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In-situ regeneration of granular activated carbon (GAC) using Fenton's reagents.

机译:使用Fenton试剂原位再生颗粒状活性炭(GAC)。

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摘要

Fenton-dependent recovery of carbon initially saturated with one of several chlorinated aliphatic contaminants was studied in batch and continuous-flow reactors. A specialty carbon, URV-MOD 1 (Calgon) was employed to minimize non-productive H2O2 demand---that which does not yield hydroxyl or superoxide radicals.; Enhancement of PCE degradation kinetics by ferric iron addition is limited by iron solubility, even at relatively low pH. Quinone addition increased the pseudo-first-order rate constant for PCE loss temporarily. Only copper addition sustainably enhanced the specific rate of PCE loss. For copper-to-iron molar ratios of 0.25 to 5, the pseudo-first-order rate constant for PCE transformation was increased by a factor of 3.5. It is apparent that the effect of copper addition on Fenton-dependent reaction rates is complex, and involves a shift in chemical mechanism, as indicated by the differing slopes in the Arrhenius plot (with and without copper).; A mathematical model was developed to evaluate the effect of operational parameters ([Fe(III)]T:[H2O2]o ratio and pH) on degradation kinetics and optimize the PCE degradation process in homogeneous reaction mixtures. The model simulated experimental degradation of the organic target in a homogeneous Fenton-reaction system. The model requires further refinement to simulate Fenton's systems in which ions in solution (such as sulfate and chloride) play significant roles.; In continuous-flow reactors, Fenton's reagents were cycled through spent GAC in columns to degrade one of seven chlorinated compounds tested. The contaminant with the weakest adsorption characteristics, methylene chloride, was 99% lost from the carbon surface during a 14-hour regeneration period. At the field site, the GAC was saturated with gases containing TCE and PCE from a soil vapor extraction (SVE) system. In the field, up to 95% of the sorbed TCE was removed from GAC during regeneration periods of 50-60 hours. Recovery of PCE-loaded GAC was significantly slower. Column experiments show that there is minimal loss of carbon adsorption capacity during Fenton treatment and that the rate of GAC regeneration is compound specific. Scoping-level cost estimates indicated that field use of Fenton regeneration is not cost effective without optimization and/or iron surface amendments, except in the case of the most soluble VOCs.
机译:在分批和连续流反应器中研究了芬顿依赖的最初被几种氯化脂肪族污染物之一饱和的碳的回收率。特种碳URV-MOD 1(Calgon)用于最大限度地减少非生产性H2O2的需求,即不产生羟基或超氧自由基的需求。即使在相对较低的pH下,通过铁的添加,铁的PCE降解动力学的增强也受到铁溶解度的限制。醌的添加暂时增加了PCE损失的拟一级反应速率常数。只有添加铜才能持续提高PCE损耗率。对于0.25:5的铜铁摩尔比,PCE转化的拟一级反应速率常数增加了3.5倍。显然,铜的添加对Fenton依赖性反应速率的影响是复杂的,并且涉及化学机理的改变,如Arrhenius图(含铜和不含铜)中不同的斜率所表明的。建立了数学模型,以评估操作参数([Fe(III)] T:[H2O2] o比和pH)对降解动力学的影响,并优化均相反应混合物中的PCE降解过程。该模型模拟了均质Fenton反应系统中有机目标的实验降解。该模型需要进一步完善以模拟Fenton系统,其中溶液中的离子(例如硫酸根和氯离子)起着重要作用。在连续流反应器中,将Fenton试剂循环通过塔中的废GAC,以降解所测试的七种氯化化合物之一。在14小时的再生期间,吸附特性最弱的污染物(二氯甲烷)从碳表面损失了99%。在现场,GAC充满了来自土壤蒸汽萃取(SVE)系统的含TCE和PCE的气体。在现场,在50-60小时的再生期间,高达95%的吸附三氯乙烯被从GAC中去除。装载PCE的GAC的恢复速度明显慢。柱实验表明,在Fenton处理过程中,碳吸附能力的损失最小,GAC的再生速率是特定于化合物的。范围层面的成本估算表明,除非使用最易溶解的VOC,否则在没有优化和/或铁表面改性的情况下,芬顿再生的野外使用并不具有成本效益。

著录项

  • 作者单位

    The University of Arizona.;

  • 授予单位 The University of Arizona.;
  • 学科 Engineering Environmental.
  • 学位 Ph.D.
  • 年度 2006
  • 页码 215 p.
  • 总页数 215
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 环境污染及其防治;
  • 关键词

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