Modelling of Resole-type Phenol Formaldehyde Polymerisation in Homogeneous, Continuous-Flow, Stirred-Tank Reactors
โ Scribed by Pal, Pralay K. ;Kumar, Anil ;Gupta, Santosh K.
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 2007
- Tongue
- English
- Weight
- 618 KB
- Volume
- 12
- Category
- Article
- ISSN
- 0007-1641
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โฆ Synopsis
Abstract
The polymerisation kinetics of resoles has been modelled and numerical results obtained for an isothermal, homogeneous, continuousโflow, stirredโtank reactor. The different reactivities of the ortho and para hydrogens on the phenolic rings, both at the โendsโ of polymeric chains as well as at the shielded โinternalโ locations, have been accounted for in the kinetic model and a sensitivity analysis has been carried out. The concentrations of phenol, formaldehyde, various sites, branch points and the numberโaverage chain length are obtained for various values of the rate constants, phenol to formaldehyde ratio in the feed stream and the average residence time in the reactor. It has been observed that the reactivity of the paraโhydrogen atom on an โendโ phenolic ring is the most important parameter.
๐ SIMILAR VOLUMES
The kinetic equations relating to the hydroxymethylation stage in base-catalyzed phenol-formaldehyde condensation have been developed as functions of the free phenol concentration. The same kinetic model was applied to the calculation of a continuous process carried out in a cascade of stirred tank
Mole balance for the molecular weight distribution in homogeneous continuos-flow stirred tank reactors (HCSTRs) for reversible step-growth polymerization has been written. The relation for the moment generating function G is found to be a nonlinear ordinary differential equation and has been solved