Ubicación: Global + English
Global Global Algérie Français Algeria English Angola Português Angola English Argentina Español Argentina English Australia English Austria Deutsch Austria English Azerbaijan English Azerbaijan Русский Bahrain English Bangladesh English Belgium English Belgium Français Belgium Nederlands Brazil Português Brazil English Bulgaria български Bulgaria English Cameroon English Cameroon Français Canada English Canada Français Chile Español Chile English China 中文 China 日本語 China English Colombia Español Colombia English Croatia English Czech Republic Čeština Czech Republic English Denmark English Djibouti English Ecuador Español Ecuador English Egypt English Estonia English Ethiopia English Finland Suomi Finland English France Français France English Georgia English Georgia Русский Germany Deutsch Germany English Ghana English Greece Ελληνικά Greece English Guatemala Español Guatemala English Hong Kong, China English Hong Kong, China 中文 Hungary Magyar Hungary English India English Indonesia English Iraq English Ireland English Italy Italiano Italy English Ivory Coast Français Ivory Coast English Japan 日本語 Japan English Jordan English Kazakhstan Русский Kazakhstan English Kenya English Kuwait English Kyrgyzstan Русский Kyrgyzstan English Latvia English Lithuania English Malaysia English Mauritius English Mauritius français (Maurice) Mexico Español Mexico English Moldova Română Moldova English Mongolia English Morocco English Morocco Français Mozambique Português Mozambique English Netherlands Nederlands Netherlands English New Zealand English Nigeria English Norway English Oman English Pakistan English Paraguay Español Paraguay English Peru Español Peru English Philippines English Poland Polski Poland English Portugal Português Portugal English Qatar English Republic of Korea 한국어 Republic of Korea English Romania Română Romania English Saudi Arabia English Serbia Српски Serbia English Singapore English Slovakia English Slovenia English South Africa English Spain English Spain Español Sri Lanka English Sweden English Switzerland Deutsch Switzerland Français Switzerland Italiano Switzerland English Tanzania English Thailand ไทย Thailand English Togo English Togo Français Tunisia English Tunisia Français Türkiye Türkçe Türkiye English Turkmenistan Русский Turkmenistan English Ukraine Українська Ukraine English United Arab Emirates English United Kingdom English Uruguay Español Uruguay English USA English Uzbekistan English Uzbekistan Русский Vietnam Tiếng Việt Vietnam English

PET flake alcoholysis, most commonly performed as glycolysis with ethylene glycol, is a proven chemical recycling route that depolymerizes waste PET bottle flakes back into monomers such as BHET. Laboratory-scale alcoholysis experiments evaluate conversion efficiency, monomer yield, purity, and processability of recycled material. This article outlines the sample types, testing items, experimental methods, analytical characterization, and industrial applications of PET flake alcoholysis testing.

PET Flake Alcoholysis Experiment: Process, Testing Items, and Applications

Technical Overview

Polyethylene terephthalate (PET) is the dominant material for beverage bottles, and large volumes of post-consumer PET flakes are generated worldwide each year. Alcoholysis is a chemical recycling technique in which an alcohol reagent cleaves the ester bonds of the PET chain through transesterification. In practice, the most widely studied form is glycolysis, which uses ethylene glycol (EG) to depolymerize PET into bis(2-hydroxyethyl) terephthalate (BHET), a monomer that can be directly reintroduced into polycondensation reactors.

A typical laboratory alcoholysis experiment is conducted at 180–200°C under a nitrogen atmosphere, with excess ethylene glycol and a transesterification catalyst such as zinc acetate. Within one to four hours, the solid flakes dissolve and convert into a mixture of BHET monomer and short oligomers. The experiment allows recyclers, resin producers, and research institutions to quantify the chemical recyclability of a specific flake stream before committing to scale-up.

  • Reaction type: solvolysis via transesterification of ester linkages
  • Primary reagent: ethylene glycol (methanol and higher alcohols are studied as variants)
  • Primary product: BHET monomer, together with MHET and cyclic or linear oligomers
  • Typical operating window: 180–240°C, 1–8 hours, catalyst loading of 0.1–1.0 wt%
  • Key performance metrics: PET conversion, BHET yield, monomer purity, and product color

Testing Samples

Hot-Washed Clear PET Flakes

Super-clear, hot-washed flakes from water and carbonated drink bottles represent the highest-quality feedstock. They generally contain minimal PVC, glue, or label contamination and deliver the highest BHET yield and best color performance in alcoholysis experiments.

Colored and Mixed Flakes

Green, blue, and mixed-color flake streams are tested to assess how dyes and pigments affect depolymerization kinetics and product color. Insoluble pigment residues are typically removed during hot filtration of the glycolysate.

Post-Industrial PET Scrap

Preforms, sheet trim, film edge trim, and fiber waste from manufacturing lines are evaluated to confirm suitability for closed-loop monomer recycling. These streams often depolymerize rapidly due to their low contamination level and known history.

Low-Grade or Contaminated Flakes

Cold-washed bale flakes, multi-layer materials, and heavily contaminated streams are tested to determine whether chemical recycling can upgrade material that would otherwise be downcycled or landfilled. The experiment quantifies insoluble residue, ash, and impurity carryover into the monomer.

Testing Items

The alcoholysis experiment evaluates both the depolymerization process and the quality of the resulting products. Core testing items include:

  • PET conversion rate, determined from the mass of undissolved solid residue after reaction
  • BHET yield and oligomer distribution, quantified by HPLC or quantitative NMR
  • BHET purity and melting point (reference value approximately 110°C) verified by DSC
  • Chemical structure confirmation by FTIR and proton NMR spectroscopy
  • Molecular weight analysis of residual oligomers by gel permeation chromatography (GPC)
  • Residual ethylene glycol content and catalyst residue in the isolated monomer
  • Color values (Hunter L, a, b) of the monomer and repolymerized resin
  • Intrinsic viscosity of repolymerized PET, tested per ASTM D4603 or ISO 1628-5
  • Ash content, moisture, and acid or hydroxyl number of the glycolysis products
  • Effect of process variables: temperature, EG-to-PET ratio, catalyst type and loading, and reaction time

Testing Methods

Reaction Procedure

Dried PET flakes are charged into a glass or stainless-steel reactor together with a weighed excess of ethylene glycol, typically at EG-to-PET mass ratios between 3:1 and 6:1. Zinc acetate dihydrate or an equivalent catalyst is added at 0.1–1.0 wt% based on PET. The reactor is purged with nitrogen, heated to the target temperature with mechanical stirring, and held for the planned residence time. Samples may be withdrawn at intervals to build a conversion-versus-time profile for kinetic analysis.

Product Isolation

After the reaction, the hot glycolysate is filtered to remove insoluble impurities such as pigments, catalyst residues, and non-PET solids. Excess ethylene glycol is recovered by distillation under reduced pressure. The crude product is dissolved in hot deionized water or left to crystallize on cooling, and BHET is separated by filtration and dried to constant weight. The isolated solid and the mother liquor are both retained for mass-balance calculation.

Analytical Characterization

The isolated BHET and oligomer fractions are characterized using a standard analytical package:

  • HPLC separation to quantify BHET, MHET, and higher oligomers
  • Proton NMR in DMSO-d6 to confirm monomer structure and estimate purity
  • FTIR to verify ester carbonyl and terminal hydroxyl functionality
  • DSC to determine melting point, melting enthalpy, and thermal purity indicators
  • GPC to measure molecular weight distribution of any oligomeric fraction
  • Karl Fischer titration or loss-on-drying for moisture content
  • Colorimetry to record L, a, and b values of the monomer product

Where the objective is closed-loop recycling, the recovered monomer is repolymerized in a bench-scale polycondensation, and the resulting PET is tested for intrinsic viscosity, color, and thermal properties to benchmark it against virgin resin.

Applications

Data from PET flake alcoholysis experiments supports a wide range of industrial applications:

  • Closed-loop chemical recycling: repolymerizing recovered BHET into food-contact-grade rPET with virgin-equivalent quality
  • Fiber and packaging resin production: supplementing mechanical recycling with monomer feedstock for bottle-to-bottle systems
  • Polyurethane polyols: using partially depolymerized PET oligomers as aromatic polyester polyols for rigid foams
  • Unsaturated polyester resins: converting glycolyzed PET into resin intermediates for composites and coatings
  • Plasticizer synthesis: producing terephthalate-based plasticizers such as DOTP from glycolysis-derived intermediates
  • Process optimization and due diligence: screening feedstock suppliers, validating catalyst systems, and de-risking commercial plant design

FAQ

What is the difference between alcoholysis, glycolysis, hydrolysis, and methanolysis of PET?

All four are solvolysis routes that break the PET ester bonds. Alcoholysis with ethylene glycol is called glycolysis and yields BHET; methanolysis yields dimethyl terephthalate; hydrolysis yields terephthalic acid and ethylene glycol. Glycolysis is favored at laboratory and commercial scale because it operates at moderate temperatures near atmospheric pressure and produces a monomer compatible with existing PET lines.

What temperature and catalyst are typically used?

Most experiments run at 180–240°C with zinc acetate as the benchmark catalyst at 0.1–1.0 wt%. Manganese, cobalt, and sodium salts as well as titanium-based catalysts are also studied. A nitrogen blanket is recommended to limit oxidative yellowing.

What conversion and BHET yield can be expected?

With clean feedstock and optimized conditions, PET conversion above 95% and isolated BHET yields of roughly 70–90% are commonly reported in laboratory studies, with the balance retained as soluble oligomers that can be recycled back into the process.

Can colored or contaminated flakes be used?

Yes. One advantage of chemical recycling is that pigments, glue residues, and many impurities remain insoluble and are removed by hot filtration. However, PVC and moisture accelerate degradation and must be tightly controlled, which is why feedstock screening experiments are performed.

How is the success of an alcoholysis experiment judged?

Success is judged by the combination of PET conversion, BHET yield and purity, mass balance closure, product color, and, where relevant, the intrinsic viscosity and optical properties of PET repolymerized from the recovered monomer.

Is glycolysis-derived rPET suitable for food contact?

When the process includes adequate purification and is operated under a recognized recycling scheme with contaminant challenge testing, monomer-to-resin routes can achieve food-contact compliance. Regulatory validation is performed separately from the laboratory conversion experiment.