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61.
荷电超滤膜对天然有机物去除及膜污染行为的影响 总被引:2,自引:1,他引:1
以Aldrich 腐殖酸溶液为水样,研究比较了溶液环境(pH值、离子强度和钙离子)对荷电改性再生纤维素超滤膜和传统中性未改性再生纤维素超滤膜过滤过程的影响.结果表明, ①pH值主要通过质子化作用影响荷电膜以及腐殖酸分子的荷电量,进而影响荷电超滤过程.溶液pH值从7.5下降到3.5时,荷电超滤膜对腐殖酸的截留率从92%减少到79%,超滤4 h时,膜通量下降从26%增加到36%.②离子强度的改变是通过影响腐殖酸分子的物化性质和静电屏蔽作用来影响超滤过程的.当溶液离子强度为0、 3和100 mmol/L时,初始截留率依次降低,分别为92%、 87%和48%,超滤4 h时,荷电超滤膜的通量下降依次增加,分别为26%、 35%和63%.③Ca2+浓度的影响,需要综合考虑静电屏蔽作用、Ca2+的架桥作用以及滤饼层的压实性等各方面的影响.④pH值、离子强度和钙离子对中性超滤膜过滤行为的影响趋势与荷电超滤膜相似,但其影响程度有着较大的差别.研究结果对荷电超滤膜技术在实际应用中选择合适环境条件提供了参考. 相似文献
62.
臭氧/混凝预处理工艺降低膜污染的研究 总被引:1,自引:0,他引:1
采用臭氧和混凝工艺分别处理黄浦江原水后进行MF膜过滤试验,考察2种预处理工艺对有机物的作用,进而考察其对MF膜过滤特性的影响.结果表明,2种预处理工艺都存在一个使膜污染下降率达到最大的最佳投药量.2种预处理工艺中,混凝降低膜污染的效果要好于臭氧,这主要与2种预处理工艺所去除的有机物性质有关.黄浦江水中有机物相对分子质量主要集中在3×103~5×103范围内,膜化学清洗液的分析表明造成膜污染的有机物相对分子质量主要集中在4.5×103附近,臭氧对相对分子质量在3×103附近的有机物去除效果较好,而混凝主要去除5×103附近的较大相对分子质量的有机物,因而混凝对这部分污染膜物质的去除效果要好于臭氧,从而有效降低了膜污染. 相似文献
63.
目的研究不锈钢-气氮板式热沉中,氮气压力、氮气入口流速以及热沉自身流道深度对热沉传热性能的影响。方法利用AnsysFluent软件,对板式热沉壁面温度分布情况以及进出口压力损失进行模拟仿真。结果提高氮气压力和氮气入口速度可以提升热沉的温度均匀性,但热沉进出口压力损失也会增大。对于气氮-板式热沉而言,流道深度的改变对热沉温度均匀性的影响不大,但流道深度较小时,进出口压力损失较大。结论建议在设计气氮-板式热沉时,流道深度选择在8~10 mm,外流程中氮气压力控制在0.3~0.4 MPa,氮气流速控制在20 m/s为宜。 相似文献
64.
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66.
印钞废水属高浓度难降解有机废水,对环境污染严重。鉴于现有处理工艺出水普遍不达标的情况,通过对比实验确定了改进方案:超滤浓缩液离心出水在进入接触氧化池前,增加新的处理单元(Fenton氧化-混凝)。Fenton氧化最佳条件:FeSO4.7H2O投加量14 g/L,H2O2的投加量34 mL/L,初始pH值6.0,氧化反应时间1.5h,温度18.8℃;混凝过程最佳条件:PAC投加量4 g/L,PAM(5‰)投加量10 mg/L,pH值7。新增单元对废水中COD去除率接近80%,可生化性提高1.6倍,色度降低36%。 相似文献
67.
Cleaning of hollow-fibre polyvinyl chloride (PVC) membrane with di erent chemical reagents after ultrafiltration of algal-rich
water was investigated. Among the tested cleaning reagents (NaOH, HCl, EDTA, and NaClO), 100 mg/L NaClO exhibited the best
performance (88.4% 1.1%) in removing the irreversible fouling resistance. This might be attributed to the fact that NaClO could
eliminate almost all the major foulants such as carbohydrate-like and protein-like materials on the membrane surface, as confirmed by
Fourier transform infrared spectroscopy analysis. However, negligible irreversible resistance (1.5% 1.0%) was obtained when the
membrane was cleaning by 500 mg/L NaOH for 1.0 hr, although the NaOH solution could also desorb a portion of the major foulants
from the fouled PVC membrane. Scanning electronic microscopy and atomic force microscopy analyses demonstrated that 500 mg/L
NaOH could change the structure of the residual foulants on the membrane, making them more tightly attached to the membrane
surface. This phenomenon might be responsible for the negligible membrane permeability restoration after NaOH cleaning. On the
other hand, the microscopic analyses reflected that NaClO could e ectively remove the foulants accumulated on the membrane surface. 相似文献
68.
69.
Catalytic bubble-free hydrogenation reduction of azo dye by porous membranes loaded with palladium (Pd) nanoparticles was studied for the first time. The effects of Pd loading, dye concentration and reuse repetitions of membranes were investigated. In reduction, the dye concentration decreased whereas the pH rose gradually. An optimal Pd loading was found. The catalytic membranes were able to be reused more than 3 times. 相似文献
70.
Fouling behavior along the length of membrane module was systematically investigated by performing simple modeling and lab-scale experiments of forward osmosis (FO) membrane process. The flux distribution model developed in this study showed a good agreement with experimental results, validating the robustness of the model. This model demonstrated, as expected, that the permeate flux decreased along the membrane channel due to decreasing osmotic pressure differential across the FO membrane. A series of fouling experiments were conducted under the draw and feed solutions at various recoveries simulated by the model. The simulated fouling experiments revealed that higher organic (alginate) fouling and thus more flux decline were observed at the last section of a membrane channel, as foulants in feed solution became more concentrated. Furthermore, the water flux in FO process declined more severely as the recovery increased due to more foulants transported to membrane surface with elevated solute concentrations at higher recovery, which created favorable solution environments for organic adsorption. The fouling reversibility also decreased at the last section of the membrane channel, suggesting that fouling distribution on FO membrane along the module should be carefully examined to improve overall cleaning efficiency. Lastly, it was found that such fouling distribution observed with co-current flow operation became less pronounced in counter- current flow operation of FO membrane process. 相似文献