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离子改性Y分子筛吸附分离1,1,1,2-四氟乙烷/1,1-二氟-2-氯乙烯 被引量:3

Adsorptive separation of 1,1,1,2-tetrafluoroethane/1,1-difluoro-2-chloroethylene over ion-exchanged Y zeolites
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摘要 用CaCl2、La(NO3)3和Ce(NO3)3溶液对NaY分子筛进行离子改性制备出CaY、LaY和CeY分子筛。将其及NaY为吸附剂,利用动态吸附法评价其吸附分离1,1,1,2-四氟乙烷(HFC-134a)产品中微量1,1-二氟-2-氯乙烯(HCFC-1122)的性能。同时采用X射线衍射(XRD)、吡啶红外(FTIR)和氨-程序升温脱附(NH3-TPD)等手段对新鲜及再生后的吸附剂进行结构和表面性质表征。结果表明:CaY、LaY与CeY分子筛上的Brφnsted酸中心可与HCFC-1122形成π-吸附配合物,从而将吸附流出气中HCFC-1122的残余率降低至1.0%以下;Brφnsted酸强度越高,π-吸附配合物越容易形成,最低吸附温度越低(CeY<LaY<CaY)。220℃下穿透吸附容量随CaY<LaY<CeY增加,归因于较少的强Brφnsted酸和弱Lewis酸数量有利于HCFC-1122的π-吸附配合物引发程度较低的聚合反应。吸附剂的热脱附再生性能不佳与其表面酸中心覆盖物难以脱除有关。 Using CaCl2, La(NO3)3 and Ce(NO3) 3 solutions, NaY was ion-exchanged to prepare CaY, LaY and CeY zeolites. Adsorptive removal of trace amount of 1,1-difluoro-2-chloroethylene (HCFC-1122) from 1,1,1,2-tetrafluoroethane product over NaY, CaY, LaY, and CeY zeolites were investigated. The structure and surface properties of fresh and regenerated adsorbents were characterized by X-ray diffraction, pyridine infrared spectra techniques and temperature programmed desorption of ammonia. Results show that the residual ratio of HCFC-1122 impurity in the eluate can be decreased to 1.0% over CaY,LaY and CeY zeolitesvia the formation ofπ-adsorption complexes between HCFC-1122 and Br?nsted acid sites. The increase of intensity of Br?nsted acid favors the formation ofπ-adsorption complexes, consequently decreasing adsorption temperature for complete removal of HCFC-1122 (CeY 〈 LaY 〈 CaY). Breakthrough adsorption capacity of HCFC-1122 at 220℃ increases in the order of CaY 〈 LaY 〈 CeY, since lower density of strong Br nsted and weak Lewis acid sites are favorable to lower degree polymerization initiated byπ-adsorption complexes. The thermal regeneration of adsorbents is unsatisfactory, attributed to hardly removal of contaminant on the acid sites of saturated adsorbents during the thermal regeneration process.
出处 《化工学报》 EI CAS CSCD 北大核心 2014年第10期3946-3952,共7页 CIESC Journal
基金 浙江省绿色化工重大专项(2007C11043)~~
关键词 离子交换 Y型分子筛 吸附 脱附 分离 ion-exchange Y-type zeolite adsorption desorption separation
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参考文献26

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