uccs battery disassembly project poster

1
Physical and Electrochemical Parameter Measurements on Commercial Lithium-Ion Cells KEVIN WESTHOFF, TREVOR VERNON, EVERETT JACKSON, DR. AMY PRIETO, DR. TODD BANDHAUER DEPARTMENT OF MECHANICAL ENGINEERING COLORADO STATE UNIVERSITY , FORT COLLINS, CO PROJECT SUMMARY Five commercial lithium-ion batteries (LIB) were disassembled and analyzed for specific physical and electrochemical parameters. Cell disassembly was completed in an Argon glove box. Detailed measurements were performed on the physical construction of the batteries with the goal of determining the volume of active material in each electrode. The open circuit potential (OCP) as a function of temperature and state of charge (SOC) for the cathode and anode active materials versus Li/Li + was measured. These tests used ¾” half-cells cycled at a C/30 rate on an Arbin battery tester while under strict environmental temperature control. The diffusion coefficient of Li + as a function of temperature and SOC in the active materials was measured using the Galvanostatic Intermittent Titration Technique (GITT). Nuclear Magnetic Resonance Spectroscopy (NMR) was used to determine the composition of the electrolyte, if enough of an electrolyte sample was harvested during cell disassembly. Extensive Scanning Electron Microscope (SEM) imaging was performed on the electrodes to determine the coating thickness and active material particle size. Additionally, Energy Dispersive Spectroscopy (EDS) was performed on all electrode samples to determine the elemental composition of the active materials. This data was then coupled with X-Ray Diffraction (XRD) crystallographic data to produce an equivalent unit cell of the active material in order to determine the theoretical lithium storage capacity. The composite electrode electronic conductivity was also determined as a function of temperature with a Gamry Reference 3000 Potentiostat. BACKGROUND AND RATIONALE 1 Battery Management Systems (BMS) are an essential part of implementing a LIB pack. These systems contain the control logic that is used for managing the energy contained within a battery pack to power auxiliary components, such as an electric motor. More specifically, BMS monitor the present status of the battery pack by determining the state-of-charge, state-of-health, state-of-life, available energy, and available power. By accurately monitoring these values, BMS can be designed to maximize the amount of energy delivered while maintaining the health and longevity of the battery pack. Current BMS employ equivalent-circuit models in their algorithms to determine the present status of a battery pack. These simple, empirically-based models are robust; however, they fail to provide insight into the electrochemical dynamics that occur internal to the cell during operation. To improve the fidelity of current BMS and ultimately improve the utilization of LIBs in all applications, physics-based models must be used. Physics-based LIB models are comprised of several coupled partial-differential equations (PDE) that describe the physical phenomena and electrochemical reactions within the battery that ultimately provide the realizable power. Paramount to physics-based models are the physical and electrochemical parameters of the battery materials, as they provide the boundary conditions to these PDE. This project seeks to provide accurate physical and electrochemical parameter measurements to be used in physics-based LIB models for the next generation of BMS. These physical and electrochemical parameter measurements are made on five commercially manufactured LIBs with varying capacities, chemistries, and applications. 1. J. L. Lee, A. Chemistruck and G. L. Plett, Journal of Power Sources, 220, 430 (2012). OBJECTIVES The physical and electrochemical parameters measured in this project are: 1. Number of positive and negative electrodes in each cell 2. Active material volume in each electrode 3. Thickness of separator 4. OCP of each electrode vs. Li/Li + at 15, 25, and 35°C 5. SEM images of positive and negative electrode active material particles (with scale) 6. SEM images of clean separator (with scale) 7. NMR analysis of electrolyte (if an electrolyte sample is harvested during disassembly) 8. Composite electrode electronic conductivity at 15, 25, and 35°C 9. Maximum lithium storage capacity of active materials in each electrode 10. Diffusion coefficient of li-ions in each electrode as a function of SOC at 15, 25, and 35°C COMMERCIAL CELLS STUDIED C OMMERCIAL LITHIUM-ION B ATTERY DISASSEMBLY AND ANALYSIS PROJECT COLLABORATORS Dr. Gregory Plett Dr. Scott Trimboli Department of Electrical and Computer Engineering University of Colorado, Colorado Springs CELL DISASSEMBLY CELL A CELL D Peeling back the vacuum sealed pouch Separating the thin layers of stacked electrode structure Removing a cathode sample Peeling back steel casing Separating unit jelly rolls from the primary jelly roll Unwinding unit jelly roll HALF CELL CONSTRUCTION FOR OCP AND GITT TESTING Removing one side of electrode material; punching a ¾” sample (anode sample shown) Stacking structure for half cell construction Completed half cell; PFA compression fitting is used for the body of the cell SEM IMAGES OF CATHODE SEM IMAGES OF ANODE Note: All anode samples are graphite Note: Refer to table for chemistry of each cathode sample PHYSICAL MEASUREMENTS SEM IMAGES OF SEPARATOR Cell E Cell A OCP TESTING RESULTS OCP data: C/30 Lithiation at 25°C GITT TESTING RESULTS GITT data: Cell E Cathode (Top) Anode (Bottom) EDS of Cell E Cathode XRD of Cell E Cathode Unit Cell & SEM Image of Cell E Cathode Active Material Particle EDS/XRD D ATA TO DETERMINE CRYSTAL STRUCTURE NMR OF CELL E ELECTROLYTE Each peak (rise in counts) in the spectrum corresponds to a particular solvent molecule Integrating the counts for the entire spectrum gives relative ratios of the different solvents Electrolyte Composition Result: 5:4:1—Dimethyl Carbonate: Ethylene Carbonate: Diethyl Carbonate SEM IMAGES OF AL 2 O 3 COATINGS Pictured: Cell E Anode. Al 2 O 3 coatings were also observed on Cell B, C, & D Sample was coated with 10 nm of gold Unit Cell and SEM Image of LiFePO 4 (Cell D) Unit Cell and SEM Image of LiMnO 2 (Cell C)

Upload: kevin-westhoff

Post on 17-Aug-2015

39 views

Category:

Documents


1 download

TRANSCRIPT

Physical and Electrochemical Parameter Measurements on Commercial Lithium-Ion Cells

KEVIN WESTHOFF, TREVOR VERNON, EVERETT JACKSON, DR. AMY PRIETO, DR. TODD BANDHAUER

DEPARTMENT OF MECHANICAL ENGINEERING

COLORADO STATE UNIVERSITY, FORT COLLINS, CO

PROJECT SUMMARY Five commercial lithium-ion batteries (LIB) were disassembled and analyzed for specific physical and

electrochemical parameters. Cell disassembly was completed in an Argon glove box. Detailed

measurements were performed on the physical construction of the batteries with the goal of determining

the volume of active material in each electrode. The open circuit potential (OCP) as a function of

temperature and state of charge (SOC) for the cathode and anode active materials versus Li/Li+ was

measured. These tests used ¾” half-cells cycled at a C/30 rate on an Arbin battery tester while under strict

environmental temperature control. The diffusion coefficient of Li+ as a function of temperature and SOC in

the active materials was measured using the Galvanostatic Intermittent Titration Technique (GITT). Nuclear

Magnetic Resonance Spectroscopy (NMR) was used to determine the composition of the electrolyte, if

enough of an electrolyte sample was harvested during cell disassembly. Extensive Scanning Electron

Microscope (SEM) imaging was performed on the electrodes to determine the coating thickness and active

material particle size. Additionally, Energy Dispersive Spectroscopy (EDS) was performed on all electrode

samples to determine the elemental composition of the active materials. This data was then coupled with

X-Ray Diffraction (XRD) crystallographic data to produce an equivalent unit cell of the active material in

order to determine the theoretical lithium storage capacity. The composite electrode electronic

conductivity was also determined as a function of temperature with a Gamry Reference 3000 Potentiostat.

BACKGROUND AND RATIONALE1

Battery Management Systems (BMS) are an essential part of implementing a LIB pack. These systems contain the control logic that is used for managing the energy contained within a battery pack to power auxiliary components, such as an electric motor. More specifically, BMS monitor the present status of the battery pack by determining the state-of-charge, state-of-health, state-of-life, available energy, and available power. By accurately monitoring these values, BMS can be designed to maximize the amount of energy delivered while maintaining the health and longevity of the battery pack. Current BMS employ equivalent-circuit models in their algorithms to determine the present status of a battery pack. These simple, empirically-based models are robust; however, they fail to provide insight into the electrochemical dynamics that occur internal to the cell during operation. To improve the fidelity of current BMS and ultimately improve the utilization of LIBs in all applications, physics-based models must be used. Physics-based LIB models are comprised of several coupled partial-differential equations (PDE) that describe the physical phenomena and electrochemical reactions within the battery that ultimately provide the realizable power. Paramount to physics-based models are the physical and electrochemical parameters of the battery materials, as they provide the boundary conditions to these PDE. This project seeks to provide accurate physical and electrochemical parameter measurements to be used in physics-based LIB models for the next generation of BMS. These physical and electrochemical parameter measurements are made on five commercially manufactured LIBs with varying capacities, chemistries, and applications. 1. J. L. Lee, A. Chemistruck and G. L. Plett, Journal of Power Sources, 220, 430 (2012). OBJECTIVES The physical and electrochemical parameters measured in this project are: 1. Number of positive and negative electrodes in each cell 2. Active material volume in each electrode 3. Thickness of separator 4. OCP of each electrode vs. Li/Li+ at 15, 25, and 35°C 5. SEM images of positive and negative electrode active material particles (with scale) 6. SEM images of clean separator (with scale) 7. NMR analysis of electrolyte (if an electrolyte sample is harvested during disassembly) 8. Composite electrode electronic conductivity at 15, 25, and 35°C 9. Maximum lithium storage capacity of active materials in each electrode 10. Diffusion coefficient of li-ions in each electrode as a function of SOC at 15, 25, and 35°C

COMMERCIAL CELLS STUDIED COMMERCIAL LITHIUM-ION BATTERY DISASSEMBLY AND ANALYSIS

PROJECT COLLABORATORS Dr. Gregory Plett Dr. Scott Trimboli Department of Electrical and Computer Engineering University of Colorado, Colorado Springs

CELL DISASSEMBLY

CELL A

CELL D

Peeling back the vacuum sealed pouch Separating the thin layers of stacked electrode structure

Removing a cathode sample

Peeling back steel casing Separating unit jelly rolls from the primary jelly roll

Unwinding unit jelly roll

HALF CELL CONSTRUCTION FOR OCP AND GITT TESTING

Removing one side of electrode material; punching a ¾” sample

(anode sample shown) Stacking structure for half cell construction

Completed half cell; PFA compression fitting is used for the body of the cell

SEM IMAGES OF CATHODE SEM IMAGES OF ANODE

Note: All anode samples are graphite Note: Refer to table for chemistry of each cathode sample

PHYSICAL MEASUREMENTS

SEM IMAGES OF SEPARATOR Cell E

Cell A

OCP TESTING RESULTS

OCP data: C/30 Lithiation at 25°C

GITT TESTING RESULTS

GITT data: Cell E Cathode (Top) Anode (Bottom)

EDS of Cell E Cathode XRD of Cell E Cathode Unit Cell & SEM Image of Cell E Cathode Active Material Particle

EDS/XRD DATA TO DETERMINE CRYSTAL STRUCTURE

NMR OF CELL E ELECTROLYTE

• Each peak (rise in counts) in the spectrum corresponds to a particular solvent molecule

• Integrating the counts for the entire spectrum gives relative ratios of the different solvents

• Electrolyte Composition Result: 5:4:1—Dimethyl Carbonate: Ethylene Carbonate: Diethyl Carbonate

SEM IMAGES OF AL2O3 COATINGS

Pictured: Cell E Anode. Al2O3 coatings were also observed on Cell B, C, & D

Sample was coated with 10 nm of gold

Unit Cell and SEM Image of LiFePO4 (Cell D) Unit Cell and SEM Image of LiMnO2 (Cell C)