Scalability of advanced oxidation processes (AOPs) in industrial applications: A review

被引:39
作者
Mahbub, Parvez [1 ,2 ,3 ,4 ,5 ]
Duke, Mikel [1 ]
机构
[1] Victoria Univ, Inst Sustainable Ind & Liveable Cities, Footscray Pk Campus,70-104 Ballarat Rd, Footscray 3011, Australia
[2] Victoria Univ, First Year Coll, Footscray Pk Campus,70-104 Ballarat Rd, Footscray 3011, Australia
[3] Dr Parvez Mahbub Bldg 2,235 Hoppers Lane, Werribee, Vic 2029, Australia
[4] Victoria Univ, Inst Sustainable Ind & Liveable Cities ISILC, Werribee Campus, Melbourne 2207, Australia
[5] Victoria Univ, Footscray Pk,Campus D416B, Melbourne, Australia
关键词
Scalable advanced oxidation processes; Continuous-flow and batch reactors; Hydroxyl and sulfate radicals; Ozone; Hydrogen peroxide; Hypochlorous acid; HYDROGEN-PEROXIDE; WATER-TREATMENT; ELECTROCHEMICAL DETECTION; HYPOCHLOROUS ACID; SINGLET OXYGEN; FLUORESCENCE PROBES; ORGANIC-COMPOUNDS; FLOW-INJECTION; FREE-RADICALS; OZONE;
D O I
10.1016/j.jenvman.2023.118861
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Disinfection and decontamination of water by application of oxidisers is an essential treatment step across numerous industrial sectors including potable supply and industry waste management, however, could be greatly enhanced if operated as advanced oxidation processes (AOPs). AOPs destroy contaminants including pathogens by uniquely harnessing radical chemistry. Despite AOPs offer great practical opportunities, no reviews to date have highlighted the critical AOP virtues that facilitate AOPs' scale up under growing industrial demand. Hence, this review analyses the critical AOP parameters such as oxidant conversion efficiency, batch mode vs continuous-flow systems, location of radical production, radical delivery by advanced micro-/mesoporous structures and AOP process costs to assist the translation of progressing developments of AOPs into their largescale applications. Additionally, the state of the art is analysed for various AOP inducing radical/oxidiser measurement techniques and their half-lives with a view to identify radicals/oxidisers that are suitable for in-situ production. It is concluded that radicals with short half-lives such as hydroxyl (10-4 & mu;sec) and sulfate (30-40 & mu;sec) need to be produced in-situ via continuous-flow reactors for their effective transport and dosing. Meanwhile, radicals/oxidisers with longer half-lives such as ozone (7-10 min), hydrogen peroxide (stable for several hours), and hypochlorous acid (10 min-17 h) need to be applied through batch reactor systems due to their relatively longer stability during transportation and dosing. Complex and costly synthesis as well as cytotoxicity of many micro-/mesoporous structures limit their use in scaling up AOPs, particularly to immobilising and delivering the short-lived hydroxyl and sulfate radicals to their point of applications. Overall, radical delivery using safe and advanced biocompatible micro-/mesoporous structures, radical conversion efficiency using advanced reactor design and portability of AOPs are priority areas of development for scaling up to industry.
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页数:12
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