Reactive extrusion recycling of polymethyl methacrylate to methyl methacrylate and methacrylic acid

The global production of polymethyl methacrylate (PMMA) reached 4 million tonnes annually, yet only 10% of PMMA, primarily post-industrial scraps, is recycled. Recycling end-of-life PMMA, which often contains additives or composite components, poses challenges in achieving crude methyl methacrylate (MMA) monomer with comparable purity to post-industrial scraps. Hydrolyzing end-of-life PMMA presents a viable alternative to produce methacrylic acid (MAA) and simplifies the purification process of crude MMA. However, current PMMA hydrolysis is limited to lab-scale and batch operations in fluidized/fixed beds and stirred tank reactors. In this study, we demonstrate a pilot-scale, two-stage reactive hydrolysis extrusion system for the continuous conversion of injection- and extrusion-grade PMMA scraps into MMA and/or MAA at 330 °C to 370 °C. Residence time distribution (RTD) tests characterized the hydrodynamics of the screw configuration for PMMA extrusion, revealing that lower screw speed and feeding rate increase reaction time. A Plackett-Burman design identified temperature and catalyst type as significant factors for MMA hydrolysis. Under optimized conditions, hydrolysis extrusion without any catalysts achieved the highest MMA yield of 89% and 96% PMMA conversion. Hydrolysis extrusion with 10% H-type zeolite Y with an SiO 2 /Al 2 O 3 ratio of 80 at 370 °C resulted in a 5.3% MAA yield, a 67% MMA yield, and near-complete PMMA conversion. Liquid acid catalysts directly hydrolyzed PMMA to poly(MMA-co-MAA) copolymer and/or PMAA, followed by dehydration of two adjacent acid groups to form six-member glutaric anhydride. KOH solution hydrolyzed PMMA to poly(MMA-co-MAA) and/or PMAA potassium salt. • A two-stage reactive hydrolysis extrusion system recycles PMMA continuously. • Non-catalytic reactive hydrolysis extrusion converts 96% PMMA at a 89% MMA yield. • Acid and alkali solutions hydrolyze PMMA to poly(MMA-co-MAA) and its salt. • Hydrolysis extrusion with 10% HY(80) yields 5.3% MAA and 100% PMMA conversion. • Switching from vacuum to atmospheric degassing boosts MMA yield by 4.8 times.

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-05-14
DOI
https://doi.org/10.1016/j.cej.2025.162709
Citations
4
Primary Topic
biodegradable polymer synthesis and properties
Type
article
Field-Weighted Citation Impact
2.39

Funders

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article

Reactive extrusion recycling of polymethyl methacrylate to methyl methacrylate and methacrylic acid

Yanfa Zhuang, Nguyen Tien Dat, Jean‐Luc Dubois, Mahdi Sharifian et al.
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Chemical Engineering Journal
biodegradable polymer synthesis and properties
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article

Reactive extrusion recycling of polymethyl methacrylate to methyl methacrylate and methacrylic acid

Yanfa Zhuang, Nguyen Tien Dat, Jean‐Luc Dubois, Mahdi Sharifian, Abdellah Ajji, Gregory Scott Patience
article en
4 citations

Abstract

The global production of polymethyl methacrylate (PMMA) reached 4 million tonnes annually, yet only 10% of PMMA, primarily post-industrial scraps, is recycled. Recycling end-of-life PMMA, which often contains additives or composite components, poses challenges in achieving crude methyl methacrylate (MMA) monomer with comparable purity to post-industrial scraps. Hydrolyzing end-of-life PMMA presents a viable alternative to produce methacrylic acid (MAA) and simplifies the purification process of crude MMA. However, current PMMA hydrolysis is limited to lab-scale and batch operations in fluidized/fixed beds and stirred tank reactors. In this study, we demonstrate a pilot-scale, two-stage reactive hydrolysis extrusion system for the continuous conversion of injection- and extrusion-grade PMMA scraps into MMA and/or MAA at 330 °C to 370 °C. Residence time distribution (RTD) tests characterized the hydrodynamics of the screw configuration for PMMA extrusion, revealing that lower screw speed and feeding rate increase reaction time. A Plackett-Burman design identified temperature and catalyst type as significant factors for MMA hydrolysis. Under optimized conditions, hydrolysis extrusion without any catalysts achieved the highest MMA yield of 89% and 96% PMMA conversion. Hydrolysis extrusion with 10% H-type zeolite Y with an SiO 2 /Al 2 O 3 ratio of 80 at 370 °C resulted in a 5.3% MAA yield, a 67% MMA yield, and near-complete PMMA conversion. Liquid acid catalysts directly hydrolyzed PMMA to poly(MMA-co-MAA) copolymer and/or PMAA, followed by dehydration of two adjacent acid groups to form six-member glutaric anhydride. KOH solution hydrolyzed PMMA to poly(MMA-co-MAA) and/or PMAA potassium salt. • A two-stage reactive hydrolysis extrusion system recycles PMMA continuously. • Non-catalytic reactive hydrolysis extrusion converts 96% PMMA at a 89% MMA yield. • Acid and alkali solutions hydrolyze PMMA to poly(MMA-co-MAA) and its salt. • Hydrolysis extrusion with 10% HY(80) yields 5.3% MAA and 100% PMMA conversion. • Switching from vacuum to atmospheric degassing boosts MMA yield by 4.8 times.

Chemical Engineering JournalVol. 515
Institut de Relations Internationales et Stratégiques (FR), Polytechnique Montréal (CA)
Université de Montréal, Natural Sciences and Engineering Research Council of Canada
Clean water and sanitation
Openalex Percentile: Top 12%
biodegradable polymer synthesis and properties
2.39
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