Polymer Crystallizer Pressure Control for Moisture Protection

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Solution Overview

Problem

Existing processes for direct crystallization of polymers under inert gas face challenges such as unsatisfactory crystallization control, homogeneity, and oxidative degradation, leading to issues like agglomeration and moisture contamination, which affect the quality and efficiency of the polymer production process.

Innovation Solution

A process and apparatus where the pressure in the crystallizer is set higher than in the pellet dryer, allowing for direct transfer of hot polymer pellets under an inert gas atmosphere, preventing cooling medium ingress and maintaining a controlled environment for crystallization, thereby enhancing crystallization control and reducing oxidative degradation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If the pellet dryer is operated as a closed system to prevent moisture ingress, then moisture protection is improved, but overpressure develops forcing water into the crystallizer and SSP reactor causing moisture contamination

Engineering Contradiction:
Improvemoisture protectionVSAvoidmoisture contamination
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

A pressure equalization line with a non-return valve is introduced as an intermediary mechanism between the pellet dryer and crystallizer. This mediator allows pressure equalization to prevent water forced by overpressure from entering the crystallizer, while maintaining the closed system's moisture protection function.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The pressure control system is segmented into multiple pathways: a main pressure relief line and a separate pressure equalization line with non-return valve. This segmentation allows selective pressure management - relieving excess pressure while preventing backflow of moisture into the crystallizer.

Inventive Principle:
Principle #1Segmentation

2Manufacturing precision

If additional heating with hot process gas is applied to crystallize the hot pellets, then crystallization quality is improved, but energy consumption increases

Engineering Contradiction:
Improvecrystallization qualityVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The pellets' own thermal energy is utilized for crystallization by controlling the cooling process and using the pellets' residual heat, combined with the exothermic crystallization reaction. This self-service approach reduces or eliminates the need for additional heating energy input while achieving the required crystallization quality.

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The crystallization process leverages the phase transition from amorphous to crystalline state, which is exothermic. By controlling the cooling rate and holding temperature, the released crystallization heat is utilized to maintain the necessary temperature for complete crystallization, reducing external energy requirements.

Inventive Principle:
Principle #36Phase transitions

3Manufacturing precision

If the pellets are cooled down after pelletization and then reheated for crystallization, then crystallization control is improved, but process time and energy consumption increase

Engineering Contradiction:
Improvecrystallization controlVSAvoidprocess time
Core Design Contradiction:
Manufacturing precisionVSLoss of time

Solution Approach 1:

The process maintains continuous heating from pelletization through crystallization without cooling down in between. The pellet dryer continuously heats the pellets during drying, and this thermal state is maintained during transfer to the crystallizer, enabling continuous useful action and eliminating the time-consuming cool-down and reheat cycles.

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

The pellets are preheated during the pelletization and drying process itself, so that when they enter the crystallizer, they are already at the appropriate temperature for crystallization. This preliminary heating action eliminates the need for subsequent reheating and reduces total process time.

Inventive Principle:
Principle #10Preliminary 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 approach ensures flexible and homogeneous temperature and crystallinity control, minimizing agglomeration and moisture issues, resulting in higher-quality polymer pellets with reduced energy consumption and operational costs.

Implementation Method 1

the pressure in the crystallizer is set higher than in the pellet dryer, allowing for direct transfer of hot polymer pellets under an inert gas atmosphere, preventing cooling medium ingress

Methodology Applied
Scientific EffectPressure gradient: Pressure Gradient

Implementation Method 2

crystallization is not always possible under an air atmosphere, since oxidative degradation can occur at the high temperatures of crystallization. With certain materials/quality requirements, therefore, it is necessary to crystallize under an inert gas atmosphere.

Methodology Applied
Scientific EffectOxidation prevention: Oxidation

Implementation Method 3

DE 103 49 016 and DE 10 2004 015 515, for example, describe so-called latent heat crystallization processes wherein crystallization is effected using solely the intrinsic heat of the pellets.

Methodology Applied
Scientific EffectLatent heat: Latent Heat

Data Source

PatentUS9943817B2Process and apparatus for direct crystallization of polymers under inert gas
Publication Date: 2018.04.17 POLYMETRIX AG
  • US9943817B2 patent drawing
  • US9943817B2 patent drawing

AI summary

An apparatus for continuous pelletization and crystallization of a polymer includes a unit for forming a polymer pellet material and cooling the pellet material in a liquid cooling medium. An after-connected drying unit has an exit opening for exporting gas and a crystallizer for crystallizing the pellet material. The crystallizer communicates via a connection line with the pre-connected unit for separating the liquid cooling medium from the pellet material and drying the pellet material. The crystallizer communicates with an inert gas tank, whereby the pressure in the crystallizer can be increased relative to the pressure in the drying unit. A related process is also disclosed.