共查询到19条相似文献,搜索用时 46 毫秒
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张春华 《水科学与工程技术》2015,(1):52-56
为提高含酚废水的处理技术,改善水生态平衡,分别采用臭氧氧化、活性炭吸附─臭氧氧化和臭氧氧化─活性炭吸附联用等方法处理含酚废水。试验结果表明:臭氧氧化─活性炭吸附联用技术处理含酚废水效果最好;得出的最佳试验条件为:活性炭加入量为30g/L、吸附时间为20min、臭氧流量为8mg/min、反应时间为20min及溶液初始p H值为8.5。在最佳试验条件下,臭氧氧化─活性炭吸附联用工艺对CODCr的去除率为74.60%。 相似文献
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以天津市某废水处理厂提标改造为基础,建立了1套活性炭回流旋流分离的活性炭吸附-混凝深度处理技术,探究污染物去除机理,系统开展中试研究了药剂投加量、回流量、反洗周期等对污染物的去除效果,中试运行结果表明在PAC 34mg/L,活性炭40mg/L,PAM 3~4mg/L,药剂成本0.3元/t的情况下,能达到《城镇污水处理厂污染物排放标准》(DB 12/599—2015)一级A排放标准,在活性炭回流比超过50%的情况下能一定程度改善处理效果,强化了对亲水性小分子污染物去除,提高处理效率。 相似文献
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含锌重金属废水藻类吸附处理技术 总被引:4,自引:1,他引:4
以小球藻为吸附剂,研究藻类吸附剂对重金属废水中Zn2+的吸附过程,分析吸附时间、温度、pH值、Zn2+起始浓度以及预处理过程等因素对小球藻吸附Zn2+性能的影响。结果表明:预处理能提高小球藻的吸附性能,其吸附过程符合Langmuir吸附特征,对废水的pH值适应范围广。对于ρ(Zn2+)=100 mg/L的重金属废水经小球藻一次处理,去除率达到98%。小球藻吸附处理废水中Zn2+的较佳工艺条件为pH值6.5、温度25℃、吸附时间60 min、小球藻用量2 g/L。 相似文献
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由于水源污染日趋严重,常规水处理工艺难以满足现代饮用水水质要求.本课题研究了应用粉末活性炭处理污染原水的工艺方法和关键技术.试验结果表明:(1)模拟静态吸附选炭试验是一种可靠的接近生产实际工况的试验方法.常用炭种中木屑炭的吸附效果较好.(2)粉末活性炭的最佳投加点是在絮凝中段.这样可有效避免吸附与混凝的竞争,并使粉末活性炭附着于矾花的表面而易分离.建议粉末活性炭投加量为10~15mg/L,该条件下COD_(Mn)去除率可稳定在20%左右, 相似文献
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在试验室条件下,在БИО-25(一种体积较小的改良型处理构筑物)曝气-沉淀池里,进行了废水的生物处理试验,并用КАД-ИОДНыИ粉状活性炭来作为吸附剂。将预先由试验方法确定的最佳和最小剂量(相应为400和800毫克/升)的炭加入装置进行试验。试验结果见下表,当活性炭的剂量为400毫克/升时,装置经9小时运转废水中就含有相当少量的有机生物体、细菌和病毒的杂质:化学需氧量和磷酸盐含量相应地从296.4毫克/升降到43.4毫克/升(去除率为85.4%)和从5.4毫克/升降到1.7毫克/升(去除率为68.6%),而大肠杆菌指数从4.1·10~7降到1.1·10~4。并发现了T_2。噬菌体含量的大量降低,从1.1·10~4降到8.2·10~2 相似文献
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活性炭吸附用于城市污水地下回灌深度处理技术研究 总被引:6,自引:0,他引:6
以城市污水处理厂二级生物处理出水地下回灌为回用目的,研究了活性炭吸附深度处理工艺。通过静态吸附试验选定了适于处理二级出水的粒状活性炭,并运用ADSA 软件对有机物在活性炭上的吸附行为进行了分析。将活性炭吸附同混凝砂滤相结合,研究两种不同组合工艺对有机物的去除效果,筛选出了适于城市污水处理厂二级出水地下回灌的深度处理工艺,再生水中以DOC 表征的有机物浓度可达3mg/L~45mg/L以下。 相似文献
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粉末活性炭悬浮吸附技术研究 总被引:6,自引:0,他引:6
《给水排水》1998,(11)
本文介绍了在饮用水处理中粉末活性炭应用的一种新方法——粉末活性炭悬浮吸附技术的试验结果和技术关键;重点阐述在一定条件下,悬浮床中的载炭量和絮凝作用对活性炭吸附效果的影响。 相似文献
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活性炭吸附池工艺设计的探讨 总被引:1,自引:0,他引:1
设计合理的活性炭吸附池应当具有处理效果好、运行管理简单、节能降耗、施工方便、维护量小等特点。而吸附池设计的关键是池型和滤层结构的选择以及冲洗方式、设计参数的确定,同时还要考虑其他一些相应的问题。结合深圳市笔架山水厂活性炭吸附池工艺设计的调整过程,探讨了当前活性炭吸附池工艺设计中普遍关注的问题,包括池型、滤层结构、冲洗方式及冲洗水源等,同时简要介绍了目前我国活性炭吸附池的应用情况。 相似文献
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Muibat Diekola Yahya Kehinde Shola Obayomi Mohammed Bello Abdulkadir Yahaya Ahmed Iyaka Adeola Grace Olugbenga 《水科学与水工程》2020,13(3):202-213
In this experiment, cobalt ferrite-supported activated carbon (CF-AC) was developed and characterized via the wet impregnation method for the removal of Cr and Pb(II) ions from tannery wastewater. Batch adsorption was carried out to evaluate the effect of experimental operating conditions (pH of solution, contact time, adsorbent dose, and temperature), and the removal efficiencies of Cr and Pb(II) ions by the developed adsorbents were calculated and recorded for all experimental conditions. These variables were estimated and reported as removal efficiencies of 98.2% for Cr and 96.4% for Pb(II) ions at the optimal conditions of 5, 0.8 g, 80 min, and 333 K for pH, adsorbent dose, contact time, and temperature, respectively. The equilibrium for the sorption of Cr and Pb(II) ions was studied using four widely used isotherm models (the Langmuir, Freundlich, Dubinin-Radushkevich, and Temkin isotherm models). It was found that the Freundlich isotherm model fit better with the coefficient of determination (R2) of 0.948 4 and a small sum of square error of 0.000 6. The maximum adsorption capacities (Qm) of Pb(II) and Cr adsorbed onto CF-AC were determined to be 6.27 and 23.6 mg/g, respectively. The adsorption process conformed well to pseudo-second order kinetics as revealed by the high R2 values obtained for both metals. The thermodynamic parameters showed that adsorption of Cr and Pb(II) ions onto CF-AC was spontaneous, feasible, and endothermic under the studied conditions. The mean adsorption energy (E) values revealed that the adsorption mechanism of Cr and Pb(II) by CF-AC is physical in nature. The results of the study showed that adsorbent developed from CF-AC can be efficiently used as an environmentally friendly alternative adsorbent, for removal of Cr and Pb(II) ions in tannery wastewater. 相似文献
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通过等温吸附试验,研究了超高交联树脂NDA-66对邻苯二甲酸(ο-PA)的吸附性能及吸附行为,同时优化了NDA-66处理增塑剂DBP生产废水吸附-脱附工艺参数。经过初步筛选发现,NDA-66树脂对ο-PA具有良好的吸附性能,在温度为15℃、30℃和45℃条件下分别测定了吸附平衡数据,ο-PA在NDA-66树脂上的吸附平衡符合Freundlich等温吸附方程,温度对吸附的影响较大。参数优化试验结果表明:树脂吸附最佳工艺参数是:pH 2.0~2.4,温度30℃,流速为1.5 BV/h;树脂脱附最佳工艺参数,脱附剂用量及组成为1 BV 8%NaOH+2 BV H_2O,脱附温度为55℃,脱附流速为1.5 BV/h。 相似文献
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The present work highlights the preparation of activated carbons (ACs) using spent coffee grounds, an agricultural residue, as carbon precursor and two different activating agents: water vapor (ACW) and K(2)CO(3) (ACK). These ACs presented the microporous nature and high surface area (620-950 m(2) g(-1)). The carbons, as well as a commercial activated carbon (CAC) used as reference, were evaluated as phenol adsorbent showing high adsorption capacity (≈150 mg g(-1)). The investigation of the pH solution in the phenol adsorption was also performed. The different activating agents led to AC with distinct morphological properties, surface area and chemical composition, although similar phenol adsorption capacity was verified for both prepared carbons. The production of activated carbons from spent coffee grounds resulted in promising adsorbents for phenol removal while giving a noble destination to the residue. 相似文献
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