Modeling fouling effects in LDPE tubular polymerization reactors. 1. Fouling thickness determination

被引:34
作者
Buchelli, A
Call, ML
Brown, AL
Bird, A
Hearn, S
Hannon, J
机构
[1] Equistar Chem LP, Lyondell Chem Co, Houston, TX 77536 USA
[2] Performance Fluid Dynam PFD Ltd, Dublin 2, Ireland
关键词
D O I
10.1021/ie040157q
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Fouling in a low-density polyethylene (LDPE) tubular polymerization reactor is caused by the polyethylene/ethylene mixture forming two phases inside the reactor. Some of the polymer-rich phase is deposited on the reactor's inside wall, which considerably reduces heat-transfer rates. At a given reactor pressure, the reactor inside wall temperature is the critical parameter in determining when fouling occurs and this is controlled by the coolant stream temperatures. In this work, plant data and a heat-transfer model were used to determine the fouling thickness in a LDPE industrial reactor and the speed at which the foulant material is deposited.
引用
收藏
页码:1474 / 1479
页数:6
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