加氢催化剂的器外再生

介绍了国内外再生技术的发展状况，对比器内和器外再生技术的优缺点以及催化剂活性恢复率的差异，说明器外再生技术是催化剂再生的发展方向。     

SO_4~（2－）／ZrO_2固体超强酸的失活与再生

初步探索了ＳＯ_４~２－／ＺｒＯ２固体超强酸的失活机理．并着重研究了催化剂的两种再生方法：灼烧法和溶剂洗涤法。催化剂主要是因结焦而失活，高温灼烧能基本恢复催化剂原有活性．且再生效果与灼烧温度有关。溶剂洗涤法有一定的再生能力，但不显著．     

常压脱高硫浅议

就用常压塔脱高硫从流程设置、设备选择、工艺条件控制以及硫回收几方面进行讨论,并着重阐述了脱硫塔、再生槽的设计要求以及吸收、再生、熔硫的工艺条件。     

萃取氧化法再生Pd/C催化剂的研究

通过甲醇用量、回流时间和硝酸浓度对催化剂活性的影响进行了讨论，研究了非那甾胺合成工艺中孕烯醇酮氢化Pd/C催化剂的再生方法。实验发现，对于1 g废Pd/C催化剂，以30 mL甲醇为萃取剂，回流萃取60 min，然后用35%的硝酸在80 ℃氧化30 min，可以达到满意的再生效果，新鲜和再生的Pd/C催化剂孕烯醇酮的氢化转化率分别为97.5%和98.5%。     

重污染阴树脂再生试验研究

通过试验,确定了分离后用盐碱溶液与纯盐酸处理的方法,处理后阴树脂的交换容量达到国标一级品。     

Regeneration of S-poisoned Pd/Al2O3 and Pd/CeO2/Al2O3 catalysts for the combustion of methane

This work investigates the regeneration of S-poisoned Pd/Al₂O₃ and Pd/CeO₂/Al₂O₃ catalysts under different CH₄ containing atmospheres. Under lean combustion conditions in the presence of excess O₂, partial regeneration took place for both systems only above 750 °C after decomposition of stable sulphate species adsorbed on the support. Under alternate lean combustion/CH₄-reducing pulse regeneration is markedly anticipated down to 550–600 °C. Experiments evidenced an effective role of ceria in preventing PdO from sulphation and in promoting regeneration via sulphates decomposition under reducing conditions.     

Advanced oxidant reactivity pertaining to granular activated carbon beds for air pollution control

The Pennsylvania State University is researching an advanced oxidation system, which includes an air-phase photolytic chamber, an air/water stripping tower, and granular activated carbon (GAC) beds, for controlling volatile organic compounds (VOCs).A laboratory-scale experimental procedure has been employed that simulated certain aspects of several full-scale installations. The apparatus has been used to characterize the loading capacity and mass transfer zone of selected VOCs on coconut shell GAC. The GAC bed has then been placed in series with an ultraviolet reactor, which generates ozone and advanced oxidants in order to regenerate the loaded GAC at intensities of advanced oxidants that were higher than full-scale installations.VOC loading tests revealed that the adsorption of methyl isobutyl ketone (MIBK) was characterized by a well-defined mass transfer zone. Upon exposure to UV/O₃, desorption and/or destruction of the MIBK and other VOCs occurred most prominently within the first inch of the GAC bed. This correlated with the penetration of advanced oxidants into the GAC bed, which also occurred most significantly in the bed's first inch. However, the amount of oxidant penetration increased with time. The removal of oxidants from air by GAC was accompanied by a decrease in mass of the GAC. The ability of oxidants to penetrate a GAC bed was altered when the bed was loaded with a VOC.     

废润滑油絮凝—吸附再生工艺的研究

以两种表面活性剂作絮凝剂、活性白土为吸附剂 ,经絮凝、吸附再生处理了废润滑油。考察了影响絮凝、吸附的各种因素。确定最佳絮凝条件 :温度 85°C、1 5 0 g废润滑油所需两种絮凝剂用量分别为 3.7g和 1 .3g;最佳吸附条件 :活性白土 1 2 .3%、温度 1 1 0°C、时间 90 min。经元素分析 ,净化精制后油品的 Zn、Pb、Ca、P等元素的含量显著降低。精制油理化指标符合国家标准。     

去酸水用于钠离子交换树脂再生试验

根据离子交换原理，利用纺丝去酸水代替食盐、芒硝再生钠离子交换树脂，可以去除硬水中的钙离子和镁离子。再生阴床排出碱性废水加入去酸水中，可降低去酸水酸度，提高出水pH，出水水质达到软化水水质标推。用去酸水再生，可减少污染，降低纺丝工艺排水酸度，具有明显的社会效益和经济效益。     

氨分解制氢装置工艺设备的技术改造

介绍了氨分解制氢工艺设备的改进.改造氨汽化器,用蒸汽加热液氨替换电加热液氨;用电加热器直接加热氮气,使分子筛加热再生,改造净化系统.