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Steady state behavior of a continuous stirred tank reactor is analyzed for styrene polymerization with bifunctional free radical initiators.
Various analytical expressions describing the hydraulic behavior of a continuous permeable reactive barrier (PRB) are developed based upon a two-dimensional approximation of the local groundwater flow system.
The model proved very successful in predicting the behavior of a continuous laboratory hydrolysis ultrafiltration set up, specifically designed for that purpose.
It is also shown that eigenvalue assignment via a state feedback (output injection) controller on isolated time scales yields desired system behavior of a continuous system.
This work is part of a larger study aimed at characterizing the viscoelastic viscoplastic behavior of a continuous fiber glass mat thermoplastic composite.
The paper shows how the knowledge of the behavior of a continuous process can be formalized in terms of relations between discrete events that are deduced from a sequence of Apache's alarms by the mean ofa stochastic approach.
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Based on the folding kinetic the dynamic behavior of such a continuous refolding reactor was simulated under different operating conditions.
Our purpose is to prove the existence, uniqueness, and global asymptotic behavior of a positive continuous solution, where (f:(0,1 times[0,infty)rightarrow[0,infty)) is continuous and dominated by a function p satisfying appropriate integrability condition.
Motivated by the above mentioned work, we study in this paper the existence, uniqueness, and global behavior of a positive continuous solution for the following superlinear fractional boundary value problem: { D α u ( x ) = u ( x ) φ ( x, u ( x ) ), x ∈ ( 0, 1 ), lim x → 0 + D α − 1 u ( x ) = − a, u ( 1 ) = b, (1.4).
The effect of frequency on fatigue behavior of an oxide oxide continuous fiber ceramic composite (CFCC) was investigated at 1200 °C in laboratory air and in steam environment.
The dynamic behavior of an actual continuous stirred tank reactor in which a second-order reaction takes place was measured and the model which describes the micromixing phenomena within the reactor was identified.
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