Chemical Industry and Engineering Progress ›› 2021, Vol. 40 ›› Issue (1): 39-47.DOI: 10.16085/j.issn.1000-6613.2020-0285
• Chemical processes and equipment • Previous Articles Next Articles
Zhe YANG1(), Dalai XI1, Ning LI1, Jun ZHOU2(
)
Received:
2020-03-02
Online:
2021-01-12
Published:
2021-01-05
Contact:
Jun ZHOU
通讯作者:
周军
作者简介:
杨哲(1990—),男,硕士,研究方向为微反应器技术研究及设备开发。E-mail:基金资助:
CLC Number:
Zhe YANG, Dalai XI, Ning LI, Jun ZHOU. Numerical simulation and experimental performance evaluation of microchannel structure[J]. Chemical Industry and Engineering Progress, 2021, 40(1): 39-47.
杨哲, 郗大来, 李宁, 周军. 微通道结构数值模拟及实验性能评价[J]. 化工进展, 2021, 40(1): 39-47.
微通道形式 | 网格划分 | 局部放大图 | 网格总数/×104个 | 料液出口温度/℃ |
---|---|---|---|---|
U形 直线形 | ![]() | ![]() | 7.05 | 78.5 |
7.25 | 84.4 | |||
7.45 | 85.0 | |||
7.65 | 85.2 | |||
伞形 | ![]() | ![]() | 6.25 | 76.0 |
6.45 | 80.5 | |||
6.65 | 81.0 | |||
6.85 | 81.5 | |||
菱形 | ![]() | ![]() | 8.35 | 81.4 |
8.55 | 85.7 | |||
8.75 | 86.0 | |||
8.95 | 86.5 |
微通道形式 | 网格划分 | 局部放大图 | 网格总数/×104个 | 料液出口温度/℃ |
---|---|---|---|---|
U形 直线形 | ![]() | ![]() | 7.05 | 78.5 |
7.25 | 84.4 | |||
7.45 | 85.0 | |||
7.65 | 85.2 | |||
伞形 | ![]() | ![]() | 6.25 | 76.0 |
6.45 | 80.5 | |||
6.65 | 81.0 | |||
6.85 | 81.5 | |||
菱形 | ![]() | ![]() | 8.35 | 81.4 |
8.55 | 85.7 | |||
8.75 | 86.0 | |||
8.95 | 86.5 |
反应器型式 | 收率/% | 进料流量/mL·min-1 | 停留时间/min |
---|---|---|---|
U形直线形微结构 | 90 | 12.00 | 2.1 |
伞形微结构 | 92 | 12.00 | 3.5 |
菱形微结构 | 97 | 12.00 | 2.8 |
常规反应器 | 82 | — | 300 |
反应器型式 | 收率/% | 进料流量/mL·min-1 | 停留时间/min |
---|---|---|---|
U形直线形微结构 | 90 | 12.00 | 2.1 |
伞形微结构 | 92 | 12.00 | 3.5 |
菱形微结构 | 97 | 12.00 | 2.8 |
常规反应器 | 82 | — | 300 |
反应器型式 | 收率/% | 进料流量/mL·min-1 | 停留时间/min |
---|---|---|---|
U形直线形微结构 | 32 | 12.00 | 0.1 |
伞形微结构 | 45 | 12.00 | 0.25 |
菱形微结构 | 97 | 12.00 | 2.8 |
反应器型式 | 收率/% | 进料流量/mL·min-1 | 停留时间/min |
---|---|---|---|
U形直线形微结构 | 32 | 12.00 | 0.1 |
伞形微结构 | 45 | 12.00 | 0.25 |
菱形微结构 | 97 | 12.00 | 2.8 |
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