Chemical Industry and Engineering Progress ›› 2019, Vol. 38 ›› Issue (08): 3679-3687.DOI: 10.16085/j.issn.1000-6613.2018-1815
• Industrial catalysis • Previous Articles Next Articles
Chengjie XIA(),Yang LIU,Ming KE(),Qi WANG,Wen LIU,Lei ZHANG
Received:
2018-09-10
Online:
2019-08-05
Published:
2019-08-05
Contact:
Ming KE
通讯作者:
柯明
作者简介:
夏成杰(1993—),男,硕士研究生。E-mail:基金资助:
CLC Number:
Chengjie XIA,Yang LIU,Ming KE,Qi WANG,Wen LIU,Lei ZHANG. Effect of Sn on V2O5/Al2O3 catalyst in dehydrogenation of isobutane[J]. Chemical Industry and Engineering Progress, 2019, 38(08): 3679-3687.
夏成杰,刘洋,柯明,王奇,刘稳,张蕾. Sn对V2O5/Al2O3催化剂在异丁烷脱氢反应中的影响[J]. 化工进展, 2019, 38(08): 3679-3687.
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催化剂 | 比表面积/m2·g-1 | 孔容/cm·g-1 | 孔径/nm |
---|---|---|---|
Al2O3 | 280.7 | 0.42 | 5.96 |
12%V2O5/Al2O3 | 260.8 | 0.39 | 5.92 |
0.5%Sn-12%V2O5/Al2O3 | 256.6 | 0.38 | 7.65 |
1%Sn-12%V2O5/Al2O3 | 254.3 | 0.38 | 8.03 |
2%Sn-12%V2O5/Al2O3 | 241.8 | 0.37 | 6.09 |
4%Sn-12%V2O5/Al2O3 | 174.3 | 0.34 | 7.89 |
催化剂 | 比表面积/m2·g-1 | 孔容/cm·g-1 | 孔径/nm |
---|---|---|---|
Al2O3 | 280.7 | 0.42 | 5.96 |
12%V2O5/Al2O3 | 260.8 | 0.39 | 5.92 |
0.5%Sn-12%V2O5/Al2O3 | 256.6 | 0.38 | 7.65 |
1%Sn-12%V2O5/Al2O3 | 254.3 | 0.38 | 8.03 |
2%Sn-12%V2O5/Al2O3 | 241.8 | 0.37 | 6.09 |
4%Sn-12%V2O5/Al2O3 | 174.3 | 0.34 | 7.89 |
催化剂 | 部分酸量/μmol·g-1 | 总酸量/μmol·g-1 | ||
---|---|---|---|---|
弱酸 | 中强酸 | 强酸 | ||
12%V2O5/Al2O3 | 959.9 | 268.9 | 328.7 | 1557.5 |
0.5%Sn-12%V2O5/Al2O3 | 952.1 | 235.5 | 410.4 | 1598.0 |
1%Sn-12%V2O5/Al2O3 | 941.6 | 203.9 | 482.7 | 1628.2 |
2%Sn-12%V2O5/Al2O3 | 779.9 | 166.7 | 616.0 | 1562.6 |
4%Sn-12%V2O5/Al2O3 | 712.9 | 150.5 | 745.5 | 1608.9 |
催化剂 | 部分酸量/μmol·g-1 | 总酸量/μmol·g-1 | ||
---|---|---|---|---|
弱酸 | 中强酸 | 强酸 | ||
12%V2O5/Al2O3 | 959.9 | 268.9 | 328.7 | 1557.5 |
0.5%Sn-12%V2O5/Al2O3 | 952.1 | 235.5 | 410.4 | 1598.0 |
1%Sn-12%V2O5/Al2O3 | 941.6 | 203.9 | 482.7 | 1628.2 |
2%Sn-12%V2O5/Al2O3 | 779.9 | 166.7 | 616.0 | 1562.6 |
4%Sn-12%V2O5/Al2O3 | 712.9 | 150.5 | 745.5 | 1608.9 |
催化剂 | H2-TPR表征 | XPS表征 | ||||
---|---|---|---|---|---|---|
温度peak/℃ | 耗氢量/mmol·g-1 | 温度peak/℃ | 耗氢量/mmol·g-1 | |||
12%V2O5/Al2O3 | — | — | 456.2 | 0.9614 | ||
0.5%Sn-12%V2O5/Al2O3 | 329.3 | 0.5315 | 456.7 | 0.4704 | ||
1%Sn-12%V2O5/Al2O3 | 330.2 | 0.6367 | 457.9 | 0.4293 | ||
2%Sn-12%V2O5/Al2O3 | 332.7 | 0.8174 | 467.4 | 0.3836 | ||
4%Sn-12%V2O5/Al2O3 | 336.6 | 1.0105 | 472.5 | 0.3184 |
催化剂 | H2-TPR表征 | XPS表征 | ||||
---|---|---|---|---|---|---|
温度peak/℃ | 耗氢量/mmol·g-1 | 温度peak/℃ | 耗氢量/mmol·g-1 | |||
12%V2O5/Al2O3 | — | — | 456.2 | 0.9614 | ||
0.5%Sn-12%V2O5/Al2O3 | 329.3 | 0.5315 | 456.7 | 0.4704 | ||
1%Sn-12%V2O5/Al2O3 | 330.2 | 0.6367 | 457.9 | 0.4293 | ||
2%Sn-12%V2O5/Al2O3 | 332.7 | 0.8174 | 467.4 | 0.3836 | ||
4%Sn-12%V2O5/Al2O3 | 336.6 | 1.0105 | 472.5 | 0.3184 |
催化剂 | 甲烷/% | 乙烷/% | 乙烯/% | 丙烷/% | 丙烯/% | 正丁烷/% | 异丁烯/% | 其他/% |
---|---|---|---|---|---|---|---|---|
12%V2O5/Al2O3 | 2.52 | 0.42 | 0.13 | 2.80 | 2.35 | 2.36 | 81.81 | 7.61 |
0.5%Sn-12%V2O5/Al2O3 | 2.36 | 0.40 | 0.11 | 2.82 | 2.70 | 2.35 | 82.72 | 6.54 |
1%Sn-12%V2O5/Al2O3 | 2.35 | 0.29 | 0.18 | 2.41 | 2.66 | 2.22 | 84.29 | 5.60 |
2%Sn-12%V2O5/Al2O3 | 2.27 | 0.33 | 0.17 | 2.18 | 2.69 | 1.70 | 85.20 | 5.46 |
4%Sn-12%V2O5/Al2O3 | 2.17 | 0.18 | 0.19 | 2.09 | 2.98 | 0.98 | 85.96 | 5.45 |
催化剂 | 甲烷/% | 乙烷/% | 乙烯/% | 丙烷/% | 丙烯/% | 正丁烷/% | 异丁烯/% | 其他/% |
---|---|---|---|---|---|---|---|---|
12%V2O5/Al2O3 | 2.52 | 0.42 | 0.13 | 2.80 | 2.35 | 2.36 | 81.81 | 7.61 |
0.5%Sn-12%V2O5/Al2O3 | 2.36 | 0.40 | 0.11 | 2.82 | 2.70 | 2.35 | 82.72 | 6.54 |
1%Sn-12%V2O5/Al2O3 | 2.35 | 0.29 | 0.18 | 2.41 | 2.66 | 2.22 | 84.29 | 5.60 |
2%Sn-12%V2O5/Al2O3 | 2.27 | 0.33 | 0.17 | 2.18 | 2.69 | 1.70 | 85.20 | 5.46 |
4%Sn-12%V2O5/Al2O3 | 2.17 | 0.18 | 0.19 | 2.09 | 2.98 | 0.98 | 85.96 | 5.45 |
反应条件 | 甲烷/% | 乙烷/% | 乙烯/% | 丙烷/% | 丙烯/% | 正丁烷/% | 异丁烯/% | 其他 /% |
---|---|---|---|---|---|---|---|---|
临氢条件 | 2.35 | 0.29 | 0.18 | 2.41 | 2.66 | 2.22 | 84.29 | 5.60 |
非临氢条件 | 4.66 | 0.54 | 0.17 | 5.20 | 4.40 | 1.47 | 81.23 | 2.33 |
反应条件 | 甲烷/% | 乙烷/% | 乙烯/% | 丙烷/% | 丙烯/% | 正丁烷/% | 异丁烯/% | 其他 /% |
---|---|---|---|---|---|---|---|---|
临氢条件 | 2.35 | 0.29 | 0.18 | 2.41 | 2.66 | 2.22 | 84.29 | 5.60 |
非临氢条件 | 4.66 | 0.54 | 0.17 | 5.20 | 4.40 | 1.47 | 81.23 | 2.33 |
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