Fixed-bed adsorption of carbon dioxide/methane mixtures on silicalite pellets

The adsorption of carbon dioxide and methane on silicalite pellets packed on a fixed bed has been studied. Equilibrium and kinetic measurements of the adsorption of carbon dioxide and methane have been performed, and a binary adsorption isotherm for carbon dioxide/methane mixtures has been obtained. A model based on the LDF approximation for the mass transfer has been used to describe the breakthrough curves obtained experimentally. A PSA cycle has been proposed for obtaining methane with purity higher than 98% from carbon dioxide/methane mixtures containing 38% and 50% methane, and its performance has been simulated using the proposed model. The simulation results show that silicalite can be a suitable adsorbent for employment in a PSA separation process for carbon dioxide removal from coalseam and landfill gases.     

Sorption of triethyleneglycol and tetraethyleneglycol by silicalite at fixed water activities

The sorption of tetraethyleneglycol by silicalite-1 and triethyleneglycol by silicalite-1 and a silicalite-1/silicalite-2 intergrowth has been studied at 25°C and at fixed water activities in the range 0.111<a _w<0.902 by an isopiestic method. All of the glycol uptakes are between 0.95 and 1.2 molecules per unit cell and in all cases they are essentially independent of water activity. The water content of the silicalite-1 was more sensitive to water activity and glycol content than was that of the silicalite-1/2 intergrowth.     

K-La-Ni/Si-2催化低碳烷烃与二氧化碳重整制合成气(英文)

Ｎｉ／Ｓｉ２催化剂具有较好的低碳烷烃与二氧化碳重整制合成气的反应性能，添加Ｌａ２Ｏ３助剂和Ｋ２Ｏ助剂可提高催化剂活性和合成气收率，从而进一步改善催化剂的低碳烷烃与ＣＯ２重整制合成气的反应性能，研制的ＫＬａＮｉ／Ｓｉ２催化剂，用于天然气与ＣＯ２重整反应制合成气可达９７％的低碳烷烃转化率和９５％以上的合成气收率。     

叔丁醇溶剂中TS-1催化丙烯环氧化的动力学研究

研究了叔丁醇溶剂中TS-1催化丙烯环氧化反应的本征动力学，反应条件为:温度303.15K～323.15K，丙稀压力0.3 MPa～0.6 MPa。根据反应机理及组分在TS-1上的吸附特点建立了如下的机理模型方程式： 根据实验数据，我们对机理模型进行了参数估值。检验结果表明拟合效果较好，反应符合Eley-Rideal机理，丙烯环氧化反应发生在吸附态的过氧化氢与游离态的丙烯之间。     

钛硅分子筛挤条成型催化剂热稳定性能的研究

采用在空气中程序升温焙烧的方式考察了钛硅分子筛挤条成型催化剂的热稳定性能．对不同温度焙烧得到的样品进行了XRD、IR、UV Raman和SEM表征．结果表明，在高温焙烧时，由于载体结构的改变引起载体与分子筛之问相互作用发生变化，导致成型催化剂中分子筛骨架破坏．随着焙烧温度的提高，IR谱图中960cm^-1处代表钛进入骨架的特征峰的强度迅速减弱，当焙烧温度达到1000℃时，960cm-1处的骨架钛特征峰移至948cm^-1．在紫外拉曼谱图中，骨架位钛物种的特征拉曼谱峰-1125cm^-1谱峰在加入SiO2载体后，高温下峰强度明显降低，这说明载体的加入降低了钛硅分子筛挤条成型催化剂的热稳定性能．     

钛硅沸石中的一种非活性钛物种

Synthesis of the titanium silicalite TS-1 was first reported by Taramasso et al[1]in 1983. TS-1 has received considerable interest during the last decade because of its unique catalytic properties in oxidation reactions involving H2O2 as the oxidant. It is accepted that the extraframework Ti species in TS-1 favor the decomposition of H2O2and should be avoided. But in the present study, it was observed that there was a kind of Ti species inactive in both the oxidation reaction and the decomposition of H2O2.     

TS-1分子筛催化双氧水氧化环己烷(英文)

系统地研究了ＴＳ－１分子筛催化双氧水氧化环己烷的反应。制备了三种ＴＳ－１分子筛,它们具有窄的粒径分布,在６０℃表现出高的活性和选择性。考察了溶剂、催化剂、反应温度、反应时间、ＴＳ－１中Ｔｉ含量及Ｈ２Ｏ７用量对氧化反应的影响。对具有完好晶型的ＴＳ－１分子筛役有必要进行预处理。最佳反应温度为８０～１１０℃,丙酮为最佳溶剂。环己酮的选择性与ＴＳ－１粒子大小有关,而Ｈ２Ｏ２选择性与ＴＳ－１用量无关。实验结果显示．溶剂在反应中间体的形成中起重要作用,Ｔｉ与丙酮配体的过氧配合物具有活化环己烷的活性。关键词 ＴＳ－１ 环己烷 催化氧化 Ｈ２Ｏ２     

丙烯环氧化反应中失活钛硅分子筛的无氧脱附研究

采用无氧脱附方法对丙烯环氧化中失活的薄层钛硅分子筛(即Spent EPO-4)和环氧丙烷(PO)与丙二醇单甲醚(MME)浸渍的TS-1催化剂(即PO／TS-1和MME／TS-1)进行了研究，脱附产物由气相色谱定性分析，无氧脱附后的催化剂以丙烯环氧化为探针反应进行再生性能评价，同时在无氧条件下考察了TS-1在300℃时催化裂化PO反应．实验结果表明：PO浸渍TS-1可使其活性明显下降，PO在TS-1上不是简单的弱吸附，存在着化学强吸附和自聚．失活催化剂(Spent EPO-4和PO／TS-1)经无氧脱附后，其催化活性可显著恢复．通过对失活催化剂脱附产物的比较，推测了丙烯环氧化反应过程中钛硅分子筛失活原因．     

TS-1分子筛对固定床中苯酚羟基化反应的催化性能

 制备了用于固定床反应器的负载型TS－1分子筛催化剂,并以苯酚羟基化为探针反应,研究了载体、钛含量和预处理剂等对负载型TS－1分子筛催化性能的影响,考察了固定床反应器中苯酚羟基化反应的工艺条件．结果表明,酸性较强的载体会加剧H2O2的分解,导致苯酚的转化率和H2O2的有效利用率下降;在所研究的ZSM－5,TiO2,Al2O3,ZrO2,SiO2和硅藻土载体中,硅藻土具有最好的催化性能;催化剂的活性与骨架钛含量有关;用HNO3,KAc,NaAc,NH4Ac和NH4Cl处理过的催化剂,活性和选择性得到提高,而用NH3·H2O,Na2CO3和Na3PO4等碱性物质处理后,催化剂的活性则下降;溶剂、反应温度、原料空速和苯酚／H2O2摩尔比对苯酚羟基化反应有很大影响．以丙酮为溶剂,在苯酚／H2O2摩尔比为3,反应温度为84℃,WHSV为8．46h－1的反应条件下,苯酚转化率、H2O2转化率、苯二酚选择性以及H2O2的有效利用率可分别达到27．7％,94．8％,97．7％和75．1％．     

TS分子筛的催化氧化性能研究Ⅴ.环己酮氨肟化反应

研究了自制的钛硅分子筛(TS-1)催化H_2O_2参与的环己酮氨肟化反应.结果表明,降低反应溶液中H_2O_2的浓度、增加NH_3用量有利于H_2O_2利用率、环己酮肟收率和选择性的提高,适宜的n(H_2O_2):n(酮)<1.0,n(NH_3):n(酮)>2.0.反应时间应控制在3.5h左右.对溶剂的研究显示,叔丁醇在溶剂中所占的体积对反应有较大的影响,在叔丁醇体积分数为0.2到0.8之间,实验获得了较好的结果.当n(NH_3):n(H_2O_2):n(酮)=2.0:1.0:1.0,叔丁醇体积分数为0.5,反应时间2.5h,反应温度353K时,H_2O_2利用率、环己酮肟收率和选择性分别达95%,94%和97%以上.并对空白实验结果和TS-1的重复性试验进行了讨论.