{"title":"天然锰矿作为分解过氧化氢的催化剂","authors":"A. H. Knol, K. Lekkerkerker-Teunissen, J. V. Dijk","doi":"10.5194/DWES-8-3-2015","DOIUrl":null,"url":null,"abstract":"Drinking water companies (are intending to) implement advanced oxidation processes (AOP) in their treatment schemes to increase the barrier against organic micropollutants (OMPs). It is necessary to decompose the excessive hydrogen peroxide after applying AOP to avoid negative effects in the following, often biological, treatment steps. A drinking water company in the western part of the Netherlands investigated decomposition of about 5.75 mg L?1 hydrogen peroxide in pre-treated Meuse river water with different catalysts on pilot scale. In down flow operation, the necessary reactor empty bed contact time (EBCT) with the commonly used granulated activated carbon (GAC) and waste ground water filter gravel (MCFgw) were found equal with 149 s, corresponding with a conversion rate constant r of 0.021 s?1. The EBCT of the fine coating of ground water filter gravel (MC) was significantly shorter with a little more than 10 s (r = 0.30 s?1). In up flow operation, with a flow rate of 20 m h?1, the EBCT of coating MC increased till about 100 s (r = 0.031 s?1), from which can be concluded, that the performance of this waste material is better compared with GAC, in both up and down flow operation. The necessary EBCT at average filtration rate of full scale dual layer filter material (MCFsw) amounted to 209 s (r= 0.015 s?1). Regarding the average residence time in the full scale filters of 700 s, applying AOP in front of the filters could be an interesting alternative which makes a separate decomposition installation superfluous, on the condition that the primary functions of the filters are not affected.","PeriodicalId":53581,"journal":{"name":"Drinking Water Engineering and Science","volume":"8 1","pages":"3-8"},"PeriodicalIF":0.0000,"publicationDate":"2015-04-22","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"1","resultStr":"{\"title\":\"Natural manganese deposits as catalyst for decomposing hydrogen peroxide\",\"authors\":\"A. H. Knol, K. Lekkerkerker-Teunissen, J. V. Dijk\",\"doi\":\"10.5194/DWES-8-3-2015\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"Drinking water companies (are intending to) implement advanced oxidation processes (AOP) in their treatment schemes to increase the barrier against organic micropollutants (OMPs). It is necessary to decompose the excessive hydrogen peroxide after applying AOP to avoid negative effects in the following, often biological, treatment steps. A drinking water company in the western part of the Netherlands investigated decomposition of about 5.75 mg L?1 hydrogen peroxide in pre-treated Meuse river water with different catalysts on pilot scale. In down flow operation, the necessary reactor empty bed contact time (EBCT) with the commonly used granulated activated carbon (GAC) and waste ground water filter gravel (MCFgw) were found equal with 149 s, corresponding with a conversion rate constant r of 0.021 s?1. The EBCT of the fine coating of ground water filter gravel (MC) was significantly shorter with a little more than 10 s (r = 0.30 s?1). In up flow operation, with a flow rate of 20 m h?1, the EBCT of coating MC increased till about 100 s (r = 0.031 s?1), from which can be concluded, that the performance of this waste material is better compared with GAC, in both up and down flow operation. The necessary EBCT at average filtration rate of full scale dual layer filter material (MCFsw) amounted to 209 s (r= 0.015 s?1). Regarding the average residence time in the full scale filters of 700 s, applying AOP in front of the filters could be an interesting alternative which makes a separate decomposition installation superfluous, on the condition that the primary functions of the filters are not affected.\",\"PeriodicalId\":53581,\"journal\":{\"name\":\"Drinking Water Engineering and Science\",\"volume\":\"8 1\",\"pages\":\"3-8\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2015-04-22\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"1\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Drinking Water Engineering and Science\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.5194/DWES-8-3-2015\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"Engineering\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Drinking Water Engineering and Science","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.5194/DWES-8-3-2015","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"Engineering","Score":null,"Total":0}
引用次数: 1
摘要
饮用水公司(打算)在其处理方案中实施高级氧化工艺(AOP),以增加对有机微污染物(OMPs)的屏障。在应用AOP之后,有必要分解过量的过氧化氢,以避免在接下来的(通常是生物的)处理步骤中产生负面影响。荷兰西部的一家饮用水公司调查了大约5.75 mg L?用不同催化剂预处理默兹河水中的过氧化氢。下流运行时,反应器空床与常用颗粒状活性炭(GAC)和废弃地下水滤石(MCFgw)的接触时间为149 s,对应的转化率常数r为0.021 s?1。地下水过滤砾石(MC)细密包覆层的EBCT显著缩短,略大于10 s (r = 0.30 s?1)。在上流工况下,流速为20 m h?1、涂层MC的EBCT增加到100 s左右(r = 0.031 s?1),由此可以看出,无论在上下流动操作中,该废料的性能都优于GAC。全尺寸双层滤料(MCFsw)平均过滤速率下所需EBCT为209 s (r= 0.015 s?1)。考虑到全尺寸过滤器中的平均停留时间为700秒,在过滤器前面应用AOP可能是一个有趣的替代方案,在过滤器的主要功能不受影响的情况下,它使单独的分解安装变得多余。
Natural manganese deposits as catalyst for decomposing hydrogen peroxide
Drinking water companies (are intending to) implement advanced oxidation processes (AOP) in their treatment schemes to increase the barrier against organic micropollutants (OMPs). It is necessary to decompose the excessive hydrogen peroxide after applying AOP to avoid negative effects in the following, often biological, treatment steps. A drinking water company in the western part of the Netherlands investigated decomposition of about 5.75 mg L?1 hydrogen peroxide in pre-treated Meuse river water with different catalysts on pilot scale. In down flow operation, the necessary reactor empty bed contact time (EBCT) with the commonly used granulated activated carbon (GAC) and waste ground water filter gravel (MCFgw) were found equal with 149 s, corresponding with a conversion rate constant r of 0.021 s?1. The EBCT of the fine coating of ground water filter gravel (MC) was significantly shorter with a little more than 10 s (r = 0.30 s?1). In up flow operation, with a flow rate of 20 m h?1, the EBCT of coating MC increased till about 100 s (r = 0.031 s?1), from which can be concluded, that the performance of this waste material is better compared with GAC, in both up and down flow operation. The necessary EBCT at average filtration rate of full scale dual layer filter material (MCFsw) amounted to 209 s (r= 0.015 s?1). Regarding the average residence time in the full scale filters of 700 s, applying AOP in front of the filters could be an interesting alternative which makes a separate decomposition installation superfluous, on the condition that the primary functions of the filters are not affected.