4A分子筛脱除四氢呋喃中微量水的研究

本文对四氢呋喃中微量水在4A分子筛上的吸附进行了研究。对该体系的吸附平衡数据进行了测定,并用Langmuir、Freundlich模型进行拟合且吻合较好;采用Crank单孔模型对测定的吸附动力学数据进行拟合,求取了不同温度下的扩散系数并计算了水在4A分子筛上吸附的活化能Ea=27.36kJ.mol-1;采用固定床测定了不同床层高度、不同流量及不同初始浓度下的动态透过曲线;实验结果为吸附工艺设计提供基础数据。     

4A分子筛吸附净化乙二醇二甲醚中微量水研究

研究了乙二醇二甲醚中微量水在4A分子筛上的吸附性能。对该体系的平衡数据进行了测定,并用Lang-mu ir、Freund lich模型进行拟合且吻合较好;采用C lausius-C lapeyron方程计算了水在4A分子筛上的吸附热,并据此探讨了吸附机理;采用Crank单孔模型对测定的吸附动力学数据进行拟合,求取了扩散系数;采用固定床测定了停留时间为60 m in时的动态透过曲线。实验结果为吸附过程的设计提供基础数据。     

3A分子筛在异丙醇脱水中的应用研究

异丙醇是一种重要的化工原料和有机溶剂,广泛应用于化工和制药行业中。工业生产过程产生大量异丙醇和水的混合废液,实现异丙醇和水的完全分离有着重要的意义。通过实验证实了3A分子筛的吸水性和可再生性,确定了通过3A分子筛得到高浓度异丙醇的最优工艺流程和方法。     

分子筛脱除偏二甲肼微量水静态吸附研究

分别测定了偏二甲肼中微量水在3A、4A、5A分子筛上的吸附等温线,并用Langmuir方程和Freundlich方程进行拟合。同时考察了吸附过程对偏二甲肼、偏腙、二甲胺等组分的影响。结果显示,水在3种分子筛上的吸附实验数据基本都适用2个吸附方程。相对而言,在3A、4A上的吸附等温线用Langmuir方程拟合最为吻合,在5A分子筛上的吸附等温线则显示Freundlich方程更适用些。吸附过程对偏二甲肼、偏腙、二甲胺等组分无影响。     

吸附干燥剂4A分子筛制备研究

在７８０～８２０℃下可将来阳高岭土锻烧成偏高岭土,后者在热条件下同碱反应生成４Ａ分子筛,研究结果表明,不同的水热反应条件对产物的吸附能力有影响。     

3A分子筛对乙酸乙酯溶液中微量水分吸附及再生的研究

论文对3A分子筛对乙酸乙酯溶剂中少量水分的吸附及再生进行了的探讨。对3A分子筛对的饱和吸附量,水分的吸附效果,分子筛的再生条件和寿命分别进行了研究,为相关工艺提供基础数据。研究结果表明:流量为5 mL/min时,吸附效果较好。分子筛再生采用干燥方式,在230℃下干燥4 h,循环使用30次后的吸附效果仍然较好。对分子筛的微观结构通过SEM进行了分析,发现新鲜分子筛和循环使用30次后的分子筛微观表面结构有所不同,这需要我们进一步进行深入的研究。     

4A分子筛吸附甲基丙烯酸甲酯中水份的研究

研究了不同温度下活化处理的4A分子筛对甲基丙烯酸甲酯中的水份、对苯二酚等其他杂质的吸附过程,详细测定分析了4A分子筛对不同含水量MMA的饱和吸附能力。结果表明,高温活化处理的4A分子筛对MMA中的水份和对苯二酚都具有很好的吸附效果。     

高颗粒强度吸附干燥剂4A分子筛制备研究

以高岭土为原料，不加粘结剂进行造粒，在７２０－７５０℃下料烧成偏高岭土，在水热条件下同碱反应烧结生成４Ａ分子筛颗粒，研究结果表明，不同的水热反应条件对产物的吸附能力和颗粒均有影响，由水热反应烧结的４Ａ分子筛的颗粒强度远大于传统法制备的４Ａ分子筛的颗粒强度，并探讨了水热反应烧结机理。     

异丙醇对合成13X分子筛的结构和吸附性能的影响

利用XRD、SEM、BET、ICP-AES等手段,对常规水热13X分子筛合成体系中加入不同量异丙醇合成的分子筛进行表征。结果发现,随着合成体系中异丙醇量增加,分子筛的相对结晶度、晶粒尺寸、以及分子筛硅铝比均减小;分子筛的孔容、孔径均增大。将分子筛样品在含1000ppm二甲醚（DME）的乙烯原料以1500h-1体积空速下,应用于乙烯中甲醇、二甲醚等含氧化合物的脱除实验表明,小晶粒、大孔容分子筛样品表现出更好的吸附性能。在合成体系中加入15wt%异丙醇的分子筛样品吸附性能更好,其单程寿命达到280min,单位时间（h）内的积炭量0.71%。     

分子筛吸附甲基丙烯酸甲酯中微量水分的研究

研究了3A，4A，5A和13X4种型号分子筛对甲基丙烯酸甲酯中微量水分的静态吸附的动力学性能，做出了4种型号分子筛的吸附动力学曲线；对其结果进行了分析讨论。并进一步研究了13X型分子筛的吸附温度和吸附剂用量对其饱和吸附量的影响。结果表明，13X型分子筛的吸附效果优于3A，4A和5A型分子筛；其在25℃时吸附效果最好，饱和吸附量最大，吸附速率也最快，分子筛的最佳用量为0．4g／mL。FTIR证明13X分子筛同时还吸附了一定量的对苯二酚。     

四氢呋喃中的微量水在4A分子筛上吸附动态曲线的模拟计算

建立了合适的吸附动态模型,用于分析四氢呋喃中的微量水在4A分子筛上动态吸附特性.利用静态平衡实验数据及孔扩散系数能够很好地对动态透过曲线进行模拟计算,平衡数据符合Langmuir模型,采用Wilke-Chang方程计算的孔扩散系数值为7.015×10-5cm2/s,该方法不仅可减少实验的工作量,而且对四氢呋喃-水体系吸附过程的工业放大设计具有指导意义,也为其他吸附过程数学模型的开发提供借鉴.     

Adsorption of lactic acid from fermentation broth and aqueous solutions on Zeolite molecular sieves

The recovery of lactic acid from fermentation broth and aqueous solutions was studied by adsorption on Silicalite molecular sieves. Batch experiments were used to measure the adsorption isotherms of the lactic acid on Silicalite. A linear correlation was found for both solutions. Silicalite showed a higher adsorptive capacity in the case of the aqueous solution than that of the fermentation broth. Henry's constants were estimated as and for the aqueous and broth solutions, respectively. The effect of temperature on adsorption was also studied in batch mode. Henry's constant dependency on temperature was derived from Van’t Hoff's equation. The heat of adsorption was calculated as (29±17) kJ/mol. The kinetics of adsorption was investigated in column studies where the breakthrough and elution curves were measured. The adsorption process was controlled by the internal diffusion in the Silicalite pellets rather than the diffusion through the fluid film around the pellet. The fluid phase resistance was estimated as 21% of the overall resistance. The glucose presence in the fermentation broth had a negligible effect on lactic acid breakthrough curve in the studied range.     

Adsorption properties of carbon molecular sieves prepared from an activated carbon by pitch pyrolysis

In this study a heat-treatment process using an activated carbon and coal-tar pitch was developed to prepare carbon molecular sieves (CMSs) for CH₄/CO₂ separation. This process results in a partial blockage of the pores of the activated carbon precursor, so that a reduction in the pore size takes place. Equilibrium CO₂ adsorption measurements at different temperatures, and CO₂ and CH₄ kinetic measurements at different temperatures and feed pressures were carried out using the TEOM technique for a carbon molecular sieve (CMS) prepared by this process (sample CB3) and a commercial CMS (Takeda 3A, sampleT3A). The overall diffusion for CO₂ in sample CB3 was faster than that in T3A and a slightly higher CO₂ adsorption capacity of CB3 was obtained. The transient uptake profiles in both samples at different temperatures and different CO₂ partial pressures were described in some cases by a micropore diffusion model, and in other cases by a dual resistance model. Both equilibrium and kinetic results demonstrate a better CO₂/CH₄ separation performance for the CMS prepared in the present study (CB3) than for the commercial CMS (Takeda 3A), due to the existence of slightly wider pore-mouth openings in sample CB3. This study demonstrates that the process used in this work is an interesting and reproducible approach to prepare CMS for CO₂/CH₄ separation.     

分子筛吸附脱除芳烃中的环状烯烃

以Y型分子筛为吸附剂脱除甲苯中的环状烯烃化合物（二聚环戊二烯,DCPD）。采用NH3-TPD测试方法分析了USY和HY分子筛的酸性中心性质。通过间歇吸附实验考察了USY和HY分子筛对甲苯中DCPD的吸附脱除能力以及温度对USY分子筛吸附能力的影响,结果表明,USY分子筛的烯烃吸附量是HY分子筛的1.68倍;当温度由30℃升至50℃时,USY分子筛的吸附速率增大。采用固定床连续实验考察了温度、体积空速和原料中烯烃浓度对USY分子筛吸附效果的影响,当温度为80℃、空速为0.133h?1时,分子筛的穿透吸附量最大;分子筛处理具有较高初始浓度的原料时得到较高的穿透吸附量,且对工业焦化甲苯溶液的处理效果明显,具有较好的工业应用前景。TGA热重分析结果表明,USY分子筛对DCPD的选择性吸附能力强于甲苯。     

Liquid and vapor phase adsorption of chlorinated volatile organic compounds on hydrophobic molecular sieves

This work focused on the potential application of various hydrophobic molecular sieves for the sorption of four model chlorinated volatile organic compounds (CVOCs, i.e., chloroform, trichloroethylene, tetrachloroethylene, and carbon tetrachloride) from dilute liquid water streams.

Results obtained thus far have shown that silicalite-1 has a high affinity for these CVOCs, higher in fact than Centaur^® activated carbon, used as a benchmark in this study. Loading results for trichloroethylene from both liquid and vapor phase indicated that the liquid phase did not penetrate the pores of silicalite-1, while the solution did penetrate the pores of Centaur^® and a dealuminated NaY used for comparison.

Finally, three definitions from the literature for the “hydrophobicity” of molecular sieves were considered. An alternative definition for hydrophobicity is introduced here, which is easy to determine and is based on water retention.     

Purification of tetrahydrofuran from aqueous azeotropic solution: continuous adsorption operation using molecular sieves

Abstract

Purification of chemicals is industrially important. Tetrahydrofuran (THF) is a useful chemical and the industrial requirement is minimum 99.5 mass %. THF forms a homogenous minimum boiling aqueous azeotrope due to which purification by distillation is difficult. The present work has used liquid-phase adsorption of the THF–water azeotropic mixture over different adsorbents in order to purify THF. Molecular sieves (3A and 4A) were observed to offer better separation. A methodology to make the process continuous is presented in this work so as to obtain high-purity THF by using adsorption over molecular sieves.     

CH_4/N_2 separation on methane molecules grade diameter channel molecular sieves with a CHA-type structure

Samples of methane molecules grade diameter channel CHA-type molecular sieves(Chabazite-K, SAPO-34 and SSZ-13) were investigated using the adsorption separation of CH_4/N_2 mixtures. The isotherms recorded for CH_4 and N_2 follow a typical type-Ι behavior, which were fitted well with the Sips model(R~20.999) and the selectivity was calculated using IAST theory. The results reveal that Chabazite-K has the highest selectivity(SCH_4/N= 5.5).2 SSZ-13 has the largest capacity, which can adsorb up to a maximum of 30.957 cm~3·g~(-1)(STP) of CH_4, due to it having the largest pore volume and surface area, but the lowest selectivity(S_(CH_4/N_2)= 2.5). From the breakthrough test, we can conclude that SSZ-13 may be a suitable candidate for the recovery of CH_4 from low concentration methane(CH_420%) based on its larger pore volume and higher CH_4 capacity. Chabazite-K is more suited to the separation of high concentration methane(CH_450%) due to its higher selectivity.     

5A分子筛对重整拔头油吸附分离工艺的研究

在固定吸附床(高度1.2 m,D50 mm)上,研究以5A分子筛为吸附剂,采用吸附分离的工艺技术,对重整拔头油进行吸附分离,考察了温度、空速、吸附/脱附循环等因素对吸附分离工艺的影响,优化了吸附分离的工艺条件。吸附分离优化的操作条件为:操作温度220℃,拔头油气态空速为50 h~(-1),进料时间为25min,脱附气体(氮气)空速为50 h~(-1),中间油吹扫4min,脱附时间21 min。脱附油中正构烷烃的质量分数可以达到99%左右。重整拔头油吸余油的辛烷值得到了提高,可以作为良好的汽油调和组分。