沸石负载型TiO2处理炼化反渗透浓缩水的研究

利用沸石负载型二氧化钛对炼化企业的反渗透浓缩水进行研究,考察了催化剂对浓缩水的处理效果及影响降解的因素。由实验结果可知:沸石负载型二氧化钛对反渗透浓缩水TOC降解率达到67.4%,降解浓缩水的最佳条件为:pH值为4～6,温度30～40℃,光照时间2.5h,催化剂投加量为1.5g/L。实验为浓缩水处理技术的发展提供了新的依据。     

我国沸石去除水中氨氮的现状研究

沸石是一种天然、有效、价廉的环境友好型材料,其对氨氮具有很强的选择吸附性。本文就国内在沸石去除水中氨氮的机理、影响因素、沸石的改性及沸石研究的发展等方面进行广泛探讨。阐述了国内沸石去除水中氨氮的应用现状和进展,并指出沸石的推广要依赖于沸石改性和与其他工艺的联用技术开发。     

水处理膜技术的发展现状及趋势

论述了国内外水处理膜技术发展概况及国内水处理膜技术的应用现状,分析了水处理膜技术应用中存在的问题,提出了水处理膜技术发展的趋势,膜技术的创新发展主要包括膜性能的提高、膜材质和制造工艺的发展及膜应用技术的提高。     

平板陶瓷膜在污水处理中的应用

介绍了陶瓷膜在我国的发展历程及应用情况,分析了陶瓷膜在水处理应用中的优势,重点介绍了平板陶瓷膜在污水处理中的基本应用情况及国内首座万吨级纳米陶瓷膜应用的工程案例,展望了平板陶瓷膜水处理应用的发展。     

利用沸石材料吸附/降解处理水体中有机污染物的研究进展

天然及人工沸石因其特殊的多孔结构及化学组成,具有吸附及催化降解水体中有机污染物的潜在能力。综述了不同类型天然及人工沸石用于吸附处理以及催化强氧化剂降解各种有机污染物的研究进展。基于其丰富的储量、低廉的成本,特别是有效的治污效果,天然及人工沸石在环境保护领域的应用前景广阔。     

高级氧化技术在油田水处理中的应用

概述了高级氧化技术的基本原理和发展历程,介绍了臭氧氧化、二氧化氯氧化及光催化氧化等典型的高级氧化技术及其在水处理中的应用进展情况。结合目前油田水处理中出现的新问题,如硫酸盐还原菌含量高、有机物浓度高、微生物易于繁殖以及结垢严重等现象,对高级氧化技术在油田水处理中的应用前景进行了论述。同时提出应进一步加强对油田采出污水杀菌、油田水的灭藻和除泥、油田地面水体油污染控制等方面的研究。     

绿色水处理技术的应用与发展

采用绿色水处理技术是实现水资源可持续发展、环境保护和生态安全的重要措施。文章列举了膜分离、绿色氧化、绿色絮凝以及超声波、微波、电磁场等环保水处理技术,以及在国内外的研究应用现状探讨了绿色水处理技术的发展趋势。     

分子量分级法在水处理工艺表征中的应用

同等分子量和物理化学性质相近的分子在同一水处理工艺中具有类似的去除效果,因此,分子量分级法被广泛应用于水处理工艺表征及工艺评价研究中。目前常用的分子量分级方法有超滤膜法、凝胶色谱法(GPC)以及液相色谱-有机碳测定仪(LC-OCD)法。超滤膜法因为设备简单、操作方便被广泛应用,并与树脂法联用来分离不同分子量不同物化性质的有机分子;GPC法较超滤膜法,可实现更为精细的分子量区间确认;LC-OCD凭借优良的分离定量性能及高灵敏度,近年来在国际上被广泛应用于多种水处理工艺的机理研究。针对不同检测手段的特点,总结了分子量分级法在水处理工艺诊断中的应用现状并得到相关科学结论,以此来指导水处理的工艺选择和工艺改进。     

粉煤灰改性及其在水处理中的应用

对粉煤灰的基本性质和组成及其在水处理应用中的作用机理进行了阐述,对粉煤灰的改性方法及其改性后的作用机理进行了研究,提出了改性粉煤灰在水处理中存在的问题。     

沸石人工湿地填料对氨氮的去除效果

选取沸石作为人工湿地填料,对沸石吸附实验的水力负荷、污染负荷、运行方式分别进行研究,探讨沸石对氨氮的去除效果及影响因素。结果表明,沸石对氨氮有较好的处理效果,相同条件下远优于砂石。水力负荷会影响沸石对氨氮的去除效果,低水力负荷下的处理效果和稳定性均较好。沸石在不同氨氮浓度下的去除效果差别不大。运行方式对氨氮的去除有一定影响,6 h间歇周期运行时,沸石填料对氨氮的去除效果好于其他间歇周期。     

MAP法与沸石吸附组合工艺的脱氮除磷实验研究

以高浓度氮磷模拟废水为处理对象,通过静态实验研究了MAP法（磷酸铵镁法）与沸石吸附组合工艺的脱氮除磷效果。以MAP法除磷脱氮后的出水作为沸石吸附过程的进水,最终出水的氮、磷去除率可达86．69％和99．9％,且在MAP反应过程中采取较高的pH值和Mg^2＋浓度有利于后期沸石对氮、磷的吸附去除。     

改性沸石对水体中硝酸盐的吸附机理及其残渣的资源化利用

利用HDTMA改性沸石制成吸附剂,研究对水体中硝酸盐的吸附能力和机理及吸附剂残渣的资源化应用前景。结果表明:HDTMA改性沸石可增强其对硝酸盐的吸附能力。通过红外光谱和差热分析它的吸附机理,表明:改性沸石HZ4吸附有十六烷基三甲基溴化铵(HDTMA)分子;吸附剂残渣NHZ4吸附有十六烷基三甲基溴化铵(HDTMA)分子和硝酸盐。盆栽实验结果表明:吸附剂残渣NHZ4能提高玉米生物量,最大增幅为30.4%。     

Pyrolysis of cellulose under catalysis of SAPO-34, ZSM-5, and Y zeolite via the Py-GC/MS method

Bio-oil from pyrolysis of biomass is an important renewable source for liquid fuel and/or for chemicals. However, the application of bio-oil was severely restricted due to its high viscosity, acidity, and low heating value. Hence, it is necessary to upgrade the bio-oil for deoxygenation or for chemicals by catalytic reactions. In this paper, the catalytic behaviors of SAPO-34, ZSM-5, and Y zeolite on pyrolysis of cellulose were investigated via pyrolyzer combined with gas chromatography and mass spectrometer (Py-GC/MS) method in Py-mode. The results showed that ZSM-5 and Y zeolite could promote the conversions of oxygen-containing components to gases, water, aromatics, and phenols. Comparatively, more gas and water were generated under the catalysis of Y zeolite at lower temperatures, while at temperatures above 700°C, the effect of ZSM-5 became more distinct; aromatics were more generated under the catalysis of ZSM-5, while Y zeolite exerted a more distinct role in promoting the formation of phenols. The effect of SAPO-34 caused more water and furfural derivatives, less aromatics and phenols, and exerted a weak influence on gases.     

Adsorption of carbon dioxide on alkali-modified zeolite 13X adsorbents

Shaped zeolite 13X adsorbent with kaolin as binder was hydrothermally modified in sodium hydroxide solution to improve its adsorption performance. The characterization of the product by XRD, N₂ adsorption–desorption and water vapour adsorption displayed that kaolin component in zeolite adsorbent can be converted into zeolite during the alkali treatment, resulting in the modified adsorbent consisting entirely of effectual adsorption composition. Compared with the unmodified adsorbent, the modified adsorbent exhibited higher adsorption capacity and uptake rate for carbon dioxide, because of the increase of effective adsorption surface and the decrease of diffusion resistance owing to conversion of kaolin binder into zeolite. The model parameters of isotherms and the isosteric heats calculated by the Clausius–Clapeyron equation for CO₂ adsorption showed the stronger interaction of adsorbate–adsorbent and the higher degree of heterogeneity of adsorption centers in modified than unmodified adsorbents.     

陶粒-沸石-活性炭组合填料生物滤池的研究

采用陶粒、沸石、活性炭填料合理组合作为曝气生物滤池的填料对高校生活污水进行处理。研究了组合填料生物滤池生物膜的培养,不同水力负荷、容积负荷和气水比对污水处理效率的影响,以及该生物滤池对生活污水的处理效果。结果表明,采用组合填料生物滤池,接种挂膜培养周期为25d,在水力负荷为2．5m3／（m2·h）,气水比3．5：1,组合填料生物滤池出水COD、BOD5、SS、NH3-N和色度平均值达到《城市污水再生利用城市杂用水水质》GB／T18920—2002水质要求。     

生物滤池强化方法对水源水中乐果去除效果的试验研究

以乐果微污染水源水为研究对象,对比研究了KMnO4与O3作为预氧化剂,石英砂、沸石与活性炭作为滤料的生物滤池对饮用水水源中乐果残留物的去除效果。实验结果表明,以石英砂、沸石和活性炭作为滤料,经高锰酸钾或臭氧预氧化处理后,乐果去除率较好,特别是沸石和活性炭的去除率达到了90%以上。臭氧处理效果比高锰酸钾好,处理率提高了10%以内。从去除率、经济性和易操作性方面考虑,高锰酸钾和沸石联用更适合中国农村供水的实际情况。     

双滤料曝气生物滤池污水深度处理的研究

采用陶粒、沸石为滤料的曝气生物滤池对生物处理系统二级出水进行深度处理回用,研究了水力停留时间、气水体积比对污染物COD和NH3-N处理效果的影响。结果表明：水力停留时间为8 h,气水体积比为3∶1的工况下,处理效果较好。稳定运行后,出水COD、BOD5、SS、NH3-N、TP和色度平均值分别为15.6 mg/L、3.2 mg/L、8.5 mg/L、1.24 mg/L、0.40mg/L和8度,达到《城市污水再生利用—城市杂用水水质》（GB/T 18920-2002）标准,出水可用于道路清扫、绿化等。     

An experimental study on the influence of zeolite on changes of pH and alkalinity in anaerobic treatment of compost leachate

With the increase of urbanization, municipal solid waste has also increased. Therefore, the need for solid waste management is also increasing compared with earlier decades. Composting is a good option for the recycling of solid waste; however, it produces leachate, which requires proper treatment systems to prevent environmental degradation. Due to high chemical oxygen demand (COD) concentrations in compost leachate, anaerobic treatment is the best option for handling the effluent, and an anaerobic baffled reactor (ABR) is one such anaerobic reactor that can be used for its treatment. Because of high ammonia and heavy metal concentrations, as well as the possibility of sludge washout in ABRs, it is important to use proper media, such as zeolite, which can reduce inhibition effects and sludge washout from the reactor. Anaerobic treatment, especially during the methanogenesis phase, is sensitive, and pH and alkalinity are parameters that influence the treatment. Therefore, adjusting these parameters within a normal range is very important to the proper functioning of anaerobic systems. In this study, a pilot‐scale ABR was used, and the last 4 of the 8 ABR compartments were filled with zeolite. The bioreactor was operated at hydraulic retention times (HRT) of 3, 4, and 5 days, with zeolite filling ratios of 10%, 20%, and 30%, and influent COD concentrations of 10,000, 20,000, and 30,000 milligrams per liter (mg/L). In this study, pH value was 6.43 ± 0.1, 6.96 ± 0.3, and 6.96 ± 0.25 at filling ratios of 10%, 20%, and 30%, respectively. According to the results, in all filling ratios, no significant changes were observed in the pH value when the organic loading rate increased and its amount was within a constant range. Influent alkalinity was equal to 2015 ± 510, 2884 ± 505, and 4154 ± 233 milligrams of calcium carbonate per liter (mg CaCO₃/L) at influent COD concentrations of 10,000, 20,000, and 30,000 mg/L, respectively, and in effluent, they were 2536 ± 336, 3379 ± 639, and 4377 ± 325 mg CaCO₃/L, respectively. The amount of alkalinity in the effluent increased compared with the alkalinity in the influent. The results show that the amount of alkalinity in the influent and effluent was similar, and the alkalinity enhancement was lower when the filling ratio was increased from 10% to 20%, and 20% to 30%. Comparisons of the results from zeolite with and without biofilm showed that, in cases of zeolite with biofilm, the amounts of silica and oxygen decreased and the amount of carbon increased, and it showed the formation of biofilm on the surface of zeolite. In addition, the absence of sodium in the zeolite with the biofilm indicated that sodium was exchanged with ammonium ions. According to the results, zeolite can be used in anaerobic reactors as a medium, and it also reduces fluctuations in pH and alkalinity at different organic loading rates, providing a normal range for anaerobic treatment.