在线监测氨氮浓度的电导测量方法研究

建立了适用于氨氮在线监测的干法蒸馏-电导法和湿法蒸馏-电导法。该方法是通入一定流量的气量于含氨试样中,全沸腾加热,蒸发出的氨和水蒸气一起经冷凝器后,进入酸吸收液中。酸吸收液的电导率随氨氮蒸馏液的吸收发生变化,其变化的值和样品中氨氮的浓度呈一定的比例关系。研制出的氨氮在线监测仪结构简单,运行稳定可靠,测量结果准确。     

膜界面探测器在工业污染场地调查中的应用

膜界面探测器是一项采用直接推进技术,可实时提供场地地下挥发性有机物近乎连续分布信息的直接感测工具。以某历史上从事有机氯农药生产的废弃工业场地为例,运用该技术,配置土壤电导率传感器、电子捕获检测器以及氢火焰离子化检测器,对该场地中潜在污染区域进行快速筛选调查,初步确定了土壤和地下水中挥发性有机物污染的热点区域及其三维分布和地层信息,为后续进一步调查方案优化、场地概念模型建立及后续修复方案设计等提供了重要的信息。     

Effects of different Ca2+ behavior patterns in the electric field on membrane fouling formation and removal of trace organic compounds

The effects of Ca²⁺on membrane fouling and trace organic compounds(TrOCs) removal in an electric field-assisted microfiltration system were investigated in the presence of Na+alone for comparison. In the electric field, negatively charged bovine serum albumin(BSA)migrated towards the anode far away from the membrane surface, resulting in a 42.9% transmembrane pressure(TMP) reduction in the presence of Na+at 1.5 V. In contrast, because of the stronger charge shielding of Ca²⁺     

Investigation of the role of biopolymer clusters in MBR membrane fouling using flash freezing and environmental scanning electron microscopy

The technique that employs flash freezing and environmental scanning electron microscopy (ESEM) was utilised for detailed investigation of the fouling materials in a membrane bioreactor (MBR). The method involves the flash freezing of a wet sample in liquid nitrogen for 10 s to preserve its structure for direct ESEM observation with a high image resolution. ESEM images show that the sludge cake formed by simple filtration of the MBR bulk sludge has a highly porous, sponge-like structure with a fairly low resistance. However, the fouling layer attached to the membrane surface contains a thin gel layer under the main body of the sponge-like sludge cake, which is similar to that formed by filtration of a dispersion of biopolymer clusters (BPCs). It is apparent that BPCs tend to accumulate on the membrane surface, and the gel layer is largely responsible for the high filtration resistance of the cake layer on the fouled membranes.     

减压膜蒸馏法处理石煤提钒废水

利用减压膜蒸馏设备处理石煤提钒废水,分别比较了废水经预处理前后,料液温度、流量、渗透侧真空度等操作条件对膜通量和截留率的影响。测定了不同浓缩倍数情况下膜通量的变化。实验表明,进料温度升高会使膜通量增加,温度为65℃时,热效率最高为70．1％。提高料液流量或真空度都会使膜通量增加。废水经VMD处理产出的淡水电导率均在10μS／cm以下,脱盐率可达99．98％以上。在温度为70％、流量为60L／h、真空度为0．095MPa时,石煤提钒废水经预处理后的废水膜通量为11．359kg／（m^2·h）,浓缩10倍时,膜通量仍有3．185kg／（m^2·h）。     

真空膜蒸馏和膜吸收及其集成工艺处理高氨氮废水

采用PP中空纤维膜组件,对VMD(真空膜蒸馏)和MA(膜吸收)脱氨过程进行了研究。考察了料液p H值(9.0~11.0)、料液进口温度(20~50℃)对脱氨效率的影响。研究结果表明,VMD和MA脱除率分别达85%和99%以上。料液p H和料液进口温度对VMD脱氨效果的影响较大,提高料液p H和进口温度可以明显提高VMD的脱氨效率;料液p H对MA的脱氨效率影响较为显著。对2种膜工艺进行了技术集成,利用该集成工艺可达到99.96%以上的氨去除率,出水可达标排放,并且可以有效防止硫酸铵的二次污染。     

Removal of arsenic from contaminated groundwater by solar-driven membrane distillation

Experimental investigations were carried out on removal of arsenic from contaminated groundwater by employing a new flat-sheet cross flow membrane module fitted with a hydrophobic polyvinylidenefluoride (PVDF) microfiltration membrane. The new design of the solar-driven membrane module in direct contact membrane distillation (DCMD) configuration successfully produced almost 100 per cent arsenic-free water from contaminated groundwater in a largely fouling-free operation while permitting high fluxes under reduced temperature polarization. For a feed flow rate of 0.120 m³/h, the 0.13 μm PVDF membrane yielded a high flux of 74 kg/(m² h) at a feed water temperature of 40 °C and, 95 kg/m² h at a feed water temperature of 60 °C. The encouraging results show that the design could be effectively exploited in the vast arsenic-affected rural areas of South-East Asian countries blessed with abundant sunlight particularly during the critical dry season.     

浸没式MBR工艺在工程化应用中膜污染的三阶段特征研究

以国内某浸没式MBR再生水工程为研究对象,在次临界通量及恒抽吸流量运行条件下,系统跨膜压差表现为早期短暂升高、中期平稳上升及后期快速升高的三阶段特征。扫描电子显微镜(SEM)观察证明MBR系统在三阶段的膜污染层具有不同的水力学结构。结合各阶段膜污染的理论分析,将临界跨膜压差值(TMP)作为膜系统体外维护清洗的控制点,实现膜系统的长期稳定运行。     

复合式膜生物反应器处理城市生活污水特性的研究

HSMBR系统表现了对于COD高且稳定的去除效果。对于TN、TP,由于不排泥,污泥浓度的升高,并且填料内部的生物膜不断形成,以及在填料内部的污泥受曝气的扰动小,而变的较为密实,反应器内形成好氧、缺氧两种微环境并存,有利于系统对于TN、TP去除率的提高。     

Effect of non-solvent additives on the morphology, pore structure, and direct contact membrane distillation performance of PVDF-CTFE hydrophobic membranes

Four common types of additives for polymer membrane preparation including organic macromolecule and micromolecule additives, inorganic salts and acids, and the strong non-solvent H2 O were used to prepare poly(vinylidene fluoride-co-chlorotrifluoroethylene)(PVDF-CTFE) hydrophobic flat-sheet membranes. Membrane properties including morphology, porosity, hydrophobicity, pore size and pore distribution were investigated, and the permeability was evaluated via direct contact membrane distillation(DCMD) of 3.5 g/L Na Cl solution in a DCMD configuration. Both inorganic and organic micromolecule additives were found to slightly influence membrane hydrophobicity. Polyethylene glycol(PEG),organic acids, Li Cl, Mg Cl2, and Li Cl/H2 O mixtures were proved to be effective additives to PVDF-CTFE membranes due to their pore-controlling effects and the capacity to improve the properties and performance of the resultant membranes. The occurrence of a pre-gelation process showed that when organic and inorganic micromolecules were added to PVDF-CTFE solution, the resultant membranes presented a high interconnectivity structure. The membrane prepared with dibutyl phthalate(DBP) showed a nonporous surface and symmetrical cross-section. When H2 O and Li Cl/H2 O mixtures were also used as additives, they were beneficial for solid–liquid demixing, especially when Li Cl/H2 O mixed additives were used. The membrane prepared with 5% Li Cl + 2% H2 O achieved a flux of24.53 kg/(m2·hr) with 99.98% salt rejection. This study is expected to offer a reference not only for PVDF-CTFE membrane preparation but also for other polymer membranes.