紫外光降解反应器去除氯苯气体模型的建立与应用

从光化学反应过程出发,基于线性光源球面辐射能量分布（LSSE）,以反应器内部空间的辐射能吸收密度、空塔停留时间、进口浓度等为主要参数,建立了气相环境中紫外光化学反应器去除氯苯的数学模型.结果表明,建立的模型能很好地模拟和预测紫外光化学反应器对氯苯气体的去除性能.氯苯气体的紫外光化学反应表现出一级反应动力学的特征.该模型包含了紫外光降解反应器设计的主要参数,同时被用于预测了反应器在不同进口浓度和不同空塔停留时间条件下的出口氯苯浓度,进而获得不同进口浓度达标排放所需要的最小空塔停留时间,为气相污染物的紫外光降解反应器的设计与运行提供了重要的理论指导.     

气溶胶质谱仪在研究有机气溶胶环境微界面过程中的应用

有机气溶胶非均相和多相反应是复杂的微界面过程,它涉及气体的吸附、扩散、反应和解吸,传统的化学分析仪器不能提供完整实时的微界面过程的化学反应信息.气溶胶质谱仪是近年来发展起来用于实时分析颗粒物化学组分的重要仪器,它弥补了传统化学分析仪器,如GC/MS在实时分析上的不足,为研究有机气溶胶非均相化学反应的微界面过程提供了新的方法.本文旨在介绍气溶胶质谱仪的结构及其在研究有机气溶胶环境微界面过程中的应用.     

零价铁（ZVI）去除Cu2+的特性及机制研究

研究了零价铁去除水溶液中铜离子的影响因素及动力学特性,并利用X射线衍射(XRD)分析对反应机制进行了探讨.结果表明,当溶液中Cu2+的浓度为300 mg/L,零价铁的用量为1 g/L时,Cu2+的去除率99%.Cu2+的去除速度很快,且反应前30min零价铁去除Cu2+的过程可以用一级反应动力学方程模拟.零价铁去除Cu2+的机制主要基于氧化还原反应,Cu2+的还原产物主要为Cu和Cu2O.     

Evaluation of multiple reactions in dilute benzoyl peroxide concentrations with additives using calorimetric technology

Benzoyl peroxide (BPO) is a typical organic peroxide widely used in food processing, particularly flour bleaching. Due to the unstable nature of the oxygen-oxygen bond in BPO, it readily reacts under even mid-low-temperature conditions. Lower concentrations of BPO are also potentially explosive, even when combined with acid or alkaline additives. Given the history of both potential and documented industrial accidents, this study investigates the thermal stability of various BPO concentrations when mixed with acid or alkaline solutions. In addition, differential and integral kinetic models were applied to verify that the apparent activation energy data from the differential scanning calorimetry experiments were valid. The results of autocatalysis reactions and nth-order reaction simulations presented characteristics consistent with the experimental findings. The findings in this paper can be used as a reference for BPO products that are mediated with either an acid or an alkaline solution during production, storage, transportation, or use.     

Assessment of the effect of technical and management characteristics on the frequency of release from piping: An application to a gas storage facility

The assessment of the frequencies of release from piping due to losses of containment is an essential step in the preparing Safety Reports, drawn up as required by the so-called “Seveso” Directive. These are usually calculated starting from the frequencies of random rupture included in international databases and are not plant-specific, furthermore, the quantification of the effect of the safety management system of the facility is not easy. A simple and flexible approach quantifying technical and management characteristics of the plant has been proposed by Milazzo and co-workers in 2010; it is based on the modification of the frequency taken from literature, through the use of the percentages of failure causes actually possible in that plant, and the judgment about their management. The data about the failure causes are taken from the literature and modified by using corrective factors to adapt them to the industrial context. To make possible the application of the method to a large number of major-hazard industry types, some aspects of the approach needed to be improved; these have been identified during a development project coordinated by RINA Consulting, on behalf of Saipem, with the collaboration of the University of Messina. The improvement of the approach focused on two main points, the development of a method to calculate the corrective factors for the failure causes associated with corrosion and erosion phenomena and the strengthening of the methodology for the formulation of the judgment about the safety management. This paper illustrates the fully improved method, as well as an application to a typical gas storage plant.     

Experimental study on detonation flame penetrating through flame arrester

In-line detonation flame arresters are important safety apparatus to prevent group tank fires caused by the spreading of fire through vapor connection lines. In this study, a DN50 experimental apparatus aimed at the detonation flame penetration characteristics and failure mechanisms in a flame arrester was set up, and a series of experiments were carried out with 6.6% C2H4 and air mixture. Pressure, and velocity of flame penetrating through flame arrester housing and filters were analyzed. Experimental results showed that the attenuation of pressure and velocity was proportional to the thickness of the filters. Two failure modes of the fire-extinguishing process in the flame arrester were captured directly with a high-speed camera. In Mode I, the detonation flame could go straight through the flame arrester filters when the filters were too thin. In Mode II, when the filters were not sufficiently thick, the remained shock wave pressure of detonation flame was still several times of the initial pressure and could rise sharply at the downstream contraction section, resulting in that the flammable gas at the downstream transition section could be compressed and reignited even the flame had been extinguished by filters. These conclusions are helpful to reveal the nature of failure modes of fire-extinguishing process and design flame arresters with high fire-resisting performance by structure improved.     

PAN dust explosion inhibition mechanisms of NaHCO3 and Al(OH)3

We investigate the PAN dust explosion inhibition behaviors of NaHCO₃ and Al(OH)₃ in a 20 L spherical explosion system and a transparent pipe explosion propagation test system. The results show that, in the standard 20 L spherical explosion system, the highest PAN dust explosion concentration is 500 g/m³, the maximum explosion pressure is 0.661 MPa, and the maximum explosion pressure increase rate is 31.64 MPa/s; adding 50% NaHCO₃ and 60% Al(OH)₃ can totally inhibit PAN dust explosion. In the DN0.15 m transparent pipe explosion propagation test system, for 500 g/m³ PAN dust, the initial explosion flame velocity is 102 m/s, the initial pressure is 0.46 MPa, and the initial temperature is 967 °C; adding 60% NaHCO₃ and 70% Al(OH)₃ can totally inhibit PAN dust explosion flames. Through FTIR and TG analyses, we obtain the explosion products and pyrolysis patterns of the explosion products of PAN dust, NaHCO₃, and Al(OH)₃. On this basis, we also summarize the PAN dust explosion inhibition mechanisms of NaHCO₃ and Al(OH)₃.     

考虑驾驶员反应时间的车辆碰撞预警模型

为了保证车辆在行驶过程中的安全性,提出了一种考虑驾驶员反应时间的车辆碰撞预警模型,改进了传统模型中驾驶员反应时间定值化的缺点。首先,依据车辆的制动过程分析了驾驶员反应时间对制动距离的影响。其次,设计驾驶员反应时间的模糊推理算法,选取驾龄、疲劳强度和应变能力3个主要因素作为评价指标来计算反应时间。最后,采用分等级的预警策略建立考虑驾驶员反应时间的碰撞预警模型,并通过Carsim-Matlab/Simulink联合仿真与传统模型进行对比分析。结果表明,设计的预警模型可以对不同类型的驾驶员进行差异化碰撞预警,在30 km/h和80 km/h两种车速下实际停车距离与理论值的最大误差为8%。     

响应曲面法优化镍转炉渣氧压选择性浸出工艺

为了优化镍转炉渣加压条件下H₂SO₄选择性浸出Co、Ni、Cu,抑制Fe浸出的工艺,采用响应曲面法的中心组合设计原理,建立影响选择性浸出率的二次多项式数学模型,研究浸出温度、c(H₂SO₄)及液固比及上述因素两两交互作用对提高Co、Ni、Cu浸出率及减少Fe浸出率的影响规律. 结果表明:浸出温度和c(H₂SO₄)对浸出率影响最显著,液固比次之. c(H₂SO₄)越高,Co、Ni、Cu和Fe的浸出率越高,而提高浸出温度有利于降低Fe浸出率. 响应曲面法优化获得的最佳工艺条件:浸出温度为210 ℃、c(H₂SO₄)为0.38 mol/L、液固比为4.25 mL/g,在该条件下,Co和Ni的浸出率均大于98%,Cu浸出率大于96%,Fe浸出率小于0.4%. 浸出控制参数优化后提高了有价金属的浸出率,同时也降低了Fe浸出率,实现了镍转炉渣中有价金属的回收及其与Fe的高效分离.