PFAS Destruction in IX Still Bottoms with Plasma Vortex Technology

IF 4.8 Q1 ENVIRONMENTAL SCIENCES
Richard J. Higgins, HyoungSup Kim, Erika Houtz, Paul Newman, Daniel Casey and Young I. Cho*, 
{"title":"PFAS Destruction in IX Still Bottoms with Plasma Vortex Technology","authors":"Richard J. Higgins,&nbsp;HyoungSup Kim,&nbsp;Erika Houtz,&nbsp;Paul Newman,&nbsp;Daniel Casey and Young I. Cho*,&nbsp;","doi":"10.1021/acsestwater.4c0086310.1021/acsestwater.4c00863","DOIUrl":null,"url":null,"abstract":"<p >The present study investigated the feasibility of remediating per- and polyfluoroalkyl substances (PFAS)-contaminated groundwater using a combined regenerable ion exchange (IX) and plasma treatment approach at Joint Base Cape Cod in Massachusetts. Approximately 1,200,000 L of groundwater was treated with regenerable IX, meeting the treatment goal of 20 nanograms per liter sum of perfluorooctanesulfonate, perfluorooctanoate, perfluorohexanesulfonate, perfluorononanoate, perfluorheptanoate, and perfluorodecanoate. After IX media regeneration with a solvent brine solution, 45 L of a distilled PFAS concentrate (“still bottom”) containing approximately 640 mg per liter total PFAS was recovered, representing an overall process concentration factor of approximately 30,000. A novel plasma vortex technology was employed to destroy the PFAS in the still bottom, which destroyed 97% of the PFAS initially present in a 25% diluted still bottoms, with 99% of the destroyed PFAS recovered as inorganic fluoride. The energy consumption of the plasma vortex process treating the dilute still bottoms was 1885 kW h/m<sup>3</sup>, or 12,140 kW h/kg PFAS destroyed. The treated still bottom was further reduced to nondetectable PFAS levels using reverse osmosis (RO) treatment, with the RO retentate returned to the plasma treatment system, thus creating a completely closed loop for plasma-treated regenerant waste with no liquid discharge.</p><p >Plasma vortex treatment, followed by reverse osmosis, resulted in a 99.99% PFAS destruction with no liquid discharge. TOF-8, calculated from the measured concentrations of 8 individual PFAS compounds, and inorganic fluoride ion (F-) as a function of plasma treatment time in a plasma vortex reactor.</p>","PeriodicalId":93847,"journal":{"name":"ACS ES&T water","volume":"5 5","pages":"2110–2119 2110–2119"},"PeriodicalIF":4.8000,"publicationDate":"2025-04-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsestwater.4c00863","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"ACS ES&T water","FirstCategoryId":"1085","ListUrlMain":"https://pubs.acs.org/doi/10.1021/acsestwater.4c00863","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENVIRONMENTAL SCIENCES","Score":null,"Total":0}
引用次数: 0

Abstract

The present study investigated the feasibility of remediating per- and polyfluoroalkyl substances (PFAS)-contaminated groundwater using a combined regenerable ion exchange (IX) and plasma treatment approach at Joint Base Cape Cod in Massachusetts. Approximately 1,200,000 L of groundwater was treated with regenerable IX, meeting the treatment goal of 20 nanograms per liter sum of perfluorooctanesulfonate, perfluorooctanoate, perfluorohexanesulfonate, perfluorononanoate, perfluorheptanoate, and perfluorodecanoate. After IX media regeneration with a solvent brine solution, 45 L of a distilled PFAS concentrate (“still bottom”) containing approximately 640 mg per liter total PFAS was recovered, representing an overall process concentration factor of approximately 30,000. A novel plasma vortex technology was employed to destroy the PFAS in the still bottom, which destroyed 97% of the PFAS initially present in a 25% diluted still bottoms, with 99% of the destroyed PFAS recovered as inorganic fluoride. The energy consumption of the plasma vortex process treating the dilute still bottoms was 1885 kW h/m3, or 12,140 kW h/kg PFAS destroyed. The treated still bottom was further reduced to nondetectable PFAS levels using reverse osmosis (RO) treatment, with the RO retentate returned to the plasma treatment system, thus creating a completely closed loop for plasma-treated regenerant waste with no liquid discharge.

Plasma vortex treatment, followed by reverse osmosis, resulted in a 99.99% PFAS destruction with no liquid discharge. TOF-8, calculated from the measured concentrations of 8 individual PFAS compounds, and inorganic fluoride ion (F-) as a function of plasma treatment time in a plasma vortex reactor.

等离子体涡旋技术在IX中的PFAS破坏
本研究调查了在马萨诸塞州科德角联合基地使用可再生离子交换和等离子体联合处理方法修复全氟烷基和多氟烷基物质污染地下水的可行性。使用可再生IX处理了大约120万升地下水,达到了每升含全氟辛烷磺酸、全氟辛酸盐、全氟己磺酸盐、全氟壬酸盐、全氟庚酸盐和全氟癸酸盐20纳克的处理目标。在用溶剂盐水溶液进行IX介质再生后,回收了45 L蒸馏的PFAS浓缩液(“仍底”),每升总PFAS含量约为640 mg,总体工艺浓度系数约为30,000。采用一种新型等离子体涡旋技术对蒸馏釜底部的PFAS进行了破坏,在25%稀释的蒸馏釜底部,PFAS的破坏率为97%,被破坏的PFAS的99%被回收为无机氟化物。等离子体涡旋工艺处理稀蒸馏器底部的能耗为1885 kW h/m3,或12140 kW h/kg PFAS破坏。通过反渗透(RO)处理,处理后的蒸馏釜底部进一步降低到无法检测到的PFAS水平,RO截留物返回到等离子体处理系统,从而形成一个完全封闭的等离子体处理再生废物回路,没有液体排放。等离子体涡旋处理,然后是反渗透,导致99.99%的PFAS破坏,没有液体排放。TOF-8,由8种单独PFAS化合物的测量浓度和无机氟离子(F-)作为等离子体涡旋反应器中等离子体处理时间的函数计算得出。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 求助全文
来源期刊
CiteScore
5.40
自引率
0.00%
发文量
0
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术官方微信