Adsorption of organic matter in oil sands process water (OSPW) by carbon xerogel

被引:45
作者
Benally, Chelsea [1 ]
Messele, Selamawit Ashagre [1 ]
El-Din, Mohamed Gamal [1 ]
机构
[1] Univ Alberta, Dept Civil & Environm Engn, Edmonton, AB T6G 1H9, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Oil sands process water; Adsorption; Carbon xerogel; Naphthenic acids; Mesoporous carbonaceous adsorbent; NAPHTHENIC ACIDS SPECIATION; PETROLEUM-COKE ADSORPTION; ACTIVATED CARBON; AQUEOUS-SOLUTION; REMOVAL; TOXICITY; NANOFILTRATION; OZONATION; PEROXIDE; ISOTHERM;
D O I
10.1016/j.watres.2019.01.053
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study illustrated the preparation, characterization and the use of carbon xerogel materials for the adsorption of acid-extractable fractions (AEF) and naphthenic acids (NAs) from oil sands process water (OSPW). Adsorption results demonstrated that the mesoporous carbonaceous material can successfully be used to adsorb persistent and toxic organic contaminants from OSPW. Carbon xerogel (CX) made at pH 5.5 showed high surface area (573 m(2)/g) and removed a larger amount of AEF than CX made at pH 6.9 (391 m(2)/g). The adsorption equilibrium was reached by 24 h for both AEF and classical NAs. 74.6% of AEF and 88.8% of classical NAs were removed by CX5.5 during 24-h adsorption. With respect to classical NAs, a larger the carbon number resulted in higher NA removal. Carbon number had more influence on NA removal when compared with hydrogen deficiency resulting from rings or unsaturated bonding formation (-Z number). The equilibrium adsorption capacity was found to be 15 mg AEF/g and 7.8 mg NAsig for CX5.5. Adsorption of AEF and classical NAs onto CX5.5 followed pseudo-second order kinetics. With respect to diffusion of AEF and NAs, there were three distinct diffusion regions: bulk, film and pore. Pore diffusion had the lowest rate constant in all cases analyzed and was thus the rate limiting step. The results of this study showed that a mesoporous carbonaceous material such as CX may have the potential to be utilized in a fixed bed adsorption/filtration systems for continuous treatment of OSPW or as a semipassive treatment method in pit lakes for the removal of organic constituents from OSPW. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:402 / 411
页数:10
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