SO_2和NO在Na-γ-Al_2O_3上的吸附及相互作用

采用固定床连续流动反应器研究423K、常压下SO2和NO在Na-γ-Al2O3上的吸附性能。研究表明,不论是否存在O2,低温下Na-γ-Al2O3均能同时或单独吸附SO2和NO,O2提高了Na-γ-Al2O3吸附或同时吸附SO2和NO的能力。SO2和NO在Na-γ-Al2O3上吸附时存在相互作用,NO可以促进SO2的吸附,而SO2对NO吸附的影响是多方面的,一方面,SO2促进NO氧化转化,使NO吸附量增加,另一方面,SO2促使NO2脱附,降低了NO吸附量。O2促进了SO2和NO间的相互作用。     

安全评价操作实务讲座(五)石油化工行业的安全评价

一、石油化工行业的生产特点 石油化工生产的特点是易燃、易爆、高温、高压.随着工业化生产规模的扩大,工艺技术的不断更新,新设备、新材料、新型催化剂及高效节能设备越来越多地被用于石油化工生产装备中,使得装置的规模越来越大,自动化程度越来越高.石油化工的生产及围绕石油天然气为原料的石油化工生产装置大致如下:炼油生产装置、基本有机合成、合成橡胶、合成树脂及塑料、合成氨及制品、石油化纤等.     

催化剂生产废水铵离子选择交换处理工艺

用铵离子选择交换工艺对催化剂生产过程排出的含氨氮废水进行处理。考察了再生液中NH3－N浓度、进水NH3－N浓度、进水悬浮物浓度、进水pH、再生液用量等因素对处理效果的影响；探讨了铵离子选择交换床液体空速与出水NH3－N浓度的关系、铵离子交换床总交换容量与进水NH3－N负荷之比与出水NH3－N浓度的关系。     

催化剂生产技术产业化研究

简要叙述催化剂生产技术工程化，产业化和生产工艺全过程质量控制，确保产品的一致性和性能稳定性。     

应用故障树法分析γ-Al2O3涂层质量的影响因素

应用故障树分析法，找到导致γ-Al2O3涂层质量不好的18个基本因素。应用故障树分析原理，对这18个因素的结构重要度进行了详细的分析。根据分析结果，结合大量实验数据和事实系统讨论了这18个因素对γ-Al2O3涂层质量的影响程度。研究结果表明，焙烧温度、焙烧时间、造孔剂种类及用量对涂层质量影响最大；应用故障树法分析γ-Al2O3涂层质量的影响因素是可行的，能给实验研究提供一定的理论指导。     

CH-20加氢催化剂的器外再生与工业应用

介绍了中石化长岭分公司300kt/a加氢装置使用的CH-20加氢催化剂器外再生前后催化剂性质对比和再生剂的工业应用情况,说明CH-20加氢催化剂器外再生后,催化剂活性得到了很好的恢复,不仅带来了可观的经济效益和环保效益,而且保证了装置长周期运转.     

炭-催化剂性能对8#滤毒罐防毒性能的影响分析

8~#滤毒罐是专门防护硫化氢气体的防护器材,所装填的药层是炭—催化剂,因此,炭—催化剂性能的优劣决定着滤毒罐防毒时间的长短。也就是说,炭—催化剂性能好,所装填的8~#罐的防毒时间就长;炭—催化剂的性能差,8~#罐的防毒时间就短。 通常,8~#滤毒罐是靠化学吸着作用达到防毒的目的。化学吸着是由吸附质与吸附剂分子之间以类似化学链的力相吸发生的,吸附质与吸附剂形成表面化合物,吸附热较高,有选择性,通常不可逆,炭—催化剂借助于     

OH radicals generated by DC corona discharge for improving the pulsed discharge desulfuration efficiency

Positive DC corona discharge is formed with needle-plate electrode configuration, in which the water vapor is ejected though the needle points. The purpose is to increase the numbers of the water-based radicals, ionize the water molecule and improve the desulfuration efficiency of pulsed corona reactor. The water ions were determined by four stages molecular beam mass spectrometer and diagnose the water-based radicals by emission spectrograph. A conclusion on formation of ions and radicals with DC corona discharges can be drawn.     

Kinetics study on catalytic wet air oxidation of phenol by several metal oxide catalysts

Four metal oxide catalysts composed of copper (Cu), stannum (Sn), copper-stannum (Cu-Sn) and copper-cerium(Cu-Ce) respectively were prepared by the co-impregnation method, and γ-alumina(γ-Al2O3 ) is selected as support. A first-order kinetics model was established to study the catalytic wet air oxidation of phenol at different temperature when these catalysts were used. The model simulations are good agreement with present experimental data. Results showed that the reaction rate constants can be significantly increased when catalysts were used, and the catalyst of 6% Cu-10% Ce/γ-Al2 O3 showed the best catalytic activity. This is consistent witht he result of catalytic wet air oxidation of phenol and the COD removal can be arrived at 98.2% at temperature 210℃, oxygen partial pressure 3 MPa and reaction time 30 rain. The activation energies of each reaction with different catalysts are nearly equal, which is found to be about 42 kJ/mol and the reaction in this study is proved to be kinetics control.