TY - JOUR
T1 - Calcination-free production of calcium hydroxide at sub-boiling temperatures
AU - Vallejo Castaño, Sara
AU - Callagon La Plante, Erika
AU - Shimoda, Sho
AU - Wang, Bu
AU - Neithalath, Narayanan
AU - Sant, Gaurav
AU - Pilon, Laurent
N1 - Funding Information:
The authors acknowledge nancial support for this research from the Department of Energy via: (a) The Office of Fossil Energy's National Energy Technology Laboratory (NETL : DE-FE0029825), (b) The Advanced Research Projects Agency-Energy (ARPA-E : DE-AR-0001147) and (c) TRANSCEND: a UCLA-NIST Consortium that is supported by its Industry and Agency partners. This research was conducted in the Laboratory for Chemistry of Construction Materials (LC2) and the Molecular Instrumentation Center at UCLA. As such, the authors gratefully acknowledge the support that has made these laboratories and their operations possible. The contents of this paper reect the views and opinions of the authors, who are responsible for the accuracy of the datasets presented herein, and do not reect the views and/or polices of the agency, nor do the contents constitute a specication, standard or regulation. The authors would also like to acknowledge: Michael Moore (TMS International) for the supply of the different slags, Prof. Zongsu Wei (Aarhus University) for his assistance with the Reverse Osmosis (RO) processing, and Boral Resources for their assistance with the XRF analysis of the slags.
Publisher Copyright:
© The Royal Society of Chemistry.
PY - 2021/1/6
Y1 - 2021/1/6
N2 - Calcium hydroxide (Ca(OH)2), a commodity chemical, finds use in diverse industries ranging from food, to environmental remediation and construction. However, the current thermal process of Ca(OH)2 production via limestone calcination is energy- and CO2-intensive. Herein, we demonstrate a novel aqueous-phase calcination-free process to precipitate Ca(OH)2 from saturated solutions at sub-boiling temperatures in three steps. First, calcium was extracted from an archetypal alkaline industrial waste, a steel slag, to produce an alkaline leachate. Second, the leachate was concentrated using reverse osmosis (RO) processing. This elevated the Ca-abundance in the leachate to a level approaching Ca(OH)2 saturation at ambient temperature. Thereafter, Ca(OH)2 was precipitated from the concentrated leachate by forcing a temperature excursion in excess of 65 °C while exploiting the retrograde solubility of Ca(OH)2. This nature of temperature swing can be forced using low-grade waste heat (≤100 °C) as is often available at power generation, and industrial facilities, or using solar thermal heat. Based on a detailed accounting of the mass and energy balances, this new process offers at least ≈65% lower CO2 emissions than incumbent methods of Ca(OH)2, and potentially, cement production.
AB - Calcium hydroxide (Ca(OH)2), a commodity chemical, finds use in diverse industries ranging from food, to environmental remediation and construction. However, the current thermal process of Ca(OH)2 production via limestone calcination is energy- and CO2-intensive. Herein, we demonstrate a novel aqueous-phase calcination-free process to precipitate Ca(OH)2 from saturated solutions at sub-boiling temperatures in three steps. First, calcium was extracted from an archetypal alkaline industrial waste, a steel slag, to produce an alkaline leachate. Second, the leachate was concentrated using reverse osmosis (RO) processing. This elevated the Ca-abundance in the leachate to a level approaching Ca(OH)2 saturation at ambient temperature. Thereafter, Ca(OH)2 was precipitated from the concentrated leachate by forcing a temperature excursion in excess of 65 °C while exploiting the retrograde solubility of Ca(OH)2. This nature of temperature swing can be forced using low-grade waste heat (≤100 °C) as is often available at power generation, and industrial facilities, or using solar thermal heat. Based on a detailed accounting of the mass and energy balances, this new process offers at least ≈65% lower CO2 emissions than incumbent methods of Ca(OH)2, and potentially, cement production.
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U2 - 10.1039/d0ra08449b
DO - 10.1039/d0ra08449b
M3 - Article
AN - SCOPUS:85099350301
SN - 2046-2069
VL - 11
SP - 1762
EP - 1772
JO - RSC Advances
JF - RSC Advances
IS - 3
ER -