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叙述无规共聚聚丙烯(PP-R)管接头加工中各种注射工艺条件对PP-R管接头冲击性能的影响。分析了注射速率,模腔压力,机筒温度,模具温度等工艺条件与PP-R管接头冲击性能的关系。指出采用尽可能低的注射速率,模腔压力,机筒温度及模具湿度有助于PP-R管接头冲击强度的提高。 相似文献
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研究了熔体温度、模具温度、状态调节温度等对均聚聚丙烯(PP)、抗冲共聚PP及无规共聚PP宏观性能的影响,分析了它们对PP微观形态的影响.结果表明,较低的熔体温度利于PP物性的提高;较高的模具温度利于PP刚性的提高.比较而言,抗冲共聚PP对熔体温度和模具温度的变化反应更加敏感. 相似文献
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注塑成型工艺对透明PP光学性能的影响 总被引:1,自引:0,他引:1
采用不同的工艺条件注塑成型无规共聚透明聚丙烯(PP),测试透光率、雾度和表面光泽度,分析了成型工艺参数对制品光学性能的影响。所选透明PP的最佳注塑工艺为:加工温度220~230℃,模具温度40~60℃。在保证制品顺利成型的情况下应尽量采用较小的注塑压力。注塑速率和注塑时间对制品的光学性能影响较小。 相似文献
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采用单因素变量法,研究了注射机料简及喷嘴温度、模具温度、冷却(保压)时间三项注射工艺参数对PP注射制件性能的影响。 相似文献
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选用4种分子量分布不同的高流动共聚聚丙烯为原料,分别调整熔体温度、注射速度和保压时间,研究其对材料性能的影响。结果表明,分子量分布较宽(PD大于7)的高流动共聚聚丙烯的材料性能对注射工艺的调整不敏感,冲击性能和热性能都非常稳定,数据波动范围分别在0. 4 k J/m2和4℃以内。分子量分布较窄(PD小于7)的高流动共聚聚丙烯的冲击性能和热性能随注射工艺的调整波动幅度明显增大。在注射工艺中,熔体温度的影响最大。熔体温度从200℃降低至180℃,可使PD为4. 8的高流动共聚聚丙烯的冲击值由7. 8 k J/m2升至10. 2 k J/m2。分子量分布较窄的高流动共聚聚丙烯在加工过程中,为提高性能数据的稳定性和可重复性,需要严格控制加工窗口。 相似文献
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考察了不同类型聚丙烯(PP)的收缩率,研究了无机填料、增韧剂改性PP的性能及其收缩率变化情况。结果表明:不同类型PP的收缩率不同,均聚PP收缩率最大,无规共聚PP次之,抗冲共聚PP最小。当抗冲共聚PP中乙烯含量增加时,其收缩率降低。模塑试样放置0.5~5.0 h以内时,模具温度越高,收缩率越大;随着放置时间延长,PP收缩率继续增大,放置5.0 h以上时收缩率随时间延长变化不大。添加无机填料改性可以降低PP收缩率,与连续玻璃纤维(GF)和短切GF相比,滑石粉改性对降低PP收缩率更有效。聚烯烃弹性体(POE)和茂金属线型低密度聚乙烯(mLLDPE)具有较好的增韧作用;当滑石粉和mLLDPE质量分数分别为30.0%和15.0%时,采用进口抗冲共聚PP制备的复合材料刚韧综合性能良好,平行和垂直流道方向的收缩率均为0.50%。 相似文献
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通过一次因子法确定Taguchi法的试验因子,再采用Taguchi法对试验因子进行权重分析与优化。结果表明,在注射成型过程中,对聚丙烯(PP)制品光泽度影响因子的权重大小顺序是熔体温度、模具温度、保压压力、注射速度。对于PP最佳光泽度的注射成型工艺控制方案为熔体温度205℃、模具温度65℃、保压压力5MPa、注射速度50%。 相似文献
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乙烯酮(双乙烯酮)是十分重要的化工中间体,其下游产品较多。江苏某化工厂开发生产乙烯酮(双乙烯酮)下游产品三十多个,年生产规模三万多吨,是国内以乙烯酮(双乙烯酮)为中间体生产精细化学品的综合骨干企业。针对乙烯酮(双乙烯酮)下游产品废水特点,该厂结合企业实际,开展了产品优化,结构调整,清洁生产,资源循环利用,节水降耗等工作,从源头削减了污染物的生产。同时投资二千多万元新建预处理装置三套,6000m3/d废水生化处理装置一套,使全厂乙烯酮(双乙烯酮)下游产品的废水得到了有效的治理。 相似文献
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D. G. Gordeev L. F. Gudarenko M. V. Zhernokletov V. G. Kudel’kin M. A. Mochalov 《Combustion, Explosion, and Shock Waves》2008,44(2):177-189
A semi-empirical equation of state for metals is described. Its capabilities are demonstrated by the example of the equation
of state for aluminum. New experimental data are presented on the location of the isentrope of aluminum for unloading from
the state at p = 229.71 GPa on the shock adiabat to an aerogel (SiO2) of density 0.08 g/cm3.
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Translated from Fizika Goreniya i Vzryva, Vol. 44, No. 2, pp. 61–75, March–April, 2008. 相似文献
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Jorge Marcelo Romero Soledad Bustillo Hugo Enrique Ramirez Maisuls Nelly Lidia Jorge Manuel Eduardo Gómez Vara Eduardo Alberto Castro Alicia H. Jubert 《International journal of molecular sciences》2007,8(7):688-694
A thermochemical rather simple experimental technique is applied to determine the enthalpy of formation of Diperoxide of ciclohexanone. The study is complemented with suitable theoretical calculations at the semiempirical and ab initio levels. A particular satisfactory agreement between both ways is found for the ab initio calculation at the 6–311G basis This set level. Some possible extensions of the present procedure are pointed out. 相似文献
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A perturbation viscometer is a differential capillary viscometer that measures the logarithmic viscosity gradient of the viscosity-composition curve for gas mixtures. Measurements are made at different gas mixture compositions. Integration of the logarithmic viscosity gradients measured over the full composition range gives the mixture viscosity relative to the viscosity of one of the pure components of the gas mixture. This method is attractive because, for measurements of equal precision, integration of the gradients is potentially an order of magnitude more precise than measurement of the viscosities directly. It can also work at high and low temperatures and perhaps high pressures.The perturbation viscometer has been used to make measurements on ideal gas mixtures at ambient and elevated temperatures. The situation is more complicated when the gas mixtures are non-ideal. Extra effects due to density differences, molar volume change on mixing and differential thermal expansion may be measured in addition to the desired viscosity change producing systematic errors in the results. Thus, a more sophisticated apparatus is required. The standard perturbation viscometer has been modified to separate out the extra effects to permit measurement of the true change in viscosity. In addition, the theoretical operation of the modified apparatus has been revised to account for the design changes to permit calculation of the viscosity-composition profiles from the results.The apparatus has been tested using helium-HFC-125 mixtures and two new viscosity-composition profiles are presented for these mixtures at 23 and . Internal consistency tests have been used to confirm that the data produced are of high quality with an estimated uncertainty in the viscosity ratio data at of 0.9% and at of 1.5%. 相似文献
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塔设备改造选型的分析 总被引:2,自引:0,他引:2
就当前扩产增容中塔设备设计和改造时板式塔和填料塔的选型问题加以分析。在评述目前国内常用的几种塔板和新型填料之后,着重介绍一种新型塔板(导向梯形浮阀塔板)和一种新型填料(波环填料——乾隆帕克)。 相似文献