Heat-release mechanism in ammonium dinitramide flame

To verify the adequacy of various models of heat release in ammonium dinitramide flame to real processes, chemical processes in products of thermal decomposition at a pressure of 10 torr and in ammonium dinitramide [ADN; NH₄N(NO₂)₂] flame at a pressure of 0.4 to 60 atm are numerically simulated. The calculations are performed on the basis of a detailed kinetic mechanism and boundary conditions correlated with experimental data, thermodynamic properties, and chemical composition of ADN. The kinetic mechanism includes submechanisms that describe high-temperature chemical processes in NH₃/N₂O/NO/NO₂/HNO₂/HNO₃ and NH₃/HN(NO₂)₂ mixtures, and the global stages of aerosol decomposition. Based on calculated and experimental data, the role of dinitraminic acid HN(NO₂)₂, aerosols, and ADN vapor in heat release in the ADN flame zone adjacent to the burning surface is estimated. The calculations predict that the main source of heat release in the cold flame zone at p ≥ 3 atm is dinitraminic acid incoming through the channel of dissociative evaporation ADN_liq → NH₃ + HN(NO₂)₂ from the burning surface. In the high-temperature flame zone, heat release is caused by the reaction that occurs in the NH₃/N₂O/NO/NO₂/HNO₂/HNO₃ mixture. At moderate pressures, the high-temperature and low-temperature zones are separated by an induction zone. The stage governing production of the OH radical, which plays an important role in combustion, in the induction zone is the reaction HNO₃ + M → OH + NO₂ + M. Because of a high activation energy of the stage, small temperature perturbations in the induction zone at low pressures lead to a finite change in the stand-off distance between the high-temperature flame zone and the burning surface. Therefore, small temperature perturbations in the induction zone, which are caused by admixtures in the sample or by heat transfer between the reacting gas and the ambient medium, may be responsible for disagreement between various experimental data and between experimental and calculated data on the stand-off distance between the high-temperature flame zone and the burning surface. In numerical calculations, the position of the high-temperature zone is effectively controlled by varying rate constants of elementary stages within admissible limits. __________ Translated from Fizika Goreniya i Vzryva, Vol. 43, No. 5, pp. 64–76, September–October, 2007.     

交流接触器温度场仿真及试验验证

将ANSYS有限元热分析应用到交流接触器热特性分析中,模仿其实际工作环境,构建交流接触器三维稳态热分析模型,确定热源、导热系数和表面散热系数,对接触器的稳态温度场进行分析;进一步改变施加的边界条件,研究不同散热方式下接触器的温度分布。最后对CJX2-0910型交流接触器进行温升试验,将温度场的仿真结果与试验结果比较,误差较小,表明所建立热分析模型的可行性。研究结果对接触器材料的选择、结构的设计及其性能的优化有重要意义。     

异形管内水力、传热性能的数值模拟

通过数值计算考察了横纹管、缩放管两种异形管内的流动与传热性能。计算时采用标准k-ε湍流模型：采用控制容积法对控制方程进行离散化；采用SIMPLE算法进行压力修正：代数方程采用超松弛法迭代求解。很出了在充分发展流时的传热努塞尔数、速度、瘴撩系数及湍动能分布，并与光滑管内的流动传热进行了比较，分析了异形管在强化传热方面的机理。计算结果和实验值比较吻合。     

电除尘器出口烟气废热的利用

介绍了采用热管锅炉回收硫酸系统电除尘器出口烟气废热情况，可回收废热生产0．8MPa饱和蒸汽1．0t/h。通过严格控制饱和蒸汽压力、炉气的三氧化硫含量及入炉原料的水分含量，热管锅炉连续运行两年未发生泄漏。运行一年即可收回成本，经济效益显著。     

内插旋流片的管内流动与换热的数值模拟

通过数值模拟,详细考察了光管内间隔插有旋转角为270.°、旋流角为38.1°旋流片的速度场与热流场的分布特性及其相互间的协同，并对4种旋流片的场协同数进行了比较。结果表明，在同样Reynolds数下，根据场协同数的大小来排列的旋流片类型依次为270-38.1、180-38.1、270-20.3、180-20.3，且与传热性能高低排列是一致的。通过改善速度场与温度梯度场的协同程度是提高换热性能的一个有效手段，且内插旋流片能有效地改善速度场与温度梯度场的协同程度从而提高换热性能。     

垃圾焚烧厂渗滤液生化出水混凝处理及其模型的建立

对采用聚合氯化铝、硫酸铝和氯化铁等混凝剂处理焚烧厂垃圾渗滤液生化出水的混凝效果及其模型进行了研究.结果表明:聚合氯化铝对焚烧厂垃圾渗滤液中CODCr、色度和浊度的去除效果比硫酸铝和氯化铁要好,且投加量相对也较少.在投加量500 mg/L、中性条件下,CODCr、浊度和色度的去除率可分别达到28.9%、91.6%和77.6%.在不同投药量、pH和搅拌速度下,PAC保持了良好的污染物去除效果,而对硫酸铝和氯化铁的处理效果影响较大.各种混凝剂的最佳投药量与起始CODCr浓度之间的关系可采用指数关系式表达.通过对PAC在各条件下混凝效果的统计分析,采用Matlab优化工具软件,建立了垃圾焚烧厂垃圾渗滤液PAC混凝处理的处理效果数学模式方程,其与试验结果的相关系数可达到0.982,表明建立的模型与混凝处理效果较为一致.     

填料并用对双组分室温硫化导热硅橡胶性能的影响

以α,ω-二羟基聚二甲基硅氧烷为基胶,Si3N4、AlN、Al2O3为导热填料,制备了填充型双组分室温硫化（RTV-2）导热硅橡胶.研究了填料Si3N4/Al2O3或AlN/Al2O3并用对RTV-2硅橡胶导热性能、工艺性能及力学性能的影响.结果表明,当填料的总体积分数为0.45时,对于Si3N4/Al2O3填充体系,随着体系中Al2O3体积分数的增加,RTV-2导热硅橡胶的热导率先升后降、拉伸强度先增后减,而扯断伸长率则呈逐渐升高的趋势,基料的粘度先减后增;当Al2O3的体积分数为0.14时,RTV-2导热硅橡胶的热导率最高、拉伸强度最大,基料的粘度最小,综合性能最佳.对于AlN/Al2O3填充体系,随着体系中Al2O3的体积分数的增加,RTV-2导热硅橡胶的热导率先升后降、拉伸强度及扯断伸长率先减后增,基料的粘度呈上升趋势;当Al2O3的体积分数为0.07时,RTV-2导热硅橡胶具有较好的导热性能和工艺性能,但力学性能偏低.     

PA6/SANMAH/GF复合材料的制备及其性能研究

采用双螺杆挤出机通过熔融共混制备了尼龙6／（苯乙烯／丙烯腈／顺丁烯二酸酐）共聚物／玻璃纤维（PA6／SANMAH／GF）复合材料，测试了材料的拉伸强度、弯曲强度、弯曲弹性模量、缺口冲击强度、热变形温度、吸水率、熔点和熔融焓，并与GF增强PA6（PA6／GF）复合材料和GF增强PA6／（苯乙烯／丙烯腈）共聚物（PA6／SAN／GF）复合材料进行了性能对比。结果表明，在PA6与SANMAH的质量比为100：3—30时，PA6／SANMAH／GF复合材料的拉伸强度与PA6／GF复合材料相当，但高于PA6／SAN／GF复合材料，弯曲强度和弯曲弹性模量高于PA6／GF和PA6／SAN／GF复合材料．缺口冲击强度高于PA6／GF复合材料，但低于PA6／SAN／GF复合材料；在PA6与SANMAH的质量比为100：40时，PA6／SANMAH／GF复合材料的拉伸强度、弯曲强度和缺口冲击强度明显降低；在整个试验范围内，PA6／SANMAH／GF复合材料的热变形温度比PA6／GF和PA6／SAN／GF复合材料低4～7℃；吸水率随着SAN-MAH用量的增加而逐渐减小。     

Shrinking rate of conducting grains in HCl–protonated polyaniline,polypyrrole, and polypyrrole/polyaniline blends with their thermal aging

The dc electrical conductivity (σ) of HCl‐protonated polyaniline, polypyrrole, and their blends was measured from 80 to 300 K for thermal aging times between approximately 0 and 600 h. The thermal aging took place at 70°C under room atmosphere. The change of σ with the temperature (T) and the decrease of σ with the thermal aging time (t) are consistent with a granular metal type structure, in which conductive grains are randomly distributed into an insulating matrix. Aging makes the grains shrink in a corrosion‐like process. From σ = σ(T) measurements the ratio s/d, where s is the average separation between the grains and d their diameter, as well as the rate d(s/d)/dt of their decrease with t were calculated. These revealed that the conductive grains consist of a shell, in which aging proceeds at a decreasing rate, and a central core, which is consumed at a much slower rate. Our measurements not only permitted the estimation of the shell thickness, which lies between 0 and 5 Å, but also gave quantitative information about the quality of the shells and the cores from their aging rates. The shells are consumed with an average rate of d(s/d)/dt = 6.6 × 10^?4 (h^?1), which is about 5 times greater than the more durable cores. © 2005 Wiley Periodicals, Inc. J Appl Polym Sci 97: 117–122, 2005     

过磷酸钙含氟尾气处理的新方法

对动态泡沫床处理过磷酸钙含氟尾气的有关技术及费用作了说明 ,指出该方法费用高 ;提出一种新方法 ,该方法不加任何化学助剂 ,采用水作吸收剂 ,只需改变动态泡沫床一些设计参数和选用一种特殊的喷头 (喷头周围设计 1个圆锥形死角区 ,使含氟气体不可能进入该区 )避免了硅胶堵塞。该方法已在湖南浦市化工总厂运行 1年多未发现堵塞 ,同时该法投资少、能耗低、排放尾气达标