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Titlebook: Chemical Reactor Design and Technology; Overview of the New Hugo I. Lasa Book 1986 Martinus Nijhoff Publishers, Dordrecht 1986 dynamics.en

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樓主: ODE
11#
發(fā)表于 2025-3-23 11:39:27 | 只看該作者
Converting Methanol into Gasoline in a Novel Pseudoadiabatic Catalytic Fixed Bed Reactor,
12#
發(fā)表于 2025-3-23 17:24:01 | 只看該作者
13#
發(fā)表于 2025-3-23 22:02:47 | 只看該作者
Tracer Methods in Chemical Reactors. Techniques and Applications,echanisms of chemical and catalytic reactions, measurement of diffusion rates, etc. All these methods rely on perturbing the system under investigation and monitoring the system’s response to such perturbations. This response is then interpreted. Some conclusions can be obtained on a model-free basis, others are model dependent.
14#
發(fā)表于 2025-3-24 00:50:50 | 只看該作者
15#
發(fā)表于 2025-3-24 05:21:11 | 只看該作者
Kinetic Data Analysis and Parameter Estimation,e at reliable parameter estimates dependent on the operating variables of the reactor, like pressure, temperature, flow conditions etc. These parameters then will be used in a reactor model, i.e., a set of equations that describe the behavior of a reactor with sufficient accuracy.
16#
發(fā)表于 2025-3-24 07:44:48 | 只看該作者
Hydrodynamics of Trickle-Beds. The Percolation Theory, the description of the fluid flow pattern is very difficult because of the high number of intricate mechanisms that can control this pattern. The situation is so complex that, in many cases, we do not even know the essential hydrodynamic parameters that may affect the performance of the reactor.
17#
發(fā)表于 2025-3-24 12:49:55 | 只看該作者
0168-132X on high energy consumption, accustomed to the use of cheap non-renewable energy and to the acceptance of eXisting imbalances between the resources and demands of countries. Despite all these stressing factors, our world is still hesitatins about the urgency of undertaking new and decisive research t
18#
發(fā)表于 2025-3-24 17:44:54 | 只看該作者
19#
發(fā)表于 2025-3-24 19:46:49 | 只看該作者
20#
發(fā)表于 2025-3-25 02:20:49 | 只看該作者
Catalyst Technology for Reactors used to Hydrocrack Petroleum Residua,Co or Ni) is also described. The catalyst is deactivated by coke and by metals. Furthermore, the reaction rate is often controlled by the rate of diffusion of the large carbonaceous molecules in the residua. All of these factors have been considered in mathematical simulations of the phenomena occuring in the catalyst.
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