Hydrate-based carbon capture via pressure swing in a packed bed of ice

The formation of mixed gas hydrates for pre- or post-combustion capture of carbon dioxide is considered a promising alternative to conventional carbon capture technologies. Yet, to keep up with conventional technologies or even reduce the cost of capture associated with them, a hydrate-based technology must have (1) a short induction time, (2) fast formation kinetics, and (3) moderate process conditions. To date, these requirements can only be met by adding promoters to the system, which comes at its own cost and disadvantages. Here, we show that the requirements can also be met without promoters by forming mixed gas hydrates in a packed bed of ice stabilized by fumed silica. While the high specific surface area of the packed bed warrants short induction times and fast kinetics, low temperatures ensure both moderate formation pressures and a high CO 2 selectivity. The favorable properties can be maintained and even improved upon over many capture/regeneration cycles when operated at temperatures lower than 253 K, as this ensures a continuous formation of pores in the ice. We demonstrate the advantages of this route for carbon capture on a bench scale through batch, semi-batch, and continuous experiments. In semi-batch operation at 233 K and 40 bar, the mole fraction of CO 2 in a synthetic flue gas is reduced from 15 mol% to 2.5 mol%. At the same thermodynamic conditions, a split fraction of 70% and a specific energy consumption below 3.0 GJ/CO 2 are achieved in continuous operation. The inherent advantages and simplicity of this process, a specific energy consumption comparable with the state of the art even though entirely based on the bench-scale experiment, as well as environmental harmlessness, emphasize the potential of this hydrate-based process to meet the demands of the industry at a minimal cost of capture. • Low temperature route to hydrate-based carbon capture strips CO 2 to <2 mol%. • High surface area of silica-stabilized bed of ice mitigates kinetic limitations. • Ice-hydrate transitions capture/release gas without breaking of hydrogen bonds. • More than 18 capture/regeneration cycles with non-degrading performance. • Continuous operation viable with KPIs proving the potential of this technology.

Authors

Institutions

Publication Details

Journal
Separation and Purification Technology
Published
2025-01-09
DOI
https://doi.org/10.1016/j.seppur.2024.131206
Citations
3
Primary Topic
Methane Hydrates and Related Phenomena
Type
article
Field-Weighted Citation Impact
2.58

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Hydrate-based carbon capture via pressure swing in a packed bed of ice

Stefan Arzbacher, Sebastian Hiller, Elias Eder, Miriam Kadinger
3 citations
Separation and Purification Technology
Methane Hydrates and Related Phenomena
2.58
article

Hydrate-based carbon capture via pressure swing in a packed bed of ice

Stefan Arzbacher, Sebastian Hiller, Elias Eder, Miriam Kadinger
article en
3 citations

Abstract

The formation of mixed gas hydrates for pre- or post-combustion capture of carbon dioxide is considered a promising alternative to conventional carbon capture technologies. Yet, to keep up with conventional technologies or even reduce the cost of capture associated with them, a hydrate-based technology must have (1) a short induction time, (2) fast formation kinetics, and (3) moderate process conditions. To date, these requirements can only be met by adding promoters to the system, which comes at its own cost and disadvantages. Here, we show that the requirements can also be met without promoters by forming mixed gas hydrates in a packed bed of ice stabilized by fumed silica. While the high specific surface area of the packed bed warrants short induction times and fast kinetics, low temperatures ensure both moderate formation pressures and a high CO 2 selectivity. The favorable properties can be maintained and even improved upon over many capture/regeneration cycles when operated at temperatures lower than 253 K, as this ensures a continuous formation of pores in the ice. We demonstrate the advantages of this route for carbon capture on a bench scale through batch, semi-batch, and continuous experiments. In semi-batch operation at 233 K and 40 bar, the mole fraction of CO 2 in a synthetic flue gas is reduced from 15 mol% to 2.5 mol%. At the same thermodynamic conditions, a split fraction of 70% and a specific energy consumption below 3.0 GJ/CO 2 are achieved in continuous operation. The inherent advantages and simplicity of this process, a specific energy consumption comparable with the state of the art even though entirely based on the bench-scale experiment, as well as environmental harmlessness, emphasize the potential of this hydrate-based process to meet the demands of the industry at a minimal cost of capture. • Low temperature route to hydrate-based carbon capture strips CO 2 to <2 mol%. • High surface area of silica-stabilized bed of ice mitigates kinetic limitations. • Ice-hydrate transitions capture/release gas without breaking of hydrogen bonds. • More than 18 capture/regeneration cycles with non-degrading performance. • Continuous operation viable with KPIs proving the potential of this technology.

Separation and Purification TechnologyVol. 361
Universität Innsbruck (AT), Vorarlberg University of Applied Sciences (AT)
Austrian Science Fund, Österreichische Forschungsförderungsgesellschaft
Openalex Percentile: Top 14%
Methane Hydrates and Related Phenomena
2.58
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.