Kinetics of selective catalytic reduction of NO by NH3 on Fe-Mo/ZSM-5 catalyst

The catalyst of Fe-Mo/ZSM-5 has been found to be more active than Fe-ZSM-5 and Mo/ZSM-5 separately for selective catalytic reduction (SCR) of nitric oxide (NO) with NH3. The kinetics of the SCR reaction in the presence of O2 was studied in this work. The results show that the observed reaction orders were 0.74-0.99, 0.01-0.13, and 0 for NO, O2 and NH3, respectively, at 350-450℃. And the apparent activation energy of the SCR was 65 kJ/mol on the Fe-Mo/ZSM-5 catalyst. The SCR mechanism was also deduced. Adsorbed NO species can react directly with adsorbed ammonia species on the active sites to form N2 and H2O. Gaseous O2 might serve as a reoxidizing agent for the active sites that have undergone reduction in the SCR process. It is also important to note that a certain amount of NO was decomposed directly over the Fe-Mo/ZSM-5 catalyst in the absence of NH3.     

吸附法油气回收装置中真空泵的安装与调试

简要介绍了济南分公司油气回收装置、真空泵的工作原理以及安装与调试应注意的问题.     

铅在棉秆基活性炭上的吸附动力学与热力学

以棉秆与棉秆纤维为原料,利用磷酸活化法制备了低成本的高比表面微孔棉秆基活性炭,通过静态实验研究了活性炭对水溶液中铅的吸附特性,测定了溶液pH值、吸附时间、溶液温度对吸附的影响,探讨了吸附动力学、热力学及吸附机制.根据低温液氮(N2/77K)吸附测定数据,以BET方程、BJH法及H-K法对活性炭孔结构进行了表征,以Boehm滴定、FTIR、零电荷点pHPZC测定及元素分析定量表征活性炭表面含氧官能团.结果表明,以棉秆和棉秆纤维为原料制备的活性炭的比表面积分别为1570和1731m2·g-1,含氧酸官能团含量分别为1.43和0.83mmol·g-1,均高于商业活性炭ST1300.静态吸附实验表明,棉秆基活性炭对铅有较大的吸附容量和吸附效率,最大吸附量超过120mg·g-1,溶液pH对吸附有较大的影响,吸附量随时间增大而增大,在5min内可达饱和吸附量的80%;吸附动力学数据符合假二级方程,Freundlich方程能更好地描述等温吸附行为;热力学研究表明,吸附吉布斯自由能(ΔG0)0,而焓变(ΔH0)0,说明吸附为吸热的自发反应过程,升温有利于吸附,离子交换可能在吸附过程中起了重要作用.     

Antimicrobial activity of thin metallic silver flakes, waste products of a manufacturing process

The aim of the research was to develop new products and processes from a manufacturing waste from an Italian metallurgic company. The company produced thin silver metallic films and the production scraps were silver flakes. The possibility to use the silver flakes in water disinfection processes was studied. The antimicrobial activity of the flakes was investigated in batch using Escherichia coli as Gram-negative microorganism model. The flakes did not show any antimicrobial activity, so they were activated with two different processes: thermal activation in reducing atmosphere and chemical activation, obtaining, respectively, reduced flakes (RF) and chemical flakes (CF). The flakes, activated with either treatment, showed antimicrobial activity against E. coli. The kill rate was dependent on the type of activated flakes. The chemical flakes were more efficient than reduced flakes. The kill rate determined for 1 g of CF, 1.0 ± 0.2 min⁻¹, was greater than the kill rate determined for 1 g of RF, 0.069 ± 0.004 min⁻¹. This was confirmed also by the minimum inhibitory concentration values. It was demonstrated that the antimicrobial capability was dependent on flakes amount and on the type of aqueous medium. Furthermore, the flakes maintained their properties also when used a second time. Finally, the antimicrobial activities of flakes were tested in an effluent of a wastewater treatment plant where a variety of heterotrophic bacteria were present.     

微波酸活化粉煤灰吸附酸性大红染料废水实验研究

以微波酸活化改性后的粉煤灰为吸附剂,对酸性大红染料废水进行吸附脱色处理,考察了吸附时间、pH值、吸附剂投加量等对吸附脱色效果的影响。在酸性大红染料溶液初始浓度为100 mg/L、pH=5、活化粉煤灰投加量为10 g/L吸附1 h时,活化粉煤灰对酸性大红的脱色效果较好,去除率可达96%。对实验数据进行相关数学模型拟合,结果表明微波酸活化改性后的粉煤灰吸附去除酸性大红的等温吸附平衡符合Langmuir吸附等温式,改性前后的吸附过程动力学符合准二级吸附动力学模型,线性相关系数良好。     

桥式起重机典型事故分析及安全管理

分析了桥式起重机典型事故发生机理,运用事故树分析法对桥式起重机事故发生进行了分析,从而为能够找出安全隐患,制定出最优的控制措施提供了理论上的依据.最后根据分析结果,系统地提出了控制危害,降低事故发生率的安全管理措施,提出一些具有可行性的建议.     

FTA和FMECA综合法对常压炉的风险分析

首先对炼油厂的常压炉系统进行了火灾爆炸事故的FTA分析,在此基础上进行了深入的FMECA分析,绘制出分析表格,并提出将这两种方法结合起来应用的优点以及一般步骤.综合两种分析方法深入分析了引起火灾爆炸事故的原因,指出系统运行的潜在危险因素,根据分析结果提出综合性的安全改进和预防措施.     

小型露天采石场爆破作业安全评价方法的探讨

应用安全检查表、事故树、作业条件危险性分析等方法对露天小型采石场爆破作业进行了分析评价,找出了导致爆破作业事故发生的可能因素及可采用的预防途径,为小型露天爆破作业事故的预防提供有益参考.     

单芯铜线过电流故障电弧熔痕的微观特征研究*

为准确认定电气火灾中过电流故障,模拟4~7倍额定电流（Ie）条件下单芯铜导线过电流故障,利用光学显微镜和扫描电子显微镜（SEM）分析过电流故障电弧熔痕的组织特征,并结合Image-Pro Plus软件测定晶粒直径、周长和面积,探究金相组织的量化判据和变化规律。结果表明:当I＝4Ie时,过电流故障电弧熔痕的金相组织主要为方向性较强的树枝晶;当I＝5Ie,6Ie时,金相组织内树枝晶占比减小,胞状晶占比升高;当I＝7Ie时,方向性较弱的胞状晶占主导。随着电流增加,晶粒的平均直径、周长和面积均呈增长趋势。通过火灾案例分析可知,实验结果与现场的电弧熔痕组织特征基本相符,验证火灾事故原因为过电流故障。     

肥煤自燃全过程热动力学特征参数研究

实验测定了林西矿肥煤样品30~900℃煤自燃全过程热动力学特征参数,得出:TG/DTG曲线显示煤样DTG初始临界温度45℃,干裂温度122℃,活性温度195℃,增速温度265℃,质量极大值温度342℃,着火温度465℃,最大热失重速率温度515℃和燃尽温度690℃;DSC曲线显示,煤样初始放热温度60℃、最大热释放速率温度511℃。结合TG-DTG-DSC曲线综合分析可知,煤温达到510℃左右时煤样反应最剧烈。由煤自燃标志气体测定实验系统得出:煤温130℃后CO,CO 2释放量迅速增加,210℃增加速度下降;CH 4,C 2 H 6含量变化具有规律性且两者变化相近;C 2 H 4出现温度为130℃;C 2 H 4/C 2 H 6比值在190~350℃有较强的规律性,呈上升趋势且上升速度较快;350℃之后,CH 4,C 2 H 6,C 2 H 4体积分数均开始急剧增大;C 2 H 4/CO与C 2 H 4/CO 2变化趋势大致相同,在130~350℃时缓慢增长,达到350℃后比值呈指数形式上升。经拟合曲线,得到活化能的3个突变点温度:70,180,220℃,其中180℃与交叉点温度相吻合。通过以上研究,得到了肥煤自燃全过程的热力学特征参数,为实际生产中防治煤自燃提供了理论依据。