低曝气下PAC强化SBR工艺同步脱氮除磷

采用序批式反应器(SBR)处理模拟生活污水,研究不同曝气量(30、24、18和12 L/h)下活性污泥同步脱氮除磷规律,并在最佳曝气量下,比较了粉末活性炭-序批式反应器(PAC-SBR)和SBR的脱氮除磷效率,分析了低曝气下PAC-SBR的运行特性和优越性。实验结果表明,当曝气量为24 L/h时,SBR内出水效果较好,其COD、TN和TP的平均去除率分别可以达到90.02%、81.13%和88.12%。在这个最佳曝气量下,PAC-SBR具有明显的优势,其COD、TN和TP的平均去除率均高于SBR,并且PAC-SBR具有较好的污泥沉降性能和较高的活性污泥浓度。在PAC-SBR中,活性污泥以PAC作为微生物载体强化了生物降解效果,并改善了低曝气下污泥絮体的结构,促使反应器内先后形成缺氧-厌氧-微氧/缺氧-缺氧的环境,利于同步硝化反硝化和反硝化聚磷,提高了PAC-SBR的同步脱氮除磷效率。     

鸟粪石循环利用处理高氨氮废水的热解行为

为了循环利用鸟粪石处理高氨氮废水,探讨了鸟粪石煅烧与加碱热解的脱氮率,利用电镜扫描(SEM)和X射线衍射(XRD)对2种热解产物进行了分析。鸟粪石煅烧条件为:温度100～225℃,时间1～5 h;加碱热解条件为:温度60～95℃,时间0.5～4 h,加碱量OH-∶NH4+摩尔比值0.4～1.5。结果表明,虽然XRD分析显示2种热解产物都已失去鸟粪石的特征峰,但是鸟粪石加碱热解效果更好,最佳热解条件为:加碱量OH-∶NH4+摩尔比值1,温度90℃,时间2 h,鸟粪石脱氮率95%以上;加碱热解产物表面为多孔状,完全失去了晶体结构;煅烧热解鸟粪石脱氮率仅为80%左右,热解产物晶体结构破坏不完全。鸟粪石在最佳条件下热解循环处理高氨氮废水,可循环使用6次,氨氮去除率80%以上,出水磷浓度小于8 mg/L。     

管道沉砂用作雨水花园土壤改良材料的可行性

以建筑黄砂为对照,采用排水管道清通作业产生的管道沉砂作为提高土壤渗透性能的改良材料,通过模拟土柱实验考察了雨水花园对路面径流污染的控制效果.实验结果表明,在装置初始运行阶段,模拟柱中污染物的淋出浓度迅速降低,污染地下水的风险很低;当污染物淋失达到稳定时,掺加同比例管道沉砂与建筑黄砂的模拟柱在提高土壤渗透速率方面效果相近,而对COD、TP、TSS、NH4+-N、NO3--N、重金属等污染物的去除两者效果则相差不大.结果表明,以管道沉砂作为土壤改良材料,在降低南方粘性土壤地区雨水花园的建造成本、实现废弃物的再利用方面具有良好前景.     

CS-Fe和CS-Fe/Ni的制备及其用于去除钴离子

以氯化铁为铁源,硼氢化钠为还原剂,壳聚糖为稳定剂,采用液相还原法制备壳聚糖稳定纳米铁（CS-Fe）;并以氯化铁为铁源,硫酸镍为镍源,硼氢化钠为还原剂,壳聚糖为稳定剂,采用液相还原共沉淀法制备壳聚糖稳定纳米铁镍（CS-Fe/Ni）。通过SEM、EDS、XRD、FT-IR等表征手段,对所制备的CS-Fe和CS-Fe/Ni的形貌及微观结构进行表征,并以Co²⁺为目标去除物评价CS-Fe和CS-Fe/Ni的反应活性。初步研究表明,制成的CS-Fe含有单质纳米铁,颗粒多数以30~90 nm球形颗粒为主;而CS-Fe/Ni材料中含有纳米铁镍,颗粒多数以30~60 nm球形颗粒为主;在相同的实验条件下,反应60 min,CS-Fe/Ni对Co²⁺的去除率高达100%,但是CS-Fe仅为88%,即CS-Fe/Ni对Co²⁺的去除率比CS-Fe高。     

四环素高效降解酵母菌Trichosporon mycotoxinivoransXPY-10降解特性

Trichosporon mycotoxinivorans XPY-10是一株分离自抗生素制药厂的高效四环素降解酵母菌。为了建立该菌株降解四环素的适宜条件,分别研究了碳源、有机氮源、金属离子等营养物质及初始底物浓度、接种量、pH、温度、装液量、摇床转速等理化因素对菌体生长及四环素降解效率的影响。结果表明,菌株XPY-10生长的最适碳源和氮源分别为蔗糖和蛋白胨。在含有0.05% FeSO₄的培养基中,菌株XPY-10降解四环素的适宜条件为：接种量2%,pH 8,温度34℃,装液量100 mL（250 mL 三角瓶）,摇床转速180 r/min。在此条件下,菌株XPY-10在7 d内对初始浓度为600 mg/L的四环素降解率为83.63%。本菌株对养殖废水及制药废水中四环素的污染治理有一定的应用前景。     

CaCl2高温热处理垃圾焚烧飞灰中重金属的挥发特性

以深圳市某垃圾焚烧厂飞灰为原料,采用高温管式电阻炉,研究了在0.6 L/min N₂气氛下,CaCl₂在不同添加量、处理温度及处理时间下对飞灰中重金属Pb、Cd、Zn和Cu挥发特性的影响,并对收集到的二次飞灰进行成分及物相分析。结果显示,X射线衍射仪和EDS分析表明,二次飞灰主要是由NaCl、KCl和部分SiCl₄组成,Zn主要以K₂ZnCl₄形式挥发,而Pb则主要以氧化物PbO和Pb₃SiO₅的形式挥发。最终得到CaCl₂热处理飞灰的最佳二次气化条件:以0.6 L/min N₂为载气,添加14 wt%的CaCl₂,在1 100℃高温下处理2.5 h。经CaCl₂热处理后的剩余飞灰,其浸出毒性达到了《生活垃圾填埋场污染控制标准》要求。     

Effects of a gradually increased load of fish waste silage in co-digestion with cow manure on methane production

This study examined the effects of an increased load of nitrogen-rich organic material on anaerobic digestion and methane production. Co-digestion of fish waste silage (FWS) and cow manure (CM) was studied in two parallel laboratory-scale (8 L effective volume) semi-continuous stirred tank reactors (designated R1 and R2). A reactor fed with CM only (R0) was used as control. The reactors were operated in the mesophilic range (37 °C) with a hydraulic retention time of 30 days, and the entire experiment lasted for 450 days. The rate of organic loading was raised by increasing the content of FWS in the feed stock. During the experiment, the amount (volume%) of FWS was increased stepwise in the following order: 3% – 6% – 13% – 16%, and 19%. Measurements of methane production, and analysis of volatile fatty acids, ammonium and pH in the effluents were carried out. The highest methane production from co-digestion of FWS and CM was 0.400 L CH4 gVS^?1, obtained during the period with loading of 16% FWS in R2. Compared to anaerobic digestion of CM only, the methane production was increased by 100% at most, when FWS was added to the feed stock. The biogas processes failed in R1 and R2 during the periods, with loadings of 16% and 19% FWS, respectively. In both reactors, the biogas processes failed due to overloading and accumulation of ammonia and volatile fatty acids.     

曝气量和曝气时长对好氧颗粒污泥活性恢复的影响

采用啤酒废水,在SBR中对在4℃的冰箱中储存8周的好氧颗粒污泥进行活性恢复。设置曝气时长分别为150 min和270 min,曝气量分别为0.1 m3/h和0.2 m3/h,考察了曝气时长和曝气量对好氧颗粒污泥活性恢复的影响。实验结果表明,好氧颗粒污泥在4℃冰箱中储存8周后,其颜色、粒径无明显变化;设置较长曝气时间(270 min)、较大曝气量(0.2 m3/h)时,颗粒污泥平均沉降速率、MLSS和SVI恢复最快,且对COD处理效果也恢复较快。而短曝气时间(150 min)、小曝气量(0.1 m3/h)有利于好氧颗粒污泥对氨氮去除效果的恢复。     

PAC混凝沉降法处理陶瓷废水操作条件的优化

采用PAC混凝沉降法对陶瓷废水进行处理,考察PAC用量、搅拌强度、搅拌时间、进水pH和沉降时间对处理效果的影响,获得优化的操作条件。实验表明:水样的脱色率、浊度去除率和悬浮物去除率随着PAC用量、搅拌强度、搅拌时间和沉降时间的增大和进水pH的降低而呈现增大的趋势;最佳操作条件为:当废水量小、处理时间充足时,选用PAC用量为12 mg/L、搅拌强度为中速、搅拌时间为10 min、进水pH为6、沉降时间为2 h,此条件下水样的脱色率、浊度去除率和悬浮物去除率分别达到95.6%、95.7%和85.6%;当废水量大、处理时间不充足时,选用PAC用量为60 mg/L,沉降时间为30 min,此条件下水样的脱色率、浊度去除率和悬浮物去除率分别达到94.1%、93.4%和84.4%。证明混凝法对于去除陶瓷废水中的悬浮与胶体颗粒均是有效的。     

Measuring biomass specific ammonium, nitrite and phosphate uptake rates in aerobic granular sludge

Aerobic granular sludge (AGS) technology offers the possibility to remove organic carbon, nitrogen and phosphorus in a single reactor system. The granular structure is stratified in such a way that both aerobic and anaerobic/anoxic layers are present. Since most of the biological processes in AGS systems occur simultaneously, the measurement and estimation of the capacity of specific conversions is complicated compared to suspended biomass. The determination of the activities of different functional groups in aerobic granular sludge allows for identification of the potential metabolic capacity of the sludge and aids to analyze bioreactor performance. It allows for comparison of different sludges and enables improved understanding of the interaction and competition between different metabolic groups of microorganisms. The most appropriate experimental conditions and methods to determine specific ammonium, nitrite and phosphate uptake rates under normal operation of AGS reactors were evaluated and described in this study. Extra biomass characterization experiments determining the maximum uptake rate of these compounds on optimized conditions were performed as well to see how much spare capacity was available. The methodologies proposed may serve as an experimental frame of reference for investigating the metabolic capacities of microbial functional groups in biofilm processes.