By E. Bruce Nauman

ISBN-10: 0470105259

ISBN-13: 9780470105252

ISBN-10: 0470282061

ISBN-13: 9780470282069

The vintage reference, now multiplied and up-to-date Chemical Reactor layout, Optimization, and Scaleup is the authoritative sourcebook on chemical reactors. This new moment variation consolidates the most recent details on present optimization and scaleup methodologies, numerical tools, and biochemical and polymer reactions. It presents the excellent instruments and data to aid readers layout and specify chemical reactors hopefully, with cutting-edge talents. This authoritative consultant:

  • Covers the basics and ideas of chemical reactor layout, besides complicated themes and functions
  • offers suggestions for facing various actual houses in reactors of every kind and reasons
  • incorporates a thoroughly new bankruptcy on meso-, micro-, and nano-scale reactors that addresses such issues as axial diffusion in micro-scale reactors and self-assembly of nano-scale buildings
  • Explains the strategy of fake transients, a numerical resolution process
  • contains feedback for extra analyzing, difficulties, and, while acceptable, scaleup or scaledown concerns on the finish of every bankruptcy to demonstrate business functions
  • Serves as a prepared reference for defined formulation, rules, and information

this can be the definitive hands-on reference for training execs and a very good textbook for classes in chemical reactor layout. it really is an important source for chemical engineers within the approach industries, together with petrochemicals, biochemicals, microelectronics, and water therapy.

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Extra resources for Chemical Reactor Design, Optimization, and Scaleup

Example text

0177. The concentration of sucrose cannot be determined without knowing the density of the solution. 10 g cm−3 at the experimental conditions. 21 × 10−4 mol cm−3 = 821 mol m−3 . 821 mol L−1 . A word of caution involves the definition of mole. 02 × 1023 molecules. There is an inconsistency in the SI system of units that may cause problems when converting molar densities and molar flow rates to mass densities and mass flow rates. , molar densities) of a and b has a mass density of ρ = a M A + bM B , where M A and M B are the molecular weights of the two components.

Among strictly chemical reactions, thermal decompositions such as CH3 OCH3 → CH4 + CO + H2 follow first-order kinetics at normal gas densities. The student of chemistry will recognize that the complete decomposition of dimethyl ether into methane, carbon monoxide, and hydrogen will not occur in a single step. 17. The decomposition does require energy, and collisions between the reactant and other molecules are the usual mechanism for acquiring this energy. Thus a second-order dependence may be observed for the pure gas at very low densities since reactant molecules must collide with themselves to acquire energy.

3 are different ways of expressing the overall mass balance for a flow system with variable inventory. In steady-state flow, the derivatives vanish, the total mass in the system is constant, and the overall mass balance simply states that input equals output. In batch systems, the flow terms are zero, the time derivative is zero, and the total mass in the system remains constant. 3 when unsteady reactors are treated in Chapter 14. Until then, the overall mass balance merely serves as a consistency check on more detailed component balances that apply to individual substances.

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Chemical Reactor Design, Optimization, and Scaleup by E. Bruce Nauman


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