Explosion in a Chemical Plant Producing Methyltris(methylethylketoxime)silane and Vinyltris(methylethylketoxime)silane from 2-Butanone Oxime

Yuchong Gao, Jie Liu, Gending Yu, Lei Wang, Zhikun Huang, Rui Li, Lingzhu Gong, Jiulai Huang, Jiale Huang* and Yih-Shing Duh*, 
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Abstract

On August 3, 2020, a disastrous explosion demolished the Lanhua Organosilicone Ltd. plant in Xiantao county, China, causing six deaths, four injuries, and a loss exceeding US$2 million. We performed an extensive case study with differential scanning calorimetry (DSC) and accelerating rate calorimetry (ARC). The calorimetric methodology can obtain thermal hazard data, such as the exothermic onset temperature, enthalpy change, maximum temperature, maximum self-heat rate, maximum pressure, maximum pressure-rising rate, adiabatic temperature rise, and time-to-maximum rate. The ARC assessed a simulation of the incident vessel by storing the product solution of vinyltris(methylethylketoxime)silane with a thermal inertia of 1.87. The thermal runaway phenomena can be scaled up directly to an industrial vessel with good adiabaticity under such low thermal inertia. An official report announced the time of explosion as 33.2 h, which agreed with the ARC-determined time-to-maximum-rate (TMR) of 28.7 h. A (dT dt–1)max is as high as 801.4 °C min–1, revealing that once the decomposition goes through the critical point, the severe thermal runaway cannot be mitigated or hindered effectively. Therefore, the explosion of the process vessel shows that the maximum pressure under thermal decomposition largely exceeded the design pressure of static tank #1 without adequate relief under overpressure. This paper not only provides a lesson learned for producing chemical products using 2-butanone oxime and alkyl silane but also stands as a guide for an inherently safer processes in similar chemical industries.

Abstract Image

Abstract Image

从 2-丁酮肟生产甲基三(甲基乙基酮肟)硅烷和乙烯基三(甲基乙基酮肟)硅烷的化工厂发生爆炸
2020 年 8 月 3 日,位于中国仙桃县的蓝华有机硅有限公司工厂发生灾难性爆炸,造成 6 人死亡,4 人受伤,损失超过 200 万美元。我们利用差示扫描量热法(DSC)和加速速率量热法(ARC)进行了广泛的案例研究。量热法可获得热危害数据,如放热起始温度、焓变、最高温度、最大自热速率、最大压力、最大压力上升速率、绝热温升和达到最大速率的时间。ARC 评估了通过储存热惯性为 1.87 的乙烯基三(甲基乙基酮肟)硅烷产品溶液对事故容器进行的模拟。在如此低的热惯性下,热失控现象可以直接放大到绝热性良好的工业容器中。官方报告公布的爆炸时间为 33.2 小时,与 ARC 确定的最大速率时间(TMR)28.7 小时相吻合,最大速率(dT dt-1)高达 801.4 ℃ min-1,表明一旦分解超过临界点,就无法有效缓解或阻止严重的热失控。因此,工艺容器的爆炸表明,热分解下的最大压力大大超过了 1 号静压罐的设计压力,而超压下没有足够的泄压措施。本文不仅为使用 2-丁酮肟和烷基硅烷生产化工产品提供了经验教训,而且也为类似化工行业采用更安全的固有工艺提供了指导。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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