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1.
Environmental Science and Pollution Research - Buildings account for nearly 2/5ths of global energy expenditure. Due to this figure, the 90s witnessed the rise of green buildings (GBs) that were...  相似文献   
2.
采用浸渍法制备金属改性SAPO-34分子筛催化剂,分析比较了不同单金属(Cu或Co)及不同比例双金属(Cu:Co=1:1、3:1、5:1,质量比)改性催化剂对NO的催化还原性能,评价了不同催化剂的N2选择性,并采用扫描电子显微镜(SEM)、比表面积测试、X射线衍射分析(XRD)、NH3-程序升温脱附(NH3-TPD)等表征手段对催化剂的物化性能进行了分析.结果表明,单金属Cu改性催化剂具有较宽的温度区间,在250~450℃范围内NO的转化率始终保持在100%;双金属改性使NO转化率保持为100%的最低温度下降了25~50℃,显著拓宽了低温段窗口,其中,Cu3Co1/SAPO-34催化剂的低温催化还原性能最好,200℃即可实现100%的NO转化率,175℃下的转化率也高达80%以上.Cu-Co双金属改性SAPO-34分子筛催化剂具有优异的低温催化还原NO性能,具有在机动车尾气、工业废气的低温脱硝治理领域应用的潜力.  相似文献   
3.
A series of highly-hydrophobic MIL-53-Al (MIL = Materials of Institut Lavoisier) frameworks synthesized via decoration of the Al-OH groups by alkyl phosphonic acid were developed as adsorbents for removing acetone from humid gas streams. The newly prepared materials were characterized by X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FT-IR), scanning electron microscope (SEM), N2 adsorption-desorption and thermogravimetric analysis (TGA). Their adsorption behaviors toward acetone vapor under dry and wet conditions were studied subsequently. Results showed that alkyl phosphonic acid was successfully grafted into MIL-53-Al skeleton through coordinating interaction with Al3+ generating [email protected]x (x = 12, 14, 18). The [email protected]x exhibited similar crystal structure and thermal stability to parent MIL-53-Al. Furthermore, the modified materials showed significantly enhanced hydrophobicity. The water vapor uptake of [email protected]14 decreased by 72.55% at 75% relative humidity (RH). Dynamic adsorption experiments demonstrated that water vapor had almost no effect on the acetone adsorption performance of [email protected]14. Under the condition of 90% RH, the acetone adsorption capacity of [email protected]14 was 102.98% higher than that of MIL-53-Al. Notably, [email protected]14 presented excellent adsorption reversibility and regeneration performance in 10 adsorption-desorption cycles. Taken together, the strategy of metal-OH group modification is an attractive way to improve the acetone adsorption performance over metal-organic frameworks (MOFs) under humid conditions. Besides, [email protected]14 would be deemed as a promising candidate for capturing acetone in high moisture environment.  相似文献   
4.
PM10作为大气污染物监测的主要指标之一,探究大气PM10浓度对大气环境质量和人体健康评价具有重要意义。黄、渤海滨海带包括京、津和辽、冀、鲁、苏等工、农业大省,区域大气PM10污染的时空分布和来源特征具有复杂性和典型性。在锦州、北京、天津、烟台、青岛、连云港和盐城7个城市布设10个采样点,含7个城市点和3个农村点,开展为期一年的大气颗粒物的采样;同时,于冬季1月和夏季7月在锦州、天津和烟台进行合计60 d的加密采样,藉以确定研究区域大气PM10的时空分布和来源特征。结果表明,黄、渤海滨海带大气年均PM10总浓度为(129’18)"g·m~(-3),单月最低值出现在2015年7月盐城农村样点15"g·m~(-3),最高值为2015年3月北京城市点307"g·m~(-3)。盐城大气PM10浓度(城市点(85’27)"g·m~(-3)和农村点(66’35)"g·m~(-3))显著低于其他样点大气PM10浓度。渤海滨海带中西部的京(140’68"g·m~(-3))、津(169’60"g·m~(-3))两市大气PM10年均浓度显著高于东部的锦州(125’41"g·m~(-3))和烟台(109’31"g·m~(-3));而且黄海滨海带大气PM10年均浓度(114"g·m~(-3))显著低于渤海滨海带年均浓度(136"g·m~(-3)),总体上表现出西高东低、北高南低的特征。黄、渤海滨海带城市点和农村点年均浓度分别为(129’18)"g·m~(-3)和(112’30)"g·m~(-3);农村点春冬季大气PM10浓度和城市点浓度相当,无显著差异,夏秋季大气PM10浓度略低于城市浓度,表明农村地区大气颗粒物污染情况也较为严重,需受到关注。区域内PM10浓度季节变化整体表现为春冬高、夏秋低。利用多元回归分析初步判断黄、渤海滨海带PM10属于复合来源,大气PM10浓度约30%的变化与降水、人均能耗和沙尘天气相关。黄、渤海滨海带大气PM10浓度的昼夜变化不大,大气PM10浓度与气温呈现正相关,与风速和降水呈现负相关,表现为受各种气象因素综合作用的影响。  相似文献   
5.
欧美等国家对于O_3污染的研究开展较早,已建立较成熟的O_3污染生成、扩散及空气质量等模型。文章主要介绍评述了美国环保局推荐使用的计算O_3前体物的相关模型(MOVES、NONROAD、SMOKE、EMFAC和EDMS),从基本原理和功能、污染源类型、研究尺度、所需参数等方面对比分析各模型的特点和适用范围,并综述其国内外研究应用情况;讨论了中国在这些模型的使用方面应该注意的问题,如加强开展模型计算结果验证和基础实验获得本土化的模型参数,以及中国开发的相关模型的优势和适用性等。  相似文献   
6.
Current studies provide little knowledge for a holistic assessment of green building (GB) studies and practices. This study addresses the gap by developing a systematic and multidisciplinary framework called “START” that integrates five interactive dimensions of GB, including S-stakeholders, To-total building life cycle concerns, A-actions of government, R-relevant contexts, and Ta-targets to facilitate scholars and policymakers' analysis of GB development and progress. A comparative review of Singapore's and China's GB journey has been conducted to illustrate the application of the framework. Results indicate that both countries face common challenges of achieving economic sustainability of GB due to market failure and lack of non-technical support. However, Singapore has made better progress in environmental and social sustainability than China. Singapore's GB program inclusively covers the whole building life phases whereas China mainly emphasizes on planning/design phase. Collectively, effective governance, strict law enforcement, engaged stakeholders, matured economy and emerging technologies facilitate the GB implementing in Singapore. Additional efforts are required for China to cope with its complexity and heterogeneity regarding climate zones, hierarchy of authority, and disparity of economy and resources allocation in various regions. The framework helps facilitate policymakers to comprehensively assess GB progress and highlights the importance of incorporating non-technical drivers, such as social, psychological, political factors, into multi-disciplinary research of GB programs.  相似文献   
7.
8.
Environmental Science and Pollution Research - Improved understanding of the fractionation and geochemical characteristic of rare earth elements (REEs) from steel plant emissions is important due...  相似文献   
9.
湟水河流域水质时空变化特征及其污染源解析   总被引:4,自引:0,他引:4  
邱瑀  卢诚  徐泽  王玉秋 《环境科学学报》2017,37(8):2829-2837
基于2012—2014年水质数据,综合应用多元统计分析与一维水质模型(Qual2Kw),系统分析了湟水河水质时空变化及其污染物来源.结果表明:湟水河河流水质主要受化学需氧量、生化需氧量、铜、六价铬、水温、溶解氧、总氮、氨氮等8项水质指标影响,且氨氮和总氮污染严重;湟水河水质时间上可划分为3个时段:时段1(6—10月)、时段2(5月和11月)和时段3(12月—4月),时段1水质明显优于时段2和时段3,湟水河水体受工业生活排放污水的影响显著,面源污染对河流水质的影响低于点源污染;空间上可分为3大区段:湟水河上游、中游和下游,中游西宁市段污染较重;基于Qual2Kw模型的污染物贡献比例计算结果揭示了湟水河民和桥断面的氨氮负荷主要来源于扎马隆(S2)-西钢桥(S3),总氮主要来源于报社桥(S5)-小峡桥(S6),其中支流点源是氨氮的主要污染源,普通点源即城镇生活污水和工业废水排放是总氮的主要污染来源,上游干流农田地表径流、畜禽养殖废水、农村生活污水等污染源氨氮、总氮排放也不容忽视.研究结果可以为湟水河流域水环境管理提供科学依据.  相似文献   
10.
Simple models for permeability and selectivity variations of the CO2/CH4 system in 6FDA-2,6-DAT membrane have been derived that include both temperature and pressure effects simultaneously in a single equation. The proposed models were used in MATLAB, for a membrane-based CO2-removal process design for natural gas sweetening. The effects of the following factors on design parameters were examined: feed temperature, feed pressure and permeate pressure. The effect of permeate pressure was found to be very significant in the optimization process. In order to reduce hydrocarbon losses to below 2%, a two-stage membrane process was modeled and simulated in MATLAB, and the extent of desired hydrocarbon recovery was shown to be crucial in the optimization process. It has also been shown that there exist minima for the total required area of the two-stage membrane-based process, and as the CO2 load increases in the feed, the position of these minima shift to higher values of methane loss.  相似文献   
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