Michael Baldea's Dynamics and Nonlinear Control of Integrated Process Systems PDF

By Michael Baldea

ISBN-10: 052119170X

ISBN-13: 9780521191708

Offering a scientific version aid and hierarchical controller layout framework for wide periods of built-in method platforms encountered in perform, this booklet first reports procedure platforms with huge fabric recycle and/or with small purge streams, by way of platforms with power integration. step by step version aid techniques are constructed to derive nonlinear decreased types of the dynamics in whenever scale. Hierarchical keep watch over architectures which includes coordinated degrees of regulate motion in numerous time scales are proposed for every category of strategy structures thought of to implement balance, monitoring functionality and disturbance rejection. a variety of procedure purposes are mentioned intimately to demonstrate the applying of the tools and their power to enhance method operations. MATLAB codes also are offered to steer additional software of the equipment constructed and facilitate sensible implementations.

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Additional resources for Dynamics and Nonlinear Control of Integrated Process Systems

Example text

18) ˆ 2 is the fast transient. 15), the term x quantity. 17), is a theorem due to A. N. Tikhonov (Tikhonov 1948). 1. 15) is valid for any t ∈ [t1 , T ]. 2. 1 states that ˆ 2 (τ ) = 0 lim x τ →∞ uniformly in x01 , t = 0; that is, x2 will come close to the quasi-steady-state value ¯ 2 at a time t1 > 0, while condition (ii) assumes that, for any t ∈ [t1 , T ], x2 will x ¯2. 3. 17). Note that, if x02 is sufficiently close ¯ 2 (t = 0), then condition (ii) encompasses condition (i). 1. 4. In a general nonlinear system, there may be several distinct solu¯ i , i ∈ {1, .

N − 1), and the recycle (j = R). 1) also makes use of the recycle number Rc, which we define below. 1. 2) Evidently, for a given production rate (set by F0 ), the value of Rc varies with the flow rate of the recycle stream. Two limit cases are of interest. Case I. Rc 1: in this case, the recycle flow rate is much smaller than the feed flow rate, the internal flow rates are comparable to the feed flow 1, Rckj = k˜j = O(1), j = 1, . . , N − 1. 3) j=1 In this case, the model of the process with recycle is a regular perturbation of the nominal (no recycle) series system.

2007, Scattolini 2009, and references therein), which use the term “hierarchy” to denote a set of guidelines, to be followed in sequence, for designing the control system for a chemical plant. 2. Non-aqueous solvents are used as a reaction medium when an aqueous synthesis route is not possible or economically feasible. ) can facilitate product and enzyme recovery in enzymecatalyzed processes (Zaks and Klibanov 1985, Illanes 2008, Kobayashi 2009, Adams et al. 2009). Ionic-liquids-based processes have garnered attention in recent years owing to improved environmental safety and enhanced solvent recovery (Wheeler et al.

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Dynamics and Nonlinear Control of Integrated Process Systems by Michael Baldea

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