共查询到20条相似文献,搜索用时 125 毫秒
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纳米二氧化钛改性聚醚砜超滤膜 总被引:1,自引:0,他引:1
采用液-固相转化法,以聚醚砜(PES)、聚乙烯吡咯烷酮(PVP)和N,N-二甲基乙酰胺(DMAc)为原料制备PES超滤膜,并添加纳米TiO_2制备改性PES超滤膜.纳米TiO_2可降低制膜液的黏度,提高膜的亲水性能和抗污染性能.在PES质量分数为18%、PVP质量分数为12%、TiO_2质量分数为5.3%、DMAc质量分数为64.7%的条件下制备的改性PES超滤膜性能最佳,在24 ℃、0.2 Mpa操作条件下,膜的纯水通量为80.31 mL/ (cm~2·h), 截留率达99.16%.改性PES超滤膜过滤出水水质达到GB/T18920-2002<城市污水再生利用城市杂用水水质>标准.清洗后,未改性PES超滤膜的膜通量恢复率为68.08%,改性PES超滤膜的膜通量恢复率为85.31%. 相似文献
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TiO2改性聚偏氟乙烯膜的性能研究 总被引:1,自引:0,他引:1
采用纳米TiO2水溶胶改性聚偏氟乙烯(PVDF)膜,并用改性膜过滤蛋白质溶液和乳化油废水,探讨了纳米TiO2水溶胶加入量对膜通量恢复率和清洗周期的影响.实验结果表明,当TiO2质量分数为0.10%时,改性膜PVDF-1的膜通量恢复率最高,过滤蛋白质溶液时膜通量恢复率达90%以上,过滤乳化油废水时膜通量恢复率达82%以上.与PVDF膜相比,改性膜的清洗周期均有不同程度的延长,PVDF-1改性膜过滤蛋白质溶液和乳化油废水时的清洗周期最长,分别达370 min和400 min.水滴与PVDF膜的接触角为93.,与PVDF-1改性膜的接触角为45.,说明改性膜的亲水性能已经明显提高. 相似文献
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采用臭氧氧化—曝气生物滤池( BAF)联合工艺处理低温高浓度苯酚模拟废水.应用Design - Expert 7.1设计系统对臭氧氧化高浓度苯酚模拟废水进行了参数优化.实验结果表明:在低温(5 ~ 10℃)、臭氧加入量为0.67 g/L、进水pH为9.85的条件下,臭氧氧化出水苯酚质量浓度为1 237.6 mg/L,苯酚去除率为38.12%;臭氧氧化后的废水经调节pH至7.00 ~8.00后进入BAF,经BAF处理后的出水苯酚质量浓度小于0.5 mg/L.该工艺操作简单,处理效果稳定,出水水质达到GB8978-1996《污水综合排放标准》. 相似文献
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采用自制聚丙烯中空纤维疏水膜,开展了内压式真空膜蒸馏处理某气田采出水的实验研究,考察了膜通量、脱盐率、产水电导率及产水水质等随运行时间的变化,针对实验后期出现的膜污染情况对膜蒸馏浓水除硬后进行二段膜蒸馏,再对出水进一步做催化臭氧氧化处理。实验结果表明:105 h后,废水中各离子浓度随着废水的浓缩而急剧升高,同时废水的高硬度造成膜堵塞,产生膜污染;除硬后去除了膜结垢污染,改善了膜疏水性能,膜通量恢复到初始膜通量的73%;膜蒸馏出水经催化臭氧氧化处理后,出水COD、TOC和ρ(NH4+-N)分别为49 mg/L、6.5 mg/L和11.0 mg/L,满足回用要求。 相似文献
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采用Fenton试剂氧化—活性炭吸附工艺处理炼油厂循环水排污水,考察了各种因素对处理效果的影响.通过实验得出最佳处理条件为:室温,H2O2加入量600 mg/L,m(H2O2):m(Fe2+)=4,水样pH5.0~5.5,Fenton试剂氧化反应时间1h,活性炭选择8~30目的无烟煤破碎炭,水样在吸附柱的停留时间约为30 min.当循环水排污水COD低于150 mg/L时,经该联合工艺处理后出水COD低于50 mg/L,达到GB8978-1996《污水综合排放标准》中的二级排放标准. 相似文献
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Advanced physico-chemical treatment experiences on young municipal landfill leachates 总被引:19,自引:0,他引:19
Ozturk I Altinbas M Koyuncu I Arikan O Gomec-Yangin C 《Waste management (New York, N.Y.)》2003,23(5):441-446
In this study, Membrane Filtration (UF+RO), Struvite (MAP) precipitation and ammonia stripping alternatives were studied on biologically pre-treated Landfill Leachate. The results indicated that the system including the Upflow Anaerobic Sludge Blanket Reactor (UASBR) and Membrane Reactors (UF+RO) has been offered as an appropriate treatment alternative for young landfill leachates. This system provided high removals of COD, colour and conductivity (>98-99%). For ammonia removal, struvite precipitation was applied at the stoichiometric ratio (Mg:NH4:PO4=1:1:1) to anaerobically pre-treated raw landfill leachate effluent having an influent ammonium concentration of 2240 mg/l. Maximum ammonium nitrogen removal was observed as 85% at pH of 9.2. In ammonia stripping following 2 h of aeration, the removal was 72% at pH=12 while the removals were around 20% at pH=10 and pH=11. When membrane reactor, and struvite precipitation or ammonia stripping was applied to anaerobically pre-treated effluents, the results indicated that each system could be used as an appropriate post-treatment option for young landfill leachates. In economic aspect, ammonia stripping was found as the cheapest alternative with high ammonium removal. However, when both high COD and ammonium removals were to be achieved membrane technology such as UF+RO (SW) could be considered as the most appropriate system due to the fact that COD removal could be obtained very low by ammonia stripping. 相似文献
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Product concentrate can be recovered from rinsing waters [cleaning in place (CIP)] of surfactant and detergent batch production processes by using ultrafiltration and nanofiltration membranes. The problem in designing a separation process for the rinsing water is that the different compositions of the CIP-batches result in different treatment characteristics. The product formulations considered in this study are based on anionic and non-ionic surfactants. Detergents additionally contain salts, dyes, perfumes and solvents. Product solution enrichment by means of ultrafiltration membranes was investigated. Flux behaviour and selectivity are modelled on the basis of the experimental results as a basis for economic optimisation of the recovery process. The model is validated with the experimental data. The simulation model is used to calculate optimal design and operation parameters for a multi-stage UF concentration plant. An optimal number of feed-and-bleed-stages can be found under economic constraints. For water purification, a nanofiltration step has to be implemented for some of the surfactant CIP-batches. Depending on the separation characteristics, the batches are treated with a single (UF) or two-step membrane process (NF/ UF). 相似文献
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分别采用石灰乳化学沉淀法和低温结晶法去除烟气脱硫溶液中的SO42-。实验结果表明:在室温、CaO溶液质量分数25%的条件下,石灰乳化学沉淀法对SO42-的去除率仅为59.51%,且向溶液中引入了Ca2+,产生的硫酸钙固体废物难以再生利用;采用低温结晶法处理烟气脱硫溶液,在结晶温度7 ℃、结晶时间3 h、NaOH加入量34.8 g/L的条件下,SO42-的去除率为82.04%、滤液中的ρ(Na+)为3.88 g/L。在现场工业应用试验中,采用低温结晶法去除烟气脱硫溶液中的SO42-,平均SO42-的去除率可达70.00%以上,滤液中的ρ(Na+)小于15.00 g/L。该法可有效抑制烟气脱硫溶液中SO42-含量的增加。 相似文献
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Chang Liu Jianlin Luo Xiaona Li Qiang Gao Jianzhang Li 《Journal of Polymers and the Environment》2018,26(1):158-165
The effects of three compounded curing agents on the properties and performance of the urea-formaldehyde (UF) resin were investigated in this study. The compounded curing agents were prepared by mixing ammonium chloride with hexamethylenetetramine, citric acid, and oxalic acid respectively at a ratio of 1:1, named N-H, N–CA, and N–OA, respectively. The curing process, crystallinity, and physical properties were measured, and the three-ply plywood was fabricated to measure its prepress strength, wet shear strength, and formaldehyde emission. Results showed that the compounded curing agents N–CA and N–OA enhanced the initial viscosity, crosslinking density and thermal stability of UF resin. Additionally, the prepress strength of the plywood bonded by UF resin with N–CA and N–OA increased by 82 and 111% respectively compared to the UF resin with NH4Cl, and the wet shear strength increased by 14 and 16%, the formaldehyde emission decreased by 19 and 42% respectively. However, owing to the short pot-life of these curing agent limited their storage time, the curing agents N–CA and N–OA should be applied to fabricate plywood in winter for obtaining a better bond strength and a lower formaldehyde emission. While the UF resin with N–HT showed a suitable pot-life, so it could be applied to fabricate plywood in summer for long time storage and avoiding procuring problem. 相似文献
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酯化废水铁还原预处理的研究 总被引:19,自引:2,他引:17
用铁还原-中和-混凝沉淀法进行酯化废水预处理试验,原废水不稀释,铁还原处理在曝气条件下运行,还原时间为7 ̄8h,处理过程中的耗铁量为每升废水120mg左右,全过程COD去除率可达30%以上,BOD5去除率可达40%以上,色度降低50%。 相似文献
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Loukas Athanasios Vasiliades Lampros Dalezios Nicolas R. 《Water, Air, & Soil Pollution: Focus》2004,4(4-5):331-347
The modification of the flood response due to future climate change is presented for the Illecillewaet watershed of British Columbia, Canada. The Canadian Centre for Climate Modeling Analysis General Circulation Model (CGCMa1) was used for the assessment of changes of precipitation and temperature due to climate change. The runoff was simulated using the UBC watershed model and considering, also, changes on the spatial distribution of precipitation with elevation, cloud cover, glaciers, vegetation distribution, vegetation biomass production, and plant physiology. The results show that the future climate would be wetter and warmer than the present climate affecting the type, the magnitude and the temporal distribution of floods as well as the frequency of flood peaks. The above changes in the flood response of the study watershed could be explained by the change of the form of precipitation from snowfall to rainfall, the consequent decrease of the snowpack, and the initiation of the snowmelt earlier in the season, under the altered climate. 相似文献
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研究了膨润土-钢渣复合吸附剂对模拟酸性矿山废水中Fe2+的吸附去除效果、Fe2+在吸附剂表面的赋存形态及其吸附机理和规律。结果表明:复合吸附剂在处理含Fe2+模拟酸性矿山废水时,不仅能释放碱性物质中和酸,且发生了吸附-聚沉协同作用;Fe2+可与膨润土发生晶格置换,还可通过静电吸附作用形成硅酸盐类矿物相,还有一部分通过配合作用生成多金属氧化物,最后一类是通过化学沉淀作用生成的 Fe(OH)2或Fe(OH)3受热分解而形成Fe2O3;被吸附的Fe2+中98.62%以残渣态形式存在于复合吸附剂中;复合吸附剂对Fe2+的吸附行为符合BET等温吸附模型和准二级动力学模型。 相似文献
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对抚顺石化公司化工塑料厂苯乙烯废水活性炭吸附装置的预处理设施、活性炭吸附及再生性能进行了评价,分析了出水水质超标的主要原因,用混凝沉淀-砂滤流程改进了原处理工艺,使出水水质得到了显著改善。 相似文献