13X微孔沸石和MCM-41介孔材料的合成及用于处理含Cd2+废水

以天津蓟县钾长石矿粉为主要原料,经选矿、煅烧、水热处理等工艺成功合成了13X微孔沸石. 以气相氧化硅、氢氧化钠、十六烷基三甲基溴化铵等为主要原料,在水热条件下合成了MCM-41有序介孔材料. 采用XRD和N2吸附-脱附等手段对合成的13X沸石和MCM-41介孔材料的物相、比表面积、孔径、孔体积等进行了分析对比. 在此基础上,对13X沸石和MCM-41介孔材料处理含Cd2+废水的效果和机理进行了对比研究,确定了不同分子筛用量、不同初始pH值、不同混合时间下13X沸石和MCM-41介孔分子筛对水中Cd2+的吸附率和吸附量. 研究发现,尽管MCM-41的比表面积和孔径远大于13X沸石,但其对水中Cd2+的处理效果却低于13X沸石,这与13X沸石和MCM-41的孔道结构类型、化学组成、表面荷电性质等有关.     

Adsorption of mercaptan from model gasoline on 13X loaded with Zn2+

Adsorption of mercaptan on 13X loaded with Zn²⁺ from model gasoline was studied at different concentration and temperatures. The results indicate that high temperature and low concentration favour the removal of mercaptan from the model gasoline. The adsorptive amount of the untreated adsorbents loaded with Zn²⁺ is less than the treated with heat obviously, but the adsorbed amount is not enhanced distinctly by the way of increasing the treating temperature. A pseudo‐first‐order mechanism has been proposed to describe the adsorption in the model gasoline system. The desulphurizing capability increases due to the Zn²⁺ impregnated. With the concentration of Zn²⁺ higher, the adsorptive amount for ethanethiol increases. Adsorption mechanism shows that it is a chemical adsorption. Two different methods of regeneration were investigated.     

13X沸石吸附处理水中苯胺的性能及应用

用天然岩石矿物为原料,经过较简单的工艺过程合成13X沸石去除水中苯胺,模拟废水的实验结果表明：沸石对苯胺的吸附速率非常快,吸附时间为10min时,吸附基本达饱和;一般当沸石用量为10g/L时,水蝇苯胺的吸附率达95％,随着pH值的增加,苯胺在沸石上的吸附率较小;温度增加,吸附率有所增加。但常温下,苯胺的吸附率也能达到93％,13X沸石对苯胺的最大吸附量可达10mg/g,其吸附规律较好地符合Freundlich吸附等温式,饱和了苯胺的沸石,用质量分数为20％,温度为60℃的氯化钠溶液洗脱,解吸率近于100％,且解吸后的沸石在未经任何处理的情况下仍能吸附苯胺;对实际苯胺废水的处理结果,也表明13X沸石不仅可有效地去除苯胺,还可以有效地去除废水中的SS,CODCr,氨氮及油等。     

Propane/Propylene Separation by Simulated Moving Bed II. Measurement and Prediction of Binary Adsorption Equilibria of Propane,Propylene, Isobutane,and 1-Butene on 13X Zeolite

Abstract

The design of a simulated moving bed (SMB) process relies on valid thermodynamic predictions of multicomponent adsorption built up from accurate binary adsorption equilibrium data. Experimental adsorption equilibria of binary mixtures constituted by propane, propylene, isobutane and 1-butene on 13X zeolite were determined using breakthrough experiments at 373 K and 150 kPa. In addition, these binary adsorption experiments allow to confirm the choice of isobutane as an interesting desorbent for the separation of propane-propylene by SMB, since it has an intermediate selectivity between the two species to separate. Various prediction models are available in the literature but only a few of them have both physical and thermodynamical consistency. The ideal adsorbed solution theory (IAST), the thermodynamically consistent extended Toth model (TCET), and the physically-consistent extended Toth isotherm (PCET) were used to predict binary adsorption equilibria from pure component adsorption isotherms parameters. The PCET model was found suitable for representing the adsorption equilibrium of the different hydrocarbon mixtures with a reasonably good accuracy.