由废气和藻类合成ω-3脂类

<正>Hem Eng,2014-12-01美国伊利诺伊州的Lanza Tech公司与印度高级生物能源研究IOC-DBT中心之间合作,开发出一种碳捕获工艺。该工艺可在藻类中合成ω-3脂类。经由一种在专门的气体发酵反应器中进行的连续发酵步骤,专有微生物将捕获到的废气(CO2和H2)转换成醋酸酯。任何CO2源均可使用。由于需要与H混合,该工艺最好使用高度浓缩的CO2(体积分数大于50%)。醋酸酯是在发酵过程中产生的唯一代谢物。所得富含醋酸酯的发酵液以及藻类被容纳在     

聚合氯化铁-聚(环氧氯丙烷-二甲胺)复合絮凝剂在模拟水处理中的混凝特性研究

制备出一系列具有不同聚合氯化铁(PFC)的碱化度(B)、不同聚(环氧氯丙烷-二甲胺)[P(EPI-DMA)]质量分数[ω(E)]和黏度(η)的PFC-P(EPI-DMA)复合混凝剂,并将其用于模拟染料废水和模拟天然地表水的絮凝脱色处理,对比探讨了ω(E)、η和B对PFC-P(EPI-DMA)中铁的形态分布及其混凝效果的影响,以及混凝作用机制.结果表明,复合絮凝剂中铁的有效形态含量随ω(E)的增大而不断降低;η=850 mPa.s时,复合混凝剂中铁的有效形态含量最高;随B值的增大,Feb含量先增大后减少,而Fec含量逐渐增大.一定程度上使用预水解程度较低、有机成分黏度较大的PFC-P(EPI-DMA)有利于混凝效果的提高,复合混凝剂中有机成分质量分数对混凝效果的影响则与处理对象有关.在模拟水处理中,复合混凝剂依靠电性中和及架桥吸附能力发挥混凝特性.     

生活垃圾填埋过程含水率变化研究

为分析垃圾在好氧和厌氧条件下降解过程中含水率变化的规律,采用时域反射测量(time domain reflectometry,TDR)技术监测了垃圾填埋过程中含水率的变化情况.结果表明,填埋过程中垃圾体积含水率随时间逐渐增大,垃圾持水性能不断提高.好氧初期垃圾内水量变化与含水率变化正相关,好氧后期则为负相关;厌氧填埋过程中,垃圾沉降压缩是含水率变化的主要原因.垃圾TDR读数与基于物质衡算的垃圾体积含水率计算值之间有较好的相关性,好氧填埋过程两者最大偏差约为±5%,厌氧填埋过程两者最大偏差约为±2%,TDR技术适用于实际填埋工程的含水率测量.     

广州市二氧化硫初始排污权分配模型研究

排污权初始分配是进行排污权市场交易的前提和基础,为排污权交易的有效进行提供保障。文章以广州市为区域研究单位,在现有排污权初始分配的理论和实践基础上,展开排污权初始分配研究。基于企业的发展规模、企业对社会的贡献性、企业对环境的污染现状以及企业运用技术治理环境的投入这4方面的因素,构建了二氧化硫初始排污权分配的评价指标体系,从而建立二氧化硫初始排污权分配的AHP层次分配模型。并以广州市火电行业为例,引入排污数据,具体研究了广州市火电行业的初始排污权分配方案,根据各指标的权重赋值,在最终得到的分配结果中,发电量多少、脱硫设施效率和二氧化硫去除率获得的权重最大,在分配中是主要考虑的指标。从分配结果看,各企业获得的排污权分配量较合理。此方法具有一定的实用性,为政府构建排污权交易市场,进行排污权初始分配提供有效方法。     

广州番禺区不同地类的非点源污染排放特征

在广州番禺区建设代表城市、农田、村镇、园地4类典型集水区的径流试验小区,对每个径流小区采集3场有效降雨径流以研究不同土地利用类型的非点源污染负荷输出特征。结果表明,不同土地利用类型的污染物输出浓度差别较大,TSS和COD输出浓度(EMC值)的大小排列顺序为园地>农田>村镇>城市;NH3--N为农田>城市>园地>村镇;NO3--N为城市>农田>村镇>园地;TN为农田>城市>园地>村镇;TP为农田>园地>城市>村镇。对于农田集水区,TSS和COD的输出明显受降雨的影响,而N、P污染物的输出受施肥的影响更为显著;对于城市集水区,晴天累积污染物的数量和降雨情况是决定初期径流中污染负荷的主要因素。污染负荷与径流量之间相关性显著,且颗粒物是携带污染物的重要载体。各径流小区的初始冲刷效应分析结果显示,不透水地面更易发生降雨初期冲刷;降雨强度是影响降雨径流初始冲刷的关键因素。     

保护层分析应用规则研究

为了确保保护层分析(LOPA)结果的客观性和可靠性,对LOPA的应用规则进行了探讨.按照LOPA应用的基本程序,对场景筛选、确定初始事件、独立保护层评估、场景频率计算、风险决策及后续跟踪等的相关规则进行了阐述.企业在应用LOPA时,应严格按照这些规则进行.     

采用体积信息熵表征颗粒污泥系统稳定性及其稳定机制

SBR反应器中培养自养硝化颗粒污泥,在絮体转化为颗粒过程中,颗粒的体积信息熵从2.05(27 d,初见颗粒)降低为1.85(95 d),熵值降低的主要动力来自于松散的絮体在较快沉速选择压条件下被淘洗出系统.当絮体被淘洗出系统即完成颗粒化过程,在129 d时测得系统中颗粒沉速分布的中位数为6.27 m.h-1,因此颗粒体积熵值的变化不再受沉速选择压(6m.h-1)的控制.颗粒的粒径、沉速及体积熵值分布均呈现周期性变化,其中信息熵的均值为2.16,最小值为1.79,最大值为2.63.在这种周期性变化过程中,系统总是表现为粒径均值先增大后减小.熵值的波动的驱动力来自于颗粒的破碎与破碎体的成长,体积分布信息熵的大小可以很好地表征系统的稳定性及其稳定机制.     

光腔衰荡光谱(CRDS)法观测我国4个本底站大气CO2

利用基于光腔衰荡光谱(CRDS)技术自组装的大气CO2在线观测系统,于2009年在青海瓦里关、浙江临安、北京上甸子和黑龙江龙风山4个世界气象组织全球大气观测网(WMO/GAW)大气本底站对大气CO2进行了在线观测.初步分析结果表明,4站全年大气CO2体积分数最低值出现在7～8月,夏季临安、龙风山和上甸子站CO2平均体积...     

Effect of nutrient conditions on the toxicity of naphthalene to Chlorella pyrenoidosa

The toxicity of naphthalene to a freshwater microalga, Chlorella pyrenoidosa, and the subsequent recovery of algae from the damage were investigated under two nutrient conditions, either enriched with nitrogen (N) and phosphorus (P), or starved of N and P. Results showed that C. pyrenoidosa was more sensitive to naphthalene under N,P-enriched condition, and the inhibitory rate generally increased at first and then decreased gradually with the evaporation of naphthalene under both nutrient conditions. Enriched N, P reduced the inhibitory rate at initial naphthalene concentration of 5 and 10 mg/L, but enhanced it at 100 mg/L, at which more severe ultrastructure damages were found than those under N,P-starved condition. Observed damages included partly or totally disappearance of nucleolus, nuclear, and plasma membranes. According to the chlorophyll content and cell density measurements, C. pyrenoidosa could recover from naphthalene damage with initial concentrations 6 50 mg/L in 7 days under both nutrient conditions, while they could not recover if the initial concentration of naphthalene was at 100 mg/L. Under the N,P-starved condition, the inability of C. pyrenoidosa to recover from the naphthalene damage was consistent with the results of high inhibitory rate, low value of specific growth rate (SGR, 0.05 day??1), and the severe destruction of cell structure. However, under the N,P-enriched conditions, the observed lower inhibitory rate, higher value of SGR (0.55 day??1), and the intact cell structure of most cells suggested that algae could potentially recover from the naphthalene damage.     

Evaluation of reusing alum sludge for the coagulation of industrial wastewater containing mixed anionic surfactants

A coagulation-flocculation process is typically employed to treat the industrial wastewater generated by the consumer products industry manufacturing detergents, soaps, and others. The expenditure of chemicals including coagulants and chemicals for pH adjustment is costly for treating this wastewater. The objective of this study was to evaluate the feasibility of reusing the aluminum sulfate (alum) sludge as a coagulant or as a coagulation aid so that the fresh alum dosage can be minimized or the removal e ciency can be enhanced. The experiments were conducted in a jar-test apparatus simulating the coagulation-flocculation process for simultaneous removals of organic matters, anionic surfactants, suspended solids, and turbidity. At the optimum initial pH value of 10 and the fresh alum concentration of 400 mg/L, the total suspended solids (TSS), total chemical oxygen demand (TCOD), total anionic surfactants, and turbidity removal e ciencies were 71.5%, 76.4%, 95.4%, and 98.2%, respectively. The addition of alum sludge as a coagulant alone without any fresh alum addition could significantly remove the turbidity, TCOD, and anionic surfactants. The TSS was left in the supernatants after the settling period, but would subsequently be removed by adding the fresh alum. The TSS, TCOD, and turbidity removal e ciencies were also enhanced when both the alum sludge and the fresh alum were employed. The TCOD removal e ciency over 80% has been accomplished, which has never fulfilled by using the fresh alum alone. It is concluded that the alum sludge could be reused for the treatment of industrial wastewater generated by the consumer products industry.