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首页> 外文期刊>Journal of loss prevention in the process industries >CFD simulation of shortstopping runaway reactions in vessels agitated with impellers and jets
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CFD simulation of shortstopping runaway reactions in vessels agitated with impellers and jets

机译:用叶轮和射流搅动的容器中的速动失控反应的CFD模拟

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摘要

Runaway reactions are continuing to be a problem in the chemical industry. A recent study showed that 26% of our major chemical plant accidents are due to runaways. The consequences of runaway reactions are usually mitigated with (a) reliefs and containment systems or (b) shortstopping (reaction inhibition). This study covers the concept of shortstopping. One of the major reasons for runaways is power failure. In the advent of a power failure, mixing an inhibiting agent with the reactor contents is challenging. However, jets or impellers driven by a small generator can be used for mixing. This study compares shortstopping results in vessels agitated with jets and impellers using computational fluid dynamics (CFD). A commercial CFD code, Fluent is used. For shortstopping systems relying on jet mixing, angle and diameter of jet nozzle and jet velocity are the key design/operating parameters. For the systems with impellers, type, size and RPM of impeller are the key parameters. In this work, mixing with a jet mixer is first investigated for three nozzle diameters and two angles of injection. The best jet mixer configuration on the basis of mixing time is used for shortstopping studies. The simulated shortstopping results with the jet mixer are then compared with those obtained with impeller (Rushton and pitched blade turbine) stirred vessels. Our results identify the conditions for effective shortstopping; i.e., agitation requirements, locations for adding the inhibitor, and the quantity of inhibitor. The distribution of excess inhibitor is shown to be an important and essential design criterion for effective shortstopping when using impeller stirred vessels. The comparative study with a single jet shows that jet mixer is ineffective when used for shortstopping. Efforts such as adding excess inhibitor and inhibition with higher reaction rates at the same power, proved to be ineffective when using jet mixer compared to the results with impellers.
机译:在化学工业中,失控反应仍然是一个问题。最近的一项研究表明,我们主要的化工厂事故中有26%是由于失控所致。失控反应的后果通常可以通过(a)泄压和围堵系统或(b)短时制(反应抑制)来减轻。这项研究涵盖了捷径的概念。失控的主要原因之一是电源故障。在停电的到来中,将抑制剂与反应器内容物混合是具有挑战性的。然而,由小型发电机驱动的射流或叶轮可用于混合。这项研究使用计算流体力学(CFD)比较了在有射流和叶轮搅动的容器中的速止结果。使用商业CFD代码Fluent。对于依赖喷射混合的短停系统,喷射喷嘴的角度和直径以及喷射速度是关键的设计/操作参数。对于带有叶轮的系统,叶轮的类型,尺寸和RPM是关键参数。在这项工作中,首先研究了使用喷射混合器进行混合的三个喷嘴直径和两个喷射角度。基于混合时间的最佳喷射混合器配置用于短时停止研究。然后,将使用喷射混合器的模拟速降结果与通过叶轮(Rushton和变桨涡轮)搅拌容器获得的结果进行比较。我们的结果确定了有效的短途终止的条件;即搅拌要求,添加抑制剂的位置和抑制剂的量。过量抑制剂的分布被证明是使用叶轮搅拌容器时有效缩短流量的重要和必不可少的设计标准。对单喷嘴的比较研究表明,喷射混合器用于短停时是无效的。与使用叶轮的结果相比,当使用喷射混合器时,诸如添加过量的抑制剂和在更高的反应速率下以更高的反应速率进行抑制的努力被证明是无效的。

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