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0000-thesis.Rnw
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%%%%%%%%
% To compile the thesis:
% $ Rscript -e "library(knitr); library(methods); knit('thesis.Rnw')"; latexmk -pdf -bibtex thesis
% Note that latexmk settings are set in the ./.latexmkrc file
%%%%%%%%
\RequirePackage{luatex85}
\PassOptionsToPackage{final}{graphicx}
\PassOptionsToPackage{final}{hyperref}
% For instructions on how to switch thesis to final mode, see \input{README.md}.
% Please avoid using absolute paths in either LaTeX or R code
% (in LaTeX code, use paths relative to the thesis root, and in R code please use the here::here() function).
\documentclass[webedition,openright,titles,swedish,english]{LuaUUThesis}
% printedition: configure thesis for physical printing (webedition by default)
% openright: force chapters to start on right-hand page (important for print edition)
% titles: show current chapter and section in top outer corner of each page (like a proper book)
% note that cleveref language switching does not work when languages are specified
% as babel package options, they need to be here. The main language should be loaded last.
% https://tex.stackexchange.com/a/20991/10824
% https://tex.stackexchange.com/questions/248341/how-to-make-a-custom-crefformat-dependent-on-language-chosen-with-babel/252847
%\input{assets/preamble/preamble.Rnw}
<<child=here::here('assets/preamble/preamble.Rnw'), label='preamble-LaTeX', cache=FALSE>>=
@
% For "LaTeX Workshop" (VSCodium extension) to do its autocomplete magic,
% our bib-files must be included here, in the main Rnw
% That also means \usepackage{biblatex} must be included in tikzLualatexPackages
\addbibresource{assets/references/library.bib}
\begin{document}
% \VerbatimFootnotes activates fancyvrb
\VerbatimFootnotes
% ----------------------------------------------------------------------
% R SETUP
% ----------------------------------------------------------------------
%\input{assets/preamble/R.Rnw}
<<child=here::here('assets/preamble/R.Rnw'), label='preamble-R', cache=FALSE>>=
@
% ----------------------------------------------------------------------
%%% FRONTMATTER
% includes abstract, dedication, list of papers, list of contents, other TOCs, glossaries
%\input{assets/components/frontmatter.Rnw}
<<child=here::here('assets/components/frontmatter.Rnw'), label='latex-frontmatter'>>=
@
%%% MAIN MATTER
\mainmatter
%%% CHAPTER:
%%% INTRODUCTION
\chapter{Introduction}
\label{ch:introduction}
The Sun is the primary source of energy for all living organisms,
and together with the cycle of day and night it is
the motive force powering the planet \cite{Schneider2005}.
Humans have always organized their lives and their settlements around the sun,
to draw warmth from it or to seek shade from it, since the earliest civilizations
\cite{Perlin2013}.
The modern world has, over the last couple of centuries, slowly turned to fossil fuels
for both domestic and industrial uses, and as we discovered more and more coal, gas,
and oil we have allowed our industry, agriculture, transportation, and
domiciles to become almost entirely dependent on them.
The resultant soot and pollution were obvious to anyone, but the effect of
\carbondiox\ on the climate perhaps less so. Still, the first scientific
reports warning about its heating effect on the atmosphere were
published so long ago \cite{Arrhenius1896,Tyndall1861,Jackson2019}
that they predate the discovery of the electron \cite{Thomson1897}.
By the end of the 1950s, anyone who read a mainstream newspaper
would have been aware of the basic idea of climate change due to anthropogenic
combustion of fossil fuels \cite{Hudson2023}.
Fossil fuels are the remains of ancient flora and fauna, compressed deep inside the Earth
for tens of millions of years. Importantly, these hydrocarbons
have been removed from the biosphere for just as long.
And we have been reintroducing them at a mind-boggling rate:
in a single year, we burn \num{55} trillion tonnes (that's \qty{55e15}{\kg}) of
this ancient carbon, which is by mass a hundred times more than everything
alive today (if we only count the carbon atoms).
Perhaps even more worryingly, over half of all the anthropogenic \gls{GHG} deposited
into the atmosphere has occurred since 1990, and all around the world we are still
prospecting for new oil and gas fields.
Due to the urgency of transitioning the energy system to a renewable basis,
scientific and technological advancements cannot solve it alone.
To successfully transition the energy system and industry to the power of sunlight,
economic incentives and policy must also align with this aim \cite{Nordhaus1972,Nordhaus1994,IRENA2019}.
And our societies must realize the need for an energy diet that respects
the physical limits of our biosphere \cite{Persson2022,Meadows1972}.
%%%% SECTION
\section{A plentiful source of exergy}
\label{intro:solar-spectrum}
The Sun is and always has been the main source of exergy in the solar system.
From it light radiates in all directions (of the Sun's total radiance about
two parts out of \num{100000} impinges Earth).
Light is nature's way of transferring energy through space.%
%\input{assets/aux/chunks/luminosity.Rnw}
<<child=here::here('assets/aux/chunks/luminosity.Rnw')>>=
@
The day-side of Earth continuously receives
\qty{\Sexpr{formatC(1e-12 * luminosity.hemispherical, format="fg", digits=3)}}{\tera\watt}
of sunlight (just outside the atmosphere), which after correcting
for Earth's albedo and the fraction irradiance absorbed by the atmosphere
(\Sexpr{earth.albedo} and \Sexpr{atmospheric.absorption}, respectively)
yields a solar power of
\qty{\Sexpr{formatC(1e-12 * luminosity.sealevel, format="fg", digits=3)}}{\tera\watt}.%
\seemore{\cref{photoec}}%
This is instantaneous \emph{power}, and summing over the number of hours in a year
yields an annual solar energy input of
\qty{\Sexpr{formatC(luminosity.sealevel * 8766 * 3600 * 1e-18, format="fg", digits=7)}}{\exa\joule},
which is around \num{10000} times greater than the world's annual energy consumption,%
\footnote{%
Which was \qty{178899}{\TWh} or \qty{644}{\exa\joule} in 2022
(equivalent to 280 million barrels of oil per day) \cite{Wolfson2018}.
}
or in other words: in one hour the planet receives more solar energy than humanity
expends in a whole year.
Next to solar power all other energy forms pale in comparison.
As far as we are concerned, sunlight is infinite, and only our imagination and
technology limits what we can use it for.
This is where modern chemistry and engineering comes into the fore.
%\input{assets/aux/fig/fig_0100-solar-spectrum-decorated.Rnw}
<<child=here::here('assets/aux/fig/fig_0100-solar-spectrum-decorated.Rnw'), label='0100-solar-spectrum-decorated'>>=
# \label{fig:solarspectrum-photoec}
# \label{tab:solarspectrum-amounts}
@
In this thesis, I will make the case for a more widespread use of photocatalysis
for production of solar fuels and for the proliferation of photocatalysts for
the degradation of environmental pollutants by exploiting low-dimensional
\ZnO\ alone and in combination with \ch{CdS} and \ch{Fe2O3}.
%%%% SECTION
\section{The energy transition and resource scarcity}
\label{intro:energy-transition}
The idea of an energy system based on renewable power is not new at all.
Exactly one hundred years ago, the evolutionary biologist \mbox{J.\ B.\ S.\ Haldane}
laid out a practical vision for the future energy system of England, saying
\cite{Haldane1923,Rajeshwar2008}
\enquote{the country will be covered with rows of metallic windmills}
feeding electricity through the grid to power stations where
\enquote{the surplus power will be used for the electrolytic decomposition of water
into oxygen and hydrogen}, and that the initial costs would be very considerable,
but \enquote{energy will be as cheap in one part of the country as another, so that
industry will be greatly decentralized; and that no smoke or ash will be produced}.
Of course, by that time the United Kingdom had been burning fossil fuels
for almost \qty{150}{\years} already, and people were getting really
worried about the visible smoke and smog engulfing their cities.
But we should note that Haldane envisioned this pollution-free energy system to
happen \emph{four hundred years} into the future, which is quite pessimistic, although
to be fair we have not managed to beat his prediction yet.
A known problem with the energy transition is that all development of renewable
energy systems is currently, and for the foreseeable future, built on logistics
fed with \emph{non}-renewable power \cite{Roos2021}.
Thus, producing the materials needed to provide renewable power
(\gls{PV} panels, wind turbines, electrolysers, \etc)
necessarily equates to emission of \gls{GHG}.
If we expect to operate all other industry as usual, then the energy transition
itself will necessarily produce even more emissions.
The only reasonable way out of this conundrum is to realize that the energy
transition, if managed responsibly, must lead to a sort of self-imposed energy scarcity
(perhaps that is a \enquote{good thing}, considering how wasteful the modern
mass-consumption economy has been).
Equally important is the question of how we will source the chemicals
necessary to build the required renewable power generation infrastructure.
\Cref{fig:0100-elements-of-photocatalysis} considers the availability of the chemical
elements commonly used in \glsdisp{PC}{photocatalytic} compounds.
Water is a critical resource for the energy transition.
Worldwide, we use more than \qty{4e12}{\cubic\metre} of freshwater each year.%
\footnote{Agriculture accounts for \qty{70}{\percent}, industry \qty{19}{\percent} and households \qty{10}{\percent}.}
Yet, three billion people are affected by water scarcity, and two billion of them
lack access to safe drinking water \cite{WWAP2020}.
By 2050, the demand for freshwater is projected to increase by more than \qty{40}{\percent}.\\
A perhaps overlooked aspect of our fossil-based
energy conversion system is that electrical power generation consumes a lot of freshwater.
In fact, of the various electrical power generation methods at our
disposal (coal/gas, nuclear, hydro, solar, wind, \etc) the renewable
generators (except for hydropower) consume hundreds or even thousands of times
\emph{less} freshwater to generate the same amount of electricity \cite{Wilson2012}.%
\footnote{%
With that in mind, we can see that operating a desalination plant on
non-renewable generated electricity would actually waste water, or in the best case
simply represent a transfer of freshwater resources from the desalination plant
to the power plant powering it.
Desalination plants should be solar powered. Recent research have shown
that it is even possible to simultaneously desalinate and produce electricity
using a composite \glstext{PV}-membrane device \cite{Wang2019}.
}
In many countries, the electrical generation sector consumes \emph{more} freshwater
than their agricultural sector.\\
The electrolysis of water into \hydrogen\ and \oxygen\ (\cref{rxn:water-splitting}),
also called \emph{water splitting}, requires around \qty{9}{\kg}
of \water\ to produce \qty{1}{\kg} of \hydrogen
and is an \enquote{uphill} reaction with a large positive Gibbs free energy,
$\state{G}=\qty{238}{\kJ\per\mol}$ or $\state{G}=\qty{1.23}{\eV}$,
comprising two half reactions, \namely, the \glsfirst{HER} and the \glsfirst{OER}
(here shown under acidic conditions at \gls{STP}):
% otherwise pagebreak inside the reactions block (too bad we couldn't make subreactions immune to pagebreaks)
\clearpage
% Be warned - vertical and horizontal spaces are held together by duct-tape here
\begin{subreactions}\begin{reactions}%
4 \proton{} + 4 \electron{} &-> 2 \hydrogen{} && $\qquad\qquad\qquad\qquad$ \AddRxnDesc{Hydrogen~evolution} "\label{rxn:hydrogen-evolution}" \\%
2 \water{} + 4 \hole{} &-> \oxygen{} + 4 \proton{} && $\qquad\qquad\qquad\qquad$ \AddRxnDesc{Oxygen~evolution} "\label{rxn:oxygen-evolution}"%
\end{reactions}\end{subreactions}%
\addtocounter{reaction}{-1}%
\vspace{-\baselineskip}%
% note that the following lengths must be adjusted if the horizontal
% extent of any reactions are changed!
\hspace{13mm}%
\begin{minipage}{59mm}%
\vspace{-\baselineskip}%
%\rule disappears inside minipage, but \hrulefill is visible, weird
\hrulefill%
\end{minipage}%
\begin{reaction}%
\qquad{}\qquad{}\quad{} 2 \water\lqd{} -> 2 \hydrogen\gas{} + \oxygen\gas{} $\quad\enspace\enspace E^0=\qty{1.23}{\voltNHE}$ \AddRxnDesc{Overall~water~splitting} "\label{rxn:water-splitting}"%
\end{reaction}%
But in practice, an electrolyser splitting water may require up to ten times more water
than stoichiometry demands.%
\footnote{%
Taking into account water treatment to meet the electrolyser's purity requirements,
water for cooling the electrolyser, and water for cooling the produced \hydrogen.}
Even when accounting for this, the water resources required for a renewably based
energy system are significantly lower than for a fossil-based system.
Even if we accept the notion that \emph{total} primary energy production must
decrease to achieve the energy transition, the inherent distributed nature
of renewable power generation \cite{Bollen2011} might actually mean that a larger
number of people get access to more electrical power than today.
There is no inherent benefit nor any technical reason to centralize solar power generation;
its inherently distributed nature makes it a more resilient power generation system.
Photoelectrochemistry lies at the cross-roads between energy and water, two
resources that will always be vital to society, but perhaps now more than ever.
It is our responsibility as a field to advice on how to produce sustainably sourced
photocatalysts for solar fuels production or for the photodegradation of pollutants.
I believe our aim must be to convert this carbon society into a photon society.
%%%% SECTION
\section{Photocatalysis with inorganic semiconductors}
\label{intro:photocatalysis}
Over \qty{90}{\percent} of all chemicals and fuels are estimated to be produced
with the aid of some catalyst \cite{NilssonPingel2018}, and catalysts contribute directly
to around a third of the world's economy \cite{Ma2005}.
Most commercial catalytic processes are heterogeneous, and commonly employ disperse
particles on high-surface area supports.
\glsdisp{PC}{Photocatalysis (PC)} is the acceleration of a photoreaction
by the presence of a catalyst \cite{Mills1997,Suppan1994}.%
\footnote{%
Note that the light is \emph{not} the catalyst, but rather a reactant.
The source of the light can be anything, really, but most commonly
natural sunlight. There is, as we have seen, a lot of it, and the
price cannot be beat.
It could also be simulated sunlight, or a lamp, as long as it emits
photons with an energy above the \glsdisp{band_gap}{band gap} of
the \glsdisp{PC}{photocatalyst}.}
A benefit of \gls{PC} is that it may (and indeed often does) rely
on atmospheric oxygen gas as the oxidant and that it can be carried out at
\gls{STP} \cite{Akyol2004}.
Photocatalysis can be employed in quite varied settings, in this thesis
we will primarily concern ourselves with the production of
energy-rich chemicals (\eg, solar fuels such as \hydrogen) and the degradation of
harmful organic compounds in water (water purification).
Photocatalysts are an important complement to \gls{PV} cells in the renewable
energy transition. Whereas \gls{PV} generates electrons in an external circuit,
\gls{PC} utilizes locally photogenerated charge carriers that can induce a chemical
redox reaction.
Many cheap, non-toxic and commonly available semiconductor materials are also
quite effective photocatalysts (\cf\ \cref{fig:0100-elements-of-photocatalysis}).
Heterogeneous catalysis is when the catalyst and catalysed species
are in different phases. In this context, heterogeneous photocatalysis is the process
of inducing chemical reactions using an irradiated photocatalyst's surface, \eg,
inorganic semiconductor surfaces \cite{Rajeshwar2015}, usually while immersed in
aqueous solution.
At the fundamental level an irradiated semiconductor nanoparticle can be considered
an electrochemical cell performing work, whose anodic and cathodic photoreactions
are in steady-state conditions. The photocurrent and the internal photovoltage
give the electric power of the cell, and the particle/cell achieves an
electrochemical potential that depends on the relative rate of its two half-cell
reactions \cite{Rajeshwar2015}.
%\input{assets/aux/fig/fig_0100-elements-of-photocatalysis.Rnw}
<<child=here::here('assets/aux/fig/fig_0100-elements-of-photocatalysis.Rnw')>>=
# \label{fig:0100-elements-of-photocatalysis}
@
But despite \ch{TiO2} having the honour of practically defining the field of
heterogeneous inorganic photocatalysis, the study of \ZnO\ as a \gls{PC} actually
predates \ch{TiO2}.
The earliest description of photocatalysis using \zincox\ dates back to 1911
in experiments by Alexander Eibner bleaching Prussian blue using
illuminated \ZnO\ \cite{vonEibner1911}, and its earliest use for
the photolysis of water is from 1953 \cite{Markham1953,Markham1955}.
In contrast to anatase \ch{TiO2} with its indirect band gap,
wurtzite \zincox\ has a direct band gap and thus higher absorption coefficient,
and similar positions of the conduction and valence band edges
(\qty{-0.5}{\voltNHE} and \qty{+2.8}{\voltNHE} at \pH{\,\num{5}}),
and have the advantage of a significantly higher charge carrier mobility
\cite{Boschloo2006,Jacobsson2012a}.
%\input{assets/aux/fig/fig_0100-bandgaps-all.Rnw}
<<child=here::here('assets/aux/fig/fig_0100-bandgaps-all.Rnw')>>=
# \label{fig:0100-bandgaps-all}
@
In metal oxides, the \gls{VBE} is determined primarily by the orbitals on the
\oxide{} anion, and the \gls{CBE} by metal cations and their bonding geometry.
The band gap of a semiconductor can be tuned using different methods:
\via\ the quantum size effect, or phase transformations, or solid solutions
with other elements.
In this thesis we have explored the quantum size effect on the band gap of \ZnO\
(\cf\ \cref{ch:quantum-confinement}).
Perhaps it would not be a mischaracterization to say that
the ultimate goal of photocatalysis is to design a \gls{PC} made out of
cheap and non-toxic materials with excellent stability in water under irradiation;
with a band gap $\geq\qty{1.6}{\eV}$ whose band edges straddle the \water\ redox
potentials;
and that performs the photocatalysed reaction at a high rate and for a long time.
Although the search for that holy graal will surely continue,
in the present the pressing need for quickly implementable solar-based
energy generation suggests that we should make do with what we have.
And what we have is very cheap \gls{PV} panels and an increasing
number of electrolysers.
%%%% SECTION
\section{The race to the bottom: benefits and risks}
\label{intro:nanoparticles-history-risks}
Many physical and chemical properties of a material change when
the constituent particles become sufficiently small.
A particle with a diameter between \qtyrange{10}{100}{\nm} is said to be
\enquote{nano}-sized, while larger particles than that are commonly referred
to as sub-micron or micron-sized.
But how small is a nanoparticle?
Getting a grip on that is mind-bendingly hard.
In \cref{fig:0100-nanoparticles-are-small} we try to put it into some perspective.
Of course, there is a limit to how small stuff we can build, and that is set by the size
of the atoms themselves. An \oxide{} ion has a diameter of \qty{0.28}{\nm},
and a \ch{Zn^{2+}} ion has a diameter of \qty{0.15}{\nm} (based on ionic crystal radii).
%\input{assets/aux/fig/fig_0100-nanoparticles-are-small.Rnw}
<<child=here::here('assets/aux/fig/fig_0100-nanoparticles-are-small.Rnw')>>=
# \label{fig:0100-nanoparticles-are-small}
@
If particles are made into nanometre dimensions, the most noticeable change is
the large increase in specific surface area (area per weight of the material),
and thus the potential to substantially increase chemical activity at the exposed surfaces.
The size of the material also changes how light interacts with it.
If a nanoparticle is made small enough (depending on its composition)
something rather special happens: its electronic states are literally
\emph{squeezed} by the constricted dimensions of the nanoparticle, which
results in drastic changes in the material's electronic and optical
properties.
This phenomenon is termed \emph{quantum confinement} and is elaborated
in \cref{ch:quantum-confinement}.
Although humans have benefitted from the use of nanoparticles or nanostructured materials
for millennia \cite{Montanarella2022} (often unwittingly), we are by no means
alone in doing so.
Many birds have iridescent plumage and many insect exoskeletons have intricate
nanostructured surfaces that create pigment-less (structural) colouration by reflecting
incident light in very specific ways \cite{Wolpert2009,Dunning2023}.
In terms of sophistication, engineered nanostructures cannot yet compete
with their counterparts in nature.
The study of such nanostructures is a major interest for applications towards
improving the efficiency of \gls{PV} panels or in technological applications such
as waveguides towards light-based computing.
Modern scientific investigations into nanoparticles were first undertaken
in the late \century{19} century by Scottish scientist John Aitken when he
took an interest in something as mundane as dust.
At the time, it was obvious that the transparency
of the air correlated to the amount of dust (and to the relative humidity).
Aitken was the first that set out to measure these effects, and created a method
for measuring these suspended dust particles in air \cite{Aitken1888},
then miniaturized the device and promptly set about travelling
across Europe to collect measurements (\enquote{the portable apparatus is reduced
to such dimensions that it adds but little to one's personal luggage}) \cite{Aitken1891}.
Aitken's device was the first example of a condensation particle counter,
which works by introducing airborne particles into a supersaturated vapour,
where the particles act as nucleation points for the vapour to form droplets
that are then counted using optical techniques.
Using this technique one can detect the presence of particles down to
a few nanometres in size.
This was the first demonstration of a characterization technique
to quantify nanoparticles (particles below \qty{50}{\nm} are generally
undetectable with light-scattering optical particle counters), but less than
\qty{50}{\years} later it was supplanted by the electron microscope.
Nanotechnology is the latest in a long line of technologies that promises
better living through chemistry \cite{Schummer2008}.
But it would behoove us to root our expectations in history, which can
be an unforgiving teacher if forgotten. Only during the \century{20}, chemical
industry managed to spread DDT over every continent, freon into the stratosphere,
and lead in every city by the combustion of leaded petrol.
To be fair, the chemical industry has also been the source of some
of our modern world's greatest successes, such as the catalytic Haber--Bosch
process that has fed the world, vaccines that have wiped out polio and many other
debilitating diseases, and the production of an amazing range of materials that
have made our lives healthier and safer.
Perhaps it is no wonder that we believe the nano-fication of chemistry
will lead to similar rapid advances.
I guess what I am trying to convey is that we must make ourselves aware of the
risks, and to do that some creativity and humility is called for.
The risks of nanosized materials may not always be the same as those experienced
by earlier generations of chemists, and widely spreading a technology that
\enquote{works in the lab} comes with its own set of new risks.
Chemists as well as chemical industry regulators (especially in the
EU and USA) have a good grasp of the risks with most industrially manufactured
chemicals.
The main risks we need to consider are those towards human health and towards the environment.
This is something that is still being actively researched
\cite{Mitchell2019,Kim2016a,Reed2012,Maynard2011}, and for that reason those working
in the field would do well to be cautious and avoid hyperbole when expressing the
benefits of nanotechnology.
When it comes to risk management, the hardest challenge might be to figure out
what exactly we should be measuring in the first place; what material
and particle attributes are most closely associated with health risks, and at what
exposure levels? \cite{Maynard2015}
%%%% SECTION
\section{Will chemistry come to the rescue?}
\label{intro:chemistry-rescue}
There is no denying that many of the technological and environmental challenges
ahead of us are well-suited for chemical solutions.
Chemistry has developed technologies and materials that can reduce pollution,
improve waste management, and clean up contaminated environments.
For example, catalytic converters in cars use chemical reactions to convert harmful
exhaust gases into less harmful compounds before they are released into the air.
Chemistry has also helped us develop materials such as activated carbon and zeolites that
can absorb and remove pollutants from air and water.
Additionally, chemistry has played a crucial role in developing principles of
\enquote{green chemistry}, that aims to design chemical products and processes
that are safe, sustainable, and minimize waste.
A not yet realized application for photocatalytic degradation lies
in the complete destruction of synthetic chemicals from various waste streams.
Synthetic chemicals of all kinds are produced in increasing quantities all over
the world, and pollution by their release into the environment is growing \cite{Bernhardt2017}.%
In particular, pharmaceuticals are dispersed in the environment \via\
water treatment plants that are presently ill-equipped to remove such compounds
from the effluent, but worse than that, the pharmaceutical production plants
themselves are a major source of local pollution and are
frequently located in countries with lax environmental regulations.
The Swedish government agency Naturvårdsverket published a report in 2017 \cite{Naturvardsverket2017}
on advanced cleaning methods of effluent from pharmaceutical residues.
The report mentions \gls{AOP} as a technology not yet in production, but showing
promise for certain use cases, such as effluent with higher concentrations of pollutants.
Ozonation has been in use in one treatment plant in Linköping since 2015.
Semiconductors are an excellent choice for photoactive materials, because their
band gaps are well-suited to produce charge separation under solar irradiation.
For a \emph{single} semiconductor material to split water (\cf\ \cref{rxn:water-splitting}),
its band gap must straddle the hydrogen and oxygen evolution reduction potentials
of \water\ (\cf\ \cref{fig:0100-bandgaps-all}) and it must allow efficient transport
of both electrons and holes.
Unfortunately, such a semiconductor does not exist (or has not been found yet, despite
well-organized research into photoelectrochemistry since at least the 1970s \cite{Maeda2011}).
Wide gap semiconductors such as \ch{TiO2} or \ZnO\ have band edges suitable
for total water splitting, but on the other hand their band gaps are so large
that they will only absorb \gls{UV} photons which make up a very small part
of the solar spectrum (\cf\ \cref{tab:solarspectrum-amounts}).
%%%% SECTION
\section{Scope of this thesis}
\label{intro:scope-thesis}
Throughout this thesis we have studied the
application of sunlight towards the synthesis of solar fuels or
the degradation of chemicals
with photocatalysts synthesized using cheap and easily scaled methods.
The work involved laboratory-scale wet-chemical synthesis
of composite nanostructured films and colloidal low-dimensional nanoparticles;
their experimental characterization using a variety of spectroscopic, microscopic,
and diffractive methods;
and proof-of-concept tests of their photocatalytic performance.
Concurrently I got the opportunity to set up a laboratory from scratch (that was really fun!)
and to create a personalized data analysis pipeline with an eye towards
reproducibility and the sharing of code and data.
In the first paper
\seepaper{P1}
we set out to synthesize a large surface area nanodigitated \glsdisp{PC}{photocatalyst}
\enquote{sandwich} of a wide gap semiconductor (\ZnO) coated with \ch{CdS}
for visible-light sensitization, which allowed us to optimize electrodeposition
parameters and study the effect of \ch{CdS} coating thickness \vs\ \gls{PC} performance.
Here the goal was to create a highly photoactive \gls{PC} material with visible-light sensitivity
\via\ an experimentally simple and economically scalable method, which we
achieved by using electrodeposition and chemical-bath deposition (both very
established methods, and relatively simple in operation), although the visible-light
sensitivity came at the cost of introducing the well-known toxicity of cadmium.
In our second paper we
\seepaper{P2}
looked for ways to avoid cadmium as well as making the outer coating
more \pH\ and photoresistant (\ch{CdS} degrades under irradiation unless sacrificial
agents are introduced in the electrolyte solution), and what could be more
durable than literal rust?
But for that to work the well-known extremely poor hole conductivity of \hematite\
required the application of an extremely thin film on the \ZnO\ \glsplural{NR},
which essentially demanded the use of \gls{ALD}.
This allowed us to study how varying the \hematite\ layer thickness affected
the properties of the photoelectrodes.
In the third paper
\seepaper{P3}
we took a step back to study the question of how \ZnO\ nanoparticle
diameter in the quantum size regime influenced the redox potential
of the photogenerated excitons.
We did this by synthesizing colloidal \zincox\ suspensions at varying
average \gls{QD} diameter and measure their \gls{PC} activity under
simulated sunlight and simulators tracking the photodegradation of \gls{MB} dye.
This kind of colloidally suspended \gls{PC} could be used to
combat distributed pollutants using nothing more than natural sunlight and
then naturally precipitate into relatively harmless \ZnO\ sediment, a process
aided by the ultrasmall size and large band gap of the \gls{PC} particles.
In our fourth paper
\seepaper{P4}
we take a deep dive into the vibronic properties of low-dimensional \ZnO\ nanocrystals,
\via\ a series of Raman spectroscopy measurements where we quantify
their phonon--phonon and electron--phonon coupling as a function of particle diameter.
This thesis also includes a chapter discussing the relative ease with which
analytical reproducibility can be achieved with the use of freely available software,
and also briefly presents some scientific software tools
this author has publicly shared during this work.
% data analysis chapter with an eye towards improved reproducibility in science via code and data sharing
\Cref{fig:0100-wordcloud-thesis-corpus} shows a word cloud of keywords;
not compiled ourselves, but rather \emph{generated}
from the corpus of all \emph{titles} of all bibliographic records
\emph{cited in this thesis}.
In a way, it is a \emph{meta}-visualization: the thesis querying itself.
%\input{assets/aux/fig/fig_0100-wordcloud-thesis-corpus.Rnw}
<<child=here::here('assets/aux/fig/fig_0100-wordcloud-thesis-corpus.Rnw'), label='0100-wordcloud-thesis-corpus'>>=
# \label{fig:0100-wordcloud-thesis-corpus}
@
%%% CHAPTER:
%%% SYNTHESIS AND PREPARATION
\chapter{Synthesis and preparation}
\label{ch:synthesis}
In my synthetical work I strove for the simple, as far as possible.
That mindset was based on the idea that if chemistry is to contribute to the
conversion of our energy system at any scale, its proposed solutions must
first and foremost be scaleable.
That same idea was also behind our choice of elements---zinc and iron being
plentiful and very cheap and practically non-toxic.
Granted, we also used cadmium which is far from non-toxic, but on account of
its sulfide being a commonly employed visible-light absorber in solar cells and because
its synthesis method is very simple, it was too tempting a target to overlook.
At an early stage of this work we attempted to synthesize anatase \ch{TiO2}
\glsplural{NR} on \gls{TCO}, but after attempting several approaches
including
electrochemical deposition with templated membranes
\cite{Limmer2001,Limmer2002,Chu2003,Chu2003b,Limmer2003a,
Limmer2004,Chu2004,Limmer2005,Yan2006},
cathodic electrodeposition in acidic baths
\cite{Natarajan1996,Karuppuchamy2001,Chenthamarakshan2002,Karuppuchamy2002,
deTacconi2003,deTacconi2004,deTacconi2005,Karuppuchamy2005,Karuppuchamy2006,
Karuppuchamy2006a,Somasundaram2006,Karuppuchamy2007,Chettah2008,Chigane2009,
Zhou2009,Chen2010h,Elhajj2010},
cathodic electrodeposition in alkaline baths
\cite{Ohya2002,Sawatani2005,Wessels2008,Wessels2008a}, and
anodic electrodeposition
\cite{Flood1995,Lokhande2005,Wessels2006,Tsai2009,Wu2009b,Wessels2010,Wu2011}
without achieving the desired synthetical outcome apart from
impressive clouds of hydrochloric acid (inside the fume hood, mind you) we looked
for an alternative photocatalytic metal oxide that could be electrodeposited
at mild processing conditions.
Zinc oxide is a semiconductor with known experimental methods of cathodic electrodeposition
of thin films or nanostructures in aqueous electrolytes \cite{Peulon1998,Pauporte2009},
which we could easily adapt.
\ZnO\ wurtzite has attractive optical, electrical, and thermal properties, such as
a wide and direct band gap (\qty{3.3}{\eV} in the bulk at \gls{RT}),
a high absorption coefficient (due to its direct band gap),
a large exciton binding energy%
\footnote{%
The exciton binding energy is the energy needed to separate the electron and hole
of an exciton into free charge carriers, \ie, the energy difference between the
fundamental gap and the optical gap.
It is significantly larger than $kT$ (\qty{26}{\milli\eV} at \gls{RT}), giving
\ZnO\ exciton emission even above \gls{RT}.
For comparison, \ch{GaN} has an exciton binding energy of \qtyrange{18}{28}{\meV} \cite{Karpina2004}.
}
\qty{60}{\milli\eV},
a high carrier mobility $>\qty{100}{\cm\squared\per\volt\per\second}$ \cite{Janotti2009},
and a high thermal conductivity,
which makes \ZnO%
\footnote{%
On a personal note, zinc was the first element that made a mark
during my undergraduate education: at one of my cohort's very
first lectures at the Arrhenius laboratory, our lecturer
Lars-Johan Norrby proclaimed zinc to be his favourite element on the periodic table!}
considered for applications in \glsdisp{PC}{photocatalysis},
\glsdisp{PV}{solar cells}, \glsplural{LED}, transparent conducting films, and more
and a viable alternative to \ch{TiO2} anatase.
\ZnO\ is amphoteric, reacting with both acids and bases, but it is nearly insoluble
around neutral \pH.%
\footnote{%
\ZnO\ solubility at \qty{298}{\kelvin} (\qty{25}{\celsius}) is
\qty{1.23e-5}{\mol} per \qty{100}{\gram} \water\ \cite{Ellis1984},
or ${\approx}\qty{1.0}{\mg}$ per \qty{100}{\gram}.}
In acids it easily forms salts,
and with increasingly alkaline conditions (starting from around \pH{\,\num{9}})
it is known to form monomeric hydroxide complexes from \ch{ZnOH+} to \ch{[Zn(OH)4]^{2-}}
\cite{Greenwood1997,Ekberg2016}.
\section[Electrodeposition of ZnO NR arrays]{\texorpdfstring{Electrochemical deposition of \ZnO\ NR arrays}{Electrochemical deposition of ZnO NR arrays}}
\label{synthesis:electrodeposition}
Electrochemical deposition is cheap, scalable, and affords
relatively good control of the conditions during synthesis \cite{Schwarzacher2006}.
In addition, semiconductor thin-film electrodeposition is a mature technology,
widely used in many industrial settings, and its basis in solution chemistry
allows a wide range of synthetical parameters.
Perhaps ironically then, the main disadvantages of electrodeposition
are also related to solution chemistry: (relatively) complicated sample handling and residual
electrolyte in the product.
Despite being cheap, electrodeposition allows
shape-controlled synthesis of \ZnO\ \glsplural{NR} \emph{without}
any capping agents or surfactant molecules that preferentially inhibit the
growth of particular crystallographic facets, which was attractive to my
experimental sensibilities.
We created \ZnO\ \glsplural{NR} by cathodic deposition at \qty{-0.7}{\voltSCE}
for \qty{90}{\minute} with an initial pulse at \qty{-1.3}{\voltSCE} with a duration
of \qtylist[list-final-separator={ or }]{0.1;0.5;1.0}{\second}.
The aqueous electrolyte solution was
\reactant[concentration=0.1,concentration-unit=\milli\Molar]{zincchloride}
with \reactant[concentration=0.1,solvent=\water]{potassiumchloride}.
The electrodeposition was done at a temperature of \qty{80}{\celsius} maintained
using a thermostat-controlled water bath.
Our primary electrodeposition setup (see \cref{{fig:0201-electrodeposition-schematic}})
used a CH~Instruments 760C%
\footnote{%
CH~Instruments 760C was a compact bench-top bipotentiostat/galvanostat
with a current range from \qty{100}{\micro\ampere} to \qty{1}{\pico\ampere} and a
voltage range $\pm\qty{10}{\volt}$.
}
bipotentiostat connected to a three-electrode cell with
a CHI111 \ch{Ag}/\ch{AgCl} reference electrode
and a CHI115 \ch{Pt} wire counter electrode.
Our secondary electrodeposition setup (see \cref{fig:0301-ED-cell-autolab})
used either a {\textmu}AUTOLABIII%
\footnote{%
The {\textmu}AUTOLABIII was a compact bench-top potentiostat with
a current range from \qty{10}{\milli\ampere} to \qty{10}{\nano\ampere} and a
voltage range $\pm\qty{5}{\volt}$ with a resolution of \qty{3}{\micro\volt}.
Controlled via a laptop computer running GPES~v4.9 software.
}
potentiostat or an AUTOLAB PGSTAT302N%
\footnote{%
The PGSTAT302N was a high-current potentiostat/galvanostat with
a current range from \qty{1}{\ampere} to \qty{10}{\nA} and a
voltage range $\pm\qty{10}{\volt}$ with a resolution of \qty{3}{\micro\volt}.
}
connected to a three-electrode cell with an AUTOLAB \gls{RE}
and a coiled \ch{Pt}-wire \gls{CE}.
The \gls{WE} was \gls{FTO} glass, \ie, sodalime%
\footnote{%
Sodalime glass is a very common type of glass commonly used in containers, plate glass,
microscope slides, pasteur pipettes and more.
It does complicate analysis slightly due to containing several different oxides (in order of abundance):
\ch{SiO2}, \ch{Na2O}, \ch{CaO}, \ch{MgO}, and \ch{Al2O3}.
Before deposition each cut glass substrate were prepared by ultrasonication
in deionized \water, followed by an \EtOH\ and then an acetone rinse,
and finally dried with \ch{N2}.
}
glass coated with a compact
layer of fluorine-doped \tinox (TEC-7).
The TEC-7 substrate has a sheet resistance of \qty{7}{\ohm\per\sq},
is insoluble in dilute acids or alkalis,
and microcrystalline with a highly oriented structure.
Its impedance is low enough to allow direct-current cathodic deposition.
The \gls{WE} was kept at a potential negative to the reduction potential
of \ch{O2\gas}, which causes oxygen gas near the electrode to be reduced to
hydroxide ions (\cref{rxn:oxygen-reduction}). The hydroxide ions react with the
zinc ions and form \ch{Zn(OH)2}, \ch{ZnOOH} or \ZnO\ (\cref{rxn:Zn-OH-O})
depending on the temperature.
% https://tex.stackexchange.com/questions/681457/half-cell-reactions-and-sum-reaction-below-horizontal-rule-with-chemmacros
% \begin{minipage}{\textwidth}%
% surrounding the whole shebang with another minipage caused horizontal width issues
\begin{subreactions}\begin{reactions}
1/2 O2 + \water{} + 2 \electron{} &<=> 2 \hydroxide{} \AddRxnDesc{Oxygen~reduction~in~water} "\label{rxn:oxygen-reduction}" \\
Zn^{2+} + 2 \hydroxide{} &-> \ZnO{} + \water{} \AddRxnDesc{Zinc~hydroxide~to~oxide} "\label{rxn:Zn-OH-O}"
\end{reactions}\end{subreactions}
% reverting the counter so the sum reaction gets the same major number as the half-cell reactions
\addtocounter{reaction}{-1}
\vspace{-\baselineskip}%
% https://tex.stackexchange.com/a/269888/10824
% this must be messiest LaTeX code in the entire thesis, just to achieve this
% ridiculously simple thing (rule extending the width of the reactions)
% I have given up on customising the thickness of the hrule
% https://tex.stackexchange.com/questions/371286/draw-a-horizontal-line-in-latex
% note that these values are hard-coded and must be adjusted if the horizontal
% extent of any reactions are changed
\hspace{14mm}%
\begin{minipage}{75mm}
\vspace{-\baselineskip}
%\rule disappears inside minipage, but \hrulefill is visible, weird
\hrulefill
\end{minipage}
\begin{reaction}
Zn^{2+}\aq{} + 2 \electron{} + 1/2 O2\aq{} -> \ZnO\sld{} \phantom{ZnOZnOZnO}
\AddRxnDesc{Zinc~oxide~electrodeposition} "\label{rxn:ZnO-dep}"
\end{reaction}
%\end{minipage}
% https://stackoverflow.com/questions/2170819/margin-figures-in-latex
\marginpar{\scriptsize\itshape%
\includegraphics[width=\marginparwidth]{synthesis/electrodeposition/model.pdf}
}
The oxygen was actively supplied to the electrolyte solution by either saturating
the headspace with \ch{O2\gas} flow or by bubbling it into the electrolyte solution.%
\footnote{%
I found that bubbling \ch{O2\gas} directly into the electrolyte solution
was better to reach and maintain saturation \ch{[O2\aq]}, but only if
it could be done without the bubbles disturbing the electrolyte solution
near either the \gls{WE} or \gls{RE}.
The alternative was to maintain \oxygen\ overpressure in the headspace,
which required the gas flow to be higher than the leak-rate out
of the headspace, and that the electrolyte solution was given enough time
prior to deposition to become saturated with \oxygen.
}
In any case, the solution was saturated in oxygen \emph{before} the deposition
started, such that the oxygen concentration was kept as-close to constant as possible
during the electrodeposition.
The role of the supplied oxygen gas was to supply a source for the hydroxide ions needed at
the working electrode. But note that this role could have been fulfilled by other means,
for example using hydrogen peroxide, nitrate or other ions such as phosphate,
carbonate, or sulfate.
\seemore{\cref{refelectrodes}}
\seemore{\hlink{https://solarchemist.se/2016/11/24/reference-electrodes}{Blog}}
%\input{assets/aux/fig/fig_0201-electrodeposition-cell-schematic.Rnw}
<<child=here::here('assets/aux/fig/fig_0201-electrodeposition-cell-schematic.Rnw')>>=
# \label{fig:0201-electrodeposition-cell-schematic} (a)
# \label{fig:0201-electrodeposition-cap-schematic} (b)
# \label{fig:0201-electrodeposition-WE} (c)
# \label{fig:0201-ED-CHI} (d)
# \label{fig:0201-electrodeposition-schematic}
@
Maintaining a steady temperature of \qty{80}{\celsius} was just as important
as maintaining a steady \ch{O2\aq} concentration.
The target temperature was low enough to allow the use of a water bath,
and for practical reasons we used a hot plate with a built-in magnetic stirrer
which meant that evaporation of the water bath itself needed to
be counter-acted since depositions were \qty{1.5}{\hour} long.
For that purpose I developed a custom-made cover made with small peripheral holes to allow
the temperature probe access to the bath and a large centre-hole for placing the
deposition cell securely (to avoid it bobbing in the water).
The cover was successful in limiting evaporation and kept the
water bath's level constant for over \qty{1.5}{\hour} at \qty{80}{\celsius}.
We also improved on the gas inlet by adapting a long glass pipette for the
purpose (instead of a typical gas needle which is metallic and interfered with
the current inside the cell).
To improve reliability and repeatability of the electrochemical depositions
I created a simple paper-based form to jot down the deposition parameters for each run
(since the potentiostats' software unfortunately offered no way to save such metadata).
These \hlink{https://github.com/solarchemist/electrodeposition-templates}{simple templates}
also allowed us to record non-potentiostat parameters
such as gas flow rate, stirring or not, temperature, \etc.
%\input{assets/aux/fig/fig_0201-ED-cell-autolab.Rnw}
<<child=here::here('assets/aux/fig/fig_0201-ED-cell-autolab.Rnw')>>=
# \label{fig:0301-ED-Autolab02-a} (a)
# \label{fig:0301-ED-electrodes-distance} (b)
# \label{fig:0301-ED-electrode-insulated} (c)
# \label{fig:0301-ED-cell-autolab}
@
The secondary electrodeposition setup (see \cref{fig:0301-ED-cell-autolab}) used
a larger-volume cell, and was used for some projects after the completion of \cref{P1}.
Due to the shallower angle of the \gls{WE} in this cell (compared to the perfectly
vertical configuration in the primary setup) it was necessary to immerse the
entire \gls{WE} in the electrolyte solution and thus to fully insulated its electrical
contacting.
The longer distances from the cell ports to the electrolyte solution also
necessitated the use of a larger \gls{RE} and \gls{CE} (coiled \ch{Pt} wire).
The larger cell also meant a longer \glsname{WE}--\glsname{CE} distance
$\approx\qty{25}{\mm}$ (about twice as long as in the primary setup).
The fully insulated contact was sturdy and created in the following way:
the electrical wire was passed through
a disposable plastic pipette (with its bulbous part cut off) and contacted to
the \gls{TCO} surface with electrically conductive silver lacquer,
then covered with a strip of aluminium tape.
The tape and the end of the plastic pipette were then fixed into place by
colourless epoxy glue to add sturdiness and chemical stability to the contact,
and the whole contact was then covered with a thin coat of nail varnish (\cref{fig:0301-ED-electrode-insulated}).
The nail varnish was applied primarily to define the active surface area, and
for purposes of easier identification since we had several
available colours.
%%%% SECTION
\section[Chemical bath deposition of CdS films]{\texorpdfstring{Chemical bath deposition of \ch{CdS} films}{Chemical bath deposition of CdS films}}
\label{synthesis:chemical-bath-deposition}
\ch{CdS} nanoparticles were chemical bath-deposited onto
\qty{1.5}{\hour} electrodeposited \zincox\ \glsplural{NR} arrays.
An aqueous bath solution of \reactant[concentration=2,concentration-unit=\milli\Molar]{cadmiumsulfate},
\reactant[concentration=10,concentration-unit=\milli\Molar]{thiourea}, and
\reactant[concentration=1]{ammonia} was
thermostatically maintained at \qty{60}{\celsius} before immersing the
substrate for a set amount of time (up to \qty{2}{\hour}).
The substrate was always suspended vertically, and the solution was continuously
stirred during the deposition.
To prepare the deposition bath (per above), I started by dissolving
\reactant[mass=1.2365]{cadmiumsulfatehydrate} in \reactant[concentration=12.8]{ammonia}
to $[\ch{Cd^{2+}}]=\qty{24}{\milli\Molar}$
then volumetrically diluted it by a factor of eight to
\reactant[%
concentration=3,%
concentration-unit=\milli\Molar,%
solvent={\qty{12.8}{\Molar} \ch{NH3\aq}}]{cadmiumsulfate}.
The cadmium sulfate salt was sourced from Merck (\ch{3 CdSO4 * 8 H2O}, \emph{pro analysi}).
Next I dissolved \reactant[mass=0.2284]{thiourea} in \qty{100}{\milli\L}~\water\
for a concentration of \qty{30}{\milli\Molar}.
The thiourea powder was sourced from Merck, \emph{for synthesis}.
% print only the number: \reactant*[switch=true]{CdSO4}
%\input{assets/aux/fig/fig_0203-CBD-synthesis.Rnw}
<<child=here::here('assets/aux/fig/fig_0203-CBD-synthesis.Rnw')>>=
# \label{fig:0203-CBD-station}
@
For a \gls{CBD}, first \qty{5}{\milli\L} of \reactant*[switch=true]{thiourea}
was added to each deposition bath (\cf\ \cref{fig:0203-CBD-station})
and allowed to reach thermal equilibrium at the set temperature
(at least \qty{15}{\minute} \qty{60}{\celsius}).
Simultaneously, a container with \reactant*[switch=true]{cadmiumsulfate} was also heated.
The substrates were lowered into each of the four deposition baths, and
\qty{10}{\mL} of \reactant*[switch=true]{cadmiumsulfate} was then added to each to start
the \gls{CBD} reaction.
The point of adding the \ch{Cd}-precursor at the last moment was to avoid unnecessarily
subjecting the \ch{ZnO}/\ch{Fe2O3} substrate to the strongly alkaline solution.
After the deposition was completed, the back of the glass substrate was
cleaned with a cotton swab soaked in $\approx\qty{0.75}{\milli\Molar}$ \ch{HCl},
then both sides were rinsed with deionized water and blow-dried with \ch{N2}.
The earliest report \cite{Nagao1968} of chemical bath deposition of \ch{CdS} from an alkaline
solution with an ammonium salt at room temperature produced thick films in the cubic structure.
Later work \cite{Nair1988,Mondal1983} found that the thickness of the deposit
\emph{decreased} with bath temperature.
The \ch{CdS} deposition proceeds along the following steps
(most mechanistic studies of \gls{CBD} of \ch{CdS} have proposed the so called
\emph{ion-by-ion} mechanism, which is what we present here) \cite{Hodes2003,Tak2009}:
\begin{subreactions}\begin{reactions}
NH3 + H2O <=>& NH4\pch[] + OH\mch[] \AddRxnDesc{Ammonium~formation} "\label{rxn:CBD-ammonia}" \\
Cd\pch[2] + 4 NH3 <=>& [Cd(NH3)4]\pch[2] \AddRxnDesc{Formation~of~cadmium~complex} "\label{rxn:CBD-Cd-complex}" \\
(NH2)2CS + OH\mch[] ->& CH2N2 + H2O + HS\mch[] \AddRxnDesc{Formation~of~hydrogen~sulfide} "\label{rxn:CBD-thiourea}" \\
HS\mch[] + OH\mch[] ->& S\mch[2] + H2O \AddRxnDesc{Release~of~sulfide~ion} "\label{rxn:CBD-sulfide}" \\
Cd\pch[2] + S\mch[2] <=>& CdS\sld{} \AddRxnDesc{Cadmium~sulfide~ion~by~ion} "\label{rxn:CBD-CdS-ionbyion}" \\
Cd\pch[2] + 2 OH\mch[] ->& Cd(OH)2\sld{} \AddRxnDesc{Cadmium~hydroxide~precipitation} "\label{rxn:CBD-OH-cluster}" \\
Cd(OH)2 + S\mch[2] ->& CdS\sld{} + 2 OH\mch[] \AddRxnDesc{Cadmium~hydroxide~dissolution} "\label{rxn:CBD-CdS-OH-cluster}"
\end{reactions}\end{subreactions}
usually described with the following overall reaction
\addtocounter{reaction}{-1}
\begin{reaction}
[Cd(NH3)4]\pch[2] + (NH2)2CS + 2 OH\mch[] ->
CdS + CH2N2 + 4 NH3 + 2 H2O \AddRxnDesc{Deposition~of~cadmium~sulfide} "\label{rxn:CBD-dep}"
\end{reaction}
Ammonia dissolved in water produces a hydroxide ion (\cref{rxn:CBD-ammonia}) and
forms a cadmium tetramine complex (\cref{rxn:CBD-Cd-complex}) which is responsible
for slowing the release of solvated \ch{Cd\pch[2]} ions.
Sulfide ions are released (\cref{rxn:CBD-sulfide}) by the hydrolysis of thiourea
in alkaline solution (\cref{rxn:CBD-thiourea}) \cite{Ortega-Borges1993,Hodes2003}.
When the product of \ch{[Cd\pch[2]]} and \ch{[S\mch[2]]} exceed the solubility
product%
\footnote{%
The \glsname{solubility_product} of \ch{CdS} has variously been reported in literature as
\num[retain-unity-mantissa=false]{1e-25} \cite{Ortega-Borges1993},
\num[retain-unity-mantissa=false]{1e-28} \cite{Hodes2003},
\num{7.1e-28} \cite{Oladeji1997}, and
\num{1.4e-29} \cite{Nair1988}.
}
of \ch{CdS} it precipitates (\cref{rxn:CBD-CdS-ionbyion}) either homogeneously
in the solution (forming colloids) \cite{Hodes1987} or
heterogeneously at the substrate surface \cite{Kaur1980}, leading to a film.
Note that formation of the hydroxide is not desired, but may still occur (which
is why it is included in the schema), but if it does occur the likelihood of sulfide
substituting for the hydroxide and forming the desired sulfide is very high due
to the much higher \glsname{solubility_product} (\num{2e-14}) of \ch{Cd(OH)2}.
%%%% SECTION
\section{Atomic layer deposition of iron oxide}
\label{synthesis:atomic-layer-deposition}
After having successfully coated electrodeposited \zincox\ \glsplural{NR} with
\ch{CdS} and achieved the intended effect of sensitizing \ZnO\ to visible
light, we considered other conformal coatings
that could alleviate two of the main drawbacks with \ch{CdS}, \namely,
the alkaline conditions during its deposition, and the toxicity of the \ch{Cd\pch[2]} ion.
Hewing to the principle of simplicity we established earlier, and considering
our alternatives, we landed on the abundant
\hematite\ (\glstext{hematite}), \ie, the principal component of rust.
The iron oxides and iron oxide hydroxides (see \cref{tab:0300-pxrd-pdfs}) have
a particularly well-studied
chemistry, which is no wonder considering their immense economic importance.
As the most thermodynamically stable iron oxide phase at \gls{STP}, \glstext{hematite} is
the end product of all steel corrosion, and has as such been studied in detail.
\hematite\ has a band gap of \Eg{2.2} (\qty{564}{\nm}), \ie, well into the visible
range, and is also non-toxic, resistant to chemical corrosion in both dark and
illuminated conditions, and its \gls{VBE} is suitable for oxygen evolution
from \water\ (\cf\ \cref{fig:0100-bandgaps-all}).