Review: recent advances in biogas purifying technologies

Biomethane production through biogas upgrading is a promising renewable energy for some industries which could be part of the equilibrium needed with fossil fuels consumption to achieve a sustainable society. This paper presents a comprehensive list of biogas upgrading technologies focused on carbon dioxide removal as well as recent advances reported by researcher with wide expertise in this topic. Additionally, an extensive costs–performance comparison among the technologies studied is discussed. Among the different alternatives, chemical scrubbing stood out to achieve high biomethane purities while cryogenic technologies proved to be effective against methane losses. Regarding the different costs, water scrubbing and membrane separation seem to be the most affordable techniques.     

可张孔曝气器曝气能耗试验研究

通过试验研究，总结出可张孔曝气阻力损失的影响因素，以优化产品的结构设计参数，降低产品在工程应用中的能耗，获取更好的经济效益。     

臭氧耦合陶瓷膜过滤对膜性能及出水消毒副产物的影响

利用臭氧（O₃）-陶瓷膜过滤（CMF）处理常规工艺出水,研究了不同O₃-CMF耦合方式对膜性能和消毒副产物（DBPs）的影响.结果表明,与单独CMF相比,异位O₃-CMF和原位O₃-CMF均可以有效缓解膜污染,原位O₃-CMF控制效果最佳.异位O₃-CMF对进水（常规工艺出水） DOC去除率（26.25%）略高于原位O₃-CMF（22.31%）,但是其SUVA去除率（83.91%）明显低于原位O₃-CMF（93.10%）.羟基自由基（·OH）生成特征表明原位O₃-CMF可促进O₃产生更多的·OH.在O₃、·OH氧化和陶瓷膜截留协同作用下,异位O₃-CMF和原位O₃-CMF出水中总荧光响应强度和相对分子质量大于0.3×10³,有机物含量降低,进而使得出水中含碳消毒副产物（C-DBPs）生成量分别降低了21.86%和32.35%,含氮消毒副产物（N-DBPs）生成量分别降低了16.16%和19.13%.但O₃和·OH氧化后生成的小分子有机物因难以被CM截留导致其在出水中含量增加,进而增加了卤代酮（HKs）、水合氯醛（CH）和三卤硝基甲烷（THNMs）的产生.本研究对于不同O₃-CMF方式下O₃与CM的协同机制的探讨,改善膜性能和提升DBPs前体物的去除具有一定指导意义.     

Determination of organophosphorus pesticides and related compounds in water samples by membrane extraction and gas chromatography

A membrane extraction-gas chromatography method was developed fordetermination of organophosphorus pesticides and related compounds including methamidophos, DDVP, dimethoate, methyl parathion, parathion, thiophosphoric acid trimethyl ester, and thiophosphoramidic acid dimethyl ester in water samples. In thismethod, surface-modified acetic cellulose membranes were used to extract the target analytes in water samples, the extracted analytes were back-extracted into a small amount of methanol, andgas chromatography with pulsed flame photometric detector (GC-PFPD) was used to determine the concentrations of targetanalytes in the extracts. The recoveries obtained for thetarget analytes spiked into the water samples ranged from 66to 94%. The method detection limit for each target analyte was 0.05 g L^-1. The method developed in this study had shown the advantages of being cheap, simple, fast, and reliable. It had been used successfully to determine the concentrations of target analytes in river water samples.     

Large pore size polyacrylonitrile membrane for ultrafiltration

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BOD微生物膜的再利用研究初探

对失去大部分活性的微生物膜进行再培养,以研究膜再利用的可能性。试验结果初部表明:在1/2MS培养基中加入一定量的植物激素,不仅可以使膜的电位值(I0)显著升高,且活性强,稳定性好,可使膜重复利用。     

潮滩生态特征及开发利用模式——以江苏大丰潮滩研究为例

根据自然地理、海洋动力、生物等特征!本文研究受大河作用的大丰潮滩地貌、沉积过程,讨论老黄河和长江对该潮滩发育的影响和潮滩生物群落空间分布及演变规律。本文评价了大丰潮滩开发利用现状,分析了它们的经济效益和环境效益,提出把目前受到强烈改造、过度利用的模式改变为顺应潮滩自然演变、有步骤合理开发利用潮滩的模式。     

江苏王港地区现代潮滩地貌发育特征

淤泥质潮滩是人类活动的强烈地带，江苏王港地区淤泥质潮滩宽广，由于人工引种大米草，滩涂围垦，大丰港的修筑，影响了王港地区原有潮滩发育的动力机制。王港地区生物分布和地貌特征具有明显的分带性。由于植被的促淤作用，王港地区潮滩南部垂向淤积速率较北部大；研究区内潮水沟的发育有两种类型。即泥滩带上的块体崩塌溯源侵蚀和零星分布的米草滩上的洞穴塌陷溯源侵蚀形成潮水沟；潮间带下部实测平均涨潮流流速小于平均落潮流流速，而涨潮平均含沙量大于落潮平均含沙量，潮间带下部潮水往复流及旋转流的作用在滩面上形成了双向波痕，陆地向海推进速度随着泥沙供给的减少以及滩面高程的降低而减慢。     

泉州湾滩涂沉积物对Cu（Ⅱ）的吸附实验

研究了Cu(Ⅱ)在泉州湾滩涂沉积物上的吸附行为。探讨了pH和温度对吸附作用的影响，测定了其吸附等温线。实验结果表明，常温下Cu(Ⅱ)在泉州湾滩涂沉积物上的吸附平衡时间约需3．5小时；吸附量随pH的升高先增大而后减少，pH=6．0左右时达最大；吸附量随温度的升高而增大；其吸附行为可以很好地用Langmuir型吸附等温线来描述。并在此基础上初步探讨了Cu(Ⅱ)在泉州湾滩涂沉积物上的吸附机理。     

Membrane fouling control by ultrasound in an anaerobic membrane bioreactor

In this study, ultrasound was used to control the membrane fouling online in an anaerobic membrane bioreactor (AMBR). Short-term running experiments were carried out under different operating conditions to explore feasible ultrasonic parameters. The experimental results indicated that when the crossflow velocity was more than 1.0 m/s, membrane fouling could be controlled effectively only by hydrodynamic methods without ultrasound. When ultrasound was applied, an ultrasonic power range of 60–150 W was suitable for the membrane fouling control in the experimental system. The experimental results showed that the membrane fouling was controlled so well that membrane filtration resistance (ΣR) could stay at 5 × 10¹¹ m⁻¹ for more than a week with the crossflow velocity of 0.75 m/s, which equaled the effect of crossflow velocity of more than 1.0 m/s without ultrasound. Translated from Techniques and Equipment for Environmental Pollution Control, 2006, 7(4): 25–29 [译自: 环境污染治理技术与设备]