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Run Run Shaw Library, City University of Hong Kong.
Title Hydrogen evolution involved electrodeposition of Cu-Ni alloys and
dealloying for supercapacitor application
Author(s) Lee, Sin Ching (李倩晴)
Citation
Lee, S. C. (2016). Hydrogen evolution involved electrodeposition of Cu-Ni alloys and dealloying for supercapacitor application (Outstanding Academic Papers by Students (OAPS)). Retrieved from City University of Hong Kong, CityU Institutional Repository.
Issue Date 2016
URL http://hdl.handle.net/2031/8808
Rights This work is protected by copyright. Reproduction or distribution of the work in any format is prohibited without written permission of the copyright owner. Access is unrestricted.
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CITYU UNIVERSITY OF HONG KONG
DEPARTMENT OF
PHYSICS AND MATERIALS SCIENCE
BACHELOR OF SCIENCE (HONS) IN APPLIED PHYSICS 2015-2016
DISSERTATION
Hydrogen Evolution Involved Electrodeposition of Cu-Ni Alloys and
Dealloying for Supercapacitor Application
By
LEE Sin Ching
March 2016
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Hydrogen Evolution Involved Electrodeposition of Cu-Ni Alloys and
Dealloying for Supercapacitor Application
By
LEE Sin Ching
Submitted in partial fulfillment of the
requirements for the degree of
BACHELOR OF SCIENCE(HONS)
IN
APPLIED PHYSICS
From
City University of Hong Kong
March 2016
Project Supervisor: LI, Yangyang
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Abstract
Previous research shows that porous nickels with closely packed tiny pores can be neither fabricated
by the method of electrochemical deposition nor the method of hydrogen bubble dynamic template.
Therefore, a combined method of electrodeposition and hydrogen evolution reaction is proposed
and which will be the main focus of this study.
This project is divided into three parts. The first part is the fabrication of porous nickel by the
combined method in different conditions. Second part is the fabrication of porous nickel with nickel
hydroxide by undergoing hydrothermal treatment. For the last part, samples were characterized by
SEM, XRD, CV and charge and discharge tests.
The results indicate that using this combined method can also fabricate porous nickels which have
high surface area. Also, because the nickel oxide is already formed in electrodeposition stage, this
method is convenient for making supercapacitors by just using one step. Last but not least, porous
nickel fabricated by this method has high specific capacitance and high retention. Therefore, this
method is potentially to be applied to large-scale fabrication of supercapacitors to be used in
industry.
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Acknowledgements
I would like to express my deepest appreciation to those who extended their helping hand to me to
complete this report. Especially, I would like to express my gratitude to my supervisor Dr. LI,
Yangyang for offering me an opportunity to learn from her. I would like to thank my second
assessor Dr. FAN, Jun for giving her precious advice to improve my project in different aspects. I
would also like to thank my tutor Mr. LI, Zhe for giving me a clear guidance and many supports.
Last but not least, I would like to thank Mr. Maurice Chan and Ms. Conny Yau for giving me a lot
of supports and suggestions on writing the essay.
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List of Figures
Figure 1 Hive like porous metal
Figure 2 Randomly distributed pores
Figure 3 Method of inverse opal
Figure 4 Porous nickel fabricated by method of hydrogen bubble template
Figure 5 Porous nickel fabricated by method of hydrogen bubble template
Figure 6 Contact Angle of Porous Nickel
Figure 7 The first supercapacitor in the world
Figure 8 SEM micrographs of
a) electrochemical dealloying b) hydrogen bubble dynamic template
Figure 9 SEM micrographs of electrodeposition at -1.4V
a) before dealloying b) after dealloying
Figure 10 SEM micrographs of electrodeposition at -1.5V
a) before dealloying b) after dealloying
Figure 11 SEM micrographs of electrodeposition at -1.6V
a) before dealloying b) after dealloying
Figure 12 XRD of different voltage of electron deposition in the range of 25°to 55°
Figure 13 XRD of different voltage of electron deposition in the range of 42.5°to 45.5°
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Figure 14 SEM micrographs of sample
a) 2-2-1 b) 2-2-2 c) 2-2-3 d) 2-2-4 e) 2-2-5
Figure 15 CV curve of sample 2-2-1
Figure 16 CV curve of sample 2-2-2
Figure 17 CV curve of sample 2-2-3
Figure 18 CV curve of sample 2-2-4
Figure 19 CV curve of sample 2-2-5
Figure 20 C-DC curve at different current densities of porous nickel with hydrothermal treatment
Figure 21 C-DC curve at different current densities of porous nickel without hydrothermal treatment
Figure 22 Specific capacitance of sample with hydrothermal treatment
Figure 23 Specific capacitance of sample without hydrothermal treatment
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List of Tables
Table 1 Comparison of technical characteristics of EES system
Table 2 Voltage and Time Used for Fabrication
Table 3 Formulation of Solution for HT
Table 4 Temperature and Time Duration for HT
Table 5 Conditions of C-DC for 2-2-4
Table 6 Conditions of C-DC for 2-2-6
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Table of Contents
Abstract----------------------------------------------------------------------------------------------------------- I
Acknowledgements-------------------------------------------------------------------------------------------- II
List of Figures---------------------------------------------------------------------------------------------- III-IV
List of Tables--------------------------------------------------------------------------------------------------- V
Table of Contents------------------------------------------------------------------------------------------- VI
1 Introduction-------------------------------------------------------------------------------------------------- 1
1.1 Porous Metals---------------------------------------------------------------------------------------- 1
1.2 Porous Nickel---------------------------------------------------------------------------------------- 1
1.3 Supercapacitor--------------------------------------------------------------------------------------- 1
1.4 Research Gap----------------------------------------------------------------------------------------- 2
1.5 Objective---------------------------------------------------------------------------------------------- 2
2 Literature Review------------------------------------------------------------------------------------------- 3
2.1 Porous Metal-------------------------------------------------------------------------------------- 3-6
2.2 Porous Nickel-------------------------------------------------------------------------------------- 7-8
2.3 Supercapacitor----------------------------------------------------------------------------------- 8-10
3 Experimental Procedure-------------------------------------------------------------------------------- 11
3.1 Fabrication of Porous Nickel Thin Film--------------------------------------------------- 11-12
3.2 Hydrothermal Treatment--------------------------------------------------------------------- 12-13
3.3 Testing----------------------------------------------------------------------------------------------- 14
3.3.1 Scanning electron microscope------------------------------------------------------------- 14
3.3.2 X-ray Diffraction---------------------------------------------------------------------------- 14
3.3.3 Cyclic Voltammetric Curve------------------------------------------------------------ 14
3.3.4 Charge and Discharge------------------------------------------------------------------- 14-15
4 Results and Discussion----------------------------------------------------------------------------------- 16
4.1 Porous Nickel-----------------------------------------------------------------------------------16-19
4.2 Porous Nickel and Nickel hydroxide---------------------------------------------------------19-24
4.3 Supercapacitor----------------------------------------------------------------------------------14-27
5 Conclusion--------------------------------------------------------------------------------------------28
6 References----------------------------------------------------------------------------------------------29-32
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1. Introduction
With the popularization of electronic devices, development of technology and
increasing concern of environmental protection, it is important to study and develop the
technique of energy storage and conversion.
1.1 Porous Metals
Porous metals are also called nanoporous metals [1]. It is known for its large surface area
[2], high surface reaction activity, and excellent electrical conductivity [3]. The major
methods of fabricating porous metals, or rather porous nickels, include inverse opal
template [4], hydrogen bubble dynamic template [5], electrochemical dealloying [6] and
etc.
1.2 Porous Nickel
Porous nickel is a multifunctional material which has been used in many aspects. For
example, it has been applied in optical devices [7], photonic coatings [8], biosensors [9],
catalysis [10], water proof coatings [3] and so on. Besides, one of its most important
applications is serving as a 3-D substrate for loading electro-active materials and the
current collector for supercapacitor.
1.3 Supercapacitor
Supercapacitor can be divided into two types, faradaic supercapacitor [11] and electrostatic
supercapacitor [12]. The advantages of a supercapacitor are high power density, high
charging and discharging rate, [12] and long life expectancy [13]. Therefore,
supercapacitor is an important technology of developing green energy as it can act as a key
role of energy storage and conversion along with a battery.
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1.4 Research Gap
From the previous researches it indicates that, the porous nickel fabricated using the method
dealloying electrochemical deposited Cu-Ni alloy, the pore size is decreased when
decreasing the voltage, also, the pores are loosely packed [5]. In another aspect, the method
of hydrogen bubble dynamic template can only form very large pores porous nickel [6] and
the lower specific surface area which is unwanted for making supercapacitors. Therefore, in
order to make a porous nickel thin film of high porosity and surface area which tiny porous
are closely packed, a combined method of electrodeposition-dealloying and hydrogen
evolution reaction is proposed which will be the main focus of this study.
1.5 Objectives
The purpose of this study is combining Cu-Ni alloy electrodeposition and hydrogen
evolution reaction, followed by dealloying, to fabricate porous nickel. We will then
characterize the material and make it into supercapacitor for test. The steps are:
1. To fabricate porous nickels by using the combined method of electrodeposition and
hydrogen evolution reaction. After the fabrication, some of the samples will be
chosen to undergo hydrothermal treatment to grow nickel hydroxide in order to
enhance the performance.
2. To characterize material by using SEM, XRD and related electrochemical test
techniques.
3. To exam the supercapacitor performance by comparing the results and data.
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2. Literature review
2.1 Porous metals
Porous metals have been studied since the 1920s. It is a kind of metal that has a lot of pores.
The pores not only can be observed on the surface of the porous metal but also lie inside it.
Moreover, the pores can be manipulated into different shapes, such as hive (Fig.1); they can
also distribute randomly (Fig.2). The materials for making porous metals can be pure metals,
metal alloy and metal oxide [14], [15].
Figure 1 Hive like porous metal[16] Figure 2 Randomly distributed pores
[By:P. Müllner et al., Northwestern University. ]
The porous metal is a kind of porous material. According to International Union of Pure and
Applied Chemistry guidelines, porous materials can be characterized into three types.[17]
When the pore size is larger than 50 nm, it is called macroporous. For pore size between 2
nm and 50 nm, it is called mesoporous. Lastly, when the pore size is smaller than 2 nm, it is
called microporous [18]. Porous metal is the metal that has meso or macro sized pores. On
the other hand, with the development of nanoscience, it is defined that things with size
between 1 nm to 100 nm, are measured on a nano scale. Therefore, we can also called
porous metal nanoporous metal generally.
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There are two ways of making porous metals. The first method involves the use of template
[19], such as Triblock-Copolymer-Assisted Hard-Template Method [20], Method of Inverse
Opal Template and Hydrogen Bubble Dynamic Template. The second one is without using
template, for instance, Chemical Dealloying and Electrochemical Dealloying. With the
development of nanotechnology, a new method of making porous nickels, the method of
Lift-off-Free Nanofabrication, was discovered by Lawrence Livermore National Laboratory
in November of 2014 [21].
For method of inverse opal template, colloidal crystal is formed by array of colloids with a
tidy arrangement. In this method, colloidal crystal acts as the template. The empty space
between the colloidal particles is filled by nanoparticles. Lastly, the template is removed
and the porous metal is formed. Using this method, the arrangement of pores and pores size
can be easily controlled by making changes on the template (Fig.3)[4], [22], [23],[24],[25]
.
Figure 3 Method of inverse opal [4]
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For method of hydrogen bubble dynamic template, the porous metal is made by applying a
strong current in the cathode; hydrogen bubbles are then formed, and at the same time the
metal deposition occurs rapidly. It is called dynamic template because of the decreasing of
hydrogen ions content in the solution, due to the formation of hydrogen bubbles, which
affects the electrodeposition process. The porous nickel formed by this method has large
pore size which is about 10μm (shown in figure 4) [5], [26].
Figure 4 Porous nickel fabricated by method of hydrogen bubble template [5]
The method of electrochemical dealloying consists of two parts, electrodeposition and
dealloying. Using CuNi as an example, during energy deposition, the compound of CuNi is
formed on the working electrode, which is basically a piece of Indium-Tin Oxide (ITO)
glass. In the process of dealloying, the copper of CuNi dissolves back to the solution and
forms copper on the side of the counter electrode. Therefore, only nickel with pores will
stay at the electrode and becomes porous nickel. The voltage used is usually above -1.2V
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because at -1.3V hydrogen evolution reaction occurs, it becomes the combined method of
electrodeposition and hydrogen evolution reaction. For the method of electrochemical
dealloying, the pore size and density of pores decreases by decreasing the voltage of
deposition. Figure 5 shows a porous nickel with loosely packed tiny pores which fabricated
at -1.2V [6], [27], [28].
Figure 5 Porous nickel fabricated by method of hydrogen bubble template
Hydrothermal treatment is conducted at high temperature and high pressure. The sample
will be put into an autoclave with set temperature and pressure for a period of time. In 2014,
Feng et al. did an experiment which showed that by using hydrothermal treatment Ni (OH)2
grow on the thin film and it turns out to be a high performance pseudocapacitor electrode
with specific capacitance 1778 F g-1 at a current density of 2.5 A g-1 [29], [30].
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2.2 Porous Nickel
Nickel has high resistance to corrosion, and it is also catalysis for hydrogenation reaction
[31]. Porous nickel is a kind of porous metal which is very hard and has good resistance
[10]. Furthermore, porous nickel provides a large surface area because of its porous
structure [3].
Porous nickel is used in many applications because of its properties, for example, in optical
devices [24], waterproof coatings, sensor and supercapacitor [32], [33]. The application of
making supercapacitors will be the focus of this project.
According to Cheng at el. [2], porous nickel can be used to make optic devices. In their
research, porous nickel was made by using porous silicon as a template. With the
dissolution of silicon, part of silicon was replaced by nickel, porous nickel was formed. It is
discovered that porous nickel gives out various responses in the range of visible spectrum
and shows the ability of optical sensation. It is a good material of being optical device. Also,
it can absorb light and reduce the noises because of its rough surface.
Porous nickel has good wettability. Gu and Tu have discovered that porous nickel thin film
has a super hydrophobic surface, without any modifications, which increases the corrosion
resistance. The measurement of wettability shows the water contact angle is more than 160°,
which proves the high waterproof capability of porous nickel (Fig.6) [10]
.
Figure 6 Contact angle of porous nickel [10]
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A research has been done by Lu et al. that porous nickel can be used as a sensor for glucose,
which helps to detect the glucose level for diabetes patients [3]. Porous nickel has a large
electrochemical active surface and high electrocatalytic activity. You et al. have found that
using porous nickel gives better result on the stability and sensation of glucose as compared
with other metals [25], [34].
2.3 Supercapacitor
A supercapacitor is similar to a battery which acts as an energy storage. It has been widely
studied since the 1990s [12]. The earliest supercapacitor was investigated in 1957 by Becker.
(as shown in Fig. 7) [35].
Figure 7 The first supercapacitor in the world [35]
Supercapacitors can be classified into two types, faradaic supercapacitor and electrostatic
supercapacitor [12]. The main difference between these two types of superconductors is that
during the charging and discharging process, faradaic supercapacitor undergoes chemical
reactions, such as redox reaction. On the other hand, electrostatic supercapacitor does not
undergo any chemical reactions [36], [37]. A faradaic supercapacitor is also called a
pseudocapacitor. It is chemically active. Similar to normal batteries, by the time charging
and discharging, redox reaction occurs. During the process, the charges are directly stored.
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Also, because of this reaction, the faradaic current is generated. Compared with an
electrostatic supercapacitor, it has higher capacitance and higher energy density, about
10-100 times greater [11], [38]. In an electrostatic supercapacitor, there is no chemical
reactions occur. During the charging process, the positive ions move to the negative side
and the negative ions move to the positive side. Opposite phenomenon occurs when it
undergoes discharging.
Compared to faradaic supercapacitor, electrostatic supercapacitor has higher power density
and stability. The higher power density is due to the relatively long duration needed for
faradaic supercapacitor to process charging and discharging. According to the equation,
power is inversely proportional to time, as the time needed for faradaic supercapacitor to
charge and discharge is longer than that for electrostatic supercapacitor.
Although faradaic supercapacitor has higher energy density, its power density is lower.
Electrostatic supercapacitor also has higher stability because its concentration of electrolyte
remains unchanged. On the contrary, the concentration of faradaic supercapacitor is not
stable because of the occurrence of redox reaction.
Low energy density is one of the disadvantages of supercapacitors as compared with
batteries. The energy density of a supercapacitor is about 5 Wh/kg and that of a battery is
more than 50 Wh/kg [12]. For supercapacitors, the energy density is proportional to the size
of the capacitor. For event that requires large storage amount of energy, a large
supercapacitor has to be built. This increases the production cost. High discharging rate is
also another problem. The daily self-discharging rate of a supercapacitor is about 20-40%
which is very high (Table 1). The disadvantage will be one of the major aspects affecting
the efficiency of the application of supercapacitor.
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Table 1 Comparison of technical characteristics of EES system [39]
One of the advantages of supercapacitor compares with batteries is high power
density. Compared with batteries, supercapacitors have higher power density which is
about 1000-10000 W/kg. On the other hand the power density for batteries is about 150W
[12]. The power density of supercapacitors is about 10-60 times higher than that of
batteries.
Also, the charging and discharging time is much shorter for supercapacitors comparing with
batteries. For instance, the time needed to fully charge and discharge of a supercapacitor is
about 30 seconds; however, it takes about an hour to charge a battery [12].
Furthermore, supercapacitors have longer life expectancy than batteries. A supercapacitor
can conduct over 500000 charge-discharge cycles and the life expectancy is predicted as 30
years. However, the life expectancy of a battery is about 5-10 years and can only conduct
10000 cycles [13].
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3. Experimental Procedures
3.1 Fabrication of Porous Nickel Thin Films
Preparation of Solution
The solution contained 0.5M of Ni (NH2SO3)2 · 4H2O, 0.05M of Cu(H2O)4SO4 · H2O,
0.6M of H3BO3 , 0.1g of saccharin and water. Saccharin was used to fabricate more uniform
porous nickel.
Electrodeposition and Dealloying
Indium-Tin Oxide (ITO) glass was used as working electrode. Platinum was used as counter
electrode. Working electrode and counter electrode were parallelly placed 2cm apart. A
reference electrode, (saturated calomel electrode) SCE was used.
In this method six samples were made. For sample 1-1 and 1-2, -1.4V of voltage with
duration of 10C of cathodic charge was used in the part of electrodeposition. For sample 2-1
and 2-2, -1.5V of voltage with duration of 10C of cathodic charge was used. For sample 3-1
and 3-2, -1.6V with duration of 10C of cathodic charge was used. After energy
electrodeposition, sample1-2, 2-2 and 3-2 were dealloyed at +0.5V for 10 minutes (or until
the voltage dropped to 10-4A). These conditions were set up to determine the influence of
voltage and time when making porous nickel (Table 2).
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Table 2 Voltage and Time Used for Fabrication
Electrodeposition Dealloying Sample Voltage Cathodic voltage Voltage Duration
1-1
1-2-1.4V
+0.5V 10min
2-1
2-2-1.5V
+0.5V 10min
3-1
3-2-1.6V
10C
+0.5V 10min
3.2 Hydrothermal Treatment (HT)
In this part, 2-2 was chosen to be studied. Six porous nickel thin films with same fabrication
condition as 2-2 were made. They underwent HT in different conditions, including solution
(Table 3), temperature and time duration (Table 4).2-2-6 was used as reference sample.
Preparation of solution
For HT five solutions were prepared. For sample 2-2-1, 2-2-2 and 2-2-4 , the
solution contained 0.02M of Urea, 0.005M of NiSO4.4H2O and water. For sample 2-2-3,
the solution contained 0.01M of Urea, 0.005M of NiSO4.4H2O and water. For sample
2-2-5, the solution contained 0.02M of Urea, 0.005M of NiSO4.4H2O and water; also,
NH3.H2O (28% weighted percentage) was added until it turned blue (0.1mL). Sample 2-2-6
worked as control set up, it did not undergo hydrothermal treatment. The formulation of the
solution is shown in Table 3.
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Table 3 Formulation of Solution for HT
Sample Chemical Concentration Amount of making
25mL
Urea 0.02M 30mg 2-2-1
NiSO4.4H2O 0.005M 40mg
Urea 0.02M 30mg 2-2-2
NiSO4.4H2O 0.005M 40mg
Urea 0.01M 15mg 2-2-3
NiSO4.4H2O 0.005M 40mg
Urea 0.02M 30mg 2-2-4
NiSO4.4H2O 0.005M 40mg
Urea 0.02M 30mg
NiSO4.4H2O 0.005M 40mg 2-2-5
NH3.H2O (28% weighted %) / 0.1mL
2-2-6
Settings of Autoclave
Different temperatures and time durations were used in the samples which shows in table 4.
Table 4 Temperature and Time Duration for HT
Sample Temperature Time Duration
2-2-1 100°C 6 hour
2-2-2 100°C 12 hour
2-2-3 100°C 12 hour
2-2-4 120°C 6 hour
2-2-5 100°C 12 hour
2-2-6
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3.3 Characterization
3.3.1 Scanning Electronic Microscope (SEM)
SEM had been done in order to check the geometry of porous nickel thin films. During this
process, 5kV of accelerating voltage was used. SEM micrographs of 1-1 to 3-2 and 2-2-1 to
2-2-5 of magnification of 1000X, 5000X and 10000X was taken.
3.3.2 X-ray Diffraction (XRD)
XRD had been done in order to check the chemical components contained inside the sample.
The results are important for determining whether nickel hydroxide had grown on porous
nickel at the stage of electrodeposition and indicate the changes of component before and
after dealloying.
3.3.3 Cyclic Voltammetric Curve (CV)
CV was used to check the performance of storing charges. The CV curve of supercapacitor
usually has a pair of redox reaction peak. Also, if it has larger CV curve enclosed area; it
means it has higher performance. CV had been done for both before HT and after HT of
sample 2-2-1 to 2-2-5. It was done the under highest voltage of 0.7V and scan rate of 0.1
V/s with 6 segments.
3.3.4 Charge and Discharged Curve (C-DC)
C-DC had been done in order to check the charging and discharging time and calculate the
specific capacitance of porous nickel. Sample 2-2-4 and 2-2-6 were chosen to undergo this
test with the following conditions (see Table 5 and Table 6).
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Table 5 Conditions of C-DC for 2-2-4
Sample Number of cycles Current Density
1000 cycles 5 mAcm-2
300 cycles 10 mAcm-2
300 cycles 5 mAcm-2
5 cycles 10 mAcm-2
5 cycles 5 mAcm-2
5 cycles 2 mAcm-2
2-2-4
5 cycles 1 mAcm-2
Table 6 Conditions of C-DC for 2-2-6
Sample Number of cycles Current Density
1000 cycles 5 mAcm-2
300 cycles 10 mAcm-2
300 cycles 5 mAcm-2
5 cycles 10 mAcm-2
5 cycles 5 mAcm-2
5 cycles 2 mAcm-2
2-2-6
5 cycles 1 mAcm-2
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4. Results and Discussion
4.1 Porous Nickel
Figure 8a) and figure 8b) show the SEM micrograph of porous nickel which fabricated by
method of electrochemical dealloying at -1.2V and hydrogen bubble dynamic template
respectively. From figure 8a) it reveals that the porous nickel fabricated by method of
electrochemical dealloying had small pore size, about 0.6μm. Besides, all the pores are
loosely packed. On the contrary, figure 8b) shows that large porous size, about 10μm,
porous nickel with a closely packed arrangement can be form by method of hydrogen
bubble dynamic template. Compare with the graphs in figure 8, figure 9 to figure 11 show
that porous nickels with small pore size and high density of pores can be fabricated by the
combined method of electrodeposition and hydrogen evolution reaction, which means that
they have higher surface area.
Figure 9 to figure 11 show the morphology of CuNi thin films and porous nickels. In figure
9a), the CuNi thin film was formed at -1.4V, large ball shaped CuNi were spread all over
the thin film. After dealloying, pores were formed on thin film. The measured pores
diameter was between 100-500nm (shown in figure 9b)). From figure 10a), the CuNi thin
film was formed at -1.5V, small grainy CuNi were uniformly distributed on the thin film.
Figure 10b) shows that after dealloying, the feature size of the pores in the porous nickel
thin film is also around 100-500nm. Compare with using -1.4V, using -1.5V for
electrodeposition could fabricate porous nickel with higher density of pores. In figure 11a)
the CuNi thin film was formed at -1.6V, it was paved with broccoli like CuNi. After
dealloying, figure 11b) indicates that very tiny pores were uniformly distributed on thin film
and formed a mesh-like porous nickel.
Due to the occurrence of hydrogen evolution reaction, porous nickel could be formed with a
lot of voids. Then, at dealloying, copper deep inside the CuNi thin film could be easily
dissolved back to the solution due to sufficient contact of electrolyte. Therefore, high
surface area porous nickel can be formed by this combined method.
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Figure 8 SEM micrographs of a) electrochemical dealloying b) hydrogen bubble dynamic template[5]
Figure 9 SEM micrographs of electrodeposition at -1.4V a) before dealloying b) after dealloying
Figure 10 SEM micrographs of electrodeposition at -1.5V a) before dealloying b) after dealloying
Figure 11 SEM micrographs of electrodeposition at -1.6V a) before dealloying b) after dealloying
a b
a
a
a
b
b
b
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Figure 12 shows the XRD pattern of different voltage of electrodeposition in the range of
25°to 55°. Four peaks can be found from figure 12 which representing NiOOH, NiO
, Ni and Ni respectively. It discloses that at the process of
electrodeposition, porous nickel had already undergone oxidation and formed nickel oxide
on it. Oxidation occurred because of the low voltage applied, this occurrence led to one-step
fabrication of supercapacitor.
Figure 12 XRD of different voltage of electron deposition in the range of 25°to 55°
Figure 13 shows XRD pattern of different voltage of electrodeposition in the range of 42.5°to
45.5°. From figure 13, it shows that peaks at different deposition voltage were shift to the right
after dealloying, which is nearer to the angle of Ni . This phenomenon took place because
copper dissolved back to the solution at the stage of dealloying and caused the increase
concentration of nickel.
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Figure 13 XRD of different voltage of electron deposition in the range of 42.5°to 45.5°
4.2 Porous Nickel with Nickel Hydroxide
Figure 14 shows that after thermal treatment, some fur liked substances were grown on the
surface of porous nickel, which is Ni(OH)2. It can help to enhance the ability of porous
nickel to store charges. It is a very important feature for being a supercapacitor. From figure
14 a), figure 14 b), figure 14 c) and figure 14 e), it is discovered that a thick layer of nickel
hydroxide was grown on the samples and block most of the pores. This blockage made the
samples cannot perform ultimately. On the contrary, for sample 2-2-4, a thin layer of nickel
hydroxide grew on the surface of the porous nickel with relatively less blockage to the pores.
Therefore, sample 2-2-4 was chosen to undergo electrical tests and had further study.
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a b
c
d e
Figure 14 SEM micrographs of sample a)2-2-1 b)2-2-2 c)2-2-3 d)2-2-4 e)2-2-5
Figure15, 16, 17, 18 and 19 show the cyclic voltammetry curve of 5 samples before and
after hydrothermal treatment. Generally, the CV of a supercapacitor has a pair of redox
reaction peak which represent the voltage for molecules to undergo redox reaction. Also, the
enclosed area of the CV curve representing the charge storage capacity of the sample. From
figure 15 to figure 19, all five samples had a pair of well-defined redox peak. The shape of
the CV curves showed the typical characteristic of a supercapacitor because at the stage of
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electrodeposition, nickel oxides had already formed on the porous metal and it acted as an
active material for supercapacitor. Figure 15 shows that, the reduction peak and oxidation
peak of sample 2-2-1 before hydrothermal treatment were at about 0.1V and 0.55V
respectively. After, hydrothermal treatment reduction peak and oxidation peak became about
-0.05V and about 0.6V. For sample 2-2-2, figure 16 shows that its reduction peak and
oxidation peak before hydrothermal treatment were at about 0.1V and 0.5V respectively.
And after hydrothermal treatment, the reduction peak and oxidation peak were about -0.1V
and 0.7V. Then, figure 17 shows that, the reduction peak and oxidation peak of sample
2-2-3 before hydrothermal treatment were at about 0.1V and 0.5V respectively. After,
hydrothermal treatment reduction peak and oxidation peak became about -0.2V and about
0.7V. Also, for sample 2-2-4, figure 18 shows that, its reduction peak and oxidation peak,
before hydrothermal treatment, were at about 0.05V and 0.55V respectively. After
hydrothermal treatment, the reduction peak was about -0.05V and the oxidation peak is
about 0.7V. Last but not least, figure 19 shows that, the reduction peak and oxidation peak
were about 0.05V and 0.55V respectively before hydrothermal treatment. After
hydrothermal treatment, they became -0.05V and about 0.65V respectively.
In comparison, after the hydrothermal treatment all samples had larger CV curve enclosed
area than that before the hydrothermal treatment. It means that all samples had larger charge
storage capacity after hydrothermal treatment. Among all samples, sample 2-2-4 shows
largest enhancement and it had been further studied with charge and discharge tests.
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Figure 15 CV curve of sample 2-2-1
Figure 16 CV curve of sample 2-2-2
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Figure 17 CV curve of sample 2-2-3
Figure 18 CV curve of sample 2-2-4
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Figure 19 CV curve of sample 2-2-5
4.3 Supercapacitor
Figure 20 and figure 21 show the charge and discharge curves at different current densities
of sample 2-2-4 (with hydrothermal treatment) and sample 2-2-6 (without hydrothermal
treatment), including 1 mAcm-2, 2 mAcm-2, 5 mAcm-2 and 10 mAcm-2. The first few cycles
of charge and discharge usually unstable, therefore, every sample had undergone 5 cycles.
Figure 20 and 21 indicate the results of the last loop. Comparing the discharged time of
sample with hydrothermal treatment and sample without hydrothermal treatment, it is
discovered that the discharging time of sample with hydrothermal treatment are larger than
the discharging time of sample without hydrothermal treatment. Therefore, sample with
hydrothermal treatment (average ~0.152 Fcm-2) must have higher capacitance than the
sample without hydrothermal treatment (average ~0.0944 Fcm-2). The capacitance of
sample with hydrothermal treatment is about 61.8% higher than that of sample without
hydrothermal treatment
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Figure 20 C-DC curve at different current densities of porous nickel with hydrothermal treatment
Figure 21 C-DC curve at different current densities of porous nickel without hydrothermal treatment
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The time needed for discharging to occur are recorded in every 100 cycles in both samples:
first 1000 cycles with current density 5 mAcm-2; then following 300 cycles with current
density 10 mAcm-2; the last one with again current density 5 mAcm-2 for 300 cycles. The
thickness of porous nickel thin film is measured in nano scale which does not contribute
effects on chemical reaction so much. Also, all samples are fragile and difficult to measure
their masses. Therefore, area is used to calculate the specific capacitance instead of using
mass. The area specific capacitance is calculated by the equation:
Where I is the current, Δt is the time needed for discharge, S is the area of porous nickel and
ΔV is the voltage range. After calculating all parameters, the areal specific capacitances
were plotted against time which shown in Figure 22 and 23 as follow.
Figure 22 Specific capacitance of porous nickel with hydrothermal treatment
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Figure 23 Specific capacitance of porous nickel without hydrothermal treatment
From figure 22, porous nickel with hydrothermal treatment first experienced a relatively
high voltage so as to charge up fast. It was discovered that the specific capacitor tended to
decrease gradually and it decreased from 0.18Fcm-2 to 0.138Fcm-2 in first 1000 cycles. It
tells that after 1000 cycles, it could still maintain its function with about 77% efficiency.
Then, porous nickel with hydrothermal treatment had experienced a higher current intensity,
10mAcm-2, for 300 cycles. It reveals that high current did not break the sample, because the
sample can still work normally at 5mAcm-2 afterwards. It tells that, porous nickel with
hydrothermal treatment not only has high specific capacitance but also has high retention.
Figure 23 shows an opposite trend compared with figure 22. The specific capacitance kept
increasing for the sample without hydrothermal treatment. It increased from 0.0920 Fcm-2 to
0.100 Fcm-2 in the first 1000 cycles and increased from 0.102 Fcm-2 to 0.106 Fcm-2 in the
last 300 cycles. This extreme difference is due to the formation of nickel oxide on the
sample because of high current.
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5. Conclusion
In this project the method combining electrodeposition-dealloying and hydrogen bubble
reaction was used to fabricate porous nickel with high surface area. The results show that by
using this combined method, the limitation of using method of electrochemical dealloying
and hydrogen bubble dynamic template can be overcome. This method uses voltage that
equal or lower than -1.3V, the critical potential for hydrogen evolution reaction to occur, to
do the electrodeposition and followed by dealloying. Because of the formation of small
hydrogen bubbles, a lot of voids can be formed between particles on the CuNi thin film.
Therefore, at dealloying, copper deep inside the CuNi thin film can be easily dissolved back
to the solution as it has sufficient contact of electrolyte. This mechanism leads to formation
of high surface area porous nickel. Moreover, this combined method is also a one-pot
fabrication method of supercapacitor, because of the occurrence of oxidation in the stage
electrodeposition-dealloying. Furthermore, by using this combined method high specific
capacitance porous nickel can be formed, which is about 0.152 Fcm-2. Also, it has high
retention as after experiencing a high current it can still work with 77% efficiency. Last but
not least, this method is potentially to be applied to large-scale fabrication of
supercapacitors to be used in industry due to cost-effectiveness, easy fabrication.
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