10.batteries & management · 2020-04-11 · lund university / lth / iea / avo reinap / mvkf25 /...
TRANSCRIPT
09-APR-2020MVKF25 Hydrogen, Batteries, Fuel Cells
10.Batteries & Management Balancing, BMS, TBMS States, degradation, models
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 2
L10: Batteries & Management•
Energy management
–
Battery management system–
Electric
and Thermal
management
•
Battery states –
Charge (SoC), Function (SoF), Health (SoH)
–
Performance deterioration
and battery degradation•
Battery characteristics and models
•
Charging
and discharging–
Charger, rechargeable battery, Li-ion Battery
–
Self-discharge
W
W
W
W
W W
W W
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 3
Guide•
Battery characteristics
and model
(Ch 1 & 2)–
Cell components
–
Electrochemical energy conversion
–
Performance characteristics
–
Electrochemical analysis methods
•
Battery control
and management
(Ch 6 & 6)
–
Energy management–
State functions
•
Battery usage
and degradation
(Ch 7)
–
Degradation mechanisms–
Degradation of Li-ion cells
–
Degradation analysis
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 4
Value chain for EV batteries
•
Not only energy management but also material usage/reusage
•
From cell realization to recycling (excluding raw materials)
•
Vehicle power (performance), energy (range) and integration (BMS)
Fig.Ref.: B. Averill, P. Eldredge, “General Chemistry: Principles, Patterns and Applications”
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 5
Energy Management vs Design
•
A cross-road of different disciplines•
Multi-dimensional (analysis) & multi-
objective (synthesis)
Construction Production
Energy Conversion
kg kW, kWh
Pack specificationPack architecture
Pack designElectrical power system
Module designElectrical distribution system
System safetyBMS design
Module CU
CELL
•Joining methods
and E, M, T criteria?
Information
Energy•
Monitoring –
measure what
is important•
Control –
keep it optimal and
constrained•
Diagnosis –
keep battery
cells healthy
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 6
Thermal
energy
management -
TBMS•
.J. Li, Z. Zhu, “Battery Thermal Management Systems of Electric Vehicles”, MSc Chalmers 2014
•
29.5/17.7 kWh
&1700/270 kg
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 7
dtdC
RE
EEEEEdtd
thambth
losses
outputinputlossesgenerationonaccumulati
1
Battery : store energy and use it ;)
CH
AR
GE
DISC
HA
RG
E
Voltage [V]
Energy [Ah]
Current [A]
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 8
Battery overview•
Parameters (of primary interest)
–
Voltage, E [V]–
Capacity, Q [Ah]
•
Models & approaches–
Mathematical: chemical process kinetics & Markov process based stochastic model
–
Electrochemical: physics based set of coupled partial differential equations connecting laws related to chemical concentration and electric current flow
–
Single particle model–
Equivalent circuit: Electric circuit consisting of RCE
Ageing modelThermal model
Electrical model
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 9
Voltage and Capacity•
Electric operation domain
–
Voltage range –
Vmin
-Vmax
–
State of Charge –
SOC•
Depth of discharge DOD=100%-SOC
–
Voltage range –
min
-max
•
Open circuit voltage OCV(SOC, )
•
Internal resistance R(SOC,I,) results voltage drop and power losses
Voltage [V]
Capacity [Ah]
Vmax
VminQmin
Qmax
%100nomQtQtSOC
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 10
More voltage and more capacity•
Series → increase voltage
•
Cells in parallel → increase capacity → unequal voltage drives current
•
The largest safely drawn charge is the one that is stored in the weakest cell
•
Purpose of BMS–
Indentify state of charge SOC
–
Maximize capacity –
Provide safe function
Voltage [V]
Capacity [Ah]
BM
S
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 11
Battery control and BMS•
Energy management
–
Electric
operation range
– energy
balancing
for
better
usage–
Thermal
operation range
–
Keep temperature & use little energy for operation
•
Battery cell-module-pack development and control is supported buy models
–
From models in physics (FEM) towards datasheet and equivalent circuit modeling
–
from
component physics towards system realisation
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 12
Battery modeling A•
Simple approach @ limited data, parameters are independent of SOC, current
(rate) and
temperature•
Cell voltage
U=Eo
-Ro
I where Ro
is internal resistance and Eo
is open circuit voltage (OCV)
•
Heating power Ploss
=(Ro
I)2
only
Ohmic
losses•
Transient temperature
rise
=Ploss
Rh
(1-e-t/RhC
h
)
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 13
Battery modelling B
Heat generation
model
Cell Electrical
model
Cell Thermal model
VtVoc
SoC
I* ϑa
Qϑ
•
Simulink SimPowerSystem
•
Generic
dynamic model
•
Pre
characterised charging/discharging
characteristics
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 14
Electric equivalent circuit
•
Electrolyte resistance –
causes resistive voltage drop at current flow
•
Diffusion and surface reaction –
results the voltage transient(s) at current step
R1
C1
R2
C2
R0
E=Uoc(Vsoc)
Ccap
Rsdc
Ibat Ibat
VsocBattery Lifetime
Voltage-Current Characteristics
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 15
Step response
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 16
Frequency response
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 17
Electrochemical force and cell
•
Chemical reaction = two half-reactions: oxidation+reduction=redox
–
Side reactions due to thermal loads, pressure?
•
Active, electrodes, non-active, the rest including electrolyte, components
B. Averill, P. Eldredge, “General Chemistry: Principles, Patterns and Applications”
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 18
Principles, definitions, realizationsLEFT:
Negative electrode
RIGHT:Positive electrode
OxRedln0 nF
RTEEEE leftrightcell
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 19
Keywords to previous slide•
Electrochemical energy conversion
–
Ch → E: Galvanic, Oxidation → loss of electrons → discharging
–
E → Ch: Electrolytic, Reduction → gain of electrons → charging
•
Nernst equation•
Electrode domain
–
μm-scale
•
From left to right = negative electrode positive electrode and boundaries for different domains in between
CH 1 : The electrochemical cell
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 20
Energy and power•
Specific energy originates from material chemistry
–
Capacity capability
•
Specific power is related to material physics and production
–
Internal power losses and thermal constrains –
durability and safety
p. 40 & 129
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 21
Cell voltage
cell
negcctposcct
negposcell
iR
EEE
•
Activation polarization – charge transfer (ηct
) from electrode surface
•
Concentration polarization – caused by concentration (ηc
) differences between electrode and electrolyte due to ionic conductivity and transport properties
•
Ohmic
polarization –
IR drop proportional to current
p. 34
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 22
Voltage hysteresis
cha
disE
cha
disQ
t
t
dttItV
dttItV
dttIQ
tSOCtSOC
0
10
•
Charge-Discharge profile•
Delay in chemical and electrochemical reactions, causes difference between charging and discharging voltages
•
Voltage hysteresis, ΔE, may
increase
with charge
and discharge rate
p. 34
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 23
Charge and Discharge rates•
A C-rate is a measure of the rate at which a battery is discharged relative to its maximum capacity.
•
A 1C rate means that the discharge current will discharge the entire battery in 1 hour.
•
Practical capacity is defined as the current density passing through the cell until the cut-off voltage is reached
•
How C-rate affect cell performance
p. 37
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 24
Capacity
Ageing model
Electrical model
current Thermal model
power
temperaturevoltage
DoD SoH
•
Specific capacity [Ah/kg] of used electrochemical active material
•
Capacity fade due to loss of recyclable Lithium and SEI build up
p. 37 & 197
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 25
Cyclic voltammetry
•
Galvanostatic
cycling –
voltage response at constant current –
study the cell capacity and degradation
•
Potentiostatic
cycling –
holding voltage constant and decline the current
•
Cyclic voltametry
for electrode reaction response at linearly changed voltage resulting current peaks
W
1.7.2 & 7.3.3
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 26
Electrochemical impedance spectroscopy
•
Frequency response of battery•
Detect changes of the interfacial properties of the electrode –
charge transfer impedance (R||C)
W
1.7.3 & 7.3.2
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 27
EIS battery testing•
Electrochemical
dynamic
response–
Respons is related
to ion-
current/diffusion
rate in the cell–
Slower
response
for weaker
batteries
•
Characterization–
LF dubbed diffusion–
MF charge transfer–
HF migration
•
Batteries with faded capacity suffer from low charge transfer and slow active Li-ion diffusion.
http://batteryuniversity.com/learn/article/testing_lithium_based_batteries
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 28
Battery performance degradation
•
Degradation –
deterioration
of useful capacity and power capabilities
•
Identification of physical and chemical processes behind degradation mechanisms . Origins related to technology and usage.
•
SoH
–
state of health remaining capacity due to ageing
http://epg.eng.ox.ac.uk/content/degradation-lithium-ion-batteries
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 29
Battery failure
•
Safety=thermal stability
→Failure mechanisms–
External/internal –
internal short circuits–
Mechanical, electrical, thermal –
abusive conditions
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 30
Thermal runaway•
Failure propagation from cell to module and pack
•
Rapid temperature increase–
Most likely due to internal spontaneous short circuits due to impurities (that can grow during time as side effect of chemical reactions)
•
Avoid thermal runaway–
Overcharge/discharge protection activated by over pressure
–
Current interrupt device (CID)–
Positive temperature coefficient (PTC)
–
Separator specified for PTC & CID, layered separators for reducing internal short circuits
6.1.2.1
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 31
Energy and power demands•
Optimal performance and lifetime capacity
–
Power demand
vs energy
capacity–
Historic
use
and outlook
–
Energy capacity
and thermal
capability
6.1 vs
5.2
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 32
Charge and discharge control
•
maintain
the voltage
limits while
respecting
the current and temperature
limits
•
LOW Constant
current
charging
followed
by voltage and temperature
control
•
HIGH current
for constant
voltage
charging•
Combined
CV+CC
6.1.1
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 33
Cell balancing•
Voltage
equalization,
which
is to fill
up energy and maximize
capacity
and life by ”removing” unbalanced
weak
links
•
Active/passive
– taking/wasting
energy
W
6.2.1.4
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 34
What is a BMS really doing?•
www.youtube.com/watch?v=OG-UUXEOZ8E
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 35
BMS•
Cell protection, charge control, demand
management, SoC
and SoH
determination, cell
balancing, authentication and identification,
communication
–
are some
objectives
for BMS
http://www.mdpi.com/1996-1073/4/11/1840/htm
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 36
BMS development
•
Overall functional
safety
is better
match to global FPGA than
to local
micro
processor units
–
parallelism for performance with fail-safe logic
https://www.altera.com/solutions/industry/automotive/applications/electric-vehicles/battery-management-system.html
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 37
BMS control sequence
•
Intelligent batteries
due to base functions of a battery management system
http://mocha-java.uccs.edu/ideate/courses.html
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 38
BMS Failure recognitionhttp://www.mpoweruk.com/bms.htm
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 39
BMS implementation
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 40
BMS architectures for xEVs
•
Communication, reliability
and accuracy•
Practical
attachment, number
of components
and
connections•
Few
architectures
with different features in
connections
and communication
http://www.electronicproducts.com/Power_Products/Batteries_and_Fuel_Cells/Battery_management_architectures_for_H
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 41
Multicell Battery Stack Monitor
•
Component
name
LTC6802-1, Up to 12 cells, 13 ms measurement
interval, up to 1000V, passive cell
balancing
http://www.linear.com/product/LTC6802-1
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 42
BMS sensor module
MM9Z1 638 4-Cell Lithium Battery BMS unit•battery stack monitor IC can measure a number of cell voltages and provide for the discharge of individual cells to bring them into balance with the rest of the stack
http://www.nxp.com/products/automotive-products/energy-power-management/can-transceivers/reference-design-mm
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 43
Some future trends by Bosch
Lund University / LTH / IEA / Avo Reinap / MVKF25 / 2020-04-09 44
Useful links•
www.mpoweruk.com
•
www.Batteryuniversity.com•
www.liionbms.com/php/cells.php