SubjectsRecycling TechnologyLesson 04 · Chemical Recycling: Pyrolysis, Depolymerisation & Solvolysis Pathways
Circular EconomyLesson 0419 PPE Syllabus Aligned

Chemical Recycling: Pyrolysis, Depolymerisation & Solvolysis Pathways

Go beyond mechanical recycling to understand the advanced chemical processes that can handle contaminated, mixed, or multi-layer plastics that mechanical recycling cannot — and why global investment is flooding into this space.

~35 min technical deep-dive·Standard Indian Curricula (CIPET / Anna Univ / ICT)

01 · Why This Matters in Industry & GATE XE-F

Applied directly across petrochemical refining, compounding plants, mold-flow simulations, and automotive part manufacturing (e.g., Reliance Industries, Supreme Petrochem, IOCL, CIPET testing protocols).

1

Molecular Mechanism: Master conformational physics, transition temperatures, and reaction kinetics.

2

Process & Quality: Predict viscosity behavior, solve molding defects, and apply ASTM/ISO testing standards.

02 · Technical Theory & Governing Equations

Chemical Recycling: Pyrolysis, Depolymerisation & Solvolysis Pathways

Plastic classification and municipal sorting station - Visual reference for Chemical Recycling: Pyrolysis, Depolymerisation & Solvolysis Pathways
Plastic classification and municipal sorting station - Visual reference for Chemical Recycling: Pyrolysis, Depolymerisation & Solvolysis Pathways

1. Why This Topic Matters

Mechanical recycling is limited by degradation (loss of properties after repeated extrusions) and cannot easily process mixed, contaminated, or multi-layer plastics. Chemical recycling (tertiary recycling) overcomes these limits by cracking polymers back into their monomer or chemical feedstocks. These feedstocks are purified and repolymerized into virgin-quality resins safe for food contact. Understanding pyrolysis, depolymerisation, and solvolysis reactions is essential for circular economy engineers.

2. Learning Objectives

  • Compare the primary chemical recycling pathways (pyrolysis, depolymerisation, solvolysis).
  • Explain the reaction kinetics and catalysts used in PET solvolysis (glycolysis, methanolysis).
  • Analyze pyrolysis products (naphtha, gas, char) as a function of temperature and residence time.
  • Solve mass balance and conversion calculations for a depolymerisation reactor.
  • Reference chemical recycling validation and certification standards.

3. Core Theory

3.1 Chemical Recycling Pathways

  • Thermal Pyrolysis: Heating mixed polyolefin waste (PE, PP) to 400600400 - 600^\circC in the absence of oxygen to break C–C bonds, producing liquid pyrolysis oil (crude naphtha analogue), hydrocarbon gases, and carbon char. The oil is co-fed into steam crackers.
  • Solvolysis: Using solvents and catalysts to cleave ester or amide bonds in condensation polymers (PET, Nylon, Polyurethane):
    • Glycolysis: Reacting PET with Ethylene Glycol (EG) to yield BHET monomer.
    • Methanolysis: Reacting PET with methanol to yield Dimethyl Terephthalate (DMT) and EG.
  • Depolymerisation: Thermally or catalytically unzipping polymers back to monomers (e.g., PMMA to MMA).

3.2 PET Glycolysis Reaction

The glycolysis of PET is a transesterification reaction catalyzed by metal acetates or ionic liquids:

PET+EG (excess)Catalyst, 180220CBHET (bis(2-hydroxyethyl) terephthalate)\text{PET} + \text{EG (excess)} \xrightarrow{\text{Catalyst, } 180 - 220^\circ\text{C}} \text{BHET } (\text{bis(2-hydroxyethyl) terephthalate})

The BHET monomer is purified and repolymerized to food-grade PET.

4. Worked Example

Problem: A chemical recycling plant depolymerises post-consumer PET flakes via glycolysis. The feed is 5.05.0 metric tonnes (MT) of PET flakes (monomer molecular weight equivalent MPET=192.2M_{PET} = 192.2 g/mol). The reactor uses excess Ethylene Glycol and a zinc acetate catalyst. The reaction yields 5.505.50 MT of purified BHET monomer (MBHET=254.2M_{BHET} = 254.2 g/mol). Calculate:

  1. The theoretical yield of BHET monomer (in MT) from 5.0 MT of PET.
  2. The chemical conversion yield (%) of the glycolysis reactor.

Solution:

  1. Calculate the theoretical yield of BHET monomer: One mole of PET repeating unit (192.2192.2 g/mol) reacts with one mole of EG to yield one mole of BHET (254.2254.2 g/mol):
Theoretical BHET=PET Feed Mass×MBHETMPET\text{Theoretical BHET} = \text{PET Feed Mass} \times \frac{M_{BHET}}{M_{PET}} Theoretical BHET=5.0 MT×254.2 g/mol192.2 g/mol=5.0×1.3226=6.613 MT of BHET\text{Theoretical BHET} = 5.0 \text{ MT} \times \frac{254.2 \text{ g/mol}}{192.2 \text{ g/mol}} = 5.0 \times 1.3226 = \textbf{6.613 MT of BHET}
  1. Calculate the chemical conversion yield (%):
Conversion Yield=Actual BHET YieldTheoretical BHET Yield×100%=5.50 MT6.613 MT×100%=83.17%\text{Conversion Yield} = \frac{\text{Actual BHET Yield}}{\text{Theoretical BHET Yield}} \times 100\% = \frac{5.50 \text{ MT}}{6.613 \text{ MT}} \times 100\% = \textbf{83.17\%}

Interpretation: The glycolysis reactor achieves an 83.17% chemical conversion yield, producing 5.50 MT of purified BHET monomer. The remaining fraction consists of unreacted oligomers and process losses, which are separated and recycled back to the reactor.

5. Indian Industry Context

Indian polyester manufacturers (such as Reliance Industries and recycling ventures) run chemical recycling setups. They depolymerise waste PET bottles and spinning waste back into DMT/TPA and EG, repolymerizing them into circular polyester yarns.

6. Key Takeaways & Glossary

  • Pyrolysis: Anaerobic thermal cracking of polyolefins into liquid fuels and feedstocks.
  • Glycolysis: Chemical recycling of PET using ethylene glycol to yield BHET monomer.
  • BHET: Bis(2-hydroxyethyl) terephthalate; the monomer intermediate produced by PET glycolysis.
  • Solvolysis: Solvent-assisted depolymerisation of condensation polymers.
  • ISCC PLUS: International certification verifying mass balance claims for chemically recycled polymers.

7. Standards Reference

  1. ISCC PLUS — International Sustainability and Carbon Certification guidelines for circular feedstocks
  2. ASTM D8058 — Standard test methods for evaluating chemical recycling pyrolysis oils

8. Practice Questions

  1. Write the balanced transesterification reaction of PET methanolysis, displaying the inputs, catalyst, and outputs.
  2. Contrast thermal pyrolysis with catalytic pyrolysis of mixed PE/PP waste. Focus on processing temperatures and product selectivity.
  3. Design a process separation schematic to purify BHET monomer from a glycolysis reactor, removing unreacted glycol, catalyst residues, and colorants.

9. Quiz

Q1. Which chemical recycling pathway involves the anaerobic thermal cracking of mixed polyolefin waste into liquid oil at 500°C?

  • B) Pyrolysis

Q2. The solvolysis of PET using Ethylene Glycol to yield BHET monomer is called:

  • C) Glycolysis

Q3. What is the theoretical yield of BHET monomer (MW = 254.2) from 10.0 tonnes of PET flakes (MW = 192.2)?

  • B) 13.22 tonnes

Q4. Which certification standard verifies the mass balance traceability of chemically recycled polymers?

  • B) ISCC PLUS

Q5. Condensation polymers like Nylon and Polyurethanes are recycled primarily through which process?

  • C) Solvolysis

Chemical Recycling: Pyrolysis, Depolymerisation & Solvolysis Pathways · Engineering Triad

Material Synthesis · Processing Hardware · Commercial Application

ASTM / ISO Aligned
1. MaterialResin / Chemistry

Standard Engineering Thermoplastic Resin

—[Monomer Backbone]ₙ— (Calibrated Molecular Weight & PDI)

Specific Gravity:1.05–1.42 g/cm³
Glass Transition (Tg):100–160 °C
Tensile Yield Strength:45–85 MPa
Melt Flow Index:5–25 g/10min
Morphology: Engineered Polymer Morphology (Amorphous / Semi-crystalline Matrix)
2. Machine & MouldShop Floor

Industrial Polymer Processing & Tooling System

Computer-Controlled Extrusion / Injection Moulding Hardware

Thermal Zones:180–280 °C (PID Controlled)
Injection / Melt Pressure:60–140 MPa
Cycle Time:15–45 seconds
Tooling Temperature:40–90 °C (Chiller Regulated)
Tooling: Hardened Tool Steel (H13/P20) Precision Cavity & Runner Layout
3. Real ProductApplication

Commercial Engineering Parts & Quality-Inspected Components

Automotive, Electrical, Medical & Packaging Applications

Standard:ASTM D3641 / ISO 294 / BIS Standard Compliance
Resin Grades: Reliance, SABIC, BASF, Covestro Standard Engineering Resins
Section 05 · Knowledge Check

Test Your Conceptual Understanding

In polymer science and processing thermodynamics, which factor most directly controls the critical transition temperature?

Select the correct option to verifyTake Complete Topic Assessment →
Summary Cheat Sheet & GATE Takeaways
  • Always evaluate molecular weight distribution (MWD) alongside zero-shear viscosity when calculating mold shear rates.
  • Differential Scanning Calorimetry (DSC) provides $T_g$, $T_c$, and $T_m$ to define optimal processing temperatures.
  • Comply with ASTM D638 / ISO 527 tensile specimen sizing to prevent premature necking artifacts.
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