螺杆构型对E-SBR／白炭黑／硅烷基橡胶-填料复合材料性能的影响

通过在同向双螺杆挤出机中进行实验,考察了E—SBR／白炭黑／硅烷基橡胶／填料复合材料（RFC）的连续混炼。在混炼区段捏合块类型变化（正向捏合块、中性捏合块和反向捏合块）情况下,研究了三种不同的螺杆构型。针对这三种不同的螺杆构型对混炼效率进行了比较。研究了胶料性能（如填料-填料相互作用、门尼黏度）以及硫化胶的机械性能,发现通过采用带反向捏合块的螺杆构型,白炭黑粒子的分散度高于带正向捏合块和中性捏合块者;利用反向捏合块所获得的胶料性能和硫化胶性能,与在密炼机内混炼的对照胶料的性能大致相当。     

啮合型同向旋转双螺杆挤出机的螺杆特性及其应用

介绍了啮合型同向旋转双螺杆挤出机的起源和发展,着重论述了该型挤出机挤压系统中的螺杆型式、螺纹元件和捏合元件的输送及混炼特性、螺杆组合型式和操作条件以及应用情况。     

啮合型同向旋转双螺杆挤出机的螺杆特征及其应用

介绍了啮合型同向旋转双螺杆挤出机的起源和发展，着重论述了该型挤出机挤压系统中的螺杆型式、螺纹元件和捏合元件的输送及混炼特性、螺杆组合型式和操作条件以及应用情况。     

同向双螺杆挤出过程不同螺杆构型的混合性能分析

利用POLYFLOW有限元分析软件列同向双螺杆挤出过程不同螺杆组合的流道进行了三维等温非牛顿流场模拟，通过计算结果后处理，分析了全正向螺纹流道、全正向捏合盘流道、全反向捏合盘流道等6种不同螺杆构型的分布混合性能和分散混合性能。     

啮合同向双螺杆挤出过程聚合物粒料熔融机理研究(二)——正向捏合块组合中熔融机理研究

以装有玻璃视窗的可视化双螺杆挤出机为手段，在不同操作条件下对高密度聚乙烯（ＨＤＰＥ）粒料在不同正向捏合块（即由正向捏合盘所组成的螺杆区段）中的熔融过程进行了实验研究。以实验现象为基础，提出了双螺杆挤出过程中海－岛式熔融模型的概念。研究表明，耗散－混合熔融是捏合块中聚合物熔融的主要机理，海－岛式熔融模型是捏合块中聚合物熔融的典型形态；螺杆构型、螺杆转速、加料量是决定聚合物颗粒熔融的主要因素。     

聚丙烯/无机纳米粒子在双螺杆挤出机内的分散混合效果数值模拟

采用三维有限元数值模拟方法,研究了聚丙烯(PP)/无机纳米粒子在双螺杆挤出机的三种螺杆组合元件流道内的分散混合效果。通过对比分析三种螺杆组合下无机纳米粒子的剪切应力和剪切速率、停留时间分布及粒径分布等结果,发现含错列角45°捏合块的螺杆组合对其流场中大部分粒子的剪切作用最强,含错列角60°捏合块的螺杆组合次之,含错列角90°捏合块的螺杆组合最弱。与另两种螺杆组合相比,含错列角45°捏合块的螺杆组合流场中,无机纳米粒子团聚体的数量最少,剥离出的碎片数量最多,即在含错列角45°捏合块的螺杆组合条件下无机纳米粒子在PP熔体中的分散效果最好。     

啮合同向双螺杆挤出过程聚合物粒料熔融机理研究（二）：正向捏合块组？…

以装有玻璃视窗的可视化双螺杆挤出机为手段，在不同操作条件下对高密度聚乙烯（ＨＤＰＥ）粒料在不同正向捏合块（即由正向捏合盘所组成的螺杆区段）中的熔融过程进行了实验研究。以实验现象为基础，提出了双螺杆挤出过程中海－岛式熔融模型的概念。研究表明，耗散－混合熔融是捏合块中聚合物熔融的典型形态；螺杆构型、螺杆转速、加料量是决定聚合物颗粒熔融的主要因素。     

挤出过程停留时间分布影响因素之间的交互作用

应用全析因设计方法,研究了捏合块角度、比产率(喂料速率/螺杆转速)和螺杆转速对双螺杆挤出机机筒不同位置的延迟时间和平均停留时间的影响,考察了各因素之间的交互作用。结果表明,在所选取的操作条件下,螺杆转速对延迟时间和平均停留时间的影响最大,捏合块角度与比产率的影响程度相近。3因素两两交互作用对延迟时间的影响程度由大到小依次为捏合块角度与比产率、螺杆转速与比产率、捏合块角度与螺杆转速;对平均停留时间的影响由大到小依次为比产率与螺杆转速、捏合块角度与比产率、捏合块角度与螺杆转速。3因素3阶交互作用对平均停留时间的影响比较显著。     

同向双螺杆熔融段螺杆组合对共混物相态变化的影响

研究了双螺杆熔融段不同螺杆组合对模型聚合物共混体系HDPE/PS相态变化的影响。发现错列角为正向30°及正向60°的捏合块具有较好的输送能力,但不利于物料的熔融和混合;90°错列角捏合块对共混物具有很好的熔融和混合效果,其混合性能甚至优于反向30°捏合块,接近反向60°捏合块;及向螺纹元件对共混物相态变化影响显著。     

用行星式螺杆挤出机连续混炼白炭黑填充胶料

研究了用行星式螺杆挤出机连续混炼的白炭黑填充胶料。研究用的原材料为乳聚SBR／白炭黑／硅烷／填料复合胶料，填料与硅烷在复合胶料的制备过程中充分反应，生成了完全硅烷化的白炭黑。由于行星式螺杆挤出机具有极强的冷却能力，所以，所有胶料组分，包括交联剂都可在同一个喂料段计量加入。未发现混炼胶有焦烧现象，连续混炼胶料的性能（如，填料分散和交联性能）以及硫化胶性能（如，拉伸强度和硬度）都与用密炼机混炼的胶料相当。连续混炼的能耗仅为密炼机混炼的1／3。     

Polymorphism of LiGa5O8 and of LiGa5O8-MgGa2O4Solid Solutions

High-temperature X-ray diffraction and differential thermal analyses showed that LiGa₅O₈ exists in two polymorphs related by the first-order transition at 1138°±3°C of the low-temperature simple-cubic form, space group (probably) O⁷, to the high-temperature spinel (fcc) form, space group O _h ⁷. The transition is rapid, and the high-temperature form in pure LiGa₅O₈ could not be quenched to room temperature under the conditions used. However, the high-temperature polymorph can be quenched under equilibrium conditions when 40 mol% or more MgGa₂O₄ is present. The subsolidus equilibrium relations in the system MgGa₂O₄-LiGa₅O₈ are discussed.     

Magnetoresistance of CuxCo1-xFe2O4 Ferrites

Magnetoresistance measurements (Δ/R) were carried out on Cu _x Co_{1- x} Fe₂O₄ samples with x =1, 0.75, 0.50, 0.25 and cobalt ferrite in the range of magnetic intensity (H) from 1.0 to 4.5 kG. Linear plots were obtained between log (Δ/R) and log H for all compositions except that of cobalt ferrite. The values of n at x =0.5 do not agree with the results of some authors. The discrepancy may be attributed to the value of magnetic field intensity at which such measurements were carried out. The similarity of features of n and μ_D with composition leads us to believe that the magnetoresistance may arise from the scattering of conduction electrons by localized electrons involving the s-d exchange interaction.     

Sintering of Si3N4-Y2O3-Al2O3

Sintering kinetics of the system Si₃N4-Y2O₃-Al₂O3 were determined from measurements of the linear shrinkage of pressed disks sintered isothermally at 1500° to 1700°C. Amorphous and crystalline Si₃N₄ were studied with additions of 4 to 17 wt% Y₂O₃ and 4 wt% A1₂O₃. Sintering occurs by a liquid-phase mechanism in which the kinetics exhibit the three stages predicted by Kingery's model. However, the rates during the second stage of the process are higher for all compositions than predicted by the model. X-ray data show the presence of several transient phases which, with sufficient heating, disappear leaving mixtures of β ' -Si₃N₄ and glass or β '-Si₃N₄, α '-Si₃N₄, and glass. The compositions and amounts of the residual glassy phases are estimated.     

Expansive properties of the mixture C4ASH12 − 2CS III. Effects of temperature and restraint

The effects of temperature and restraint upon the hydration and the expansion of $\text{C}{}_4\text{A}\text{S}\text{H}{}_{12}\text{? 2}\text{C}\text{S}$ mixture compacts in different contact solutions have been investigated. Temperatures above 20°C do apparently hinder the formation of an impervious felt-like layer of ettringite around the $\text{C}{}_4\text{A}\text{S}\text{H}{}_{12}$ particles, thus greatly reducing the retarding effect of the lime. An uniaxial restraint of 1 Kg/cm² is enough to reduce sensibly the expansions which remain however high (about 100%). The results can be satisfactorily interpreted by the reaction and expansion mechanism hypothesized in our previous papers.     

Raman Study of Glasses of Ba2TiSi2O8 and Ba2TiGe2O8

Raman spectra are reported for fresnoite (Ba₂Ti(Si,Ge)₂O₈ glasses, and comparison is made between the Raman spectra of the corresponding crystalline powders and glasses of Ba₂TiSi₂O₈ and Ba₂TiGe₂O₈. The Ba₂TiGe₂O₈ glass spectra show correspondence with the Ba₂TiGe₂O₈ crystalline Raman spectra; the v _s(Ge–O–Ge) mode occurs at 518 cm⁻¹ in the glass and at 521 cm⁻¹ in the crystalline material. Five-fold coordinated titanium is the majority species present in the Ba₂TiGe₂O₈ glass as revealed by a strong band at 824 cm⁻¹ in the I glass spectrum. The Ba₂TiSi₂O₈ glass spectra are similar to the Ba₂TiSi₂O₈ crystalline spectrum; the strongest band is found at 836 cm⁻¹ in the I glass spectrum. Through comparison with the previous Raman data of other titania silicate glasses, we conclude that the Ba₂TiSi₂O₈ glass has a structure similar to the crystalline phase.     

Preparation and properties of poly(Nε,Nε-dicarboxymethyl-l-lysine)

A new ampholytic homopolypeptide, $\text{poly}\text{(N}{}^{\mathrm{\epsilon }}\text{,N}{}^{\mathrm{\epsilon }}\text{-}\text{dicarboxy-methyl-}\text{l}\text{-lysine}\text{)}$, which has one tertiary amino and two carboxyl groups in the side chain has been derived from a hydrochloride salt of poly(L-lysine). The polymer in aqueous solution seems to be in the coil form with locally extended structure (LES) at neutral pH. In both the acidic and alkaline regions, the molar ellipticity of the polymer changes as a result of change in net charge on the side chain. The conformational changes may be from the coil with LES to other coiled forms. 5–7 M NaClO₄ and 80% aqueous methanol induce the α-helix in the polymer at neutral pH. Divalent cations, Cu²⁺ and Ca²⁺, do not induce any remarkably ordered structures such as α-helix or β-structure in the polymer in aqueous solution at any pH. Ultraviolet absorption studies show an absorption peak of the polymer-Cu²⁺ complex near 240 nm. Dependence of the peak intensity on pH at various q values ($\text{q =}\text{[}\text{Cu}{}^{\mathrm{2+}}\text{]}\text{[}\text{residue}\text{]}$) indicates the two steps of the complex formation. At q less than 0.64, the formation is described only with the first step. An average coordination number for Cu²⁺ at the first step was calculated to be about 2 by the method of Mandel and Leyte. The association constant of Cu²⁺ with the residue at the step was determined from the absorption data to be far smaller than that for the Cu²⁺-EDTA complex. The second step of the formation occurs in the case of large q but the absorption data for the second step cannot be obtained exactly due to precipitation.     

Effects of metal-support interactions on the hydrogenation of CO over PdSiO2 and PdLa2O3

A study of CO hydrogenation over $\text{Pd}\text{SiO}{}_2$ and $\text{Pd}\text{La}{}_2\text{O}{}_3$ has been carried out for the purpose of identifying the effects of Pd dispersion, Pd morphology, and support composition on the catalytic activity of supported Pd. The specific activity of each catalyst for methanol and methane synthesis was determined from microreactor studies carried out at a fixed set of reaction conditions. Palladium dispersion was measured by H₂O₂ titration, and the morphology of the Pd crystallites, as expressed by the distribution of Pd(100) and Pd(111) planes, was determined from in situ infrared spectra of adsorbed CO. The crystallite morphology of the $\text{Pd}\text{SiO}{}_2$ catalysts is the same, independent of Pd weight loading: 90% of the surface is comprised of Pd(100) planes and 10% of the surface is comprised of Pd(111) planes. By contrast, the crystallite morphology of the $\text{Pd}\text{La}{}_2\text{O}{}_3$ catalysts changes with Pd loading. Primarily Pd(100) planes are exposed at low-weight loadings while Pd(111) planes are exposed at high-weight loadings. The Pd dispersion has little effect on the methanol turnover frequency over both $\text{Pd}\text{SiO}{}_2$ and $\text{Pd}\text{La}{}_2\text{O}{}_3$, for dispersions between 10 and 20%. On the other hand, the methane turnover frequency is independent of Pd dispersion over $\text{Pd}\text{SiO}{}_2$, but increases with decreasing dispersion over $\text{Pd}\text{La}{}_2\text{O}{}_3$. It is further observed that the Pd morphology influences the specific activity of $\text{Pd}\text{La}{}_2\text{O}{}_3$ for methanol synthesis: Pd(100) is nearly threefold more active than Pd(111). For a fixed morphology, the specific methanol synthesis activity of $\text{Pd}\text{La}{}_2\text{O}{}_3$ is a factor of 7.5 greater than that of $\text{Pd}\text{SiO}{}_2$.     

In situ laser raman spectroscopy of the sulfiding of Moγ-Al2O3 catalysts

Raman spectra of sulfided $\text{Mo}\text{γ-}\text{Al}{}_2\text{O}{}_3$ catalysts were obtained using in situ techniques for two sulfiding methods. For samples sulfided by 10% $\text{H}{}_2\text{S}\text{H}{}_2$ at 400 °C, MoS₂ structures were observed. A stepwise sulfiding using 10% $\text{H}{}_2\text{S}\text{H}{}_2$, with spectra recorded at 150, 250, and 350 °C, resulted in observation of molybdenum oxysulfide, reduced molybdate, and surface “MoS₂” phases. Reexposure of these samples to air led to radical modification of the oxysulfide structures as well as transformation of some sulfide phases. A model incorporating terminal and bridging MoS bonding and anion vacancies is proposed. This model is based on the conversion of isolated and aggregated molybdate and MoO₃ species to oxysulfide and reduced molybdenum phases. Conversion of reduced molybdenum phases to sulfides is observed to be slow.     

Wet Milling of Fe/Al/Al2O3 and Fe2O3/Al/Al2O3 Powder Mixtures

Wet milling of Al₂O₃-aluminide alloy (3A) precursor powders in acetone has been investigated by milling Fe/Al/Al₂O₃ and Fe₂O₃/Al/Al₂O₃ powder mixtures. The influence of the milling process on the physical and chemical properties of the milled powders has been studied. Particle refinement and homogenization were found not to play a dominant role, whereas plastic deformation of the metal particles leads to the formation of dislocations and a highly disarranged polycrystalline structure. Although no chemical reactions among the powder components in Fe₂O₃/Al/Al₂O₃ powder mixtures were observed, the formation of a nanocrystalline, ordered intermetallic FeAl phase in Fe/Al/Al₂O₃ powder mixtures caused by mechanical alloying was detected. Chemical reactions of Fe and Al particle surfaces with the atmosphere and the milling media lead to the formation of highly porous hydroxides on the particle surfaces. Hence the specific surface area of the powders increases, while the powder density decreases during milling. The fraction of Fe oxidized during milling was determined to be 0.13. The fraction of Al oxidized during milling strongly depends on the metal content of the powder mixture. It ranges between 0.4 and 0.8.