Unsaturated Polyester Resin Synthesis from Waste Polycarbonate

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Solution Overview

Problem

Existing methods for producing unsaturated polyester resin from recycled materials are time-consuming and energy-intensive, requiring over 12 hours and high temperatures, which is inefficient and environmentally costly.

Innovation Solution

A method involving alcoholysis, etherification, and condensation steps to produce unsaturated polyester resin from polycarbonate, using lower temperatures and shorter reaction times, followed by dilution with styrene or acrylic monomers to achieve a high solid content, and a curing process at room temperature with a free radical initiator.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If recycled PET is reacted with propylene glycol, ethylene glycol, diethylene glycol, and a catalyst at 210°C for 6 hours, then unsaturated polyester resin can be produced, but the overall reaction time takes more than 12 hours and consumes huge amounts of electrical power

Engineering Contradiction:
Improvereaction timeVSAvoidelectrical power consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent segments the manufacturing process into three distinct steps: (1) alcoholysis of polycarbonate with diol at 130-190°C for 2-6 hours to produce diol-containing oligomer, (2) condensation with dianhydride/diacid monomers at 170-230°C for 2-6 hours, and (3) dilution with styrene/acrylic monomers. This segmentation allows optimization of each step's conditions and reduces total time and energy consumption compared to conventional single-step or two-step processes

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent changes key process parameters: using lower alcoholysis temperature (130-190°C vs conventional 210°C), using organic alkaline catalysts (DBU, TBD, triethylamine, pyridine) instead of traditional catalysts, and controlling specific temperature ranges for each step. These parameter changes reduce energy consumption while maintaining product quality

Inventive Principle:
Principle #35Parameter changes

2Reliability

If the reaction temperature is increased to 210°C for 6 hours to complete the reaction, then the unsaturated polyester resin can be produced, but the manufacturing time and energy consumption increase significantly

Engineering Contradiction:
Improvemechanical strength of resinVSAvoidmanufacturing time
Core Design Contradiction:
ReliabilityVSLoss of time

Solution Approach 1:

The patent performs preliminary alcoholysis of polycarbonate with diol to produce diol-containing oligomer before the condensation step. This preliminary action creates reactive intermediates that facilitate faster subsequent condensation reactions, reducing total manufacturing time while ensuring the final resin achieves required mechanical strength properties

Inventive Principle:
Principle #10Preliminary action

3Ease of manufacture

If conventional methods are used to produce unsaturated polyester resin from recycled materials, then the resin can be produced, but the process is time-consuming and energy-intensive

Engineering Contradiction:
Improveprocess efficiencyVSAvoidenergy consumption
Core Design Contradiction:
Ease of manufactureVSUse of energy by stationary object

Solution Approach 1:

The patent uses organic alkaline catalysts (DBU, TBD, triethylamine, pyridine) instead of conventional catalysts, controls temperature ranges (130-190°C for alcoholysis, 170-230°C for condensation), and optimizes reaction times (2-6 hours per step). These parameter changes improve process efficiency while reducing energy consumption compared to conventional high-temperature, long-duration processes

Inventive Principle:
Principle #35Parameter changes

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The method reduces manufacturing time and energy consumption while maintaining mechanical strength, enabling the production of unsaturated polyester resin with excellent properties and facilitating the reuse of waste polycarbonate, thereby reducing carbon emissions.

Implementation Method 1

In the alcoholysis step, a polycarbonate, a diol compound and an organic alkaline catalyst are mixed and heated to an alcoholysis temperature to obtain a first mixture

Methodology Applied
Scientific EffectAlcoholysis: Hydrolysis

Implementation Method 2

In the condensation step, the second mixture is cooled and a dianhydride monomer or a diacid monomer is added to the second mixture, and the second mixture and the dianhydride monomer or the diacid monomer are heated to a condensation temperature to obtain a third mixture

Methodology Applied
Scientific EffectCondensation reaction: Condensation

Implementation Method 3

The polymer can form a cross-linked network structure at the room temperature by being diluted with a monomer having free radicals and followed by the addition of a peroxide

Methodology Applied
Scientific EffectFree radical polymerization: Photopolymerisation

Data Source

PatentUS20250346700A1Method for manufacturing unsaturated polyester resin, unsaturated polyester resin and unsaturated polyester cured product
Publication Date: 2025.11.13 SWANCOR INNOVATION & INCUBATION CO LTD
  • US20250346700A1 patent drawing
  • US20250346700A1 patent drawing
  • US20250346700A1 patent drawing

AI summary

A method for manufacturing an unsaturated polyester resin includes alcoholysis step, etherification step, condensation step and dilution step as follows. In alcoholysis step, a polycarbonate, a diol compound and an organic alkaline catalyst are mixed and heated to an alcoholysis temperature to obtain a first mixture. In etherification step, a carbonate compound is added to the first mixture and the first mixture and the carbonate compound are maintained at an etherification temperature to obtain a second mixture. In condensation step, the second mixture is cooled and a dianhydride or diacid monomer is added, and the second mixture and the dianhydride or diacid monomer are heated to a condensation temperature to obtain a third mixture. In dilution step, the third mixture is cooled to a dilution temperature, and a styrene or acrylic monomer is added to dilute it to a predetermined solid content to obtain an unsaturated polyester resin.