Chemical Industry and Engineering Progress ›› 2021, Vol. 40 ›› Issue (S2): 315-321.DOI: 10.16085/j.issn.1000-6613.2021-0962
• Materials science and technology • Previous Articles Next Articles
YAO Desong1(), LIU Huang1(), CHEN Li2, LI Ruijing1, WANG Jian1
Received:
2021-05-06
Revised:
2021-07-06
Online:
2021-11-12
Published:
2021-11-12
Contact:
LIU Huang
通讯作者:
刘煌
作者简介:
姚德松(1999—),男,硕士研究生,研究方向为油气藏开发。E-mail:基金资助:
CLC Number:
YAO Desong, LIU Huang, CHEN Li, LI Ruijing, WANG Jian. Theoretical analysis of CO2 dissolution ability in ZIF-8/glycol-2-methylimidazole slurry[J]. Chemical Industry and Engineering Progress, 2021, 40(S2): 315-321.
姚德松, 刘煌, 陈莉, 李瑞景, 王舰. CO2在ZIF-8/乙二醇-2-甲基咪唑浆液中溶解能力理论分析[J]. 化工进展, 2021, 40(S2): 315-321.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2021-0962
293.15K | 303.15K | 313.15K | |||
---|---|---|---|---|---|
压力 /MPa | 吸附量 /mol·kg-1 | 压力 /MPa | 吸附量 /mol·kg-1 | 压力 /MPa | 吸附量 /mol·kg-1 |
0 | 0 | 0 | 0 | 0 | 0 |
0.25 | 2.028 | 0.617 | 3.575 | 0.61 | 3.389 |
0.567 | 3.711 | 0.959 | 4.956 | 1.08 | 4.588 |
1.031 | 5.659 | 1.599 | 6.018 | 1.78 | 5.510 |
1.541 | 6.627 | 2.202 | 6.592 | 2.79 | 6.267 |
2.115 | 7.274 | 3.092 | 7.273 | 4.2 | 6.681 |
2.552 | 7.552 | 4.11 | 7.691 | ||
3.066 | 7.913 | ||||
3.556 | 8.277 | ||||
4.192 | 8.564 |
293.15K | 303.15K | 313.15K | |||
---|---|---|---|---|---|
压力 /MPa | 吸附量 /mol·kg-1 | 压力 /MPa | 吸附量 /mol·kg-1 | 压力 /MPa | 吸附量 /mol·kg-1 |
0 | 0 | 0 | 0 | 0 | 0 |
0.25 | 2.028 | 0.617 | 3.575 | 0.61 | 3.389 |
0.567 | 3.711 | 0.959 | 4.956 | 1.08 | 4.588 |
1.031 | 5.659 | 1.599 | 6.018 | 1.78 | 5.510 |
1.541 | 6.627 | 2.202 | 6.592 | 2.79 | 6.267 |
2.115 | 7.274 | 3.092 | 7.273 | 4.2 | 6.681 |
2.552 | 7.552 | 4.11 | 7.691 | ||
3.066 | 7.913 | ||||
3.556 | 8.277 | ||||
4.192 | 8.564 |
293.15K | 303.15K | 313.15K | |||
---|---|---|---|---|---|
压力 /MPa | 溶解度 /mol·L-1 | 压力 /MPa | 溶解度 /mol·L-1 | 压力 /MPa | 溶解度 /mol·L-1 |
0 | 0 | 0 | 0 | 0 | 0 |
0.0153 | 0.195 | 0.0289 | 0.126 | 0.035 | 0.201 |
0.114 | 0.738 | 0.193 | 0.826 | 0.37 | 0.907 |
0.279 | 1.319 | 0.335 | 1.172 | 0.61 | 1.185 |
0.513 | 1.851 | 0.529 | 1.537 | 0.77 | 1.365 |
0.735 | 2.217 | 0.783 | 1.877 | 0.93 | 1.534 |
0.857 | 2.422 | 0.957 | 2.082 | 1.25 | 1.837 |
0.974 | 2.607 | 1.213 | 2.401 | 1.47 | 2.031 |
293.15K | 303.15K | 313.15K | |||
---|---|---|---|---|---|
压力 /MPa | 溶解度 /mol·L-1 | 压力 /MPa | 溶解度 /mol·L-1 | 压力 /MPa | 溶解度 /mol·L-1 |
0 | 0 | 0 | 0 | 0 | 0 |
0.0153 | 0.195 | 0.0289 | 0.126 | 0.035 | 0.201 |
0.114 | 0.738 | 0.193 | 0.826 | 0.37 | 0.907 |
0.279 | 1.319 | 0.335 | 1.172 | 0.61 | 1.185 |
0.513 | 1.851 | 0.529 | 1.537 | 0.77 | 1.365 |
0.735 | 2.217 | 0.783 | 1.877 | 0.93 | 1.534 |
0.857 | 2.422 | 0.957 | 2.082 | 1.25 | 1.837 |
0.974 | 2.607 | 1.213 | 2.401 | 1.47 | 2.031 |
温度/K | 饱和吸附量A | 系数1 | 系数2 |
---|---|---|---|
293.15 | 9.7966 | 1.2403 | 1.1435 |
303.15 | 8.7831 | 1.2650 | 1.1801 |
313.15 | 7.7411 | 1.3359 | 1.0952 |
温度/K | 饱和吸附量A | 系数1 | 系数2 |
---|---|---|---|
293.15 | 9.7966 | 1.2403 | 1.1435 |
303.15 | 8.7831 | 1.2650 | 1.1801 |
313.15 | 7.7411 | 1.3359 | 1.0952 |
温度/K | 生成焓(Hm)/kJ·mol-1 | 平衡常数(km) |
---|---|---|
293.15 | 3.8441 | 0.1340 |
303.15 | 5.3812 | 0.1139 |
313.15 | 8.1756 | 0.0765 |
温度/K | 生成焓(Hm)/kJ·mol-1 | 平衡常数(km) |
---|---|---|
293.15 | 3.8441 | 0.1340 |
303.15 | 5.3812 | 0.1139 |
313.15 | 8.1756 | 0.0765 |
系数 | 293.15K | 303.15K | 313.15K |
---|---|---|---|
x1 | 4.0171 | 1.6542 | -1.1366 |
x2 | -88.0456 | -68.0804 | -65.2812 |
x3 | -1.0840 | -1.7063 | -3.0891 |
x4 | 0.4112 | -0.1267 | 0.2531 |
x5 | 4.4929 | 3.7818 | 4.2774 |
x6 | 2.2519 | 2.8605 | 4.5994 |
系数 | 293.15K | 303.15K | 313.15K |
---|---|---|---|
x1 | 4.0171 | 1.6542 | -1.1366 |
x2 | -88.0456 | -68.0804 | -65.2812 |
x3 | -1.0840 | -1.7063 | -3.0891 |
x4 | 0.4112 | -0.1267 | 0.2531 |
x5 | 4.4929 | 3.7818 | 4.2774 |
x6 | 2.2519 | 2.8605 | 4.5994 |
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