水力停留时间对热液喷口沉积物污泥产生硫化物的影响及其对去除铜、锌和铝的作用

Emir Martínez-Gutiérrez, Claudia Guerrero Barajas
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引用次数: 0

摘要

本研究旨在评估在上流式厌氧污泥毯(UASB)反应器中采用不同的水力停留时间(HRT)和不同的硫酸盐负荷率产生硫化物的情况,该反应器利用醋酸盐-丁酸盐作为电子供体,并将反应器与结晶器相连以去除金属。用于 UASB 的硫化污泥来自热液喷口沉积物,在室温(18-22 ºC)下运行。硫酸盐还原过程与 Cu2+、Zn2+ 和 Al3+ 在与 UASB 反应器(两级系统)耦合的结晶器中沉淀有关,以避免金属对污泥的毒性。溶解硫化物的浓度随着 HRT 的延长而增加,在 HRT 3 d 时达到 312.9 mg HS-/L。随着硫酸盐负荷率的增加,在 500 mg SO4-2/L/d(1500 mg/L)时,硫化物的最大浓度为 376.8 mg HS-L,而 Cu2+、Zn2+ 和 Al3+ 的浓度分别为 150、100 和 100 mg/L。分别投加 Cu2+、Zn2+ 和 Al3+ 时,去除率高于 98%。当加入金属混合物时,去除率接近 80%。在所有情况下,金属的回收率均低于 57%。硫化物的产生得到了醋酸-丁酸盐的支持,前者通常是由于高级有机化合物的氧化而积累起来的;在这种情况下,醋酸-丁酸盐的利用维持了硫酸盐的还原。这一过程可由 HRT 和硫酸盐加载率等参数控制,以提高生物反应器在两级系统中处理受金属污染的污水的性能。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effect of hydraulic retention time on sulfide production with sludge from hydrothermal vent sediments and its utilization on the removal of Cu, Zn, and Al
The present work aimed to evaluate the production of sulfide through the application of different hydraulic retention times (HRT) and different sulfate loading rates in an up-flow anaerobic sludge blanket (UASB) reactor utilizing acetate-butyrate as electron donors and the coupling of the reactor to a crystallizer to remove metals. The sulfidogenic sludge for the UASB was generated from hydrothermal vent sediments and this was operated at room temperature (18-22 ºC). The sulfate reduction process was linked to the precipitation of Cu2+, Zn2+ and Al3+ in a crystallizer coupled to the UASB reactor (two-stage system) to avoid the toxicity of the metals to the sludge. The concentration of dissolved sulfide increased with the HRT up to 312.9 mg HS–/L at 3 d of HRT. As the sulfate loading rate was increasing, the maximum sulfide concentration obtained was of 376.8 mg HS–/L at 500 mg SO4–2/L/d (1500 mg/L), whereas the concentration of Cu2+, Zn2+ and Al3+ was up to 150, 100, and 100 mg/L, respectively. The removal efficiencies of Cu2+, Zn2+, and Al3+ were higher than 98% when they were fed separately. When a mixture of metals was added, the removal efficiency was close to 80%. Recovery of metals was lower than 57% in all cases. The sulfide production was supported with acetate-butyrate, being the former commonly accumulated because of the oxidation of higher organic compounds; in this case, its utilization sustained sulfate reduction. This process could be controlled by parameters such as HRT and sulfate loading rate to improve the performance of the bioreactor in the treatment of the effluents contaminated with metals in a two-stage system.
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