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Reactor operating procedures for start up of continuously operated chemical plants

机译:连续运行的化工厂启动的反应堆操作程序

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摘要

Rules are presented for the startup of an adiabatic tubular reactor, based on a qualitative analysis of the dynamic behavior of continuously-operated vapor- and liquid-phase processes. The relationships between the process dynamics, operating criteria, and operating constraints are investigated, since a reactor startup cannot be isolated from an entire plant startup. Composition control of the process material is critical to speed up plant startup operations and to minimize the amount of offgrade materials. The initial reactor conditions are normally critical for a successful startup. For process conditioning, a plant should have an operating mode at which the reactor can be included in a recycle loop together with its feed system and downstream process section. Experimental data of an adiabatic tubular reactor startup and thermal runaway demonstrate some operational problems when such an intermediate operating stage is missing. The derived rules are applied to an industrial, highly heat-integrated reactor section, and the resulting startup strategy is summarized in an elementary-step diagram.
机译:基于对连续操作的气相和液相过程的动态行为的定性分析,提出了绝热管式反应器启动的规则。研究了过程动力学,运行准则和运行约束之间的关系,因为无法将反应堆启动与整个工厂启动隔离开来。工艺材料的成分控制对于加快工厂启动操作并最大程度降低不合格材料的数量至关重要。初始反应器条件通常对于成功启动至关重要。对于过程调节,工厂应具有一种操作模式,在该模式下,反应器及其进料系统和下游过程段可包含在循环回路中。当缺少这种中间操作阶段时,绝热管式反应器启动和热失控的实验数据证明了一些操作问题。所推导的规则将应用于工业,高度热集成的反应堆段,并在基本步骤图中概述了所得的启动策略。

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