Vinyl Aromatic Distillation Column Passivation
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Solution Overview
Problem
Distillation units for vinyl aromatic compounds, such as styrene, face fouling issues due to polymerization, leading to decreased efficiency and the need for frequent maintenance to remove polymer seeds.
Innovation Solution
A cleaning process involving mechanical cleaning followed by passivation, where a flux comprising a passivation mixture is passed through the distillation columns at elevated temperatures and pressures, using polymerization inhibitors and steam or hydrocarbons devoid of vinyl groups.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Reliability
If mechanical cleaning is performed to remove polymer seeds, then fouling is reduced, but polymer seeds remain as living chain residues that reactivate fouling
Solution Approach 1:
The cleaning process is followed by a passivation step that performs preliminary deactivation of polymer seeds before the distillation unit is restarted. This preliminary action ensures that harmful polymer seeds are neutralized in advance, preventing reactivation and fouling during subsequent operation.
Solution Approach 2:
The passivation mixture converts the harmful polymer seeds into inactive forms through chemical reaction. The polymerization inhibitors in the passivation mixture react with the living chain polymer residues, transforming them from harmful active seeds into benign inactive compounds, thereby eliminating the fouling problem.
2Reliability
If polymerization inhibitors are used during distillation to prevent polymerization, then polymerization is inhibited, but costs increase
Solution Approach 1:
Instead of continuously adding polymerization inhibitors during distillation, the process performs a preliminary passivation step during cleaning that deactivates polymer seeds. This preliminary action eliminates the need for continuous inhibitor addition, reducing costs while maintaining polymerization prevention.
Solution Approach 2:
The passivation step enables the distillation unit to self-protect against polymerization by deactivating polymer seeds during cleaning. This self-service mechanism eliminates the need for continuous external intervention with polymerization inhibitors, reducing operational costs.
3Ease of manufacture
If high-pressure cleaning is used to remove dirt from heat exchangers, then cleaning effectiveness is improved, but jet water cannot reach every nook and cranny
Solution Approach 1:
The patent replaces mechanical high-pressure jet cleaning with a thermal-chemical passivation process. The passivation mixture, heated to elevated temperatures, chemically deactivates polymer seeds and penetrates into nooks and crannies where mechanical jets cannot reach, achieving complete cleaning effectiveness.
Solution Approach 2:
The passivation process changes the temperature parameter by heating the cleaning medium to elevated temperatures (typically 50-100°C). This temperature increase enhances the penetration ability of the cleaning solution into difficult-to-reach areas and accelerates the chemical deactivation of polymer seeds, overcoming the limitations of mechanical high-pressure cleaning.
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 process effectively deactivates polymer seeds, reducing the need for polymer inhibitors during distillation, and restores the original efficiency of the distillation unit.
Implementation Method 1
a flux comprising a passivation mixture is passed through at least one distillation column under passivation conditions comprising a temperature of at least 90° C.
Implementation Method 2
a flux comprising a passivation mixture is passed through at least one distillation column
Data Source
AI summary
The disclosure relates to a cleaning process of a vinyl aromatic compounds distillation unit wherein the vinyl aromatic compounds distillation unit comprises one or more distillation columns, the process comprises a step of cleaning one or more distillation columns followed by a step of passivation of at least one distillation column wherein a flux comprising a passivation mixture is passed through at least one distillation column under passivation conditions comprising a temperature of at least 90° C., wherein the passivation mixture comprises a component A being one or more polymerisation inhibitors; and a component B selected from steam and/or one or more hydrocarbons devoid of vinyl group. The disclosure also relates to the process of purification and of production of one or more vinyl aromatic compounds that include the said cleaning process.

