CN102701292A - Preparation method of cobalt carbonate material with compact structure and spheroid shape - Google Patents

Preparation method of cobalt carbonate material with compact structure and spheroid shape Download PDF

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CN102701292A
CN102701292A CN2012101730638A CN201210173063A CN102701292A CN 102701292 A CN102701292 A CN 102701292A CN 2012101730638 A CN2012101730638 A CN 2012101730638A CN 201210173063 A CN201210173063 A CN 201210173063A CN 102701292 A CN102701292 A CN 102701292A
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cobalt
solution
carbonate material
compact structure
value
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CN102701292B (en
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吉鸿安
朱来东
王同敏
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Northwest Research Institute of Mining and Metallurgy
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Abstract

The invention discloses a preparation method of a cobalt carbonate material with a compact structure and a spheroid shape, and aims to solve the problems of loose microstructure, disordered shape and poor uniformity of the cobalt carbonate material prepared by a conventional method. The preparation method comprises the following specific steps: placing a cobalt chloride solution with system temperature, pH value and cobalt concentration meeting the requirements into a reaction kettle, and keeping the cobalt chloride solution relatively constant; uniformly adding an ammonium bicarbonate solution into a cobalt solution system according to a certain flow, and taking a limited pH value as a reaction end point parameter of a control system; aging for a certain time, filtering, and repeatedly washing to obtain the required cobalt carbonate material. The cobalt carbonate material prepared by the method has the characteristics of spheroidal morphology, uniform particle size, compact structure and better particle size distribution, adopts standard conventional equipment, is easy to control process parameters, is simple to operate and is suitable for large-scale production.

Description

A kind of compact structure, globoid pattern cobaltous carbonate preparation methods
Technical field
The invention belongs to new forms of energy, field of new; Relate to the cobaltous carbonate preparation methods that microscopic appearance and physicals is had characteristic requirements, the cobaltous carbonate that this preparation method makes can be used for producing the precursor raw material of the powder blue product of battery material, wimet, electronic material etc.
Background technology
Flourish along with electronics, communications industry, various household electrical appliance, mobile phone, notebook computer are doubled and redoubled to the demand of lithium-ion secondary cell, and tricobalt tetroxide has also obtained quick progress as its production technology of important source material of lithium cell cobalt acid lithium material.Powder blue (particularly tricobalt tetroxide) product appearance is grey black or black powder; Be a kind of important transition metal oxide, usually as main raw material and the tinting material of ceramic industry and the catalyzer in the chemical industry of producing wimet, battery material, electronic material.In chemical industry, Co 3O 4It is a kind of efficient, persistent catalyzer.The working method of the used cobaltous carbonate precursor of powder blue is more at present; Routine joins carbonate solution and cobalt salt solution in the reaction vessel; The cobaltous carbonate that makes is invisible in a jumble because of its throw out particle aggregation bodily form looks, loose frangible powder blue that only can the production common grade when producing powder blue with precursor material, more is difficult to satisfy the needs that battery material etc. is produced required " globoid pattern densification high-quality carbonic acid cobalt precursor material ".
Summary of the invention
The purpose of this invention is to provide a kind of compact structure, globoid pattern cobaltous carbonate preparation methods, loose with the cobaltous carbonate material microstructure that solves the preparation of conventional working method, pattern mixed and disorderly, the problem of lack of homogeneity.
Technical scheme of the present invention is following:
A kind of compact structure, globoid pattern cobaltous carbonate preparation methods is characterized in that concrete steps are following:
Figure 2012101730638100002DEST_PATH_IMAGE001
will be through filtering, and cobalt concentration is that the cobalt chloride solution of 1~2 mol/L, pH value 4.75~5.20 is inserted in the reaction kettle;
Figure 440044DEST_PATH_IMAGE002
is under agitation condition; Heating steps
Figure 470317DEST_PATH_IMAGE001
solution; Make the solution system temperature be controlled at 55~65 ℃, and keep system temperature relatively stable;
Figure 2012101730638100002DEST_PATH_IMAGE003
the pre-filtered and the concentration of 1.8 ~ 2.5? mol / L ammonium bicarbonate solution was 250 ~ 800L / h flow rate of uniform spray to step
Figure 566449DEST_PATH_IMAGE002
of the system;
Solution system pH value 7.0~7.5 promptly stops the interpolation of ammonium bicarbonate soln as the system reaction end in
Figure 278053DEST_PATH_IMAGE004
controlled step
Figure 205557DEST_PATH_IMAGE003
;
is with 20~40 minutes after-filtration of step
Figure 344415DEST_PATH_IMAGE004
gained solid-liquid system ageing; Repetitive scrubbing promptly gets material requested.
The present invention adopts the conversion unit of standard normal just can produce " compact structure, globoid pattern cobaltous carbonate material ".This method as reaction system, is utilized the spontaneous adsorbent solution medium ionic effect in solution of throw out particle, the IT of adjustment system based on cobalt chloride solution the most common, the marketization; Simultaneously, in the chemical precipitation process, nascent particulate is easy to the selective adsorption ion identical with its composition from solution; Make the throw out particle surface charged, produce double electrical layers, help improving dispersion of particles property at solid-liquid interface; Be reduced to nuclear energy and build, form the particle aggregation electricity and build, help dispersion of particles; Prevented particle aggregation to a certain extent, also comprised dispersion process and agglomeration in the sedimentary in addition process of growth, when two phase mixing systems reach balance; System can change to making the total surface free energy be tending towards minimum direction; The result has the small-particle dissolving of high surfaces free energy and macrobead is able to growth, makes particle size distribution trend homogeneous, thus the pattern of control particle.Agglomeration accounts for consequence in the process of growth of particle.In the cobalt salt system, reunion is the main mode of particle growth.In the particle growth process, growth velocity reduces with the increase of particle radius, finally also can form the consistent particle aggregate of epigranular.After small-particle gathers on the macroparticle, can " fusing " among macroparticle, form a bigger integral particles through surface reaction, surface diffusion or volume diffusion; But also possibly only between particle, be in contact with one another place's local " fusing ", form a porous granule.If " fusing " reaction is enough fast; Promptly " fuse " pitch time of required time of reaction less than the adjacent secondary effective collision of particle; Then can form a bigger integral particles cluster of grains, otherwise then form the porous granule aggregate through assembling, thus the control particle size.
The advantage that the cobaltous carbonate material of the inventive method preparation has is:
Figure 927843DEST_PATH_IMAGE001
cobaltous carbonate material microscopic appearance be globoid, particle size evenly, compact structure and the preferable characteristic of size-grade distribution.
Figure 239875DEST_PATH_IMAGE002
adopts standard normal equipment; Processing parameter is easy to control; Simple to operate, be fit to large-scale production.
Description of drawings
Fig. 1 is the globoid pattern structure iron that the embodiment of the invention 1 makes material;
Fig. 2 is the particle size distribution figure that the embodiment of the invention 1 makes material;
Fig. 3 is the globoid pattern structure iron that the embodiment of the invention 2 makes material;
Fig. 4 is the particle size distribution figure that the embodiment of the invention 2 makes material;
Fig. 5 is the globoid pattern structure iron that the embodiment of the invention 3 makes material;
Fig. 6 is the particle size distribution figure that the embodiment of the invention 3 makes material;
Fig. 7 is the globoid pattern structure iron that the embodiment of the invention 4 makes material;
Fig. 8 is the particle size distribution figure that the embodiment of the invention 4 makes material.
Embodiment
Following embodiment can further specify structure and the physical index characteristic that present method prepares the cobaltous carbonate material, and institute gives an actual example and only is used to explain the present invention, is not to be used to limit scope of the present invention.
Embodiment 1
Figure 225149DEST_PATH_IMAGE001
will be through filtering, and the cobalt chloride solution of cobalt concentration 1.0 mol/L, pH value 4.75 is inserted in the reaction kettle;
Figure 534907DEST_PATH_IMAGE002
is under agitation condition; Heating steps
Figure 605632DEST_PATH_IMAGE001
solution; Make the solution system temperature be controlled at 55 ℃, and keep system temperature relatively stable;
Figure 222820DEST_PATH_IMAGE003
will be pre-filtered and the concentration of 1.8? mol / L of ammonium bicarbonate solution to 800L / h flow uniform spray to step
Figure 62600DEST_PATH_IMAGE002
of the system;
Solution system pH value 7.5 promptly stops the interpolation of ammonium bicarbonate soln as the system reaction end in
Figure 605577DEST_PATH_IMAGE004
controlled step
Figure 898018DEST_PATH_IMAGE003
;
Figure 755116DEST_PATH_IMAGE005
is with 20 minutes after-filtration of step
Figure 449402DEST_PATH_IMAGE004
gained solid-liquid system ageing; Repetitive scrubbing promptly gets material requested.
Embodiment 1 makes globoid pattern structure and size-grade distribution such as Fig. 1 and Fig. 2 of material, and physical index " granularity and density measurement result " is like table 1.
Embodiment 2
Figure 163280DEST_PATH_IMAGE001
will be through filtering, and the cobalt chloride solution of cobalt concentration 1.5 mol/L, pH value 4.80 is inserted in the reaction kettle;
is under agitation condition; Heating steps solution; Make the solution system temperature be controlled at 63 ℃, and keep system temperature relatively stable;
Figure 214916DEST_PATH_IMAGE003
will be pre-filtered and the concentration of 2.0? mol / L of ammonium bicarbonate solution to 588L / h flow uniform spray to step
Figure 302957DEST_PATH_IMAGE002
of the system;
Solution system pH value 7.2 promptly stops the interpolation of ammonium bicarbonate soln as the system reaction end in
Figure 569991DEST_PATH_IMAGE004
controlled step ;
is with 30 minutes after-filtration of step
Figure 991985DEST_PATH_IMAGE004
gained solid-liquid system ageing; Repetitive scrubbing promptly gets material requested.
Embodiment 2 makes globoid pattern structure and size-grade distribution such as Fig. 3 and Fig. 4 of material, and physical index " granularity and density measurement result " is like table 1.
Embodiment 3
will be through filtering, and the cobalt chloride solution of cobalt concentration 1.6 mol/L, pH value 5.09 is inserted in the reaction kettle;
Figure 483327DEST_PATH_IMAGE002
is under agitation condition; Heating steps
Figure 69029DEST_PATH_IMAGE001
solution; Make the solution system temperature be controlled at 60 ℃, and keep system temperature relatively stable;
Figure 498873DEST_PATH_IMAGE003
will be pre-filtration and concentration of 1.86? mol / L of ammonium bicarbonate solution to 280L / h flow uniform spray to step
Figure 474919DEST_PATH_IMAGE002
of the system;
Solution system pH value 7.2 promptly stops the interpolation of ammonium bicarbonate soln as the system reaction end in
Figure 15622DEST_PATH_IMAGE004
controlled step
Figure 659093DEST_PATH_IMAGE003
;
Figure 56576DEST_PATH_IMAGE005
is with 30 minutes after-filtration of step gained solid-liquid system ageing; Repetitive scrubbing promptly gets material requested.
Embodiment 3 makes globoid pattern structure and size-grade distribution such as Fig. 5 and Fig. 6 of material, and physical index " granularity and density measurement result " is like table 1.
Embodiment 4
Figure 864312DEST_PATH_IMAGE001
will be through filtering, and the cobalt chloride solution of cobalt concentration 2.0 mol/L, pH value 5.20 is inserted in the reaction kettle;
Figure 362290DEST_PATH_IMAGE002
is under agitation condition; Heating steps
Figure 930674DEST_PATH_IMAGE001
solution; Make the solution system temperature be controlled at 65 ℃, and keep system temperature relatively stable;
Figure 146892DEST_PATH_IMAGE003
will be pre-filtered and the concentration of 2.5? mol / L of ammonium bicarbonate solution to 250L / h flow uniform spray to step
Figure 29397DEST_PATH_IMAGE002
of the system;
Solution system pH value 7.0 promptly stops the interpolation of ammonium bicarbonate soln as the system reaction end in
Figure 381881DEST_PATH_IMAGE004
controlled step
Figure 888211DEST_PATH_IMAGE003
;
Figure 326146DEST_PATH_IMAGE005
is with 40 minutes after-filtration of step
Figure 746763DEST_PATH_IMAGE004
gained solid-liquid system ageing; Repetitive scrubbing promptly gets material requested.
Embodiment 4 makes globoid pattern structure and size-grade distribution such as Fig. 7 and Fig. 8 of material, and physical index " granularity and density measurement result " is like table 1.
Cobaltous carbonate granularity that table 1 embodiment makes and density measurement result

Claims (1)

1. a compact structure, globoid pattern cobaltous carbonate preparation methods is characterized in that concrete steps are following:
(1) will be through filtering, cobalt concentration is that the cobalt chloride solution of 1~2 mol/L, pH value 4.75~5.20 is inserted in the reaction kettle;
(2) under agitation condition, the solution in the heating steps (1) makes the solution system temperature be controlled at 55~65 ℃, and keeps system temperature relatively stable;
(3) will filter in advance and concentration is that the ammonium bicarbonate soln of 1.8~2.5 mol/L at the uniform velocity sprays to the system of step (2) with the flow of 250~800L/h;
(4) solution system pH value 7.0~7.5 promptly stops the interpolation of ammonium bicarbonate soln as the system reaction end in the controlled step (3);
(5) with 20~40 minutes after-filtration of step (4) gained solid-liquid system ageing, repetitive scrubbing promptly gets material requested.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102910686A (en) * 2011-08-04 2013-02-06 深圳市格林美高新技术股份有限公司 Cobalt carbonate preparation method and superfine cobalt powder preparation method
CN103351030A (en) * 2013-06-29 2013-10-16 西北矿冶研究院 Preparation method of low-anion residual basic cobalt carbonate
CN104944475A (en) * 2015-07-16 2015-09-30 南京寒锐钴业股份有限公司 Preparation method of cobalt carbonate with super coarse particles and high purity
CN106711449A (en) * 2017-01-06 2017-05-24 苏州宇量电池有限公司 Synthetic method of nanowire cobalt carbonate negative electrode material
CN114249355A (en) * 2021-12-20 2022-03-29 厦门厦钨新能源材料股份有限公司 Layered cobaltosic oxide material and preparation method and application thereof
CN115710022A (en) * 2022-11-17 2023-02-24 科立鑫(珠海)新能源有限公司 Preparation method of high-density cobalt carbonate

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CN101857278A (en) * 2010-06-25 2010-10-13 浙江华友钴业股份有限公司 Method for preparing spherical carbonate
CN101913659A (en) * 2010-08-10 2010-12-15 江苏东新能源科技有限公司 Battery-grade cobaltosic oxide preparation method

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CN101857278A (en) * 2010-06-25 2010-10-13 浙江华友钴业股份有限公司 Method for preparing spherical carbonate
CN101913659A (en) * 2010-08-10 2010-12-15 江苏东新能源科技有限公司 Battery-grade cobaltosic oxide preparation method

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102910686A (en) * 2011-08-04 2013-02-06 深圳市格林美高新技术股份有限公司 Cobalt carbonate preparation method and superfine cobalt powder preparation method
CN103351030A (en) * 2013-06-29 2013-10-16 西北矿冶研究院 Preparation method of low-anion residual basic cobalt carbonate
CN104944475A (en) * 2015-07-16 2015-09-30 南京寒锐钴业股份有限公司 Preparation method of cobalt carbonate with super coarse particles and high purity
CN106711449A (en) * 2017-01-06 2017-05-24 苏州宇量电池有限公司 Synthetic method of nanowire cobalt carbonate negative electrode material
CN106711449B (en) * 2017-01-06 2019-12-31 苏州宇量电池有限公司 Synthesis method of nano linear cobalt carbonate negative electrode material
CN114249355A (en) * 2021-12-20 2022-03-29 厦门厦钨新能源材料股份有限公司 Layered cobaltosic oxide material and preparation method and application thereof
CN114249355B (en) * 2021-12-20 2023-09-22 厦门厦钨新能源材料股份有限公司 Layered cobaltosic oxide material and preparation method and application thereof
CN115710022A (en) * 2022-11-17 2023-02-24 科立鑫(珠海)新能源有限公司 Preparation method of high-density cobalt carbonate

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