Importance of the topic
Mechanical recycling of commodity polymers like polypropylene (PP) often leads to molecular degradation and loss of performance, limiting reuse in high-value applications. Reactive extrusion with compatibilizers offers a scalable route to upcycle reprocessed PP (rPP) into robust blends with engineering polymers such as polyamide 12 (PA12). This study demonstrates a validated workflow combining twin-screw reactive extrusion, rheology, mechanical testing, and micro-ATR FTIR chemical imaging to quantify interfacial stabilization, recover mechanical properties, and provide objective metrics for process optimization.
Objectives and study overview
- Assess the impact of reactive extrusion using PP grafted with maleic anhydride (PP-g-MA) to compatibilize blends of PA12 with 50% rPP.
- Characterize molecular and morphological consequences of reprocessing and reactive blending via oscillatory rheology, tensile testing, DSC, and micro-ATR FTIR mapping.
- Establish quantitative chemical-homogeneity metrics from FTIR maps to correlate with rheological and mechanical performance.
Materials and methods
- Materials: virgin PP (vPP), reprocessed PP (rPP generated by high-shear reprocessing), PA12, and PP-g-MA compatibilizer.
- Blend formulations: Reactive blend = 50% PA12 / 40% rPP / 10% PP-g-MA; Non-reactive = 50% PA12 / 50% rPP.
- Reactive compounding: Thermo Scientific Process 11 co-rotating twin-screw extruder with modular screw (11 mm; 40 L/D). Typical processing: ~400 rpm, ~40 s residence time; reactive blending performed at ~185–200 °C.
- Specimen production: HAAKE MiniJet Pro piston injection molder to produce discs for rheology and dog-bone tensile bars.
- Thermal analysis: DSC to track crystallinity changes after reprocessing and in blends.
Used instrumentation
- Thermo Scientific Process 11 Twin-Screw Extruder (modular co-rotating screws).
- Thermo Scientific HAAKE MiniJet Pro Injection Molding System.
- Thermo Scientific HAAKE MARS iQ rotational rheometer (parallel plate geometry; amplitude and frequency sweeps).
- Thermo Scientific Nicolet RaptIR+ FTIR Microscope with diamond ATR for micro-ATR chemical mapping (10 × 10 µm sampling, >1000 spectra per map).
Key methodological details
- rPP produced by reprocessing vPP at 400 rpm with temperature profile from 120 °C to 200 °C (die at 190 °C), generating practical recycled feedstock showing molecular degradation.
- Rheology: amplitude sweeps to determine LVR and frequency sweeps (oscillatory) at 180 °C for PP samples and 220 °C for blends; Cox–Merz considerations applied to interpret complex viscosity.
- FTIR mapping: micro-ATR spectra collected at 8 cm⁻¹ resolution with 64 scans per point; chemical markers chosen were PA12 amide I (~1636 cm⁻¹) and PP methyl deformation (~1376 cm⁻¹). A PA12/PP peak-area ratio was computed for each spectrum (areas: 1680–1610 cm⁻¹ for PA12; 1390–1345 cm⁻¹ for PP) to quantify local composition and generate histogram/statistics.
Main results and discussion
- Reprocessing effects: DSC indicated a decrease in PP crystallinity from 63.1% (vPP) to 58.1% (rPP), consistent with chain scission under high shear. Rheology of rPP showed reduced plateau storage modulus (G') and complex viscosity relative to vPP, reflecting lower molecular weight and fewer entanglements.
- Reactive compatibilization: In reactive blends (10% PP-g-MA), in situ reaction between maleic anhydride grafts and PA12 terminal amines forms interfacial diblock copolymers. No bulk crosslinking or torque spikes were observed, indicating interfacial rather than bulk chemistry.
- Rheological signatures: Reactive blends exhibited higher G' across the LVR, increased low-frequency elasticity, and an extended LVR compared to non-reactive blends. These features indicate constrained relaxation and enhanced interfacial elasticity from copolymer anchoring.
- Mechanical performance: Both blends showed increased modulus relative to neat PA12 (attributed to semi-crystalline PP reinforcement). Tensile strength of the non-reactive blend decreased substantially (≈32.5 MPa vs 41.8 MPa for PA12), consistent with weak interfaces. The reactive blend recovered tensile strength to near-PA12 levels (~41.9 MPa) and increased yield stress (from ~15.0 to ~20.2 MPa), demonstrating effective stress transfer and suppression of interfacial debonding.
- FTIR chemical mapping: High-density micro-ATR maps (>1000 spectra per area at 10×10 µm resolution) enabled quantitative phase analysis. Reactive blend ratio values (PA12/PP area) ranged narrowly 2.6–4.8 (std dev = 0.306), implying homogeneous mixing and domain sizes below the 10 µm spatial resolution. Non-reactive blend ratios ranged widely 1–12 (std dev = 1.65) with near-pure domains detected (~1% mapped area), indicating poor mixing and large phase heterogeneity.
- Correlation across techniques: Narrower composition histograms, higher G' and extended LVR, and recovery of tensile strength converge to show that reactive extrusion with PP-g-MA stabilizes morphology and restores performance in blends with 50% recycled PP.
Benefits and practical applications
- Enables incorporation of high fractions of recycled PP into engineering-grade PA12 while retaining mechanical integrity—supporting circular economy goals.
- Reactive extrusion provides in-line compatibilization that prevents bulk gelation and targets interfacial chemistry, scalable to industrial twin-screw platforms.
- Micro-ATR FTIR mapping offers an objective, quantitative metric (ratio histograms and standard deviation) for assessing compatibilization efficacy and for process control/optimization.
- Combined rheology-mechanics-chemical imaging workflow accelerates formulation development by linking process parameters (screw design, mixing intensity, compatibilizer content) to measurable performance outcomes.
Future trends and opportunities
- Refinement of screw element design and residence-time/temperature profiles to maximize interfacial area while minimizing thermal/mechanical degradation of recycled streams.
- Extension to other immiscible polymer pairs and exploration of alternative reactive compatibilizers (tailored graft densities, multifunctional chemistries) to broaden material combinations.
- Integration of in-line spectroscopic monitoring (e.g., on-line ATR-FTIR) for real-time control of compatibilization kinetics and to reduce offline testing cycles.
- Application of higher-resolution chemical imaging (e.g., AFM-IR or synchrotron-based techniques) to resolve sub-micron domain structure and further link morphology to fatigue, impact, and long-term durability.
Conclusion
This application study demonstrates that reactive twin-screw extrusion using PP-g-MA effectively upcycles reprocessed PP into PA12-based blends containing 50% recycled content. Interfacial diblock copolymer formation yields stabilized morphologies, reflected in rheological signatures (elevated G' and extended LVR), quantitative micro-ATR FTIR homogeneity metrics, and recovery of tensile strength to near-virgin PA12 values. The combined analytical workflow provides robust, quantitative indicators for process optimization and supports scalable strategies for performance-oriented polymer recycling.
References
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- Crawford NC. Thermo Fisher Application Note AN56376 – Examining the rheological behavior of three nearly identical linear low-density polyethylene (LLDPE) samples. Thermo Fisher Scientific.
- Cox WP, Merz EH. Correlation of dynamic and steady flow viscosities. Journal of Polymer Science, 28, 619 (1958).
- Effect of PP-g-MAH compatibilizer content in polypropylene/nylon-6 blends. Polymer Bulletin. Springer Nature.
- Lee HG, Sung Y-T, Lee YK, Kim WN, Yoon HG, Lee HS. Effects of PP-g-MAH on the mechanical, morphological and rheological properties of polypropylene and poly(acrylonitrile-butadiene-styrene) blends, 2009.
- Effect of different polypropylenes and compatibilizers on the rheological, mechanical and morphological properties of nylon 6/PP blends. Journal of Materials Science. Springer Nature.
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