PRODUCING FUELS AND ENERGY STORAGE
CHEMICALS SPECIES DERIVED FROM CO2 ELECTRO-REDUCTION
INTRODUCTION
Wind
and solar are important sources of energy supply. However, factors such as
weather conditions affect bridging demand and production (supply). The biggest
challenge faced by societies today is ensuring energy supply for future
generations as well as reducing sole dependence on fossil fuels is attained.
This owes to the fact that primarily, fossil fuel is gradually extinguishing
and reducing its value, and secondly, the amount of CO
2
emissions is on the rise outbalancing its consumption rate on earth
1.
These CO
2
emissions from fossil fuels combustions produces approximately billion tons of
carbon dioxide annually
2.Per research, since 1970s to
date, carbon dioxide concentrations in the atmosphere is responsible mainly for
the earth s climate change (greenhouse effect) and oceans PH change
2.Due
to these challenges, considerations are being given to study an efficient way
of converting CO
2 to reduced forms which serve as a source
energy. CO
2
electro-reduction being the most efficient and cost effective way of converting
CO
2 to harmless reduced forms which serve as a source energy
1-11. With
CO
2 electro-reduction being the most efficient and cost effective
way to convert CO
2
to other chemical species, this research will be focusing on this. CO
2
electro-reduction is the conversion of carbon dioxide to more reduced chemical
species using electrical energy
2. This reduced chemical species can
be used as energy storage medium for renewable energy sources or as working
fluid. Electrochemical
reduction proceeds with more positive potentials through two-, four-, six- and
eight-electron reduction pathways in gaseous and non-aqueous phases at high and
low temperatures
2. The scheme shown below is the basic
half-electrochemical chemical reaction as follows in aqueous/non-aqueous media:CO
2 + 2H
+ + 2e
CO + H
2O
1,2,3 Carbon
monoxide (CO) as seen in the scheme 1
below is one of the main reduction products obtained in this process.Other reduction products include formate,
formic acid, methane, alcohol and ethylene, aldehyde, oxalate, oxalic acid,
methanol. We will be focusing on methane, alcohol and methanol. In
CO
2
electro-reductive processes, ionic liquids (electrolytes) are salts in the
liquid state with melting points lower than 100
oC
or existing at room temperatures. They are made up of ions and short-lived ion
pairs and they have very low vapour pressure which accounts for their
conductivity and stability as liquids for longer periods
4. This
property makes them very useful in optical spectrometric methods to detect
reaction intermediates.
Ionic
liquids sometimes called ionic melts, liquid salts, fused salts are
environmentally friendly and are used as good solvents, electrically conducting
fluids, useful for CO
2 electro-reduction and prevention of
H
2
evolution because of the absence of water. A commonly encountered ionic liquid
is 1-butyl-3-methlimidazolium hexafluorophosphate ([BMIM]PF6).
THE
RESEARCH ISSUE, AIMS OR QUESTIONS I INTEND TO ADDRESSThere
are a lot of challenges currently in CO2 electro-reduction. It
chiefly concerns economic feasibility,
1.
Low catalytic activity (Degradation of catalyst).2.
Energetic efficiency
3.
Current
density 4. Faradaic
efficiency (Low product selectivity)5. Insufficient
catalyst stability and durability. (Application of technology - far from satisfactory/quality).
6.
Unsatisfactory
technology application 7. Optimization
of electrode/reactor and system design for practical applications8. Process
costs. Economic feasibility: Low catalytic activity:Per
Jinli et al, catalyst developed so far exhibit normally high over-potential for
CO
2 electro-reduction, indicating poor examples for practical
applications in terms of energy efficiency
1. Energetic Efficiency: Huei reported difficulty in optimizing the
energetic, current density and product selectivity as a leading challenge till
date
3. Current Density:
Kendra et al reported no desirable products at high current densities
(conversion rate) as one of the challenges currently
6. Faradaic efficiency (Low product
selectivity):Jinli
et al emphasized that few attempts of some catalyst have been made on CO
2
electro-reduction giving desirable product selectivity and stable yields under
continuous operation. E.g. the use of Sn, Pb, and Hg metal electrodes to
produce formate/formic acid
1. Insufficient catalyst
stability/durability for Industry scale: Jinli
et al proposed single biggest challenge in CO
2 electro-reduction.
This is caused either by the active electrode/catalyst surface being slowly
covered by the reaction intermediates (carbon films or poisonous species) or
by-products poisoning or blocking catalyst active sites leading to rapid
catalyst activity degradation
1. Unsatisfactory technology
application:The
technological application is far from satisfactory due to insufficient
understanding of the reaction process coupled with insufficient feed quantity
(industry scale)
1,6. Electrode/reactor optimization and
system design for practical application:According
to Jinli Qiuo, the main limitation to CO
2 electro-reduction caused
by electrode/reactor design is the rapid catalyst degradation, slow transport
of CO
2 to electrode surface and insufficient reaction turnover
1. Process cost:
Main challenge in this area is the high cost of production. This includes
consumption, capital and energy cost
3. IMPORTANCE OF RESEARCH PROPOSAL In
tackling low catalytic activity, exploring innovative ways of increasing
catalytic contact and activity is necessary. In this research, we will focus on
creating an enol-like surface intermediate of the copper surface catalyst.Studies
have shown that Copper metal catalyses the formation of C-C bonds generating C
2,
C
3
molecules products from the electro-reduction of CO
2 7.
Research
investigations has further shown that the pathway leading to the generation of
large range of C
2 and C
3
products could occur through an enol-like surface intermediate of the copper
surface catalyst
6.
The
surface preparation of the Cu specie electrode (working electrode) would be a
perfect morphology of carbon supported sputter/nanoparticle coat for high selectivity
towards CO
2
electro-reduction due to the high abundance of uncoordinated sites
7.
Energetic efficiency, current
efficiency and faradaic efficiency: Optimization
of these three parameters have been a subject of concentration which is quite difficult
till date. In this research, optimizing these parameters will be key. Suggested
usage of optimized Cu electrode surface structure with a special morphology as
well as Cu catalyst for high selectivity (faradaic efficiency), energy
utilization towards the final product (energetic efficiency), and conversion
rate (current density) is deemed.Research
investigations have shown that electro-reduced CO
2
using an electrolytic cell generates methane, ethylene and alcohols used to
carry energy in cells. However, in aqueous solutions, the current efficiency
for CO
2
electro-reduction is low from high activation barrier. The competing H
2
gas evolution causes difficulties in the electro-reduction and optical
spectrometric usage for detection of intermediate reactions. Current research show
that ionic liquids used as the electrolyte instead of an aqueous solution can
combat hydrogen evolution reducing competing reactions during electro-reduction
of CO
2
5.
Electrode-reactor and system design optimization
for practical application including unsatisfactory technology application: With
an indebt understanding of different approaches, I would like to consider this
approach The
three-dimensional structures of carbon-supported copper will be incorporated
into ionic-liquid based electro-polished copper specie electrode using
electro-deposition. This copper foam provides both the nanostructured surfaces and
cavities necessary to facilitate the reaction between the absorbed CO
2
and hydrogen species to generate high order hydrocarbons from the process.
The
electrode working area should be large and a small electrolyte volume in both
compartments and a reasonable gas headspace above the electrolyte in each
compartment bearing in mind the working electrode is parallel to the counter
electrode for uniform voltage. A
study on a special anionic exchange membrane that will be used to separate the
working and counter electrode compartments to prevent the oxidation of the
products from reduced CO
2 and prevent passage of the anionic
products acetate and formate as well
6.
CO
2
flow through the cell for optimum current efficiency for reduction is key in
this process so an insight study on the optimum flow rate of CO
2
transport to the surface as well as prevent interference with bubbles hitting
the surface would be carried out. During
CO
2
electro-reduction, some volatile liquid phase products are produced, so study
on the optimum temperature of the whole electrolytic cell that prevents
evaporation of the volatile products and is optimum simultaneously for the
stability of the whole system as a process will be carried out. Lastly
a perfect blend of the ionic liquid for use as an electrolyte to combat
challenges of electrochemical window, hydrogen evolution interference, CO
2
solubility and still serve its purpose like an aqueous electrolyte has been
lingering for decades, the best so far that has been used are
1-butyl-3-methylimidazolium hexafluorophosphate [BMIM][PF6],
2-hydroxy-N,N,N-trimethylethanaminium (choline ion), etc. despite the
uncertainty about their hydrocarbon formation due to the absence of efficient
hydrogen ions, stability and sensitivity to oxygen and difficulty in recovering
the products from the ionic liquid as extraction with water works for only
hydrophilic products, distillation not suitable for poorly volatile or
non-thermal labile products, and liquid-liquid extraction not suitable as
organic solvents leads to cross-contamination. CO
2
solubility in that ionic liquid is high reaching a mole fraction of 0.6 at 8
Mpa but both phases are not completely miscible since increase in pressure to
40 Mpa at 25 C showed increase in mole fraction
from 1.3 - 7.2%
9. So, this proposed
research will consider the synthesis of ionic liquids that can dissolve CO
2 almost completely
and still serve its electrolytic abilities efficiently and be stable. Including
efficient ways of extracting products from the ionic liquid. Synthesis
of ionic liquids will be based on some characteristics like: Temperature liquefaction Anion
natureLarge size difference between cation and anion in case of
low liquefaction temperature.Non-flammable
liquids with a very low vaporization pressure at temperatures below 150 C.Large liquid temperature rangeHigh
thermal stability (250-300 C)
4 Process Cost:Energy
(electricity) usage has been another challenge so far Huge amount of electricity
required for small product volume in electro-reduction of CO
2.
Leading to capital, consumption loss or economical infeasibility. This research
will consider cutting down process cost using solar energy approach. OBJECTIVES OF RESEARCH The
goal of this research is to: Prepare
the most suitable blend of Copper catalyst or any other catalyst for optimum
selective electro-reduction of CO
2
to produce the desired amounts of hydrocarbons reducing by product, over potential
and in turn increasing current density, energetic efficiency and faradaic
efficiency to a desired level. Delving
into the surface chemistry of the catalyst (Cu or other metals), (i.e.
improving the surface-intermediate between the catalyst specie electrode and
the electrolyte), principally at the enol-like surface intermediate and will
make us determine the C
1 and C
2
species involved in C-C bond formation. Looking
at the ionic liquid used as electrolyte for this process and prepare the
optimum blend of ionic liquid that reduces all negativities during the process. Optimize
the electrode/reactor and system design for practical application as well improving its technological
application using model approach combined with lifecycle analyses. Lowering cost of production to a minimal level.And
finally, researching ways of incorporating it into large scale.