journal article·2020-01-14

Toward a Mechanistic Understanding and Optimization of Molten Alkali Metal Borates (AxB1–xO1.5–x) for High-Temperature CO2 Capture

Cameron Halliday, Takuya Harada, T. Alan Hatton

Chemistry of Materials· Volume 32· Issue 1
Publisher page

Abstract

Carbon capture, utilization, and storage technologies are needed to meet carbon emission reduction targets and prepare the energy industry for a carbon constrained world. Recent breakthroughs have identified the first liquid phase sorbents for CO2 capture at high temperatures. In this work, the material design space of the molten alkali metal borates (AxB1–xO1.5–x) is explored finding sodium and sodium-rich lithium–sodium borates with a mixing ratio, x, of around 0.75 to be optimal. A mechanistic understanding of the material is developed through exploration of the sodium borate phase diagram, the development of a kinetic equilibrium model, and estimation of effective diffusion coefficients. Interesting features of the sorbents, such as the proposed formation of dicarbonate ions and counter-intuitive trends in the diffusion coefficient, are identified and explained with implications for the design of future high temperature carbon capture facilities discussed.
Source: openalex_inverted_index · Quality: baseline

Research context

OpenAlex topics: Chemical Looping and Thermochemical Processes · Carbon Dioxide Capture Technologies · Thermal Expansion and Ionic Conductivity

SciVX discovery tags are terminology-based. OpenAlex topics are source-provided classifications.

Affiliations

Department of Chemical Engineering, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Cambridge, Massachusetts 02139, United States

Funding

Massachusetts Institute of Technology

References (55)

Show source-provided references
1. Global CCS Institute. The Global Status of CCS: 2018: Canberra, Australia, 2018.
2. 10.1039/c7ee02342a10.1039/c7ee02342a ↗
3. 10.1016/j.jcou.2014.12.00110.1016/j.jcou.2014.12.001 ↗
4. Song C. · 2002 · 809 · 210.1021/bk-2002-0809.ch001 ↗
5. 10.1016/j.pecs.2012.03.00310.1016/j.pecs.2012.03.003 ↗
6. 10.1016/j.rser.2014.07.09310.1016/j.rser.2014.07.093 ↗
7. 10.1016/j.supflu.2017.07.02910.1016/j.supflu.2017.07.029 ↗
8. 10.1016/j.egypro.2017.03.120910.1016/j.egypro.2017.03.1209 ↗
9. 10.1021/es015886110.1021/es0158861 ↗
10. 10.1016/j.ijggc.2015.05.02810.1016/j.ijggc.2015.05.028 ↗
11. 10.1016/j.ijhydene.2016.01.00910.1016/j.ijhydene.2016.01.009 ↗
12. 10.1016/s0360-3199(02)00074-510.1016/s0360-3199(02)00074-5 ↗
13. 10.1016/j.compchemeng.2016.08.00510.1016/j.compchemeng.2016.08.005 ↗
14. Bottoms, R. Process for Separating Acidic Gases. U.S. Patent 1,783,901 A, 1930.
15. 10.1126/science.117673110.1126/science.1176731 ↗
16. 10.1016/j.applthermaleng.2009.05.00510.1016/j.applthermaleng.2009.05.005 ↗
17. 10.1016/j.ijggc.2012.06.01510.1016/j.ijggc.2012.06.015 ↗
18. Global CCS Institute. CO2 Capture Technologies: Precombustion with CO2 Capture: Canberra, Australia, 2012.
19. 10.1021/ef201142w10.1021/ef201142w ↗
20. 10.1021/acs.iecr.5b0138410.1021/acs.iecr.5b01384 ↗
21. 10.1021/ie403000610.1021/ie4030006 ↗
22. 10.1016/j.enconman.2018.09.05810.1016/j.enconman.2018.09.058 ↗
23. 10.1016/j.egypro.2009.01.09710.1016/j.egypro.2009.01.097 ↗
24. 10.1016/j.ijggc.2012.06.01010.1016/j.ijggc.2012.06.010 ↗
25. 10.1016/j.ijggc.2012.06.02110.1016/j.ijggc.2012.06.021 ↗
26. 10.1016/j.ces.2010.04.03810.1016/j.ces.2010.04.038 ↗
27. 10.1021/cm503295g10.1021/cm503295g ↗
28. 10.1021/acs.chemmater.5b0390410.1021/acs.chemmater.5b03904 ↗
29. Pfeiffer H. · 2010 · 1056 · 23310.1021/bk-2010-1056.ch015 ↗
30. 10.1016/j.apenergy.2015.10.12110.1016/j.apenergy.2015.10.121 ↗
31. 10.1039/c7ta06167f10.1039/c7ta06167f ↗
32. 10.1039/c4ee01647e10.1039/c4ee01647e ↗
33. 10.1039/c5ee01228g10.1039/c5ee01228g ↗
34. 10.1016/j.egypro.2009.01.08210.1016/j.egypro.2009.01.082 ↗
35. 10.1021/ie010867l10.1021/ie010867l ↗
36. 10.1016/j.ijggc.2014.02.01510.1016/j.ijggc.2014.02.015 ↗
37. 10.1016/j.ces.2005.08.02210.1016/j.ces.2005.08.022 ↗
38. 10.1021/acssuschemeng.9b0091110.1021/acssuschemeng.9b00911 ↗
39. 10.1002/aic.1233710.1002/aic.12337 ↗
40. 10.1039/c9ta09122j10.1039/c9ta09122j ↗
41. 10.1002/aic.69029011110.1002/aic.690290111 ↗
42. 10.1016/j.fuproc.2005.01.01210.1016/j.fuproc.2005.01.012 ↗
43. 10.1016/j.ijggc.2013.04.00910.1016/j.ijggc.2013.04.009 ↗
44. 10.1002/ente.20160062810.1002/ente.201600628 ↗
45. 10.1007/s11669-003-0003-710.1007/s11669-003-0003-7 ↗
46. Tran H. · Pulp Pap. Can. · 1999 · 100 · 35
47. Lindberg, D. Thermochemistry and melting properties of alkali salt mixtures in black liquor conversion processes. Ph.D. Dissertation, Åbo Akademi University, Åbo, Finland, 2007.
48. 10.1021/ie040016o10.1021/ie040016o ↗
49. Tran, H.; Mao, X.; Lesmana, N.; Kochesfahani, S. H.; Bair, C. M.; McBroom, R. Effects of partial borate autocausticizing on kraft recovery operations—The technology is particularly good for boilers that are thermally limited. Pulp and Paper Canada, 2002; Vol. 103, pp 74–78.
50. 10.1016/0378-4363(79)90102-510.1016/0378-4363(79)90102-5 ↗
51. 10.1088/0953-8984/7/23/01010.1088/0953-8984/7/23/010 ↗
52. 10.1002/(sici)1099-0682(199904)1999:4<583::aid-ejic583>3.3.co;2-p10.1002/(sici)1099-0682(199904)1999:4<583::aid-ejic583>3.3.co;2-p ↗
53. 10.1063/1.55566510.1063/1.555665 ↗
54. Kamitsos E. I. · Phys. Chem. Glasses · 1989 · 30 · 19
55. 10.1016/0022-3093(89)90288-310.1016/0022-3093(89)90288-3 ↗