Chemistry of inorganic compounds – Carbon or compound thereof – Oxygen containing
Reexamination Certificate
1997-11-24
2004-03-02
Hendrickson, Stuart L. (Department: 1754)
Chemistry of inorganic compounds
Carbon or compound thereof
Oxygen containing
Reexamination Certificate
active
06699453
ABSTRACT:
The present invention relates to basic cobalt(II) carbonate, agglomerated from fine primary particles and of general composition Co[(OH)
2
]
a
[CO
3
]
1−a
, where 0.1≦a≦0.9, and to spheroidal cobalt(II) hydroxide, to a process for producing them and to their use.
Pure-phase cobalt(II) hydroxide is required for a series of industrial applications. For example, it can be used directly or after prior calcination to form cobalt(II) oxide as a component in the positive electrode of modern high-capacity secondary batteries based on nickel/cadmium or nickel/metal hydride.
It is uniformly distributed in the electrode material, via cobaltates(II) formed as intermediates which are soluble in the alkaline electrolyte of the battery (30% by weight KOH), and is deposited there by oxidation in what is termed the forming cycle as an electrically conductive CoOOH layer on the nickel hydroxide particles. Proportions of cobalt(II) which are present in the starting material do not form soluble cobaltates and therefore cannot be utilised.
The use of cobalt compounds in alkaline secondary batteries based on nickel/cadmium or nickel/metal hydride is disclosed in EP-A 353837. In addition, pure cobalt(II) oxides are used in electronics and catalyst technology.
Cobalt(II) hydroxide or carbonate is also used for the production of other cobalt compounds. Amongst others, these include the cobalt salts of weak acids, which are termed metal soaps. These are not only used as driers for lacquers and varnishes, but are also employed as catalysts, just like cobalt(II) oxide.
The catalytic use of cobalt(II) acetate in the production of adipic acid may be cited as an example.
Cobalt(II) hydroxide can be prepared from aqueous solutions of cobalt(II) salts by precipitation with alkaline liquors. The resulting precipitates generally have a gel-like consistency, are difficult to filter and are thus difficult to wash to render them neutral and free from salts. Moreover, they are very sensitive to oxidation in alkaline medium, so that the filtration and washing processes have to be carried out with the careful exclusion of atmospheric oxygen.
The cause of the poor filtration properties is based on the fine structure of the primary crystals and their irregular agglomeration. Fine primary particles are often desired for the applications described above, however. Firstly, fine primary particles dissolve more rapidly in acids, and secondly the calcination or reduction of cobalt(II) hydroxides such as these results in correspondingly fine primary particles of cobalt(II) oxide or cobalt metal powder.
A corresponding cobalt(II) hydroxide with a fine primary particle structure can only be produced at considerable cost by conventional processes, however, so that a large discrepancy exists between the required property profile and a technically stable, reproducible and economical method of production.
The poor filtration and washing behaviour described above does not occur with spheroidally agglomerated primary particles. For example, spherical nickel hydroxide, which is used in modern alkaline secondary batteries, exhibits excellent filtration and washing behaviour.
The production of spherical nickel hydroxide from aqueous solutions of nickel salts by precipitation with alkaline liquors in the presence of ammonia is disclosed in EP-A 353 837. In principle, this process could also be applied to the element cobalt. However, compared with nickel the process is made more difficult due to the generally known fact that cobalt(II) in its complexed state is readily oxidised to its trivalent state. It therefore has to be ensured that atmospheric oxygen is excluded even more rigorously than in the conventional precipitation. A general disadvantage of this process, which applies both to nickel and to cobalt, is the fact that the filtrates contain ammonia and complexed metal cations. A costly effluent treatment procedure cannot therefore be circumvented.
The object of the present invention was therefore to provide a cobalt(II) hydroxide which does not exhibit the prior art disadvantages described and which can be reproducibly produced by an economical process.
It has now been found that spheroidally agglomerated cobalt(II) carbonate having variably adjustable properties, such as average agglomerate diameter and specific surface for example, and which can subsequently be converted into other compounds, e.g. spheroidally agglomerated cobalt(II) hydroxide, in a series of chemical reactions whilst retaining its secondary morphology, can be produced by a technically simple and economical process.
This cobalt carbonate is a basic cobalt(II) carbonate which is agglomerated from fine primary particles, of general composition Co[(OH)
2
]
a
[CO
3
]
1−a
, where 0.1≦a≦0.9, wherein the agglomerates have a spheroidal habit and the average agglomerate diameter is 3 to 50 &mgr;m. The agglomerate diameter is preferably 5-20 &mgr;m. The basic cobalt(II) carbonate agglomerates according to the invention preferably have tap densities of ≧1.6 g/cm
3
and bulk densities of ≧1.2 g/cm
3
.
This invention also relates to a process for producing the cobalt(II) carbonate agglomerates according to the invention. This is characterised in that aqueous solutions of cobalt salts of general formula CoX
2
, where X represents Cl—, NO
3
— and/or ½ SO
4
2
—, are reacted with aqueous solutions or suspensions of alkali and/or ammonium carbonates and/or hydrogen carbonates at temperatures between 40 and 100° C., preferably 60 to 90° C., and the resulting basic cobalt(III) carbonate agglomerates are subsequently filtered off and washed until they are neutral and free from salts.
The process according to the invention is preferably carried out with alkali carbonates, both for environmental and economic reasons. However, it may also be carried out using ammonium carbonates in order to obtain products which are particularly low in alkali.
This process is preferably carried out continuously with intensive mixing of the reactants. Residence times in this mode of operation should preferably be between 0.5 hours and 10 hours, most preferably between 1 and 5 hours.
Depending on the process parameters, particularly temperature, concentration, pH, residence time and intensity of stirring, the chemical composition, the size of the primary particles, and the size and distribution of the secondary particles, can be adjusted within wide limits, as is further illustrated in Examples 1 to 4 and
FIGS. 1
to
4
.
The process according to the invention is characterised by simple process control. The basic cobalt(II) carbonates according to the invention are insensitive to oxidation by atmospheric oxygen, which permits them to be handled easily. Surprisingly, it has emerged that the basic cobalt(II) carbonate agglomerates according to the invention can be converted in highly concentrated suspension with alkaline liquors into pure-phase cobalt(II) hydroxides whilst retaining the spheroidal secondary morphology; this is described in more detail in Examples 5 and 6.
This can be effected in a technically simple batch process. In combination with good sedimentation, filtration and washing behaviour, the best possible screening from atmospheric oxygen can be achieved in this manner, and the process as a whole can also be carried out economically on an industrial scale without high costs.
This invention thus also relates to a process for producing agglomerated cobalt(II) hydroxide, wherein the basic cobalt(II) carbonate agglomerates according to the invention are reacted in suspension with aqueous alkaline liquors and/or ammonia. The cobalt(II) hydroxide agglomerates obtainable by the process according to the invention are characterised in that they consist of spheroidally agglomerated, polygonal, lamellar primary particles which have average diameter to thickness ratios between 3 and 15.
The spheroidal agglomerates have an average diameter of 3-50 &mgr;m, preferably 5 to 20 &mgr;m. Their tap densities are preferably ≧1 g/cm
Görge Astrid
Meese-Marktscheffel Juliane
Naumann Dirk
Olbrich Armin
Schrumpf Frank
Akorli Godfried R.
Eyl Diderico van
H.C. Starck GmbH & Co KG
Hendrickson Stuart L.
LandOfFree
Spheroidally agglomerated basic cobalt(II) carbonate and... does not yet have a rating. At this time, there are no reviews or comments for this patent.
If you have personal experience with Spheroidally agglomerated basic cobalt(II) carbonate and..., we encourage you to share that experience with our LandOfFree.com community. Your opinion is very important and Spheroidally agglomerated basic cobalt(II) carbonate and... will most certainly appreciate the feedback.
Profile ID: LFUS-PAI-O-3249860