CIESC Journal ›› 2019, Vol. 70 ›› Issue (3): 922-928.DOI: 10.11949/j.issn.0438-1157.20181246
• Catalysis, kinetics and reactors • Previous Articles Next Articles
Hanlin WANG1(),Deqiang WANG2(),Kai WANG1(),Guangsheng LUO1
Received:
2018-10-22
Revised:
2018-12-28
Online:
2019-03-05
Published:
2019-03-05
Contact:
Deqiang WANG,Kai WANG
通讯作者:
王德强,王凯
作者简介:
<named-content content-type="corresp-name">王瀚琳</named-content>(1996—),男,本科生,<email>wanghl14@mails.tsinghua.edu.cn</email>|王德强(1973—),男,博士,讲师,<email>ciacwdq@163.com</email>|王凯(1983—),男,博士,副教授,<email>kaiwang@tsinghua.edu.cn</email>
基金资助:
CLC Number:
Hanlin WANG, Deqiang WANG, Kai WANG, Guangsheng LUO. Continuous synthesis of anisole in microreactor system[J]. CIESC Journal, 2019, 70(3): 922-928.
王瀚琳, 王德强, 王凯, 骆广生. 微反应器内苯甲醚连续合成[J]. 化工学报, 2019, 70(3): 922-928.
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URL: https://hgxb.cip.com.cn/EN/10.11949/j.issn.0438-1157.20181246
Q T /(ml·min-1) | T max /℃ | T max管道位置/m | 反应时间/min |
---|---|---|---|
2.83 | 74.9 | 7 | 7.77 |
5.66 | 83.1 | 9 | 2.50 |
11.3 | 89.9 | 9 | 1.66 |
22.6 | 94.9 | 9 | 1.25 |
28.3 | 97.7 | 9 | 1.00 |
33.8 | 95.6 | 9 | 0.84 |
45.3 | 94.3 | 11 | 0.76 |
Table 1 Relation between reaction time and flow rate
Q T /(ml·min-1) | T max /℃ | T max管道位置/m | 反应时间/min |
---|---|---|---|
2.83 | 74.9 | 7 | 7.77 |
5.66 | 83.1 | 9 | 2.50 |
11.3 | 89.9 | 9 | 1.66 |
22.6 | 94.9 | 9 | 1.25 |
28.3 | 97.7 | 9 | 1.00 |
33.8 | 95.6 | 9 | 0.84 |
45.3 | 94.3 | 11 | 0.76 |
n PhONa,0/n DMS,0 | PhONa质量分数/% | w PhONa/% | y DMS/% |
---|---|---|---|
1.0 | 20 | 56.6 | 56.6 |
0.9 | 20 | 57.8 | 52.0 |
0.8 | 20 | 59.6 | 47.7 |
1.0 | 30 | 80.4 | 80.4 |
0.9 | 30 | 82.4 | 74.2 |
0.8 | 30 | 86.4 | 69.1 |
1.0 | 40 | 89.2 | 89.2 |
0.9 | 40 | 93.5 | 84.2 |
0.8 | 40 | 93.6 | 74.9 |
Table 2 Effect of sodium phenolate concentration on its conversion and DMS utility
n PhONa,0/n DMS,0 | PhONa质量分数/% | w PhONa/% | y DMS/% |
---|---|---|---|
1.0 | 20 | 56.6 | 56.6 |
0.9 | 20 | 57.8 | 52.0 |
0.8 | 20 | 59.6 | 47.7 |
1.0 | 30 | 80.4 | 80.4 |
0.9 | 30 | 82.4 | 74.2 |
0.8 | 30 | 86.4 | 69.1 |
1.0 | 40 | 89.2 | 89.2 |
0.9 | 40 | 93.5 | 84.2 |
0.8 | 40 | 93.6 | 74.9 |
参数 | 实验条件 1 | 实验条件2 |
---|---|---|
PhONa质量分数/% | 30 | 40 |
n PhONa,0/n DMS,0 | 1.0 | 0.8 |
Q T/(ml·min-1) | 28.3 | 28.3 |
w PhONa/% | 80.9,81.3,80.4 | 93.6,93.5 |
y DMS/% | 80.9,81.3,80.4 | 74.9,74.8 |
Table 3 Results of repeated experiments
参数 | 实验条件 1 | 实验条件2 |
---|---|---|
PhONa质量分数/% | 30 | 40 |
n PhONa,0/n DMS,0 | 1.0 | 0.8 |
Q T/(ml·min-1) | 28.3 | 28.3 |
w PhONa/% | 80.9,81.3,80.4 | 93.6,93.5 |
y DMS/% | 80.9,81.3,80.4 | 74.9,74.8 |
操作时间/h | DMS/mol | PhOH/mol | NaOH/mol | PhONa质量分数/% | w PhONa/% |
---|---|---|---|---|---|
1 | 0.1 | 0.2 | 0.3 | 38.9 | 54.6 |
1 | 0.1 | 0.2 | 0.3 | 26.2 | 39.3 |
Table 4 Yield for batch synthesis of anisole[14]
操作时间/h | DMS/mol | PhOH/mol | NaOH/mol | PhONa质量分数/% | w PhONa/% |
---|---|---|---|---|---|
1 | 0.1 | 0.2 | 0.3 | 38.9 | 54.6 |
1 | 0.1 | 0.2 | 0.3 | 26.2 | 39.3 |
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