-glycidoxypropylmethyldiethoxysilane, (3) a silane containing epoxy group, a glycidoxy group and / or a glycidoxypropyl group-containing silane such as gamma-glycidoxypropyltrimethoxysilane, -Glycidoxypropyl) trimethoxysilane, (3-glycidoxypropyl) hexyltrimethoxysilane, and beta - (3,4-epoxycyclohexyl) -ethyltriethoxysilane; Silane containing a vinyl group such as vinyltriethoxysilane, vinyltrimethoxysilane, vinyltris- (2-methoxyethoxy) silane, vinylmethyldimethoxysilane, vinyltriisopropoxysilane; Gamma-methacryloxypropyltrimethoxysilane, gamma-methacryloxypropyl, triisopropoxysilane, gamma-methacryloxypropyltriethoxysilane, octyltrimethyloxysilane, ethyltrimethoxysilane, propyltriethoxy Silane, phenyltrimethoxysilane, 3-mercaptopropyltriethoxysilane, cyclohexyltrimethoxysilane, cyclohexyltriethoxysilane, dimethyldimethoxysilane, 3-chloropropyltriethoxysilane, 3-methacryl Butyl triethoxysilane, trimethylethoxysilane, phenyldimethylethoxysilane, hexamethyldisiloxane, trimethylsilyl chloride, vinyltriethoxysilane, hexamethyldisilazane, and mixtures thereof. . US 4,927,749 further describes suitable silanes that can be used in the present invention.

According to one embodiment, at least about 1% by number of the silanol surface groups on the colloidal silica particles can be bonded or linked to the silane group of the silane compound, for example at least about 5%, or at least about 10%, or at least About 30%, or at least about 50% of the silane group is bonded or linked to the silane group.

According to one embodiment, the silane compound is diluted, for example, with water, prior to mixing with the colloidal silica particles such that the weight ratio of silane to water is suitably from about 1: 8 to about 8: 1, or from about 3: 1 to about 1: : 3, such as from about 1.5: 1 to about 1: 1.5, to form a premix of silane and water. The resulting silane-water solution is substantially clear and stable and is easy to mix with colloidal silica particles. Upon continuous addition of the silane to the colloidal silica particles, the mixing continues for about 1 second to about 30 minutes, or about 1 minute to about 10 minutes after silane addition is stopped.

According to one embodiment, the pigment is an inorganic pigment. According to one embodiment, the inorganic pigment is selected from the group consisting of calcium carbonate, barium sulfate, iron (II, III) oxides such as Fe ₃ O ₄ , a-Fe ₂ O ₃ , iron (III) FeOOH, chromium (III) oxide, cobalt compounds such as cobalt aluminate, zinc oxide, zinc sulfide, basic lead sulfate, basic lead carbonate, antimony oxide, lithopone, Titanium, such as rutile form or TiO _{2 in an} anatase form, or mixtures thereof. According to one embodiment, the pigment may be a filler material having clay or pigment properties such as kaolin, such as fumed silica, microsilica, precipitated silica or silica gel.

According to one embodiment, the pigment has a particle size in the range of from about 10 nm to about 5000 nm, such as from about 100 nm to about 1000 nm, or from about 100 nm to about 500 nm, or from about 200 nm to about 400 nm.

According to one embodiment, the weight ratio of silica to pigment is from about 0.01 to about 0.7, such as from about 0.01 to about 0.6, or from about 0.01 to about 0.5, or from about 0.01 to about 0.4, or from about 0.01 to about 0.3, Or from about 0.01 to about 0.2, or from about 0.02 to about 0.05, of the pigment is mixed with the silanized colloidal silica particles.

According to one embodiment, a mixer, such as a dissolver turbine at 1400 rpm, is used to mix the pigment with silanized colloidal silica particles. The mixing time can be from about 1 minute to about 40 minutes, such as from about 5 minutes to about 30 minutes, or for example from about 10 minutes to about 20 minutes. The mixing temperature may be from about 1 째 C to about 80 째 C, such as from about 10 째 C to about 60 째 C, or from about 20 째 C to about 40 째 C. According to one embodiment, the radial velocity is from about 1 m / s to about 50 m / s, such as from about 5 m / s to about 35 m / s, such as from about 15 m / About 25 m / s.

One of the many pigments, the TiO ₂ pigment, is a conventional rutile or anatase modification produced by the chloride or sulfate process. According to one embodiment, rutile TiO ₂ particles having a particle size of from about 100 nm to about 500 nm and produced by the chloride process are used. According to one embodiment, the TiO ₂ particles used to make the TiO ₂ pigment are basic TiO ₂ , and here TiO ₂ particles directly removed from the oxidized TiCl ₄ before the finishing step and / . In the sulfate process, basic TiO ₂ is referred to as TiO ₂ particles before the surface treatment step is applied. Alternatively, the TiO ₂ particles used to make the pigments of the present invention are finished TiO ₂ particles and may be prepared by conventional finishing steps and / or hydrous oxides such as alumina, silica, zirconia, etc. Or TiO ₂ particles surface treated with a combination of these materials. Singer oxide is, for about 16% by weight or less, for example, based on the weight of the total TiO ₂ pigment product may be up to about 10% by weight.

The present invention also relates to aqueous pigment dispersions obtainable by the process as defined herein.

The present invention also relates to aqueous pigment dispersions substantially free of organic binders, wherein the weight ratio of silica to silanized colloidal silica particles, wherein the weight ratio of silane to silica is from about 0.2 to about 1.5, 0.0 > and / or < / RTI > about 0.8.

According to one embodiment, up to about 20%, such as up to about 10% by volume or up to about 5% by volume of a water soluble or water dispersible organic solvent (such as a lower alcohol) can be included in the prepared aqueous pigment dispersion have. The dispersion may be formed from an aqueous dispersion comprising a part of an organic solvent (e.g., silica sol, silane compound), or a pigment in which at least a part of the organic solvent or medium is dispersed.

According to one embodiment, the pigment is an inorganic pigment. According to one embodiment, the pigment is present in the resulting pigment dispersion in an amount of from about 25% to about 85%, such as from about 50% to about 80%, or from about 60% to about 75% Are mixed in the obtained amount. According to one embodiment, the weight ratio of silica to pigment in the pigment dispersion obtained is from about 0.01 to about 0.7, for example from about 0.01 to about 0.6, or from about 0.01 to about 0.5, or from about 0.01 to about 0.4, or from about 0.01 To about 0.3, or from about 0.01 to about 0.2, or from about 0.02 to about 0.05.

The total content of silica in the pigment dispersion prepared comprises modified silanized silica particles which may be present in the prepared dispersion and silica present in the non-modified silica particles. The total amount of silane compound is based on all silane compounds connected or bonded by silane groups or silane derivatives and all freely dispersed or dissolved silane compounds. Therefore, the weight ratio of silane to silica in the prepared pigment dispersion, including both the liberated groups and the connected or bonded groups, is mixed within the weight ratio of silane and silica components, for example from about 0.25 to about 1.5, such as about 0.3 to about 1.2, or about 0.35 to about 0.8, or about 0.4 to about 0.8.

According to one embodiment, the aqueous pigment dispersion comprises colloidal silica particles freely dispersed and / or colloidal silica particles prepared from the silane compounds and colloidal silica particles disclosed herein, and silanized colloidal silica particles.

According to one embodiment, the aqueous pigment dispersion comprises the inorganic pigments disclosed herein. The characteristics of the components contained in the aqueous pigment dispersion are further described in the method section.

The stability of the pigment dispersion is easy to handle and apply in its use since it can be stored and does not need to be prepared just prior to use. Therefore, the dispersions already prepared can easily be used directly. Also, the dispersion is beneficial in the sense that it does not contain deleterious amounts of toxic components.

The dispersion may contain, in addition to the silanized colloidal silica particles, some degree of non-silanized colloidal silica particles depending on the size of the silica particles, the weight ratio of the silane to the silica, the form of the mixed silane compound, have. Suitably, at least about 40 weight percent, at least about 65 weight percent, or at least about 90 weight percent, or at least about 95 weight percent, such as at least about 99 weight percent, of the colloidal silica particles are silanized. The dispersion may contain unbound silane compounds that are freely dispersed to some extent in addition to silane groups in the form of silane groups or silane derivatives bonded or connected to the surface of the silica particles. Suitably at least about 40 weight percent, such as at least about 60 weight percent, or at least about 75 weight percent, such as at least about 90 weight percent, or at least about 95 weight percent of the silane compound is bonded to the surface of the silica particles, .

According to one embodiment, the pigment dispersion prepared comprises from about 1% to about 80%, such as from about 5% to about 80%, or from about 10% to about 80% by weight, % To about 80 wt%, such as from about 25 wt% to about 70 wt%, or from about 30 wt% to about 60 wt%.

The resulting pigment dispersions can be used in coating applications including construction coatings, interior and exterior coatings, stains, industrial coatings (e.g. coil coatings, paper coatings as well as protective coatings) Or other applications including papermaking, laminate and composite materials, such as paper, plastic, rubber, concrete and cementitious systems, inks, ceramics such as ceramic tiles, It is suitable. Pigment dispersions can also be used in painted or non-absorbed substrates, such as glass-fiber wallpaper, to reduce or prevent bubble formation in, for example, plaster or putties .

The present invention is disclosed, which may be varied in a number of ways. The following examples will further illustrate how to practice the described invention without limiting the scope of the invention.

All parts and percentages are by weight unless otherwise stated.

The present invention relates to a process for providing an aqueous pigment dispersion having improved stability. The present invention provides a method of making storage and shelf life longer and provides acceptable pigment properties such as light scattering efficiency when mixed with a formulation comprising paint.

The silica sol used had a silica content of 13.4 wt.% Unless otherwise stated, and Sample 11 and Sample 12 had a silica content of 4.46 wt.% Before being used as a pigment dispersant. The colloidal silica particles of the sol are modified with gamma-glycidoxypropyltrimethoxysilane. Silane modification is carried out at 60 占 폚 as described in patent application WO 2004/035474 A1. The different colloidal silica dispersions used in this evaluation are listed in Table 1 below and also include the conventionally used polyacrylates as references.

number Silica sol (particle size and degree of silane modification) One 5 nm, silane / SiO ₂ : 0.4 2 5 nm, the silane / SiO _2: 0.2 3 4 nm, silane / SiO ₂ : 0.2 4 4 nm, silane / SiO ₂ : 0.4 5 5 nm, no silane 6 7 nm, silane-free, modified with aluminate 7 7 nm, silane / SiO ₂ : 0.2 8 12 nm, no silane 9 12 nm, a silane / SiO _2: 0.15 10 Polyacrylate (Dispex 40N), 0.4 wt% 11 5 nm, silane / SiO ₂ : 0.4 12 5 nm, silane / SiO ₂ : 0.4 13 5 nm, silane / SiO ₂ : 0.4

Manufacture of pigment paste

300 g of titanium dioxide (a highly grounded titania pigment, Tiona 595, supplied by Univar) was added to 100 g of the diluted silica sol according to Table 1 under gentle agitation for about 20 seconds to give 75% by weight of pigment A paste was obtained (see Table 2). The pigment is dispersed at 1400 rpm for 10 minutes in a 40 mm diameter dissolver turbine to provide a finely dispersed pigment. The paste numbers correspond to the numbers of silica sols used as dispersants in Table 1 above.

Pigment paste
number Characteristic One Stable, constant viscosity (after 9 days) 2 Slightly more viscous earlier than pigment paste 1. After 1 day: very viscous, thixotropic, 3 It is more viscous earlier than pigment paste 2. No fluidity after about 1 hour. After 1 day: Solid 4 Slightly more viscous earlier than pigment paste 1. After 1 day: viscous, thyrotoxic 5 Initially gel (after 8 minutes dispersion) 6 Initially gel (after 1 minute dispersion) 7 The paste becomes solid after adding about 260-270 g of TiO ₂ . 8 Initially, the gel (after addition of TiO ₂ , before dispersion) 9 Early gel. The paste becomes the solid after the addition of TiO ₂ of about 220 g 10 Thixotropic behavior after 1 day, still fluid after 9 days through the separated phase; Water on top 11 Having a low viscosity initially at lower than pigment paste 1, but showing thixotropy after 3 hours 12 Of the paste in 350 g TiO _2. Gelling after 15 minutes. The paste solidifies as soon as it is added to the binder 13 Dispersed for 20 minutes at 2000 rpm. Stable and consistent viscosity (after 6 days)

Coating series

The paste is incorporated into a resin emulsion to form a coating composition for optical evaluation. The resin emulsion used is Setalux® 6774 supplied by Nuplex Resins. The coating compositions prepared comprise 5 wt%, 10 wt%, 20 wt%, 30 wt%, 40 wt% and 50 wt% titanium oxide pigment, respectively, in the dried coating composition. The film is cast using a film applicator with 100 micron openings. Each coating composition contains 50 g of a resin emulsion (equivalent to 22 g of dry resin).

Evaluation of Film

Optical measurements are made at wavelengths in the visible range (300-700 nm). The reflectance of the colored coating was measured with a Beckman Acta 5240 spectrophotometer equipped with an integrating sphere using barium sulphate as a reflectance reference. Coating compositions based on pigment pastes 1-4, 10, 11 and 13 were evaluated. Pigment pastes 5, 6, 8, 9 and 12 as described in Table 2 above are gelled immediately or after a short period of time, and the pigment paste 7 becomes a solid after addition of 260-270 g of TiO ₂ . In this specification, pigment paste 5, 6 or 8 does not include silanized colloidal silica particles, and the silanes for the silica weight ratios of 7 and 9 are 0.2 and 0.15, respectively. While the pigment paste 12 contains an excess of pigment, for example 350 g TiO ₂ in the paste.

Stability of pigment paste

The high degree of silane modification of colloidal silica improved paste stability compared to the low degree of modification; For example, in Table 2, pigment paste 1 (high), pigment paste 2 (low), pigment paste 3 (low) and pigment paste 4 (high) are compared. "Reference" Paste 10 using Dispex N40, a polyacrylate as dispersing agent, exhibited settling tendency and paste separation.

Coating composition

The coating composition was confirmed after 7.5 months. All samples were separated. The TiO ₂ pigment was deposited on the bottom of the sample. However, the coating series 1, 4 and 13 are easily redispersed and the coating series 3, 10 (see) and 11 have a solid "cake" that is harder at the bottom of the sample.

Pigment Light scattering  efficiency

Here we focused on light scattering as a conventional reflected light (λ: 300-700 nm wavelength range) integrated in a colloidal silica dispersion for a conventional polyacrylate dispersant, Dispex N40. Pigment efficiency can be greatly increased if 0.40% by weight of the colloidal silica dispersion is used instead of Dispex N40 as the pigment dispersant at the recommended dose by the supplier: in Table 3 below, Series 1 (including silica sol 1) and series 10 (including No. 10 Dispex N40 as described in Table 1). This results in the most significant effect in high pigment loading; For example, a 30% by weight titania content dispersed by colloidal silica provides the same reflectance as in about 40% by weight titania dispersed by Dispex N40 in the coating film.

Particle size

A particle size of 5 nm corresponding to a specific surface area of 500 m ² / g appears somewhat more effective than a particle size of 4 nm corresponding to a specific surface area of 750 m ² / g in terms of reflectivity Compare Series 1 and 4).

Colloidal  Of the silica dispersion Silane  Degree of modification

The degree of high silane modification of the colloidal silica is also beneficial especially in the visible light spectrum (wavelength 300-700 nm) in the 5 nm particle. The reason for this phenomenon depends on the improved stability to improved pigment wetting and agglomeration and the constant spacing of the titanium oxide pigment, although the difference in subsequent coating series is not significant (silica sol 1-4 is dispersed in the dispersions of series 1-4 respectively Mixed for manufacturing, and compared to coating series 1-4 in Table 5).

Claims (16)

A process for the preparation of an aqueous pigment dispersion, comprising up to 1% by weight of an organic binder,
Dispersing a water-soluble or water-dispersible silane compound and at least one colloidal silica particle having an average particle diameter of 2 to 100 nm dispersed in an aqueous solvent, Forming silanized colloidal silica particles wherein the at least one silane compound is mixed with the colloidal silica particles such that the weight ratio of silane to silica is from 0.25 to 0.4; And
Mixing said silylated colloidal silica particles with an organic pigment, an inorganic pigment or an organic and inorganic pigment to form an aqueous pigment dispersion having a weight ratio of silica to pigment of from 0.001 to 0.8,
Wherein up to 5 vol% of a water soluble or water dispersible organic solvent can be included in the dispersion to be prepared. The method according to claim 1,
Wherein the pigment has a particle size in the range of 10 nm to 5000 nm. 3. The method according to claim 1 or 2,
Wherein the pigment content in the dispersion is from 25% to 85% by weight. The method according to claim 1,
Pigments, characterized in that the TiO _2. The method according to claim 1,
Wherein the weight ratio of silica to pigment is in the range of 0.01 to 0.4. The method according to claim 1,
Wherein the aqueous dispersion comprises 20 vol% or less of a water soluble or water dispersible organic solvent. An aqueous pigment dispersion obtained by the process according to claim 1. An aqueous pigment dispersion comprising not more than 1% by weight of an organic binder,
Silanized colloidal silica particles having a weight ratio of silane to silica in the pigment dispersion of from 0.25 to 0.4 and having an average particle diameter of from 2 to 100 nm; And organic pigments, inorganic pigments, or organic and inorganic pigments having a weight ratio of silica to pigment of from 0.001 to 0.8,
Wherein up to 5 vol% of a water soluble or water dispersible organic solvent can be included in the dispersion. 9. The method according to claim 7 or 8,
Wherein the pigment has a particle size in the range of 10 nm to 5000 nm. 9. The method according to claim 7 or 8,
Wherein the weight ratio of silica to pigment is 0.01 to 0.4. 9. The method according to claim 7 or 8,
Wherein the silica content in the dispersion is from 1% to 80% by weight. 9. The method according to claim 7 or 8,
Wherein the pigment content in the dispersion is from 25% to 85% by weight. 9. The method according to claim 7 or 8,
Wherein the pigment is an inorganic pigment. 9. The method according to claim 7 or 8,
Lt; _{RTI ID = 0.0} > TiO2. ≪ / _RTI > A method for coating a dispersion according to claim 7 or 8 for coating. A process according to claim 7 or 8 for use in reducing bubble formation.