苯和甲苯硝化及磺化反应热危险性分级研究

首先介绍了化工工艺热安全性的内涵,并从反应过程热危险性分析的方法学出发,介绍间隙、半间歇化学反应工艺热危险性分级研究的总体思路及方法。然后,围绕甲苯和苯的硝化、磺化反应,用全自动反应量热仪(RC1e)和加速度量热仪(ARC)测定其反应过程的绝热温升(△Tad)、目标反应所能达到的最高温度(TM)、分解反应最大速率到达时间(θD)等参数。运用风险评价指数矩阵法(方法1)和基于失控过程温度参数的热危险评估法(方法2)分别对其硝化和磺化反应过程的热危险性进行了分级评估。结果表明,这两种方法具有良好的一致性;给定工艺条件下甲苯和苯的一段硝化反应过程的热危险度等级较低;而磺化反应的热危险较高。尽管这两种方法还有一定的局限性,但对于间歇、半间歇合成工艺的本质安全化设计、工艺热危险性的评估具有重要的参考价值和实用意义。     

过氧化苯甲酰合成工艺热危险性分析

采用RC1e反应量热仪对过氧化苯甲酰(BPO)合成工艺危险性进行研究,测试不同Na OH溶液初始浓度(1.96 mol/L、3.93 mol/L、7.14 mol/L)下反应的放热历程,获得BPO合成反应过程中的热危险性参数,并采用PHI-TECⅡ绝热加速量热仪对产物进行热稳定性分析,最后评估该反应热风险。结果表明,Na OH浓度为7.14 mol/L时,反应初期放热速率慢,热累积度大,后期反应剧烈,绝热温升(ΔTad)及热失控时工艺反应达到的最高温度(MTSR)最大。热稳定性试验表明,合成的粗产物BPO初始分解温度、活化能、指前因子、最大放热速率到达时间为24 h时的对应温度(TD24)均低于纯BPO。利用合成粗产物BPO的TD24对反应进行危险度评估,该工艺热危险性等级均为5级,工艺危险性大。     

反应量热仪RC1在化工热危险性分析中的应用

介绍了一种新型热危险性分析仪器--反应量热仪RC1的设计原理和内部结构,运行模式以及所能获得的温度、传热系数、热转化率、绝热温升、最大合成反应温度等数据类型,并通过阐述其在过程安全、工艺过程开发及优化和基础研究等方面的应用,指出了反应量热仪在化工热安全领域中的特点和优势.     

硝酸甲胺反应过程的安全性研究

用反应量热仪(RC1e)对硝酸溶液与一甲胺溶液在反应过程中的热安定性进行初步研究,分别测试不同反应温度、加料速度和初始硝酸浓度下反应的放热情况。实验结果表明:该中和过程反应迅速,在室温就能进行;与反应温度、加料速度相比,起始硝酸浓度对反应安全性影响最大,且硝酸浓度越高,反应的速度和反应的完全程度也越高。实验还表明:RC1e是研究反应过程中热安定性情况的有效工具,能通过反应过程的热量变化体现反应速率,所得结果对硝酸甲胺的工业化生产具有重要的参考价值。     

混酸中甲苯半间歇硝化过程的危险性研究

为了解甲苯在混酸中硝化的危险性,用差示扫描量热法(DSC)测试甲苯、混酸及一硝基甲苯的热分解情况,用反应量热仪(RC1e)研究搅拌速度、温度及硝酸过用率3因素对目的反应的影响。结果表明,混酸分解温度最低,而当目的反应的3因素出现异常,以及反应过程中发生冷却失效时,均可导致硝化反应体系不稳定,此时若不停止加料,并采取措施,易引起混酸的分解,进一步可引起一硝基甲苯的分解,导致严重后果。     

环己酮半间歇过氧化反应过程热失控研究

采用反应量热仪(RC1e)、差示扫描量热仪(DSC)和绝热加速量热仪(ARC)对环己酮过氧化反应过程的热失控危险性进行了研究,利用冷却失效情形法对该工艺进行危险性分级。结果表明:温度的升高使环己酮过氧化反应速率加快,体系比热容增加,温度升高也使产物各种中间体及副反应活跃程度增加,提高搅拌速度也能促进环己酮氧化,而延长加料时间可以将反应热量较好地移出,但同时降低反应速率,使过氧化环己酮得率降低。依据风险评价指数矩阵法和失控情景分析法,得到环己酮半间歇过氧化反应的热失控危险程度级别为5级,而降低环己酮的加入量,危险程度等级为2级。     

硝酸及氯离子对高温硝酸铵水溶液热危险性的影响研究

国内外学者对硝酸铵的危险性进行了大量的研究,而对其水溶液的危险性至今开展不多。笔者采用差示扫描量热仪(DSC)及全自动反应量热仪(RC1e)对高温状态下的硝酸铵水溶液的热分解危险性、杂质离子对其稳定性的影响进行了研究。纯硝酸铵和90%硝酸铵水溶液的DSC实验表明,90%硝酸铵溶液和分析纯硝酸铵具有相似的热爆炸危险;90%硝酸铵水溶液在140~180℃之间的RC1e试验表明:硝酸或氯离子单独存在时,对硝酸铵分解都有不同程度的抑制作用,而同时存在时则大大降低体系的热稳定性。该结果对保障硝酸铵在生产、使用过程中的安全具有重要的参考价值。     

化学品活性反应危险性表征方法研究

通过对国内外典型活性化学反应事故的研究,在传统和通用的化学反应危险性评价表征方法的基础上,提出使用化学反应的最大功密度表征化学反应热危险性的新方法。该方法将化学反应的热力学参数和动力学参数相结合,全面表征了反应过程的热危险性。采用加速量热仪模拟硝酸铵、过氧化氢,以及多种有机过氧化物的绝热反应放热情况,并运用测得的参数,计算得到其最大功密度,并与传统动力学计算方法得到的结果进行比较。根据对实验和计算结果的分析证明:利用最大功密度的方法评价化学反应的危险性更符合化学反应的实际情况,该方法为化学品安全生产提供可靠的技术支持。     

绝热加速量热仪在化工生产热危险性评价中的应用

本文介绍了一种新型热危险性分析仪器--绝热加速量热仪的设计原理和内部结构,运行模式以及所能获得的温度、压力和最大温升速率时间等数据类型.并通过阐述其在化学动力学研究、自加速分解温度的计算、化学工艺安全性分析和化学工艺过程开发以及热爆炸事故原因调查等方面的应用,指出了绝热加速量热仪在化工生产危险评价方面的特点和优势.     

瞬时功密度在化学品热危险性分析中的应用

采用C80量热仪测定几种化学品的放热反应特性,根据试验数据得到相应的动力学和热力学参数,进一步求得瞬时功密度(ρIPD).依据化学品热不稳定性分级标准对所测定化学品的热危险性进行分级.结果表明,以瞬时功密度为依据得出的化学品热危险程度与化学品的实际危险情况接近,真实、全面地反映了化学品反应过程能量释放的危险程度,可为化学品危险性评价与事故预防提供可靠的技术支持.     

Essential hazard and process safety assessment of para-toluene sulfonic acid through calorimetry and advanced thermokinetics

Para-toluene sulfonic acid is a typical intermediary for the synthesis of pharmaceuticals, pesticides, and dyes and is a catalyst for organic synthesis. The consumption of para-toluene sulfonic acid used in organic synthesis has increased substantially. The toluene sulfonation process is the central path for synthesizing para-toluene sulfonic acid in China. However, the process has risks and has resulted in numerous disasters. This study utilized a reaction calorimeter 1 to reproduce the commercial toluene sulfonation process in a laboratory. The para-toluene sulfonic acid product was examined with an accelerating rate calorimeter and through differential scanning calorimetry. Both differential and integral isoconversional methods were used to determine the thermal stability of and appropriate thermokinetic models for para-toluene sulfonic acid. The safety parameters of para-toluene sulfonic acid were estimated. The research findings can be used for optimization of the toluene sulfonation process and for safe handling of para-toluene sulfonic acid.     

2-氨基-2,3-二甲基丁酰胺氧化合成热危险性研究

为研究2-氨基-23,-二甲基丁酰胺氧化合成的热危险性,采用差示扫描量热仪(DSC)测试2-氨基-2,3-二甲基丁腈和2-氨基-2,3-二甲基丁酰胺的热分解情况,采用反应量热仪(RC1)研究反应温度、双氧水滴加速度和氢氧化钠用量对反应的影响。研究结果显示,2-氨基-2,3-二甲基丁腈吸热热分解温度为149.5℃2,-氨基-2,3-二甲基丁酰胺表现为吸热和放热2段分解过程,吸热和放热分解温度分别为234.4℃和456℃。反应放热速率主要为加料控制,但是,存在一定的热累积。热失控体系最高温度(MTSR)低于2-氨基-23,-二甲基丁腈和2-氨基-23,-二甲基丁酰胺的分解温度,高于体系沸腾温度,在热失控的条件下,反应体系容易导致冲料危险;在优惠的工艺条件范围内,提高反应温度,延长滴加时间,可降低反应的MTSR,提高热转化率和反应安全性。     

Hazard evaluation for chlorination and amination reactions of fluorocytosine production process

Reaction thermal runaway is one of the most important reasons leading to chemical accidents. With the rapid development of the chemical industry in the world, especially the fine chemical industry, various safety accidents also occur frequently. Therefore, it is necessary to study the exothermic behavior of the reaction process. In this study, reaction calorimeter was used to study the exothermic phenomena during the chlorination reaction and amination reaction. Differential scanning calorimetry was performed on the reactants, and thermogravimetric experiments were performed on the products. In addition, adiabatic experiment was performed to study the thermal runaway behavior of amination products under adiabatic conditions. The results showed that the target reactions generated a large amount of heat in the initial stage. The maximum temperature of amination reaction is higher than the initial decomposition temperature of the amination product under adiabatic condition. The pyrolysis of amination product was divided into three stages. The product had a high apparent activation energy at the beginning of decomposition, and the apparent activation energy decreased as the decomposition progressed.     

Thermal decomposition kinetic of liquid organic peroxides

This study demonstrates the application of isothermal calorimeter for investigating the thermal decomposition of several liquid organic peroxides, such as t-Butyl peroxy acetate (TBPA), Di-tert butyl peroxide (DTBP), and Cumene hydroperoxide (CHP). The decomposition mechanism and kinetic can be identified from case to case. TBPA and DTBP undergo first order reaction, whereas CHP occurs autocatalysis. Accurate kinetic can be assessed on the basis of discerning these various schemes of given samples. Consequently, the thermal runaway or reactive hazards potential of organic peroxides can be determined, for instance as a self accelerating decomposition temperature (SADT).     

Numerical simulation of the thermal inertia of an adiabatic reaction calorimeter in reaction thermal safety process

Obtaining accurate thermal risk assessment parameters of chemical processes and substance properties is essential for improving the safety of chemical production and substance use and storage, and the adiabatic reaction calorimeter (ARC) has been employed by many researchers for this purpose. However, with the improvement and upgrading of the instrument, an examination of the factors that affect its detection accuracy is warranted. A simplified reaction model of the adiabatic thermal decomposition of tert-butyl peroxyacetate was constructed using computational fluid dynamics in which the adiabatic thermal decomposition kinetic model and fluid-solid coupling model were combined to simulate heat transfer. To verify the reliability of the parameters of the numerical calculation model, the effects of the sample cell's material, wall thickness, and mass were investigated in relation to the thermal inertia of the ARC. The results indicated that the thermal inertia of the system was lowest when the sample cell was composed of titanium. When the sample pool's composition is determined, the thermal inertia of the system can be reduced to a certain extent through an approximate increase in the sample mass. Finally, an analysis of the heat flow cloud diagram of the wall of sample pools made from different materials revealed that the thermal conductivity of titanium was high; this information can assist in controlling the adiabatic process.