Dynamics and stability analysis of solid catalyzed gas-phase polymerization of olefins in continuous stirred bed reactors

Chemical Engineering Science

Volumn 55, Issue 20, 2000, Pages 4461-4479

  Gorbach, A B ^a   Naik, S D ^b   Ray, W H ^c  

^a Inst fur Chem Verfahrenstechnik   (Germany)

^b Firestone Tire and Rubber Company   (United States)

^c University of Wisconsin Madison   (United States)

Author keywords

Modelling; Multi stage process; Nonlinear Dynamics; Polymerization; Propylene; Stability

Indexed keywords

CATALYSIS; CHEMICAL REACTORS; MATHEMATICAL MODELS; MELTING; POLYPROPYLENES; PROCESS CONTROL;

CONTINUOUS STIRRED BED REACTORS (CSBR);

POLYMERIZATION;

ALKENE; DYNAMICS; POLYMERIZATION; STABILITY; STIRRED TANK;

EID: 0034307048     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0009-2509(00)00080-4     Document Type: Article

References (11)

1. Theoretical modeling of Amoco's gas phase horizontal stirred bed reactor for the manufacturing of polypropylene resins
2. The dynamic behavior of a fluidized bed reactor for solid catalyzed gas phase olefin polymerization
3. The dynamic behavior of continuous stirred-bed reactors for the solid catalyzed gas phase polymerization of propylene
4. Dynamics and stability of polymerization process flow sheets
5. The bifurcation behavior of tubular reactors
6. Methods of removing heat from polymerization reactions of monomers in the gas phase
7. Reactor residence time distribution effects on the multistage polymerization of olefins-I, Basic principles and illustrative examples, polypropylene