19th POWERON ��9-11-2025, Ghaziabad, Delhi��High Life Lead-Acid Battery – �A true game changer in e-rickshaw Applications��Dr.Nanjan Sugumaran��International Battery Consultant�nanjans@hotmail.com�mob: 9412084170
eV – Field Status | ||
Category | Successfully implemented Nations | Technology |
2W | China | Lead-Acid ( VRLA) – 60% / LFP – 40% |
3W | India/Bangladesh/Nepal/China | Flooded Tubular Battery- 95%/ LFP – 5% |
4W | China | NMC/NCA/LFP |
Lead vs Lithium (3W eV) - Reality check for Atmanirbhar product ( Indian context) | |||
S.no | Parameters | Lead-Acid | Lithium |
1 | Local Manufacturing | Yes | Only Assembly/ Not Cell manufacturing |
2 | Local Material | Yes | Imported |
3 | Technology suitable to local eco system | Yes | Capital Expensive/ Not MSME friendly |
4 | Material shall be 100% recyclable | Yes | Not possible at present |
5 | Affordable to local eco system | Yes | 3 times Costly |
6 | Product shall be suitable to local eco system | Yes | LFP is safe and NMC is prone to fire |
7 | Consistency in quality | Low | Good |
8 | Life of Battery | Low | Good |
LFP in e-Rickshaw protocol (28+/- 3C) |
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Benchmark target for LFP and Lead-Acid in e-Rickshaw protocol | ||
S.No | Factors | Bench Mark |
1 | Total No. of cycles for LFP battery in laboratory | 1300 cycles |
2 | Failure modes | SEI growth/ Lithium electro plating on anode |
3 | Realistic life in the field ( Hot summer/ Cold winter) | 900 cycles |
4 | Lead-Acid Battery – 400 cycles | Red carpet to LFP. Lead Acid will be out from the market |
5 | Lead – Acid Battery – 400 to 600 cycles | LFP/LA can co-exist |
6 | Lead – Acid Battery – 600 to 900 cycles | LA will dominate |
9 | Lead – Acid Battery > 900 cycles | LFP will be out from the market |
Reasons for 3W eV Lead acid battery failure vs Life in the field | |||||
Failure Modes | 0 to 6 months | 6 to 12 months | 12 to 18 months | 18 to 24 months | 24 to 36 months |
Manufacturing Defects | | | | | |
Positive plate Defect | | | | | |
Separator related failures | | | | | |
Gauntlet related failures | | | | | |
Inconsistency between the cells | | | |||
Positive active material shedding | | | |||
Positive spine corrosion | | | |||
Negative plate failure | | | |||
Manufacturing Defects | |||
Type of Failure | Section | Type of Defects | What to attack |
1) Manufacturing Defects | Assembly/ Group Burning section | Lead run down | 1) Tool design 2) Operator’s skill |
Plate disconnect | |||
Lead piece | |||
2) Positive plate Defect | Tube filling | Empty tube | 1) Oxide nature/quality 2) Machine capability 3) Gauntlet quality |
Tube loose | |||
3) Separator related failures | Component/ Assembly | Separator puncture | Assembly/Enveloping/ plate design/plate handling |
Separator Brittleness | Separator quality/Design | ||
4) Gauntlet related failure | Component/Tube filling | Gauntlet bursting | Gauntlet quality – Nature of yarn, resin content, resin quality |
Gauntlet damage | Plate handling | ||
PAM leaching | Pore size and uniform distribution | ||
5) Importance of Consistency | |||||||||||||||||||||||||||
1 | Typical e Rickshaw battery systems: 48V/100 Ah, 48V/120 Ah, 48V/150 Ah, 60V/120 Ah, 60V/150 Ah | ||||||||||||||||||||||||||
2 | A 48V system comprises 4 batteries in series. Each battery comprises of 6 cells. Hence, 24 cells are in series | ||||||||||||||||||||||||||
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Battery – 1 (12V) | | Battery – 2 (12V) | | Battery – 3 (12V) | | Battery – 4 (12V) | |||||||||||||||||||||
1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | 10 | 11 | 12 | 13 | 14 | 15 | 16 | 17 | 18 | 19 | 20 | 21 | 22 | 23 | 24 | ||||
+ | - | + | - | + | - | + | - | + | - | + | - | | + | - | + | - | + | - | + | - | + | - | + | - | |||
- | + | - | + | - | + | | - | + | - | + | - | + | | - | + | - | + | - | + | | - | + | - | + | - | + | |
- | Battery Bank – ( 48V) | + | |||||||||||||||||||||||||
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3 | Since 24 cells are in series, the lowest performer (lowest capacity) will determine system behaviour. | ||||||||||||||||||||||||||
4 | Capacity of cell is in turn related to weight of the plates | ||||||||||||||||||||||||||
5 | Variation in plate weight, or inconsistency in group weight, is one of the major reason for failure of battery | ||||||||||||||||||||||||||
5) Importance of consistency - Reasons for Negative Plate Weight Variation | |
1 | Machine capability of pasting machine ( Machine, type of belt, usage of belt) |
2 | Variation of negative paste density over the pasting duration; the pasting process lasts 45-60 mins, during which time density, moisture, and “pasteability” change. Material which can retain proper moisture during this period will improve consistency. |
3 | Is it possible to have the cured plate weight variation +/- 5 grams or even lower |
4 | Suppose if the process capability is +/- 8 grams and by other statistical tools how to bring down to +/- 3 grams |
5) Importance of Consistency - Reasons for Positive Plate Weight Variation | |
1 | Capability of tubular gauntlet filling machine ( Dry, Slurry, Paste filling) |
2 | Variation of tap density of blended oxide; most manufacturers buy oxide from multiple vendors, but controlling tap density of a blend is a major challenge. |
3 | Barton and Ball mill oxides are having different flow characteristics. Red lead% and oxide type will alter the consistency |
4 | Is it possible to have the tubular plate weight variation +/- 5 grams, or lower, without manual intervention? |
5 | Manual intervention / rework shall be avoided; this results in another type of failure mode due to density variation which is detrimental to life of battery |
6 | Suppose if the process capability is +/- 20 grams and by other statistical tools how to bring down to +/- 5 grams |
5) Importance of Consistency - How to Reduce the Variation in Performance | ||
S.No | Methodology | Practical implication |
1 | Built a new factory with very expensive machines | Commercially not feasible. Lithium industry adopted this approach because they started from scratch. |
2 | Segregate plates, and make batteries of various grades | Huge complication in manufacturing and will be a manufacturing nightmare |
3 | Segregate batteries based on capacity and grade the batteries | Reduces plant output, and also a manufacturing nightmare. In addition, it will be another nightmare from sales point of view. Lithium is doing this and hence plenty of spurious cells in the market |
4 | Reject/rework the plates falling out of specification | Reduces plant capacity and increases cost of manufacturing. |
5 | Use statistical tool/methodology | Will reduce variation to an order of 75% with minimal effort |
6) Positive Active Material Shedding | |||
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| Beginning | During operation | End of Life |
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Journal of Energy Storage - Sugumaran, Paul Everill, 78, p 110048, 2024
PAM
High Faradic Capacitance (HFC) Material
HFC-Active
Will disintegrate
HFC - Passive
Buffer to HFC Active/Become Inactive
Low Faradic Capacitance (LFC) Material
LFC - Active
A slight disintegration
LFC - Passive
Remains intact
6) Positive Active Material Shedding -How to Identify the Two Types of PAM having different electrochemical activity | |
Present analysis | Modified Analysis |
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55% HFC
45% LFC
Journal of Energy Storage - Sugumaran, Paul Everill, 78, p 110048, 2024
Feature 1 (HFC)
Feature 2 (LFC)
Feature 1 (HFC)
Feature 2 (LFC)
6) Positive Active Material Shedding | ||
1 | Delaying the disintegration of HFC active material and increasing buffer capacity duration | Add suitable PAM additive - 1 |
Optimise pack density | ||
Improve oxide purity | ||
2 | Keep HFC passive material stable for long duration so that the buffer capability is more | Add suitable PAM additive -2 |
Select proper positive alloy | ||
Optimise pack density | ||
3 | Altering ratio of HFC to LFC | PAM/NAM ratio |
(PAM+NAM)/Acid ratio | ||
Red lead/ Total oxide ratio, Oxide type | ||
Oxide particle size | ||
Charging methodology | ||
7) Positive Spine Corrosion |
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Positive Spine Corrosion – Sb alloy
Uniform corrosion vs Grain boundary corrosion
Grain refiner % in the alloy and distribution pattern in the alloy matrix
Spine Casting conditions
8) Negative Plate Failure: Sulphate Build-Up | ||
1 hr | 2 hrs | 3 hrs |
4 hrs | 5 hrs | 6 hrs |
7 hrs | 8 hrs | 9hrs |
10 hrs | Due to the ON/OFF nature of the e-Rickshaw operation duty cycle, the negative plate is unable to fully recharge and always will have variety of non-uniform PbSO4 crystals with different charge acceptance tendency | |
8) Negative plate Failure - Impact of Carbon During Overcharging in NAM |
Carbon – Hydrogen atom storage capability (H2O splitter) | Electrolysis of H2O to H2 and O2 leading to water Loss | 2 H+ + 2 e- H2 | Overall |
H+ + e- Had (RDS) | Volmer (Lead) | ||
Had + Had H2 | |||
H+ + e- Had | Heyrovsky (Carbon) | ||
Had + H+ + e- H2 (RDS) | |||
H+ + e- Had | Tafel (Platinum) | ||
Had + Had H2 (RDS) |
8) Negative plate Failure - How Atomic Hydrogen Prevent Lead sulphate formation |
| During overcharging Heyrovsky additives and dCNT generates plenty of nascent Hydrogen atom. Hydrogen is captured in dCNT due to intercalation |
During rest period after charging, the stored hydrogen acts as a capacitor. The chemically formed PbSO4 acts as a resistor in parallel. Internal shorting between Capacitor and Resistor results in reduction of PbSO4 | |
PbSO4 + 2Had Pb + H2SO4 | |
Additives having highest hydrogen atom storage capacity will effectively convert all PbSO4 in to Pb | |
dCNT due to its discrete nature has the highest hydrogen storage capacity and hence good PbSO4 recovery capability |
( stored hydrogen)
( PbSO4)
8) Negative plate Failure -Stable Crystal Structure in Solar/eRickshaw Cycles: | |
Standard Carbon | With dCNT added to NAM (Sulphate Inhibitor) |
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Long life e-rickshaw Lead-acid Battery – Game changer |
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Is it possible to develop e-ricksha Battery with more than 1000 cycles in e-rickshaw protocol
Yes
All the failure modes shall be properly addressed
Long life Lead-Acid Battery is a real game changer
Conclusions | |
Positive plate Improvements | Optimise Type-A and Type-B behaviour using design and process methodology. Fix the Sanskar/DNA of a Battery |
Use proper positive plate additives and alloy to strengthen Type-A active material from disintegration and improve the buffer capability when not in use | |
Use appropriate raw materials in proper ratio and fix the sanskar of a battery | |
Revisit battery design | |
Use appropriate SG of acid to maintain higher % of Type-B active material | |
Negative plate Improvements | Use Carbon/dCNT in a proper way along with proper expander to reduce sulphation and minimise water loss |
Consistency in Battery/Cells | Maintain paste density of Negative paste through the pasting duration with special additive |
Improve machine capability of pasting machine | |
Maintain tap density of blended oxide 24/7 duration in tube filling operation | |
Improve machine capability of tube filling machine | |
Use advanced statistical tools to reduce variation (+/- 3 g for NAM, +/5 g for PAM) | |
Conclusions | |
Manufacturing Defects | Adopt good manufacturing practices such as good tools/fixtures and have a good work force |
Good quality positive plate | Have positive plate free from empty tube/Loose tube- Good quality oxide and good quality tube filling machine will ensure this |
Separator related failures | A good quality separator in resonace with proper enveloping machine/ Assembly operation/ proper plate design/plate handling methodology will ensure this |
Gauntlet related Failures | Gauntlet quality – Proper yarn, resin content and resin quality along with proper assembly operation will ensure this |
Spine corrosion | Optimise spine casting conditions. Select proper alloy and grain refiner in such a way that the corrosion is uniform instead of grain boundary pattern. Use appropriate spine thickness and spine design. |