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equilibrium dead
平衡死区
MULTICOMPONENT DIFFUSION MODEL FOR EFFECTIVENESS FACTORS OF POROUS CATALYST (Ⅴ) FINITE ELEMENT METHOD FOR EFFECTIVENESS FACTORS OF SURFACE POISONED CYLINDRICAL CATALYST WITH EQUILIBRIUM DEAD ZONE 多孔催化剂效率因子的多组分扩散模型(Ⅴ) 表面中毒并伴有平衡死区圆柱状催化剂效率因子的有限元求解 短句来源 The single component model and multicomponent model of effectiveness factor ξd of surface poisoned catalyst were presented and solved by orthogonal collocation and Broyden method. Not only surface poisoning but also center equilibrium dead zone was found in catalyst pellets. The average of absolute values of relative deviations between experimental values and calculated values lor ξd was less than 11%. 探讨了计算表面中毒催化剂效率因子的甲醇单组分模型和多组分模型的正交配置解,解决了颗粒催化剂存在表面中毒和中心平衡死区的效率因子的求解问题,中毒催化剂效率因子的实验值与模型计算值的相对误差,其绝对值的平均值在11%以内,表明表面中毒催化剂效率因子的计算模型是可行的. 短句来源 On the basis of the distinguishing features of two-dimensional reaction -diffusion equations describing the surface poisoned cylindrical catalyst with equilibrium dead zone, Finite Element Method (FEM) is used to solve this kind of problem, which is often difficult to solve for other methods. 针对表面中毒并伴有平衡死区二维圆柱状催化剂的反应-扩散偏微分方程组的特殊性,引入有限元方法求解该类问题,建立了求解步骤。 短句来源 
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The global reaction rates of methanol decomposition of C207 Cu-based catalyst under atmospheric pressure were determined in an internal recycle gradientless reactor and mlet. 7.19×10-4) with addition of H2S for 4 hours, 8 hours and 12 hours respectively. The pore size distribution, and the tortuosity factors of φ 5 × 5mm cyindrica catalyst pellets were also measured. Hydrogen sulfide poisoning of commerial catalyst is considered as surface poisoning. The experimental values of non-poisoned dimensionless rad... 在常压下内循环无梯度反应器中测定了工业颗粒C207铜基化剂在入口硫化氢含量7.19×10~(-4)通硫化氢4、8、12h后甲醇分解反应宏观速率,测定了催化剂孔径分布和曲折因子.由俄歇电子能谱测定获得,通H_2S 4h未中毒比半径x_c为0.938,通H_2S 8h为0.916,通H_2S 12h为0.896,与由本征失活动力学获得的计算值相符合.探讨了计算表面中毒催化剂效率因子的甲醇单组分模型和多组分模型的正交配置解,解决了颗粒催化剂存在表面中毒和中心平衡死区的效率因子的求解问题,中毒催化剂效率因子的实验值与模型计算值的相对误差,其绝对值的平均值在11%以内,表明表面中毒催化剂效率因子的计算模型是可行的. 文摘来源 On the basis of the distinguishing features of two-dimensional reaction -diffusion equations describing the surface poisoned cylindrical catalyst with equilibrium dead zone, Finite Element Method (FEM) is used to solve this kind of problem, which is often difficult to solve for other methods. A comparison of calculated effectiveness factors with experimental data shows that FEM has the advantages of simplicity and accuracy and it is easy to be used to analogous systems. 针对表面中毒并伴有平衡死区二维圆柱状催化剂的反应-扩散偏微分方程组的特殊性,引入有限元方法求解该类问题,建立了求解步骤。实际计算所得效率因子与实验值对照表明,本法结果准确,过程简单,容易推广应用于各种相类似的体系。 文摘来源 A 3D reaction-diffusion model for irregular methane steam reforming catalyst is developed. The model was solved in non-isothermal condition with finite element method (FEM). FEM is simple, accurate and especially suitable for irregular geometries. The simulation was carried out over seven-channel spherical catalyst. Intraparticle concentration, temperature, reaction rate and temperature gradient profile are calculated. The effectiveness factor of the catalyst is 0.2～0.4. The simulation data of the model are... 针对甲烷蒸汽转化催化剂异形化过程中理论研究困难、性能数据主要依靠实测的问题,建立了适用于异形甲烷蒸汽转化催化剂的传质-传热耦合三维数学模型,用有限元法求解,求解方法简单、快速、精确。应用本模型计算了七孔球形转化催化剂的效率因子,获得了催化剂粒内的浓度、温度、反应速率、温度梯度分布。效率因子模型值与实验值较为吻合,平均相对误差8 22%。模拟结果表明:七孔球形催化剂效率因子在0 2～0 4之间,粒内存在10～16℃的温差,不能视为等温;催化剂粒内浓度、温度变化剧烈,有效反应区仅存在于靠近催化剂外表面的较小范围内,粒内存在较大的死区。 文摘来源 
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