|
Volumn 49, Issue 2, 2010, Pages 719-734
|
Design and control of the cumene process
|
Author keywords
[No Author keywords available]
|
Indexed keywords
CAPITAL COSTS;
CAPITAL INVESTMENT;
CHEMICAL PROCESS;
DESIGN AND CONTROL;
DESIGN OPTIMIZATION;
DIISOPROPYLBENZENE;
ECONOMIC DESIGN;
ECONOMIC EFFECT;
ENERGY COST;
LARGE DISTURBANCE;
OPTIMUM DESIGNS;
ORDER OF MAGNITUDE;
PLANTWIDE CONTROL;
PRODUCTION RATES;
RAW MATERIAL COSTS;
REACTOR SIZES;
REACTOR TEMPERATURES;
RECYCLE FLOW;
RECYCLE STREAM;
TUBULAR REACTORS;
VAPOR-PHASE REACTORS;
ACTIVATION ENERGY;
BENZENE;
BENZENE REFINING;
COSTS;
DESIGN;
DISTILLATION;
DISTILLATION COLUMNS;
ECONOMIC AND SOCIAL EFFECTS;
EFFLUENTS;
HYDRAULICS;
INVESTMENTS;
MATERIALS HANDLING;
OPTIMIZATION;
PROPYLENE;
RECYCLING;
SYNTHESIS (CHEMICAL);
PROCESS CONTROL;
|
EID: 75249086445
PISSN: 08885885
EISSN: None
Source Type: Journal
DOI: 10.1021/ie9011535 Document Type: Article |
Times cited : (63)
|
References (4)
|