基于景观指数的新疆生产建设兵团生态环境变化

在遥感与地理信息系统技术支持下,以兵团2000、2005、2010年3期TM影像和HJ1A-CCD1影像为主要数据源,研究了兵团景观空间格局变化特征。结果表明,兵团景观类型从2000—2010年发生了较大变化,农田和城镇面积显著增加,草地、灌丛和冰川(永久积雪)显著减少。城镇景观受人为活动干扰强度最大。分析认为,人口和农业机械化是影响农田景观的主要驱动因素,经济发展和小城镇建设是影响城镇景观格局的主要因素,而政策导向是调节兵团景观格局变化的有效途径。     

某废弃农药生产场地地下水挥发性有机物污染健康风险评价

对常州某废弃农药生产场地地下水中挥发性有机物污染状况和健康风险进行了调查评价。结果表明,该场地地下水中挥发性有机物污染以苯系物、氯代苯类和氯代烃类为主;部分点位地下水健康风险评价结果超出可接受范围,可能危害人体。     

氮源对克雷伯氏菌NⅢ2分泌絮凝剂特性的影响

实验研究了蔗糖为碳源,硝酸钠、脲、蛋白胨、硫酸铵和氯化铵等氮源对NⅢ2发酵产絮凝剂的影响。结果表明,发酵液起始pH值为7.50,以硝酸钠为氮源,发酵液pH会上升,升至7.60～8.34时,NⅢ2菌株开始大量分泌微生物絮凝剂,发酵72 h,产量可达7.5 g/L,该产量是目前报道的克雷伯氏菌产絮凝剂的最高值。脲为氮源,pH则下降,降至5.04～6.49时,大量分泌絮凝剂,发酵72 h产量达5.2 g/L。蛋白胨、氯化铵和硫酸铵等为氮源时,pH下降十分明显,pH小于3.71时有絮凝剂分泌,发酵72 h产量约2.0 g/L或更小。以硝酸钠和脲为氮源时,发酵液中有黄色物质分泌,该黄色物质出现或黄色逐渐加深,是NⅢ2菌高产絮凝剂的标志。除硫酸铵外,其他氮源发酵所产絮凝剂为O-糖蛋白。当以硝酸钠、脲、蛋白胨、硫酸铵和氯化铵为氮源时,絮凝剂中蛋白的含量分别为9.55%、33.28%、19.39%、13.81%和15.51%,且蛋白含量越高,絮凝剂活性越大。     

一种新型微生物菌剂处理生活污水

利用从食材中筛选纯化的特定微生物制成复合菌剂,在自然、厌氧和曝气3种不同的供氧条件下,添加不同比例的菌剂处理生活污水,以COD和氨氮浓度为参考指标,考察菌剂对污水的净化效果,并分析其原因。结果表明:(1)菌剂投加量在0.5‰～1‰时对污水中COD的去除具有明显促进作用,自然、厌氧和曝气3种条件下,COD去除率最大分别提高了8.77%、11.22%和11.11%;(2)氨氮的去除效果受反应条件影响很大,厌氧条件下菌剂对污水中氨氮的去除作用不明显,自然和曝气条件下,菌剂对氨氮去除效果显著,去除率增幅最高分别达到22.6%和52.28%;(3)以0.5‰的菌剂投加量曝气处理2 d,COD和氨氮的去除率可以分别提高11.11%和14.13%,初步研究显示,该菌剂对生活污水具有较好的净化效果。     

氟化工建设项目清洁生产评价

针对某大型氟化工项目,从氟化工产业链的发展、清洁生产控制指标、持续清洁生产等方面分析评价了该企业所采取的清洁生产措施。指出企业在以后的生产过程中应密切关注产品生产新工艺的进展,研究对原有工艺参数的优化,完善环境管理制度,不断探索先进的管理经验,从源头消减污染物的产生量,提高企业经济效益。     

国产脱硝催化剂在国电长源荆州电厂2×300MW机组上的应用

随着新火电厂大气污染物排放标准的出台,NOx排放标准提高,现有的脱硝技术难以满足要求,需要增加后端烟气脱硝处理技术.选择性催化还原法是较成熟的烟气脱硝技术,催化剂是SCR技术的核心.针对国内某催化剂在国电长源荆州电厂的应用情况,详细描述了催化剂的设计选型过程.运行结果表明,该催化剂完全可以满足长源荆州电厂的性能要求,说明国产脱硝催化剂的设计选型、生产以及运行等技术能力已达到要求.     

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.     

厌氧-好氧工艺处理造纸废水工程实例及清洁生产

介绍了万隆造纸厂废水处理工程改建实例,分析了厌氧-好氧工艺相比原好氧工艺的优势及其运行状况与处理成本。工程改造并实行清洁生产后,污染物质排放总量明显减少,水质可达到GB18918-2002一级A标准,满足一般回用水的质量要求,同时与原有的好氧生物处理工艺相比可节省动力约55%。工程采取节水措施后,产品耗水量仅为7～9 m3/t,有效控制了水资源消耗。通过运行状况可知活性污泥法作为厌氧后处理工艺操作控制方便,并可在较低溶解氧(0.9～1.2 mg/L)条件下运行,有效减少了能耗,是实际工程中较为理想的厌氧后处理工艺。     

一体化生物膜技术处理滨海农村污水

对厌氧-3级好氧/缺氧生物膜工艺进行技术改进,并对改进后的"一体化生物膜技术"处理低碳氮比农村生活污水进行了实际应用。新工艺增设了回流泵(回流比2∶1),且厌氧段悬浮填料装填率由原来的15%提高到30%,3级好氧/缺氧段YDT型弹性立体填料装填率依次由原来的50%、40%、25%提高到70%、60%和40%。装置连续稳定运行12个月,平均进水量为18 m3/d,HRT为3.7 d,监测结果表明:对COD、BOD、NH3-N、TN、TP和SS平均去除率分别为75.6%、85.9%、86.7%、63.9%、69.3%和85.5%;出水COD、BOD、NH3-N、TN、TP和SS的平均浓度分别在34.9、8.9、3.4、9.9、0.9和6.9 mg/L以下。改进后出水BOD和TN的去除能力有较大提高,除TP外其他各项指标均达到了设计要求。     

Contamination and emission factors of PCDD/Fs, unintentional PCBs, HxCBz, PeCBz and polychlorophenols in chloranil in China

The production of chloranil is regarded as a potentially significant source of unintentional POPs. This research aimed to identify the contamination levels of polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/Fs), polychlorinated biphenyls (PCBs), hexachlorobenzene (HxCBz), pentachlorobenzene (PeCBz) and polychlorophenols in chloranil samples and identify the formation pathways. The toxicity equivalent (TEQ) values for PCDD/Fs in the chloranil samples ranged from 163 to 1 540 200 pg I-TEQ g⁻¹, while the PCB TEQ values ranged from 1.9 to 3.3 pg WHO-TEQ g⁻¹. High levels of HxCBz, PeCBz and polychlorophenols were also detected in the chloranil samples. The average emission factors were 522.2 mg I-TEQ t⁻¹ (PCDD/Fs), 0.0026 mg WHO-TEQ t⁻¹ (PCBs), 32.6 mg t⁻¹ (HxCBz), and 136.6 mg t⁻¹ (PeCBz). The PCDD/Fs and PCBs are thought to be formed from the polychlorophenols and polychlorobenzenes generated during the chloranil production process. Purification of the chloranil products can reduce the unintentional POPs releases and protect the environment.