城郊关键带土壤中溶解性有机质的光谱特性及其时空变异

溶解性有机质(DOM)作为地球关键带中物质与能量循环的重要活性组分,其与关键带中诸多重要环境过程有着密切关系.本研究以宁波樟溪流域作为城郊关键带的典型代表区域,采集土壤样品,结合紫外可见光谱(UV-Vis)、三维荧光光谱(3D-EEM)进行特征表征,分析不同类型土壤中DOM的分布特征、影响因素和季节性变化规律.主要结果如下:林地DOC平均含量均大于耕地,其中林地秋季(15.4 mg·L~(-1))林地春季(12.5 mg·L~(-1));耕地秋季(11.9 mg·L~(-1))耕地春季(11.4 mg·L~(-1));DOM结构在紫外可见光谱下表现为耕地DOM芳香化程度(SUVA_(254))、疏水性组分(SUVA_(260))和分子量(S_R)较林地大,其中耕地秋季最为突出;三维荧光光谱结合平行因子分析(PARAFAC)把土壤DOM分为5种组分,主要以富里酸类物质为主(C_1、C_3、C_5),也含有色氨酸、酪氨酸类蛋白质(C_4)和腐殖酸(C_2)等物质,其中耕地春季的腐殖化程度最大,耕地秋季比春季含有较多类蛋白质,林地较耕地含有更多的类蛋白质,林地春秋两季中DOM结构变化不大.     

城市黑臭水体的产生原因及治理对策

在我国经济发展势头如此迅猛的背景下,城市污染问题日益严重。城市黑臭水体对城市生态环境造成严重影响,如果不能及时进行治理,则会对原有水生态循环系统造成破坏,影响城市居民正常生活。本文首先对城市黑臭水体产生原因进行分析,然后提出有效的治理对策。     

杭州夏季一次降雨过程雨水中全氟化合物及主要化学组分的变化特征

采用分段采样的方式收集杭州市2018年8月2日—3日一场降水样品，测定其中16种全氟化合物（PFCs）及主要化学组分浓度。结果发现，此次降雨过程水样的pH值范围为5.04～5.32，均为弱酸性降水，酸雨类型为复合型，检出的主要阳离子为NH+4，主要阴离子为SO2-4和NO-3；样品中检出7种中短链PFCs，包括2种全氟烷基磺酸（PFSAs）和5种全氟烷基羧酸（PFCAs），ΣPFCs质量浓度范围为4.41 ng/L～25.2 ng/L，主要污染因子全氟辛酸（PFOA）质量浓度范围为096 ng/L～13.1 ng/L；降雨过程对大气污染清除作用的统计结果表明，区域大气环境中的主要化学组分及除全氟丁酸（PFBA）之外的PFCs污染主要吸附在云下大气颗粒物上；雨水中各污染因子浓度变化特征及相关性统计结果提示，杭州市大气中PFCAs和PFSAs两类PFCs可能来自不同的污染源。     

海洋陆源污染的产生原因与防治模式

海洋陆源污染是陆域经济社会活动行为及其对海洋生态环境造成的负面影响进而出现的污染性问题。累积性的陆源排污不仅会对海洋环境容量造成不良影响,同时也会对海洋自净能力造成减弱影响,不利于沿海地区的经济发展。目前,关于海洋陆源污染问题的防治工作刻不容缓,本文就从多个方面进行统筹规划与科学部署,通过深入掌握海洋陆源污染的具体成因,提出了针对性防治模式,以期为相关人员提供一定的借鉴价值。     

空气污染天气过程与气象要素之间的关联性分析

随着经济和社会的不断发展,地球的环境正在遭受着严重的侵害,关于环境的问题也日益显现出来,比如全球变暖、雾霾等现象。本文分析了空气污染的因素、气象要素对空气质量的影响,并提出了防治空气污染的对策。     

危险工艺本质安全化技术

<正>化工行业不可避免的涉及各种具有潜在风险的化学品及工艺,如何降低化学品及其工艺过程可能带来的危害是任何一个化工企业不可回避的课题。经过多年的探索和积累,青岛安全工程研究院建立了一支经验丰富、朝气蓬勃的研究团队和健全的实验手段,以危险化工工艺本身危害特点为研究对象,采用实验室模拟和计算机软件模拟相结合的方式,开展危害辨识、工艺危害特征及防范措施、工艺安全临界     

油气回收技术推广介绍

<正>汽油在储存、运输过程中挥发的油气对环境、健康和安全产生的危害越来越引起人们的重视。据统计,中国石化作为我国最大的成品油供应商,2005年汽油产量就达到2.298×10~7t,如此巨量的汽油在储运环节中,每年排到大气中的油气可达几万吨。因此,全面推广油气回收技术,控制油气的排放,实现清洁生产,不但满足HSE等方面的需要。也体现了中国石化作为中央企业的一种社会责任感。     

某麦芽生产厂废水管理与处理实践研究

麦芽生产过程包括清选、浸麦、发芽、烘干以及除根等工序,废水主要来自于浸麦、发芽等工序。某麦芽生产厂根据麦芽过程用水和废水产生的特点,采用设备改进、加强工艺管理、用水管理、废水回用、提高员工技能等措施,通过源头削减和生产全过程控制,合理调节生产用水,降低生产用水量和废水产生量,麦芽生产水耗指标为2.4 m3水/吨麦芽。麦芽废水采用SBR工艺进行处理,出水水质满足排放标准要求。该麦芽企业废水管理和处理经验为同行业提供了较好的案例。     

Antimony smelting process generating solid wastes and dust：Characterization and leaching behaviors

A large amount of solid waste has been produced by the antimony smelting process in the＂World Capital of Antimony＂, Xikuangshan area in China. This study comprehensively investigated the physical and chemical characteristics of the various solid wastes, as well as the leaching behavior of the solid wastes, which included water-quenched slag,arsenic-alkali residue, desulfurized slag and blast furnace dust. These four types of waste were enriched in a variety of heavy metals and metalloids and more specifically with As and Sb levels up to 8.6 × 104 and 3.16 × 105mg/kg, respectively, in arsenic-alkali residue. For desulfurized slag and water-quenched slag, the leaching concentration of Sb significantly exceeded the acceptable limits during the leaching tests using the toxicity characteristic leaching procedure and the synthetic precipitation leaching procedure. In addition, As leaching in arsenic-alkali residue was extraordinarily hazardous, being three orders of magnitude higher than the regulatory level of As. According to the results of the extraction tests, all the tested wastes were classified as hazardous waste.     

Fouling distribution in forward osmosis membrane process

Fouling behavior along the length of membrane module was systematically investigated by performing simple modeling and lab-scale experiments of forward osmosis （FO） membrane process. The flux distribution model developed in this study showed a good agreement with experimental results, validating the robustness of the model. This model demonstrated, as expected, that the permeate flux decreased along the membrane channel due to decreasing osmotic pressure differential across the FO membrane. A series of fouling experiments were conducted under the draw and feed solutions at various recoveries simulated by the model. The simulated fouling experiments revealed that higher organic （alginate） fouling and thus more flux decline were observed at the last section of a membrane channel, as foulants in feed solution became more concentrated. Furthermore, the water flux in FO process declined more severely as the recovery increased due to more foulants transported to membrane surface with elevated solute concentrations at higher recovery, which created favorable solution environments for organic adsorption. The fouling reversibility also decreased at the last section of the membrane channel, suggesting that fouling distribution on FO membrane along the module should be carefully examined to improve overall cleaning efficiency. Lastly, it was found that such fouling distribution observed with co-current flow operation became less pronounced in counter- current flow operation of FO membrane process.