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COMPARISON OF MESOPOROUS CARBON/CARBON SUPERCAPACITOR AND NiO / MESOPOROUS

CARBON HYBRID ELECTROCHEMICAL CAPACITOR

TERESSA A/P LUDU NATHAN

UNIVERSITI SAINS MALAYSIA

2008

COMPARISON OF MESOPOROUS CARBON/CARBON SUPERCAPACITOR

AND NiO / MESOPOROUS CARBON HYBRID ELECTROCHEMICAL CAPACITOR

By

TERESSA A/P LUDU NATHAN

Thesis submitted in fulfillment of the requirements for the degree

of Masters of Science

MAY 2008

ii

ACKNOWLEDGEMENTS

I would like to express my gratitude to my supervisor Professor Dr. Ahmad

Fauzi Mohd Noor who has always been there to help me despite his schedules with

research, administration work and teaching. He has been extremely helpful in not only

suggesting worthwhile content and research strategy, but also offering advice on

authoring and effective thesis writing skills. Words fall short to express his enthusiasm

and invaluable help towards executing this research tasks in USM.

Sincere thanks are extended to Assoc. Prof. Azizan Aziz, the Deputy Dean of

Post Graduate studies in the School of Materials and Mineral Sciences for granting me

the permission to use electrochemical workstation and Arbin battery testing system,

which was the major contribution in obtaining the electrochemical data for this thesis.

I am deeply indebted to my field supervisor Assoc. Prof. Dr. SRS Prabaharan

from the University of Nottingham, Malaysia Campus for his efforts and time in

producing this worthwhile thesis. He has supported and encouraged me in many ways

in terms of valuable ideas and research techniques. His stimulating suggestions and

encouragement helped me finish thesis on time. Thanks are also due to his valuable

time and advice in thesis write-up.

Without these scholars, the completion of this thesis would have been an

impossible proposition.

Special thanks go to Prof. A R West, Head of Engineering Materials Dept., The

University of Sheffield, UK, and his post docs, Dr. Gabby and Dr. Deni Pasero who

rendered me their guidance in all possible ways and helped me using Tony’s

laboratory facilities. The initial experimental work, which was carried out in his lab, has

benefited me a lot and it was used as a yardstick to complete this work.

I would also like to gratefully acknowledge the support of some very special individuals,

Mr. Sunnil Kraemer, Managing Director of IKA Works (Asia) Sdn Bhd, Mr. Muthu,

(TEM) from School of Biology, Mr. Rashid (FE-SEM) from School of Material and

iii

Mineral Sciences, Mr. Karuna (XRD) from School of Physics and Mr. Suhaimi

(Electronics lab) from School of Material and Mineral Science who have been directly

or indirectly of help offering their encouragement and support.

Special thanks to Dr. Siluvai Michael, SSN Engineering College, India for

sharing her knowledge in this field during the early days of my studies. Last but not

least; I would like to thank my parents and siblings who had perpetually encouraged

and supported me throughout this thesis work.

iv

TABLE OF CONTENTS

Page ACKNOWLEDGEMENTS ii

TABLE OF CONTENTS iv

LIST OF TABLES ix

LIST OF FIGURES x

LIST OF ABBREVIATION xv

LIST OF PUBLICATIONS & SEMINARS xvi

ABSTRAK xvii

ABSTRACT xix

CHAPTER ONE : INTRODUCTION

1.0 Introduction 1

1.1 Research Background 3

1.2 Justification of Study 10

1.3 Objectives of present research 12

CHAPTER TWO : LITERATURE REVIEW

2.0 Fundamental Understanding 13

2.1 Current understanding of Electrochemical capacitors

15

2.1.1 Basic principle of a capacitor 15

2.1.1.2 Capacitance 16

2.1.2 Electrochemical Capacitor 17

2.1.2.1 Introduction of Electrochemical Double Layer Capacitor

17

2.1.2.2 Concept of Electrochemical Double Layer Capacitor

18

2.1.2.3 Non-Faradaic 20

2.1.2.4 Faradaic 20

2.1.2.5 Characteristics of Electrochemical Double layer Capacitor

21

2.2 Classifications of Electrochemical capacitors

22

2.2.1 Supercapacitor , Pseudocapacitor, Hybrid Capacitor

22

2.2.2 Pseudocapacitance 22

2.2.3 Hybrid Capacitor 24

v

2.2.4 Electrolytic capacitors 25

2.2.5 Main Applications of EDLC 26

2.2.5.1 Current and potential applications for EDLC 26

2.3 Overview of electrodes and electrolytes 29

2.3.1 Nomenclature of EDLC 29

2.4 Electrode material 29

2.4.1 Carbon 29

2.4.1.2 Desirable properties of carbon for electrochemical applications

31

2.4.1.3 Porous Carbon 31

2.4.1.4 Activated Carbons 33

2.4.1.5 Carbon Aerogels 34

2.4.1.6 Carbon Nanotubes 34

2.4.2 Metal Oxides 35

2.4.3 Polymers 36

2.5 Electrolyte 37

2.5.1 Aqueous Electrolyte 38

2.5.2 Non-Aqueous (organic) Electrolyte 39

2.6 Separator 40

2.7 Binder and current collector 40

2.8 Cell Design 41

2.9 Comparison of Capacitor, EDLC and battery 42

2.10 Choice of Electrode materials: A rationale 44

2.10.1 Nanostructured NiO as positive electrode 44

2.10.2 Soft-chemistry Approach for synthesis of transition metal oxides

46

2.10.3 Synthesis of nanostructured NiO

47

2.10.4 Nanostructured (Mesoporous) carbon as negative electrode

48

2.11 Effect on equivalent series resistant (ESR) 49

2.11.1 Additive carbon 52

CHAPTER THREE : EXPERIMENTAL METHODOLOGY

3.1 Introduction 53

vi

3.1.1 Methodology overview 53

3.2 Electrode Preparation

3.2.1 Mesoporous Carbon and additive carbon 54

3.2.2 Carbon Black Electrode Preparation 57

3.3 Soft-chemistry synthesis

58

3.3.1 Synthesis of nanostructured NiO

58

3.3.2 Nickel Oxide Electrodes : Preparation

60

3.3.3 Three-electrode electrochemical cell

construction

60

3.4 Fabrication of Symmetric and Asymmetric EC

61

3.5 Instrumentation techniques employed 62

3.5.1 Phase Analysis (XRD) 62

3.6 Morphological studies

3.6.1 Field Emision Scanning Electron Microscopy

(FESEM)

63

3.6.2 Transmission Electron Microscopy (TEM) /

Selected Area Electron Diffraction (SAED)

64

3.6.2 Thermogravimetic Analysis (TG) 65

3.7 Electrochemical Techniques 65

3.7.1 Cyclicvoltammetry (CV) 65

3.7.2 Galvanostatic – constant current charge and

discharge measurements

67

3.7.3 EIS – AC Impedance Spectroscopy 69

CHAPTER FOUR : RESULT AND DISCUSSION

4.1

Physical Characterization of Nanostructured (Mesoporous)

Carbon as negative electrode

71

4.1.1 XRD 71 4.1.2 TEM 72 4.1.3 FE-SEM 73 4.1.4 Electrochemical impedance spectroscopy (EIS) 74 4.1.5 Cyclic voltammetry (CV) 81

vii

4.1.6 Galvanostatic – constant current charge and

discharge measurements

86

4.1.7 Ragone plot – Power density and Energy

Density

91

4.2 Studies on additive carbons in the composite EM2K nanoporous carbon electrode: Effect on ESR improvisation

92

4.2.1 Electrochemical impedance spectroscopy (EIS) 93

4.2.2 Galvanostatic – constant current charge and

discharge measurements

95

4.2.3 Ragone plot – Power density and Energy

Density

100

4.3 Low temperature Synthesis of Nanostructured NiO for

Electrochemical Capacitors

104

4.3.1 Synthesis of Nanostrucutred NiO using a

solvothermal low temperature process

104

4.3.2 Physio-chemical Characterization 105

4.3.2.1 Thermogravimetric analysis (TG) 105

4.3.2.2 Phase Analysis 106

4.3.2.3 FE-SEM/HR-TEM analysis 107

4.3.3 Electrochemical Studies 111

4.3.3.1 Single Electrode Behavior vs. standard calomel

electrode

111

4.4 Asymmetric Hybrid capacitor NiO (+)/ Mesoporous Carbon

EM2K

115

4.4.1 NiO(+)/EM2K (assembled) based on single

electrode characterization as electrodes for ECs

115

4.4.2 AC-impedance (Nyquist) Analysis (EIS) 116

4.4.3 Current-voltage response using Cyclic Voltammetry

119

4.4.4 Constant current charge-discharge analysis 121

4.4.5 Ragone Plot - Power density versus Energy

density

125

CHAPTER FIVE : SUMMARY AND CONCLUSION

127

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5.1 Summary 127

5.2 Conclusion 130

5.3 Future recommendation 131

REFERENCES 132

APPENDIX 139

PAPER PUBLICATION 144

ix

LIST OF TABLES Page

2.1 Comparison of Capacitor and Double Layer Capacitor 43

2.2 Comparison of Double Layer Capacitor and battery 44

3.1 Physical properties of EM2K 55

3.2 Summary of physical properties of EM2K, BP2K and AB 57

3.3 Different type of composition of Emperor 2000 (EM2K) used in

this work and its cell assembly.

57

3.4 Asymmetric EC configuration using NiO 58

4.1 Summary of values of specific capacitance values obtained at

different scan rates.

84

4.2 summary of the Specific capacitance obtain ranging from 13.28

F/g to 27.35 F/g at different current density in ascending

manner

88

4.3 Summary of the overall capacitance obtained from three

different methods ( AC Impedance, cyclic voltammetry and

Gavanostatic).

90

4.4 Summary of specific power density and specific energy density

taken obtained different current density.

92

4.5 Summary of the ESR values and the specific capacitances

obtained in all three carbon composition

94

4.6 EM2K with 10% of AB as electrode at different current

densities

99

4.7 EM2K with 10% of BP2K as electrode at different current

density

100

4.8 Specific Capacitance Comparison of cell A, B & C at different

current density

100

4.9 Summary of the power and the energy density comparison of

all three carbon composites

101

4.10 Summary of specific capacitance obtained at different scan

rates

121

4.11 Summary of the specific capacitance values achieved for

NiO/C hybrid cell obtained by means of constant current

charge-discharge technique.

124

4.12 Power density and energy density at various scan rate 126

5.1 Energy density and Power density comparison of the four EC configurations studied in this work

129

x

LIST OF FIGURES

Page

1.1 FE-SEM image of the as-grown single walled CNT 6

2.1 Classification of different type of commercially available

capacitors.

14

2.2 Principle of electrostatic induction 15

2.3 Behavior of electrolyte in ion ( positive charge) in the pore

when charged and discharge

18

2.4 Helmholtz double layer 19

2.5 Typical distribution of charges at the interface and its

electrode potential before and after charging.

20

2.6 A Li-doped graphite in the anode of the hybrid capacitor that

intercalates Li+ ions into its interlayer in the charging process

and de-intercalates Li+ ions in the discharging process

24

2.7 Working principle of a hybrid capacitor. 25

2.8 Illustration of a mesoporous activated carbon structure and

EDLC configuration.

30

2.9 IUPAC classification of porous materials 33

2.10 EDLC Cell construction 42

2.11 Comparison chart indicating the specific power density and

energy density of capacitor, supercapacitors, batteries and

fuel cells.

43

2.12 Equivalent circuit describing the impedance behavior of a

typical double layer capacitor

50

3.1 Flow chart of the methodology approached 54

3.2 TEM image of acetylene black. 56

3.3 TEM image of Black pearls 2000. 56

3.4 Flow chart showing the soft chemistry method to synthesis of

Nickel oxide by using a new solvolysis technique at low

temperature

59

3.5 Open beaker three electrode cell, comprising active material

electrodes (composite electrode cut into a pre-determined

size) as working electrode, saturated calomel electrode using

saturated KCl solution as the reference electrode and

platinum foil as the counter electrode.

61

xi

3.6 Stainless steel cell used in EC cell fabrication 62

3.7 Comparison of ideal and real cyclic voltammograms 66

3.8 Typical frequency dependent impedance plot of EDLC drawn

Z” (imaginary impedance due to capacitive components) vs.

real impedance Z’

69

4.1 XRD Pattern of Emperor 2000 carbon (EM2K) 71

4.2 TEM Image of Emperor 2000 carbon (EM2K) 72

4.3 (a) Nanoporous (mesoporosity) morphology with particle sizes within the range, 9-13 nm. Image x 50,000 magnification

73

4.3 (b) Nanoporous (mesoporosity) morphology with particle sizes within the range, 9-13 nm. Image x 100,000 magnification

74

4.4(a) The Nyquist complex plane impedance plot, Z″ (real) versus Z′ (imaginary), the real and the imaginary components of the impedance are obtained in variant of frequency range from 10 kHz to 1mHz.

75

4.4(b) Exploded view of the Nyquist plot within the range of 10kHz

to 10Hz

75

4.5 Specific capacitance vs Frequency of EM2K symmetric configuration (soaked in Electrolyte for 1 hr)

77

4.6 (a) Comparison of Nyquist plots for similar electrodes soaked in two different condition (atmospheric pressure and vaccum (degassed))

78

4.6 (b) Exploded view of two Nyquist comparison of similar electrodes soaked in two different condition (atmospheric pressure and vaccum (degassed))

78

4.7 Comparison of Specific capacitance vs Frequency plot for similar electrodes soaked in two different condition (atmospheric pressure and vaccum (degassed))

80

4.8 RC plot depicting the region I, the propagation occurs along the more expanded mesopore structures and the region II that could be ascribed to the penetration of ac signal into the narrow mesopores.

81

4.9 Rate dependant voltammograms of EM2K symmetric cell

84

4.10 Cyclic voltammogram of EM2K symmetric cell at a scan rate of 10mV/s

85

xii

4.11 Cyclic voltammogram of EM2K symmetric cell at a scan rate of 100mV/s

85

4.12 Variation of Specific Capacitances with respect to scan rate

86

4.13 Charge/Discharge profile of EM2K similar electrode obtained at different current densities.

88

4.14 (a) Galvanostatic-Charge/Discharge of EM2K similar electrode at 56.6mA/cm2

89

4.14 (b) IR drop observed during Charge/Discharge of EM2K similar electrode at 56.6mA/cm2

89

4.15 (a) Galvanostatic-Charge/Discharge of EM2K similar electrode at 11.3mA/cm2

90

4.15 (b) IR drop observed during Charge/Discharge of EM2K similar electrode at 11.3mA/cm2

90

4.16 Ragone Plot of EM2K similar electrode exhibiting the relationship of power and energy density

92

4.17 Nyquist complex plane impedance plot, Z″ (real) versus Z′

(imaginary) obtained in variant of frequency range from 10

kHz to 1mHz comparing all three cell with different

composition.

94

4.18 Specific Capacitance vs Frequency comparing all three cell

with different composition.

95

4.19(a) Galvanostatic-Charge/Discharge profile of Similar Electrodes

of Emperor 2000/AB at different current densities

96

4.19(b) Galvanostatic-Charge/Discharge profile of Similar Electrodes

of EM2K with 10% of BP2K as electrode at different current

density

96

4.20(a) Similar Electrodes of Emperor 2000/AB - Galvanostatic-

Charge/Discharge at 56.6mA/cm2

97

4.20(b) Similar Electrodes of Emperor 2000/BP2K -Galvanostatic-

Charge/Discharge at 56.6mA/cm2

97

4.20(c) Similar Electrodes of Emperor 2000/AB -Galvanostatic-

Charge/Discharge at 11.3 mA/cm2

98

4.20(d) Similar Electrodes of Emperor 2000/BP2K -Galvanostatic-

Charge/Discharge at 11.3 mA/cm2

98

4.21 The charge/discharge behavior of composite carbons ( AB +

BP2K) as compared to virgin EM2K at 28.3 mA/cm2 current

density

99

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4.22 Comparison of Energy Density (Wh/kg) and power density

(W/kg) of Similar Electrodes of EM2K/ AB at different current

densities.

102

4.23 Comparison of Energy Density (Wh/kg) and power density

(W/kg) of Similar Electrodes of EM2K/ BP2K at different

current densities

103

4.24 Comparison of Energy Density (Wh/kg) and power density

(W/kg) of Similar Electrodes of EM2K, EM2K/ AB and

EM2K/BP2K at different current densities

103

4.25 TGA Analysis of nickel nitrate precursor before NiO formation 106

4.26 X-ray diffractogrmas of NiO at different heat treatment

temperature

107

4.27 FE-SEM picture of NiO heated at (a) 400oC , (b) 600 oC and

(c) 800 oC in air for 1 hr

108

4.28 HR-TEM picture of NiO heated at 400oC (1h/air) (Inset: Bright

field SAED pattern of the NiO heated at 400°C/ 1hr in air)

110

4.29 EDAX analysis of nickel oxide calcined at 400oC 110

4.30 Scan rate dependent cyclic voltammetry of nanostructured

NiO against SCE reference electrode.

111

4.31 Specific Capacitance vs Potential plot of nanostructured NiO

against SCE reference electrode.

113

4.32 Nyquist plot (Z” vs Z’) NiO(+)/Na+/C(-) hybrid cell illustrating

the capacitive behaviour (spike-like frequency response) at

frequencies below 170 Hz

117

4.33 Specific Capacitance vs frequency of NiO(+)/Na+/C(-) hybrid

cell

118

4.34 Cyclic voltametry of NiO(+)/Na+/C(-) hybrid cell at different

scan rate

120

4.35 (a) Cyclic voltametry of NiO(+)/Na+/C(-) hybrid cell at 5mV/s 120

4.35 (b) Cyclic voltametry of NiO(+)/Na+/C(-) hybrid cell at 100mV/s 120

4.36 Specific capacitance vs Potential plot of NiO(+)/Na+/C(-)

hybrid cell at different scan rate

121

4.37 Galvanostatic charge/discharge cycles at different current

densities. (a) 56.6 mA/cm2 (b) 28.3 mA/cm2, (c) 11.3 mA/cm2

(d) 5.7 mA/cm2 (e) 2.8 mA/cm2 (f) 0.6 mA/cm2

123

xiv

4.39 (a) Galvanostatic-Charge/Discharge at 0.6mA/cm2 of

NiO(+)/Na+/C(-) hybrid cell

124

4.39 (b) Galvanostatic-Charge/Discharge at 56.6 mA/cm2 of

NiO(+)/Na+/C(-) hybrid cell

125

4.40 Power density vs. energy density relationship of

NiO(+)/Na+/C(-) hybrid cell

126

5.1 Comparison of Ragone plot of the four EC configurations studied in this work

129

xv

LIST OF ABBREVIATION

1.1 EC - Electrochemical Capacitor

1.2 SC - Supercapacitor

1.3 UC- UItracapacitor

1.4 EDLC - Electrochemical Double layer Capacitor

1.5 ESR - Equivalent Series Resistant

1.6 CV - Cyclic Voltametry

1.7 EM2K- Emperor 2000

1.8 BP2K – Black Pearls 2000

1.9 AB – Acetalyne Black

xvi

LIST OF PUBLICATIONS & SEMINARS

1.1 1.2

Nanostructured NiO for Electrochemical Capacitors: Synthesis and Electrochemical properties Teressa L Nathan, Azizan Aziz, Ahmad Fauzi Noor , SRS Prabaharan ICMAT 2007 Singapore Solid State Electrochem DOI 10.1007/s10008-007-0465-3, Springer-Verlag 2007 Low temperature Synthesis of Nanostructured NiO for Electrochemical Capacitors, Teressa L Nathan, Azizan Aziz, Ahmad Fauzi Noor , SRS Prabaharan, Presented at the 4th COE Workshop on Regional Network Formation for Enhancing Research and Education on Materials Engineering, Bandung (Indonesia) June 26-28, 2006 organised by Institute Technology Bandung Indonesia and Nagaoka University Technology, Japan. Paper submitted to Advances in Technology of Materials and Materials Processing Journal (ATM ISSN 1440-0731)

140

xvii

PERBANDINGAN ANTARA KARBON/KARBON SUPERKAPASITOR DAN NIO/ KARBON MESOOLIANG KAPASITOR ELEKTROKIMIA HIBRID

ABSTRAK

Kapasitor elektrokimia adalah satu teknologi mantap yang mempunyai potensi

tinggi sebagai peranti penyimpan tenaga. Keupayaannya memenuhi keperluan tenaga

semasa, dari sudut ketumpatan tenaga dan kuasa yang tinggi, membolehkannya

menjadi alternatif kepada bateri dalam aplikasi-aplikasi khusus yang memerlukan

kuasa output yang besar. Bahagian pertama kajian tertumpu kepada pencirian bahan

berkarbon tanpa grafit, khususnya karbon hitam Emperor 2000 (EM2K). Sel

elektrokimia dibentuk dengan pellet EM2K yang kemudiannya direndam ke dalam

larutan elektrolit 2M NaOH dan diuji pada pelbagai ketumpatan arus untuk melihatkan

kelakuan cas/discasnya. Voltametri siklik dan ciri-ciri impedans juga dianalisis dan

disimpulkan memberi kapasitans sebanyak 20F/g. Kekonduksian elektrod adalah

penting mempengaruhi rintangan bersiri ekuivalen (ESR) bagi sel kapasitor.

Pengurangan ESR dapat dilakukan dengan meningkatkan kekonduksian elektrik untuk

elektrod karbon dengan cara menambahkan karbon hitam berkekonduksian tinggi,

seperti asetalin hitam (AB) dan/atau Black Pearl 2000 (BP2K). Komposit elektrod yang

mengandungi karbon hitam berkekonduksian tinggi ini, dengan 10% berat AB dan/atau

BP2K, telah menghasilkan kapasitans tentu 24 F/g dan 39 F/g masing-masing. Dalam

kajian ini juga, nikel oksida (NiO) dipilih sebagai elektrod positif disebabkan sifat-sifat

redoknya melibatkan pengoksidaan Ni2+ /Ni3+ yang menerbitkan keupayaan discas

spesific berbalik yang besar. NiO berstruktur nano disintesis melalui keadah nitrat-

sitrat, menggunakan Ni(NO3)2 sebagai bahan mula dalam kehadiran asid sitrik serta

menggunakan gabungan metanol/aseton. Struktur nano hasil akhir telah dipastikan

dengan analisis TEM dengan butiran primer dalam julat 7-15 nm. Kelakuan redoks

(penurunan/pengoksidaan) satu kebolehbalikan hasilan disintesis telah ditentu pasti

dengan kajian voltametri siklik 3 elektrod. NiO (+)/C(-) hybrid EC telah difabrikasikan

xviii

menggunakan pellet NiO yang ditekan dan dipanaskan pada 400 º C sebagai elektrod

positif melawan EM2K dalam larutan 2M NaOH. Kapasitans spesifik setinggi 16 F/g

pada 1mHz telah dicapai. Ketumpatan tenaga dan ketumpatan kuasa yang dihitung

daripada keluk cas/discas adalah masing-masing 3.9 Wh/kg dan 2727 W/kg dan

kemudian dianalisa menggunakan plot ragone (Ketumpatan tenaga lawan ketumpatan

kuasa). Keupayaan sedemikian bagi hibrid EC adalah disebabkan penyimpanan cas

pada permukaan dan pukal bagi aktiviti redoks.

xix

COMPARISON OF MESOPOROUS CARBON/CARBON SUPERCAPACITOR AND NiO / MESOPOROUS CARBON HYBRID ELECTROCHEMICAL

CAPACITOR

ABSTRACT

Electrochemical capacitors (EC) are superior breed of technology that is

regarded as highly potential energy storage device. Its ability of fulfilling the current

demand of energy, in terms of high energy and power density simultaneously, turns out

to be a very promising alternative to batteries in niche applications requiring significant

power output. The first part of the thesis focused on investigating non-graphitized

carbonaceous materials namely Emperor 2000 (EM 2K) carbon black (courtesy of

Cabot Malaysia). An electrochemical cell, assembled using EM2K pellets as similar

electrodes immersed in aqueous electrolyte medium (2M NaOH) was tested at a

different current density to reveal its charge/discharge behavior. Cyclic voltammetry

and the impedance characteristics were analyzed deducing a capacitance of ~20 F/g.

Electrode conductivity is one of the important parameters affecting the equivalent

series resistance (ESR) of the capacitor cell. In order to reduce the ESR, conducting

carbons such as acetylene black (AB) and/or Black Pearl 2000 (BP2K) were added.

Accordingly, the composite electrode consisting of these highly conducting black

carbons (10 wt %) AB and/or BP2K providing a specific capacitance of ~24 F/g and

~39 F/g respectively. This being a negative electrode, nickel oxide was chosen as

positive electrode which is one of the transition metal oxides known to possess

excellent pseudocapacitive due to its redox properties involving oxidation of Ni2+/Ni3+

giving rise to a large reversible specific discharge capacity. Nanostructured NiO was

synthesized via a nitrate-citrate method using Ni(NO3)2 as starting material in the

presence of citric acid by using solvolysis agents such as methanol/acetone mixture.

The product thus obtained was subjected to thermal treatment at 400oC for 1hr in air

showed a single phase cubic structure as confirmed by XRD. The nanostructure of the

final product was confirmed by TEM analysis with primary particles within the range 7-

xx

15 nm in sizes. The redox behavior (reduction/oxidation) and its reversibility of the

synthesized product were confirmed by 3-electrode cyclic voltammetry studies. Hybrid

EC (NiO(+)/C(-) asymmetric combination) was fabricated utilizing pellet pressed NiO

annealed at 400 oC as positive electrode against EM2K in 2M of NaOH aqueous

solution. The specific capacitance of 16 F/g at 1mHz was achieved. The energy density

and power density calculated from the charge/discharge curve were 3.9 Wh/kg and

~2747 W/kg respectively and analyzed using the Ragone plot (Energy density vs.

Power density). Such a performance of hybrid EC was attributed to charge storage in

both surface and bulk redox activity.

1

CHAPTER 1 INTRODUCTION

1.0 Introduction

Electrical energy storage devices are mandatory in myriad applications viz.,

telecommunication devices (cell phones, remote communication, walkie-talkies etc),

standby power systems, and electric hybrid vehicles in the form of storage components

(batteries, supercapacitors and fuel cells). These prompted the need for advanced

power sources offering high power density (Conway, 1999). The electrochemical

capacitors (ECs) or supercapacitors (SCs) represent a new generation of

electrochemical energy storage components with very high capacitance for energy

storage. ECs store energy in either capacitive (double layer of electrostatic charges) or

pseudocapacitive (a faradic battery-like reaction) nature. Exploiting both the

advantages of battery (high energy density) and conventional capacitors (high power

density), ECs easily offer higher specific capacitance values up to several thousand

Farad for applications requiring pulse power (appliances requiring high power bursts in

the seconds range). They can also be cycled several hundred thousand times. Being

an entity of ECs, hybrid capacitors (incorporating a battery-like anode (+) and a carbon-

based cathode (-) having non-faradic character) have more to render in terms of power

and energy (Conway, 1999).

This class of energy storage device is commonly known in many names such

as supercapacitor, ultracapacitor (SC) or electrochemical double-layer capacitor

(EDLC). It is capable of condensing energy, by arraying electrical charges,

electrostatically at the electrode/electrolyte interface, known as the helmholtz layer,

achieving capacitance in the order of Farads. The term “EC” is referred commonly in

this thesis. Penetrating into the current market as a feasible alternative to batteries,

ECs are paving ways for researchers to investigate all possible materials that could

deliver enhanced performances in terms of power and energy density, charge-

2

discharge characteristics, cycling stability and reversibility (Conway, 1999; Burke,

2000; Kotz and Carlen, 2000). New materials for electrodes such as activated

carbons, nanostructured carbon, carbon nanotubes, activated fibers and graphite of

high porosity, nano sized transition metal oxides, conducting polymers etc provides

high specific surface area with good electrical conductivity. Since electrical capacitance

of ECs is quite dependent on the number of ions (anions or cations) present at the

electrode/electrolyte interface, highly increased specific surface area of these new

electrode materials is essential for the ECs to obtain remarkably increased number of

ions adsorbed on the surface of electrodes so as to realize the so-called “super-

capacitance”.

To be specific, the term supercapacitor (SC) is commonly used to describe

carbon/carbon symmetrical cells exhibiting “super-capacitance” with several tens of

hundreds of farads. SCs in general, are attributed to the purely non-diffusional charge

reaction during the polarization. Hence, SCs do not exhibit redox (reduction/oxidation)

reaction for electricity storage. Thus, the charge-discharge cycle life of SCs can be

over 300,000 cycles (charge/discharge) and the turn around efficiency is up to 96%

without significant degradation between the operating temperatures of –25 and +50oC.

In addition, the charge time becomes very rapid up to a few seconds and the specific

power density is at least two order higher than the secondary or rechargeable batteries

(Conway, 1999; Burke, 2000; Kotz and Carlen, 2000). These are the most distinctive

outstanding characteristics as a new type of energy storage power source that any

other types of electric storage devices such as advanced lithium-ion and lithium

polymer rechargeable batteries cannot offer power density as high as what SCs could

offer. However, the specific energy density of the SCs is hitherto one order of

magnitude less than that of rechargeable lithium batteries.

Research into ECs is presently classified into two main areas that are based

primarily on their mode of energy storage, namely: (i) the electrochemical double layer

capacitor also referred to as pseudo capacitors. The former stores energy (electricity)

3

in the form of electrostatic means that is typically the same way as a traditional

capacitor and secondly (ii), the redox supercapacitor exhibits reversible Faradaic-type

charge transfer and the resulting capacitance is not electrostatic in origin and hence

the name pseudo capacitors (Conway, 1999; Burke, 2000; Kotz. and Carlen, 2000).

Invoking the developmental pace of advanced materials such as nanostructured

transition metal oxides, carbons and electro-conductive porous polymers, the

electrochemical capacitor (EC) and the battery (lithium battery) will soon be rolled in

the same area of energy storage in which energy is paramount in the so-called hybrid

energy storage device. It is with the above-astounded advantages and applications in

mind, the present work was embarked at developing ECs using novel nanostructured

metal oxides and inexpensive nanoporous carbonaceous materials as potential

electrodes focusing on high power ECs in general and pulse power applications in

particular.

1.1 Research Background

Research activities have been intensified over the decades to identify plausible

materials as candidate electrodes for energy storage applications. The priority has

been given to high energy, easily available, cheap and environmental friendly material.

In view of the mentioned rationale for choice of materials, activated carbons are the

most commonly used electrode material in commercial supercapacitors (SCs) at

present. Carbon in its various forms is currently the most extensively examined and

widely utilized electrode materials in EDLCs with development focusing on achieving

high surface-area with low matrix resistivity. Carbons being an attractive as electrodes

for supercapacitors arise from a unique combination of chemical and physical

properties, namely: (Conway, 1999; Burke, 2000; Kotz and Carlen, 2000).

- High conductivity.

- High surface-area range (~ 1 to 2000 m2g-1)

4

- Good corrosion resistance

- High temperature stability

- Controlled pore structure

- Processability and compatibility in composite materials

- Relatively low cost.

Nevertheless, the first two of these properties are critical to the construction of

supercapacitors. As will be discussed, the properties of carbon allow both conductivity

and surface area to be manipulated and optimized. Carbon has four crystalline

(ordered) allotropes: diamond (obtained through sp3 hybridization), graphite (sp2

bonding), carbine (sp1) and fullerenes (distorted sp2 bonding) (Mc Enaney and

Burchell, 1999).

Due to the wide range of carbon materials and to avoid confusion, the term

‘carbon’ is typically used to describe the element rather than its form. Carbon blacks

are group of materials that are characterized by having near spherical carbon particles

of colloidal size, which are produced by the partial combustion or thermal

decomposition of hydrocarbons. The key properties of carbon blacks are considered to

be fineness (primary particle size) structure (aggregate size/shape), porosity, and

surface chemistry. Carbon blacks are routinely used as conductive agents in many

types of batteries and supercapacitor electrodes (Zheng, 1999; Osaka et al,1999;

Osaka et al, 1998; Liu and Osaka, 1997). The conductivity of carbon blacks is typically

in the range 10-1 to 102 (Ω cm-1) (Donnett et al, 1993). Supercapacitor electrodes have

been produced from high surface-area blacks (containing a binder) with specific

capacitances up to 250 Fg-1 (Richner et al, 2002). On the other hand, the “active”

carbons are obtained through carbonised organic precursor (a ‘char’) referred to as

activated carbons. Chars usually have a relatively low porosity and their structure

consists of elementary crystallites with a large number of interstices between them.

The interstices tend to be filled with ‘disorganized’ carbon residues (tars) that block the

pore entrances. Activation opens these pores and can also create additional porosity.

5

Activation can be done by means of two general categories: thermal activation and

chemical activation (Pierson, 1993; Bansal et al, 1988).

Yang et al (2002)employed a commercial activated carbon (AC) as electrodes

for SCs. In order to enhance more active sites within the pores, they performed a

secondary activation under steam in the presence of FeCl2 catalyst in the temperature

range of 800-950°C . Consequently, the re-activation of AC enhances both the specific

capacitance and high rate capability of electrochemical double-layer capacitors

(EDLCs). For AC treated under optimized conditions, its discharge specific

capacitance compared to the original AC, exhibits increase in capacitance up to 55.65

Fg-1, an increase of about 33% and the high rate capability was increased significantly.

On the other hand, Laforgue & Simon obtained more than 25 Fcm-2 per electrode, with

a time constant close to 3s, and power outputs compatible with automotive applications

using electrode composition: activated carbon and SFG44 (Laforgue and Simon,

2003).

The influence of pore size distribution in carbon material that τ in turn

improvises the accessibility of the pores to the electrolyte was studied by Frackowiak,

et-al, Endo et-al and Linares-Solano et-al. The mobility of ions within the pores is

different to the mobility of ions in the bulk of the electrolytic solution, and is greatly

influenced by pore size. If the pores are too small to allow easy access to electrolyte

ions they will not contribute to double-layer capacitance ( Frackowiak and Be´guin,

2001; Lozano-Castello et al, 2003; Endo and Maeda, 2001)

Nanoporous materials are a subset of porous materials, typically having large

porosities, and pore diameters between 1-100 nm. The definition of pore size

according to the International Union of Pure and Applied Chemistry (IUPAC) is that

micropores are smaller than 2 nm in diameter, mesopores 2 to 50 nm and macropores

larger than 50 nm. Prabaharan et al fabricated symmetric carbon/carbon

electrochemical capacitors employing mesoporous carbon black (MCB) powders

(nongraphitized) having modest surface area and studied their double layer

6

capacitance (Prabaharan et al, 2006). They observed rectangular shape cyclic

characteristics confirming the double layer behavior of these carbon electrodes. The

mechanism of double layer formation and frequency dependent capacitance were

deduced from the ac-impedance analysis. Specific capacitance, power density and

energy density were derived from constant current charge/discharge measurements.

MCB powders demonstrated a specific capacitance of about 39 Fg−1 and the power

density of 782Wkg-1 at a current density of 32 mAcm-2. The test cells demonstrated the

stable cycle performance over several hundreds of cycles. Interestingly, the measured

specific capacitance values obtained using the above methods are very much

comparable. The results suggest that the present mesoporous carbon could be useful

as candidate for the development of EDLCs.

There is considerable interest in the application of carbon nanotubes (CNTs) as

electrode materials for supercapacitors and other energy-storage devices (Lee et al,

2002). Nanotubes offer a new possibility for carbon electrodes, but least preferred due

to high manufacturing cost. Figure 1.1 shows the FE-SEM image of the as-grown

single walled CNT.

Fig. 1.1: FE-SEM image of the as-grown single walled CNT (An et al, 2001)

Considerable interest has also been shown in conducting polymer materials,

and research suggests that high specific capacitances could be attainable. Work at Los

Alamos National Laboratory has reported prototype polymer film capacitors with an

energy density of 39 Wh/kg and a power density of 35 kW/kg (Li et al, 2005)

7

The current trend in supercapacitor technology is called the hybrid

supercapacitor of an asymmetrical configuration in which a battery type electrode

replaces one activated carbon electrode (Li et al, 2005; Naoi et al, 2002; Sugimoto et

al, 2003). The battery electrodes accumulate charge through Faradaic electrochemical

process (redox reaction), which increases not only the specific capacitance of the

capacitor, but also extends the working voltage. This facilitates the energy density of

the capacitor is enlarged considerably. Generally, there are three categories of redox-

reaction materials are used in the hybrid supercapacitors nowadays, metal oxides,

conductive polymers and intercalation compounds. Transition metal oxides have

always been an attractive electrode material due to their low resistance and high

specific capacitance, but their excessive cost has generally ruled them out as a

commercially viable option. Traditionally a strong sulfuric acid has been used as an

electrolyte with metal-oxide electrodes in order to increase the ion mobility, and hence

the rate of charge/discharge is increased. This however limits the choice of electrode

materials because of the fact that most material becomes unstable and corrodes in a

strongly acidic electrolyte.

The most promising results seem to lie in the use of hybrid configurations,

which consist of activated carbons and conducting polymers or metal-oxides. Seung et

al (2003) prepared ruthenium/carbon composite materials by impregnating

ruthenium(III) acetylacetonate into a mesoporous carbon (average pore diameter = 12

mn, pore volume = 3.6 cm3/g) and then heat treated it at 320C for 2 h under an argon

atmosphere. The metallic ruthenium nanoparticles were converted to pseudo-

capacitive hydrous ruthenium oxide by electrochemical oxidation at 0.75V (versus

SCE) for 2 h in 2.0 M H2SO4. The specific capacitance of the composite electrodes,

which is the sum of the double-layer capacitance of mesoporous carbon and the

pseudo-capacitance of hydrous ruthenium oxide, reached 243 F/g with heavy loading.

The rate capability of composite electrodes also decrease with increase in ruthenium

loading, due to an increase in both the equivalent series resistance (ESR) and the

8

overall capacitance value. The ESR increment is caused mainly by the increase in the

electrolyte resistance within pores which, in turn, results from a pore narrowing with

ruthenium loading hindered by ionic motion in narrowed pores can explain this feature

(Seung et al, 2003).

Transition metal oxides like RuO2 and IrO2 exhibit faradaic pseudocapacitance

with capacitance reported to be as large as 760 F/g (Zheng et al, 1995). However the

high cost of these materials limits their commercialization. To circumvent the draw

back, metal oxides such as nickel oxide (Nam and Kim, 2002; Wang and Qin, 2002;

Srinivasan et al, 2000) cobalt oxide (Lin et al, 1998) and manganese oxides (Pang et

al, 2000) are studied because they are inexpensive and capable of exhibiting

pseudocapacitance behavior similar to that of RuO2 and IrO2. Nickel oxide has received

a considerable amount of attention over the last few years due to its large surface area,

and high conductivity pseudocapacitive behavior. It is applied in diverse fields, such as

smart windows, active optical fibers, catalysis (Sheela et al, 1995), electrochromic films

(Chigane and Ishikawa, 1992), fuel cell electrodes (Makkus et al, 1994), gas sensors

and others (Yoshimura et al, 1995).

NiO (Nickel Oxide) electrode has high resistivity, which is a serious drawback to

apply for practical applications to ECs. It is crucial to enhance the electrode

conductivity in order to improve the energy density and power density of electrodes.

Moreover, the specific surface area of electrodes is directly related to the specific

capacitance. However, the specific surface area of the NiO in general is not high

enough for high capacitance. The carbon nanotube has been known to yield high

conductivity and large specific surface area (Niu et al, 1997; Ray et al, 2002;

Frackowiak et al, 2001; An et al, 2001). With a view to improvise the electrode

conductivity of NiO, Nam et-al studied Nickel oxide/carbon nanotube (Ni1−xO/CNT) film

nanocomposite electrodes for electrochemical capacitors, which were prepared by

electrochemically precipitating nickel hydroxide onto a CNT film substrate and heating

9

it in air at 300°C. For comparison, nickel oxide thin film and nickel oxide/carbon paper

Ni1−xO/C paper electrodes were also prepared via electrochemical route. The nickel

oxide layers (~5 nm thickness) in the Ni1−xO/CNT film electrode were coated uniformly

on the surface of the individual CNTs, constructing a 3D nanoporous network structure

through the entire thickness of the film. In comparison to the thin film and Ni1−xO/C

paper electrodes, the Ni1−xO/CNT film electrode showed a very high specific

capacitance of ~1000 F/g with a high rate capability in 1M KOH. The high specific

capacitance and good power characteristics of the Ni1−xO/CNT nanocomposite

electrode can be attributed to the construction of an electrode with a very thin film of

electroactive materials with a nanometer thickness on a CNT film substrate with a 3D

nanoporous network structure (Nam et al, 2005).

Zhang et al synthesized nanocrystalline NiO by a simple liquid-phase process.

A specific capacitance approximately to 300 Fg-1 could be achieved with NiO in the

range of 0.0–0.5V (Zhang et al, 2004). Liu and Anderson studied the capacitance of

sol-gel derived NiO films heated in different atmosphere and concluded that the sample

annealed in air show only a slightly higher capacitance compared to the one heated in

pure nitrogen or oxygen (Liu and Anderson,1995).

Lee et-al (2005) have fabricated supercapacitor electrodes employing nickel

oxide (NiO)/carbon nanotubes (CNTs) nanocomposite formed by a simple chemical

precipitation method. The presence of CNT network in the NiO significantly improved (i)

the electrical conductivity of the host NiO by the formation of conducting network of

CNTs and (ii) the active sites for the redox reaction of the metal oxide by increasing its

specific surface area. In addition, it was also found that the power density and cycle life

were improved. Their work explained the simple chemical precipitation method for

formation of the NiO/CNT nanocomposite and the close relationship of specific surface

area and the specific capacitance of the composite. The CNTs in the NiO/CNT

nanocomposite form electrically conductive network, decreasing the electrical resistivity

10

of electrode materials, and thereafter decreasing the ESR of supercapacitors. The CNT

with high specific surface area is required to form high electrical double-layer

capacitance and more active sites for redox reaction of metal oxides. Their approach

created avenue for practical applications of metal oxides by improving the

electrochemical properties.

1.2 Justification of Study

Electrochemical capacitors (ECs) offer extended battery life in mobile

communications equipment using the battery/supercapacitor combination (Battery

Energy Saving Technology Capacitor). Additionally, it is suitable for use in hybrid

battery packs to reduce peak power on demand and extending the battery life.

It is a well known fact that rechargeable batteries such as lithium-ion and lithium

polymer though advanced cannot offer high power density as certain applications still

do demand power density. Example being the near future electric and/or hybrid

electric vehicle (EVs or HEVs) which require high power density devices for load

leveling. That is, to propel electrified vehicles, most of the energy is focused at the on-

board battery pack. Nevertheless, batteries cannot sustain high power during peak

powering and hence demands high power devices to compensate the peak power loss

during load leveling. EDLC or EC is the only choice to meet such peak power demand.

That is, EC can serve as a peak power provider in conjunction with high-energy

batteries. Therefore, this proposal aims at developing electrochemical capacitor

materials and devices based on carbon materials and metal oxide.

In the past, stored energy was provided by capacitor banks, which proved to be

bulky and more prone to failure. EC is needed where space was at a minimum. In this

sense, the focus of the present proposal has been designed carefully to address this

major issue and also to design and develop a high power EC for low voltage

applications at < 0.5 Hz (DC applications).

11

ECs are energy storage devices that display high pulse-power capabilities.

Various types of materials such as activated carbon (Osaka et al, 1999; Osaka et al,

1998; Bansal et al, 1988) highly crystalline carbon (Richner et al, 2002; Pierson, 1993)

carbon nanotube (CNT) (Lee et al, 2002; An et al, 2001; Niu et al, 1997 and An et al,

2001), transition metal oxides (Zhang et al, 2004; Lee et al, 2005) and conducting

polymers (Arbizzani et al, 1996) have been used as thin-film electrode materials for the

fabrication of ECs.

Nanostructured materials are found to demonstrate unique properties in terms

of electrode conductivity and particle to particle contact due to their nanometer sizes

where electron tunneling is quicker than micron-sized particles. The latter aspect is vital

for supercapacitor as it directly influence the equivalent series resistant (ESR) of the

cell. Therefore, employing nanosized particles as electrode for such application would

certainly help to achieving such high rate capability within the cell. It is in this context,

the present work has thus been justified as timely and important to develop such high

rate power sources namely hybrid supercapacitors. Obtaining uniform nanograin sizes

in metal oxide powders is a crucial challenge for material scientists. This requires an

appropriate synthesis approach. Therefore, the present work has been aimed at

developing uniform sized NiO spherical nano-sized particles with a view to enhancing

the electrode properties and characterizing its electrode-active qualities in

electrochemical supercapacitors.

The motivation for the present work thus far has been centered on the above

aspects focusing on the preparation of nanocrystalline metal oxide namely porous NiO

adopting a simple solvothermal approach and to characterize the metal oxide thus

obtained in an aqueous electrochemical cell (against a calomel reference electrode) to

determine its single electrode capacitance and in turn to use it as a positive electrode

against a mesoporus nanocomposite carbonaceous negative electrode fabricating a

hybrid supercapacitor namely NiO(+)/C(-) with a view to study the energy/power

density for pulse power applications.

12

1.3 Objectives of present research

Several objectives have been set for this study. They are: • To study the characteristics of commercially available mesoporous carbon based

similar electrode electrochemical capacitor - EM2K (Cabot), BP2K(Cabot) and

AB(Denka)

• To synthesize nanostructured transition metal oxide based on nickel and study the

nanostructure characteristics using FESEM, HR-TEM and XRD techniques for use

as electrodes for fabricating electrochemical capacitors

• To evaluate single electrode capacitance of the synthesized NiO using three

electrode measurements by employing aqueous electrolyte.

• To fabricate and test the hybrid capacitors with nanooxide/mesoporous carbon

asymmetric configuration using different electrochemical techniques

13

CHAPTER 2 LITERATURE REVIEW

2.0 Fundamental understanding

There are two major types of capacitors: fixed and variable. The fixed capacitor

has a specific value of capacitance while a variable capacitor allows for a range of

capacitance. Variable capacitors are designed so that capacitance can be changed

through a mechanical means such as adjusting a screw or turning a shaft. Variable

capacitors are used when the application requires an adjustment of capacitance such

as in a radio tuner.

Figure 2.1 shows the classification of different type of commercially available

capacitors. Fixed capacitors have capacitance values that cannot be physically

adjusted. They can be divided into electrostatic and electrochemical categories. In the

latter, electrolytic capacitors use either a solid or liquid electrolyte in their construction.

They have high capacitance values and offer the highest energy densities compared to

the conventional capacitors. These capacitors are inherently polar due to their

construction. A polar capacitor can only handle current flow in only one direction. The

electrochemical double layer capacitors are a new type of capacitors. These are also

known as ultra-capacitors or super-capacitors because their capacitance values can

measure as high as several hundred farads. These capacitors are used in battery-

assisted applications such as cell phones and electric vehicles (Conway, 1999).

14

Figu

re 2

.1:

Cla

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com

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9).

15

2.1 Current understanding of Electrochemical capacitors

2.1.1 Basic principle of a capacitor

A capacitor is commonly known as an electrical condenser. The amount of

electricity which a capacitor will hold depends on the electrical pressure or voltage

applied to the capacitor. The plates are charged with equal amounts of positive and

negative electrical charges, respectively. This is a "physical" storage of electricity and

is analogous with the "chemical" storage in a battery. A capacitor is said to be charged

when there are more electron on one conductor plate than on the other. If an electric

potential (voltage) is applied to the capacitor plates, the plates will become charged,

one positively and one negatively. The plate with the larger number of electrons has

the negative polarity. The opposite plate then has the positive polarity. When a

capacitor is charged, the energy is stored in the dielectric material in the form of

electrostatic field. When an electron is added to one plate of a capacitor, one electron

is driven away from the opposite plate. This phenomenon is known as the principle of

electrostatic induction. Figure 2.2 shows the principle of electrostatic induction in a

capacitor.

Figure 2.2: Principle of electrostatic induction (Conway, 1999).

16

2.1.1.2 Capacitance

Capacitors, regardless of type or kind, are all designated by their electrical size.

In capacitors, this electrical size is designated as capacity. The capacity of an electrical

capacitor is the ratio of the quantity of electricity and the electrical pressure or voltage.

In other words the capacity of a capacitor depends on the amount of electricity it will

hold at a certain electrical pressure or voltage. (Conway, 1999).

This ratio may be expressed as follows:

Q = CV ------- Eq. 2.1

Q = quantity of electricity

C = capacity of the capacitor

V = electrical pressure or voltage

By the same token the capacity may be expressed as follows:

C = Q / V ------- Eq. 2.2

Where the capacity is equal to the quantity of electricity divided by the electrical

pressure or voltage. The capacity of a capacitor is dependent upon the size and

spacing of the conducting plates and the type of insulating or dielectric medium

between the plates. It is known as capacitance.

C = ε A / d ------- Eq. 2.3

C = capacitance in farads, F

ε = dielectric constant

ε = εoεr

ε o is the space permittivity (8.854 x 10 –12 F/m2)

ε r is the relative permittivity

A = area of one plate in square meters, m2

d = distance between plates in meters, m

17

The capacitance is directly proportional to the surface areas of the plates, and

is inversely proportional to the separation between the plates. Capacitance also

depends on the dielectric constant of the substance separating the plates. The

standard unit of capacitance is the farad, abbreviated F. This is a large unit; more

common units are the microfarad, abbreviated μF (1 μF = 10-6 F) and the picofarad,

abbreviated pF (1 pF = 10-12 F). The greater the area for storing charge, and the closer

the separated charges, the greater is the capacitance.

2.1.2 Electrochemical Capacitor

2.1.2.1 The Electrochemical Double Layer Capacitor

As mentioned briefly in the earlier literature review, ELDCs or ECs store

charges in the electrode/ electrolyte interface. High surface area electrodes are used in

electrochemical capacitors resulting in large double layer capacitance, and much of the

storage capacity which is due to the charging/discharging of the double layer. At some

surface oxidation/reduction also occurs, but in contrast to reactions occurring in

batteries, this is limited to a monolayer or two on the electrode surfaces. Consequently,

the device behaves more like a capacitor than a battery. EDLC is also called

"supercapacitor" (SCs) and "ultracapacitor" depending upon the materials and

electrodes used. EDLC typically have much larger power density but much smaller

energy density than batteries. Charge is stored electrostatically in polarized liquid

layers between an ionically conducting electrolyte and an electrochemically-conducting

electrode. This energy storage mechanism is either based on capacitive (non-faradic)

or pseudocapacitive (faradic) which will be discussed later (Conway, 1999).

.

18

2.1.2.2 Concept of Electrochemical Double Layer Capacitor

Electrochemical double layer capacitor stores energy using the double layer

concept. This double layer is realized when two electrodes immersed in an electrolyte,

are polarized. The polarized charges at both the positive and negative electrodes

resemble two capacitors connected in series (see Figure 2.3).

Figure 2.3: Behavior of electrolyte in ion ( positive charge) in the pore when charged and discharge

Analyzing the exploded view of the individual electrode, Helmhortz has

identified the existence of a 'double layer' in the electrochemical cell in 1879. And it is

named after him as Helmholtz layer. There are several theoretical models that describe

the structure of the double layer such as the Gouy-Chapman model, and the Gouy-

Chapman-Stern model. However the most common one would be the Helmholtz

model.

Helmholtz double layer is a structure of charge accumulation and charge

separation that always occurs at the interface when an electrode is immersed into an

19

electrolyte solution. This layer is formed as the solvated ions are blocked and

accumulated at the electrode/electrolyte interface. This would create a charge

separation between the solvated ions and the electrode material that resembles the

charge storage mechanism similar to conventional capacitor, where d is distance

between conducting plate and insulating material. Refer Equation 2.3. In general,

positive and negative charges are arrayed at counter position with an extremely short

distance, such as atomic distance (~ 10 Å), between both at the contact interface of

two different phases where, in this case, the two phases would be the solid carbon

electrode and the electrolyte. This interfacial charge distribution layer is explained as

the helmholtz layer in Figure 2.4. The excess charge on the electrode surface is

compensated by an accumulation of excess ions of the opposite charge in the solution.

This structure behaves essentially as a capacitor as it possesses the double layer. The

amount of charge is a function of the electrode potential. Figure 2.5 illustrates the

electrode potential before and after charging. The charges are polarized at the

interface forming the helmholtz layer. Thus creating a electrical potential which was be

observed after the charging (Conway, 1999; Burke, 2000; Kotz and Carlen, 2000).

Figure 2.4: Helmholtz double layer

20

Figure 2.5: Typical distribution of charges at the interface and its electrode potential before and after charging (Conway, 1999).

2.1.2.3 Non-Faradaic

The charge accumulation is achieved electrostatically by positive and negative

charges residing on two interfaces separated by a vacuum or a molecular dielectric

(the double layer or, e.g., a film of mica, a space of air or an oxide film, as in electrolytic

capacitors) (Conway, 1999).

2.1.2.4 Faradaic

The charge storage is achieved by an electron transfer that produces chemical

or oxidation state changes in the electroactive materials according to Faraday’s laws

(hence the term) related to electrode potential. This is known as pseudocapacitance in

ECs. The energy storage is indirect and is analogous to that in a battery. In a battery

cell, every electron charges is Faradaically neutralized by charge transfer, resulting in a

charge of oxidation stage of some redox-electroactive reagent, e.g., Ni3+ O2- OH- + e +

H+ → Ni2+ 2OH- in the cathode of an Ni-Cd battery (Conway, 1999).

The electrons involved in a double-layer charging are the delocalized

conduction-band electrons of the metal or carbon electrode, while the electrons

involved in Faradaic battery-type processes are transferred to or from valence-electron

states (orbital) of redox cathode or anode reagent, although they may arrive in or

21

depart from the conduction-band states of the electronically conducting support

material. In certain cases, the faradaically reactive battery material itself is metallically

conducting (e.g., PbO2, some sulfides, RuO2 (Trasatti and Buzzanca, 1971) or else is a

well-conducting semiconductor and a productor, e.g., NiOOH (Oliva et al, 1982).

2.1.2.5 Characteristics of Electrochemical Double layer Capacitor

Some of the main characteristic of EDLC (Conway, 1999);

It employs carbon or metal oxides as the material for the electrodes

Its capacitance values can be measured as high as several hundreds of Farads

(F)

Fast charge time up to a few seconds

High specific power density compared to batteries ( at least two order of

degree) but specific energy density is one order less than batteries.

It can be charged to any voltage within its voltage rating.

Stores much more energy than a conventional capacitor of similar size.

Able to deliver frequent pulses of energy without any detrimental effects unlike

batteries which experience reduced life if exposed to frequent high power

pulses

Can be charged extremely fast while batteries are damaged by fast charging.

Can be cycled hundreds of thousands of times unlike batteries which are

cyclable only up to few hundred cycles.

No charge circuit (Self charge)

No explosion risk

It requires no maintenance and is robust to environmental extremities such a

arctic temperatures.

Wide temperature range ( operation )

Pollution free

No liquid leak (if properly sealed)

22

2.2 Classifications of Electrochemical capacitors

2.2.1 Supercapacitor , Pseudocapacitor, Hybrid Capacitor

As mentioned earlier, ultracapacitors, supercapacitors, powercapacitor and

pseudocapacitors are also known as other names for double layer capacitor which are

established colloquial names. They are named duly by the cell performance. The term

“super” capacitor is most commonly used for carbon based double layer capacitors

because of its high capacitance value. On the other hand, double layer capacitors with

metal oxide electrodes are known as hybrid electrochemical capacitors / ultracapacitors

for their very low equivalent series resistance value (ESR). It is also known as

pseudocapacitor if it exhibits pseudocapacitance behaviour ( faradaic reaction like in

battery). Figure 2.1 is the summary of classification of capacitor.

2.2.2 Pseudocapacitance

There are two basic reactions, which lead to electrochemical cell. Both occur at

the interface between a conductor and an electrolyte and both benefit from very high

specific surface areas at the electrode. Surface areas around 2,000 m2/g are

commonly available for carbons while 140 m2/g commonly available for ruthenium

oxide (metal oxide). The first mechanism commonly referred to as charge separation,

which is well documented as a non-Faradic mechanism and is the basis for EDLC. The

charges are basically blocked at the electrode/electrolyte interface, preventing the

charges to diffuse. The second reaction commonly referred to as an oxidation-

reduction reaction (redox) due to faradic mechanism, which is the basis for

pseudocapacitance. In here, the charges are partially blocked where some charges

diffuse into the electrode material and intercalate. The term pseudocapacitor is

commonly used to explain the pseudocapacitance behaviour of such double layer

capacitors. Carbon is an example of a charge separation of non-Faradic electrode

23

material and ruthenium oxide is an example of faradic electrode material (Conway,

1999).

Although, pseudocapacitor has electrochemical reaction similar to battery (the

faradic mechanism), the distinction between a battery and an electrochemical double

layer capacitor is not explicit. A battery relies on electrochemical reactions that involve

active materials in the electrode, where the charges are not blocked, diffuse into the

material and intercalate. In this case, active means that the materials participate in the

reaction, and a transfer of electrons between the active material and ionic species in

solution occurs across the solid/liquid interface. On the other hand, in an "ideal"

electrochemical capacitor that utilizes carbon or metal oxides, the electrodes play

passive role. That is, the electrode surface only participates by serving as sites for

charged species to accumulate and no electron transfer occurs across the

solid/liquidinterface. In a "practical" electrochemical capacitor there may occur some

surfaceoxidation/reduction on the electrodes, that is, it operates partly as a capacitor

and partly as a battery. Of course, this phenomenon is depends on the material

properties. So, in order to characterize a double layer capacitor, one has to investigate

the above behavior (Conway, 1999).

The metal oxide technology of the pseudocapacitor utilizes an electrochemical

reaction similar to battery technology for energy storage, thus improving potential

energy density. Since the pseudocapacitor uses a dense metal oxide as the electrode

material, the load of the oxide is three times that of the EDLC for the same-coated

area. With this advantage, pseudocapacitor cell needs to be only 60% in volume as

compared to an EDLC of the same capacitance. Conversely, it also means the

pseudocapacitor holds 80% more energy than the equivalent-size EDLC. Finally, the

pseudocapacitor uses the same manufacturing processes and facilities as EDLC

production.

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2.2.3 Hybrid Capacitor

A hybrid capacitor is a double layer capacitor fabricated with one electrode

purely double layer (carbon based as the negative electrode) and another electrode

with pseudocapacitance (e.g., metal oxide based as the positive electrode). The energy

density of these devices is found to be significantly higher than that of pure EDLCs.

Like the activated carbon cathode in EDLC, an activated carbon in the cathode of the

hybrid capacitor absorbs anions at the electric double-layer and linearly polarizes to

positive side in the charging process. On the other hand, as shown in Figure 2.6, a Li-

doped graphite in the anode of the hybrid capacitor that intercalates Li+ ions into its

interlayer in the charging process and de-intercalates Li+ ions in the discharging

process. When the anode is charged, potential of the anode becomes very negative

and approaches the deposition potential of Li-metal anode as illustrated in Figure 2.6.

Figure 2.6: A Li-doped graphite in the anode of the hybrid capacitor that intercalates Li+ ions into its interlayer in the charging process and de-intercalates Li+ ions in the

discharging process (Pasquier, A. et al, 2001).

The voltage is largely developed at anode but negligibly at cathode. Voltage

developed in the electrolyte is due to a solution resistance the so-called ohmic drop (IR

drop). The voltages developed at each electrode are made from resulting charge

stored and electrode capacity. Because the cathode capacity is much larger than that

of anode, voltage development occurs mostly at anode when a cell is charged. Figure.

2.7 indicates the working principle of a hybrid capacitor. The single-cell hybrid capacitor

can withstand high voltages due to the nature of the anode. In contrast, the cell voltage