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Oct 20, 2011 - The work presented here deals with the Advanced Battery, where carbon has been added to the negative acti
Carbon-Enhanced VRLA Batteries October 20th, 2011 David G. Enos, Summer R. Ferreira, Wes E. Baca Sandia National Laboratories Rod Shane East Penn Manufacturing

Sandia National Laboratories is a multi-program laboratory managed and operated by Sandia Corporation, a wholly owned subsidiary of Lockheed Martin Corporation, for the U.S. Department of Energy’s National Nuclear Security Administration under contract DE-AC04-94AL85000.

The Advanced VRLA Battery • Recently, there are several manners in which carbon has been added to a Pb-Acid battery  The work presented here deals with the Advanced Battery, where carbon has been added to the negative active material Advanced VRLA Battery PbO2

Pb

Lead-Acid Cell

Ultrabattery

PbO2

Carbon

Asymmetric Supercapacitor

PbO2 PbO2

Separator

Pb + C

Why add excess carbon to the NAM? • Carbon additions to the negative active material (NAM) can substantially reduce hard sulfation

 Fernandez, 2010*

Standard

Carbon Addition

*M.Fernandez, J.Valenciano, F.Trinidad, N. Munoz, Journal of Power Sources, Vol. 195 (2010), pp. 4458-4469.

Research Goals • The overall goal of this work is to quantitatively define the role that carbon plays in the electrochemistry of a VRLA battery.  What reactions/changes take place on the surface of the carbon particles?  What processes govern the increase and then eventual decrease in capacity with increasing # of cycles?  Are the kinetics of the charge/discharge process different when carbon is present vs. when it is not?  Why are some carbons effective additions while others are not? Are there any distinguishing characteristics of effective additions? Is the effectiveness controlled by aspects of the plate production method? etc.

Constituent Material Analysis • Given the limited understanding of what characteristics yield an effective carbon addition, a broad spectrum approach is being taken to quantify the carbon particle properties. Carbon Black

Graphite

Actetylene Black

Activated Carbon

20 nm

20+ µm

20 nm

100+ µm

75 m2/g

6 m2/g

75 m2/g

>2000 m2/g

Structure (XRD)

Semicrystalline

Crystalline

Semicrystalline

Amorphous

Acid Soluble Contamination

Clean

Clean

Very Clean

Na, PO4

Particle size Effective surface area (BET)

Performance Testing Shows Some Differentiation between Control and Carbon Modified Batteries 1.0

1.0

0.8

Cumulative Probability

0.8

Cumulative Probability

Impedance

Control Carbon Black + Graphite Acetylene Black Activated Carbon

Capacity

0.6

0.4

0.6

0.4

0.2

0.2

0.0 1950

0.0 9.5

10.0

10.5

11.0

11.5

12.0

12.5

2000

Capacity (Ah)

2100

2150

Alber Impedance ()

250

1.0

Float Current

Self Discharge

200

0.8

Cumulative Probability

Float Current (mA)

2050

150

100

50

0 2.26

0.6

0.4

0.2

2.28

2.30

2.32

2.34

2.36

2.38

Float Voltage (V)

2.40

2.42

2.44

2.46

0.0 0

10

20

30

6 Month Self Dischage (%)

40

Performance Testing Shows Similarities Between Control and Carbon Modified Batteries HPPC Discharge Capacity

HPPC Charge Capacity 320

300

300

260

Pulse Power Capacity (W)

Pulse Power Capacity (W)

280

240 220 200 180 160 Control Carbon Black + Graphite Acetylene Black Activated Carbon

140 120

280 260 240 220 200 180 160

100 0

20

40

60

Depth of Discharge (%)

80

100

0

20

40

60

Depth of Discharge (%)

Note: These HPPC data are for new cells

80

100

More Dramatic Differentiation Observed as the Batteries are Cycled • Comparable behavior observed for all four battery types at 1k cycles • At 10k cycles, capacity loss was evident in the control, acetylene black, and activated carbon batteries (but not in the carbon black + graphite cell) • Control battery failed at 11,292 cycles  Failure defined as a capacity loss of greater than 20% after three discharge/charge cycles in an attempt to recover.

Log Differential Intrusion (mL/g)

Porosity and Pore Size Distribution 0.30 0.25 0.20 0.15 0.10 0.05 0.00 0.01

Log Differential Intrusion (mL/g)

Raw

Control Carbon Black + Graphite Acetylene Black Activated Carbon

0.1

0.5

1

10

Pore Size Diameter (m)

100

Formed

0.4

0.3

0.2

0.1

0.0 0.01

0.1

1

Pore Size Diameter (m)

10

100

Log Differential Intrusion (mL/g)

0.6

Log Differential Intrusion (mL/g)

Porosity and Pore Size Distribution

0.6

0.5 0.4

1k Cycles

Control Carbon Black + Graphite Acetylene Black Activated Carbon

0.3 0.2 0.1 0.0 0.01

0.1

1

10

100

10k Cycles

Pore Size Diameter (m) 0.5 0.4 0.3 0.2 0.1 0.0 0.01

0.1

1

Pore Size Diameter (m)

10

100

Minimal Sulfation at 1k Cycles Control

Activated Carbon

Acetylene Black

Carbon Black + Graphite

100 microns

Significant Sulfation at 10k Cycles for Two of the Batteries Control

20% Capacity Loss

Acetylene Black

15% Capacity Loss

100 microns

Activated Carbon

15% Capacity Loss

Carbon Black + Graphite

4% Capacity Gain

250 microns

Summary/Conclusions to Date •

Battery performance  Pb-C batteries had lower initial capacity, higher initial internal resistance, higher float current, comparable HPPC performance, and superior HRPSoC cycling performance



Material Characterization  Pore structure in Pb-C batteries notably smaller (order of

magnitude), but comparable in overall volume  Hard sulfation becoming significant after 10k cycles with the control battery and activated carbon battery

Future Tasks • Cycle testing will continue  50k and 100k cycles  Cycle to end of life  Analysis of cycled battery materials

• Program will conclude in August 2012