Stressing the AMP/PZ-BasedSolvent CESAR1PilotPlant Testing on the Effect of O<sub>2</sub>, NO<sub>2,</sub> andRegeneration Temperature on Solvent Degradation

Degradation of amine-based CO<sub>2</sub> capture solvents causes not only higher solvent consumption but also more effort for controlling the emissions of volatile degradation products and for the removal of degradation products that are accumulating in the solvent. Guiding principles to minimize degradation processes generally are targeting at the reduction of oxidative and thermal stress for the solvent during the operation of the capture plant. For example, it is recommended to reduce the contact of potentially aggressive compounds in the flue gas, like O<sub>2</sub> and NO<sub>2</sub>, with the amines as much as possible by their removal from the flue gas or the solvent. Additionally, the maximum temperature of the CO<sub>2</sub>-loaded solvent in the reboiler and desorber sump and the time of exposure should be minimized. The results of testing campaigns with the CESAR1 solvent at the pilot plant at Niederaussem show that the effects of elevated O<sub>2</sub> and NO<sub>2</sub> contents in the flue gas (increase from 5 to 16 vol % O<sub>2</sub> and from <0.1 to >53 mg/m<sup>3</sup> NO<sub>2</sub>) and of an elevated solvent regeneration temperature (increase from 120 to 130 °C) are small.

Publication Details

Journal
Figshare
Published
2025-02-06
DOI
https://doi.org/10.1021/acs.iecr.4c04285.s001
Primary Topic
Mycorrhizal Fungi and Plant Interactions
Type
article
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article

Stressing the AMP/PZ-BasedSolvent CESAR1PilotPlant Testing on the Effect of O2, NO2, andRegeneration Temperature on Solvent Degradation

Figshare
Mycorrhizal Fungi and Plant Interactions
article

Stressing the AMP/PZ-BasedSolvent CESAR1PilotPlant Testing on the Effect of O2, NO2, andRegeneration Temperature on Solvent Degradation

article en

Abstract

Degradation of amine-based CO<sub>2</sub> capture solvents causes not only higher solvent consumption but also more effort for controlling the emissions of volatile degradation products and for the removal of degradation products that are accumulating in the solvent. Guiding principles to minimize degradation processes generally are targeting at the reduction of oxidative and thermal stress for the solvent during the operation of the capture plant. For example, it is recommended to reduce the contact of potentially aggressive compounds in the flue gas, like O<sub>2</sub> and NO<sub>2</sub>, with the amines as much as possible by their removal from the flue gas or the solvent. Additionally, the maximum temperature of the CO<sub>2</sub>-loaded solvent in the reboiler and desorber sump and the time of exposure should be minimized. The results of testing campaigns with the CESAR1 solvent at the pilot plant at Niederaussem show that the effects of elevated O<sub>2</sub> and NO<sub>2</sub> contents in the flue gas (increase from 5 to 16 vol % O<sub>2</sub> and from <0.1 to >53 mg/m<sup>3</sup> NO<sub>2</sub>) and of an elevated solvent regeneration temperature (increase from 120 to 130 °C) are small.

Figshare
Openalex Percentile: Top 57%
Mycorrhizal Fungi and Plant Interactions
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