Effects of dissolved organic matter on the desorption of Cd in freeze–thaw treated Cd-contaminated soils

Lab-scale experiments were conducted to investigate the effects of dissolved organic matter (DOM) on the desorption of Cd in freeze–thaw treated Cd-contaminated soils. The results indicated that DOM significantly facilitated the desorption of Cd from freeze–thaw treated soils when comparing with that of non-frozen soils. Effects of DOM on the Cd desorption were highly dependent on the soil type and contamination concentration. The maximum desorption ratios of Cd by DOM generated from straw and sludge were 15.6% and 13.65%, respectively, in brown soils, and the maximum desorption ratios reached 14.7% and 9.3%, respectively, when using black soils through the same treatment. The higher the Cd contamination concentration in soils, the higher the ratio of Cd desorption by DOM. This was because of the integrated effects of the soil properties changed by the freeze–thaw treatment and the species transformation of Cd. The characteristics of DOM, such as its concentration and properties, had shown obvious impacts on the Cd desorption by DOM. The desorption was promoted with the increased DOM concentration and the hydrophilic fraction, and lowered pH and the low-molecular-weight of DOM.     

沸石滤池深度处理石化废水二级出水研究

采用小试规模沸石滤池,深度处理石化废水二级出水,通过考察滤池对CODCrNH4^-N和挥发酚的去除情况,分析了沸石去除污染物的规律和机理。结果表明：沸石滤池对CODCr,NH4^＋-N和挥发酚的平均去除率分别达到27．32％、94．67％和34．47％。在滤池运行初期,离子交换起主要作用。随着反应器的运行,离子交换因沸石饱和而减弱,而生物氧化逐渐起作用。由于沸石资源丰富、价格低廉和性能优越,所以沸石滤池作为三级深度处理技术具有广阔应用前景。     

硫酸铝渣和硫铁矿烧渣制聚硅酸硫酸铁的研究

研究硫酸铝渣和硫铁矿烧渣制聚硅酸硫酸铁的工艺流程及其主要参数.提取硫酸铝渣中的SiO2得到Na2SiO3溶液,提取硫铁矿烧渣中铁得到FeSO4结晶.用FeSO4结晶制备聚合硫酸铁.用含3.5% SiO2的Na2SiO3溶液,控制pH=4.0,制得聚硅酸,将聚合硫酸铁加入聚硅酸制得聚硅酸硫酸铁絮凝剂.红外光谱分析表明,聚硅酸硫酸铁结合了SO2-4.检测了聚硅酸硫酸铁对模拟浊水和垃圾填埋场渗滤液的絮凝效果,用铁和硅物质的量比为0.5、用量0.5 mL/L的聚硅酸硫酸铁,处理模拟浊水,除浊率可达90%以上.用铁和硅物质的量比为1.5、用量4.0 mL/L的聚硅酸硫酸铁处理垃圾填埋场渗滤液生化处理尾水,CODCr去除率可达60%.     

轧钢污泥综合利用的技术研究

阐述了一种轧钢污泥的回收处理技术,该技术可把轧钢污泥有效地分离成氧化铁粉和混合油,实现综合利用,减少铁素资源浪费,有良好的经济效益和环境效益.     

内循环流化床烟气脱硫装置结构及流化性能

提出了开发一种新型内循环流化床烟气脱硫装置的设想,通过不同型式床顶、床底结构的试验,确定了实现这一构想的最佳流化床结构型式;研究了冷态条件下该装置内床料流化的状态及固含率轴向分布情况,初步考察了其流体力学性质.实验结果表明,气速在2.5～5m/s时,装置能实现大量固体颗粒的内循环,床料在床内的运动呈"环-核"结构,床内固体颗粒物浓度高于传统等径流化床,可将其用于烟气脱硫工艺.     

磁性载体生物膜反应器处理生活污水的试验研究

选取天然多孔矿物-浮石、网络状塑料外壳、磁铁为材料,开发出一种新型磁性载体,并将该载体应用于生物膜反应器中进行废水处理试验,结果表明:该磁性载体生物膜反应器在载体的挂膜性能及主要污染物去除功能上均优于非磁性载体生物膜反应器.磁性载体可在5d内完成挂膜,而非磁性载体则需8d,磁性载体生物膜反应器对COD、NH+ 4-N的去除率比非载体生物膜反应器分别高出5%和20%左右.在载体中心磁场强度为200Gs,水中溶解氧DO为2.0~3.5mg/L,水力停留时间HRT为5h的条件下,校园生活污水经磁性载体生物膜反应器处理后,出水中COD稳定在20mg/L左右, NH4+-N在5mg/L以下,两者的去除率均在90%左右,出水总氮为15mg/L,去除率在50%以上.实验结果还表明:连续运行60d后,磁性载体反应器内的生物膜量和悬浮污泥量仅为非磁性载体反应器的70%,说明磁场的存在有利于污泥减量化.磁载体生物膜反应器中载体外表面附着污泥及生物膜的SOUR值均大于非磁载体生物膜反应器,表明一定的磁场强度可以提高微生物活性.     

高温碱间歇式处理对互花米草厌氧发酵特性的影响

以互花米草为原料,采用中温(35±1)℃批式发酵的方式,考察了NaOH高温碱间歇式处理对互花米草厌氧消化过程的影响.结果表明,互花米草一次发酵至产气停止,单位TS产气量为263mL/g,发酵过程中出现酸化现象, pH值最低为5.17.二次发酵原料为一次发酵后的固体残余物,主要组分为可分解有机物以及一些难分解有机物,过程中未出现酸化现象, pH值经短暂下降后很快稳定在7.5左右,累积产气量在一次发酵的基础上提高了46%.互花米草单位TS产气量为383mL/g.消化液中有机酸乙酸含量最大,丙酸和丁酸含量相当.     

不同水域凤眼莲厌氧发酵产甲烷研究

采集滇池白山湾、滇池草海、太湖(武进段水域)以及江苏省农科院2号塘生长的凤眼莲,进行了批式厌氧发酵对比试验研究.结果发现,凤眼莲的产气潜力和水体氮磷水平有关系.水体氮磷浓度最高的滇池草海凤眼莲产气量最高,为390mL/gTS(498mL/gVS);水质最好的滇池白山湾的凤眼莲产气量最低,为289mL/gTS(334mL/gVS).白山湾凤眼莲的纤维素、半纤维素和粗蛋白等组分的降解率均最低.4个水体凤眼莲产生的有机酸均以乙酸和丙酸为主,草海凤眼莲发酵产生的有机酸浓度最高,可达2466mg/L,白山湾凤眼莲最低,仅为915mg/L.研究发现水体氮、磷浓度影响凤眼莲化学组分含量的差异及结构组成(根冠比),可能是影响凤眼莲厌氧生物降解性能及产气量差异的主要因素.     

气体分离循环对高温厌氧消化过程的影响

采用厌氧序批式反应器,研究了气体循环(包括气体直接循环和脱除气体中的氢气后循环)对以葡萄糖和乙酸钠配制的模拟废水在高温厌氧消化过程中乙酸代谢速率、出水性质及微生物相的影响,并采用尺寸排除色谱和三维荧光光谱技术,对溶解性微生物产物(SMP)的分子量分布和荧光物质组成进行了分析.结果显示,气体循环使得出水中残余挥发性脂肪酸的浓度由238.2mg/L(未脱氢)和129.6mg/L(脱氢)分别减少至8.5mg/L和8.2mg/L,并最终降低了SMP产量,45d时分别降至气体循环前的36.8%和59.2%.脱氢气体循环促进了乙酸化和乙酸氧化,导致了微生态环境和甲烷化基质浓度的差异,促进了高分子量SMP向低分子量SMP的转化,污泥中的微生物形态亦发生了较大变化.可见气体循环改善了基质与微生物的混合状况,改善了出水水质,而脱氢气体循环加速了乙酸的代谢,有望更快速地解除易降解有机物高温厌氧消化过程中的酸抑制,提高厌氧消化效率.     

Continuous biohydrogen production from diluted molasses in an anaerobic contact reactor

An anaerobic contact reactor (ACR) system comprising a continuous flow stirred tank reactor (CSTR) with settler to decouple the hydraulic retention time (HRT) from solids retention time (SRT) was developed for fermentative hydrogen production from diluted molasses by mixed microbial cultures. The ACR was operated at various volumetric loading rates (VLRs) of 20–44 kgCOD·m^-3·d^-1 with constant HRT of 6 h under mesophilic conditions of 35°C. The SRT was maintained at about 46–50 h in the system. At the initial VLR of 20 kgCOD·m^-3·d^-1, the hydrogen production rate dropped from 22.6 to 1.58 L·d^-1 as the hydrogen was consumed by the hydrogentrophic methanogen. After increasing the VLR to 28 kgCOD·m^-3·d^-1 and discharging the sludge for 6 consecutive times, the hydrogentrophic methanogens were eliminated, and the hydrogen content reached 36.4%. As the VLR was increased to 44 kgCOD·m^-3·d^-1, the hydrogen production rate and hydrogen yield increased to 42.1 L·d^-1 and 1.40 mol H₂·molglucose-consumed^-1, respectively. The results showed that a stable ethanol-type fermentation that favored hydrogen production in the reactor was thus established with the sludge loading rate (SLR) of 2.0–2.5 kgCOD·kgMLVSS^-1·d^-1. It was found that the ethanol increased more than other liquid fermentation products, and the ethanol/acetic acid (mol/mol) ratio increased from 1.27 to 2.45 when the VLR increased from 28 to 44 kgCOD·m^-3·d^-1, whereas the hydrogen composition decreased from 40.4% to 36.4%. The results suggested that the anaerobic contact reactor was a promising bioprocess for fermentative hydrogen production.