2020
DOI: 10.1021/acs.iecr.0c01726
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Gallate-Based Metal–Organic Frameworks for Highly Efficient Removal of Trace Propyne from Propylene

Abstract: Purification of propylene from the propyne (C3H4)/propylene (C3H6) mixture is a significant and challenging process in the chemical industry. Nowadays, the removal of propyne from propylene mainly relies on the energy-intensive hydrogenation catalyzed by noble metals. We herein report three gallate-based metal–organic frameworks, namely, M­(II)-gallate (M = Ni, Mg, Co), which provide excellent performance in terms of removing propyne from the propyne/propylene mixture (1:99, v/v). The C3H4 uptake capacities of… Show more

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Cited by 15 publications
(11 citation statements)
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“…The Th(IV) atoms in Th-TFBPDC-i have the same coordination atoms with those in Th-TFBPDC (Figure S2b). Once again, the Th−O w bond distances of 2.702(8), 2.678(8), and 2.702 (17) Å are longer than other Th−O bond distances between 2.343 (7) and 2.533( 9) Å (Table S1).…”
Section: ■ Results and Discussionmentioning
confidence: 86%
See 1 more Smart Citation
“…The Th(IV) atoms in Th-TFBPDC-i have the same coordination atoms with those in Th-TFBPDC (Figure S2b). Once again, the Th−O w bond distances of 2.702(8), 2.678(8), and 2.702 (17) Å are longer than other Th−O bond distances between 2.343 (7) and 2.533( 9) Å (Table S1).…”
Section: ■ Results and Discussionmentioning
confidence: 86%
“…In contrast, the previously reported MOFs showed low C 3 H 4 sorption amounts with typical values lower than 4 mmol g −1 at 298 K (Figure 5). For example, the C 3 H 4 capacity at 298 K is much higher than those of JXNU-6 (5.07 mmol g −1 ), 9 SIFSIX-2-Cu-i (4.46 mmol g −1 ), 16 Co-Gallate (3.75 mmol g −1 ), 17 GeFSIXdps-Cu (3.7 mmol g −1 ), 18 ZU-62 (3.64 mmol g −1 ), 19 UTSA- 200 (3.58 mmol g −1 ), 20 and NKMOF-1-Ni (3.5 mmol g −1 ). 21 The C 3 H 4 sorption amount of Th-TFBPDC is comparable to that of the top-performing SIFSIX-1-Cu (8.76 mmol g −1 ).…”
Section: ■ Results and Discussionmentioning
confidence: 93%
“…丙烯是工业产量仅次于乙烯的重要烯烃原料, 主 要用作聚合单体生产如聚丙烯等下游产品, 被广泛用 于塑料、制药、纺织品、涂料等国民经济各个行业 [1][2][3][4] 。目前,丙烯生产主要通过蒸汽裂解的方式进行, 该技术会难以避免地引入少量丙炔和丙二烯等杂质 气体,严重影响后续的丙烯聚合过程,因此,实现丙 烯与丙炔和丙二烯有效分离是丙烯纯化过程中的关 键 [5,6] 。现有的丙炔/丙烯、丙二烯/丙烯分离技术主要 是选择性催化加氢, 通过将丙烯中的丙炔或丙二烯转 化为丙烯,从而达到丙烯纯化的效果,但该过程存在 丙烯过度加氢得到副产物丙烷的问题, 同时存在分离 能耗大、成本高等缺点,因此需要开发更为经济有效 的分离方法 [7,8] 。 近年来, 以离子液体作为溶剂的吸收分离技术受 到广泛关注 [9][10] 。 吸收分离技术流程简单, 处理量大, 同时离子液体具有极低的蒸气压、 良好的化学稳定性 和丰富的结构可设计性, 可以克服常规溶剂的局限性, 使吸收过程无溶剂损失,同时易于回收利用,无交叉 污染 [11][12] 。在气体分离领域,离子液体已被研究应用 于 CO2 捕集 [13][14][15][16] 、NH3 捕集 [17] 、H2S 和 SO2 脱除 [18][19][20] 以及低碳烃分离等方面 [21][22][23][24] 。其中,Kim 等人测定了 C2-C3 炔烃烯烃在几种咪唑类离子液体中的溶解度 [25] , 其中 [ [26][27] ,有望与 丙炔和丙二烯分子发生相对较强的氢键相互作用, 获 得较高的溶解度 [28] , 同时引入结构不对称的三丁基乙 基鏻阳离子([P4442] + )能显著降低离子液体粘度,且 合成的离子液体具备良好的热稳定性,分解温度在 580 K 左右 [29][30] [27][28] 进行溶解度测试前, 合成的离子液体经过 1 mbar [29][30]…”
Section: 引言unclassified
“…Others regard bio-MOFs as a subcategory of highly porous MOFs that are useful for biological and medical applications. 18,68 Bio-MOFs have several advantages, which are listed in Figure 4. 18 Bio-MOFs have been applied for H 2 O adsorption and desorption, selective CO 2 adsorption, catalysis, drug delivery, photostable sensor fabrication, O 2 antibacterial activity, and storage of various gases.…”
Section: ■ Bio-mofs As Adsorbentsmentioning
confidence: 99%
“…There is no clear definition of what constitutes a bio-MOF. Some define a bio-MOF as an MOF in which one or more biomolecules function as organic ligands. Others regard bio-MOFs as a subcategory of highly porous MOFs that are useful for biological and medical applications. , Bio-MOFs have several advantages, which are listed in Figure …”
Section: Bio-mofs As Adsorbentsmentioning
confidence: 99%