Fractionation of heavy metals in shallow marine sediments from Jinzhou Bay, China

This work investigated the distribution and speciation of Cd, Cu, Pb, Fe and Mn in the shallow sediments of Jinzhou Bay, Northeast China, which has been heavily contaminated by nonferrous smelting activities. The concentrations of Cd, Cu and Pb in sediments were found to be 100, 13 and 7 times, respectively, being higher than the national guideline (GB 18668-2002). Sequential extraction test showed that 39%-61% of Cd were exchangeable fractions, indicating that Cd in the sediments posed a high risk to local...     

Iron-doped Mn-Ce/TiO2 catalyst for low temperature selective catalytic reduction of NO with NH3

The catalysts of iron-doped Mn-Ce/TiO 2(Fe-Mn-Ce/TiO 2) prepared by sol-gel method were investigated for low temperature selective catalytic reduction(SCR) of NO with NH 3.It was found that the NO conversion over Fe-Mn-Ce/TiO 2 was obviously improved after iron doping compared with that over Mn-Ce/TiO 2.Fe-Mn-Ce/TiO 2 with the molar ratio of Fe/Ti = 0.1 exhibited the highest activity.The results showed that 96.8% NO conversion was obtained over Fe(0.1)-Mn-Ce/TiO 2 at 180°C at a space velocity of 50,000 hr 1.Fe-Mn-Ce/TiO 2 exhibited much higher resistance to H 2 O and SO 2 than that of Mn-Ce/TiO 2.The properties of the catalysts were characterized using X-ray diffraction(XRD),N 2 adsorption,temperature programmed desorption(NH 3-TPD and NOx-TPD),and Xray photoelectron spectroscopy(XPS) techniques.BET,NH3-TPD and NOx-TPD results showed that the specific surface area and NH3 and NOx adsorption capacity of the catalysts increased with iron doping.It was known from XPS analysis that iron valence state on the surface of the catalysts were in Fe3+ state.The doping of iron enhanced the dispersion and oxidation state of Mn and Ce on the surface of the catalysts.The oxygen concentrations on the surface of the catalysts were found to increase after iron doping.Fe-Mn-Ce/TiO2 represented a promising catalyst for low temperature SCR of NO with NH3 in the presence of H2 O and SO2.     

Removal of humic acid from aqueous solution by cetylpyridinium bromide modified zeolite

Natural zeolite was modified by loading cetylpyridinium bromide (CPB) to create more e cient sites for humic acid (HA) adsorption. The natural and CPB modified zeolites were characterized with X-ray di raction, field emission scanning electron microscopy, Fourier transform infrared spectroscopy and elemental analysis. The e ects of various experimental parameters such as contact time, initial HA concentration, solution pH and coexistent Ca2+, upon HA adsorption onto CPB modified zeolites were evaluated. The results showed that natural zeolite had negligible a nity for HA in aqueous solutions, but CPB modified zeolites exhibited high adsorption e ciency for HA. A higher CPB loading on natural zeolites exhibited a larger HA adsorption capacity. Acidic pH and coexistent Ca2+ were proved to be favorable for HA adsorption onto CPB modified zeolite. The kinetic process was well described by pseudo second-order model. The experimental isotherm data fitted well to Langmuir and Sips models. The maximum monolayer adsorption capacity of CPB modified zeolite with surfactant bilayer coverage was found to be 92.0 mg/g.     

应对大型油罐特大火灾的研究——LASTFIRE项目组简介

简要介绍了LASTFIRE项目组的成立背景、组织结构、研究领域、研究目的、研究思路、研究进展等内容,总结了该项目组近几年的研究成果,指出我国的相关企业或研究机构应积极参与这种国际研究组织,实现研究国外资源共享,共同提高大型储罐的安全技术和管理水平。     

原油外输泵房噪声分析与防治

介绍了采油厂原油外输泵房的噪声现状及噪声对职工造成的危害,分析了噪声的主要来源为电磁噪声、机械噪声、空气动力l陛噪声以及阀门噪声、摩擦噪声和管路噪声等,其声压级在90～104dB之间,频率主要集中在200～3000Hz范围,并制定了噪声治理方案。     

焦炭塔现场操作的危险原因分析和解决措施

根据具体的事故案例,对焦炭塔现场操作过程存在的各种危险进行了原因分析,提出要从完善仪表控制、加强操作工培训、改善操作条件、进行技术动改及不断完善操作规程和各类制度等方面入手,切实做好各类基础工作,才能消除危险,保障安全。     

碳排放交易制度下城市减排的机会成本研究——基于中国碳排放试点城市的实证检验

作为全球气候治理的重要手段,碳排放交易制度受到了广泛的关注与讨论。基于此,本文采用我国2010-2016年城市面板数据,运用非参数方法构建方向性环境距离函数测算了2009-2015年城市减排的机会成本,计算结果显示,试点地区与非试点地区的碳排放的机会成本整体表现为上升的趋势,且试点地区的碳排放的机会成本总体低于非试点地区。在测算城市减排机会成本的基础上,运用双重差分法来检验碳排放交易制度的有效性。经检验发现：碳排放交易制度有利于降低城市减排的机会成本,然而由于碳排放交易制度还存在碳排放权初始分配制度缺失、碳排放交易制度的定价机制扭曲等问题,因此其对降低城市减排的机会成本作用较小,并且进一步通过对政策时间趋势的分析得出政策效应随时间推移而逐渐减弱。     

“二级厌氧-微氧-好氧”组合工艺处理模拟碳纤维生产废水

对模拟碳纤维生产废水进行“厌氧-好氧”静态小试,根据COD的去除效果确定该碳纤维废水的可生化性。采用“二级厌氧-微氧-好氧”组合工艺进行动态中试,考察废水的处理效果及系统的抗冲击性能。试验结果表明：该工艺对碳纤维生产废水的处理效果较好;系统具有厌氧池出水pH增大的特点,且抗冲击能力较强;在厌氧池水温为28~38 ℃、好氧池水温不低于15 ℃、废水流量为100 L/h、进水COD为660 mg/L、进水ρ（氨氮）为4.9 mg/L的条件下,出水COD稳定在50 mg/L以下,ρ（氨氮）稳定在5 mg/L以下,能够满足GB 8978-1996《污水综合排放标准》的要求。     

SBR不同进水中反硝化除磷颗粒污泥的培养

分别以人工配水、加Ca~(2+)人工配水和实际生活污水为进水水源,在A/O/A运行模式的3套SBR反应器(R1、R2和R3)中培养反硝化除磷颗粒污泥,研究了其生化特性和启动过程的除污性能,分析了反硝化除磷能力,最后对颗粒化机理进行了探讨,重点考察了反硝化除磷颗粒污泥启动过程中对COD、NH_4~+-N、TN和TP的去除情况.结果表明,R1~R3均在30 d内成功得到反硝化除磷颗粒污泥,颗粒污泥平均粒径大于600μm,比重和比耗氧速率较大,含水率较低;培养过程中出水COD平均值低于40 mg·L~(-1),出水TN、NH+4-N及TP平均浓度低于1 mg·L~(-1);系统稳定后一个典型周期内试验表明,COD、NH_4~+-N、TN和TP的去除效果良好,对COD、NH+4-N、TN及TP的去除率可达90%以上;R1~R3中最大比释磷速率分别达14.34、8.32和2.32 mg·g·h~(-1)(以每g MLVSS每小时释放的P量(mg)计),R1~R2中最大比吸磷速率分别达14.13和2.34mg·g·h~(-1)(以每g MLVSS每小时吸收的P量(mg)计);试验结果表明,Ca~(2+)对颗粒化有促进作用.