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801.
Typical top-down regional assessments of CO2 storage feasibility are sufficient for determining the maximum volumetric capacity of deep saline aquifers. However, they do not reflect the regional economic feasibility of storage. This is controlled, in part, by the number and type of injection wells that are necessary to achieve regional CO2 storage goals. In contrast, the geomechanics-based assessment workflow that we present in this paper follows a bottom-up approach for evaluating regional deep saline aquifer CO2 storage feasibility. The CO2 storage capacity of an aquifer is a function of its porous volume as well as its CO2 injectivity. For a saline aquifer to be considered feasible in this assessment it must be able to store a specified amount of CO2 at a reasonable cost per ton of CO2. The proposed assessment workflow has seven steps that include (1) defining the storage project and goals, (2) characterizing the geology and developing a geomechanical model of the aquifer, (3) constructing 3D aquifer models, (4) simulating CO2 injection, (5,6) evaluating CO2 injection and storage feasibility (with and without injection well stimulation), and (7) determining whether it is economically feasible to proceed with the storage project. The workflow was applied to a case study of the Rose Run sandstone aquifer in the Eastern Ohio River Valley, USA. We found that it is feasible in this region to inject 113 Mt CO2/year for 30 years at an associated well cost of less than US $1.31/t CO2, but only if injectivity enhancement techniques such as hydraulic fracturing and injection induced micro-seismicity are implemented. 相似文献
802.
Paper recycling is an environmental important activity that is carried out in all the countries, but during the recycling process a paper waste is produced. Generally these wastes are placed in landfill sites but it is possible to profit it as secondary fuel and raw material in manufacture furnaces.
In this work the combustion of the waste papers with cement and ceramic raw material has been studied with the objective to analyse the interaction of these substances with the emitted pollutants like PAHs and PCDD/Fs.
The results of the study show that the presence of inorganic material produces an increment in the lighter PAH emission but chlorinated compounds are not affected. The PCDD/F emission level found in the combustion of this waste is quite low compared with other wastes subjected to similar conditions. 相似文献
803.
Bauer RD Maloszewski P Zhang Y Meckenstock RU Griebler C 《Journal of contaminant hydrology》2008,96(1-4):150-168
Various abiotic and biotic processes such as sorption, dilution, and degradation are known to affect the fate of organic contaminants, such as petroleum hydrocarbons in saturated porous media. Reactive transport modeling of such plumes indicates that the biodegradation of organic pollutants is, in many cases, controlled by mixing and therefore occurs locally at the plume's fringes, where electron donors and electron-acceptors mix. Herein, we aim to test whether this hypothesis can be verified by experimental results obtained from aerobic and anaerobic degradation experiments in two-dimensional sediment microcosms. Toluene was selected as a model compound for oxidizable contaminants. The two-dimensional microcosm was filled with quartz sand and operated under controlled flow conditions simulating a contaminant plume in otherwise uncontaminated groundwater. Aerobic degradation of toluene by Pseudomonas putida mt-2 reduced a continuous 8.7 mg L(-1) toluene concentration by 35% over a transport distance of 78 cm in 15.5 h. In comparison, under similar conditions Aromatoleum aromaticum strain EbN1 degraded 98% of the toluene infiltrated using nitrate (68.5+/-6.2 mg L(-1)) as electron acceptor. A major part of the biodegradation activity was located at the plume fringes and the slope of the electron-acceptor gradient was steeper during periods of active biodegradation. The distribution of toluene and the significant overlap of nitrate at the plume's fringe indicate that biokinetic and/or microscale transport processes may constitute additional limiting factors. Experimental data is corroborated with results from a reactive transport model using double Monod kinetics. The outcome of the study shows that in order to simulate degradation in contaminant plumes, detailed data sets are required to test the applicability of models. These will have to deal with the incorporation of existing parameters coding for substrate conversion kinetics and microbial growth. 相似文献
804.
橡胶促进剂M盐废水生物处理技术研究 总被引:1,自引:0,他引:1
为探讨微生物技术在橡胶促进剂M盐废水处理中的应用,利用高效优势蘸强化A2O工艺对橡胶促进剂M盐废水进行处理,整个系统运行过程分为污泥的培养与驯化阶段及稳定运行阶段。在稳定运行阶段COD0平均去除率达90.71%,氨氮平均去除率达78.31%。以Mn^2+、Fe^2+、Mg^2+、Ni^2+为4个影响因子,通过正交实验分析无机离子对橡胶促进剂M盐废水中有机物降解的促进作用。由实验数据的摄差大小可知,各无机离子对优势复合菌降解橡胶有机废水的影响从大到小依次为:Mn^2+、Fe^2+、Ni^2+和Mg^2+。4种离子最佳质量浓度组合为:0.500mg/L的Mn^2+、1.00mg/L的Fe^2+、35.0mg/L的Mg^2+和0.025mg/L的Ni^2+。 相似文献
805.
啤酒酵母吸附Cu^2+的模拟实验 总被引:17,自引:0,他引:17
研究了啤酒酵母吸附重金属Cu2+离子的可行性及反应条件对去除作用的影响.结果表明:用啤酒酵母处理Cu2+,在起始浓度ρ0为20~400mg/L的范围内,吸附量w为2.98~12.03mg/g,说明用啤酒酵母去除重金属Cu2+是可行的.吸附反应在10~20min基本达到吸附平衡.最适反应温度(θ)和pH分别为15~20℃和4.0~6.0,酵母细胞有一最适投加用量.Freundlich吸附等温方程的分析表明,η与重金属离子种类有关,与酵母细胞种类关系较小;k值与酵母种类和重金属离子种类有关. 相似文献
806.
807.
808.
809.
Zn^2+对水鳖的毒性作用 总被引:3,自引:0,他引:3
研究了不同浓度Zn^2 毒害对水鳖叶片膜脂过氧化作用及其体细胞超微结构的影响。结果表明,随着Zn^2 浓度的增加,叶绿素含量、SOD、CAT、POD活性先后升降,叶绿素a/b值值则逐渐减小,而MDA含量增加,O2^-产生速率也逐渐增大。同功酶分析表明,Zn^2 可以诱导新的POD同功酶,电镜观察发现,低浓度Zn^ 处理下,水鳖叶细胞中核质空泡化,叶绿体膨胀变形,线粒体嵴膨胀,溶酶体、小泡数量增加,且出现了多膜复合体;随着Zn^2 浓度的增加,核质消失,叶绿体和线粒体解体,而根尖分生细胞中则出现了多核仁现象。 相似文献
810.
海洋巨藻(Durvilaea potatorum)生物吸附剂对Hg~(2 )的吸附动力学研究 总被引:2,自引:0,他引:2
对经特殊的稳定化预处理所得的海洋巨藻 (Durvillaeapotatorum)生物吸附剂对Hg2 的吸附动力学进行了研究 ,报导了不同Hg2 初始浓度、温度以及生物吸附剂平均粒径下动态吸附量与时间的关系 .结果显示 ,各吸附动力学曲线呈优惠型 ;当生物吸附剂平均粒径为 0 .45mm时 ,Hg2 的半饱和时间tS均不超过 6 0min ;Hg2 初始浓度和生物吸附剂粒径越小 ,吸附温度越大 ,达到吸附平衡所需的时间越短 .在测试范围内 ,生物吸附剂的平衡吸附容量与粒径和温度无关 .同时考察了吸附过程中的传质效应并对液膜传质系数kL进行了关联 ,结果表明 :当吸附时间t≤tS时 ,Hg2 的吸附速率为液膜传质控制 ;在测试范围内 ,kL为 0 .0 40 7~ 0 .112cm/s.本研究结果为利用海洋巨藻 (Durvillaeapotatorum)生物吸附剂处理含汞废水的规模化应用提供了一定的依据 .图 5表 2参 11 相似文献