Segmented Esterification Reactor for PBT Manufacturing

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Solution Overview

Problem

Conventional methods for manufacturing polybutylene terephthalate result in high catalyst usage, leading to issues such as yellowing, color defects, and reduced filterability due to catalyst-related problems like hydrolysis and residue formation.

Innovation Solution

A modified esterification method with a stirred first zone followed by a non-stirred follow-up zone, optimizing the molar ratio of butanediol to terephthalic acid and using a reduced amount of titanium-based catalyst, which reduces catalyst demand and minimizes back-mixing, allowing for higher TPA turnover and improved polymer quality.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If conventional stirred tank reactors are used for esterification, then mixing and reaction efficiency are maintained, but catalyst usage increases leading to yellowing and color defects

Engineering Contradiction:
Improvereaction efficiencyVSAvoidyellowing and color defects
Core Design Contradiction:
Ease of manufactureVSObject-affected harmful factors

Solution Approach 1:

The esterification reactor is divided into two distinct zones: a first stirred zone for initial mixing and reaction, and a second non-stirred zone for completion of esterification. This segmentation allows the reaction to proceed efficiently while minimizing catalyst contact time and back-mixing, thereby reducing catalyst-related color defects and yellowing in the final product.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different regions of the reactor are assigned different functional qualities: the first zone provides mechanical stirring for reaction initiation, while the second zone eliminates stirring to reduce back-mixing. This local differentiation optimizes both reaction efficiency and product quality by controlling catalyst exposure in specific reactor regions.

Inventive Principle:
Principle #3Local quality

2Productivity

If high catalyst amounts are used to achieve high TPA turnover, then reaction speed increases, but filterability decreases due to residue formation

Engineering Contradiction:
ImproveTPA turnoverVSAvoidresidue formation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

By segmenting the reactor into stirred and non-stirred zones, the process achieves high TPA turnover in the first zone while the second zone allows clean reaction completion with minimal catalyst residue formation, thereby maintaining both productivity and filterability.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The non-stirred second zone allows the reaction to rush through to completion without the disruptive effect of continuous stirring, minimizing the time catalyst residues can form and thereby improving filterability while maintaining high productivity.

Inventive Principle:
Principle #21Skipping (Rushing through)

3Stability of the object's composition

If continuous stirring is applied throughout esterification, then reaction homogeneity is maintained, but back-mixing occurs reducing process efficiency

Engineering Contradiction:
Improvereaction homogeneityVSAvoidprocess efficiency
Core Design Contradiction:
Stability of the object's compositionVSProductivity

Solution Approach 1:

The reactor is segmented into a stirred zone for achieving reaction homogeneity and a non-stirred zone for preventing back-mixing. This allows the system to maintain composition stability where needed while maximizing overall process efficiency by eliminating counterproductive mixing in the second zone.

Inventive Principle:
Principle #1Segmentation

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 significantly reduces catalyst usage, enhancing product quality by minimizing color defects and increasing filter life, while achieving high TPA turnover and stable flow rates, thus improving the overall manufacturing process.

Implementation Method 1

the esterification of terephtalic acid with butanediol... TPA is esterified with BD and hydroxybutyl groups formed

Methodology Applied
Scientific EffectEsterification: Chemical Bonding

Implementation Method 2

the esterification product is subsequently subjected to a first polycondensation... a further polycondensation to the final medium to high viscous product

Methodology Applied
Scientific EffectPolycondensation: Chemical Bonding

Implementation Method 3

catalysts are employed, in particular catalysts based on organic titanium compounds

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS8143367B2Method for the esterification of terephtalic acid with butanediol, method for the manufacture of polybutylene terephtalate and a device therefor
Publication Date: 2012.03.27 LURGI ZIMMER GMBH
  • US8143367B2 patent drawing
  • US8143367B2 patent drawing
  • US8143367B2 patent drawing

AI summary

The present invention relates to an improved method for the esterification of terephthalic acid with 1,4-butanediol, an improved method for the manufacture of polybutylene terephthalate as well as reactors and devices that are suited for the application in this method.