CN117326577A - Micro-powder-grade lithium oxide and preparation method thereof - Google Patents
Micro-powder-grade lithium oxide and preparation method thereof Download PDFInfo
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Abstract
Description
技术领域Technical field
本发明涉及氧化物制备技术领域,尤其涉及一种微粉级氧化锂及其制备方法。The present invention relates to the technical field of oxide preparation, and in particular to a micron powder grade lithium oxide and a preparation method thereof.
背景技术Background technique
氧化锂是一种性能优良的非水电解质,用它制成的电池除了具有一般锂电池的特性外,还有成本低、无污染等优点。氧化锂除了在锂电池中有重大应用外,还可作为添加剂在玻璃工业中使用,改善玻璃的性能,另外,氧化锂还被用于特种玻璃和锂化合物制备及核聚变反应堆等方面。Lithium oxide is a non-aqueous electrolyte with excellent performance. In addition to the characteristics of general lithium batteries, batteries made with it also have the advantages of low cost and no pollution. In addition to its important applications in lithium batteries, lithium oxide can also be used as an additive in the glass industry to improve the properties of glass. In addition, lithium oxide is also used in the preparation of special glass and lithium compounds and nuclear fusion reactors.
现工业上电池级氧化锂生产主要以金属锂为原料,采用火烧法,经氧化煅烧、筛选、球磨、筛分得到电池级氧化锂,但在球磨及筛分过程中,主要采用半机械化操作,存在设备密封性差,扬尘量大,产品易吸潮、收率低且不环保,生产场所操作人员劳动量大等问题。The current industrial production of battery-grade lithium oxide mainly uses metallic lithium as raw material, using the fire method, and then oxidizing, calcining, screening, ball milling, and screening to obtain battery-grade lithium oxide. However, in the ball milling and screening process, semi-mechanized operations are mainly used. There are problems such as poor sealing of equipment, large amount of dust, easy moisture absorption of products, low yield and non-environmental protection, and heavy workload of operators in the production site.
因此,研究得到一种能够提高氧化锂产品收率以及纯度的制备方法具有重要意义。Therefore, it is of great significance to study a preparation method that can improve the yield and purity of lithium oxide products.
发明内容Contents of the invention
有鉴于此,本发明提供了一种微粉级氧化锂及其制备方法,其目的是解决现有工艺制备氧化锂效率低、纯度低的问题。In view of this, the present invention provides a micro-powder grade lithium oxide and a preparation method thereof, which aims to solve the problems of low efficiency and low purity of lithium oxide prepared by existing processes.
为了达到上述目的,本发明采用如下技术方案:In order to achieve the above objects, the present invention adopts the following technical solutions:
本发明提供了一种微粉级氧化锂的制备方法,包括以下步骤:The invention provides a method for preparing micron-grade lithium oxide, which includes the following steps:
1)将金属锂加热熔化后经氧气喷吹并进行氧化反应,得到氧化锂液滴;1) Heat and melt metallic lithium, then blow it with oxygen and perform an oxidation reaction to obtain lithium oxide droplets;
2)将氧化锂液滴冷却后顺次进行分离和筛分,得到微粉级氧化锂。2) Cool the lithium oxide droplets and then separate and screen them sequentially to obtain micro-powder grade lithium oxide.
优选的,所述金属锂的纯度为≥99.9%。Preferably, the purity of the metallic lithium is ≥99.9%.
优选的,所述加热熔化在真空状态进行,真空状态的真空度为≤1×10-1Pa。Preferably, the heating and melting is performed in a vacuum state, and the degree of vacuum in the vacuum state is ≤1×10 -1 Pa.
优选的,所述加热熔化的温度为390~410℃,所述加热熔化的时间为50~70min。Preferably, the heating and melting temperature is 390-410°C, and the heating and melting time is 50-70 minutes.
优选的,所述氧气的纯度为≥99.99%。Preferably, the oxygen purity is ≥99.99%.
优选的,所述喷吹的气体压力为≥4MPa。Preferably, the blown gas pressure is ≥4MPa.
优选的,所述冷却的温度≤25℃,所述冷却的介质为白油。Preferably, the cooling temperature is ≤25°C, and the cooling medium is white oil.
优选的,所述分离为多级旋风分离。Preferably, the separation is multi-stage cyclone separation.
本发明还提供了所述微粉级氧化锂的制备方法所制得的微粉级氧化锂。The present invention also provides micro-powder-grade lithium oxide prepared by the preparation method of micro-powder-grade lithium oxide.
优选的,所述微粉级氧化锂的D90为60~80μm。Preferably, the D90 of the fine powder grade lithium oxide is 60-80 μm.
经由上述的技术方案可知,与现有技术相比,本发明的有益效果如下:It can be seen from the above technical solutions that compared with the prior art, the beneficial effects of the present invention are as follows:
1)本发明所述加热熔化在真空环境下进行,避免了杂质的引入,得到的氧化锂纯度更高,同时仅发生金属锂跟氧气的反应,不产生其他副产品,其收率更高。1) The heating and melting in the present invention is carried out in a vacuum environment, which avoids the introduction of impurities, and the obtained lithium oxide has higher purity. At the same time, only the reaction between metallic lithium and oxygen occurs, no other by-products are produced, and the yield is higher.
2)本发明采用气雾化法制备氧化锂粉,无需经过球磨操作,简化制备流程,节省劳动力,且避免了球磨过程中引入杂质的问题,提高了氧化锂的纯度及收率。2) The present invention uses a gas atomization method to prepare lithium oxide powder without ball milling operation, which simplifies the preparation process, saves labor, avoids the problem of introducing impurities during the ball milling process, and improves the purity and yield of lithium oxide.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据提供的附图获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the drawings needed to be used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings in the following description are only These are embodiments of the present invention. For those of ordinary skill in the art, other drawings can be obtained based on the provided drawings without exerting creative efforts.
图1为本发明的微粉级氧化锂制备方法的工艺流程图;Figure 1 is a process flow chart of the preparation method of micro-powder grade lithium oxide of the present invention;
图2为实施例3所得微粉级氧化锂的粒径分布图。Figure 2 is a particle size distribution diagram of the fine powder grade lithium oxide obtained in Example 3.
具体实施方式Detailed ways
本发明提供了一种微粉级氧化锂的制备方法,包括以下步骤:The invention provides a method for preparing micron-grade lithium oxide, which includes the following steps:
1)将金属锂加热熔化后经氧气喷吹并进行氧化反应,得到氧化锂液滴;1) Heat and melt metallic lithium, then blow it with oxygen and perform an oxidation reaction to obtain lithium oxide droplets;
2)将氧化锂液滴冷却后顺次进行分离和筛分,得到微粉级氧化锂。2) Cool the lithium oxide droplets and then separate and screen them sequentially to obtain micro-powder grade lithium oxide.
本发明中,所述金属锂的纯度优选为≥99.9%,进一步优选为≥99.99%。In the present invention, the purity of the metallic lithium is preferably ≥99.9%, and further preferably is ≥99.99%.
本发明中,所述加热熔化在真空状态进行,真空状态的真空度优选为≤1×10-1Pa,进一步优选为≤5×10-2Pa,更优选为≤3×10-2Pa。In the present invention, the heating and melting is performed in a vacuum state, and the degree of vacuum in the vacuum state is preferably ≤1×10 -1 Pa, more preferably ≤5×10 -2 Pa, and more preferably ≤3×10 -2 Pa.
本发明中,所述加热熔化的温度优选为390~410℃,进一步优选为395~405℃,更优选为398~402℃,所述加热熔化的时间优选为50~70min,进一步优选为55~65min,更优选为58~62min。In the present invention, the heating and melting temperature is preferably 390 to 410°C, more preferably 395 to 405°C, and more preferably 398 to 402°C, and the heating and melting time is preferably 50 to 70 min, further preferably 55 to 55 min. 65min, more preferably 58-62min.
本发明中,所述喷吹优选在喷盘中进行,喷盘中含有角度可调的喷嘴,所述喷嘴的角度优选为0~80°,进一步优选为30~60°,更优选为40~50°。In the present invention, the blowing is preferably performed in a spray plate, which contains an angle-adjustable nozzle. The angle of the nozzle is preferably 0 to 80°, more preferably 30 to 60°, and more preferably 40 to 40°. 50°.
本发明中,加热熔化后的金属锂通过导流嘴流至喷盘,所述导流嘴的温度优选为≥250℃,进一步优选为≥300℃,更优选为≥320℃。In the present invention, the heated and melted metallic lithium flows to the spray plate through the guide nozzle, and the temperature of the guide nozzle is preferably ≥250°C, more preferably ≥300°C, and more preferably ≥320°C.
本发明中,所述氧气的纯度优选为≥99.99%,进一步优选为≥99.999%。In the present invention, the purity of the oxygen is preferably ≥99.99%, and further preferably ≥99.999%.
本发明中,所述喷吹的气体压力优选为≥4MPa,进一步优选为4~6MPa,更优选为4.5~5.5MPa。In the present invention, the blown gas pressure is preferably ≥4MPa, more preferably 4-6MPa, and more preferably 4.5-5.5MPa.
本发明中,所述冷却的温度优选≤25℃,进一步优选为≤23℃,更优选为≤20℃,所述冷却的介质优选为白油。In the present invention, the cooling temperature is preferably ≤25°C, more preferably ≤23°C, and more preferably ≤20°C, and the cooling medium is preferably white oil.
本发明中,所述白油优选为化妆级白油。In the present invention, the white oil is preferably cosmetic grade white oil.
本发明中,所述分离优选为多级旋风分离。In the present invention, the separation is preferably multi-stage cyclone separation.
本发明中,所述分离后优选对分离后产物进行筛分,所述筛分优选采用振动筛。In the present invention, the separated product is preferably screened after the separation, and a vibrating screen is preferably used for the screening.
本发明还提供了所述微粉级氧化锂的制备方法所制得的微粉级氧化锂。The present invention also provides micro-powder-grade lithium oxide prepared by the preparation method of micro-powder-grade lithium oxide.
本发明中,所述微粉级氧化锂的D90优选为60~80μm,进一步优选为63~78μm,更优选为65~70μm。In the present invention, the D90 of the fine powder grade lithium oxide is preferably 60 to 80 μm, more preferably 63 to 78 μm, and even more preferably 65 to 70 μm.
下面结合实施例对本发明提供的技术方案进行详细的说明,但是不能把它们理解为对本发明保护范围的限定。The technical solutions provided by the present invention will be described in detail below with reference to the examples, but they should not be understood as limiting the protection scope of the present invention.
实施例1Example 1
在不锈钢坩埚中加入5kg纯度为99.99%的金属锂,抽真空至5×10-2Pa,在400℃下加热60min,制得完全熔化的金属锂;Add 5kg of metallic lithium with a purity of 99.99% into a stainless steel crucible, evacuate to 5×10 -2 Pa, and heat at 400°C for 60 minutes to obtain completely melted metallic lithium;
将喷盘的喷嘴角度调至45°,以4MPa的气压通入纯度为99.99%的氧气,打开导流嘴阀门,提起不锈钢坩埚底部金属堵杆,使金属锂液经300℃的导流嘴流至喷盘中,经氧气喷吹破碎雾化,破碎的金属锂液与氧气进行氧化反应,得到氧化锂液滴;Adjust the nozzle angle of the spray plate to 45°, introduce oxygen with a purity of 99.99% at an air pressure of 4MPa, open the guide valve, lift the metal blocking rod at the bottom of the stainless steel crucible, and allow the metallic lithium liquid to flow through the 300°C guide nozzle. To the spray plate, it is broken and atomized by oxygen injection, and the broken lithium metal liquid undergoes an oxidation reaction with oxygen to obtain lithium oxide droplets;
将氧化锂液滴通入冷却介质为化妆级白油的冷却室内冷却至25℃,得到氧化锂粉,氧化锂粉在引风机中进行多级旋风分离后进入收集罐,将收集罐中的氧化锂粉末通过振动筛对氧化锂粉末进行筛分,得到微粉级氧化锂。The lithium oxide droplets are passed into a cooling chamber in which the cooling medium is cosmetic-grade white oil and are cooled to 25°C to obtain lithium oxide powder. The lithium oxide powder undergoes multi-stage cyclone separation in an induced draft fan and then enters the collection tank, where the oxidized water in the collection tank is removed. The lithium powder is sieved through a vibrating sieve to obtain micro-powder grade lithium oxide.
本实施例所得微粉级氧化锂的质量为10.809kg,微粉级氧化锂的纯度为99.281%,粒度D10=5.323μm,D50=30.210μm,D90=78.862μm。The mass of the micronized lithium oxide obtained in this example is 10.809kg, the purity of the micronized lithium oxide is 99.281%, and the particle size is D10=5.323μm, D50=30.210μm, and D90=78.862μm.
实施例2Example 2
在不锈钢坩埚中加入5kg纯度为99.99%的金属锂,抽真空至3×10-2Pa,在410℃下加热55min,制得完全熔化的金属锂;Add 5kg of metallic lithium with a purity of 99.99% into a stainless steel crucible, evacuate to 3×10 -2 Pa, and heat at 410°C for 55 minutes to obtain completely melted metallic lithium;
将喷盘的喷嘴角度调至45°,以5MPa的气压通入纯度为99.99%的氧气,打开导流嘴阀门,提起不锈钢坩埚底部金属堵杆,使金属锂液经250℃的导流嘴流至喷盘中,经氧气喷吹破碎雾化,破碎的金属锂液与氧气进行氧化反应,得到氧化锂液滴;Adjust the nozzle angle of the spray plate to 45°, introduce oxygen with a purity of 99.99% at an air pressure of 5MPa, open the diversion nozzle valve, lift the metal blocking rod at the bottom of the stainless steel crucible, and allow the metallic lithium liquid to flow through the diversion nozzle at 250°C. To the spray plate, it is broken and atomized by oxygen injection, and the broken lithium metal liquid undergoes an oxidation reaction with oxygen to obtain lithium oxide droplets;
将氧化锂液滴通入冷却介质为化妆级白油的冷却室内冷却至23℃,得到氧化锂粉,氧化锂粉在引风机中进行多级旋风分离后进入收集罐,将收集罐中的氧化锂粉末通过振动筛对氧化锂粉末进行筛分,得到微粉级氧化锂。The lithium oxide droplets are passed into a cooling chamber in which the cooling medium is cosmetic-grade white oil and are cooled to 23°C to obtain lithium oxide powder. The lithium oxide powder undergoes multi-stage cyclone separation in the induced draft fan and then enters the collection tank. The lithium powder is sieved through a vibrating sieve to obtain micro-powder grade lithium oxide.
本实施例所得微粉级氧化锂的质量为10.803kg,微粉级氧化锂的纯度为99.374%,粒度D10=4.805μm,D50=25.201μm,D90=64.745μm。The mass of the micronized lithium oxide obtained in this example is 10.803kg, the purity of the micronized lithium oxide is 99.374%, and the particle size is D10=4.805μm, D50=25.201μm, and D90=64.745μm.
实施例3Example 3
在钛坩埚中加入8kg纯度为99.99%的金属锂,抽真空至8×10-3Pa,在395℃下加热65min,制得完全熔化的金属锂;Add 8kg of metallic lithium with a purity of 99.99% into the titanium crucible, evacuate to 8×10 -3 Pa, and heat at 395°C for 65 minutes to obtain completely melted metallic lithium;
将喷盘的喷嘴角度调至45°,以5MPa的气压通入纯度为99.99%的氧气,打开导流嘴阀门,提起钛坩埚底部金属堵杆,使金属锂液经350℃的导流嘴流至喷盘中,经氧气喷吹破碎雾化,破碎的金属锂液与氧气进行氧化反应,得到氧化锂液滴;Adjust the nozzle angle of the spray plate to 45°, introduce oxygen with a purity of 99.99% at an air pressure of 5MPa, open the diversion nozzle valve, lift the metal blocking rod at the bottom of the titanium crucible, and allow the metallic lithium liquid to flow through the diversion nozzle at 350°C. To the spray plate, it is broken and atomized by oxygen injection, and the broken lithium metal liquid undergoes an oxidation reaction with oxygen to obtain lithium oxide droplets;
将氧化锂液滴通入冷却介质为化妆级白油的冷却室内冷却至25℃,得到氧化锂粉,氧化锂粉在引风机中进行多级旋风分离后进入收集罐,将收集罐中的氧化锂粉末通过振动筛对氧化锂粉末进行筛分,得到微粉级氧化锂。The lithium oxide droplets are passed into a cooling chamber in which the cooling medium is cosmetic-grade white oil and are cooled to 25°C to obtain lithium oxide powder. The lithium oxide powder undergoes multi-stage cyclone separation in an induced draft fan and then enters the collection tank, where the oxidized water in the collection tank is removed. The lithium powder is sieved through a vibrating sieve to obtain micro-powder grade lithium oxide.
本实施例所得微粉级氧化锂的质量为17.289kg,微粉级氧化锂的纯度为99.332%,粒度D10=5.731μm,D50=30.390μm,D90=78.716μm。The mass of the micronized lithium oxide obtained in this example is 17.289kg, the purity of the micronized lithium oxide is 99.332%, and the particle size is D10=5.731μm, D50=30.390μm, and D90=78.716μm.
实施例4Example 4
在钛坩埚中加入5kg纯度为99.99%的金属锂,抽真空至5×10-3Pa,在400℃下加热60min,制得完全熔化的金属锂;Add 5kg of metallic lithium with a purity of 99.99% into the titanium crucible, evacuate to 5×10 -3 Pa, and heat at 400°C for 60 minutes to obtain completely melted metallic lithium;
将喷盘的喷嘴角度调至60°,以4MPa的气压通入纯度为99.99%的氧气,打开导流嘴阀门,提起钛坩埚底部金属堵杆,使金属锂液经250℃的导流嘴流至喷盘中,经氧气喷吹破碎雾化,破碎的金属锂液与氧气进行氧化反应,得到氧化锂液滴;Adjust the nozzle angle of the spray plate to 60°, introduce oxygen with a purity of 99.99% at an air pressure of 4MPa, open the diversion nozzle valve, lift the metal blocking rod at the bottom of the titanium crucible, and allow the metallic lithium liquid to flow through the diversion nozzle at 250°C. To the spray plate, it is broken and atomized by oxygen injection, and the broken lithium metal liquid undergoes an oxidation reaction with oxygen to obtain lithium oxide droplets;
将氧化锂液滴通入冷却介质为化妆级白油的冷却室内冷却至20℃,得到氧化锂粉,氧化锂粉在引风机中进行多级旋风分离后进入收集罐,将收集罐中的氧化锂粉末通过振动筛对氧化锂粉末进行筛分,得到微粉级氧化锂。The lithium oxide droplets are passed into a cooling chamber in which the cooling medium is cosmetic-grade white oil and are cooled to 20°C to obtain lithium oxide powder. The lithium oxide powder undergoes multi-stage cyclone separation in an induced draft fan and then enters the collection tank. The oxidation in the collection tank is The lithium powder is sieved through a vibrating sieve to obtain micro-powder grade lithium oxide.
本实施例所得微粉级氧化锂的质量为10.804kg,微粉级氧化锂的纯度为99.351%,粒度D10=4.168μm,D50=27.022μm,D90=69.069μm。The mass of the micro-powder grade lithium oxide obtained in this example is 10.804kg, the purity of the micro-powder grade lithium oxide is 99.351%, and the particle size is D10=4.168 μm, D50=27.022 μm, and D90=69.069 μm.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above are only preferred embodiments of the present invention. It should be noted that those skilled in the art can make several improvements and modifications without departing from the principles of the present invention. These improvements and modifications can also be made. should be regarded as the protection scope of the present invention.
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4221775A (en) * | 1978-12-26 | 1980-09-09 | Research Dynamics, Inc. | Method of producing porous lithium oxide |
| GB8707609D0 (en) * | 1986-04-11 | 1987-05-07 | Lithium Corp | High purity lithium oxide process |
| CN102515211A (en) * | 2011-12-06 | 2012-06-27 | 江西赣锋锂业股份有限公司 | Method for preparing high-purity lithium oxide |
| JP2012252853A (en) * | 2011-06-02 | 2012-12-20 | Toyota Industries Corp | Method for manufacturing lithium-containing complex oxide, positive electrode active material, and secondary battery |
| CN115650263A (en) * | 2022-11-04 | 2023-01-31 | 成都开飞高能化学工业有限公司 | Preparation method of battery-grade lithium oxide |
-
2023
- 2023-10-24 CN CN202311381855.9A patent/CN117326577A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4221775A (en) * | 1978-12-26 | 1980-09-09 | Research Dynamics, Inc. | Method of producing porous lithium oxide |
| GB8707609D0 (en) * | 1986-04-11 | 1987-05-07 | Lithium Corp | High purity lithium oxide process |
| JP2012252853A (en) * | 2011-06-02 | 2012-12-20 | Toyota Industries Corp | Method for manufacturing lithium-containing complex oxide, positive electrode active material, and secondary battery |
| CN102515211A (en) * | 2011-12-06 | 2012-06-27 | 江西赣锋锂业股份有限公司 | Method for preparing high-purity lithium oxide |
| CN115650263A (en) * | 2022-11-04 | 2023-01-31 | 成都开飞高能化学工业有限公司 | Preparation method of battery-grade lithium oxide |
Non-Patent Citations (2)
| Title |
|---|
| 曾郴林编: "《电化学法废水处理技术及其应用》", vol. 2022, 31 January 2022, 中国环境出版集团, pages: 234 - 235 * |
| 游曦鸣;佟立丽;曹学武;: "熔融锂液滴与冷却剂在不同温度下的相互作用实验研究", 核科学与工程, no. 03, 15 June 2017 (2017-06-15), pages 36 - 41 * |
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