The role of intraparticle diffusion path length during electro-assisted regeneration of ion exchange resins: Implications for selective adsorbent design and reverse osmosis pretreatment
被引:20
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作者:
Dong, Hang
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机构:
Stanford Univ, Dept Chem Engn, Stanford, CA 94305 USAStanford Univ, Dept Chem Engn, Stanford, CA 94305 USA
Dong, Hang
[1
]
Wu, Ziyan
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机构:
Stanford Univ, Dept Civil & Environm Engn, Stanford, CA 94305 USAStanford Univ, Dept Chem Engn, Stanford, CA 94305 USA
Wu, Ziyan
[2
]
Liu, Matthew J.
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Stanford Univ, Dept Chem Engn, Stanford, CA 94305 USAStanford Univ, Dept Chem Engn, Stanford, CA 94305 USA
Liu, Matthew J.
[1
]
Tarpeh, William A.
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机构:
Stanford Univ, Dept Chem Engn, Stanford, CA 94305 USA
Engn Res Ctr Reinventing Nations Urban Water Infr, Stanford, CA 94305 USAStanford Univ, Dept Chem Engn, Stanford, CA 94305 USA
Tarpeh, William A.
[1
,3
]
机构:
[1] Stanford Univ, Dept Chem Engn, Stanford, CA 94305 USA
[2] Stanford Univ, Dept Civil & Environm Engn, Stanford, CA 94305 USA
[3] Engn Res Ctr Reinventing Nations Urban Water Infr, Stanford, CA 94305 USA
Electrochemical water splitting;
Ferric oxide nanoparticles;
Hybrid ion exchange;
Membrane scaling;
Phosphate recovery;
Resource recovery;
PHOSPHATE REMOVAL;
PHOSPHORUS RECOVERY;
WATER REUSE;
WASTE;
DESALINATION;
CALCIUM;
CARBON;
PERFORMANCE;
BICARBONATE;
URINE;
D O I:
10.1016/j.cej.2020.127821
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
Inorganic membrane scaling is a major cause of process failure for reverse osmosis (RO). Pretreatment using selective ion exchangers can reduce membrane scaling by removing scale-forming ions such as calcium (Ca2+) and phosphate (P). Ca- and P-selective ion exchangers also enable calcium phosphate recovery via precipitation from spent regenerants enriched with both ions. However, conventional regeneration approaches require substantial chemical and energy inputs. In this study, we designed a RO pretreatment process using electro-assisted regeneration of a column train containing a hybrid anion exchanger (HAIX) and a weak acid cation exchanger (WAC) to selectively remove > 90% Ca2+ and P from synthetic secondary effluent. HAIX and WAC were regenerated using pH 11 catholyte and pH 3 anolyte produced via electrochemical water splitting. HAIX contains ferric oxide nanoparticles (FeOnp) in a parent strong base anion exchanger (SBA). By comparing P regeneration efficiency of HAIX and SBA, we identified that FeOnp dopants reduced intraparticle diffusivity by 85% from SBA to HAIX. However, HAIX exhibited faster column regeneration kinetics than SBA, potentially due to the shortened intraparticle diffusion path length caused by the surface-distributed P in saturated HAIX, which overcompensated for low intraparticle diffusivity. Regenerability enhancement caused by the reduced intraparticle diffusion path length was also confirmed by comparing WAC with shallow-shell WAC (SSWAC), which has surface-distributed carboxylate functional groups. We anticipate that this study will inform selective adsorbent design by identifying strategies to improve regenerability, facilitate process intensification by replacing chemical inputs with electricity, and enhance resource recovery from wastewater.