Polyester Granulate Acetaldehyde Reduction Underwater

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Solution Overview

Problem

Current methods for producing polyester granulates with low acetaldehyde content are energy-intensive, require expensive nitrogen gas, and involve complex equipment and multiple processing stages, which are inefficient and costly, while also facing challenges in maintaining high viscosity and crystallinity for packaging applications.

Innovation Solution

A method involving underwater granulation of high-viscosity polyester melts, followed by centrifugal separation and treatment with rinsing air at controlled temperatures to reduce acetaldehyde content without the need for additional crystallization stages, using a device comprising an underwater granulator, centrifuge, and dealdehydisation container to produce granulates with low acetaldehyde levels and improved processing characteristics.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Object-generated harmful factors

If solid state polycondensation is used to increase intrinsic viscosity and reduce acetaldehyde content, then the acetaldehyde content is lowered and viscosity is increased, but the process requires expensive nitrogen gas, complex equipment, and multiple processing stages

Engineering Contradiction:
Improveacetaldehyde contentVSAvoidprocessing stages
Core Design Contradiction:
Object-generated harmful factorsVSDevice complexity

Solution Approach 1:

The patent combines underwater granulation, centrifugal separation, and dealdehydisation into a single integrated device. The granulator includes both the granulation chamber and centrifugal separation mechanism, eliminating the need for separate crystallization equipment and reducing overall process complexity while achieving the same acetaldehyde reduction and viscosity enhancement effects

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent extracts and eliminates the need for expensive nitrogen gas by using air as the processing medium. The dealdehydisation process operates in atmospheric conditions where acetaldehyde is removed through evaporation and air flow, replacing the nitrogen atmosphere required by conventional solid state polycondensation methods

Inventive Principle:
Principle #2Taking out (Extraction)

2Strength

If solid state polycondensation is used to achieve high intrinsic viscosity, then the required strength is reached, but energy consumption increases and processing time is extended

Engineering Contradiction:
Improvepolyester strengthVSAvoidenergy consumption
Core Design Contradiction:
StrengthVSUse of energy by moving object

Solution Approach 1:

The patent changes the processing parameters by conducting dealdehydisation at atmospheric pressure and moderate temperatures (50-150°C) rather than the high temperatures and pressures required by solid state polycondensation. The centrifugal force parameter is introduced to achieve rapid separation, reducing the time and energy required for processing while maintaining the necessary polymer strength through controlled acetaldehyde removal

Inventive Principle:
Principle #35Parameter changes

3Productivity

If conventional granulation methods are used, then granulates are produced, but acetaldehyde content remains high and additional treatment stages are required

Engineering Contradiction:
Improvegranulate productionVSAvoidacetaldehyde content
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent merges granulation and dealdehydisation into a single simultaneous process. As granulates are formed underwater and separated centrifugally, hot air flows through the granulate bed to evaporate and remove acetaldehyde in real-time, eliminating the need for subsequent separate dealdehydisation treatment stages and maintaining high productivity

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent establishes continuous acetaldehyde removal throughout the granulation process. Hot air continuously circulates through the granulate bed during formation and separation, maintaining constant low acetaldehyde levels without interruption or additional processing steps, thereby sustaining both high productivity and low harmful content

Inventive Principle:
Principle #20Continuity of useful action

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

This method simplifies the process, reduces energy consumption, and maintains high-quality polyester granulates with low acetaldehyde content, allowing for efficient production of granulates suitable for food packaging with minimal acetaldehyde reformation and improved crystallinity, enabling processing at lower temperatures with reduced equipment complexity.

Implementation Method 1

a) the polyester melt strand is broken up under water at the highest possible temperature

Methodology Applied
Scientific EffectUnderwater granulation:

Implementation Method 2

b) the accompanying water is separated, preferably by spinning, from the granulate with the least possible cooling of the granulate

Methodology Applied
Scientific EffectCentrifugal separation: Centrifugal Separation

Implementation Method 3

d) the granulate in the dealdehydisation container is treated using a flow of rinsing air with an intake temperature between 180° C. and 210° C.

Methodology Applied
Scientific EffectEvaporation: Evaporation

Data Source

PatentUS7521522B2Method and device to reduce the acetaldehyde content of polyester granulate
Publication Date: 2009.04.21 LURGI ZIMMER GMBH
  • US7521522B2 patent drawing
  • US7521522B2 patent drawing
  • US7521522B2 patent drawing

AI summary

The invention relates to a method for producing a granulate with a low acetaldehyde content and improved processing properties from a high-viscosity polyester melt, wherein the polyester melt strand is fragmented under water at the highest possible temperature, the accompanying water is separated from the granulate with the least possible cooling of the granulate, the low-water granulate obtained in this way is passed after removal of the water directly into a dealdehydisation container and the granulate in the dealdehydisation container is treated with a flow of rinsing air, plus a device for carrying out this method.