58 research outputs found
Pendekatan Qspm Sebagai Dasar Perumusan Strategi Peningkatan Pendapatan Asli Daerah Kabupaten Batang, Jawa Tengah
The aim of this research is to analyse of increasing Local Original Income (LOI) strategy and his influence to increasing the regional income. The research was done at Local Government Income of Batang regency. This research also want to know that the LOI strategy was based on the potencies and opportunities. The analyzing use the IFE, EFE, SWOT, and then QSPM to choose strategic formulation; and proportion models. The result of Internal ā External analysis show that increasing strategy of LOI have not based on the potencies and opportunities that they have yet. The Local Government Income of Batang Regency needs the intensification strategy for increasing the LOI. By the QSPM analysis, the Local Government Income of Batang Regency needs extensification strategy for LOI acceptance
Determination of Fast Electrode Kinetics Facilitated by Use of an Internal Reference
The concept of using an internal
reversible reference process as
a calibration in the determination of fast electrode kinetics has
been developed and applied with the technique of Fourier transformed
large amplitude ac voltammetry to minimize the influence of errors
arising from uncertainties in parameters such as electrode area (<i>A</i>), concentration (<i>C</i>), diffusion coefficient
(<i>D</i>), and uncompensated resistance (<i>R</i><sub>u</sub>). Since kinetic parameters (electron transfer rate constant, <i>k</i><sup>0</sup>, and electron transfer coefficient, α)
are irrelevant in the voltammetric characterization of a reversible
reaction, parameters such as <i>A</i>, <i>C</i>, <i>D</i>, and <i>R</i><sub>u</sub> can be calibrated
using the reversible process prior to quantification of the electrode
kinetics associated with the fast quasi-reversible process. If required,
new values of parameters derived from the calibration exercise can
be used for the final determination of <i>k</i><sup>0</sup> and α associated with the process of interest through theory-experimental
comparison exercises. Reference to the reversible process is of greatest
significance in diminishing the potentially large impact of systematic
errors on the measurement of electrode kinetics near the reversible
limit. Application of this method is demonstrated with respect to
the oxidation of tetrathiafulvalene (TTF), where the TTF<sup>0/ā¢+</sup> process is used as a reversible internal reference for the measurement
of the quasi-reversible kinetics of the TTF<sup>ā¢+/2+</sup> process. The more generalized concept is demonstrated by use of
the Fc<sup>0/+</sup> (Fc = ferrocene) reversible process as an internal
reference for measurement of the kinetics of the Cc<sup>+/0</sup> (Cc<sup>+</sup> = cobaltocenium) process. Via the internal reversible reference
approach, a <i>k</i><sup>0</sup> value of 0.55 cm s<sup>ā1</sup> was obtained for the TTF<sup>ā¢+/2+</sup> process
at a glassy carbon electrode and 2.7 cm s<sup>ā1</sup> for
the Cc<sup>+/0</sup> one at a carbon fiber microelectrode in acetonitrile
(0.1 M Bu<sub>4</sub>NPF<sub>6</sub>)
Investigations of Fast Electrode Kinetics for Reduction of 2,3,5,6-Tetrafluoro-7,7,8,8-tetracyanoquinodimethane in Conventional Solvents and Ionic Liquids Using Fourier Transformed Large Amplitude Alternating Current Voltammetry
Fourier transformed large
amplitude alternating current voltammetry has been used under high
frequency (up to 1.233 kHz) conditions to probe the fast electron
transfer kinetics associated with the reduction of 2,3,5,6-tetrafluoro-7,7,8,8-tetracyanoquinodimethane
(F<sub>4</sub>TCNQ) in the molecular solvents acetonitrile and dimethylsulfoxide
at glassy carbon, platinum, gold and boron doped diamond macrodisk
electrodes and in ionic liquids (ILs) at carbon fiber and platinum
microdisk electrodes. The limitations encountered with measurements
under high frequency conditions are discussed in detail. Electrode
kinetic data obtained for the F<sub>4</sub>TCNQ<sup>0/ā¢ā</sup> process in the molecular solvents (0.060ā1.0 cm s<sup>ā1</sup>) are compared with results found in 1-butyl-3-methylimidazolium
hexafluorophosphate, 1-butyl-1-methylpiperidinium bisĀ(trifluoromethylsulfonyl)Āimide,
and 1-butyl-1-methylpyrrolidinium bisĀ(trifluoromethylsulfonyl)Āimide
ionic liquids (0.0030ā0.10 cm s<sup>ā1</sup>). The effect
of solvent viscosity ranging from 0.30 to 371 cP on mass transport
is substantial. The influences of the electrode material and structure
of the cation of the ionic liquid on the electrode kinetics also have
been established
Dual-Frequency Alternating Current Designer Waveform for Reliable Voltammetric Determination of Electrode Kinetics Approaching the Reversible Limit
Alternating
current (ac) voltammetry provides access to faster
electrode kinetics than direct current (dc) methods. However, difficulties
in ac and other methods arise when the heterogeneous electron-transfer
rate constant (<i>k</i><sup>0</sup>) approaches the reversible
limit, because the voltammetric characteristics become insensitive
to electrode kinetics. Thus, in this near-reversible regime, even
small uncertainties associated with bulk concentration (<i>C</i>), diffusion coefficient (<i>D</i>), electrode area (<i>A</i>), and uncompensated resistance (<i>R</i><sub>u</sub>) can lead to significant systematic error in the determination
of <i>k</i><sup>0</sup>. In this study, we have introduced
a kinetically sensitive dual-frequency designer waveform into the
Fourier-transformed large-amplitude alternating current (FTAC) voltammetric
method that is made up of two sine waves having the same amplitude
but with different frequencies (e.g., 37 and 615 Hz) superimposed
onto a dc ramp to quantify the close-to-reversible Fc<sup>0/+</sup> process (Fc = ferrocene) in two nonhaloaluminate ionic liquids.
The concept is that from a single experiment the lower-frequency data
set, collected on a time scale where the target process is reversible,
can be used as an internal reference to calibrate <i>A</i>, <i>D</i>, <i>C</i>, and <i>R</i><sub>u</sub>. These calibrated values are then used to calculate <i>k</i><sup>0</sup> from analysis of the harmonics of the higher-frequency
data set, where the target process is quasi-reversible. With this
approach, <i>k</i><sup>0</sup> values of 0.28 and 0.11 cmĀ·s<sup>ā1</sup> have been obtained at a 50 μm diameter platinum
microdisk electrode for the close-to-diffusion-controlled Fc<sup>0/+</sup> process in two ionic liquids, 1-ethyl-3-methylimidazolium bisĀ(trifluoromethanesulfonyl)Āimide
and 1-butyl-3-methylimidazolium bisĀ(trifluoromethanesulfonyl)Āimide,
respectively
Is the Imidazolium Cation a Unique Promoter for Electrocatalytic Reduction of Carbon Dioxide?
There
has been considerable recent interest in the use of the imidazolium
cation as a promoter in the heterogeneous and homogeneous electrocatalysis
of CO<sub>2</sub> reduction. However, despite its widespread use for
this purpose, the mechanism by which imidazolium operates is not yet
fully established. The present work reveals that enhanced catalytic
activity is achieved by addition of many cations other than imidazolium.
Under cyclic voltammetric conditions at a Ag electrode in acetonitrile
solutions (0.1 M <i>n</i>-Bu<sub>4</sub>NPF<sub>6</sub>),
2.0 mM concentrations of imidazolium, pyrrolidium, ammonium, phosphonium,
and (trimethylamine)-(dimethylethylamine)-dihydroborate cations can
all enhance the kinetics of catalytic CO<sub>2</sub> reduction with
imidazolium and pyrrolidium being the most active. Analysis of the
voltammetric data suggests that imidazolium cations achieve their
impact by directly acting as cocatalysts with Ag whereas the other
cations affect the reaction rate by modifying the electrochemical
double layer. The results also confirm that the active form of the
cocatalyst is the reduced imidazolium radical which forms a complex
with CO<sub>2</sub> before being further reduced to CO or other products
at Ag and not an imidazolium carboxylate formed between an imidazolium
carbene and CO<sub>2</sub>. In fact, imidazolium is deactivated during
CO<sub>2</sub> reduction by the latter reaction. Addition of water
inhibits this deactivation pathway allowing the imidazolium cation
to remain active in a long-term for CO<sub>2</sub> reduction. In contrast,
the pyrrolidium cation, where enhanced catalysis is attributed to
an electrochemical double layer effect, retains its catalytic activity
for very long periods of time regardless of the presence or absence
of water
Mass-Transport and Heterogeneous Electron-Transfer Kinetics Associated with the Ferrocene/Ferrocenium Process in Ionic Liquids
The ferrocene/ferrocenium
(Fc<sup>0/+</sup>) redox couple is regarded
as a kinetically facile process under voltammetric conditions. It
also possesses a nearly āsolvent independentā formal
potential, and for this reason is commonly used as a āreferenceā
redox system for electrochemical studies in nonaqueous electrolyte
media. Fc<sup>0/+</sup> has also been adopted as a āmodel systemā
in ionic liquid (IL) media, although conflicting reports on the mass-transport
and kinetics have brought its āidealityā into question.
In this study, the mass-transport and heterogeneous electron-transfer
kinetics associated with the Fc<sup>0/+</sup> process at a platinum
electrode are reported in 14 ILs with dynamic viscosities (Ī·)
ranging from 20 to 620 cP. The diffusivity of Fc (<i>D</i><sub>Fc</sub>) was calculated in each of the ILs using convolution
voltammetry and was found to be inversely proportional to the viscosity
of the medium, as per the StokesāEinstein relation (i.e., <i>D</i> ā 1/Ī·). The heterogeneous electron-transfer
rate constant (<i>k</i><sup>0</sup>) associated with the
Fc<sup>0/+</sup> process was measured in each of the ILs using large-amplitude
Fourier transformed alternating current (FTAC) voltammetry, and a
plot of lnĀ(<i>k</i><sup>0</sup>) versus lnĀ(Ī·) was
found to be linear, with a slope of ā1.0, as predicted by the
Marcus theory of electron transfer for an adiabatic process that involves
predominantly solvent reorganization rather than inner-shell vibrations.
Analysis of the lnĀ(<i>k</i><sup>0</sup>) versus lnĀ(Ī·)
data suggests a slight dependence of <i>k</i><sup>0</sup> on the constituent anion of the IL, which is thought to arise due
to electrostatic interactions between the anion and positively charged
Fc<sup>+</sup>. Finally, extrapolating the <i>D</i> versus
1/Ī· and lnĀ(<i>k</i><sup>0</sup>) versus lnĀ(Ī·)
plots to Ī· values typically encountered in acetonitrile-based
electrolyte media (i.e., 0.5 cP) predicts <i>D</i> and <i>k</i><sup>0</sup> values of approximately 2 Ć 10<sup>ā5</sup> cm<sup>2</sup> s<sup>ā1</sup> and 10 cm s<sup>ā1</sup>, in excellent agreement with literature reports. Overall, the results
presented in this study strongly suggest that the Fc<sup>0/+</sup> redox couple displays the characteristics of an āidealā
outer-sphere electron transfer process in IL media
Parameterization of Water Electrooxidation Catalyzed by Metal Oxides Using Fourier Transformed Alternating Current Voltammetry
Detection and quantification of redox
transformations involved
in water oxidation electrocatalysis is often not possible using conventional
techniques. Herein, use of large amplitude Fourier transformed ac
voltammetry and comprehensive analysis of the higher harmonics has
enabled us to access the redox processes responsible for catalysis.
An examination of the voltammetric data for water oxidation in borate
buffered solutions (pH 9.2) at electrodes functionalized with systematically
varied low loadings of cobalt (CoO<sub><i>x</i></sub>),
manganese (MnO<sub><i>x</i></sub>), and nickel oxides (NiO<sub><i>x</i></sub>) has been undertaken, and extensive experiment-simulation
comparisons have been introduced for the first time. Analysis shows
that a single redox process controls the rate of catalysis for Co
and Mn oxides, while two electron transfer events contribute in the
Ni case. We apply a āmolecular catalysisā model that
couples a redox transformation of a surface-confined species (effective
reversible potential, <i>E</i><sub>eff</sub><sup>0</sup>) to a catalytic reaction with a substrate
in solution (pseudo-first-order rate constant, <i>k</i><sub>1</sub><sup>f</sup>), accounts for
the important role of a BrĆønsted base, and mimics the
experimental behavior. The analysis revealed that <i>E</i><sub>eff</sub><sup>0</sup> values
for CoO<sub><i>x</i></sub>, MnO<sub><i>x</i></sub>, and NiO<sub><i>x</i></sub> lie within the range 1.9ā2.1
V vs reversible hydrogen electrode, and <i>k</i><sub>1</sub><sup>f</sup> varies from 2
Ć 10<sup>3</sup> to 4 Ć 10<sup>4</sup> s<sup>ā1</sup>. The <i>k</i><sub>1</sub><sup>f</sup> values are much higher than reported for any
water electrooxidation catalyst before. The <i>E</i><sub>eff</sub><sup>0</sup> values provide
a guide for in situ spectroscopic characterization of the active states
involved in catalysis by metal oxides
Simplifying the Evaluation of Graphene Modified Electrode Performance Using Rotating Disk Electrode Voltammetry
Graphene modified electrodes have been fabricated by
electrodeposition
from an aqueous graphene oxide solution onto conducting Pt, Au, glassy
carbon, and indium tin dioxide substrates. Detailed investigations
of the electrochemistry of the [RuĀ(NH<sub>3</sub>)<sub>6</sub>]<sup>3+/2+</sup> and [FeĀ(CN)<sub>6</sub>]<sup>3ā/4ā</sup> and
hydroquinone and uric acid oxidation processes have been undertaken
at glassy carbon and graphene modified glassy carbon electrodes using
transient cyclic voltammetry at a stationary electrode and near steady-state
voltammetry at a rotating disk electrode. Comparisons of the data
with simulation suggest that the transient voltammetric characteristics
at graphene modified electrodes contain a significant contribution
from thin layer and surface confined processes. Consequently, interpretations
based solely on mass transport by semi-infinite linear diffusion may
result in incorrect conclusions on the activity of the graphene modified
electrode. In contrast, steady-state voltammetry at a rotating disk
electrode affords a much simpler method for the evaluation of the
performance of graphene modified electrode since the relative importance
of the thin layer and surface confined processes are substantially
diminished and mass transport is dominated by convection. Application
of the rotated electrode approach with carbon nanotube modified electrodes
also should lead to simplification of data analysis in this environment
Double-Layer Capacitance at Ionic LiquidāBoron-Doped Diamond Electrode Interfaces Studied by Fourier Transformed Alternating Current Voltammetry
This article reports
the electrochemical double layer behavior
at the interfaces of ionic liquids (ILs) and a boron-doped diamond
(BDD) electrode as measured by large-amplitude Fourier transformed
alternating current (AC) voltammetry (FT-ACV). Data are collected
over a ā„2 V potential range and fitted to a simple resistorācapacitor
circuit model. The absence of significant higher-order AC harmonic
components implies nearly ideal capacitive behavior in the potential
ranges examined. Capacitance values for two protic ILs and three aprotic
ILs range from 3 to 8 μF cm<sup>ā2</sup> and generally
increase (1ā2 μF cm<sup>ā2</sup> V<sup>ā1</sup>) as the potential is swept from negative to positive values. Capacitanceāpotential
data display little dependence on the composition of the IL. The generally
featureless, linear dependence of capacitance on potential over a
wide potential range is similar to that reported for BDD electrodes
in aqueous electrolyte media, suggesting that the BDD electrode is
largely insensitive to the nature of the electrolyte media. The present
study concludes that FT-ACV affords an efficient approach to probe
the ILāelectrode interface, with minimal capacitive hysteresis
based on the potential scanning direction
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