METHOD FOR PREPARING PARTICLES OF TIN OXIDE

申请号 EP92919560.0 申请日 1992-09-16 公开(公告)号 EP0605500B1 公开(公告)日 1996-12-11
申请人 KODAK-PATHE; EASTMAN KODAK COMPANY; 发明人 ROBERT, Jean-Christophe Kokak-Pathé;
摘要 The invention relates to a method for preparing particles of metal oxide, as well as particles obtained by such method. The method consists in: precipitating a hydroxide, adding an inorganic compound such as a salt having a melting point lower than the oxide crystallization temperature, and heating the hydroxide and the salt at a high temperature. An oxide in the form of a fine powder is obtained, thus particularly allowing to perform thin conductive layers.
权利要求 Method for preparing particles of tin oxide, comprising the following steps :(a) precipitation of a hydroxide of tin oxide,(b) separation and drying of said hydroxide,(c) mixing this hydroxide with an inorganic compound having a melting point lower than the crystallization temperature of the metal oxide, and(d) heating the mixture resulting from step (c) at such temperature that the components of the mixture are in a molten state, whereby particles of tin oxide are formed and grown.The method of claim 1, wherein the precipitated hydroxide is tin hydroxide.The method of claim 1, wherein in step (a), at least a second hydroxide is co-precipitated.The method of claim 3, wherein the second precipitated hydroxide represents from 0.01 to 20 mole% based on tin hydroxide.The method of claim 3 or 4, wherein the co-precipitated hydroxide is antimony hydroxide.The method of claim 1, wherein the inorganic compound is selected in the class of halides and borates of alkali or earth alkali metals.The method of claim 6, wherein the inorganic compound is an alkali metal halide.The method of claim 1, wherein the thermal treatment is carried out at a temperature in the range of 400-1200°C.The method of claim 3, for preparing particles of a tin oxide, said method comprising the steps of :(a) coprecipitating tin hydroxide and antimony hydroxide(b) separating and drying the resulting precipitate, and(c) submitting the dried precipitate to a thermal treatment, similar to step (d) of Claim 1 wherein, prior to submitting the dried precipitate to the thermal treatment, it is mixed with a halide or borate of an alkali or earth alkali metal having a melting point lower than the crystallization temperature of the oxide.
说明书全文

The present invention relates to a method for obtaining particles of tin oxides ; the invention relates also to the resulting oxide particles as well as their use as antistatic agent, particularly for photographic films.

The metal oxide powders have various applications, particularly in the field of antistatic or conductive compositions.

A technique well known to prepare these oxides consists in precipitating a hydroxide from a salt, and then recovering this hydroxide and submitting it to a calcination treatment at a high temperature, higher than 500°C and even 1000°C. During this calcination treatment, various phenomena can occur which modify the texture or the crystalline morphology of the metal oxide particles, and produce a sintering, i.e., a clustering of these particles. As a result, materials in the form of particles exhibiting irregular sizes are obtained. With these particles, it is difficult to prepare dispersions and coating compositions in order to obtain thin conductive or antistatic layers. Moreover, the physical properties of such layers are not very reproducible. Therefore, a mechanical treatment such as grinding, is necessary to obtain finer particles and more homogeneous powders, in order to render these materials suitable for the applications considered. However, grinding causes crystalline defects to appear in the particles, which defects must be often resorbed by means of an additional thermal treatment.

In some cases, the oxide precipitation is a coprecipitation, because either a second metal hydroxide or an insoluble salt of another metal is coprecipitated with the hydroxide. An example is the initial step for preparing hexaferrites of alkaline-earth metals, where a ferric hydroxide and an alkaline-earth metal carbonate are co-precipitated. This precipitate is then thermally processed at about 1000°C in order to obtain the hexaferrite. In order to promote the reaction between hydroxide and carbonate, it is known to add a promoter which can be an alkali metal borate, PbO, Bi2O3, an alkali metal ferrite, a molybdate, an alkali metal chloride or sulfate. This method which consists in calcinating the hydroxide/carbonate mixture in presence of the promoter, in order to accelerate a chemical reaction, is disclosed in US Patent 3,793,443.

However, US Patent 3,810,973 indicates that using, as a flux, compounds such as B2O3, alkali metal borates or halides gives variable results and accordingly, proposes to form a sodium chloride and potassium chloride mixture in situ in order to promote the formation of a ferrite.

US Patent 4,401,643 discloses a method for preparing barium ferrites whereby a mixture of mixed barium and iron carbonate and of sodium salt is obtained by coprecipitation ; then, this mixture is heated at a temperature higher than 680°C, but lower than the sodium salt melting temperature and a finely divided ferrite powder is obtained, which is separated from the sodium salt.

EP 441,426 discloses the preparation of a fluorine doped tin oxide powder by combining a solution of the corresponding hydroxide and calcining the resulting precipitate by heating it to a temperature of at least 500°C. But using a promoter during the calcination step is neither mentioned nor suggested.

DE 1,273,507 describes a method for obtaining a gamma-aluminium oxide with a minor content of alpha-aluminium oxide. An inorganic compound is added to hinder the formation of alpha-aluminium oxide.

Moreover, the technical literature discloses the preparation of numerous metal oxides such as ZnO, SnO2, In2O3, MgO, TiO2, by precipitating and calcinating the corresponding hydroxide. In this literature, it is not mentioned or suggested to use a promoter or a flux during the calcination step.

From the foregoing, it can be stated that it is still a problem to obtain metal oxides in the form of fine, homogeneous particles exhibiting a determined morphology and appropriate conductive properties. The thermal treatment of oxides and the sintering it generates remain an obstacle in this regard.

The present invention is directed to an improved method for obtaining, in a simple and economical manner, a fine powder of tin oxide exhibiting electrically conductive properties.

The method consists in (a) preparing a hydroxide precursor of tin oxide, (b) separating and drying said hydroxide precursor, (c) mixing this precursor with an inorganic compound having a melting point lower than the crystallization temperature of said metal oxide and then (d) heating the mixture resulting from step (c) at such temperature that the components of the mixture are in a molten state, whereby particles of tin oxide are formed and grown.

The inorganic compound can be incorporated after or before drying the tin oxide precipitate. Inorganic compounds can be oxides such as boron oxide, or salts. Prefered compounds are salts of alkali or earth alkali metals, and more especially halides or borates of alkali or earth alkali metals such as halides of alkali metals. The amount of inorganic compound may depend widely on factors such as the nature of the hydroxide and the nature of the inorganic compound. The normally skilled man will determine in each case easily the appropriate amount to be used, but the inorganic compound to hydroxide weight ratio will be comprised generally between 0.5 and 20 and preferably between 1 and 10.

Using this inorganic compound allows to perform the thermal treatment in a more homogeneous medium, because the seed formation and the particle growth are performed in a molten state. It results in less clustering and, finer particles exhibiting a narrower size distribution. Taking this into account, the dimension and the size distribution of the metal hydroxide particles depend on the characteristics of the hydroxide precipitate and on the drying method chosen.

The method according to the invention can serve to prepare simple oxides, mixed oxides or doped oxides. In the case of doped oxides, doping can be performed with atoms of metals other than that of the oxide or with metalloid atoms, for example, halogen atoms. Common doping agents are disclosed in the literature and depend on the host oxide ; for example, tin oxide Sn2O can be doped with antimony, niobium or an halide. The amount of doping agent, varying according to the oxide nature, the doping agent nature and the applications considered, can range from 0,01 to 20 mole%.

The oxide particles are obtained from a hydroxide ; this hydroxide itself can be obtained by any of the techniques well-known in this respect, particularly by precipitation by means of alkali from salts in an aqueous, hydroalcoholic or alcoholic medium, or by alkoxide hydration or by decomposition of organometallic compounds. It is often desirable to remove the salt, at the end of the process ; this can be simply performed by washing with water in the case of salts such as alkali metal halides. The resistivity of the resulting oxide particles widely varies depending on the oxide nature, the possible doping but, considering applications using the conductive character of these particles, the resistivity is lower than 108 ohm.cm and preferably, 105 ohm.cm.

The thermal treatment conditions of step (d) are well-known and disclosed in the literature. These conditions must be controlled according to their influence on the size and the morphology of the particles. It can be desirable to perform, in some cases, the thermal treatment under an inert or reactive atmosphere, for example, under a reductive atmosphere. For the thermal treatment, the hydroxide can be sprayed in a colloidal form in an oven heated at a high temperature. It can also be carried out under a vapor state or by evaporation under vacuum. The temperature of the treatment varies according to the oxide, but generally, it is ranging from 400 to 1200°C.

Because of their fineness, the particles obtained by the method according to the invention are particularly adapted to the preparation of thin layers or coating compositions exhibiting antistatic properties, for example, from dispersions in appropriate binders or directly from powders.

EXAMPLE 1

40 g of tin chloride IV, SnCl4, 5H2O and 0,94 g of antimony trichloride are dissolved in 700 ml of ethanol. After dissolution, both alcoholic solutions are mixed and this mixture is slowly poured into 750 ml of water at 90°C in order to co-precipitate the IV tin and antimony hydroxides. This precipitate is allowed to ripen for 2 hours, then is filtered, washed and dried at 120°C.

A portion of this precipitate which is calcinated at 800°C during 3 hours, is picked up. A tin and antimony oxide powder is thus obtained. The characteristics of this powder are illustrated in the table below.

Another portion of the precipitate, mixed with KCl according to a KCl/precipitate weight ratio equal to 7.3, is picked up. This mixture is submitted to a 3 hour thermal treatment at 800°C. The characteristics of the resulting powder are illustrated in Table I below. The specific surfaces are measured by the well known BET absorption technique. The resistances are measured on oxide pellets compacted under a pressure of 500 kg/cm2.

TABLE I

Chemical treatment

Salt

Specific surface (m2/g)

Resistance ohm.cm

1-a

800°C-3h

-

17.2

< 10

1-b

800°C-3h

KCl

51.8

< 10

The increase in the specific surface shows the sintering reduction between the particles during the thermal treatment, and thus, a better dispersibility.

These dispersions can be applied as homogeneous thin layers exhibiting conductive and antistatic properties.

EXAMPLE 2

The procedure of example 1 is repeated, except that, after precipitation, the precipitate is separated and dried by spraying.

A portion of the precipitate is simply thermally treated, while another portion is mixed with KCl according to a KCl/precipitate weight ratio equal to 7.3, then thermally treated. Conditions of thermal treatment are those specified in Table II below.

TABLE II

Chemical treatment

Salt

Specific surface (m2/g)

Resistance ohm.cm

2-a

700°C-1h

-

26.9

20

2-b

700°C-1h

KCl

72.3

130

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