This post could be classified as being about carbon utilization, the U in CCUS. In these cases, it involves changing waste industrial gases such as CO2 into chemicals and fuels, one of the major pathways of carbon utilization. Technical feasibility continues to be assessed via projects like the Flue2Chem Initiative which aims to convert captured carbon into products and is also considered recycling and developing a circular economy.
One
project modeled the lifecycle of industrial gas recovery for carbon
utilization, concluding that the environmental benefits were considerable and
desirable, but the costs were high. No real surprise there. Specifically, the
study evaluated the life cycle of converting waste gases from steel plants and
paper mills in the UK into the production of chemical surfactants. The
researchers concluded that making surfactants from steel and paper mill waste
gases would reduce global warming potential (GWP) by 82% over making them from
conventional processes.
The
waste gas recovery process requires heat, electricity, and hydrogen. Where
those come from affects the final GWP of the process. The greenest scenario
involves renewable electricity and green hydrogen. The steel and paper mill
study was published in the Journal of CO2 Utilization. Highlights, tables,
and figures from the study, and its abstract are shown below.
Abstract
This novel study presents
an effective comprehensive life cycle assessment (LCA) of a novel sustainable
carbon dioxide capture and utilization (CCU) system to co-produce alcohol
ethoxylate (AE7), a valuable surfactant (a high-value chemical component of liquid
detergents), and low-medium distillate range liquid fuel. Conventionally, AE7
is produced by reacting fatty alcohols with ethylene oxide from mostly fossil
and marginally bio-based resources. This research develops novel AE7 production
using carbon sources from flue gas of paper and steel industries, addressing a
critical gap in the literature. The core process is Fischer-Tropsch (FT)
synthesis using syngas formed by the reverse-water-gas-shift reaction, where
recycled CO2 reacts with H2. FT produces C11-C13 alkanes and a light-to-medium
fuel co-product. The alkanes are converted into C12-C14 fatty alcohols through
dehydrogenation, hydroformylation, and hydrogenation. Fatty alcohols react with
ethylene oxide to form AE7. The yields (w/w) of AE7 and the fuel co-products
are 3.7 % and
3.4 % for
paper industry flue gas, and 8.0 % and 9.5 % for steel industry flue gas,
respectively. Renewable (wind) electricity meets the hydrogen demand and
electricity needs for the reactions, a total of 13.4 and 33.3 kWh/kg flue gas,
respectively. The life cycle impact assessment includes global warming potential
(GWP) and other impacts using ReCiPe, Impact+ , and Product Environmental Footprint
methods. Baseline scenarios show GWP ranging from 2.2 to 3.6 kg CO2e/kg surfactant for conventional
cradle-to-gate AE production systems. The new systems have GWP ranging 0.4–1.3 kg CO2e/kg flue gas (cradle-to-gate)
using mass allocation. Meanwhile, the paper industry’s flue gas system has biogenic CO2, while the steel
industry’s CO2 is fossil-based. Considering the
GWP reductions due to biogenic CO2 contents, their overall GWP is 2.56 kg CO2e and 10.33 kg CO2e per kg of product (AE7 +fuel) (cradle-to-grave) using
economic allocation. Thus, biogenic CCU is critical for the sustainable
co-production of high-value surfactants and fuel.
Another
study published in December 2024 in Digital Chemical Engineering modeled costs
for converting steel mill waste gases the chemical surfactant alcohol
ethoxylate (AE7). Perhaps the key finding is that the lowest minimum selling
price MSP of $8.77/kg exceeds the forecasted $3.75/kg for fossil-based AE7 and
the biggest factor affecting MSP was the cost of green hydrogen.
It
makes me wonder why they didn’t model blue hydrogen, made from the steam
reforming of methane with CO2 capture, since blue hydrogen is cheaper than
green hydrogen. Since, as MS Copilot informs me, green hydrogen is 2-3 times
more costly than blue hydrogen, it seems to me utilizing blue hydrogen in the
recovery and utilization process can be comparable or even better priced than
fossil-based surfactants, presumably where the hydrogen is grey hydrogen
sourced from the unabated steam reforming of methane. The total environmental
benefits in the form of GWP would be somewhat less but the costs would make it
feasible. I really think they should incorporate blue hydrogen into their
modeling. If surfactants can be produced with blue hydrogen at a comparable
cost to fossil-based methods then the environmental and climate benefits could
be obtained with little to no change in costs, which makes it a no-brainer,
right?
An
April 2025 study in Nature: Scientific Reports examined
optimizing sintering by optimizing air volume. According to Wikipedia”
“Sintering or frittage
is the process of compacting and forming a solid mass of material by pressure
or heat without melting it to the point of liquefaction. Sintering happens as
part of a manufacturing process used with metals, ceramics, plastics, and other
materials. The atoms/molecules in the sintered material diffuse across the
boundaries of the particles, fusing the particles together and creating a solid
piece.”
The optimization of
sintering means that the fuel chemical energy is utilized most efficiently. The
researchers found an ideal air volume to optimize the process. It is another
way waste industrial gases can be utilized most efficiently, which means less
emissions. The abstract is shown below.
Abstract
This study examines the
impact of sintering air volume on the characteristics of combustible lean gases
(CO, H2, and CH4) in sintering flue gas. By conducting experiments using a
fixed combustion test bench, we analyzed the changes in sintering negative pressure,
flue gas composition, and sinter quality under various air volume conditions.
The results demonstrate that an air volume of 90 m³/(m²·min) leads to a lower
combustion ratio (ω(CO)/ω(CO + CO2)), indicating more efficient
utilization of fuel chemical energy. Additionally, increasing the air volume
per unit area reduces the sintering time. The mass fractions of CO and H2
decrease with increasing air volume, and the mass fraction of CH4 also
decreases, underscoring the importance of its recovery due to its high global
warming potential (28 times that of CO2). These findings provide guidance for
optimizing sintering conditions to improve lean gas recovery and reduce
environmental impacts.
References:
How
industrial waste gases could replace fossil fuels in everyday consumer products.
Science X staff. TechXplore. March 13, 2025. How industrial waste gases could
replace fossil fuels in everyday consumer products
Novel
comprehensive life cycle assessment (LCA) of sustainable flue gas carbon
capture and utilization (CCU) for surfactant and fuel via Fischer-Tropsch
synthesis. Jhuma Sadhukhan, Oliver J. Fisher, Benjamin Cummings, and Jin Xuan.
Journal of CO2
Utilization. Volume 92, February 2025, 103013. Novel comprehensive life cycle
assessment (LCA) of sustainable flue gas carbon capture and utilization (CCU)
for surfactant and fuel via Fischer-Tropsch synthesis - ScienceDirect
Optimizing
sintering air volume for enhanced lean gas recovery and environmental
performance. Xinwei Guo, Jiaoyang Ji, Yanyang Gao, Xingyuan Wu, Yiming Guo,
Weishu Wang, Meng Wen, Xiaojiang Wu & Zhongxiao Zhang. Scientific Reports
volume 15, Article number: 11146 (2025). Optimizing sintering air volume for
enhanced lean gas recovery and environmental performance | Scientific Reports
Flue2Chem:
initiative to make products from CO2 begins. SCI. March 13, 2024. Flue2Chem:
initiative to make products from CO2 begins
Techno-economic
analysis and process simulation of alkoxylated surfactant production in a
circular carbon economy framework. Oliver J. Fisher, Jhuma Sadhukhan, Thorin
Daniel, and Jin Xuan. Digital Chemical Engineering. Volume 13, December 2024,
100199. Techno-economic
analysis and process simulation of alkoxylated surfactant production in a
circular carbon economy framework - ScienceDirect
Flue2Chem.
SCI - Flue2Chem
Sintering.
Wikipedia. Sintering -
Wikipedia
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