Energy Efficiency of Two‐Phase Mixing in a Modified Bubble Column

Energy efficiency for gas liquid mixing in a modified downflow bubble column reactor has been analyzed in this paper. Efficiencies of the different parts of the bubble column have been assessed on the basis of energy dissipation. Prediction of the energy dissipation coefficient as well as energy utilization efficiency due to gas‐liquid mixing as a function of different physical, geometric and dynamic variables of the system has been done by correlation method. The distribution of energy utilization in the different zones of the column has also been analyzed. Experiments were carried out with air‐water and air‐aqueous solutions of carboxy methyl cellulose with different concentrations.     

取代基及分子量对非离子型纤维素醚表面特性的影响

根据Washburn的浸渍理论(Penetration Theory)和van Oss-Good- Chaudhury的组合理论(Combining Theory)及应用柱状灯芯技术(Column Wicking Technique),对几种非离子型纤维素醚,如甲基纤维素、羟丙基纤维素和羟丙基甲基纤维素的表面特性进行了测试。由于这些纤维素醚的取代基、取代度和分子量不同,所以它们的表面能及其组成部分有着明显的差异。数据说明,非离子型纤维素醚Lewis碱大于Lewis酸,表面自由能的主要成分是Lifshitz-van der Waals力。羟丙基的表面能及其成分都大于羟甲基。而在相同取代基和取代度的前提下,羟丙基纤维素的表面自由能正比于分子量;而羟丙基甲基纤维素的表面自由能则正比于取代度,反比于分子量。实验还发现非离子型纤维素醚中的取代基羟丙基和羟丙基甲基的表面能似乎都大于纤维素的表面能,而实验证明所测试得出的纤维素的表面能及其成分的数据是与文献所吻合的。     

毛细管色谱法同时测定异戊二烯中环戊二烯、甲基吡咯烷酮和二甲基甲酰胺

用毛细色谱法建立异戊二烯中各组分定性分析方法及环戊二烯,N-甲基吡咯烷酮,N,N-二甲基甲酰胺的测定方法。气相色谱条件:采用OV-1701毛细管气相色谱柱,50 m×0.32 mm×0.53μm。程序升温60℃保持5 min后,以10℃/min升至190℃,保持3 min。氮气(纯度99.999%)为载气,柱前压为69 kPa。分流进样,分流比1∶100。进样口温度200℃,FID检测器,检测器温度为200℃。结果表明,异戊二烯中各组分均达到良好分离。环戊二烯、N-甲基吡咯烷酮、N,N-二甲基甲酰胺的线性范围均为0.5~1 200μg/mL;回收率分别为96.0%~98.5%,95.0%~102%,96.0%~99.6%;检出限均达到0.5μg/mL。其方法简单、快捷且灵敏度高,可以用于异戊二烯中杂质含量的控制。     

气相色谱法低柱温技术在测定环境样品痕量八氟异丁烯中的应用

研究了色谱柱柱温对柱流失、分离效果的影响，采用低柱温技术显著降低了柱流失造成的背景，有利于痕量组分的分析；低柱温技术还明显提高了色谱柱分离效率，有利于在复杂成分样品中低沸点物质的测定。研究了在测定痕量全氟异丁烯中采用ECD检测器与相匹配的色谱柱问题，发现采用交联聚甲基硅氧烷类色谱柱比较适宜。利用本技术测定废水、环境气体中的痕量全氟异丁烯得到了满意的效果。     

振冲置换法在长江护岸地基处理中的应用

为解决长江高填方护岸深厚覆盖层地基的抗滑稳定问题,采用振冲置换法对地基进行加固处理。计算分析表明,振冲碎石桩处理范围、桩间距、桩长等参数应结合地形、地质条件进行设计,振冲置换法与其他地基处理方式进行有机结合能够取得更好的处理效果;护岸地基通过振冲置换处理后,抗滑稳定性能够满足规范要求。采用振冲碎石桩对软弱地基进行置换形成复合地基,能够有效解决地基砂土液化问题、承载力问题及抗剪强度问题。     

板柱与梁板结构受力性能对比研究

以某工程为算例,分别选取合理板柱与梁板结构计算模型,按照相关规范进行大型广场在平时工况与战时工况顶板各构件承载力计算,并对其两种结构型式的受力性能分析对比,以总结出地下人防结构顶板的适用原则,为实际工程设计提供参考依据。     

带约束拉杆L形方钢管混凝土组合异形柱的受力研究

为研究对拉约束拉杆对组合柱性能的影响,针对L形组合异形柱设置不同类型的约束拉杆、不同强度材料等进行数值模拟,对比该类型下的相应试验结果,分析验证了对拉约束拉杆对L形组合异形柱的性能改善作用,得到了对拉约束在柱延性及承载力方面的积极影响效果。最后基于线性回归分析的理论计算方法表现出了和数值结果较高的一致性,建立了具有较高参考价值的带约束拉杆的组合异形柱承载力计算公式。     

气相色谱法测定3-氯-1-丙醇

以填充柱气相色谱对 3 氯 1 丙醇进行了分析研究 ,方法变异系数 0 .5 % ,回收率99.5 0 %～ 10 0 .6 7%     

Vapour- and liquid-side volumetric mass transfer coefficients measured in distillation column. Comparison with data calculated from absorption correlations

Volumetric mass transfer coefficients in liquid and vapour phases in distillation column were measured by the method consisting of a fitting of the concentration profile of liquid phase along the column obtained by the integration of a differential model to the experimental one. The mathematical model of distillation process includes mass and energy balances and the heat and mass transfer equations. The film model flux expressions with the convective transport contributions have been considered in the transfer equations. Vapour and liquid phases are supposed to be at their saturated temperatures along the column. Effect of changes of phase flows and physical properties of phases on the mass transfer coefficients along the column and non-ideal thermodynamic behaviour of the liquid phase have been taken into account. The concentration profiles of liquid phase are measured in the binary distillation of the ethanol-water and methanol-ethanol systems at total reflux on metal Pall Rings and Intalox saddles 25 mm in the column with diameter of 150 mm. The distillation mass transfer coefficients obtained by the fitting procedure are compared with those calculated from absorption data using Onda's, Billet's and Linek's correlations. The distillation heat transfer coefficients calculated from the model assuming saturated temperatures in both phases are compared with those calculated from the Chilton-Colburn and penetration model analogy between mass and heat transfer. The results have confirmed an agreement neither between distillation and from absorption correlations calculated mass transfer coefficients nor between analogy and from enthalpy balance calculated heat transfer coefficients. Also the concentration profiles obtained by the integration of the differential model of the distillation column using the coefficients from absorption correlation have differed from the experimental profiles considerably.     

新型螺旋式浓硝酸漂白塔及其应用

针对传统的帽罩式浓硝酸漂白塔存在的缺点和不足，找出原因并予以改进，开发研制出螺旋式浓硝酸漂白塔，改进了工艺状况，减少了维修工作量，达到了节能降耗的目的，确保了直接法浓硝酸装置的长周期运行。