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Generalized stiffness and effective mass coefficients for power-law Euler-Bernoulli beams
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作者 Piotr Skrzypacz Daulet Nurakhmetov Dongming Wei 《Acta Mechanica Sinica》 SCIE EI CAS CSCD 2020年第1期160-175,共16页
We extend the well-known concept and results for lumped parameters used in the spring-like models for linear materials to Hollomon’s power-law materials.We provide the generalized stiffness and effective mass coeffic... We extend the well-known concept and results for lumped parameters used in the spring-like models for linear materials to Hollomon’s power-law materials.We provide the generalized stiffness and effective mass coefficients for the power-law Euler-Bernoulli beams under standard geometric and load conditions.In particular,our mass-spring lumped parameter models reduce to the classical models when Hollomon’s law reduces to Hooke’s law.Since there are no known solutions to the dynamic power-law beam equations,solutions to our mass lumped models are compared to the low-order Galerkin approximations in the case of cantilever beams with circular and rectangular cross-sections. 展开更多
关键词 Power-law Euler-Bernoulli beams Lumped parameter models Generalized stiffness coefficient effective mass coefficient
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Mass transfer between bubbles and the dense phasein gas fluidized beds
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作者 Hongyong Xie Zhiguo Sun 《Particuology》 SCIE EI CAS CSCD 2014年第5期213-217,共5页
Mass transfer between a bubble and the dense phase in gas fluidized beds of Group A and Group B particles was proposed based on previous experimental results and literature data. The mass transfer coefficient between ... Mass transfer between a bubble and the dense phase in gas fluidized beds of Group A and Group B particles was proposed based on previous experimental results and literature data. The mass transfer coefficient between bubbles and the dense phase was determined by kbe = 0.21 db. A theoretical analysis of the mass transfer coefficient between a bubble and the dense phase using diffusion equations showed that the mass transfer coefficient between a bubble and the dense phase is kbe α εmf√ub/db in both three- and two-dimensional fiuidized beds. An effective diffusion coefficient in gas fluidized beds was introduced and correlated with bubble size as De = 13.3db2.7 for Group A and Group B particles. The mass transfer coefficient kbe can then be expressed as kbe = 0.492εmf√ubdb1.7 for bubbles in a three-dimensional bed and kbe = 0.576εm√ubdb1.7 for bubbles in a two-dimensional bed. 展开更多
关键词 Fluidized bedsBubblesDense phase mass transfer effective diffusion coefficient
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