在线富集流动注射——火焰原子吸收法测定地面水中痕量CU,Zn,Pb,Cd

利用NP-多胺基磷酸树脂作为浓缩柱,结合流动注射技术,对地面水中痕量的Cu、Zn、Pb、 Cd进行富集,用火焰原子吸收法进行测定,对Cu、Zn、Pb、Cd四种常测重金属元素,本方法的变异系数分别为 2.0％、 3.6％、2.1％和 4.6％。富集倍率可以达到两个数量级,接近石墨炉原子吸收法的灵敏度,有较好的精密度。     

火焰原子吸收分光光度法测定生活垃圾堆肥中镍

通过试验研究,建立了硝酸-氢氟酸-高氯酸消解、火焰原子吸收分光光度法测定生活垃圾堆肥产品中的镍。该方法的检出限为5mg/kg(按称取0.5g试样消解定容至50ml计算),用于不同地域堆肥样品中镍的测定,其相对标准偏差(RSD)均在6.51%以下,加标回收率介于91.2%~102%之间,可作为一种较理想的检验堆肥产品质量的方法。     

管道内火焰加速的模型及其应用

建立了一端密闭、一端敞开且点火源位于密闭端时管道内火焰加速的一个简单模型,其解与试验结果一致。文章还探讨了将其应用于管道自动抑爆系统的可能性。     

铁,镍,锰的火焰塞曼原子吸收分光光度分析

运用火焰塞曼原子吸收对铁、镍、锰等谱线较复杂的元素进行了测定，在实验的基础上，提出了仪器最佳工作条件，并对该分析方法的灵敏度、精密度及准确度进行了探讨。     

水雾抑制气体爆炸火焰传播的实验研究

利用自行设计的全程透明的火焰加速管系统和细水雾实验系统 ,对不同水雾条件下的气体火焰传播现象进行了实验研究。运用光电传感器与CCD摄像技术 ,笔者分析了不同水雾条件下的甲烷预混气体火焰传播速度、传播火焰阵面轨迹 ;探讨了水雾抑制气体火焰传播的机理及条件。实验发现了在一定条件水雾作用下的气体传播火焰阵面拉伸与火焰驻留的现象与条件 ,实验结果表明 :水雾对气体爆炸火焰传播的抑制是由于水雾作用于火焰阵面反应区 ,降低了反应区内火焰温度和气体燃烧速度 ,减缓了火焰阵面传热与传质的进行 ,从而使传播火焰得以抑制 ;而水雾对气体爆炸火焰传播的抑制效果与水雾通量、雾区浓度、水雾区长度以及火焰到达水雾区的火焰传播速度有关     

Explosive properties of selected aerosols determined in a spherical 5-L test chamber

Combustible liquids in the form of aerosols are important for many industrial processes. Therefore the problem of explosion hazards posed by the aerosols becomes increasingly more prominent. To correctly assess the explosion risk and fulfil the requirements of the ATEX directive, it is necessary to obtain information regarding the flammable and explosive properties of the aerosols. Unlike in the case of gases and dusts, no standard procedures aimed at obtaining quantitative information of this type exist. Factors that influence the explosion dynamics of aerosols include: concentration, droplet size, temperature etc. Some of these factors are strongly dependent on the aerosol generation methods. A prototype apparatus was designed and constructed to address that dependence. The apparatus was used in an attempt to determine the basic explosion parameters of liquid flammable aerosols. The device consisted of a 5-L spherical vessel equipped with a pump-injection system that generated aerosols as well as a spark ignition source. A wide variety of injection settings were tested to select the most suitable conditions over a broad range of concentrations and fluid properties. A measurement procedure was developed for operating the device. Prototype tests were carried out with fluids commonly used in industry: isopropanol and kerosene. The tests demonstrated the significant influence of the vessel wall temperature on the result accuracy. Correct temperature control made it possible to obtain relationships between the aerosol concentration and the following explosion parameters: maximum explosion pressure and maximum rate of pressure rise.     

Effects of combined porous media on quenching and re-ignition characteristics of methane/air premixed combustion in a duct

During the study of foam metal suppression of methane combustion in ducts, it was found that under certain conditions, after the flame is extinguished, a re-ignition phenomenon occurs in the area upstream of the foam metal. In this paper, the process and mechanism for the occurrence of this phenomenon were investigated. The porous media used in the experiments is a two-layer structure consisting of a combination of iron-nickel foam and copper foam and was mounted in a transversal position. Each layer of foam metal has a thickness of 5 mm and a pore size of 20 or 40 holes pores per inch (ppi). The results show that flame extinguishment and re-ignition are highly dependent on the material and pore density of the porous media used. After the flame was quenched by the combination of iron-nickel foam with the same pore density of 40ppi, the re-ignition intensity was higher (a dazzling white light could be observed) and the flame area was larger. However, when a combination of iron-nickel foam with different pore densities was used, the re-ignition intensity, flame oscillation frequency and amplitude were significantly lower. However, both re-ignition flames can last for a long time. In addition, the incorporation of copper foam with high thermal conductivity resulted in the decay of flame propagation speed and the overpressure before and after quenching increased significantly with the increase of pore density of the first layer of iron-nickel foam.     

Study on the preparation of novel FR-245/MCM-41 suppressant and its inhibition mechanism on oil shale deflagration flame

Oil shale development is of great significance because oil and gas resources are scarce. Research on the prevention of oil shale dust explosion is particularly important for guaranteeing the safe development and utilization of oil shale resources. In this work, the flame morphology and velocity of oil shale dust with and without MCM-41 or FR-245 were compared. Furthermore, the novel green FR-245/MCM-41 inhibitor was prepared by jet mill method and used in oil shale dust explosion for the first time. The best ratio of FR-245/MCM-41 for flame inhibition was obtained, which was 9: 1. The pyrolysis oxidation behavior of oil shale before and after adding FR-245/MCM-41 was analyzed and compared by FWO and KAS methods, respectively. The results showed that the activation energy calculated by FWO and KAS methods greatly increased after adding FR-245/MCM-41, which increased by 95.36% and 115.15% than that before adding inhibitor, respectively. Significantly, the activation energy is particularly high for two methods when α between 0.2 and 0.6, due to that MCM-41 and FR-245 coexisted to limit the oxidation of oil shale. For α between 0.7 and 0.9, the activation energy is still high because of the existence of MCM-41. Combining the oil dust flame propagation behavior with the characterization results before and after explosion, the physical-chemical synergy mechanism of oil dust flame propagation inhibition was revealed.     

Investigation on the suppression effect of high momentum C6F12O (Novec-1230) flow on hydrogen jet flame

This work investigates the suppression effect of Novec-1230 on H₂ jet flame. The suppressants are motivated by N₂ flow to get higher momentum and approach the reaction kernel at flame base. The flame area with Novec-1230 is always smaller than that with water mist at the same condition. Novec-1230 exhibits better suppression effect on reaction kernel. The higher-momentum jet flame is more difficult to be suppressed. This is because that the higher-momentum flame makes the suppressant approach the reaction kernel more difficult. In addition, the high N₂ flow rate containing suppressant could destroy flame temperature structure and decrease it. Results inferred that the temperature of flame with Novec-1230 is higher than that with water mist. Moreover, the lower minimum extinguishing time indicates that the suppression efficiency of Novec-1230 is better than that of water mist. The jet flame is extinguished only when H₂ flow rate is low and N₂ flow rate is high. There are two reasons: one is that the higher-momentum jet flame prevents suppressants to enter flame core. The other one is that the burner nozzle is heated to as igniting source during suppression progress. Furthermore, the burning velocity, adiabatic flame temperature, heat production and free radicals are investigated theoretically at Φ = 1.6, 1.0, 0.8 and 0.6. Results indicate that the burning velocity with Novec-1230 is much lower than that with water mist. The adiabatic flame temperature, heat production and free radicals increase firstly and then decrease with Novec-1230 addition at lean flame.     

Minimum ignition energy theoretical model for flammable gas based on flame propagation layer by layer

To achieve the rapid prediction of minimum ignition energy (MIE) for premixed gases with wide-span equivalence ratios, a theoretical model is developed based on the proposed idea of flame propagation layer by layer. The validity and high accuracy of this model in predicting MIE have been corroborated against experimental data (from literature) and traditional models. In comparison, this model is mainly applicable to uniform premixed flammable mixtures, and the ignition source needs to be regarded as a punctiform energy source. Nevertheless, this model can exhibit higher accuracy (up to 90%) than traditional models when applied to premixed gases with wide-span equivalence ratios, such as C₃H₈-air mixtures with 0.7–1.5 equivalence ratios, CH₄-air mixtures with 0.7–1.25 equivalence ratios, H₂-air mixtures with 0.6–3.15 equivalence ratios et al. Further, the model parameters have been pre-determined using a 20 L spherical closed explosion setup with a high-speed camera, and then the MIE of common flammable gases (CH₄, C₂H₆, C₃H₈, C₄H₁₀, C₂H₄, C₃H₆, C₂H₂, C₃H₄, C₂H₆O, CO and H₂) under stoichiometric or wide-span equivalence ratios has been calculated. Eventually, the influences of model parameters on MIE have been discussed. Results show that MIE is the sum of the energy required for flame propagation during ignition. The increase in exothermic and heat transfer efficiency for fuel molecules can reduce MIE, whereas prolonging the flame induction period can increase MIE.