CIESC Journal ›› 2024, Vol. 75 ›› Issue (7): 2565-2573.DOI: 10.11949/0438-1157.20240120
• Separation engineering • Previous Articles Next Articles
Taohong WANG1(), Chao WANG2, Zheng LI1, Ying LIU2, Ge TIAN1, Ganggang CHANG1(
), Xiaoyu YANG1, Zongbi BAO2
Received:
2024-01-26
Revised:
2024-05-23
Online:
2024-08-09
Published:
2024-07-25
Contact:
Ganggang CHANG
王涛虹1(), 王超2, 李政1, 刘莹2, 田歌1, 常刚刚1(
), 阳晓宇1, 鲍宗必2
通讯作者:
常刚刚
作者简介:
王涛虹(2000—),女,硕士研究生,wangtaohong@whut.edu.cn
基金资助:
CLC Number:
Taohong WANG, Chao WANG, Zheng LI, Ying LIU, Ge TIAN, Ganggang CHANG, Xiaoyu YANG, Zongbi BAO. Immobilize Cu(Ⅰ) into π-complexed MOF adsorbent for selectivity separation of ethane/ethylene[J]. CIESC Journal, 2024, 75(7): 2565-2573.
王涛虹, 王超, 李政, 刘莹, 田歌, 常刚刚, 阳晓宇, 鲍宗必. 固载Cu(Ⅰ)的π络合MOF吸附剂用于乙烷/乙烯的选择性分离[J]. 化工学报, 2024, 75(7): 2565-2573.
Fig.2 N2 adsorption isotherm of Cu(Ⅰ)@UiO-66-(OH)2 at 77 K (a); Single-component adsorption isotherms of Cu(Ⅰ)@UiO-66-(OH)2 at 298 K and 1 bar (b); Single-component adsorption-desorption isotherms of 3%Cu(Ⅰ)@UiO-66-(OH)2 at different temperatures (c); Adsorption heats of C2H6 and C2H4 in 3%Cu(Ⅰ)@UiO-66-(OH)2 (d) [in figures (a) and (c), the hollow sphere represents desorption, the solid sphere represents adsorption; in figure (b), the hollow sphere represents ethane, the solid sphere represents ethylene]
样品名称 | CuCl浸渍量/mg | C2H6吸附量/(mmol·g-1) | C2H4吸附量/(mmol·g-1) | BET比表面积/(m2·g-1) |
---|---|---|---|---|
UiO-66-(OH)2 | — | 2.83 | 3.21 | 788.3 |
0.5%Cu(Ⅰ)@UiO-66-(OH)2 | 30 | 2.69 | 2.97 | 693.3 |
3%Cu(Ⅰ) @UiO-66-(OH)2 | 65 | 2.21 | 2.95 | 352.3 |
11%Cu(Ⅰ)@UiO-66-(OH)2 | 100 | 2.28 | 2.79 | 308.0 |
Table 1 Adsorption capacity of C2H6 and C2H4 of UiO-66-(OH)2 and different loads of Cu(Ⅰ)@UiO-66-(OH)2 and their BET specific surface area
样品名称 | CuCl浸渍量/mg | C2H6吸附量/(mmol·g-1) | C2H4吸附量/(mmol·g-1) | BET比表面积/(m2·g-1) |
---|---|---|---|---|
UiO-66-(OH)2 | — | 2.83 | 3.21 | 788.3 |
0.5%Cu(Ⅰ)@UiO-66-(OH)2 | 30 | 2.69 | 2.97 | 693.3 |
3%Cu(Ⅰ) @UiO-66-(OH)2 | 65 | 2.21 | 2.95 | 352.3 |
11%Cu(Ⅰ)@UiO-66-(OH)2 | 100 | 2.28 | 2.79 | 308.0 |
吸附剂 | 吸附质 | q1/(cm3·g-1) | q2/(cm3·g-1) | b1 | b2 | R2 |
---|---|---|---|---|---|---|
UiO-66-(OH)2 | C2H4 | 3.416 | 1.896 | 0.136 | 0.007 | 0.999 |
C2H6 | 3.162 | 1.256 | 0.327 | 0.010 | 0.999 | |
3%Cu(Ⅰ)@UiO-66-(OH)2 | C2H4 | 4.008 | 0.747 | 0.397 | 0.013 | 0.999 |
C2H6 | 2.863 | 0.401 | 0.491 | 0.017 | 0.999 |
Table 2 Dual-Site Langmuir fitting parameters for adsorption isotherms of C2H4 and C2H6 of UiO-66-(OH)2 and 3%Cu(Ⅰ)@UiO-66-(OH)2 at 298 K
吸附剂 | 吸附质 | q1/(cm3·g-1) | q2/(cm3·g-1) | b1 | b2 | R2 |
---|---|---|---|---|---|---|
UiO-66-(OH)2 | C2H4 | 3.416 | 1.896 | 0.136 | 0.007 | 0.999 |
C2H6 | 3.162 | 1.256 | 0.327 | 0.010 | 0.999 | |
3%Cu(Ⅰ)@UiO-66-(OH)2 | C2H4 | 4.008 | 0.747 | 0.397 | 0.013 | 0.999 |
C2H6 | 2.863 | 0.401 | 0.491 | 0.017 | 0.999 |
Fig.4 Dynamic breakthrough curve of C2H6/C2H4 (50∶50, volume ratio) gas mixture (a) and 5 cycles adsorption curve for ethylene (b)of 3%Cu(Ⅰ)@UiO-66-(OH)2 at 298 K and 1 bar; PXRD pattern (c) and N2 adsorption isotherm (d) of 3%Cu(Ⅰ)@UiO-66-(OH)2 before and after multiple cycles
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