TY - JOUR
T1 - Effect of CaCO3 crystal morphology on osmosis membrane performance during integration of direct air capture with pressure retarded osmosis process
AU - Guan, Lingxue
AU - Richter, Christiaan Petrus
AU - Wu, Bing
N1 - Publisher Copyright: © 2025 Elsevier B.V.
PY - 2025/12/14
Y1 - 2025/12/14
N2 - The direct air capture-pressure retarded osmosis (DAC-PRO) hybrid process was proposed as a feasible modification to mitigate the high energy and water consumption of the hydroxide-based DAC process. However, residual calcium carbonate (i.e., CaCO3) with various polymorph compositions may be present after sorbent regeneration in the DAC process, potentially causing scaling in the PRO process using the CO2-captured hydroxide solution as the draw solution. This study investigated the osmosis membrane performance in the presence of different polymorphs of CaCO3 scalants (formed at 20 °C, 40 °C, and 60 °C) in NaHCO3- or NaHCO3/Na2CO3-based draw solutions under PRO mode. The results revealed that (1) increasing the calcite proportion in the scalants (a mixture of calcite, vaterite, aragonite) promoted the formation of cake layers with higher porosity and lower resistance, while increasing amorphous calcium carbonate (ACC) in the scalants (a mixture of ACC, vaterite, aragonite) caused denser and more resistant scaling layers; (2) the properties of CaCO3 polymorphs, such as surface charge, specific surface area, and hydration level, were associated with scalant-scalant and scalant-membrane interactions and further influenced on water and reverse solute fluxes. The ACC-dominant scaling layer resulted in more water flux decline and reverse flux increase compared to those deposited with other CaCO3 polymorphs; (3) the composition ratios of CaCO3 polymorphs in the scaling layer dynamically changed with PRO operation, leading to variable scaling layer properties (porosity, resistance) and water/reverse solute fluxes. This study reveals the potential influences of operating conditions of the DAC process on the PRO performance.
AB - The direct air capture-pressure retarded osmosis (DAC-PRO) hybrid process was proposed as a feasible modification to mitigate the high energy and water consumption of the hydroxide-based DAC process. However, residual calcium carbonate (i.e., CaCO3) with various polymorph compositions may be present after sorbent regeneration in the DAC process, potentially causing scaling in the PRO process using the CO2-captured hydroxide solution as the draw solution. This study investigated the osmosis membrane performance in the presence of different polymorphs of CaCO3 scalants (formed at 20 °C, 40 °C, and 60 °C) in NaHCO3- or NaHCO3/Na2CO3-based draw solutions under PRO mode. The results revealed that (1) increasing the calcite proportion in the scalants (a mixture of calcite, vaterite, aragonite) promoted the formation of cake layers with higher porosity and lower resistance, while increasing amorphous calcium carbonate (ACC) in the scalants (a mixture of ACC, vaterite, aragonite) caused denser and more resistant scaling layers; (2) the properties of CaCO3 polymorphs, such as surface charge, specific surface area, and hydration level, were associated with scalant-scalant and scalant-membrane interactions and further influenced on water and reverse solute fluxes. The ACC-dominant scaling layer resulted in more water flux decline and reverse flux increase compared to those deposited with other CaCO3 polymorphs; (3) the composition ratios of CaCO3 polymorphs in the scaling layer dynamically changed with PRO operation, leading to variable scaling layer properties (porosity, resistance) and water/reverse solute fluxes. This study reveals the potential influences of operating conditions of the DAC process on the PRO performance.
KW - Calcium carbonate
KW - Osmosis membrane
KW - Reverse salt flux
KW - Scalant morphology
KW - Scaling
KW - Water flux
UR - https://www.scopus.com/pages/publications/105007990407
U2 - 10.1016/j.seppur.2025.133940
DO - 10.1016/j.seppur.2025.133940
M3 - Article
SN - 1383-5866
VL - 376
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 133940
ER -