journal article·2022-01Open access

Optimization of initiator contents in room temperature polymerization of methyl methacrylate

Ming Gong, Daijun Zhang, Jiayang Zhang, Jun Li, Xiangbao Chen

Abstract

Vinyl polymerization is an important path for in-situ polymerization of thermoplastic resins. BPO (Benzoyl peroxide) and DMT (dimethyl-p-toluidine) were chosen to initiate the radical polymerization of MMA (methyl methacrylate) in this work. Optimization of initiator concentration was studied through reaction rate of polymerization progress and properties of PMMA (polymethyl methacrylate). At first, the catalytic of DMT in MMA polymerization was studied through polymerization experiments and rheological experiments. Results showed that DMT could catalyze more than one molecular BPO in the whole reaction period. It can catalyze the decomposition of BPO after being connected to PMMA chains. Second, the BPO: DMT ratio was set to 2:1 to study the ideal content by comparing the mechanical properties of PMMA. Results showed that with the increase of initiator contents, T g , molecular weight, and residual monomer were all declining. Meanwhile, the mechanical properties of PMMA matrix first increased and then decreased. This phenomenon was analyzed by 1H-NMR and SEM. And the optimal BPO-DMT concentration was 1.0 mol%–0.5 mol%.
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Research context

OpenAlex topics: Advanced Polymer Synthesis and Characterization · Epoxy Resin Curing Processes · Injection Molding Process and Properties

SciVX discovery tags are terminology-based. OpenAlex topics are source-provided classifications.

Affiliations

Aero Engine Corporation of China Beijing Institute of Aeronautical Materials, Beijing, China

National Key Laboratory of Advanced Composites, Beijing, China

Funding

National Key Laboratory of Advanced Composite Materials

References (33)

Show source-provided references
1. 10.1016/j.compositesa.2006.05.00710.1016/j.compositesa.2006.05.007 ↗
2. 10.3144/expresspolymlett.2017.3210.3144/expresspolymlett.2017.32 ↗
3. Köhler T · IOP Conf · 2017 · 254 · 042019
4. 10.1016/S0168-874X(03)00119-710.1016/S0168-874X(03)00119-7 ↗
5. 10.1002/pc.2007410.1002/pc.20074 ↗
6. 10.1177/089270570505441210.1177/0892705705054412 ↗
7. 10.1016/j.compositesa.2017.10.02210.1016/j.compositesa.2017.10.022 ↗
8. Liu G · Chem Engineering Equipment · 2018 · 5 · 1
9. 10.1002/macp.1948.02001030110.1002/macp.1948.020010301 ↗
10. 10.1002/mats.20070000310.1002/mats.200700003 ↗
11. 10.1002/macp.1975.02176030310.1002/macp.1975.021760303 ↗
12. Feng X · J Macromolecules · 2005 · 4 · 27
13. Cao W · Acta Macromolecular Sinica · 1982 · 1 · 96
14. Fu J · Acta Polymerica Sinica · 1990 · 1 · 67
15. Qiu K · Acta Polymerica Sinica · 1988 · 1 · 74
16. Qiu K · Polym Communications · 1985 · 1 · 58
17. 10.1177/0022034579058010060110.1177/00220345790580100601 ↗
18. 10.1016/S0032-3861(96)01014-210.1016/S0032-3861(96)01014-2 ↗
19. 10.4012/dmj.2018-16610.4012/dmj.2018-166 ↗
20. Liu Y · Polym Materials Science Engineering · 2018 · 34 · 36
21. 10.1002/(SICI)1099-0518(19960930)34:13<2783::AID-POLA24>3.0.CO;2-710.1002/(SICI)1099-0518(19960930)34:13<2783::AID-POLA24>3.0.CO;2-7 ↗
22. 10.1016/S1385-8947(98)00064-310.1016/S1385-8947(98)00064-3 ↗
23. 10.1002/macp.1997.02198051810.1002/macp.1997.021980518 ↗
24. Xiao B · Plastics Industry · 1988 · 5 · 27
25. 10.1002/marc.20040040710.1002/marc.200400407 ↗
26. 10.1002/app.4739110.1002/app.47391 ↗
27. 10.1002/app.3321410.1002/app.33214 ↗
28. 10.1016/0032-3861(93)90084-N10.1016/0032-3861(93)90084-N ↗
29. Zoller A · Polym Chemistry · 2015 · 31 · 1
30. 10.2514/3.59410.2514/3.594 ↗
31. Zhang D · Chem Production Technology · 2010 · 17 · 28
32. 10.1103/PhysRevA.33.362810.1103/PhysRevA.33.3628 ↗
33. 10.1023/A:101856580772710.1023/A:1018565807727 ↗