Crystal Growth Kinetics of Na <sub> <b>2</b> </sub> CO <sub> <b>3</b> </sub> Hydrate Phases in the Na <sub> <b>2</b> </sub> CO <sub> <b>3</b> </sub> –NaOH–H <sub> <b>2</b> </sub> O System for Sustainable Soda Ash Production

As part of the CODA project, which is laying the foundation for a novel sustainable soda ash (Na<sub>2</sub>CO<sub>3</sub>) production strategy, this study provides essential parameters and insights for the design, optimization, and scale-up of the required crystallization processes. It investigates the crystal growth kinetics of Na<sub>2</sub>CO<sub>3</sub>·10H<sub>2</sub>O and Na<sub>2</sub>CO<sub>3</sub>·1H<sub>2</sub>O within the Na<sub>2</sub>CO<sub>3</sub>-NaOH-H<sub>2</sub>O system using cooling and vacuum evaporative crystallization, respectively. Experimental studies were conducted utilizing a shortcut method based on seeded batch experiments in a 3 L-scale. The growth rate of Na<sub>2</sub>CO<sub>3</sub>·10H<sub>2</sub>O was studied over a temperature range of 17-6 °C, while Na<sub>2</sub>CO<sub>3</sub>·1H<sub>2</sub>O was examined at a constant temperature of 50 °C under a fixed evaporation rate. Minimal secondary nucleation was confirmed through offline crystal size distribution measurements. Na<sub>2</sub>CO<sub>3</sub>·10H<sub>2</sub>O growth peaked at a critical supersaturation (∼1.03) and afterward slowed despite further increases in supersaturation, alluding to a potential crystal surface roughening mechanism. The presence of NaOH did not alter the crystal habit of Na<sub>2</sub>CO<sub>3</sub>·10H<sub>2</sub>O but did alter that of Na<sub>2</sub>CO<sub>3</sub>·1H<sub>2</sub>O. Despite the relatively low supersaturation, the monohydrate exhibited a higher growth rate than the decahydrate. Furthermore, the monohydrate produced yielded dense (heavy) soda ash, addressing a significant challenge within the soda ash industry.

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Journal
ACS Omega
Published
2026-01-23
DOI
https://doi.org/10.1021/acsomega.5c09440
Primary Topic
Chemical Looping and Thermochemical Processes
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article
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article

Crystal Growth Kinetics of Na 2 CO 3 Hydrate Phases in the Na 2 CO 3 –NaOH–H 2 O System for Sustainable Soda Ash Production

H. Lorenz, Jonathan Gänsch, Somayyeh Ghaffari, Peter Schulze
ACS Omega
Chemical Looping and Thermochemical Processes
article

Crystal Growth Kinetics of Na 2 CO 3 Hydrate Phases in the Na 2 CO 3 –NaOH–H 2 O System for Sustainable Soda Ash Production

H. Lorenz, Jonathan Gänsch, Somayyeh Ghaffari, Peter Schulze
article en

Abstract

As part of the CODA project, which is laying the foundation for a novel sustainable soda ash (Na<sub>2</sub>CO<sub>3</sub>) production strategy, this study provides essential parameters and insights for the design, optimization, and scale-up of the required crystallization processes. It investigates the crystal growth kinetics of Na<sub>2</sub>CO<sub>3</sub>·10H<sub>2</sub>O and Na<sub>2</sub>CO<sub>3</sub>·1H<sub>2</sub>O within the Na<sub>2</sub>CO<sub>3</sub>-NaOH-H<sub>2</sub>O system using cooling and vacuum evaporative crystallization, respectively. Experimental studies were conducted utilizing a shortcut method based on seeded batch experiments in a 3 L-scale. The growth rate of Na<sub>2</sub>CO<sub>3</sub>·10H<sub>2</sub>O was studied over a temperature range of 17-6 °C, while Na<sub>2</sub>CO<sub>3</sub>·1H<sub>2</sub>O was examined at a constant temperature of 50 °C under a fixed evaporation rate. Minimal secondary nucleation was confirmed through offline crystal size distribution measurements. Na<sub>2</sub>CO<sub>3</sub>·10H<sub>2</sub>O growth peaked at a critical supersaturation (∼1.03) and afterward slowed despite further increases in supersaturation, alluding to a potential crystal surface roughening mechanism. The presence of NaOH did not alter the crystal habit of Na<sub>2</sub>CO<sub>3</sub>·10H<sub>2</sub>O but did alter that of Na<sub>2</sub>CO<sub>3</sub>·1H<sub>2</sub>O. Despite the relatively low supersaturation, the monohydrate exhibited a higher growth rate than the decahydrate. Furthermore, the monohydrate produced yielded dense (heavy) soda ash, addressing a significant challenge within the soda ash industry.

ACS OmegaVol. 11(5)
Max Planck Institute for Dynamics of Complex Technical Systems (DE)
Responsible consumption and production
Openalex Percentile: Top 80%
Chemical Looping and Thermochemical Processes
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Crystal Growth Kinetics of Na <sub> <b>2</b> </sub> CO <sub> <b>3</b> </sub> Hydrate Phases in the Na <sub> <b>2</b> </sub> CO <sub> <b>3</b> </sub> –NaOH–H <sub> <b>2</b> </sub> O System for Sustainable Soda Ash Production — H. Lorenz, Jonathan Gänsch, et al. · ACS Omega (2026) | TGRS Research Map | TGRS