化工学报 ›› 2021, Vol. 72 ›› Issue (7): 3832-3838.DOI: 10.11949/0438-1157.20210208
韩维辰1(),王佳铭1,贺曼罗2,贺高红1,焉晓明1,阮雪华1()
收稿日期:
2021-02-03
修回日期:
2021-04-19
出版日期:
2021-07-05
发布日期:
2021-07-05
通讯作者:
阮雪华
作者简介:
韩维辰(1995—),男,硕士研究生,基金资助:
HAN Weichen1(),WANG Jiaming1,HE Manluo2,HE Gaohong1,YAN Xiaoming1,RUAN Xuehua1()
Received:
2021-02-03
Revised:
2021-04-19
Online:
2021-07-05
Published:
2021-07-05
Contact:
RUAN Xuehua
摘要:
间苯二甲胺(MXDA)与甲基异丁基酮(MIBK)合成的甲基异丁基酮二亚胺(MIBKDI),是单组分环氧胶常用的潜伏型固化剂。反应残余的MXDA,可直接与环氧树脂发生交联,显著降低储存稳定性。工业生产通过超高酮胺比使MXDA充分转化,但MIBK损失大、回收能耗高。本研究首先采用正交实验对反应温度、时间和酮胺比进行权重分析和因素效应分析,然后通过单因素实验系统研究反应时间、酮胺比对MXDA转化率的影响。结果表明,酮胺摩尔比超过5∶1(反应温度170℃、时间4 h)制备的固化剂,储存稳定性满足市场需求。在典型条件下,环氧树脂完全固化后剪切强度12.9 MPa,拉伸强度19.2 MPa,达到国家标准GB/T 2567—2008要求。与工业方案相比,酮胺比优化为5∶1以后,能耗大大降低,同时MIBK消耗有效节约,总成本得到客观降低。
中图分类号:
韩维辰, 王佳铭, 贺曼罗, 贺高红, 焉晓明, 阮雪华. 潜伏型环氧固化剂甲基异丁基酮二亚胺的合成及工艺优化[J]. 化工学报, 2021, 72(7): 3832-3838.
HAN Weichen, WANG Jiaming, HE Manluo, HE Gaohong, YAN Xiaoming, RUAN Xuehua. Process optimization for synthesizing latent epoxy curing agent based on methyl isobutyl ketone and m-xylylenediamine[J]. CIESC Journal, 2021, 72(7): 3832-3838.
Experiment | A T/°C | B θ/ h | C MIBK∶MXDA | Conversion/% |
---|---|---|---|---|
P-1 | 140 | 1 | 2∶1 | 20 |
P-2 | 140 | 2 | 3∶1 | 32 |
P-3 | 140 | 3 | 4∶1 | 48 |
P-4 | 140 | 4 | 5∶1 | 64 |
P-5 | 140 | 5 | 6∶1 | 78 |
P-6 | 150 | 1 | 3∶1 | 30 |
P-7 | 150 | 2 | 4∶1 | 52 |
P-8 | 150 | 3 | 5∶1 | 72 |
P-9 | 150 | 4 | 6∶1 | 83 |
P-10 | 150 | 5 | 2∶1 | 40 |
P-11 | 160 | 1 | 4∶1 | 40 |
P-12 | 160 | 2 | 5∶1 | 62 |
P-13 | 160 | 3 | 6∶1 | 85 |
P-14 | 160 | 4 | 2∶1 | 42 |
P-15 | 160 | 5 | 3∶1 | 58 |
P-16 | 170 | 1 | 5∶1 | 56 |
P-17 | 170 | 2 | 6∶1 | 67 |
P-18 | 170 | 3 | 2∶1 | 48 |
P-19 | 170 | 4 | 3∶1 | 65 |
P-20 | 170 | 5 | 4∶1 | 83 |
P-21 | 180 | 1 | 6∶1 | 37 |
P-22 | 180 | 2 | 2∶1 | 32 |
P-23 | 180 | 3 | 3∶1 | 55 |
P-24 | 180 | 4 | 4∶1 | 67 |
P-25 | 180 | 5 | 5∶1 | 85 |
表1 固化剂MIBKDI合成条件的正交实验结果
Table 1 Orthogonal experiment results about MIBKDI synthesis condition
Experiment | A T/°C | B θ/ h | C MIBK∶MXDA | Conversion/% |
---|---|---|---|---|
P-1 | 140 | 1 | 2∶1 | 20 |
P-2 | 140 | 2 | 3∶1 | 32 |
P-3 | 140 | 3 | 4∶1 | 48 |
P-4 | 140 | 4 | 5∶1 | 64 |
P-5 | 140 | 5 | 6∶1 | 78 |
P-6 | 150 | 1 | 3∶1 | 30 |
P-7 | 150 | 2 | 4∶1 | 52 |
P-8 | 150 | 3 | 5∶1 | 72 |
P-9 | 150 | 4 | 6∶1 | 83 |
P-10 | 150 | 5 | 2∶1 | 40 |
P-11 | 160 | 1 | 4∶1 | 40 |
P-12 | 160 | 2 | 5∶1 | 62 |
P-13 | 160 | 3 | 6∶1 | 85 |
P-14 | 160 | 4 | 2∶1 | 42 |
P-15 | 160 | 5 | 3∶1 | 58 |
P-16 | 170 | 1 | 5∶1 | 56 |
P-17 | 170 | 2 | 6∶1 | 67 |
P-18 | 170 | 3 | 2∶1 | 48 |
P-19 | 170 | 4 | 3∶1 | 65 |
P-20 | 170 | 5 | 4∶1 | 83 |
P-21 | 180 | 1 | 6∶1 | 37 |
P-22 | 180 | 2 | 2∶1 | 32 |
P-23 | 180 | 3 | 3∶1 | 55 |
P-24 | 180 | 4 | 4∶1 | 67 |
P-25 | 180 | 5 | 5∶1 | 85 |
因素效应 | A T/°C | B θ/ h | C MIBK∶MXDA |
---|---|---|---|
k1/% | 48.4 | 36.6 | 36.4 |
k2/% | 55.4 | 50.6 | 48.0 |
k3/% | 59.0 | 61.6 | 58.0 |
k4/% | 63.8 | 64.2 | 69.4 |
k5/% | 55.2 | 68.8 | 70.0 |
F | 0.24 | 1.23 | 1.53 |
optimum group | A4 | B5 | C5 |
表2 固化剂MIBKDI合成工艺中MXDA转化率的极差分析
Table 2 Range analysis for MXDA conversion in MIBKDI synthesis
因素效应 | A T/°C | B θ/ h | C MIBK∶MXDA |
---|---|---|---|
k1/% | 48.4 | 36.6 | 36.4 |
k2/% | 55.4 | 50.6 | 48.0 |
k3/% | 59.0 | 61.6 | 58.0 |
k4/% | 63.8 | 64.2 | 69.4 |
k5/% | 55.2 | 68.8 | 70.0 |
F | 0.24 | 1.23 | 1.53 |
optimum group | A4 | B5 | C5 |
Sample | MIBK∶MXDA | Reaction time/h | MXDA/ %(mass) | MIBK/ %(mass) | MIBKDI/ %(mass) | Amine value |
---|---|---|---|---|---|---|
S-1 | 4∶1 | 5 | 10.0 | 1.0 | 89.0 | 327 |
S-2 | 5∶1 | 4 | 4.1 | 0.8 | 95.1 | 283 |
S-3 | 5∶1 | 5 | 1.9 | 0.9 | 97.2 | 279 |
S-4 | 6∶1 | 4 | 2.2 | 0.8 | 97.0 | 275 |
S-5 | 6∶1 | 5 | 1.1 | 0.8 | 98.1 | 273 |
S-6 | 10∶1 | 5 | 0.4 | 0.6 | 99.0 | 271 |
表3 不同反应条件对固化剂MIBKDI组成及胺值的影响
Table 3 Effects of synthesis condition on MIBKDI curing agent's composition and amine value
Sample | MIBK∶MXDA | Reaction time/h | MXDA/ %(mass) | MIBK/ %(mass) | MIBKDI/ %(mass) | Amine value |
---|---|---|---|---|---|---|
S-1 | 4∶1 | 5 | 10.0 | 1.0 | 89.0 | 327 |
S-2 | 5∶1 | 4 | 4.1 | 0.8 | 95.1 | 283 |
S-3 | 5∶1 | 5 | 1.9 | 0.9 | 97.2 | 279 |
S-4 | 6∶1 | 4 | 2.2 | 0.8 | 97.0 | 275 |
S-5 | 6∶1 | 5 | 1.1 | 0.8 | 98.1 | 273 |
S-6 | 10∶1 | 5 | 0.4 | 0.6 | 99.0 | 271 |
Synthesis condition | Distillation/ h | Material consumption | Energy consumption | Total cost/ CNY | ||||
---|---|---|---|---|---|---|---|---|
MIBK∶MXDA | Time/h | MXDA/g | MIBK/g | Cost/CNY | Power/kWh | Cost/CNY | ||
5∶1 | 4 | 2.0 | 480 | 910 | 54.3 | 17.5 | 14.0 | 68.3 |
6∶1 | 4 | 2.5 | 470 | 960 | 54.4 | 21.0 | 16.8 | 71.2 |
10∶1 | 5 | 4.0 | 460 | 1210 | 58.0 | 34.5 | 27.6 | 85.6 |
表4 固化剂MIBKDI(每千克)生产成本
Table 4 Production cost about MIBKDI curing agent under various process conditions
Synthesis condition | Distillation/ h | Material consumption | Energy consumption | Total cost/ CNY | ||||
---|---|---|---|---|---|---|---|---|
MIBK∶MXDA | Time/h | MXDA/g | MIBK/g | Cost/CNY | Power/kWh | Cost/CNY | ||
5∶1 | 4 | 2.0 | 480 | 910 | 54.3 | 17.5 | 14.0 | 68.3 |
6∶1 | 4 | 2.5 | 470 | 960 | 54.4 | 21.0 | 16.8 | 71.2 |
10∶1 | 5 | 4.0 | 460 | 1210 | 58.0 | 34.5 | 27.6 | 85.6 |
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