膜生物反应器在汽爆稻草秸秆酶解中应用研究

以汽爆稻草秸秆为原料,通过将几个酶解罐串联来提高最终还原糖浓度.考察了酶浓度,酶解单元组成以及稀释率对汽爆稻草秸秆酶解的影响.结果表明,最佳条件为:20FPU/g,酶解单元由4个酶解罐组成,稀释率为0.075/h.在此条件下,酶解时间为24h时,与传统批次酶解相比,汽爆稻草秸秆总转化率从18%～21%提高到39.5%.与只有1个酶解罐的膜反应器相比,每g底物还原糖产量从0.25g提高到0.4g,最终所得还原糖的平均浓度从4.56g/L提高到27.23g/L.     

高炉煤气洗涤水处理方法的研究

采用化学絮凝法处理高炉煤气洗涤水,通过实验确定了最佳的实验条件和工艺条件。     

沸腾液体扩展蒸气爆炸机理及相关计算理论模型研究

剖析了沸腾液体扩展蒸气爆炸 (BLEVE)的发生、发展过程 ,阐述了其机理及相关条件 ,研究并提出了两种BLEVE火球热辐射模拟计算理论模型 ,即近地面和抬升火球模型 ,以及爆炸超压模型。与有关实验结果比较和与已有模型的对比计算表明了所建模型的有效性     

三氯化氮排放槽爆炸事故原因分析及预防处理措施

对某化工厂液氯包装工序三氯化氮排放槽爆炸事故进行了分析 ,提出了预防及处理措施     

气体反溶剂(GAS)过程细化技术及对炸药安全性能的影响研究

介绍了气体反溶剂 (GAS)过程细化技术原理及影响细化结果的主要因素 ,并从理论和实验角度分析了炸药重结晶细化处理后 ,对撞击感度和冲击波感度的影响 ;结果表明 ,GAS过程不仅可以有效地控制炸药颗粒的粒度、粒度分布、晶形 ,而且可以有效降低炸药撞击感度和冲击波感度 ,改善炸药安全性能     

浅谈土锅炉的危害及治理

本文分析了近几年土锅炉的存在原因及爆炸事故,阐述了土锅炉的危害及以预防措施。     

Efficiency of triggered barriers in dust explosion suppression in galleries

The paper describes large-scale tests of triggered barriers of different design. Main stress was put on examining suitability of the flame detector developed in US Bureau of Mines to work as a trigger for the barriers. It was found that the detector works satisfactorily with the barriers of different design providing a suitable mean to suppress explosions in galleries, either in mines or in other industries.     

Evaluation of the explosibility of malt grain dust based on static electrification during pneumatic transportation

The possibility of dust explosions by static electricity in a malt grain silo was investigated. Two kinds of experimental equipment were applied. One was to supply electrostatic charge in order to investigate the charge build up characteristics. The other was to transport the malt grain pneumatically in order to investigate the frictional charge accumulation in the transportation system.

The particle charge of the pulverized malt grain was in the order of 10⁻¹⁴ C. The particle charge of the malt grain was in the order of 10⁻⁹ C and the pipe charge in the transport system was also in the order of 10⁻⁹ C. The charge accumulated on both the pulverized particle and the grain particle were small in view of the incendiary potentiality. However, attention must be paid when the particles are dumped into isolated space. There might be a charge accumulation that will lead to the ignition of the dust cloud.     

Ignition wave in a two-velocity two-temperature multiphase mixture

The theory of stationary adiabatic and non-adiabatic ignition waves in magnesium aerosuspension is developed on the basis of the mathematical model based on two-velocity two-temperature approach of mechanics of heterogeneous media. Specifically, the conditions such that the particle cloud ignites under the action of an initiating shock wave (SW) are defined. An agreement between the adiabatic one-velocity model and the adiabatic two-velocity model on the ignition delay time for small particles is shown. Influence of particle size on this characteristic is compared for both models. Validation of the two-velocity model is performed on the basis of comparison with the experimental data. The unified formula for calculation of the induction period of the magnesium particle mixture in oxygen which takes into account its dependence on the SW Mach number and particle radius is found.     

Effects of a carbon monoxide-dominant gas mixture on the explosion and flame propagation behaviors of methane in air

This work aimed to experimentally evaluate the effects of a carbon monoxide-dominant gas mixture on the explosion characteristics of methane in air and report the results of an experimental study on explosion pressure measurement in closed vessel deflagration for a carbon monoxide-dominant gas mixture over its entire flammable range. Experiments were performed in a 20-L spherical explosion tank with a quartz glass window 110 mm in diameter using an electric spark (1 J) as the ignition source. All experiments were conducted at room temperature and at ambient pressure, with a relative humidity ranging from 52 to 73%. The peak explosion pressure (P_max), maximum pressure rise rate ((dp/dt)_max), and gas deflagration index (K_G) were observed and analyzed. The flame propagation behavior in the initial stage was recorded using a high-speed camera. The spherical outward flame front was determined on the basis of a canny method, from which the maximum flame propagation speed (S_n) was calculated. The results indicated that the existence of the mixture had a significant effect on the flame propagation of CH₄-air and increased its explosion risk. As the volume fraction of the mixed gas increases, the P_max, (dp/dt)_max, K_G and S_n of the fuel-lean CH₄-air mixture (7% CH₄-air mixture) increase nonlinearly. In contrast, addition of the mixed gas negatively affected the fuel-rich mixture (11% CH₄-air mixture), exhibiting a decreasing trend. Under stoichiometric conditions (9.5% CH₄-air mixture), the mixed gas slightly lowered P_max, (dp/dt)_max, K_G, and S_n. The P_max of CH₄-air mixtures at volume fractions of 7%, 9.5%, and 11% were 5.4, 6.9, and 6.8 bar, respectively. The S_n of CH₄-air mixtures at volume fractions of 7%, 9.5%, and 11% were 1.2 m/s, 2.0 m/s, and 1.8 m/s, respectively. The outcome of the study is comprehensive data that quantify the dependency of explosion severity parameters on the gas concentration. In the storage and transportation of flammable gases, the information is required to quantify the potential severity of an explosion, design vessels able to withstand an explosion and design explosion safety measures for installations handling this gas.