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1.
多釜串联实验有利于理解多釜串联反应器的返混特性、停留时间分布与多釜串联模型的关系、模型参数的物理意义、模型参数的计算方法和停留时间分布的测定方法。该改进设计加入了一个并行的大釜对照反应器,能使学生更直观地了解系统的流动特性,理解多釜串联模拟理想反应器的实际意义。相比单理想反应器,多釜串联模拟是在较高浓度下进行的,减少了混合作用所产生的稀释效应,使过程的推动力得以提高。 相似文献
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采用热重-质谱法(TG-MS)和热解-气相色谱法(Py-MS)相结合的方法对模型化合物(十四硫醇、二丁基硫醚、苯硫醚、二甲基噻吩、苯并噻吩和二苯并噻吩等)在惰性气氛下硫的脱除及释放行为进行研究。惰性气氛下硫的脱除顺序为:十四硫醇>二丁基硫醚>二甲基噻吩>苯并噻吩>苯硫醚>二苯并噻吩,苯硫醚除外,该顺序与含硫官能团的热分解顺序一致。在热解过程中,所有模型化合物在质谱和气相色谱仪上均被检测到SO2;除苯硫醚和二苯并噻吩外,其他模型化合物中均检测到了COS;而只在十四硫醇、二丁基硫醚和二甲基噻吩中检测到了H2S。且热解气中SO2含量要显著高于H2S和COS。这是由于活性炭作载体时,惰性气氛下内部氢的含量显著小于内部氧的含量,所以大多数的含硫自由基易与内部氧结合以SO2的形式逸出。对于苯硫醚、苯并噻吩和二苯并噻吩中没有检测到H2S,是由于内部氢的不足,使得含硫自由基不能与内部氢结合,所以没有检测到H2S逸出。 相似文献
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La掺杂 BiFeO3对苯酚光催化降解性能的影响 总被引:2,自引:0,他引:2
苯酚是一种稳定、毒性大且难降解的有机物,对人类和生态环境产生很大威胁,因此急需研发出能有效移除工业废水中苯酚污染物的方法.其中,绿色、高效的光催化氧化技术得到研究人员青睐.在半导体光催化剂中, BiFeO3具有带隙窄(2.2–2.5 eV)、化学稳定性好及成本低等优点,被看作是最有潜力的光催化剂.但是, BiFeO3存在光生电子空穴对复合率高,制备过程中易形成杂质相的缺点,使得其光催化活性很差,限制了 BiFeO3在光催化领域的应用.异种离子的引入能产生杂质能级或裁剪半导体带隙,同时促进光生载流子分离,故可考虑采用离子掺杂改性 BiFeO3的手段来抑制杂质相生成,提高载流子分离,从而提高 BiFeO3的光催化性能.本文以柠檬酸为络合剂,通过一步溶胶凝胶法合成了系列样品 Bi1-xLaxFeO3(摩尔分数x =0,0.10,0.15,0.20).通过 X射线衍射(XRD)、扫描电镜(SEM)、能谱(EDS)、透射电镜(TEM)、X射线光电子能谱(XPS)、紫外可见漫反射(UV-Vis DRS)及荧光光谱(PL)等手段对不同样品的物相、形貌、表面价态和光学性能进行了表征.并通过活性物种捕获实验和羟基自由基(?OH)产生实验分析了 Bi0.85La0.15FeO3样品在苯酚降解过程中的主要活性物种和降解机理.相对于单相 BiFeO3, La改性 BiFeO3催化剂的光降解苯酚性能均有提高,其中 La最佳掺杂量为0.15.在模拟太阳光下照射180 min后, Bi0.85La0.15FeO3的光催化活性达到96%,同时 COD去除率达到81.53%,并表现出好的循环使用活性和稳定性.研究发现,该光催化过程中主要的活性物种为?OH. XRD, SEM, TEM和 EDS结果表明, La元素掺杂进 BiFeO3结构中,且各元素分布均匀,同时,适量 La元素掺杂能有效抑制杂质相 Bi25FeO40的形成,而且 La掺杂 BiFeO3样品的颗粒尺寸略有减小,有利于电子空穴转移. XPS显示, La改性 BiFeO3样品的表面有氧空位形成,将有利于有机物的吸附和降解;另外,羟基氧和吸附氧含量增大,有利于活性氧物种形成. UV-Vis DRS和 PL测试证明, La改性后的样品对可见光的响应增强,样品带隙变窄,产生杂质能级,抑制了光生载流子复合,有利于产生更多载流子来促进活性物种形成,从而提高光催化活性.氧物种捕获实验说明,在 Bi0.85La0.15FeO3参与的苯酚降解过程中的主要活性物种是?OH,同时?OH的产生实验也证明了在光照下?OH在 Bi0.85La0.15FeO3光催化剂表面持续产生,并提出了光催化降解机理. 相似文献
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Combustion catalysts La0.8Sr0.2MnO3 supported on γ-Al2O3, α-Al2O3, cordierite (2MgO•2Al2O3•5SiO2) and ZrO2 were compared. Further investigation was focused on LSM/ γ-Al2O3 catalyst. It was observed that LSM/γ-Al2O3 catalyst loaded with 20% (mass fraction) LSM (La0.8Sr0.2MnO3 or corresponding oxides), heated at 750℃ or above, perovskite-type oxides were found by XRD examination, whereas, the same catalyst loaded with 10% or less LSM, perovskite oxides were absent, calcination temperature about 750℃ is necessary for the formation of perovskite structure in LSM/γ-Al2O3 catalysts. High activity of complete oxidation of xylen will be obtained when perovskite-type oxides.
Investigation of TPR showed that neat LSM or LSM/γ-Al2O3(20%) was reduced by H2-N2 mixed gas. Two degradation processes took place. In the first, reduced temperature peak was about 350 - 450℃. If reduction ended at 400℃, perovskite structure was retained, which may be due to the reduction of Mn3+to Mn2+ on the surface of LSM only. In the second process, perovskite structure was destroied, and La2O3, Mn2O3, Mn - Sr - O oxides could be obtained, which took place in the temperature range 685 - 750℃ and ended at 800℃. This was proved by TPR experiments (Fig. 3, 5) and XRD patterns (Fig. 4)
Catalysts LSM/γ-Al2O3(10% or 20%) heated at 500℃ have only one TPR peak, i. e. lower temperature peak. This is due to the absence of perovskite-type oxides in the catalysts. However, neat LSM or LSM/γ-Al2O3(20%) heated 750℃ or above, not only the first low temperature TPR peak but also the second peak, which is contributed by the perovskite-type oxides in these catalysts appeared. Therefore, the second TPR peak, i. e. the higher temperatue peak is a characteristic peak for perovskite-type oxides in the reduced process. When LSM/ γ-Al2O3 (10%) catalys is heated at 750℃, no perovskite-type oxides were detected by XRD, and the second reduction peak was absent also in TPR process. \
The order of the second reduction peak temperature(characteristic peak of perovskite - type ox- ides) is: neat LSM(750℃)> LSM/γ-Al2O3 20% (685-698℃) -deposited LSM/γ-Al2O3 (698℃) > LSM/γ-Al2O3 15% (677 - 680℃) >(LSM/γ-AL2O3 10% 620 - 630℃, for Mn - Al - O medium oxides on surface). It is correleted with the increasing of the effect of support sequentially.
When LSM/γ-Al2O3 catalysts were heated at 900℃, more stable phase, spinel MnAl2O4 appeared, which could be proved by TPR of model catalyst MnAl2O4/γ-Al2O3. 相似文献
Investigation of TPR showed that neat LSM or LSM/γ-Al2O3(20%) was reduced by H2-N2 mixed gas. Two degradation processes took place. In the first, reduced temperature peak was about 350 - 450℃. If reduction ended at 400℃, perovskite structure was retained, which may be due to the reduction of Mn3+to Mn2+ on the surface of LSM only. In the second process, perovskite structure was destroied, and La2O3, Mn2O3, Mn - Sr - O oxides could be obtained, which took place in the temperature range 685 - 750℃ and ended at 800℃. This was proved by TPR experiments (Fig. 3, 5) and XRD patterns (Fig. 4)
Catalysts LSM/γ-Al2O3(10% or 20%) heated at 500℃ have only one TPR peak, i. e. lower temperature peak. This is due to the absence of perovskite-type oxides in the catalysts. However, neat LSM or LSM/γ-Al2O3(20%) heated 750℃ or above, not only the first low temperature TPR peak but also the second peak, which is contributed by the perovskite-type oxides in these catalysts appeared. Therefore, the second TPR peak, i. e. the higher temperatue peak is a characteristic peak for perovskite-type oxides in the reduced process. When LSM/ γ-Al2O3 (10%) catalys is heated at 750℃, no perovskite-type oxides were detected by XRD, and the second reduction peak was absent also in TPR process. \
The order of the second reduction peak temperature(characteristic peak of perovskite - type ox- ides) is: neat LSM(750℃)> LSM/γ-Al2O3 20% (685-698℃) -deposited LSM/γ-Al2O3 (698℃) > LSM/γ-Al2O3 15% (677 - 680℃) >(LSM/γ-AL2O3 10% 620 - 630℃, for Mn - Al - O medium oxides on surface). It is correleted with the increasing of the effect of support sequentially.
When LSM/γ-Al2O3 catalysts were heated at 900℃, more stable phase, spinel MnAl2O4 appeared, which could be proved by TPR of model catalyst MnAl2O4/γ-Al2O3. 相似文献
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铜钴尖晶石复合氧化物催化剂的组成对二甲苯完全氧化反应催化性能的影响 总被引:5,自引:0,他引:5
具有特定结构的复合氧化物,如ABO3,A2BO4及AB2O4等对某些反应比单一氧化物具有更好的催化性能[1,2]. 然而,有关尖晶石型复合氧化物AB2O4对有机物燃烧反应催化性能的研究相对较少,且常用的模型反应大都是一氧化碳或甲烷的催化氧化反应[3]. 超微粒子由于具有大的比表面积和高的表面能等特性,在催化领域已日益引起人们的重视[4]. 低温固相合成是近十几年发展起来的一种新的超细粒子制备方法[5]; 它具有不使用溶剂,无废液排放,工艺过程简单,能耗低等优点,属于对环境友好的“绿色化学”. 目前,此法在合成多组分复合氧化物及催化化学中的应用仍不多见. 本文以含有结晶水的醋酸铜和醋酸钴为原料,采用低温固相合成法制备了单组分氧化铜和氧化钴,以及三种不同铜钴比的铜钴尖晶石型复合氧化物,并以二甲苯氧化为模型反应,采用XRD,BET及程序升温还原(TPR)等手段进行了研究. 相似文献
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掺杂型稀土双钙钛矿光催化剂La2FeTiO6葡萄糖络合法制备与表征 总被引:1,自引:0,他引:1
采用葡萄糖络合法制备了双钙钛矿型催化剂La2FeTiO6,进行不同量Sr掺杂改性。利用X射线粉末衍射(XRD)、H2-程序升温还原(H2-TPR)、比表面(BET)、扫描电镜(SEM)、磁性与电性测试等手段对其进行表征,以可见光催化降解对氯苯酚为探针讨论了Sr掺杂对La2FeTiO6催化剂的物理化学性质及可见光催化活性的影响。结果表明:催化剂La2FeTiO6在掺杂Sr后,催化剂的可见光催化活性均有所提高,其中Sr掺杂量为0.08时,催化剂的光催化活性提高最大,光照1 h时对氯苯酚的降解率就已经达到了90%,5 h后降解率达到99.2%。La2FeTiO6通过Sr掺杂改性后光照5 h降解率提高了37.1%。比表面测试和程序升温还原试验结果表明,碱土金属Sr的掺杂提高了催化剂的比表面,促进了双钙钛矿La2FeTiO6中Fe的还原,使其还原峰面积增大,还原温度也有所降低。电性和磁性测量结果说明,碱土金属Sr的掺杂明显影响其催化剂的电磁性能。 相似文献
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利用超声波制备了SnCl2-ZnCl2/C无汞乙炔氢氯化催化剂,同时加入稀土化合物以稳定催化剂的性能。通过黄金分割法与抛物线法确定了活性组分SnCl2与ZnCl2的最优质量比为2∶1。优选制备工艺,发现在反应温度140℃,乙炔空速300 h-1,V(HCl)/V(C2H2)=1.10时,由0.67 g SnCl2、0.33 g ZnCl2、0.05 g Tb4O7以及4 g焙烧过的活性炭组成的催化剂,其乙炔平均转化率最高,为67.70%。实验表明,载体的处理方式是影响催化剂性能的重要因素。 相似文献
10.
XPS法研究煤表面碳官能团的变化及硫迁移行为 总被引:3,自引:0,他引:3
采用XPS对六枝(Liuzhi)和遵义(Zunyi)原煤及其固定床热解半焦表面的含碳官能团和硫迁移行为进行了研究。在氮气气氛下,在400℃~700℃遵义煤焦表面O=C-O, C-H 和 C-C含量与原煤相比,呈现下降趋势,而C=O和O-C-O、C-O含量却呈现增加趋势; 六枝煤焦表面的O=C-O、C=O和O-C-O、C-O含量的变化规律与遵义煤相似,而C-H和C-C含量的变化却与遵义煤相反。在氢气气氛下, 遵义煤焦表面不仅O=C-O含量与原煤相比下降, 而且C=O和O-C-O、C-O含量也下降,但C-H和C-C含量却增加; 六枝煤除了C=O 和O-C-O含量下降外, 其他官能团的变化与其在氮气气氛下相似。两种煤焦表面S/C比在氮气气氛下随着温度的升高而升高,氢气气氛下在400℃~600℃随着温度的升高却下降,700℃又显著升高。这说明在热解过程中硫在两种气氛下都能从体相向表面迁移,但是氢气能够和含硫自由基反应,所以氢气气氛下煤焦表面的S/C比率低于其氮气气氛下的。 相似文献