INFLUENCE OF GAS DISTRIBUTOR IN AN INDUSTRIAL FLUIDIZED-BED

被引：0

作者：

ORRANTIA, MEG ^{[1
]}

MATEO, CGC ^{[1
]}

LINARES, EP ^{[1
]}

机构：

[1] INGN TELECOMMUN BILBAO,BILBAO,SPAIN

来源：

ANALES DE QUIMICA | 1994年 / 90卷 / 01期

关键词：

D O I：

暂无

中图分类号：

O6 [化学];

学科分类号：

0703 ;

摘要：

As a consequence of the development and parametrization of a model ad hoc for a fluidized bed industrial furnace for arsenical pyrites roasting, it has been necessary to study the particularities of the grid region. It has been supposed a jet gas flow pre-heating the feed air, to use in the global modelling of the roaster. Being the supposed diameter of the distributor orifice 9.2.10(-3) m, and as the first estimation in the variables initialization, it has been established that the gas starts the reaction at 350-degrees-C and at 8.42.10(-2) m above the distributor.

引用

页码：65 / 79

页数：15

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