itinerary
发表于 2025-4-1 05:49:56
Transport Restrictions in Catalyst Particles with Several Chemical Reactions,restrictions against mass and heat transfer in the interior and in the gas film surrounding the particle, and it accepts a general type reaction rate expression such as a power law expression or a Langmuir-Hinshelwood expression. The model is reduced to a number of coupled second order differential
得罪
发表于 2025-4-1 07:59:47
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ascetic
发表于 2025-4-1 11:20:03
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公猪
发表于 2025-4-1 15:35:55
Tracer Methods in Chemical Reactors. Techniques and Applications,apillary permeability of the microcirculation in medicine and by flow visualization in channels and around airplane wings in mechanical and aerospace engineering. Other applications are flow and transport measurements in rivers in hydrology, transport measurements of pollutants in soils in civil eng
保存
发表于 2025-4-1 19:39:01
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罐里有戒指
发表于 2025-4-2 02:17:08
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Diluge
发表于 2025-4-2 06:44:45
Design Aspects of Industrial Fluidized Bed Reactors. Research Needs. Selected Subjects,s and their effect on the quality of fluidization; (2) bubble size control through small solid particle size or baffles; (3) particle recovery by means of cyclones; (4) heat transfer tubes; (5) solids circulation systems; (6) instrumentation, corrosion and erosion, mathematical models, pilot plants
Medicaid
发表于 2025-4-2 07:19:47
Three-Phase Fluidized Bed Reactors,, Baker and Muroyama and Fan . Epstein distinguished in particular the difference between three-phase fluidized beds and slurry reactors. In slurry reactors the size of the solid particles is normally smaller than 0.1 mm while in three-phase fluidization the particle diameter is bigger