Determination of 4-tert-octylphenol in surface water samples of Jinan in China by solid phase extraction coupled with GC-MS

Octylphenols, considered as xenoestrogens, mainly exist as 4-tert-octylphenol (OP) in aquatic environments. The high stability and accumulation of OP in aquatic systems have caused endocrine disruption. The OP in surface water in Jinan, China was analyzed by gas chromatography-mass spectrometry (GC-MS) coupled with solid phase extraction (SPE). Water samples were extracted by SPE on a cartridge system containing C-18 as sorbent. To increase sensitivity and selectivity, OP was derivatized to 4-tert-octyl-phenoxy silane. With the use of phenanthrene-d10 as internal standard, the detection limit based on signal-to-noise ratio (S/N = 3) was 0.06 ng/mL. The average recovery was from 84.67% to 109.7%. The precision of the method given as the relative standard deviations (RSD) was within the range 6.24%-12.96%. In the target water samples, the concentrations of OP were as follows: 15.88-71.24 ng/L for Jinxiuchuan Reservoir, 3.850-26.68 ng/L for the city moat, 6.930-41.56 ng/L for Daming Lake, 66.03-474.2 ng/L for Xiaoqing River, 14.66-17.72 ng/L for the Yellow River, and 10.60-26.43 ng/L for Queshan Reservoir. The Xiaoqing River was seriously polluted due to the discharge of wastewater from Jinan. Jinxiuchuan Reservoir had a higher concentration of OP compared with the Yellow River and Queshan Reservoir, which is ascribed to the surrounding human activities. These data are reported for the first time, providing strong support for the control of OP pollution in Jinan.     

内部营销理论与HSE推广

介绍了内部营销理论的发展历程,分析了内部营销理论在指导HSE推广工作中的可行性与必要性。     

一体化管理体系与HSE管理

介绍了一体化管理体系的特点和框架,阐明了建立一体化管理体系对HSE管理的作用,指出了实施一体化管理体系的注意事项。     

氯化镧改性黏土固化湖泊底泥中磷的研究

用氯化镧对14种黏土进行改性并研究了这些改性黏土固化磷的效果.研究了pH对改性高岭土磷吸附率和镧离子溶出的影响.结果表明,通过氯化镧改性,不同黏土的磷固定率由改性前的3%～14%提高到改性后的52%～95%.氯化镧改性高岭土在pH为5时,达到磷吸附率的最大值94.85%,并在pH值4～8范围内,保持较高的磷吸附率（>80%）.在pH>6.5的范围,La³⁺溶出浓度低于0.0178 mg/L.     

Barriers to the adoption of proactive environmental strategies

This study contributes to the knowledge of the difficulties or barriers found by firms when adopting proactive environmental strategies, providing empirical evidence from 240 Spanish industrial firms. A set of 25 barriers are initially evaluated by the managers of the sample firms and are grouped into four types of difficulties facing firms: external barriers, endemic limitations of the firm, limited environmental motivation and limited preparation of employees and operational inertia. The estimation of a structural equation model leads us to conclude that only the barriers identified as endemic limitations of the firm can be characterized as “effective barriers”, defined as problems preventing firms from progressing toward proactive environmental behavior.     

内循环(IC)反应器运行规律研究

研究采用自制内循环(IC)反应器,以实验室模拟废水为进水,接种城市污水处理厂的剩余污泥,对反应器的启动及运行过程进行研究,在经过污泥驯化、颗粒培养、调整及稳定的不同阶段连续运行.结果表明:启动初期反应器pH过低,产甲烷菌生长受抑制,导致VFA累积,容易酸化.通过改变模拟废水中微量元素的浓度及添加缓冲溶液,酸化的反应器可...     

微生物电解系统生物阴极的硫酸盐还原特性研究

针对传统硫酸盐生物还原方法中供氢体系能耗大和氢气利用率低的特点,构建双极室微生物电解系统(microbial electrolysis system,MES),研究了微生物利用阴极作为电子供体去除废水中硫酸盐及电子利用的特性.外加电压为0.8 V时,MES生物阴极在36 h内SO2-4平均去除量为109.8 mg·L-1,平均还原速率可达73.2 mg·(L·d)-1.运行时MES的最高电流密度为50~60 A·m-3,电子回收率为(43.3±10.7)%,约90%的电子被用于还原SO2-4.微生物利用MES阴极产生的H2作为电子供体还原SO2-4,主要还原产物为溶解态的S2-和气态的H2S,还原过程主要发生在前12 h.对MES施加不同外加电压的实验显示,外加电压为0.8 V时的SO2-4去除率和电荷量都比0.4 V时高;但0.4 V情形下MES的电子回收率可达到70%,且周期结束时阴极H2低于检出限,推测微生物可以直接利用阴极的电子从而提高了能量效率.实验结果最终表明,微生物可利用MES的阴极进行代谢去除废水中的SO2-4,阳极微生物产生电子降低了系统能耗,这为含硫酸盐废水的高效低耗处理提供了新的研究思路.     

浅谈实验室内审员与监督员

内审员、监督员是实验室不可缺少的关键岗位人员,他们在很多方面存在不同,二者正常有效工作能够促进管理体系规范有序运作,《实验室资质认定评审准则》对其做了言简意赅的介绍与要求,大部分实验室的内审与监督工作也有了长足的进步,但在一部分实验室存在内审工作质量不高、监督工作有缺陷等问题,个别实验室存在应付评审或监督检查现象。实验室必须加以重视并且积极改正,加强管理,进一步强化管理体系运行的有效性。     

IC反应器处理MTO废水的中试研究

中试研究了内循环(IC)反应器处理甲醇制烯烃(MTO)废水的启动和运行过程,同时考察了颗粒污泥的性状及沼气产量的变化情况。试验过程运行稳定,系统抗冲击性强。以絮状污泥为接种污泥,经过131 d的启动和运行,IC反应器的COD去除负荷可达10 kg/(m~3·d)以上,COD去除率可达90%以上。IC反应器中的成熟颗粒污泥形状规则、密实、粒径大、沉降速率快。IC反应器的沼气产量符合理论预期。     

高氯酸钾项目生产过程中的环境风险及防范措施

根据国家环保总局发布的"高污染、高环境风险"产品名录(2009年),无机盐产品高氯酸钾属于高环境风险的产品,其生产存在较大风险。高氯酸钾项目在生产过程中的环境风险主要来源于强酸、强碱、有毒有害、易燃易爆等原辅材料、产品,运输、贮存和使用过程产生的燃爆、泄漏、贮运风险以及工艺废气治理措施失效等环节。识别项目产生的环境风险主要包括爆炸风险、泄漏风险、危险化学品贮运风险及氯气直排风险,并从生产管理、生产工艺及贮运等方面提出相应的防范措施。