单级与二级BAF工艺除碳硝化效能的对比研究

在总曝气量、HRT、水温、进水水质相同的条件下,对比研究了单级(BAF C/N)和二级曝气生物液池(BAF C+N)处理生活污水的除碳硝化效能。结果表明,将除碳和硝化分级有利于提高BAF工艺的处理效能。分级后,C柱较C/N柱具有更高的COD去除容积负荷,且出水COD浓度稳定低于50 mg/L;二级BAF工艺出水NH4+-N浓度由单级BAF的5～12 mg/L降至5 mg/L以下,且N柱在pH<6.3时依然能够进行硝化;N柱中下部具有较高的微生物活性,平均比耗氧速率为32 mg O2/(g VAS·h)。二级BAF中C柱的反冲洗周期和强度与单级BAF相同,而N柱的反冲洗周期则延长至5～7 d,能够降低反冲洗能耗和用水量。     

Characterization of residue from leached cathode ray tube funnel glass: reutilization as white carbon black

Cathode ray tube (CRT) funnel glass remains an urgent environmental problem and is composed mainly of lead oxide and silicon oxide. In this research, the residue could be obtained from 2 h to 500 rpm activated CRT funnel glass after extracting lead via acid leaching under the conditions of HNO₃ concentration 1.0 mol/L, leaching temperature 95 °C and leaching time 1 h. In order to reutilize the residue, its physico-chemical properties were characterized by scanning electron microscopy, Brunauer–Emmett–Teller, thermogravimetric analysis, X-ray diffraction and Fourier transform infrared spectroscopy. The results indicated that the residue was an amorphous superfine powder with approximately 93 wt% silica oxide and specific surface area of more than 170 m²/g. It can be reutilized as white carbon black.     

含氯有机物机械化学法脱氯试验研究

难降解含氯有机物的处理一直是环境治理中的难点,研究开发高效、安全的新型降解技术是目前研究工作的当务之急.以含氯有机物四氯苯醌为研究对象,采用新型的机械化学法(球磨)对其进行脱氯降解试验,研究了四氯苯醌的脱氯速率与还原剂种类(铁酸锌、烟尘、锌粉、石灰)及添加比例、球磨时间等参数之间的关系.试验结果表明:石灰作为还原剂脱氯效果最好,当四氯苯醌与石灰质量比为1∶11、球磨时间为4h时,其脱氯率接近100％.通过对球磨产物进行XRD、IR、GC-MS分析,结果发现球磨后产物大部分是CaO和Ca(OH)2,氯从四氯苯醌上脱除并形成了碳氢键,氯离子可能以无定形形态存在.     

北京秋冬季一次重污染过程PM2.5来源数值模拟研究

利用WRF模式(The Weather Research and Forecasting Model)和嵌套网格空气质量模式(NAQPMS)对2016年11月发生在京津冀地区一次PM_(2.5)污染事件进行模拟研究并分析污染过程中的天气形势变化.结果表明,均压场、低空逆温层和偏南暖湿气流输送的存在为北京地区PM_(2.5)形成提供了有利条件,NAQPMS模式能够合理的再现北京大气污染物时空变化,细颗粒物PM_(2.5)和可吸入颗粒物PM_(10)模拟与观测数据相关系数达0.71,模拟数据在观测数据两倍范围内占比(FAC2)达65%.源解析结果表明,在不考虑临时实施减控措施下,11月18日区域外输送对北京PM_(2.5)浓度贡献为55.25%,区域内输送贡献为44.75%,北京东北区域PM_(2.5)外地源主要为河北中部、河北南部、天津和山东,所占贡献为9.67%、9.01%、7.90%和7.99%.污染物主要来源为生活源、交通源和工业源,分别占比39.6%、34.6%和20.0%.而实际上北京在唐山、保定采取一系列控制措施后仍在研究时段内出现高PM_(2.5)浓度,意味着在同样天气形势下需要对河北中部、河北南部、天津和山东等浓度贡献占比大的城市加强减排管控才能有效减缓高PM_(2.5)浓度的出现.     

Triclosan in waste and surface waters from the upper Detroit River by liquid chromatography-electrospray-tandem quadrupole mass spectrometry

Triclosan (5-chloro-2-(2,4-dichlorophenoxy)phenol) is an antimicroibial disinfectant agent used in a wide array of consumer products. An analytical method based on solid-phase extraction (SPE) followed by reverse phase, liquid chromatography coupled with electrospray ionization (negative)-tandem quadrupole mass spectrometry (LC-ESI(-)-MS/MS; in the multiple reaction monitoring (MRM) mode) was developed, optimized and validated for the determination of triclosan in wastewater/sewage treatment plant (WSTP) effluent and surface waters from the upper Detroit River (Canada). The mean recoveries (+/-%RSD) of triclosan and the internal standard 2'-HO-tribromodiphenyl ether (2'-HO-BDE-28) spiked to surface water and WSTP effluent samples ranged similarly from 104+/-8% and 91+/-10%, respectively, and method limits of quantification were in the low ppb/high ppt range. However, ESI(-) enhancement was found for both analytes due to sample matrix effects, as indicated by % process efficiencies (a measure of ESI(-) enhancement/suppression), which were in the 111-128% range. We report the first known assessment of triclosan in the Detroit River watershed of the Great Lakes, which preliminarily examined the presence and UV-treatment effects on triclosan in effluent from the major WSTP serving the City of Windsor, Ontario, Canada, and fate in surface waters of the upper Detroit River. Triclosan in WSTP effluent decreased 22% after final UV treatment to a mean concentration of 63 ng/L. Concentrations were further reduced to 4 and 8 ng/L (a >90% reduction) in surface water samples from sites downstream on the Canadian shoreline of the Detroit River, which was due to dilution. Two hydroxylated tribrominated diphenyl ethers, which are structurally similar to triclosan, were also detected in WSTP effluent and surface water samples.     

膨润土对Pb2+、Cu2+、Cr3+的吸附动力学及等温线研究

研究所用膨润土的主要成分为SiO2和Al2O3,属于Ca基膨润土,BET表面积为50.83 m2/g.在恒温及恒定pH条件下,用静态吸附法研究了膨润土对Pb2 、Cu2 、Cr3 的吸附特性,结果表明其较好地符合Lagergten二级吸附速率方程,对这3种离子的吸附速率为Pb2 ＞Cu2 ＞Cr3 .利用3种等温线方程对吸附过程进行拟合,发现利用Langmuir吸附等温方程计算的值与膨润土吸附Pb2 、Cu2 、Cr3 试验数据最为吻合.膨润土对3种金属离子的平衡吸附量为Cr3 ＞Cu2 ＞Pb2 .     

工艺安全管理系统的适用范围——危险化学品目录及临界量的确定

从工艺安全管理（PSM）的角度,对美国、欧盟等的工艺安全管理系统适用范围的定义进行分析,结合目前国内《重大危险源辨识》中给出的部分危险化学品的临界量,以此为基础制定适合我国国情的危险化学品目录并确定各物质的临界量,提出在我国推行工艺安全管理系统的建议。     

我国部分河流重金属水-固分配系数及在河流质量基准研究中的应用

计算了我国部分河流天然物理化学条件下重金属在水相－颗粒物相间的分配系数,长江水系重金属水－固分配系数大于黄河反映了颗粒物度组成的差异,而长江口重金属－固分配系数大于长江武汉段则反映了离子强度的影响,在此基础上,运用平衡分配法根据实测天然分配系数尝试了长江,黄河沉积物某重金属的质量基准。     

粘胶化纤厂废气治理试验

采用ＴＦ－ＴＡ工艺治理粘胶化纤厂废气。先以ＴＦ脱硫液选择脱除ＨＺＳ,再以ＴＡ液体脱除ＣＳ２。Ｈ２Ｓ脱除和再生能一步完成,脱除率９８％以上,其表达ηＨ２ｓ＝９９．５＋４．７１×１０－４ｘ－３．６８×１０－７ｘ２。ＣＳ２脱除率在气液比２００—３００时达８０％─９０％,其表达式：ηＣＳ２＝９８．９－１．３２×１０－３ｘ—２．００×１０－４ｘ２。文中还讨论了粘胶化纤厂废气总体治理意见。     

Experimental study on agitated drying characteristics of sewage sludge under the effects of different additive age

Drying experiments of dewatered sewage sludge (DSS) were conducted on a agitated paddle dryer, and the effects of additive agents, i.e., CaO, pulverized coal (PC), heavy oil (HO), and dried sludge ("DS" through back mixing) on the agitated drying characteristics of DSS were investigated. The results indicated that CaO can significantly increase the drying rate of DSS. The drying rate at CaO/DSS (mass ratio) = 1/100 was 135% higher than that of CaO/DSS = 0. Pulverized coal has no obvious effect on drying rate, but the increase of PC/DSS can promote breaking up of sludge lump. Heavy oil was found to be slightly effective in improving the drying rate of DSS in the examined experimental range of HO/DSS = 0-1/20. It is also found thatHOcan reduce the torque of the dryer shaft, due to its lubrication effect. Back mixing of DS was found to be effective in alleviating the unfavorable effect of the lumpy phase by improving the mixing effect of the paddle dryer. There was a marked increase of drying rate with an increase of the DS/DSS in the experimental range of DS/DSS = 0-1/3.