Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (9): 4779-4792.DOI: 10.16085/j.issn.1000-6613.2023-1335
• Chemical processes and equipment • Previous Articles
LI Chuanxi(), LU Xu, LI Yang, LI Wenbing, WEI Xiaohui, LI Jin, LIU Shi, YANG Weisheng()
Received:
2023-08-04
Revised:
2023-09-10
Online:
2024-09-30
Published:
2024-09-15
Contact:
YANG Weisheng
李传玺(), 鲁旭, 李阳, 李文冰, 魏晓慧, 李金, 刘时, 杨卫胜()
通讯作者:
杨卫胜
作者简介:
李传玺(1993—),男,博士,研究方向为化工过程开发及优化。E-mail:lichuanxi010@petrochina.com.cn。
CLC Number:
LI Chuanxi, LU Xu, LI Yang, LI Wenbing, WEI Xiaohui, LI Jin, LIU Shi, YANG Weisheng. Research progress on preparation technology of norbornene[J]. Chemical Industry and Engineering Progress, 2024, 43(9): 4779-4792.
李传玺, 鲁旭, 李阳, 李文冰, 魏晓慧, 李金, 刘时, 杨卫胜. 降冰片烯制备工艺进展[J]. 化工进展, 2024, 43(9): 4779-4792.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2023-1335
项目 | 气相工艺 | 液相工艺 | 气液相结合 |
---|---|---|---|
反应温度 | ≥300℃ | 170~260℃ | 170~350℃ |
停留时间 | 0.3s~1.5min | 2~5h | — |
优点 | 转化率高 | 操作温度低,相对安全 | 兼顾气相、液相解聚的优点 |
缺点 | 温度高,反应剧烈,壁面易形成高聚物 | 反应时间长,釜底容易生成多聚物结焦 | — |
稀释剂 | CO2、N2、水蒸气、脂肪烃、芳烃等 | 高沸点脂肪烃、芳香烃 | — |
阻聚剂 | 丁炔二酸、对苯二酚、苯醌、四甲基哌啶醇、四甲基儿茶酚、复配阻聚剂 |
项目 | 气相工艺 | 液相工艺 | 气液相结合 |
---|---|---|---|
反应温度 | ≥300℃ | 170~260℃ | 170~350℃ |
停留时间 | 0.3s~1.5min | 2~5h | — |
优点 | 转化率高 | 操作温度低,相对安全 | 兼顾气相、液相解聚的优点 |
缺点 | 温度高,反应剧烈,壁面易形成高聚物 | 反应时间长,釜底容易生成多聚物结焦 | — |
稀释剂 | CO2、N2、水蒸气、脂肪烃、芳烃等 | 高沸点脂肪烃、芳香烃 | — |
阻聚剂 | 丁炔二酸、对苯二酚、苯醌、四甲基哌啶醇、四甲基儿茶酚、复配阻聚剂 |
参数 | 乙烯 | CPD | NB | DCPD | 甲苯 |
---|---|---|---|---|---|
熔点①/℃ | -169.4 | -90 | 44.5 | 33.6 | -95 |
沸点①/℃ | -104.1 | 41 | 96 | 170 | 110.6 |
临界温度/℃ | 9.3① | 233.9②/259.5③ | 316.8① | 386.9②/391.3③ | 319.8① |
临界压力/MPa | 5.06① | 5.15②/5.01③ | 4.86① | 3.06②/3.36③ | 4.1① |
参数 | 乙烯 | CPD | NB | DCPD | 甲苯 |
---|---|---|---|---|---|
熔点①/℃ | -169.4 | -90 | 44.5 | 33.6 | -95 |
沸点①/℃ | -104.1 | 41 | 96 | 170 | 110.6 |
临界温度/℃ | 9.3① | 233.9②/259.5③ | 316.8① | 386.9②/391.3③ | 319.8① |
临界压力/MPa | 5.06① | 5.15②/5.01③ | 4.86① | 3.06②/3.36③ | 4.1① |
项目 | 气相工艺 | 液相工艺 | 超临界工艺 |
---|---|---|---|
特点 | 使DCPD/CPD汽化,与乙烯混合进行反应 | DCPD/CPD在反应过程中呈液态,乙烯气体溶于液相后进行加成反应 | 反应物处于超临界状态 |
温度 | 220~340℃ | 150~320℃ | 180~300℃ |
压力 | 1.22~6.9MPa | 1.2~68.9MPa | 5~30MPa |
停留时间 | 4s~30min | 6min~10h | — |
优点 | 物料混合充分,选择性高 | 相对安全,易于实现规模化生产 | 强化传质、传热效率,减少副反应发生 |
缺点 | 物料摩尔体积大,高温带来更多安全隐患 | 副反应多,容易产生多聚物堵塞设备,加入惰性溶剂可以有效抑制副反应 | — |
稀释剂 | H2等 | 高沸点惰性烷烃溶剂、卤代烃溶剂 | — |
项目 | 气相工艺 | 液相工艺 | 超临界工艺 |
---|---|---|---|
特点 | 使DCPD/CPD汽化,与乙烯混合进行反应 | DCPD/CPD在反应过程中呈液态,乙烯气体溶于液相后进行加成反应 | 反应物处于超临界状态 |
温度 | 220~340℃ | 150~320℃ | 180~300℃ |
压力 | 1.22~6.9MPa | 1.2~68.9MPa | 5~30MPa |
停留时间 | 4s~30min | 6min~10h | — |
优点 | 物料混合充分,选择性高 | 相对安全,易于实现规模化生产 | 强化传质、传热效率,减少副反应发生 |
缺点 | 物料摩尔体积大,高温带来更多安全隐患 | 副反应多,容易产生多聚物堵塞设备,加入惰性溶剂可以有效抑制副反应 | — |
稀释剂 | H2等 | 高沸点惰性烷烃溶剂、卤代烃溶剂 | — |
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