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Fuel cell and battery hybrid system

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(1)

1

hybrid system

Naehyuck Chang

Dept. of EECS/CSE

Seoul National University

[email protected]

(2)

Motivation

Human portable applications

Light weight, small volume but longer operational life time

Low-power consumption

More energy density

Wearable computers

30W+ average and 70W+ peak power

Fuel cell: next generation power sources

High energy density

A Li-Ion battery pack (in cellular phones): 250 Wh/L

A methanol based fuel cell: 4780 Wh/L

A hydrogen based fuel cell (NaBH4): 7314 Wh/L

(3)

3

Fuel cell basics

Fuel cell

Electrochemical energy conversion device

An electrochemical device that directly converts chemical energy in fuels into electrical energy without combustion

Uses external supply of fuel and oxygen

Produces just a water as a byproduct

Advantages of Fuel cell

High energy density  longer lifetime for same weight/size

Instant recharge

No performance degradation during discharge

Clean, zero emission

(4)

Fuel cell basics

Fuel cells in industries

Hydrogen fuel cell vehicles (FCVs)

Hyundai, GM, BMW, Toyota, etc.

(5)

5

Fuel cells in industries

Laptops powered by fuel cells

Samsung, LG, Toshiba, Motorola, etc.

Mostly DMFC

Functional demonstration

Fuel cell basics

(6)

Types of fuel cells

Fuel Cell

Type Electrolyte Anode Gas Cathode Gas Temperature Efficiency Proton Exchange

Membrane (PEM)

solid polymer

membrane hydrogen pure or

atmospheric oxygen

75°C

(180°F) 35–60%

Alkaline

(AFC) potassium

hydroxide hydrogen pure

oxygen below

80°C 50–70%

Direct Methanol

(DMFC) solid polymer

membrane methanol solution

in water atmospheric

oxygen 75°C

(180°F) 35–40%

Phosphoric Acid

(PAFC) Phosphorous hydrogen atmospheric

oxygen 210°C

(400°F) 35–50%

Molten Carbonate

(MCFC) Alkali-

Carbonates hydrogen,

methane atmospheric

oxygen 650°C

(1200°F) 40–55%

Fuel cell basics

(7)

6

Types of fuel cells

Fuel Cell

Type Electrolyte Anode Gas Cathode Gas Temperature Efficiency Proton Exchange

Membrane (PEM)

solid polymer

membrane hydrogen pure or

atmospheric oxygen

75°C

(180°F) 35–60%

Alkaline

(AFC) potassium

hydroxide hydrogen pure

oxygen below

80°C 50–70%

Direct Methanol

(DMFC) solid polymer

membrane methanol solution

in water atmospheric

oxygen 75°C

(180°F) 35–40%

Phosphoric Acid

(PAFC) Phosphorous hydrogen atmospheric

oxygen 210°C

(400°F) 35–50%

Molten Carbonate

(MCFC) Alkali-

Carbonates hydrogen,

methane atmospheric

oxygen 650°C

(1200°F) 40–55%

Solid Oxide

(SOFC) Ceramic Oxide hydrogen,

methane atmospheric

oxygen 800–1000°C

(1500–1800°F) 45–60%

Fuel cell basics

(8)

Types of fuel cells

Fuel Cell

Type Electrolyte Anode Gas Cathode Gas Temperature Efficiency Proton Exchange

Membrane (PEM)

solid polymer

membrane hydrogen pure or

atmospheric oxygen

75°C

(180°F) 35–60%

Alkaline

(AFC) potassium

hydroxide hydrogen pure

oxygen below

80°C 50–70%

Direct Methanol

(DMFC) solid polymer

membrane methanol solution

in water atmospheric

oxygen 75°C

(180°F) 35–40%

Phosphoric Acid

(PAFC) Phosphorous hydrogen atmospheric

oxygen 210°C

(400°F) 35–50%

Molten Carbonate

(MCFC) Alkali-

Carbonates hydrogen,

methane atmospheric

oxygen 650°C

(1200°F) 40–55%

Fuel cell basics

(9)

7

Fuel cells for portable systems

Both types have their own advantages/disadvantages.

PEMFC (Polymer electrolyte membrane fuel cell)

Use H2 as a fuel

Require fuel processing to generate H2

• The extraction of H2 from Sodium Borohydride (NaBH4) seems to be a promising solution.

DMFC (Direct methanol fuel cell)

Use methanol directly as a fuel

Relatively low efficiency and shorter membrane lifetime

Fuel cell basics

(10)

PEMFC components

An ion exchange membrane

An electrically conductive porous backing layer

An electro-catalyst (the electrodes)

Cell interconnects and flowplates

Fuel cell basics

(11)

9

PEMFC operation

Oxidation at anode: 2H

2

4H

+

+ 4e

-

Reduction at cathode: O

2

+ 4H

+

+ 4e

-

 2H

2

O

Fuel cell basics

(12)

Fuel cell system design issues

Stack/cell/membrane

Develop more efficient and durable membranes and electrodes

Fuel generation/processing

Find easier and more convenient ways to obtain H

2

System control techniques for efficient operation

Include battery management, fuel flow control, temperature management, humidity management, and water management

Optimize the fuel consumption, the system size, the response time, etc. according to the applications such as vehicles,

residence, portable electronics

 More studies on system control techniques, especially for portable electronics are required

Work in progress

(13)

11

Work in progress

Most previous work is in the context of hybrid automobiles

No prior work on system-level optimization of fuel cell powered embedded systems

Features Automobile applications Embedded applications

Primary loads Traction motor Processor, memory and peripherals Power generation from the load > 100 Amps for seconds No

Load dynamics > 10 miliseconds 1 miliseconds

Fuel flow control by load variation Moderate Very difficult

Load scheduling Not applicable DPM and DVS

Load type Symmetric Asymmetric

Joint fuel cell and load control Not applicable Desirable

Operating temperature > 60 centigrade 45 to 60 centigrade

Power requirement Best effort Guaranteed

Battery cycle life Important Critical

Comparison with automobile and embedded applications

(14)

Fuel cell characteristics

The cell output voltage is largely dependent on the load current

The cell efficiency is proportional to the cell output voltage

Efficiency = (Operating cell voltage)/(Ideal cell voltage (1.23V@PEM))

Fuel cell and battery hybrid

Unstable chemical reaction Load following

w/fuel flow rate control

Higher fuel efficiency Higher power output

Theoretical m a x i m u m

power P r a c t i c a l

m a x i m u m power

Voltage Power

(15)

13

Fuel cell characteristics

Activation-related losses

Electrochemical reactions

Ohmic losses

Mass-transport-related losses

Finite mass transport limitations rates of the reactants and

depend strongly on the current density, reactant activity, and electrode structure

Current Density (mA/cm ) Theoretical EMF voltage

Region of activation polarization (reaction rate loss)

Region of concentration polarization

(gas transport loss) 1.0

0.5

0

2

Total loss

Region of ohmic polarization (resistance loss)

Fuel cell and battery hybrid

(16)

Motivation of hybrid system

Power density vs. energy density

Fuel cells: low power density, but high energy density

Batteries: high power density, but low energy density

BCS 20W fuel cell stack

Fuel cell and battery hybrid

(17)

Fuel cell and battery hybrid

FC and battery hybrid systems for portable electronics applications

Power range

A few dozens of milli-Watts to hundreds of Watts

Very low supply voltage ranges

3.3 V @ 350 nm, 2.5 V @ 250 nm, 1.8 V @ 180 nm, 1.2 V @ 130 nm, and 1.1 V @ 90 nm semiconductor technologies

Current range is a few dozens mili-Ampere to hundreds of Amperes when VDD <

5 V

Requires extremely low ESR and ESL

Need to avoid diode drops

System dynamics of digital systems are extremely fast

Program phases and I/O device access patterns

Load variation is very high

Modern dynamic power management makes larger variation

15

(18)

Fuel cell and battery hybrid

Power variation of a portable electronics system

Up to 8X difference between the peak and average power in SDRAM

(19)

Fuel cell current Unstable chemical reaction Load following

w/fuel flow rate control

Higher fuel efficiency Higher power output

Theoretical m a x i m u m

power P r a c t i c a l

m a x i m u m power

Voltage Power

Why dynamic current sharing?

Optimal determination of the FC and battery current

ILoad = IFC + IBattery

Fuel cell efficiency is not constant

Large IFC implies low efficiency

Smaller IFC operation is desirable whenever possible

Should be jointly optimized with the dynamic power management of the electronics system

Arbitrary proportion of the current sharing is required

17

Fuel cell and battery hybrid

FC stack

Battery a

1-a

1 Out

(20)

Objective

Purpose of FC and battery hybrid systems for portable electronics applications

Achieve the least possible fuel consumption

Achieve stable operation under range of operating conditions

Increase the power capacity

Reduce the battery size

Extend the battery life cycle

Reduce the form factor

Provide data acquisition and analysis capability

Achieve FC control and BOP interface

Demonstration of portable applications

(21)

Objective

Design consideration

Dynamic active current sharing between the FC and battery

Arbitrary current proportion of the FC and battery

High-efficiency architecture

Precise battery charge management

Scheduled constant-current and constant-voltage charging

Determination and control of the battery charging current

Dual battery support

Self-start capability

32-bit RISC microprocessor-based FC control and BOP interface

Graphic LCD user interface

Communication port with a computer (load)

Joint FC control and dynamic power management of the electronics systems

19

(22)

Architecture of Hybrid Setups

Passive hybrid setups

The proportion of the FC current and the battery current is not controllable, but determined by the device characteristics

Parallel connection

Two-diode connection

MOSFET Diode-OR (enhanced two-diode connection)

Active hybrid setups

The proportion of the FC current and the battery current is controllable

Static selection

Parallel connection with a DC-DC converter

Two-diode with a DC-DC converter

Multiple-input bidirectional DC-DC converters

Multiple-input bidirectional choppers

Multiple-input active current sharing DC-DC converters

(23)

Architecture of Hybrid Setups

Passive hybrid setups

Parallel connection

A fuel cell and a battery are connected together

The simplest setup

Disadvantages

• Constant voltage charging

• Deep-cycle operation is not feasible

• Decrease safety

• Charging and discharging control is passive

21

FC stack

Battery

Vout

FC stack

Battery Constant voltage charging

Charging current

FC stack

Battery Vout

Constant voltage charging

Discharging current FC current

+

!

RFC

+

! VFC

VBat

RBat Vout

(24)

Architecture of Hybrid Setups

Passive hybrid setups

Two-diode connection

The FC and battery outputs are tied together after diodes

In general, RFC >> RBat

VFC is clamped to VBat

• FC stack current is bounded to max(IFC)

• Simple but guaranteed operation

Disadvantages

• Battery voltage and stack voltage should match with each other

• Subject to diode loss

+

RFC

RBat Vout

Voltage

FC stack

Battery

Vout

A: the FC supplies current

B: the FC and battery supply current

(25)

Architecture of Hybrid Setups

Passive hybrid setups

MOSFET Diode-OR (enhanced two-diode connection)

Two-diode setup results in diode loss

To overcome the diode loss, voltage-sensitive MOSFET switches are used

• Feasible with a commercial controller: LT4351

Advanced passive hybrid setup

23

FC stack

Battery

Controller Vout

Controller

www.linear.com

(26)

Architecture of Hybrid Setups

Active hybrid setups

Static selection

Switch between the FC and battery

• When the load current is smaller the than the FC current limit, the switch selects the FC

• When the load current exceeds the FC current limit, the switch selects the battery

Very simple structure

Disadvantage

• Very frequently repeated

charge/discharge of the battery

• The maximum hybrid system

capacity is the battery capacity Driver

Battery FC stack

MOSFET switch

(27)

Architecture of Hybrid Setups

Active hybrid setups

Parallel connection with a DC-DC converter

FC stack voltage is stepped up/down by a DC-DC converter

• Battery voltage need not match with the FC stack voltage

Disadvantages

• Constant voltage battery charging

• Precise current sharing is tricky to control because RDC-DC ≈ RBat

• Cascaded DC-DC converter loss

• Needs a dynamically adjustable DC-DC converter for dynamic sharing

25

FC stack

Battery

Vout DC-DC

converter +

!

+

! VBat

RBat Vout RDCDC

VDCDC

(28)

Architecture of Hybrid Setups

Active hybrid setups

Two-diode with a DC-DC converter

Battery voltage is stepped up/down by a DC-DC converter

• Battery voltage need not match with the FC stack voltage

The proportion of the FC and battery current can be actively controlled by the DC-DC converter voltage

Disadvantages

• Cascaded DC-DC converter loss plus diode loss

• Needs a dynamically adjustable DC-DC converter

Diode-OR can be replaced with a MOSFET diode-OR to avoid diode loss

FC stack

Voltage

Adjustable VDCDC

(29)

Architecture of Hybrid Setups

Active hybrid setups

Multiple-input bidirectional DC-DC converters

Flyback DC-DC converter with rectifiers

Easy to control the current sharing

• No phase synchronization of inverters

Disadvantages

• Diode loss for low-voltage applications

• Complicated flyback DC-DC converter

27

Inverter Rectifieror

Inverter Rectifieror

Inverter Rectifieror FC stack

Battery

Load

(30)

Architecture of Hybrid Setups

Active hybrid setups

Multiple-input Bidirectional choppers

Standard buck- and boost- operations

Advantage

• Easy to control

• Fast response time

Disadvantages

• Less efficient than

synchronous converters

• Significant loss for low-voltage operations

FC stack

Load

DriverDriverDriverDriv

(31)

Architecture of Hybrid Setups

Hybrid setups for portable electronics applications

Low diode loss

Avoid using

• Multiple-input flyback DC-DC converters

• Bidirectional choppers

Two diodes

Active current sharing and charge current setting

No passive current sharing is desirable

True active current sharing is more desirable

• Avoid using parallel connection with a DC-DC converter

Less DC-DC converter loss

No cascaded DC-DC converter is desirable

• Avoid using two diodes with a DC-DC converter

Synchronous DC-DC converter is desirable

• Avoid using a bidirectional chopper

29

(32)

Architecture of Hybrid Setups

Proposed hybrid setup

DTC (Dynamic Input Duty Ratio Control)

True active current sharing

Synchronous duty ratio controlled multiple-input DC-DC converter

Synchronous buck converter-based

No diode loss

TG Vout

Driver

D Q

CPU

Demux

FC stack

Battery

(33)

Architecture of Hybrid Setups

Proposed hybrid setup

DTC (Dynamic Input Duty Ratio Control)

Active proportion control regardless of the fuel cell or battery voltage

Microprocessor controlled

• Open-loop control for rough operation

• Feedback control for nonlinearity compensation

31 Synchronous

DC-DC converter

TG BG

Vout

Driver

D Q

CPU

Demux

FC stack

Battery

Driver

D Q

(34)

Architecture of Hybrid Setups

Proposed hybrid setup

DTC (Dynamic Input Duty Ratio Control)

Input cycle is determined by the microprocessor

Gate control signal is generated by the DC-DC converter

TG BG

Vout

Driver

D Q

CPU

Demux

FC stack

Battery

Driver

D Q

(35)

DTC operation

33

Synchronous DC-DC converter

TG BG

Vout

Driver

D Q CPU

Demux

FC stack

Battery

Driver

D Q

High V Low V

On Off

On Off

Power source switching

(36)

DTC operation

Synchronous DC-DC converter

TG BG

Vout

Driver

D Q CPU

Demux

FC stack

Battery

Driver

D Q

On Off

On Off

Power source switching

(37)

Architecture of Hybrid Setups

Measured system efficiency of the proposed hybrid setup

Including the control circuits and BOP power consumption

35

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(38)

Architecture of Hybrid Setups

Measured system efficiency of the proposed hybrid setup

Excluding the control circuits and BOP power consumption

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(39)

Architecture of Hybrid Setups

Measured system efficiency of the proposed hybrid setup

37

5 W 15 W 25 W 35 W

Battery Portion (%) Efficiency (%)

(40)

Architecture of Hybrid Setups

Additional consideration

PolyPhase DC-DC converters

For high-capacity, low-ripple DC-DC converters

Currently realizes equal current sharing

FC stack

Battery

Battery

(41)

39

A fuel cell system

Fuel cell stack

H

2

generator

Cooling system

Purging system

Humidifier

Hybrid platform

(42)

Battery Management

The standard charge algorithm for Li-ion batteries

Apply a 1C charging current to the battery until the voltage limit is approached

E.g., 1C discharging means to discharge 1 Ah battery in an hour

After the battery terminal voltage reaches to the limit, constant voltage charging is continued

Quick charge methods for Li-ion batteries

1.5C charging current is permitted by a few cell manufactures

E.g., 1.5C charging means to charge 1.5 Ah battery in an hour

2.0C is generally not allowed by the manufactures

Affect the safety and life cycle of the battery

(43)

Battery Management

Three charging phases

Pre-charging: for empty battery

Constant current charging

Constant voltage charging

41

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I_charging

Time V_REG

V_START

V_MIN

I_START

I_REG

Pre-charging Constant current charging Constant voltage charging

V_BATTERY

(44)

Battery Management

Two Li-ion batteries

Allows 2-cell and 3-cell battery packs

Mode change policy

Each battery has charge and discharge modes

One battery is in charge mode, the other is in discharge mode

Once a battery is in discharge mode, it keeps discharging until the mode is changed to prevents from frequent charge/discharge mode changes

Current

FC current Load current Battery 2 discharge

Battery 1 charge Battery 2 discharge

Battery 2 charge Battery 1 discharge

Battery 2 discharge

(45)

Battery Management

Determination of the charging current

Within the range of the charge current limit, the charing current is determined by the FC current

For a given load current, ILoad, determine the FC current IFC

ICharge = IFC - ILoad

• FC current determines the efficiency

43 FC stack

Microprocessor TMS470

LT1769 Li-ion charger

DC-DC converter

Battery2 Battery1

HT0440

FAN7384 SN74HCT139 FAN7384 SN74HCT139 FAN7384 SN74HCT139

HT0440 Charge current

control

Fuel cell current Unstable chemical reaction Load following

w/fuel flow rate control

Higher fuel efficiency Higher power output

Theoretical m a x i m u m

power P r a c t ic a l m a x i m u m

power

Voltage Power

(46)

Self-Start

The hybrid system must be able to start with the

battery

Startup power is supplied by the battery

LDO regulates the battery voltage

Diode stops the startup power after the main DC- DC converter wakes up

Flip flop is reset during the startup sequence until the FC is ready

Startup 5V Vo FC stack

(12~17V)

Battery

(10~12V)

LT1129-5

DC-DCMain converter LT1129

-3.3 3.3V

5V

Startup-done signal

BG (DTC sync)

FAN7384 FAN7384 Battery

select

Fuel cell select

LDO

LDO

Hard-off switch

D Q 74HTC74

R

D Q 74HTC74

S

Vin

Vo Vin

Vo

Vin

Shut down

Prevent from both on Power-on

reset

(47)

Stack and BOP

FC stack operation

Hydrogen pressure

Hydrogen humidity

Stack temperature

Air pressure

Water management

45

H2

H2

H2

Pressure sensor

Pressure regulator

Purge valve

Room temperature PEMFC stack out

Cooling fan Air (oxygen)

supply fan Inlet

temperature sensor

Stack temperature sensor +

out Humidifier

Hydrogen canister

Pressure sensor

Non-relieving type

Hydrogen pressure

Stack temperature Air supply (conviction type)

Water management Fuel

tank

Humidity management

(48)

Stack and BOP

FC stack

BCS 20 W PEMFC stack

20 W with 20 stacks

Conviction type

The next generation will use a

pressured air PEM fuel cell for better efficiency

Self humidification

Use external humidifier for better efficiency

(49)

Stack and BOP

Safety valve

Opens at 8 psig

Protect the PEM fuel cell stack in case of emergency (controller failure)

Check valve

Prevent from negative pressure and thus reverse flow

Opens at 2 psig

47

Safety valve

Check valve

(50)

Stack and BOP

Purge valve

Drain accumulated water at the hydrogen anode

Solenoid valve

Periodically opened by the microprocessor

Emergency open when the hydrogen

inlet pressure exceeds the limit

(51)

Stack and BOP

Humidifier

Generates wet hydrogen

Needs upgrade for portable applications

Pressure regulator

Generate 2 to 4 psig hydrogen pressure

Non-relieving type for hydrogen

Need to tolerate wide input pressure range for various types of hydrogen generators

49

(52)

Stack and BOP

Pressure sensor

0 to 15 psi and 0 to 100 psi

Differential voltage output

Signal conditioning with an instrument amplifier

Previous Current

(53)

Monitoring and User Interface

Control and monitoring software

Current, voltage, pressure and temperature monitoring

DTC status monitoring

Battery status monitoring

51

Output status Voltage of power sources Inlet hydrogen

pressure &

temperature

Stack hydrogen pressure &

temperature

DTC status

Battery status

(54)

Implementation

Microprocessor DC-DC Converter DTC

Gate Driver

Boot-up LDO

ADC ports

Temp.

Sensor

Pressure Sensor

Current Shunt Monitor Charge

Circuit

Serial Port

LDO FC stack

Battery

Load

Architecture

(55)

Implementation

A proof-of-concept prototype

No miniature BOP components

Basic hybrid operation

53

ACM SIGDA University Booth 2006

(56)

Implementation

Revision 2.0 Prototype

Side view

Compact hybrid system

controller LCD status

monitor Pressure

regulator

Temperature sensor

Li-ion batteries

Conviction-type PEM fuel cell stack

Safety valve

Purge

(57)

Implementation

Revision 2.0 Prototype

Top view

55

Humidifier Pressure sensors

Compact hybrid system

controller LCD status

monitor

Pressure regulator

Temperature sensor

Li-ion batteries

Conviction-type PEM fuel cell stack

Safety valve

Purge valve

(58)

Implementation

Hybrid system controller

Microcontroller

LCD connector Primary DC-DC

converter

Pressure sensor

signal conditioning 12 V

Step-up DC-DC DTC MOSFET

gate drive

LCD driver Battery

charger Battery charging

control

Boot-up LDO

(59)

Implementation

ISLPED ’07 Design Contest Award

Operation of a PMP

57

(60)

Implementation

Experimental environment

(61)

59

Hybrid system optimization

Maximize the lifetime of the fuel cell

Fuel cell lifetime is determined by the fuel consumption

Fuel consumption rate is proportional to the current value

Total fuel consumption is proportional to the total charge consumption

Maximizing the lifetime  minimizing the charge consumption

Other objectives  minimizing the form factors (battery size, etc.)

Objectives: efficiency

(62)

Fuel cell system efficiency

Fuel cell output voltage considering the controller power

consumption

(63)

61

Fuel cell system efficiency

DC-DC converter efficiency

(64)

Fuel cell system efficiency

System efficiency

(65)

63

Challenges

Fuel flow control

Various hydrogen supply

Slow dynamics

Efficiency analysis

Various control schemes and design specifications

Joint power management

How to utilize the efficiency characteristics

Energy aware versus FC aware

Implementation issues

(66)

wearable computer application

Load characteristics

Navigation: 5W

Night vision: 20W

CCD video camera with an MPEG2 encoder: 5W

Laser scope for distance measurement: 5W

Laptop: 30W in active mode and 1W in sleep mode

GPS:1W

Communication: 5W during transmission and 1W during receiving

Head mount display: 4W

Audio cue: 1W in active mode

Satellite communication: 30W during transmission and 2W during receiving

(67)

65

wearable computer application

Synthetic one-day outdoor wearable computer application scenario

Load profile

Battery and fuel cell voltage

(68)

wearable computer application

Synthetic one-day outdoor wearable computer application scenario

Load profile

Battery and fuel cell current

(69)

67

wearable computer application

Synthetic one-day outdoor wearable computer application scenario

Load profile

Battery state of charge

(70)

Example 2: Fuel cell DVS

Minimize

Bleeder

Embedded system Energy provider Energy consumer

 When fuel cell power is less than load power

Battery provides extra power to support the system

 When fuel cell power is larger than load power

Fuel cell system

Battery

(71)

69

I

F

= 500mA, B

max

= 2000 mA-min, B

kini

=1000mA-min, Task T

k

has execution time 10min. i

k

(1)=500mA

DVS scales from 1 to 2.5 with steps of 0.1,

Case I: energy efficient scaling sk = 2, ik=170mA

Qtask = 3400 mA-min Qwaste= 5600 mA-min Qsys= 9000 mA-min

Qtask 20min

170mA

500mA IF

Qwaste Charge stored into the battery

Case I: Energy efficient scaling

Qtask

11min 500mA

411mA IF

mA Charge stored

into the battery

Case II: Fuel cell efficient scaling Case II: fuelcell efficient scaling

sk = 1.1, ik = 411mA Qtask = 4521 mA-min Qwaste= 0

Qsys= 4521 mA-min

Example 2: Fuel cell DVS

Fuel cell-aware DVS with fixed fuel cell current (DAC06)

(72)

Example 2: Fuel cell DVS

Power source setting: I

F

= 800mA, B

max

=250mA-hr (load current is 700mA on highest frequency)

Fuel cell-aware DVS with fixed fuel cell current (DAC06)

(73)

71

0 value means the configuration is not feasible Configuration

with bad efficiency

Configuration with good efficiency

Fuel cell-aware DVS with fixed fuel cell current (DAC06)

Now we vary both fuel cell current and battery capacity

I

F

: 250mA – 700mA with steps of 50mA

B

max

: 100mA-min to 204,800mA-min (~ 3500mA-hr)

Example 2: Fuel cell DVS

(74)

Example 2: Fuel cell DVS

Task parameters

Fuel cell-aware DVS with fuel flow rate control (ISLPED06)

(75)

72

Example 2: Fuel cell DVS

Task parameters

Task-by-task fuel flow control

Fuel cell-aware DVS with fuel flow rate control (ISLPED06)

(76)

Example 2: Fuel cell DVS

Fuel cell-aware DVS with fuel flow rate control (ISLPED06)

(77)

74

Conclusions

Fuel cell

Convert chemical energy into electrical energy

Clean and efficient power source

Fuel cell and battery hybrid system

Provide both high energy density and high power density

A promising solution for portable electronics as well as vehicles

Most fuel cell researchers focus on the stack/cell/membrane

Need contributions for the hybrid systems and controllers

Suitable for CSE people

Hybrid system optimization for portable electronics

Optimize fuel consumption, size, power/energy density, etc.

Must consider the characteristics of the application, the fuel cell efficiency, the

battery charging/discharging efficiency and the wasted charge

(78)

Acknowledgment

Design and implementation

Kyungsoo Lee (SNU), Youngjin Cho (SNU), Donghwa Shin (SNU), Jaehyun Park (SNU), Younghyun Kim (SNU), and Jihun Kim (SNU)

Fuel cell operation support

Dr. Dominic Gervasio (ASU) and Sonja Tasic (ASU)

Funding support

Dr. Ken Han (KITECH)

Collaborative research for the

advanced power management and an FC simulator

Prof. Chaitali Chakrabarti (ASU), Prof. Sarma Vrudhula (ASU), Jianli Zhuo (ASU),

and Sudheendra Kardi (ASU)

KITECH Arizona State University

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