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Effects of resin formulation, catalyst, and curing temperature were studied for particleboard binder‐type urea‐formaldehyde (UF) and 6 ~ 12% melamine‐modified urea‐melamine‐formaldehyde (UMF) resins using the dynamic mechanical analysis method at 125 ~ 160°C. In general, the UF and UMF resins gelled and, after a relatively long low modulus period, rapidly vitrified. The gel times shortened as the catalyst level and resin mix time increased. The cure slope of the vitrification stage decreased as the catalyst mix time increased, perhaps because of the deleterious effects of polymer advancements incurred before curing. For UMF resins, the higher extent of polymerization effected for UF base resin in resin synthesis increased the cure slope of vitrification. The cure times taken to reach the vitrification were longer for UMF resins than UF resins and increased with increased melamine levels. The thermal stability and rigidity of cured UMF resins were higher than those of UF resins and also higher for resins with higher melamine levels, to indicate the possibility of bonding particleboard with improved bond strength and lower formaldehyde emission. © 2005 Wiley Periodicals, Inc. J Appl Polym Sci 97: 377–389, 2005 相似文献
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在平板卧式超滤膜元件结构模型的基础上,建立了膜元件运行的微分方程数学模型.由膜元件运行参数限定了微分方程的边界条件,推导出微分方程组具有唯一解.膜元件运行微分方程模型的建立,为分析膜元件系统的运行提供了数学理论基础. 相似文献
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GAC,UF,RO去除饮用水中氯仿,四氯化碳性能的试验研究 总被引:2,自引:0,他引:2
研究了粒状活性炭(GAC),超滤(UF)和反渗透(RO)对自来水中氯仿和四氯化碳的去除性能,探讨了GAC对氯仿和四氯化碳去除的物理吸附和微生物降解机理。试验发现UF膜对氯仿和四氯化碳的快速吸附与脱附现象,并讨论了RO膜对不同浓度氯仿、四氯化碳的去除效果和作用机理。 相似文献
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介绍铝材电泳涂装后封闭清洗回收系统,在保证清洗质量的前提下,该系统的应用,提高了电泳涂料的回收率;减少了废水排放,节省了处理费用;节约了纯水的用量。并对该系统中主要设备(超滤和反渗透)的透过量的设计计算进行了介绍。 相似文献
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In this study, nine flat-sheet commercially available hydrophobic PTFE membranes were used in desalination by direct contact membrane distillation and their characteristics were investigated under different operating conditions including feed temperature, feed flow rate, cold stream flow rate, and feed concentration. Membrane properties, i.e. pore size, thickness, support layer, and salt rejection were also studied. Moreover, membrane module designs including flow arrangements (co-current, counter-current and tangential) for process liquid and depth both on hot and cold sides were tested experimentally. Finally, the long-term performance of the selected membranes for direct contact membrane distillation as a stand-alone desalination process was investigated. The results indicated that increasing feed temperature, hot feed flow rate, and module depth on the cold side led to increase permeate flux. On the other hand, increasing membrane thickness and module depth on the hot side (at constant flow rate) had negative effects on the flux. The highest permeation flux and salt rejection was achieved when the membranes with a pore size of 0.22 μm were used in the cross-current follow arrangement of hot and cold streams. In addition, the requirements for support layer for a successful DCMD process has been extensively discussed. 相似文献