CN103232075B - Preparation method for cobalt oxyhydroxide - Google Patents

Preparation method for cobalt oxyhydroxide Download PDF

Info

Publication number
CN103232075B
CN103232075B CN201310124558.6A CN201310124558A CN103232075B CN 103232075 B CN103232075 B CN 103232075B CN 201310124558 A CN201310124558 A CN 201310124558A CN 103232075 B CN103232075 B CN 103232075B
Authority
CN
China
Prior art keywords
cobalt
sodium hydroxide
preparation
hydroxide solution
solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201310124558.6A
Other languages
Chinese (zh)
Other versions
CN103232075A (en
Inventor
訚硕
尹桂珍
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hunan Yacheng New Energy Co.,Ltd.
Original Assignee
HUNAN YA CHENG NEW MATERIALS DEVELOPMENT Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by HUNAN YA CHENG NEW MATERIALS DEVELOPMENT Co Ltd filed Critical HUNAN YA CHENG NEW MATERIALS DEVELOPMENT Co Ltd
Priority to CN201310124558.6A priority Critical patent/CN103232075B/en
Publication of CN103232075A publication Critical patent/CN103232075A/en
Application granted granted Critical
Publication of CN103232075B publication Critical patent/CN103232075B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

本发明提供了一种大颗粒球形羟基氧化钴的制备方法。具体方法为(1)配制0.5-2.0mol/L的钴盐溶液和5-10mol/L的氢氧化钠溶液,并在氢氧化钠溶液中添加络合剂和还原剂;(2)在氮气保护的条件下,向反应釜中同时泵入步骤(1)制得的钴盐溶液和氢氧化钠溶液,并通过调节氢氧化钠溶液的流量控制pH值10-12,连续反应,料浆粒度在15-20微米之间;(3)得出球形度、结晶度好的氢氧化亚钴,洗涤过滤,将含水量控制在10-30%之间,转入氧化釜中,鼓入空气,进行氧化;(4)将氧化后的料浆放入鼓风烘箱中,烘干,即得。The invention provides a preparation method of large particle spherical cobalt oxyhydroxide. The specific method is (1) prepare 0.5-2.0mol/L cobalt salt solution and 5-10mol/L sodium hydroxide solution, and add complexing agent and reducing agent to the sodium hydroxide solution; (2) under nitrogen protection Under certain conditions, pump the cobalt salt solution and sodium hydroxide solution prepared in step (1) into the reaction kettle at the same time, and control the pH value to 10-12 by adjusting the flow rate of the sodium hydroxide solution to continuously react. The slurry particle size is Between 15-20 microns; (3) Get cobaltous hydroxide with good sphericity and crystallinity, wash and filter, control the water content between 10-30%, transfer it to the oxidation kettle, blow in air, and carry out Oxidation; (4) Put the oxidized slurry into a blast oven and dry it to obtain.

Description

一种羟基氧化钴的制备方法A kind of preparation method of cobalt oxyhydroxide

技术领域technical field

本发明涉及一种无机材料的制备方法,具体地说,涉及一种羟基氧化钴的制备方法。The invention relates to a preparation method of an inorganic material, in particular to a preparation method of cobalt oxyhydroxide.

背景技术Background technique

八十年代以来,钴粉作为高能电池充放电的活化剂,大量地应用于充电电池领域。九十年代初,日、德等国科学家成功地将亚钴材料添加到电池原料中,使其成为电池行业研究与发展的高价值、高技术产品。钴粉和氧化亚钴粉等钴的化合物作为一种性能优良的电池材料添加剂,能够改善Ni(OH)2的质子电导,降低氧化电位,提高析氧电位,对提高电极性能有显著效果。在充电前期可以保证电极充分充电,使Ni(OH)2充分转化为NiOOH,同时遏制氧的析出,提高充电效率,增加电极比容量。近年来,随着锂离子电池的发展,钴氧化物作为制备锂离子电池电极材料的原料,也使其消费量不断增加。我国的钴酸锂生产近几年快速发展,因而对Co304的需求也相应迅猛增加。电池级Co304作为锂离子电池正极材料钴酸锂的主要原料,也随锂离子二次电池的需求量增加而增加。2002年全球钴的消耗总量为8800万磅,钻应用在电池行业中的份额迅速上升达到32%。而随着小型分立的可移动电源需求的进一步增长,像移动通信的迅猛发展和笔记本电脑普及率的快速增长,为锂离子电池工业的发展创造了更好的机遇,对应地,对锂离子电池正极材料LiCo02的需求也大幅增长。预计到2015年钴的应用将达到2.3亿磅,其中56%将应用在锂电池行业。Since the 1980s, cobalt powder has been widely used in the field of rechargeable batteries as an activator for charging and discharging high-energy batteries. In the early 1990s, scientists from Japan, Germany and other countries successfully added sub-cobalt materials to battery raw materials, making it a high-value, high-tech product for the research and development of the battery industry. As a battery material additive with excellent performance, cobalt compounds such as cobalt powder and cobalt oxide powder can improve the proton conductance of Ni(OH) 2 , reduce the oxidation potential, and increase the oxygen evolution potential, which has a significant effect on improving electrode performance. In the early stage of charging, it can ensure that the electrode is fully charged, so that Ni(OH) 2 can be fully converted into NiOOH, and at the same time, the precipitation of oxygen can be suppressed, the charging efficiency can be improved, and the specific capacity of the electrode can be increased. In recent years, with the development of lithium-ion batteries, cobalt oxide is used as a raw material for the preparation of lithium-ion battery electrode materials, and its consumption is also increasing. China's lithium cobalt oxide production has developed rapidly in recent years, so the demand for Co 3 0 4 has also increased rapidly. Battery-grade Co 3 0 4 is the main raw material of lithium cobalt oxide, the cathode material of lithium-ion batteries, and it also increases with the demand for lithium-ion secondary batteries. Global cobalt consumption totaled 88 million pounds in 2002, and the share of cobalt applications in the battery industry has risen rapidly to 32%. With the further increase in the demand for small discrete mobile power sources, such as the rapid development of mobile communications and the rapid growth of the penetration rate of notebook computers, better opportunities have been created for the development of the lithium-ion battery industry. Correspondingly, for lithium-ion batteries The demand for cathode material LiCo0 2 has also increased significantly. It is estimated that the application of cobalt will reach 230 million pounds by 2015, 56% of which will be used in the lithium battery industry.

随着便携式电子产品不断发展,对其所使用的电池也不断提出了新的要求。特别是不断涌现的智能手机和平板电脑对电池续航能力要求更高,尤其是平板电脑,大多数都采用内嵌电池设计结构,不可拆卸,电池续航能力已成为其发展软肋。钴酸锂所谓一种高能量密度正极材料,是当前智能手机和平板电脑电池的主要正极材料。With the continuous development of portable electronic products, new requirements are constantly put forward for the batteries used in them. In particular, the ever-emerging smartphones and tablet PCs have higher requirements for battery life, especially tablet PCs, most of which use an embedded battery design structure, which cannot be disassembled. Battery life has become a weakness in its development. Lithium cobalt oxide is a so-called high-energy-density cathode material, which is the main cathode material for current smartphone and tablet batteries.

羟基氧化钴作为钴酸锂生产的基本原料之一,既适合于制备各种钴的化合物,还适合于制备高活性的锂离子电池正极材料钴酸锂,同事,羟基氧化钴也可作为电池的添加剂,在充电的过程中,形成到点网络,改善电池的充放电性能和循环寿命,因此,羟基氧化钴具有较高的发展前景。As one of the basic raw materials for the production of lithium cobalt oxide, cobalt oxyhydroxide is not only suitable for the preparation of various cobalt compounds, but also suitable for the preparation of lithium cobalt oxide, a positive electrode material for lithium-ion batteries with high activity. At the same time, cobalt oxyhydroxide can also be used as a Additives form a point-to-point network during the charging process to improve the charge-discharge performance and cycle life of the battery. Therefore, cobalt oxyhydroxide has a high development prospect.

专利申请201210016504.3公开了一种羟基氧化钴的的制备方法,此方法是在反应过程中通过添加氧化剂的方法直接合成羟基氧化钴。专利申请201110327857.0公开了一种湿法化学反应制取羟基三价氧化钴生产钴酸锂的方法,此方法是先合成氢氧化亚钴,然后再通过次氯酸钠将氢氧化亚钴氧化成羟基三价氧化钴,最后再通过烧结制成钴酸锂。专利申请201010117854.X公开了一种制备三羟基氢氧化钴的方法,此方法是通过水热方法合成三羟基氢氧化钴。但上述公开的方法生产的羟基氧化钴的形貌不是类球形,会造成下游产业混料的不均匀,降低了混料的效率和效果,且产品稳定性较差,在合成过程中添加氧化剂会造成反应的不均匀,难以具备大批量生产化。Patent application 201210016504.3 discloses a preparation method of cobalt oxyhydroxide, which is to directly synthesize cobalt oxyhydroxide by adding an oxidizing agent during the reaction process. Patent application 201110327857.0 discloses a method for producing lithium cobaltate by wet chemical reaction to produce cobaltous hydroxide trivalent oxide. This method first synthesizes cobaltous hydroxide, and then oxidizes cobaltous hydroxide to hydroxyl trivalent oxidation by sodium hypochlorite. Cobalt, and finally sintered to make lithium cobaltate. Patent application 201010117854.X discloses a method for preparing cobalt trihydroxide, which is to synthesize cobalt trihydroxide by hydrothermal method. However, the morphology of the cobalt oxyhydroxide produced by the above-mentioned disclosed method is not spherical, which will cause uneven mixing in downstream industries, reduce the efficiency and effect of mixing, and the product stability is relatively poor. Adding an oxidizing agent during the synthesis process will cause The unevenness of the reaction is caused, making it difficult to mass-produce.

发明内容Contents of the invention

针对现有技术中存在的缺陷,本发明的目的是提供一种大颗粒球形羟基氧化钴的制备方法,为大批量生产钴酸锂提供稳定性强的原料,增加混料的效果和效率。In view of the defects existing in the prior art, the object of the present invention is to provide a method for preparing large-particle spherical cobalt oxyhydroxide, which provides a highly stable raw material for mass production of lithium cobaltate, and increases the effect and efficiency of mixing materials.

为了实现本发明的目的,本发明提供一种羟基氧化钴的制备方法,具体步骤如下:In order to realize the purpose of the present invention, the present invention provides a kind of preparation method of cobalt oxyhydroxide, concrete steps are as follows:

(1)配制0.5-2.0mol/L的钴盐溶液和5-10mol/L的氢氧化钠溶液,并在氢氧化钠溶液中添加络合剂和还原剂;(1) Prepare 0.5-2.0mol/L cobalt salt solution and 5-10mol/L sodium hydroxide solution, and add complexing agent and reducing agent to the sodium hydroxide solution;

(2)在pH值10-12、温度40-70℃、转速300-400转/分钟并在氮气保护的条件下,向反应釜中同时泵入步骤(1)制得的钴盐溶液和氢氧化钠溶液,并通过调节氢氧化钠溶液的流量控制pH值10-12,连续反应,得到料浆;(2) Under the conditions of pH 10-12, temperature 40-70°C, rotation speed 300-400 rpm and nitrogen protection, simultaneously pump the cobalt salt solution and hydrogen prepared in step (1) into the reactor Sodium oxide solution, and by adjusting the flow of sodium hydroxide solution to control the pH value of 10-12, continuous reaction, to obtain slurry;

(3)得出球形度、结晶度好的氢氧化亚钴,洗涤过滤,将含水量控制在10-30%之间,转入氧化釜中,鼓入空气,进行氧化;(3) Get the cobaltous hydroxide with good sphericity and crystallinity, wash and filter, control the water content between 10-30%, transfer it to the oxidation kettle, blow in air, and oxidize;

(4)将氧化后的料浆放入鼓风烘箱中,烘干,即得。(4) Put the oxidized slurry into a blast oven and dry it.

具体地,所述步骤(1)中的钴盐溶液为CoSO4、CoCl2或Co3(NO3)2的一种或两种以上。Specifically, the cobalt salt solution in the step (1) is one or more of CoSO 4 , CoCl 2 or Co 3 (NO 3 ) 2 .

作为优选,所述步骤(1)中添加络合剂为每升氢氧化钠溶液中添加0.5-1.5L氨含量25%氨水,或50-100克乙二胺四乙酸二钠。Preferably, the complexing agent added in the step (1) is 0.5-1.5L ammonia water with 25% ammonia content per liter of sodium hydroxide solution, or 50-100 grams of disodium edetate.

作为优选,所述步骤(1)中的添加还原剂为每升氢氧化钠溶液中添加20-50毫升含量80%的水合肼溶液。Preferably, the reducing agent added in the step (1) is 20-50 ml of 80% hydrazine hydrate solution per liter of sodium hydroxide solution.

作为优选,所述步骤(2)连续反应后,得到料浆粒度控制在15-20微米之间。Preferably, after the continuous reaction in the step (2), the particle size of the obtained slurry is controlled between 15-20 microns.

作为优选,所述步骤(3)中转入氧化釜中,在100-200℃温度下鼓入空气,进行氧化。As a preference, in the step (3), it is transferred into an oxidation kettle, and air is blown in at a temperature of 100-200° C. for oxidation.

作为优选,所述氧化的时间为3-6小时。Preferably, the oxidation time is 3-6 hours.

作为优选,所述步骤(4)将氧化后的料浆放入鼓风烘箱中,在120℃情况下进行烘干,即得。As a preference, in the step (4), put the oxidized slurry into a blast oven and dry it at 120°C to obtain the finished product.

本发明还提供了上述制备方法生产得到的羟基氧化钴颗粒。The present invention also provides the cobalt oxyhydroxide particles produced by the above preparation method.

本发明还提供了上述制备方法在生产羟基氧化钴中的应用。The present invention also provides the application of the above preparation method in the production of cobalt oxyhydroxide.

本发明提供的一种大颗粒球形羟基氧化钴的制备方法,生产得到的羟基氧化钴为类球形,可使下游产业混料均匀,产品稳定性强,可为大批量生产钴酸锂提供稳定性强的原料,增加混料的效果和效率。The preparation method of a large-particle spherical cobalt oxyhydroxide provided by the invention, the cobalt oxyhydroxide produced is spherical, which can make the downstream industry mix evenly, and the product has strong stability, which can provide stability for mass production of lithium cobaltate Strong raw materials, increase the effect and efficiency of mixing.

附图说明Description of drawings

图1为本发明一种羟基氧化钴的制备方法制得的羟基氧化钴的XRD图;Fig. 1 is the XRD figure of the cobalt oxyhydroxide that a kind of preparation method of cobalt oxyhydroxide of the present invention makes;

图2为本发明一种羟基氧化钴的制备方法制得的羟基氧化钴的SEM图;Fig. 2 is the SEM picture of the cobalt oxyhydroxide that a kind of preparation method of cobalt oxyhydroxide of the present invention makes;

图3为根据专利申请201210016504.3公开的羟基氧化钴的制备方法制得的羟基氧化钴的SEM图。Fig. 3 is an SEM image of cobalt oxyhydroxide prepared according to the method for preparing cobalt oxyhydroxide disclosed in patent application 201210016504.3.

具体实施方式detailed description

以下实施例用于说明本发明,但不用来限制本发明的范围。The following examples are used to illustrate the present invention, but are not intended to limit the scope of the present invention.

实施例1Example 1

1、钴液配置:称量1.5千克氯化钴晶体,并加入去离子水进行溶解,定容至5升,为配置足够的钴液,以上步骤可重复操作;1. Cobalt liquid configuration: Weigh 1.5 kg of cobalt chloride crystals, add deionized water to dissolve, and set the volume to 5 liters. In order to configure enough cobalt liquid, the above steps can be repeated;

2、碱液配置:称量1千克氢氧化钠晶体,加入去离子水进行溶解,定容至3升,然后再添加0.7L氨含量25%氨水和20毫升含量80%的水合肼溶液,最后定容至5L,为配置足够的碱液,以上步骤可重复操作;2. Alkaline preparation: Weigh 1 kg of sodium hydroxide crystals, add deionized water to dissolve, set the volume to 3 liters, then add 0.7 L of ammonia water with 25% ammonia content and 20 ml of hydrazine hydrate solution with 80% content, and finally Set the volume to 5L, in order to configure enough lye, the above steps can be repeated;

3、清洗反应釜,在PH值11.1、温度65℃、转速(300-转/分钟)并保持氮气的保护条件下,同时泵入步骤1的钴液和步骤2的碱液,并通过调节氢氧化钠流量稳定控制PH值在11.1,连续反应,经过12小时进料后,检测料浆粒度在15-20微米之间,此时为合格产品;3. Clean the reaction kettle, and pump the cobalt solution in step 1 and the lye solution in step 2 at the same time under the conditions of pH 11.1, temperature 65°C, rotation speed (300-rpm) and nitrogen protection, and adjust the hydrogen The flow rate of sodium oxide is stable and the pH value is controlled at 11.1, and the reaction is continuous. After 12 hours of feeding, the particle size of the slurry is detected to be between 15-20 microns, which is a qualified product at this time;

4、将粒度达到15-20微米的料浆取出,经过离心分离、水洗3次后,得到含水量12%的粉红色物料,再转入氧化釜中,开启搅拌进行升温,温度控制在150℃,鼓入空气,经过4小时氧化后,得到黑色的羟基氧化钴物料。4. Take out the slurry with a particle size of 15-20 microns. After centrifugation and washing for 3 times, a pink material with a water content of 12% is obtained, and then transferred to the oxidation kettle, and the stirring is started to raise the temperature. The temperature is controlled at 150°C , air was blown in, and after 4 hours of oxidation, a black cobalt oxyhydroxide material was obtained.

5、将黑色物料装盘放入鼓风烘箱中,经过120℃烘干后,得到黑色粉末状产物,即为产品羟基氧化钴。得到的羟基氧化钴XRD图如图1所示,SEM图与图2类似。5. Put the black material into a tray and put it into a blast oven, and after drying at 120°C, a black powdery product is obtained, which is the product cobalt oxyhydroxide. The XRD pattern of the obtained cobalt oxyhydroxide is shown in Figure 1, and the SEM pattern is similar to that in Figure 2.

实施例2.Example 2.

1、钴液配置:称量2.2千克氯化钴晶体,并加入去离子水进行溶解,定容至5升,为配置足够的钴液,以上步骤可重复操作;1. Cobalt liquid configuration: Weigh 2.2 kg of cobalt chloride crystals, add deionized water to dissolve, and set the volume to 5 liters. In order to configure enough cobalt liquid, the above steps can be repeated;

2、碱液配置:称量1千克氢氧化钠晶体,加入去离子水进行溶解,定容至3升,然后再添加0.9L氨含量25%氨水和20毫升含量80%的水合肼溶液,最后定容至5L,为配置足够的碱液,以上步骤可重复操作;2. Alkaline preparation: Weigh 1 kg of sodium hydroxide crystals, add deionized water to dissolve, and set the volume to 3 liters, then add 0.9L ammonia water with 25% ammonia content and 20 ml hydrazine hydrate solution with 80% content, and finally Set the volume to 5L, in order to configure enough lye, the above steps can be repeated;

3、清洗反应釜,在PH值10.9、温度50℃、转速(350-转/分钟)并保持氮气的保护条件下,同时泵入步骤1的钴液和步骤2的碱液,并通过调节氢氧化钠流量稳定控制PH值在10.9,连续反应,经过12小时进料后,检测料浆粒度在15-20微米之间,此时为合格产品;3. Clean the reaction kettle, and pump the cobalt liquid in step 1 and the lye in step 2 at the same time under the protection conditions of pH value 10.9, temperature 50°C, rotation speed (350-rpm) and nitrogen gas, and adjust the hydrogen The flow rate of sodium oxide is stable and the pH value is controlled at 10.9, and the reaction is continuous. After 12 hours of feeding, the particle size of the slurry is detected to be between 15-20 microns, which is a qualified product at this time;

4、将粒度达到15-20微米的料浆取出,经过离心分离、水洗3次后,得到含水量12%的粉红色物料,再转入氧化釜中,开启搅拌进行升温,温度控制在100℃,鼓入空气,经过3小时氧化后,得到黑色的羟基氧化钴物料。4. Take out the slurry with a particle size of 15-20 microns, centrifuge and wash 3 times to obtain a pink material with a water content of 12%, then transfer it to the oxidation kettle, start stirring to heat up, and control the temperature at 100°C , air was blown in, and after 3 hours of oxidation, a black cobalt oxyhydroxide material was obtained.

5、将黑色物料装盘放入鼓风烘箱中,经过120℃烘干后,得到黑色粉末状产物,即为产品羟基氧化钴。得到的羟基氧化钴XRD图与图1类似,SEM图如图2。5. Put the black material into a tray and put it into a blast oven, and after drying at 120°C, a black powdery product is obtained, which is the product cobalt oxyhydroxide. The XRD pattern of the obtained cobalt oxyhydroxide is similar to that shown in Figure 1, and the SEM pattern is shown in Figure 2.

实施例3Example 3

1、钴液配置:称量1.9千克硫酸钴晶体,并加入去离子水进行溶解,定容至5升,为配置足够的钴液,以上步骤可重复操作;1. Cobalt liquid configuration: Weigh 1.9 kg of cobalt sulfate crystals, add deionized water to dissolve, and set the volume to 5 liters. In order to configure enough cobalt liquid, the above steps can be repeated;

2、碱液配置:称量1千克氢氧化钠晶体,加入去离子水进行溶解,定容至3升,然后再添加0.9L氨含量25%氨水和20毫升含量80%的水合肼溶液,最后定容至5L,为配置足够的碱液,以上步骤可重复操作;2. Alkaline preparation: Weigh 1 kg of sodium hydroxide crystals, add deionized water to dissolve, and set the volume to 3 liters, then add 0.9L ammonia water with 25% ammonia content and 20 ml hydrazine hydrate solution with 80% content, and finally Set the volume to 5L, in order to configure enough lye, the above steps can be repeated;

3、清洗反应釜,在PH值11.5、温度40℃、转速(400-转/分钟)并保持氮气的保护条件下,同时泵入步骤1的钴液和步骤2的碱液,并通过调节氢氧化钠流量稳定控制PH值在11.5,连续反应,经过12小时进料后,检测料浆粒度在15-20微米之间,此时为合格产品;3. Clean the reaction kettle, and pump the cobalt solution in step 1 and the lye solution in step 2 at the same time under the conditions of pH 11.5, temperature 40°C, rotation speed (400-rpm) and nitrogen protection, and adjust the hydrogen The flow rate of sodium oxide is stable and the pH value is controlled at 11.5, and the reaction is continuous. After 12 hours of feeding, the particle size of the slurry is detected to be between 15-20 microns, which is a qualified product at this time;

4、将粒度达到15-20微米的料浆取出,经过离心分离、水洗3次后,得到含水量12%的粉红色物料,再转入氧化釜中,开启搅拌进行升温,温度控制在120℃,鼓入空气,经过5小时氧化后,得到黑色的羟基氧化钴物料。4. Take out the slurry with a particle size of 15-20 microns. After centrifugation and washing for 3 times, a pink material with a water content of 12% is obtained, and then transferred to the oxidation kettle, and the stirring is started to raise the temperature. The temperature is controlled at 120°C , air was blown in, and after 5 hours of oxidation, a black cobalt oxyhydroxide material was obtained.

5、将黑色物料装盘放入鼓风烘箱中,经过120℃烘干后,得到黑色粉末状产物,即为产品羟基氧化钴。得到的羟基氧化钴XRD图与图1类似,SEM图与图2类似。5. Put the black material into a tray and put it into a blast oven, and after drying at 120°C, a black powdery product is obtained, which is the product cobalt oxyhydroxide. The XRD pattern of the obtained cobalt oxyhydroxide is similar to that of Figure 1, and the SEM pattern is similar to that of Figure 2.

实施例4Example 4

1、钴液配置:称量2.5千克氯化钴晶体,并加入去离子水进行溶解,定容至5升,为配置足够的钴液,以上步骤可重复操作;1. Cobalt liquid configuration: Weigh 2.5 kg of cobalt chloride crystals, add deionized water to dissolve, and set the volume to 5 liters. In order to configure enough cobalt liquid, the above steps can be repeated;

2、碱液配置:称量2千克氢氧化钠晶体,加入去离子水进行溶解,定容至3升,然后再添加1.2L氨含量25%氨水和40毫升含量80%的水合肼溶液,最后定容至5L,为配置足够的碱液,以上步骤可重复操作;2. Alkaline preparation: Weigh 2 kg of sodium hydroxide crystals, add deionized water to dissolve, and set the volume to 3 liters, then add 1.2 L of ammonia water with 25% ammonia content and 40 ml of hydrazine hydrate solution with 80% content, and finally Set the volume to 5L, in order to configure enough lye, the above steps can be repeated;

3、清洗反应釜,在PH值12、温度70℃、转速(380-转/分钟)并保持氮气的保护条件下,同时泵入步骤1的钴液和步骤2的碱液,并通过调节氢氧化钠流量稳定控制PH值在12,连续反应,经过12小时进料后,检测料浆粒度在15-20微米之间,此时为合格产品;3. Clean the reaction kettle, and pump the cobalt solution in step 1 and the alkali solution in step 2 at the same time under the protection conditions of pH value 12, temperature 70°C, rotation speed (380-rpm) and nitrogen gas, and adjust the hydrogen The flow rate of sodium oxide is stable and the pH value is controlled at 12, and the reaction is continuous. After 12 hours of feeding, the particle size of the slurry is detected to be between 15-20 microns, which is a qualified product at this time;

4、将粒度达到15-20微米的料浆取出,经过离心分离、水洗3次后,得到含水量12%的粉红色物料,再转入氧化釜中,开启搅拌进行升温,温度控制在180℃,鼓入空气,经过5小时氧化后,得到黑色的羟基氧化钴物料。4. Take out the slurry with a particle size of 15-20 microns, centrifuge and wash 3 times to obtain a pink material with a water content of 12%, then transfer it to the oxidation kettle, start stirring to heat up, and control the temperature at 180°C , air was blown in, and after 5 hours of oxidation, a black cobalt oxyhydroxide material was obtained.

5、将黑色物料装盘放入鼓风烘箱中,经过120℃烘干后,得到黑色粉末状产物,即为产品羟基氧化钴。得到的羟基氧化钴XRD图与图1类似,SEM图与图2类似。5. Put the black material into a tray and put it into a blast oven, and after drying at 120°C, a black powdery product is obtained, which is the product cobalt oxyhydroxide. The XRD pattern of the obtained cobalt oxyhydroxide is similar to that of Figure 1, and the SEM pattern is similar to that of Figure 2.

实施例5Example 5

1、钴液配置:称量2.2千克硝酸钴晶体,并加入去离子水进行溶解,定容至5升,为配置足够的钴液,以上步骤可重复操作;1. Cobalt liquid configuration: Weigh 2.2 kg of cobalt nitrate crystals, add deionized water to dissolve, and set the volume to 5 liters. In order to configure enough cobalt liquid, the above steps can be repeated;

2、碱液配置:称量2千克氢氧化钠晶体,加入去离子水进行溶解,定容至3升,然后再添加60克乙二胺四乙酸二钠和40毫升含量80%的水合肼溶液,最后定容至5L,为配置足够的碱液,以上步骤可重复操作;2. Alkaline preparation: Weigh 2 kg of sodium hydroxide crystals, add deionized water to dissolve, and set the volume to 3 liters, then add 60 g of disodium edetate and 40 ml of 80% hydrazine hydrate solution , and finally set the volume to 5L. In order to configure enough lye, the above steps can be repeated;

3、清洗反应釜,在PH值10、温度45℃、转速(340-转/分钟)并保持氮气的保护条件下,同时泵入步骤1的钴液和步骤2的碱液,并通过调节氢氧化钠流量稳定控制PH值在10,连续反应,经过12小时进料后,检测料浆粒度在15-20微米之间,此时为合格产品;3. Clean the reaction kettle, and pump the cobalt solution in step 1 and the alkali solution in step 2 at the same time under the protection conditions of pH value 10, temperature 45°C, rotation speed (340-rpm) and nitrogen gas, and adjust the hydrogen The flow of sodium oxide is stabilized and the pH value is controlled at 10, and the reaction is continuous. After 12 hours of feeding, the particle size of the slurry is detected to be between 15-20 microns, which is a qualified product at this time;

4、将粒度达到15-20微米的料浆取出,经过离心分离、水洗3次后,得到含水量12%的粉红色物料,再转入氧化釜中,开启搅拌进行升温,温度控制在200℃,鼓入空气,经过6小时氧化后,得到黑色的羟基氧化钴物料。4. Take out the slurry with a particle size of 15-20 microns, centrifuge and wash 3 times to obtain a pink material with a water content of 12%, then transfer it to the oxidation kettle, start stirring to heat up, and control the temperature at 200°C , air was blown in, and after 6 hours of oxidation, a black cobalt oxyhydroxide material was obtained.

5、将黑色物料装盘放入鼓风烘箱中,经过120℃烘干后,得到黑色粉末状产物,即为产品羟基氧化钴。得到的羟基氧化钴XRD图与图1类似,SEM图与图2类似。5. Put the black material into a tray and put it into a blast oven, and after drying at 120°C, a black powdery product is obtained, which is the product cobalt oxyhydroxide. The XRD pattern of the obtained cobalt oxyhydroxide is similar to that of Figure 1, and the SEM pattern is similar to that of Figure 2.

实施例6Example 6

根据专利申请201210016504.3公开的羟基氧化钴的制备方法,得到产品羟基氧化钴。得到羟基氧化钴SEM图如图3所示。According to the preparation method of cobalt oxyhydroxide disclosed in patent application 201210016504.3, the product cobalt oxyhydroxide was obtained. The obtained cobalt oxyhydroxide SEM image is shown in Figure 3.

通过比较图2和图3,可以明显看到,本发明得到的产品均匀度更好,且在形状上比对比文件得到的产品更接近类球形,对下游产业混料均匀性和产品的稳定性,有着更好的效果,可为大批量生产钴酸锂提供稳定性强的原料,增加混料的效果和效率。By comparing Fig. 2 and Fig. 3, it can be clearly seen that the uniformity of the product obtained by the present invention is better, and the product obtained by the comparison file is closer to a spherical shape in shape, which is beneficial to the mixing uniformity of the downstream industry and the stability of the product , has a better effect, can provide a stable raw material for mass production of lithium cobalt oxide, and increase the effect and efficiency of mixing materials.

虽然,上文中已经用一般性说明及具体实施方案对本发明作了详尽的描述,但在本发明基础上,可以对之作一些修改或改进,这对本领域技术人员而言是显而易见的。因此,在不偏离本发明精神的基础上所做的这些修改或改进,均属于本发明要求保护的范围。Although the present invention has been described in detail with general descriptions and specific embodiments above, it is obvious to those skilled in the art that some modifications or improvements can be made on the basis of the present invention. Therefore, the modifications or improvements made on the basis of not departing from the spirit of the present invention all belong to the protection scope of the present invention.

Claims (3)

1.一种羟基氧化钴的制备方法,其特征在于,具体步骤如下:1. a preparation method of cobalt oxyhydroxide, is characterized in that, concrete steps are as follows: (1)配制钴离子浓度为0.5-2.0mol/L的钴盐溶液和5-10mol/L的氢氧化钠溶液,并在氢氧化钠溶液中添加络合剂和还原剂;(1) preparation of cobalt ion concentration is the cobalt salt solution of 0.5-2.0mol/L and the sodium hydroxide solution of 5-10mol/L, and adds complexing agent and reducing agent in sodium hydroxide solution; (2)在pH值10-12、温度40-70℃、转速300-400转/分钟并在氮气保护的条件下,向反应釜中同时泵入步骤(1)制得的钴盐溶液和氢氧化钠溶液,并通过调节氢氧化钠溶液的流量控制pH值10-12,连续反应,得到粒度控制在15-20微米之间的料浆;(2) At a pH value of 10-12, a temperature of 40-70°C, a rotating speed of 300-400 rpm and under the condition of nitrogen protection, simultaneously pump the cobalt salt solution and hydrogen prepared in step (1) into the reaction kettle Sodium oxide solution, and by adjusting the flow of sodium hydroxide solution to control the pH value of 10-12, continuous reaction, to obtain a slurry whose particle size is controlled between 15-20 microns; (3)得出球形度、结晶度好的氢氧化亚钴,洗涤过滤,将含水量控制在10-30%之间,转入氧化釜中,在100-200℃温度下鼓入空气,进行氧化;氧化的时间为3-6小时;(3) Obtain cobaltous hydroxide with good sphericity and crystallinity, wash and filter, control the water content between 10-30%, transfer it to the oxidation kettle, and blow air into it at a temperature of 100-200°C to carry out Oxidation; oxidation time is 3-6 hours; (4)将氧化后的料浆放入鼓风烘箱中,烘干,即得;(4) put the oxidized slurry into a blast oven, and dry to obtain final product; 其中,所述步骤(1)中添加络合剂为每升氢氧化钠溶液中添加0.5-1.5L氨含量25%氨水,或50-100克乙二胺四乙酸二钠;Wherein, the complexing agent added in the step (1) is to add 0.5-1.5L ammonia water with an ammonia content of 25% per liter of sodium hydroxide solution, or 50-100 grams of disodium edetate; 所述步骤(1)中的添加还原剂为每升氢氧化钠溶液中添加20-50毫升含量80%的水合肼溶液。The reducing agent added in the step (1) is to add 20-50 ml of 80% hydrazine hydrate solution per liter of sodium hydroxide solution. 2.根据权利要求1所述的制备方法,其特征在于,所述步骤(1)中的钴盐溶液为CoSO4、CoCl2或Co(NO3)2的一种或两种以上。2. The preparation method according to claim 1, characterized in that the cobalt salt solution in the step (1) is one or more of CoSO 4 , CoCl 2 or Co(NO 3 ) 2 . 3.根据权利要求1所述的制备方法,其特征在于,所述步骤(4)将氧化后的料浆放入鼓风烘箱中,在120℃情况下进行烘干,即得。3. The preparation method according to claim 1, characterized in that, in the step (4), put the oxidized slurry into a blast oven and dry it at 120°C to obtain the finished product.
CN201310124558.6A 2013-04-11 2013-04-11 Preparation method for cobalt oxyhydroxide Active CN103232075B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310124558.6A CN103232075B (en) 2013-04-11 2013-04-11 Preparation method for cobalt oxyhydroxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310124558.6A CN103232075B (en) 2013-04-11 2013-04-11 Preparation method for cobalt oxyhydroxide

Publications (2)

Publication Number Publication Date
CN103232075A CN103232075A (en) 2013-08-07
CN103232075B true CN103232075B (en) 2015-06-03

Family

ID=48880162

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310124558.6A Active CN103232075B (en) 2013-04-11 2013-04-11 Preparation method for cobalt oxyhydroxide

Country Status (1)

Country Link
CN (1) CN103232075B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105129869A (en) * 2015-08-28 2015-12-09 上饶市鼎鑫金属化工有限公司 Novel ammonia-free continuous production technology of spherical large-particle-size CoOOH

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103482710B (en) * 2013-08-27 2015-09-09 江苏华东锂电技术研究院有限公司 Preparation method of spherical cobalt oxyhydroxide
CN103754959B (en) * 2013-12-31 2016-05-04 常州博杰新能源材料有限公司 A kind of preparation method of large granular spherical cobaltosic oxide
CN106549153B (en) * 2015-09-16 2019-04-02 中国科学院大连化学物理研究所 A kind of hollow hexagonal shape hydroxy cobalt oxide nano material and preparation method thereof
CN105271441B (en) * 2015-09-30 2017-08-25 兰州金川新材料科技股份有限公司 A kind of preparation method of the big granularity cobaltosic oxide of LITHIUM BATTERY
CN105869892B (en) * 2016-04-05 2018-03-06 上海交通大学 A kind of High-performance graphene membrane electrode and preparation method thereof
CN107452955B (en) * 2016-06-01 2020-05-19 中国科学院大连化学物理研究所 Hexagonal-prism-shaped cobalt oxyhydroxide material with hollow structure and preparation method thereof
CN105869916B (en) * 2016-06-23 2018-04-24 华中科技大学 A kind of preparation method of hydroxy cobalt oxide nanotube electrode
CN106552630A (en) * 2016-10-26 2017-04-05 上海纳米技术及应用国家工程研究中心有限公司 A kind of spherical CoOXBase catalyst and preparation method and application
CN106340629A (en) * 2016-11-07 2017-01-18 珠海格力电器股份有限公司 Modification method of lithium cobaltate material
CN110655115A (en) * 2019-10-24 2020-01-07 湖南德景源科技有限公司 Production process for continuously synthesizing high-activity spherical manganese oxyhydroxide by one-step method
CN113663672B (en) * 2020-05-15 2023-08-15 香港城市大学深圳研究院 A kind of cobaltous oxide photocatalytic material with high photoelectric catalytic activity and preparation method thereof
CN111924890B (en) * 2020-07-01 2023-07-07 陕西师范大学 Preparation method of CoO (OH) nanoflower
CN113788501B (en) * 2021-09-24 2023-10-17 南通金通储能动力新材料有限公司 Method for preparing cobalt oxyhydroxide
CN116062800B (en) * 2022-12-29 2025-07-08 贵州雅友新材料有限公司 Preparation method and application of cobalt oxyhydroxide

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101687666A (en) * 2007-06-29 2010-03-31 优米科尔公司 High density lithium cobalt oxide for rechargeable batteries
CN102344173A (en) * 2011-10-25 2012-02-08 中信大锰矿业有限责任公司 Method for producing lithium cobaltite by preparing hydroxyl trivalent cobalt oxide through wet chemical reaction
CN102689933A (en) * 2012-03-15 2012-09-26 湖南红太阳电源新材料股份有限公司 Method for producing hydroxy cobalt oxide
CN102881896A (en) * 2012-10-22 2013-01-16 吉林吉恩亚融科技有限公司 Cobalt coating method for spherical nickel hydroxide by mechanical fusion

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101687666A (en) * 2007-06-29 2010-03-31 优米科尔公司 High density lithium cobalt oxide for rechargeable batteries
CN102344173A (en) * 2011-10-25 2012-02-08 中信大锰矿业有限责任公司 Method for producing lithium cobaltite by preparing hydroxyl trivalent cobalt oxide through wet chemical reaction
CN102689933A (en) * 2012-03-15 2012-09-26 湖南红太阳电源新材料股份有限公司 Method for producing hydroxy cobalt oxide
CN102881896A (en) * 2012-10-22 2013-01-16 吉林吉恩亚融科技有限公司 Cobalt coating method for spherical nickel hydroxide by mechanical fusion

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
一种氢氧化钴合成新工艺;龙长江等;《硅谷》;20110930(第18期);第28-29页 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105129869A (en) * 2015-08-28 2015-12-09 上饶市鼎鑫金属化工有限公司 Novel ammonia-free continuous production technology of spherical large-particle-size CoOOH

Also Published As

Publication number Publication date
CN103232075A (en) 2013-08-07

Similar Documents

Publication Publication Date Title
CN103232075B (en) Preparation method for cobalt oxyhydroxide
CN108598400B (en) Three-layer core-shell structure cathode material, preparation method and lithium ion battery
CN107324405B (en) A precursor of nickel-cobalt lithium manganese oxide material and its preparation method, and a lithium-ion battery prepared from the precursor
JP6395951B2 (en) Nickel cobalt aluminum precursor material having aluminum element gradient distribution and method for producing positive electrode material
US10916767B2 (en) Carbon-coated ternary positive electrode material, preparation method therefor, and lithium ion battery
CN102709544B (en) Nickel cobalt lithium manganate composite cathode material and preparation method of nickel cobalt lithium manganate composite cathode material
CN104852038B (en) Preparation method of high-capacity quickly-chargeable/dischargeable lithium ion battery ternary anode material
CN114188536B (en) Lithium ion battery anode material uniformly coated with MOF and preparation method thereof
CN103022476B (en) A kind of preparation method of high nickel content anode material for lithium-ion batteries
CN103715424A (en) Core-shell structured cathode material and preparation method thereof
CN104362341B (en) A kind of high density nano lithium iron phosphate material and preparation method thereof
CN113735190B (en) A kind of small particle ternary precursor and preparation method thereof
CN103570083B (en) A kind of preparation method of lithium ion battery anode material nickel cobalt aluminium spherical precursor
CN115403076A (en) A kind of porous spherical ternary precursor and its preparation method, ternary positive electrode material, positive electrode sheet and battery
CN109103446B (en) Silicon oxide coated high-nickel precursor, modified high-nickel material and preparation method thereof
CN107706366A (en) A kind of positive electrode of indium oxide or tin-doped indium oxide cladding and preparation method thereof
CN104733714B (en) Modification method of lithium ion battery cathode material
CN115072801A (en) Positive electrode material precursor, positive electrode material, preparation method and application thereof
CN103531789A (en) Iron oxide-carbon nanotube ternary composite material and preparation method thereof
CN113178573A (en) Lithium battery spherical positive electrode material with lithium fluoride coating layer and preparation method
CN104716318A (en) Preparation method of spherical nickel-cobalt-manganese precursor
CN105720242A (en) Method for modifying lithium ion battery cathode material
CN116514180A (en) Ternary precursor material, preparation method, ternary cathode material and lithium ion battery
WO2007000075A1 (en) Method for preparing spherical nickelous hydroxide which is dopped and multiple metal oxides, and lithium ion secondary battery
CN103178259A (en) Preparation method of cobalt-coated lithium ion battery anode material

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP01 Change in the name or title of a patent holder

Address after: 410600, Hunan City, Ningxiang province Changsha economic and Technological Development Zone, new road, Accor City Industrial Park

Patentee after: HUNAN YACHENG NEW MATERIAL STOCK CO.,LTD.

Address before: 410600, Hunan City, Ningxiang province Changsha economic and Technological Development Zone, new road, Accor City Industrial Park

Patentee before: HUNAN YACHENG NEW MATERIALS DEVELOPMENT Co.,Ltd.

PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Preparation method for large-grained spherical cobalt oxyhydroxide

Effective date of registration: 20160520

Granted publication date: 20150603

Pledgee: Bank of Beijing Limited by Share Ltd. Changsha branch

Pledgor: HUNAN YACHENG NEW MATERIAL STOCK CO.,LTD.

Registration number: 2016430000008

PLDC Enforcement, change and cancellation of contracts on pledge of patent right or utility model
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20170628

Granted publication date: 20150603

Pledgee: Bank of Beijing Limited by Share Ltd. Changsha branch

Pledgor: HUNAN YACHENG NEW MATERIAL STOCK CO.,LTD.

Registration number: 2016430000008

PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Preparation method for large-grained spherical cobalt oxyhydroxide

Effective date of registration: 20170719

Granted publication date: 20150603

Pledgee: Ningxiang Hunan rural commercial bank Limited by Share Ltd.

Pledgor: HUNAN YACHENG NEW MATERIAL STOCK CO.,LTD.

Registration number: 2017430000044

PE01 Entry into force of the registration of the contract for pledge of patent right
CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: 410600, Hunan City, Ningxiang province Changsha economic and Technological Development Zone, new road, Accor City Industrial Park

Patentee after: HUNAN YACHENG NEW MATERIAL CO.,LTD.

Address before: 410600, Hunan City, Ningxiang province Changsha economic and Technological Development Zone, new road, Accor City Industrial Park

Patentee before: HUNAN YACHENG NEW MATERIAL STOCK CO.,LTD.

PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20181026

Granted publication date: 20150603

Pledgee: Ningxiang Hunan rural commercial bank Limited by Share Ltd.

Pledgor: HUNAN YACHENG NEW MATERIAL STOCK CO.,LTD.

Registration number: 2017430000044

PC01 Cancellation of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Preparation method for large-grained spherical cobalt oxyhydroxide

Effective date of registration: 20200706

Granted publication date: 20150603

Pledgee: Gaoxin sub branch of Bank of Changsha Co.,Ltd.

Pledgor: HUNAN YACHENG NEW MATERIAL Co.,Ltd.

Registration number: Y2020980003799

CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: Yacheng Industrial Park, Xinkang Road, Ningxiang Economic and Technological Development Zone, Changsha City, Hunan Province, 410600

Patentee after: Hunan Yacheng New Energy Co.,Ltd.

Address before: Yacheng Industrial Park, Xinkang Road, Ningxiang Economic and Technological Development Zone, Changsha City, Hunan Province, 410600

Patentee before: HUNAN YACHENG NEW MATERIAL CO.,LTD.

PM01 Change of the registration of the contract for pledge of patent right
PM01 Change of the registration of the contract for pledge of patent right

Change date: 20221024

Registration number: Y2020980003799

Pledgor after: Hunan Yacheng New Energy Co.,Ltd.

Pledgor before: HUNAN YACHENG NEW MATERIAL CO.,LTD.

PM01 Change of the registration of the contract for pledge of patent right
PM01 Change of the registration of the contract for pledge of patent right

Change date: 20250110

Registration number: Y2020980003799

Pledgee after: Bank of Changsha Co.,Ltd. Kaifu sub branch

Pledgee before: Gaoxin sub branch of Bank of Changsha Co.,Ltd.