Verification of a complex, variable viscosity model for a tubular polymerization reactor

Chemical Engineering Science

Volumn 44, Issue 1, 1989, Pages 179-188

  Chen, C C ^a   Nauman, E B ^a  

^a RENSSELAER POLYTECHNIC INSTITUTE   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

CHEMICAL REACTIONS--MATHEMATICAL MODELS; STYRENE--POLYMERIZATION; VISCOSITY;

INERT TRACER; RESIDENCE TIME DISTRIBUTION; TUBULAR REACTOR; VARIABLE VISCOSITY MODEL; VELOCITY PROFILES;

CHEMICAL EQUIPMENT;

EID: 0024859736     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/0009-2509(89)85243-1     Document Type: Article

References (16)

1. Confirmation of the Mayo mechanism for the initiation of the thermal polymerization styrene
2. Thermal Polymerization of styrene at high conversions and temperatures
3. Flow stability of multitubular continuous polymerization reactors
4. Polymerization in a tabular ractor
5. The dimerization of styrene
6. A staged multitubular process for crystal polysterene
7. Effect of radial velocities on laminar flows tabular reactor models
8. The density thermal expansion vapor pressure and refractive index of styrene and the density and thermal expansion of polysterene
9. Continous production of polystyrene in a tubular reactor