Skip to main content

Lithium-ion Full Cell Manufacturing Process Training--Cathode Electrode Materials Section

1.Battery structure

1.1.Commonly used battery structures

 

 

Pouch battery    Aluminum shell battery  Cylindrical batteries         Coin cell


 

1.2.Internal structure - Pouch battery

 

1.2.1.Winding structure

 

1.2.2.Laminated structure

2.Cell size

2.1.Pouch battery model:425868

 

3.Design principles

3.1.Electrode Size

 

3.1.1.Margin of Width:

Negative electrode width-positive electrode width≥1.5mm(C1+C2)

Separator width - negative electrode width≥1.5mm(S1+S2)

 

3.1.2.Length Surplus:

Negative Electrode Length-Positive Electrode Length≥2.0mm(A1+A2)

Separator width - negative electrode width≥5.0mm(B1+B2)

3.2.N/P ratio

3.2.1.N/P =anode reversible capacity/cathode reversible capacity

3.2.2.=Negative electrode delithium capacity (charging during deduction) / Positive electrode lithium intercalation capacity (discharging during deduction)

 

3.2.3.1st C.E.=Reversible Capacity / (Reversible + Irreversible) Capacity

3.2.4. =De-lithiation Capacity of the Negative Electrode / Lithiation Capacity of the Negative Electrode

3.2.5. =Lithiation Capacity of the Positive Electrode / De-lithiation Capacity of the Positive Electrode

 

3.2.6.The negative electrode lithium intercalation capacity/positive electrode lithium delithium capacity is more practical, and only >1 can theoretically ensure that there is no problem of lithium separation

 
 

3.2.7.Therefore, conventional lithium cobalt oxide and lithium iron can match the N/P value of graphite material 1.08~1.12

3.2.8.The N/P value of ternary materials with low initial efficiency matching graphite materials needs to be increased to 1.15~1.20, because (the first effect of the positive electrode/the first effective value of the negative electrode) is obviously low

3.2.9.The N/P value of conventional lithium cobalt oxide and lithium iron matched silicon carbon 550 can be reduced by 1.06 because the first efficiency of silicon carbon 550 is low

 
 

3.3.Charge-discharge interva

3.3.1.Design principles of charge and discharge voltage range:

3.3.2.(1) The charge and discharge capacity should be accurate (convenient to

accurately calculate the capacity of the positive and negative electrodes by

coating weight)

3.3.3.(2) Within the charging and discharging voltage window, the positive and negative

electrode capacities are basically exerted

3.3.4.The capacity of the positive electrode 3.0~3.6V interval and the negative electrode

0.6~1.5V interval is very small

3.3.5.(3) Whole cell voltage = positive potential - negative potential

3.3.6.The positive electrode is 3.0~4.45V, the negative electrode is 0.005~1.5V

3.3.7.Therefore, the conventional lithium cobalt oxide capacity is set at 3.0~4.45V

(3.0=3.6-0.6)

3.4.Three-electrode test

 

3.5.Coating weight

3.5.1.Coating range: 7mg/cm2< cathode coating weight<25mg/cm2 (ternary, lithium

cobalt oxide empirical value)

3.5.2.If the coating surface density is too low, the equipment has limitations and coating

leakage may occur. If the surface density is too high (commonly known as thick coating),

the kinetic performance will be deteriorated, leading to poorer battery performance

(such as cycle life, rate capability, etc.).

 

3.6.Tabs

3.6.1.Tab design principles:

3.6.2.Capacity<1Ah, tab size 2mm*0.08mm (width * thickness)

3.6.3.1Ah< capacity <3Ah, tab size 4mm*0.08mm

3.6.4.3Ah< capacity <5Ah, tab size 6mm*0.1mm

3.6.5.5Ah< capacity <8Ah, tab size 6mm*0.15mm

3.6.6.Capacity>8Ah, tab size widened, thickness 0.2mm

 
 

3.7.Others

3.7.1.Other materials, such as foil, aluminum-plastic film and separator, etc., are

selected according to the application, if only an experiment, recommended foil

material:

copper foil ≥ 8um, aluminum foil ≥ 14um, aluminum-plastic film: ≥113um, separator≥

12um.

3.7.2.If it is a high energy density requirement, a thinner one can be considered, but

this material requires high process capacity, otherwise will sacrificed the yield.

    
 

Foil material            Aluminum-plastic film             Separator

 

 

4.Canrd Brief Introduce

Canrd use high battery R&D technology(core members are from CATL) and strong Chinese supply chain to help many foreign companies with fast R&D.    We provide lab materials, electrodes, custom dry cells, material evaluation, perfomance and test, coin/pouch/cylindrical cell equipment line, and other R&D services.

 

Email: contact@canrd.com    Phone/Wechat/WhatsApp: +86 19867737979

Canrd Official Web     Canrd Company Vedio     Canrd Company profile

Website : www.canrud.com

 

Comments

Popular posts from this blog

Lithium-ion Full Battery Manufacturing Process Training

Lithium-ion Full Battery Manufacturing Process Training 1. Basic Knowlege Of Mixing Slurry mixing is the process of adding active materials, conductive carbon black, dispersants, binders, additives, and other components to a mixing equipment in a certain proportion and order. Under the mechanical actions such as turning, kneading, and shearing generated by the equipment, these components are mixed together to form a uniform, stable solid-liquid suspension system suitable for coating.The goal is to achieve uniformity and consistency on both the macro and micro levels.

Lithium-ion Full Cell Manufacturing Process Training--Soft-Pack Battery Formation - Part 2

1.  Key Factors Influencing Formation: Mechanism Generation Process of SEI Membrane: l  Electrons are transferred from the current collector, through the conductive agent, to point A inside the graphite particles where the SEI membrane is to be formed. l  Solvated lithium ions, wrapped in the solvent, diffuse from the cathode to point B on the surface of the SEI membrane that is currently being formed. l  The electrons at point A diffuse to point B through the electron tunneling effect. l  The electrons that jump to point B react with lithium salt, solvated lithium ions, film-forming agents, etc., to continue generating the SEI membrane on the surface of the existing SEI membrane. This process results in the continuous increase of the SEI membrane thickness on the surface of the graphite particles, ultimately leading to the formation of a complete SEI membrane.

Lithium-ion Full Battery Manufacturing Process Training--Coating

  1. Coating Basics Purpose: To uniformly coat a fluid slurry onto the surface of a metal foil, dry it, and produce a battery electrode Principle: The coating roller rotates to carry the slurry, and the amount of slurry transferred is adjusted by adjusting the gap between the doctor blade and the roller. The relative rotation of the back roller and the coating roller is used to transfer the slurry onto the substrate. Subsequently, the solvent in the slurry is evaporated through drying and heating, causing the solid matter to adhere to the substrate.