共查询到19条相似文献,搜索用时 78 毫秒
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采用熔融纺丝法研究了低密度聚乙烯(PE-LD)、线形低密度聚乙烯(PE-LLD)和高密度聚乙烯(PE-HD)熔体的拉伸流变性能。结果表明,PE-LD、PE-LLD和PE-HD熔体的熔体强度都随温度的升高而下降;随着拉伸应变速率和温度的升高,PE-LD、PE-LLD和PE-HD熔体的拉伸黏度下降;随着挤出速率的提高,相同应变速率下,PE-LD、PE-LLD和PE-HD熔体的拉伸应力和拉伸黏度都有所降低。 相似文献
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利用毛细管流变仪对四种不同聚乳酸切片的流变行为进行了对比分析,并探讨了流变性能差异对熔融纺丝性能的影响。结果表明:四种聚乳酸熔体均呈现剪切变稀现象,具有非牛顿流体的流动特征;随着温度升高,聚乳酸熔体的非牛顿指数n增大;四种聚乳酸熔体的粘流活化能E_η较小,粘度随温度的变化小,有利于纺丝成型;四种聚乳酸熔体的结构粘度指数△η介于0.8~1.4,可纺性和稳定性较好。 相似文献
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LDPE熔融接枝丙烯酸的研究 总被引:4,自引:0,他引:4
本文选择丙烯酸作为接枝单体与过氧化二异丙苯、低密度聚乙烯混合,在单螺杆挤出机中进行熔融接枝反应。实验研究了挤出条件、DCP用量以及丙烯酸单体用量对熔融接枝的影响。 相似文献
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LDPE熔融接枝的研究 总被引:12,自引:0,他引:12
本文介绍了马来酸酐(MAH)、丙烯酸(AA)、乙烯在三乙氧硅烷(A151)与LDPE的挤出熔融接枝工艺以及枝物与氢氧化铝(ATH)配合后填充体系的力学性能。研究了挤出温度、DCP用量和MAH用量对接枝物分子结构的影响,得出温度在210-230℃的范围内挤出物的接枝及MFI变化不大,当温度升到250℃后接枝率及MFI均不下降,DCP用量达到0.10phr以后,接枝率渐趋平衡而物料的MFI却迅速下降,表明有严重的交联反应;随MAH用量的增加,接枝率相应增加,当用量达0.5phr后接枝率基本稳定,不随MAH用量增加而继续提高。由接枝物-ATM填充体系的拉伸强度(σ拉)表明,虽然三种不同单体接枝的LDPE自身的σ拉与纯LDPE基本相同,但填充体系的σ拉均明显高于未接枝的。PE与ATH以1:1双例配合时,测得PE接枝MAH和枝A151的σ拉分别为15.3MPa和14.9MPa,比相同配比下未接枝的7.4MPa提高一倍以上。 相似文献
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采用毛细管流变仪考察了温度、剪切速率、预热时间对聚乳酸(PLA)、聚丙烯(PP)、低密度聚乙烯(LDPE)流变性能的影响。结果表明:PLA属切力变稀流体,在210℃时的非牛顿指数为0.68,而该温度下PP的非牛顿指数为0.56,LDPE为0.49;在剪切速率为100~2000s-1时,PLA的黏流活化能为61.51~141.52kJ/mol,PP为14.6~31.92kJ/mol,LDPE为13.89~36.47kJ/mol;在低剪切速率时,增加预热时间不仅使PLA的黏度明显下降,而且使其非牛顿指数和黏流活化能增加,当预热时间从150s增加到300s时,PLA在210℃的非牛顿指数从0.44增加到0.68,剪切速率为100~5000s-1的黏流活化能从32.99~91.67kJ/mol增加到50.40~141.52kJ/mol。 相似文献
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Haijin Zhu Yanfang Wang Yifan Su Qingkui Chen Cun Geng Charles C. Han 《Polymer》2007,48(17):5098-5106
A systematic investigation on the origin of the haze of LDPE blown films was conducted, aiming to correlate the film haze with the molecular architecture and melt rheological properties. First of all, the haze measurement indicated that the surface haze, rather than the bulk haze, is the dominating factor for the total haze of the investigated films. No spherulitic crystals or other superstructures were observed for the LDPE blown films, implying that the crystallites formed in the film-blowing process are too small to be responsible for the optical haze. Rheological study revealed that the surface roughness was originated from the irregular flow of LDPE melt during the extrusion process. NMR, GPC and parallel-plate rheology were applied to study the molecular architecture of the LDPE resins. It was found that the LDPE sample with higher haze value exhibits distinctly larger portion of higher molecular weight component, broader molar mass distribution, significantly higher side chain branch density. 相似文献
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Almost all polymer processing operations involve moving and shaping the polymer as a melt and then cooling it, usually quite rapidly, to a solid state. In order to develop models for such processes we have begun systematic studies in non-isothermal rheology; here we interpret the results in the context of melt spinning. Theoretical predictions of stress vs distance from the spinneret were calculated from generalized (non-isothermal) viscoelastic theory and compared with Dees' melt spinning data on high density polyethylene. Despite certain experimental and theoretical difficulties, the agreement is good. Surprisingly, an additional theoretical curve, based on a simple Trouton viscosity, also gave a reasonable approximation over much of the distance, despite the transient nature of the flow. To understand this phenomenon further, a more tractable theoretical problem was studied in detail; the problem, of constant elongational flow (? = constant) in the presence of a constant rate of temperature change (dT/dt = constant). The results depend on two dimensionless groupings; the first is the usual product of a relaxation time and ?; the second involves the ratio of normalized dT/dt to ?. When the second group is large, a quasi-viscous state exists. The melt spinning data for the HDPE may be near this state. 相似文献
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司徒建崧 《高科技纤维与应用》2014,(4):36-39
聚己内酯(PCL)是一种全微生物分解性高分子聚合物,由于其降解产物无毒,在生物医学、纺织服装和环保领域都得到了广泛的关注。在水平牵伸单丝实验设备上进行PCL熔融纺丝试验,通过对切片干燥、螺杆温度、水浴温度、牵伸比等工艺参数的调试和控制。探索了PCL熔融纺丝的工艺参数和关键技术。试验表明,采用切片干燥温度50~55℃、干燥时间13~18 h、纺丝温度150~180℃、牵伸比3.8~4.3等工艺参数,可制得直径为0.14 mm、物理性能指标良好的单丝样品。 相似文献
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A theoretical and experimental study has been carried out on extrudate swell B, especially the influence of rheological properties and applied take-up force on the emerging melt. The problem is analyzed in terms of (1) dimensional analysis, (2) force–momentum balances, (3) partially constrained elastic recovery. Analyses in terms of force–momentum balances are only able to give extrudate swell B in the asymptote of high Reynolds numbers. For low Reynolds numbers, they simply relate the take-up force to the pressure field in the spinneret. Increasing the take-up force predicts a decrease in the exit pressure. The partially constrained elastic recovery theory yields an expression for B as a decreasing function of applied take-up force. Specifically, this is where B(0) is the extrudate swell in the absence of applied forces, λeff is the effective relaxation time, μ is viscosity (both evaluated at the capillary wall), and D is the spinneret capillary diameter. An experimental study of extrudate swell of several rheologically characterized melts (high density polyethylene, low-density polyethylene, polypropylene, polystyrene) has been carried out at 180°C by four different methods (frozen, annealed in hot silicone oil, photographed emerging into air, photographed emerging through 180°C silicone oil) in the absence of applied take-up forces. Extrudate swell for a melt emerging from dies with differing diameters correlates with capillary-wall shear rate. A comparison of extrudate swell with normal stress–shear stress ratio shows the best agreement for frozen extrudates and photographs of melts emerging into air. The data is compared to the Tanner theory of extrudate swell. B has been determined during melt spinning and shown to be a function of take-up force for both a high-density polyethylene and polypropylene melt. B decreases rapidly with applied take-up stresses. The results are compared to the predictions of the partially constrained elastic recovery theory. 相似文献
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