阅读说明：本技术 一种锂离子电池正极浆料的匀浆方法 (Homogenizing method of lithium ion battery anode slurry ) 是由 陈慧 郭彬彬 于 2020-05-21 设计创作，主要内容包括：本发明提供一种锂离子电池正极浆料的匀浆方法,步骤如下：S1、使用自动下料系统,将正极活性物质、导电剂干粉、粘结剂干粉按照配比逐一下料至双行星搅拌机中进行粉体预混合得到干粉混合料；S2、将溶剂分成两份,在步骤S1制成的干粉混合料中按配比加入导电剂浆料和一份溶剂,进行第一次混合得到半成品浆料；S3、开启高速混合机,将步骤S2得到的半成品浆料和另一份溶剂输入高速混合机中进行高速混合分散,将混合完成后的浆料打入A循环罐中；S4、将A循环罐中的浆料再次输入高速混合机中进行高速混合分散,混合完成后的浆料打入B循环罐中。本发明中同时使用双行星搅拌机和高速混合机,可提高浆料分散均匀性,浆料颗粒度一致性更好。(The invention provides a homogenizing method of lithium ion battery anode slurry, which comprises the following steps: s1, using an automatic blanking system to blank the positive active material, the conductive agent dry powder and the binder dry powder one by one according to the proportion into a double-planet mixer to pre-mix the powder to obtain a dry powder mixture; s2, dividing the solvent into two parts, adding the conductive agent slurry and one part of the solvent into the dry powder mixture prepared in the step S1 according to the proportion, and mixing for the first time to obtain semi-finished product slurry; s3, starting a high-speed mixer, inputting the semi-finished slurry obtained in the step S2 and the other part of solvent into the high-speed mixer for high-speed mixing and dispersing, and pumping the mixed slurry into a circulation tank A; and S4, inputting the slurry in the circulation tank A into the high-speed mixer again for high-speed mixing and dispersing, and driving the mixed slurry into the circulation tank B. According to the invention, the double-planet stirrer and the high-speed mixer are used at the same time, so that the dispersion uniformity of the slurry can be improved, and the uniformity of the granularity of the slurry is better.)

1. A homogenizing method of lithium ion battery anode slurry is characterized by comprising the following steps:

s1, using an automatic blanking system to blank the positive active material, the conductive agent dry powder and the binder dry powder one by one according to the proportion into a double-planet mixer to pre-mix the powder to obtain a dry powder mixture;

s2, dividing the solvent into two parts, adding the conductive agent slurry and one part of the solvent into the dry powder mixture prepared in the step S1 according to the mixture ratio, and still adopting a double-planet mixer to carry out primary mixing to obtain semi-finished product slurry;

s3, starting a high-speed mixer, inputting the semi-finished slurry obtained in the step S2 and the other part of solvent into the high-speed mixer for high-speed mixing and dispersing, and pumping the mixed slurry into a circulation tank A;

and S4, inputting the slurry in the circulation tank A into the high-speed mixer again for high-speed mixing and dispersing, and driving the mixed slurry into the circulation tank B.

2. The method for homogenizing lithium ion battery positive electrode slurry according to claim 1, wherein in step S1, the revolution speed of the double planetary mixer is 13 to 17rpm, the dispersion linear speed is 10 to 17m/min, and the mixing time is 15 to 30 min.

3. The method for homogenizing lithium ion battery positive electrode slurry according to claim 1, wherein in step S2, the revolution speed of the double planetary mixer is 13 to 17rpm, the dispersion linear speed is 1 to 10m/min, and the mixing time is 30 to 60 min.

4. The method for homogenizing lithium ion battery positive electrode slurry according to claim 1, wherein the rotating speed of the high-speed mixer in steps S3 and S4 is 3000-6000 rpm, the linear speed is 25-70 m/S, and the flow rate is 30-60L/min.

5. The method for homogenizing lithium ion battery positive electrode slurry according to claim 1, wherein in step S2, the solvent is first divided into two parts of 50% to 70% and 30% to 50% by mass; one part accounting for 50-70% of the total amount of the solvent is added in the step S2, and one part accounting for 30-50% of the total amount of the solvent is added in the step S3.

6. The method for homogenizing lithium ion battery positive electrode slurry according to claim 1, wherein the solid content of the semi-finished slurry in the step S2 is 78-85%, and the solid content of the slurry after mixing in the step S3 is 70-75%.

7. The method for homogenizing lithium ion battery positive electrode slurry according to claim 1, wherein the semi-finished slurry and the solvent are fed into a high-speed mixer using a screw machine in step S3.

8. The method for homogenizing lithium ion battery positive electrode slurry according to claim 1, wherein the slurry in the circulation tank a is again fed into the high-speed mixer using a screw pump in step S4.

9. The method for homogenizing lithium ion battery positive electrode slurry according to claim 1, further comprising the steps of:

and S5, slowly stirring the slurry in the B circulation tank, vacuumizing, defoaming, and then carrying out performance detection, if the slurry is not qualified, repeating the mixing and dispersing process of the high-speed mixer in the steps S3 and S4 until the slurry is qualified, and discharging the qualified slurry to a transfer tank.

Technical Field

The invention belongs to the technical field of lithium ion battery production and manufacturing, and particularly relates to a homogenizing method of lithium ion battery anode slurry.

Background

With the continuous fermentation of hot topics such as energy conservation and emission reduction and environmental protection, the technology of new energy vehicles is rapidly developed in nearly two years, and various large whole vehicles and factories are rapidly distributed in the field of new energy vehicles, and lithium ion power batteries serving as one of three core parts of the new energy vehicles are also rapidly developed. In recent two years, the capacity of each large power battery plant has a major breakthrough, and cost reduction and efficiency improvement become a hot topic in the power battery industry in the competitive environment of the trade.

In the production and manufacture of lithium ion power batteries, homogenate is the first process, which not only directly determines the performance of the lithium ion batteries, but also influences the cost of battery core manufacture. How to stir out the positive and negative electrode slurry with rheological property suitable for coating in a short time, good viscosity consistency and high slurry stability, improve the production efficiency and reduce the cost is a problem that practitioners in the industry always think.

The invention patent CN 107910546A discloses a conductive adhesive anode homogenate process, which adopts the steps that a binder is dissolved in a part of solvent to form a glue solution, conductive carbon is added into the glue solution and stirred to form conductive adhesive, then a main material is added into the conductive adhesive and stirred, and finally the residual solvent is added and stirred to form slurry with target solid content and viscosity. The disadvantages of this method are: the time from feeding to discharging exceeds 10 hours, the production efficiency and the equipment utilization rate are very low, and a large number of mixers need to be purchased to meet the capacity requirement during mass production, so the equipment investment cost and the occupied area are very large.

The invention patent CN 110600671A discloses a semidry batching process for lithium ion battery electrode slurry, which comprises the steps of preparing a part of adhesive into adhesive liquid, and then respectively dividing adhesive dry powder and adhesive liquid into N equal parts to be gradually added into main material and conductive agent dry powder. However, this homogenization method has the following disadvantages: (1) the operation steps are complicated, at least more than 15 times of operations such as feeding, parameter setting and the like are performed, and the operation of staff is easy to make mistakes, so that the operation is not beneficial to normal mass production; (2) the adhesive is divided into two forms of powder and glue solution, and a method of adding for multiple times is adopted; the requirement on an equipment metering system is extremely high, and the accumulated error in the process is gradually increased, so that the deviation between the actual blanking weight and the theoretical blanking weight is increased; (3) the homogenization time is long, the whole process needs at least 300min, the high-efficiency production is not facilitated, and the operation cost such as electricity charge and the like is increased; (4) the consistency of the slurry viscosity is poor, the binder is added in multiple steps, the amount of free binder is unstable, and the discharge viscosity has large fluctuation.

The invention patent CN 103268931B discloses a lithium battery positive and negative electrode slurry production process and system, in which powder is gradually added into a double-screw extruder according to the flow of a mixture ratio, so that online discharging is realized while feeding is realized. Greatly shortens the homogenate time and improves the homogenate efficiency. The disadvantages of this method are: (1) the homogenization time is too short, and the powder is about 10min from the screw inlet to the screw outlet. The soaking time of the powder by the liquid is insufficient, so that the consistency of the slurry is poor; the time for coating the main material by the conductive agent and the binder is insufficient, so that the slurry is easy to agglomerate; (2) the viscosity of the discharged slurry is greatly influenced by the rotating speed of the double screws, and is greatly influenced by the parameters of the supplied raw materials, and the data of the supplied raw materials have certain fluctuation; therefore, the viscosity fluctuation of the slurry prepared from different batches of raw materials is large; (3) the device has huge slurry loss during discontinuous production, and a large amount of slurry filling residues can be left in the double-screw extruder when the production is stopped and can not be discharged; a large amount of slurry fill is also required when the purged twin screw extruder is restarted.

The invention patent CN 110265624A discloses a preparation method of lithium ion battery anode slurry, which comprises the following steps: s1, mixing the positive electrode active material, the conductive agent and the adhesive, stirring and dispersing to obtain a mixture; s2, dividing the solvent into at least two parts, pouring the solvent into the mixture in batches, and stirring to obtain a coarse mixed slurry; and S3, stirring the rough mixed slurry at a high speed to obtain the fine mixed slurry. The disadvantages of this method are: all solvents are added in the double-planet stirrer, the high-speed dispersion stirrer is a high-capacity stirrer similar to the double-planet stirrer, and all materials are added in the high-speed stirrer, so that the problem of uneven mixing is caused, and the granularity of the slurry is inconsistent.

Disclosure of Invention

In order to overcome the problems in the prior art, the homogenizing method of the lithium ion battery anode slurry is high in homogenizing efficiency, low in operation cost, good in slurry consistency and high in stability.

In order to achieve the purpose, the invention is realized by the following technical scheme:

a homogenizing method of lithium ion battery anode slurry comprises the following steps:

s1, using an automatic blanking system to blank the positive active material, the conductive agent dry powder and the binder dry powder one by one according to the proportion into a double-planet mixer to pre-mix the powder to obtain a dry powder mixture;

s2, dividing the solvent into two parts, adding the conductive agent slurry and one part of the solvent into the dry powder mixture prepared in the step S1 according to the mixture ratio, and still adopting a double-planet mixer to carry out primary mixing to obtain semi-finished product slurry;

s3, starting a high-speed mixer, inputting the semi-finished slurry obtained in the step S2 and the other part of solvent into the high-speed mixer for high-speed mixing and dispersing, and pumping the mixed slurry into a circulation tank A;

and S4, inputting the slurry in the circulation tank A into the high-speed mixer again for high-speed mixing and dispersing, and driving the mixed slurry into the circulation tank B.

Further, in step S1, the revolution speed of the double planetary stirrer is 13-17 rpm, the dispersion linear speed is 10-17 m/min, and the stirring time is 15-30 min.

Further, in step S2, the revolution speed of the double planetary mixer is 13-17 rpm, the dispersion linear speed is 1-10 m/min, and the mixing time is 30-60 min.

Furthermore, the rotating speed of the high-speed mixer in the steps S3 and S4 is 3000-6000 rpm, the linear speed is 25-70 m/S, and the flow rate is 30-60L/min.

Further, in step S2, the solvent is first divided into two portions of 50% -70% and 30% -50% by mass; one part accounting for 50-70% of the total amount of the solvent is added in the step S2, and one part accounting for 30-50% of the total amount of the solvent is added in the step S3.

Further, the amount of the solvent added in step S3 is 30% to 50% of the total amount of the solvent.

Further, the solid content of the semi-finished slurry in the step S2 is 78-85%.

Further, the solid content of the slurry mixed in the step S3 is 70-75%.

Further, the semi-finished slurry and the solvent are fed into the high-speed mixer using a screw machine in step S3.

Further, the slurry in the a-cycle tank was again input into the high-speed mixer using a screw pump in step S4.

Further, the method also comprises the following steps:

and S5, slowly stirring the slurry in the B circulation tank, vacuumizing, defoaming, and then carrying out performance detection, if the slurry is not qualified, repeating the mixing and dispersing process of the high-speed mixer in the steps S3 and S4 until the slurry is qualified, and discharging the qualified slurry to a transfer tank.

The type of the positive electrode active material is not particularly limited, and various positive electrode active materials commonly used in the art may be used. Preferably, the positive active material is lithium nickel cobalt manganese oxide (NCM) or lithium iron phosphate (LFP).

The positive electrode conductive agent may be various positive electrode conductive agents commonly used in lithium ion batteries, for example, one or more of Super-P (small particle conductive carbon black), graphite, acetylene black, carbon fiber, Carbon Nanotube (CNT), carbonyl nickel powder, copper powder, iron powder, zinc powder, and aluminum powder. Preferably, the positive electrode conductive agent is a mixture of Super-P and carbon nanotubes.

The kind and content of the positive electrode binder may be conventionally selected in the art, for example, at least one of polyvinylidene fluoride (PVDF), Polytetrafluoroethylene (PTFE), polyacrylic acid (PAA), sodium carboxymethylcellulose (CMC), and Polyethylene (PE). Preferably, the positive electrode binder is polyvinylidene fluoride (PVDF).

The kind of the solvent is not particularly limited, and various solvents commonly used in the art may be used. Preferably, the solvent is N-methylpyrrolidone (NMP).

The invention has the following beneficial effects:

(1) the homogenizing time is short, the homogenizing efficiency is greatly improved, meanwhile, 1500L tanks are used in the circulating dispersion process of the double-planet stirrer, the high-speed mixer, the circulation tank A, the high-speed mixer and the circulation tank B, the flow rate is 50L/min, only 30min is needed for one circulation, only 60min is needed for two times, and the total time can be controlled to be 3-3.5h by about 1.5h of the operation of the double-planet stirrer, so that the homogenizing time is greatly reduced, the homogenizing efficiency is improved, and each machine can prepare more than 700kg/h of anode slurry.

(2) According to the invention, the slurry and the solvent are metered by one weight before entering the high-speed mixer, an error of three to five thousandths exists, so that some differences exist in the formula, if the high-speed mixer is used, the unilateral circulation method of the circulation tank A is adopted, the slurry in the tank A can only be slowly stirred and coarsely mixed by the stirring device of the circulation tank A, slight differences exist in the formula proportion of the slurry at the upper layer and the lower layer, and the difference is expressed in solid content and viscosity.

(3) According to the invention, the double-planet stirrer and the high-speed mixer are used at the same time, and the circulation tank A and the circulation tank B are designed to contain the slurry, so that the problem of uneven slurry dispersion caused by a preparation method only using the high-speed mixer and the circulation tank A is solved, the slurry dispersion uniformity can be improved through a circulation dispersion mode of high-speed dispersion for two times, and the consistency of the viscosity and the solid content of the slurry is better.

(4) The invention uses the double-planet mixer, and solves the problem of higher viscosity caused by the circulation and dispersion of a single high-speed mixer. Meanwhile, the solid content of the slurry can be further improved, and the raw material cost of a single battery cell can be reduced.

(5) The invention uses the high-speed mixer, which has the function of quickly dispersing the slurry at high speed, so that the conductive agent and the CNT in the slurry can be dispersed more uniformly in the high-speed dispersion process of feeding the slurry upwards and discharging the slurry downwards, and the resistivity of the coated pole piece is better in consistency.

(6) According to the invention, the dry powder of the conductive agent, the dry powder of the binder and other auxiliary materials are mixed with the dry powder of the main material, and then part of the solvent and the CNT slurry are added, so that the condition that the dry powder of the conductive agent and the dry powder of the binder are concentrated together and the dispersion is not uniform due to serious agglomeration of the CNT is avoided.

Drawings

Fig. 1 is a flow diagram of the preparation of a lithium ion battery positive electrode slurry according to the present invention.

Detailed Description

In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention will be described in further detail below with reference to the accompanying drawings and specific embodiments.

The embodiment of the invention provides an electrolyte for a lithium ion battery and a preparation method of the lithium ion battery.

The type of the positive electrode active material is not particularly limited, and various positive electrode active materials commonly used in the art may be used. Preferably, the positive active material is lithium nickel cobalt manganese oxide (NCM) or lithium iron phosphate (LFP).

The positive electrode conductive agent may be various positive electrode conductive agents commonly used in lithium ion batteries, for example, one or more of Super-P (small particle conductive carbon black), graphite, acetylene black, carbon fiber, Carbon Nanotube (CNT), carbonyl nickel powder, copper powder, iron powder, zinc powder, and aluminum powder. Preferably, the positive electrode conductive agent is a mixture of Super-P and carbon nanotubes.

The kind and content of the positive electrode binder may be conventionally selected in the art, for example, at least one of polyvinylidene fluoride (PVDF), Polytetrafluoroethylene (PTFE), polyacrylic acid (PAA), sodium carboxymethylcellulose (CMC), and Polyethylene (PE). Preferably, the positive electrode binder is polyvinylidene fluoride (PVDF).

The kind of the solvent is not particularly limited, and various solvents commonly used in the art may be used. Preferably, the solvent is N-methylpyrrolidone (NMP).

1. The present invention will be further illustrated by the following comparative examples and examples, but the present invention is not limited to these examples.

Comparative example 1

Weighing slurry comprising 97 parts of NCM powder, 1 part of Super-P powder (as a conductive agent), 1.5 parts of PVDF powder (as a binder) and 0.5 part of CNT (as a conductive agent) according to mass fraction, and preparing the anode slurry by adopting a traditional wet conductive adhesive batching process, wherein the method comprises the following specific steps:

step 1: dissolving 1.5 parts of PVDF powder in NMP to prepare PVDF glue solution, controlling the solid content of the glue solution at 6.5%, and stirring for 4-6 h.

Step 2: adding 1 part of Super-P powder into the glue solution, stirring for 30min, adding slurry containing 0.5 part of CNT, starting revolution for 15-17r/min, rotating at a linear speed of 13-18m/s, and stirring at a high speed for 2-4 h.

And step 3: adding 96 parts of NCM powder and the residual NMP into the glue solution in the step 2, starting revolution for 15-17r/min, linear speed for 15-23m/s, starting temperature control, and stirring at high speed for 2-4 h.

And 4, step 4: opening the stirring kettle to vacuum-85 kPa, revolving at 15-17r/min, controlling the linear velocity at 15-23m/s, controlling the starting temperature, stirring at high speed for 0.5-1.5h, testing the viscosity, fineness and solid content of the slurry, and discharging when the slurry is qualified; otherwise, stirring for 30min under the same parameters.

The traditional wet homogenization method consumes 8-11h in total time, and has long homogenization time and low homogenization efficiency.

Comparative example 2

Weighing 97 parts of LFP powder, 0.5 part of Super-P powder (serving as a conductive agent), 1.8 parts of PVDF powder (serving as a binder) and 0.7 part of slurry containing CNT (serving as a conductive agent) according to mass fraction, and preparing the anode slurry by adopting a semi-dry kneading batching process, wherein the method comprises the following specific steps:

step 1: and (3) dissolving 1.8 parts of PVDF powder in NMP to prepare a PVDF glue solution, wherein the solid content is controlled to be 6.5 percent, and the time is consumed for 4-6 hours.

Step 2: putting 97 parts of LFP powder and 0.5 part of Super-P powder into a double-planet stirrer, starting revolution for 15-17r/min, rotating for 8-13m/s, and stirring for 30 min.

And step 3: adding the slurry containing 0.7 part of CNT into a stirrer, and starting revolution for 15-17 r/min. Rotating at 8-13m/s, and stirring for 30 min.

And 4, step 4: and (3) adding 50% of the glue solution prepared in the step (1) into a stirrer, starting revolution for 15-17r/min, rotating for 10-15m/s, controlling the starting temperature, and stirring for 90-120 min.

And 5: adding the rest glue solution and NMP into a stirrer, starting revolution for 15-17r/min, rotating for 18-23m/s, starting temperature control, and stirring for 150-.

Step 6: and (3) starting the stirring kettle to have vacuum of-85 kPa, revolving for 15-17r/min, controlling the linear velocity for 15-23m/s, starting temperature control, stirring at a high speed for 0.5-1.5h, testing the viscosity, fineness and solid content of the slurry, discharging when the slurry is qualified, and stirring for 30min if the slurry is not qualified.

Comparative example 3

Weighing 97 parts of NCM powder, 1 part of Super-P powder (as a conductive agent), 1.5 parts of PVDF powder (as a binder) and 0.5 part of slurry containing CNT (as a conductive agent) according to mass fraction, and preparing the anode slurry by adopting a full dry mixing process, wherein the specific steps are as follows:

step 1: 97 parts of NCM powder, 1 part of Super-P powder and 1.5 parts of PVDF powder are added into a double-planet stirrer, and the revolution is started to be 13-17r/min, the rotation is started to be 300-fold and 500r/min, and the stirring is carried out for 30 min.

Step 2: adding slurry containing 0.5 part of CNT and 50% of NMP into a stirrer, starting revolution for 15-17r/min, rotating for 300-500r/min, and stirring for 60 min.

And step 3: adding the rest 50% of solvent into the stirrer, starting revolution at 15-17r/min, and stirring at 1100r/min for 90-120min by dispersion at 800-.

Step 4: and (3) conveying the slurry in the step (3) to an impeller type high-speed mixer with the rotating speed of 5000r/min by adopting a screw according to a fixed flow, and pumping the slurry into a circulation tank A after mixing for 30-60 min.

And 5: testing the viscosity, solid content and granularity of the slurry after completion; discharging when the viscosity is qualified, otherwise adding a certain amount of NMP according to the viscosity data, and adjusting the viscosity according to the parameters in the step 4.

Comparative example 4

Weighing 97 parts of NCM powder, 1 part of Super-P powder (as a conductive agent), 1.5 parts of PVDF powder (as a binder) and 0.5 part of slurry containing CNT (as a conductive agent) according to mass fraction, and preparing the anode slurry by adopting a full dry mixing process, wherein the specific steps are as follows:

step 1: 97 parts of NCM powder, 1 part of Super-P powder and 1.5 parts of PVDF powder are added into a double-planet stirrer, and the revolution is started to be 13-17r/min, the rotation is started to be 300-fold and 500r/min, and the stirring is carried out for 30 min.

Step 2: adding slurry containing 0.5 part of CNT and 50% of NMP into a stirrer, starting revolution for 15-17r/min, rotating for 300-500r/min, and stirring for 60 min.

And step 3: adding the rest 50% of solvent into the stirrer, starting revolution at 15-17r/min, and stirring at 1100r/min for 90-120min by dispersion at 800-.

Step 4: and (3) conveying the slurry in the step (3) to an impeller type high-speed mixer with the rotating speed of 5000r/min by adopting a screw according to a fixed flow, and pumping the slurry into a circulation tank A after mixing for 30-60 min.

And 5: and (3) in the circulation tank A, starting stirring for 10-15r/min, keeping the vacuum degree at-80 kPa, slowly stirring, vacuumizing for 30min, and testing the viscosity, the fineness and the solid content of the slurry.