SO2在Co—Mo／AC催化剂上的还原

本文研究了活性焦（ＡＣ）担载Ｃｏ－Ｍｏ催化剂对ＳＯ２还原的催化性能。考查了催化剂不同的预处理方法,Ｈ２／ＳＯ２摩尔比和还原温度对还原过程硫产率的影响,并就硫化后的Ｃｏ－Ｍｏ和活性焦在催化床不同的构成对硫产率的影响进行了研究。结果表明,经硫化后的催化剂在ＳＯ２＋２Ｈ２→Ｓ＋２Ｈ２Ｏ反应有较高的催化活性,在最佳反应温度３００℃,Ｈ／ＳＯ摩尔比为３,空速６０００Ｌ;ｋｇ＾－１．ｈ＾－１条件下,生成硫的产     

Regulated emission characteristics of in-use LNG and diesel semi-trailer towing vehicles under real driving conditions using PEMS

On-road driving emissions of six liquefied natural gas(LNG) and diesel semi-trailer towing vehicles(STTVs) which met China Emission Standard IV and V were tested using Portable Emission Measurement System(PEMS) in northern China.Emission characteristics of these vehicles under real driving conditions were analyzed and proved that on-road emissions of heavy-duty vehicles(HDVs) were underestimated in the past.There were large differences among LNG and diesel vehicles, which also existed between China V vehicles and China IV vehicles.Emission factors showed the highest level under real driving conditions, which probably be caused by frequent acceleration, deceleration, and start-stop.NOx emission factors ranged from 2.855 to 20.939 g/km based on distance-traveled and 6.719–90.557 g/kg based on fuel consumption during whole tests, which were much higher than previous researches on chassis dynamometer.It was inferred from tests that the fuel consumption rate of the test vehicles had a strong correlation with NOx emission, and the exhaust temperature also affected the efficiency of Selected Catalytic Reduction(SCR) aftertreatment system, thus changing the NOx emission greatly.THC emission factors of LNG vehicles were 2.012–10.636 g/km, which were much higher than that of diesel vehicles(0.029–0.185 g/km).Unburned CH_4 may be an important reason for this phenomenon.Further on-road emission tests, especially CH_4 emission test should be carried out in subsequent research.In addition, the Particulate Number(PN) emission factors of diesel vehicles were at a very high level during whole tests, and Diesel Particulate Filter(DPF)should be installed to reduce PN emission.     

硝基苯类废水的预处理技术研究

Fe(OH)2对硝基苯具有强烈的还原作用，短时间内可把硝基苯还原为苯胺。催化铁屑法处理硝基苯类废水，除了包括铁屑法处理废水的各种反应外，还能使硝基苯在其表面直接还原，且反应在弱碱性条件下效果较好。m(Fe)：m(Cu)为10：1，pH为9．5，废水硝基苯进水质量浓度为250mg／L，反应时间为30min，硝基苯的去除率达100％。     

La-Na-Co-Mn-O系钙钛矿型催化剂同时去除柴油机碳颗粒和NOx性能的研究

采用低温燃烧法制备了Na+部分取代La3+的La1-xNaxCo0.5Mn0.5O3系钙钛矿型复合氧化物催化剂。利用程序升温反应(TPR)技术,对催化剂应用于柴油机常规排放物中的碳微粒(soot)和氮氧化合物(NOx)的同时催化脱除性能进行了研究。     

有机废气催化燃烧技术

对催化燃烧处理有机废气的基本原理、特点及经济性，以及催化剂、动力学和工艺流程等研究进展进行综述。     

催化分解法处理臭氧尾气的研究

以活性炭和γ -Al2 O3 为载体制备出负载锰和铜氧化物的用于臭氧尾气处理的催化剂 ,并采用固定床反应器进行分解臭氧尾气的实验研究。实验结果表明 ,活性炭负载锰和铜氧化物的催化剂的性能最好 ,1g催化剂在臭氧初始浓度为2 .5 g/m3 ,反应时间为 0 .0 36s条件下 ,其对臭氧的分解率可达 97.2 %。在相同臭氧初始浓度 ,反应时间为 0 .1s条件下 ,1g催化剂可以连续运转达 98h ,处理臭氧总量为 8.8g ,且湿度对其催化活性影响较大。     

糠醛加氢废催化剂的回收再利用

以糠醛液相加氢生产糠醇所用的废铜铬氧化物催化剂为原料，通过与纯碱氧化——钠化焙烧、浸取分离铜铬离子，分别制得铬酸钠和硝酸铜，并以此为原料进一步制得新催化剂，回用于糠醛液相加氢制糠醇。Cr(Ⅲ)与Cu(Ⅱ)的转化率均在90％以上，制得的新催化剂回收率大于85％，使用效果好。研究了铬转化率与焙烧温度、时间、返渣量等条件的关系。     

催化湿法氧化处理垃圾渗滤液中Co/Bi催化剂的回收与再生

利用硝酸盐熔融法制备Co/Bi催化剂,用于催化湿法氧化(CWAO)处理垃圾渗滤液。对一次利用后的 Co/Bi催化剂进行回收和再生,在反应温度260 ℃、催化剂用量 2 g、氧分压 0. 5 MPa条件下,催化剂的回收率可达到(97. 09±0. 74)%。利用XRD、BET分析方法对新鲜制备、一次回收、一次再生、二次回收的催化剂进行表征,根据表征结果可知催化剂的活性为:新鲜制备>一次再生>二次回收>一次回收。利用上述催化剂在不同温度条件下降解垃圾渗滤液,在 280 ℃、300 ℃条件下,催化剂的活性为新鲜制备≈一次再生>一次回收,而在220 ℃、240 ℃、260 ℃条件下,则是新鲜制备>一次再生≈一次回收,表明低温条件下,一次再生的催化剂和一次回收的催化剂出现失活现象,并分析了催化剂失活的原因。     

Advanced treatment of biologically pretreated coal gasification wastewater by a novel heterogeneous Fenton oxidation process

Sewage sludge from a biological wastewater treatment plant was converted into sewage sludge based activated carbon(SBAC) with Zn Cl2 as activation agent, which was used as a support for ferric oxides to form a catalyst(Fe Ox/SBAC) by a simple impregnation method.The new material was then used to improve the performance of Fenton oxidation of real biologically pretreated coal gasification wastewater(CGW). The results indicated that the prepared Fe Ox/SBAC significantly enhanced the pollutant removal performance in the Fenton process, so that the treated wastewater was more biodegradable and less toxic. The best performance was obtained over a wide p H range from 2 to 7, temperature 30°C, 15 mg/L of H2O2 and 1 g/L of catalyst, and the treated effluent concentrations of COD, total phenols,BOD5 and TOC all met the discharge limits in China. Meanwhile, on the basis of significant inhibition by a radical scavenger in the heterogeneous Fenton process as well as the evolution of FT-IR spectra of pollutant-saturated Fe Ox/BAC with and without H2O2, it was deduced that the catalytic activity was responsible for generating hydroxyl radicals, and a possible reaction pathway and interface mechanism were proposed. Moreover, Fe Ox/SBAC showed superior stability over five successive oxidation runs. Thus, heterogeneous Fenton oxidation of biologically pretreated CGW by Fe Ox/SBAC, with the advantages of being economical, efficient and sustainable, holds promise for engineering application.     

Toluene decomposition performance and NOx by-product formation during a DBD-catalyst process

Characteristics of toluene decomposition and formation of nitrogen oxide (NO_x) by-products were investigated in a dielectric barrier discharge (DBD) reactor with/without catalyst at room temperature and atmospheric pressure. Four kinds of metal oxides, i.e., manganese oxide (MnOx), iron oxide (FeOx), cobalt oxide (CoOx) and copper oxide (CuO), supported on Al₂O₃/nickel foam, were used as catalysts. It was found that introducing catalysts could improve toluene removal efficiency, promote decomposition of by-product ozone and enhance CO₂ selectivity. In addition,NO_xwas suppressedwith the decrease of specific energy density (SED) and the increase of humidity, gas flow rate and toluene concentration, or catalyst introduction. Among the four kinds of catalysts, the CuO catalyst showed the best performance in NO_x suppression. The MnOx catalyst exhibited the lowest concentration of O₃ and highest CO₂ selectivity but the highest concentration of NOx. A possible pathway for NOx production in DBD was discussed. The contributions of oxygen active species and hydroxyl radicals are dominant in NOx suppression.