树脂与活性炭吸附油气的实验研究

吸附剂的性能对油气吸附分离的效果起着决定性的作用。测定了活性炭和吸附树脂在常温下对油气的静态吸附和脱附特性，比较吸附树脂与活性炭的吸附率、解吸率。实验结果表明，吸附树脂吸附率高，解吸容易。测定了活性炭和吸附树脂对油气的吸附穿透曲线和热效应。实验结果表明，吸附树脂的穿透时间长，温升略低，适于油气吸附分离。同时，利用Yoo...     

活性炭处理甲苯气体吸附再生实验研究

研究了活性炭对甲苯废气的吸附穿透过程及热空气解吸过程.穿透曲线实验结果表明,在常规空塔气速范围内,传质区高度基本在5.06～9.75 cm,传质区不饱和度在0.4～0.7.在动态运行情况下,活性炭对甲苯的饱和吸附容量在0.16～0.24 g/g.热空气吹脱实验表明,适宜的脱附工况条件为脱附温度180 ℃、脱附空气流速0.106 m/s、脱附时间40 min.     

改性疏水硅胶用于油气吸附解吸的研究

吸附法为油气回收的常用方法,对吸附剂的研究有着重要的意义。为了开发出高吸附量、高热稳定性和疏水性的油气回收专用硅胶,对常规硅胶的物理及化学改性方法进行了研究。通过分析热处理温度、热处理时间及升温速度等因素对改性硅胶吸附效果的影响,提出了汽油油气吸附率高、吸水率低的硅胶改性条件为:酒石酸改性剂,热处理温度550~650℃,热处理时间3~10 h,升温速度3~10℃/min。同时,研究了影响改性硅胶解吸效果的因素,结果表明,真空度越高,温度越高,解吸次数越多,改性硅胶的解吸率越高。     

微波加热及真空集成再生活性炭

吸附法油气回收技术中，吸附剂的再生是一个难点和研究重点。微波加热再生作为一种新技术，受到人们的广泛关注。运用正交实验，研究了微波功率、辐照时间、活性炭量和真空度对吸附了汽油油气的富活性炭的再生率和损耗率的影响，发现影响顺序为微波功率〉辐照时间〉活性炭量〉真空度。综合考虑各方面因素，得出实验的最优方案为微波功率300W、辐照时间240s、活性炭量4g、真空度O．06MPa。还研究了活性炭多次吸附一再生后平衡吸附率和表面结构的变化。结果表明，微波和真空法对活性炭的表面结构影响不大，有利于活性炭的多次循环利用。综合比较真空再生法、真空和加热再生法、微波和真空再生法的再生效果，结果表明，微波和真空再生法稳定性较好。     

不同再生工艺对活性炭吸附性能的影响分析

吸附法油气回收技术中,吸附剂的再生是一个难点和研究重点。微波加热作为一种新的再生技术,受到人们日益的重视。实验利用比表面积及孔隙分析仪测定了经多次微波真空,加热真空和加热再生后的活性炭的表面结构变化,通过对比分析,探讨了3种工艺多次再生活性炭对活性炭表面结构的影响。结果表明,3种工艺均对活性炭结构都有所破坏,但微波真空再生对活性炭比表面积和孔容破坏最小,净吸附容量最大,从效率及能耗上都比较好。     

油气吸附剂及其改性方法

吸附剂的性能对油气吸附分离的效果起着决定性的作用。介绍了活性炭、活性炭纤维、疏水硅胶和疏水沸石等油气吸附剂的吸附性能及改性工艺,提出了吸附剂的改性、复合吸附剂的使用、配套吸附器的开发、新型吸附剂对油气的吸附及解吸工艺将是今后研究的重点。     

改性污泥活性炭对水中镉离子的吸附性能

以城市污水处理厂的剩余污泥为原料,氯化锌为活化剂制备污泥活性炭,对一部分污泥活性炭用6.0 mol/L的硝酸进行改性,并研究了未改性和改性的污泥活性炭对Cd2＋的吸附行为的影响。结果表明,在pH为5.0、Cd2＋初始浓度为100 mg/L、吸附剂投加量为2.0 g/L、反应温度为25℃时,未改性的污泥活性炭吸附容量为8.45 mg/g,硝酸改性的污泥活性炭吸附容量达到了23.35 mg/g。改性和未改性的污泥活性炭对Cd2＋都有较好的吸附容量,硝酸改性大幅度提高了污泥活性炭对Cd2＋的吸附性能。常温下改性污泥活性炭对Cd2＋的吸附符合Langmuir吸附等温式。     

核桃壳炭化吸附废水中Cr(Ⅵ)的性能研究

采用氯化锌活化法制备生物质废物硬壳活性炭,工艺条件为:核桃壳与氯化锌溶液质量比为1∶1.5、氯化锌溶液质量分数50%、炭化温度300℃、炭化时间90 min、活化温度600℃、活化时间60 min。对产品比表面积、孔径和表征进行了分析,并探讨了该核桃壳活性炭吸附废水中六价铬的pH值、废水初始浓度、吸附时间、振动转速等影响因素。结果表明:制得的活性炭碘吸附值为1 038.33 mg/g,比表面积为645.36 m2/g,平均孔半径为1.37 nm。当活性炭用量为0.1 g,废水pH=3,吸附接触时间为1 h,取100 mL浓度为50 mg/L的含Cr6+废水时,处理吸附量可达48.57 mg/g。活性炭最大饱和吸附值为80.24 mg/g。吸附符合Langmuir等温模式,吸附等温方程式为Ce/Qe=0.0083+0.0121Ce。     

微波活化制备加拿大一枝黄花活性炭及对Cd（Ⅱ）的吸附

以入侵植物加拿大一枝黄花为原料,在400℃氮气保护下,直接碳化90 min后,以KOH为活化剂,微波活化的方法制备了高比表面积微孔活性炭SCAC。结果显示活性炭SCAC的表面面积为1 888 m2/g,总孔容量为0.804 cm3/g,微孔容量为0.741 cm3/g,平均孔径0.567 nm,微孔平均孔径0.488 nm。通过静态吸附实验研究了活性炭添加量、溶液初始浓度、初始pH及吸附时间对SCAC吸附Cd(Ⅱ)的影响,通过动力学方程拟合探讨了活性炭对Cd(Ⅱ)的吸附机理。结果表明,吸附平衡时间、最佳pH及活性炭添加量分别为120 min、pH>7.5及0.05 g/50 mL,活性炭SCAC吸附动力学过程符合准二级方程模型。     

生物质活性炭的制备及其染料废水中的应用

以城市污水厂活性污泥为原料,用3 mol/L ZnCl2溶液活化,通入水蒸气作活化气制备活性炭吸附剂.实验结果表明,温度为600℃条件下,活化时间为1 h,制得的活性炭其碘吸附值为374.10 mg/g,比表面积为381.62 m2/g,孔容积为0.25 cm3/g,微孔容积为0.11cm3/g.并进一步将生物质活性炭应用于染料废水的处理,考察了吸附时间、活性炭投加量和pH对色度及TOC的脱除效果的影响.室温下,酸性大红GR染料废水初始浓度为300 mg/L,污泥活性炭的最佳投加量为2%(质量分数),吸附15min,废水色度脱除率可达99.6%,TOC去除率可达99.7%,利用等温吸附实验作吸附等温线,吸附等温线可以用Freundlich或Langmuir方程描述.     

纳米氧化铈对汽油发动机尾气污染物排放的影响

通过非水微乳液法制备了纳米氧化铈，并将之添加到90^#汽油中，研究了纳米氧化铈对汽油动力性能、尾气污染物CO、HC、PM、NOx排放的影响。结果表明：非水微乳液法制备的纳米氧化铈粒径在30～50nm之间，粒径分布较窄；添加浓度为100mg／L时，不会对汽油的动力性能产生明显影响，但可以明显降低90。汽油尾气中的CO、HC、PM、NOx排放。其中，800r／min的正常怠速下可以降低CO排放19．39％、HE排放19．92％、NOx排放51．19％、PM排放25％；在2000r／min的高怠速下可降低CO排放16．17％、NOx排放46．92％、PM排放16．67％。     

PEMFC制氢技术现状

本文系统地论述了目前国内外离子交换膜燃料电池（ＰＥＭＦＣ）制氢技术现状,较全面的分析了ＰＥＭＦＣ汽油重整制氢技术存在的问题,并对开发适合于ＰＥＭＦＣ汽油重整制氢工作提出了几点建议。     

加油站油气排放治理技术

分析了国内外加油站的油气排放治理现状，指出对我国加油站的油气排放进行全面治理已迫在眉睫。针对我国加油站油气排放的特点并在现有技术基础上，提出了“冷凝+吸附”油气处理集成技术，并借助Aspen模拟软件及实验对此技术进行了研究，结果认为该技术回收率高达99.2％，油气尾气浓度可控制在11.2 g/m³。该技术原理简单，成本低，可为提高加油站的本质安全、环境保护及节能降耗提供有力的技术支撑。     

在用轻型汽油车排放随行驶里程劣化规律分析

基于佛山市3.5万条简易稳态工况(ASM)下的尾气排放检测数据,通过分类统计和线性拟合方法分析在用轻型汽油车的污染物排放浓度随行驶里程的劣化规律。分析结果表明,该地区轻型汽油车污染物排放浓度主要分布于低值区间,超过85%的样本数据低于最低排放限值;车辆排放劣化特征随行驶里程呈规律性变化,行驶里程在0~5万km时污染物排放缓慢增长,5万~16万km时呈快速线性增长,16万km后震荡缓慢增长;行驶里程在16万km前,不同车型的排放特征存在一定差异,其中轻型货车和轻型客车的排放浓度高、劣化速度快;CO、HC、NO随行驶里程的劣化规律可用线性增长模型表示。本研究结论可为预测机动车污染变化趋势、完善在用车检查/维护制度、高排放车辆识别和淘汰等方面提供理论支持。     

甲基叔丁基醚(MTBE)对环境的污染及其对我国汽油生产的影响

本文简要介绍了汽油添加剂MTBE对环境的污染及减少MTBE污染机理研究的进展 ,同时介绍了对我国汽油生产的影响     

乙醇汽油对减少机动车污染排放的机理研究与分析

以93#国Ⅲ乙醇汽油(E10)、93#国Ⅲ普通汽油和93#国Ⅳ普通汽油为实验对象,对GB18352.3-2005中要求限定的CO、HC和NOx,以及颗粒物(PM)和CO2等主要污染物的排放进行了测量和对比研究,并对CO、HC、PM、NOx、CO2和苯系物等污染物的形成原因和减排机理进行了分析.和93#国Ⅲ普通汽油相比,93 #国Ⅲ乙醇汽油(E10)排放的尾气中:CO降低了19.7％,HC降低了16.4％;和93#国Ⅳ普通汽油相比,93#国Ⅲ乙醇汽油(E10)排放的尾气中:CO降低了1.8％,HC降低了12.9％,CO2降低了2.4％.研究表明,乙醇汽油在减少CO、HC、NOx、颗粒物和苯系物等有毒物质排放方面具有显著功效,使用乙醇汽油可以减少环境污染物的排放,显著改善空气质量.     

Methyl tert-butyl ether (MTBE) in urban and rural precipitation in Germany

The use of the oxygenate methyl tert-butyl ether (MTBE) in gasoline has led to detectable concentrations in urban and rural air up to 160 ppbV. Results from MTBE measurement in precipitation have not been reported so far. In the present study, 120 samples of precipitation collected at 17 sampling locations all over Germany have been analyzed for their MTBE content. Analysis is performed by a combination of headspace-solid-phase microextraction (HS-SPME) and gas chromatography/mass spectrometry (GC-MS). A 75 μm poly(dimethylsiloxane)/Carboxene fiber and a cryostat is used for SPME. The detection limit is 10 ng/l. In precipitation samples, MTBE was detected in wintertimes only with a maximum concentration of 85 ng/l. Measurement at Frankfurt/M City from 6 September 2000 to 12 March 2001 provided for 49% of the data concentrations in the range of 30–85 ng/l (n=17). Sampling in winter 2000/2001 at several German cities and rural locations showed that MTBE is more often detectable in urban (86%, n=78) than in rural (18%, n=42) precipitation. By comparing the results with corresponding temperatures and amounts of precipitation it can be concluded that the detection of MTBE in urban precipitation is observed at ambient temperatures lower than about 10–15°C. Moreover, the first precipitation after a dry period accumulates more MTBE than precipitation during or at the end of a wet period (wash-out effect). Highest concentrations occurred in snow samples. Corresponding mean air equilibrium concentrations of 0.04 ppbV (urban samples) and 0.01 ppbV (rural samples) are calculated. This is about one magnitude lower than year round and summertime measurements in the US and in Switzerland. Urban runoff (n=12) and corresponding precipitation sampling indicate that urban runoff might be composed of about 20% MTBE that is already transported by air and precipitation, whereas about 80% may be attributed to direct uptake of vehicle emissions and leakage near the road during precipitation.     

Partitioning of aromatic and oxygenated constituents into water from regular and ethanol-blended gasolines

Variability in gasoline-water partitioning of major aromatic constituents (benzene, toluene, ethylbenzene, and xylenes (BTEX)) and methyl tert-butyl ether (MTBE) were examined for regular and ethanol-blended gasolines. By use of a two-phase liquid-liquid equilibrium model, the distribution of nonpolar solutes between fuel phase and water was related to principles of equilibrium. The models derived using Raoult's law convention for activity coefficients and liquid solubility is presented. The observed inverse log-log linear dependence of K_fw values on aqueous solubility, could be well predicted by assuming gasoline to be an ideal solvent mixture. Oxygenated additives (i.e., ethanol and MTBE), in the low percent range (below 5%), were shown to have minimal or negligible cosolvent effects on hydrocarbon partitioning. In the case of high fuel-to-water ratio (e.g., 1:1) or near contaminant source zone, the cosolvent effect of oxygenated gasoline with high content of ethanol (e.g., E85) will be environmentally significant.     

Fingerprinting of Gasoline and Coal Tar NAPL Volatile Hydrocarbons Dissolved in Groundwater

Accidental spills and chronic leaks of fuel oil or other hydrocarbon material (e.g., coal tar) often result in subsurface accumulation of nonaqueous phase liquid (NAPL), which can be a subsequent source of contamination in groundwater. Linking hydrocarbons in groundwater to a source NAPL has been difficult when using standard target analytes (e.g., BTEX) because of differences in partitioning properties of the analytes between the source NAPL and groundwater. Because aqueous solubility is predicted to be the controlling influence in the partitioning of hydrocarbons from NAPL to groundwater, a solubility-based approach to matching dissolved hydrocarbons in groundwater to their source NAPL has been developed and validated for two sites with commonly encountered types of NAPL contamination. Specifically, a gasoline LNAPL and a coal tar DNAPL from two separate sites (West Virginia and California) and groundwater interfaced with these NAPLs were analyzed for approximately 50 gasoline-range hydrocarbons consisting of paraffin, isoparaffin, (mono-) aromatic, naphthene, and olefin compounds (PIANO). Solubility characteristics of selected alkyl aromatic hydrocarbons from the PIANO analysis were used to identify a set of diagnostic hydrocarbons, expressed as hydrocarbon ratios, which were found to be useful in distinguishing the source(s) of hydrocarbons in groundwater. At the West Virginia site, the diagnostic ratios in a downgradient groundwater sample were similar to those of a gasoline NAPL at that site, indicating the source of hydrocarbons to the groundwater was the upgradient gasoline NAPL. The diagnostic ratios of the groundwater in contact with the gasoline NAPL and the remote groundwater were also similar, providing evidence that the diagnostic ratios were retained during transport in the aquifer. At the California site, diagnostic ratios in a cross-gradient groundwater sample differed from those of the coal tar NAPL at that site, indicating that the remote groundwater hydrocarbons did not originate from the coal tar contamination. Environmental factors such as selective degradation of specific isomers and various geological conditions (e.g., soil mineralogy, and organic content) may confound the application of this solubility-based fingerprinting approach. Thus, it is recommended that multiple diagnostic pairs be simultaneously evaluated when considering this fingerprinting approach for specific sites and product types.     

水碳比变化对汽油氧化重整制氢影响的研究

本文用正辛烷代替汽油从理论和实验两方面研究了水碳比变化对汽油氧化重整制氢反应的影响。理论研究表明 ,在绝热反应条件下 ,对应确定的反应温度存在一个最佳的氧油比及水碳比 ;实验研究表明 ,在非绝热反应体系中 ,在一定的氧油比及反应温度条件下 ,反应体系的转化率及生成氢的选择性均随水碳比的增加而增加 ,为实现燃料电池汽油制氢自热反应 ,反应体系应在一定水碳比条件下进行 ,实验条件下最佳的水碳比范围是 1.5— 2 .5之间。