Optimization of complex reactor networks—I. Isothermal operation
References (39)
- et al.
Yield optimization for complex reactor systems
Chem. Engng Sci.
(1981) - et al.
Determination of optimal reactor type
Chem. Engng Sci.
(1970) The degree of mixing in continuous flow systems
Chem. Engng Sci.
(1959)- et al.
Algorithmic synthesis of chemical reactor networks using mathematical programming
Ind. Engng Chem. Fundam.
(1986) - et al.
A superstructure based approach to chemical reactor netwrok synthesis
Comput. chem. Engng
(1988) - et al.
Developing targets for the performance index of a chemical reactor network: isothermal systems. Accepted for publication in
Ind. Engng Chem.
(1988) - (1964)
- (1969)
Partitioning procedures for solving mixed-variable programming problems
Number. Math.
(1962)- et al.
On the Development of a general algebraic modeling system in a strategic planning environment
Math. Prog. Study
(1982)
(1987)
(1976)
Studies on yield optimization for complex reactions. 1. Ideal reactors
Ind. Engng Chem. Process Des. Dev.
(1984)
Synthesis of optimal serial reactor structures for homogeneous reactions
A.I.Ch.E. J.
(1985)
Chemical reactors in process synthesis
Process Syst. Engng Symp. Ser.
(1985)
(1965)
Reactor optimization problems for reversible exothermic reactions
Can. J. chem. Engng
(1967)
Optimum distributed feed reactors for exothermic reversible reactions
J. Optimization Theory Applic.
(1967)
Optimum adiabatic cascade reactor with direct intercooling
Ind. Engng Chem. Fundam.
(1969)
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