Ethylene Glycol Purification via Hot Water Extraction
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Solution Overview
Problem
Current methods for purifying by-product ethylene glycol from the polyester conversion process struggle with low purity due to the azeotropic nature of ethylene glycol and 2-ethylhexanol, making it difficult to separate and reuse the ethylene glycol as a raw material for other products.
Innovation Solution
A continuous method involving inputting a reaction liquid waste stream into an ethylene glycol dehydration tower with a hot water stream to separate ethylene glycol from 2-ethylhexanol, followed by dehydration and subsequent distillation to achieve high purity ethylene glycol, utilizing a reboiler loop with high pressure steam for heat and controlled temperature and pressure conditions.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Loss of energy
If conventional evaporation method is used to remove water from reaction liquid waste stream, then water removal is achieved, but ethylene glycol purity remains low due to azeotropic mixture with 2-ethylhexanol
Solution Approach 1:
The purification process is divided into multiple sequential stages: first evaporation to remove bulk water, then extraction to separate 2-ethylhexanol, followed by distillation to achieve high purity ethylene glycol. This segmentation allows each stage to optimize for its specific function rather than attempting single-step purification.
Solution Approach 2:
An extractant (organic solvent) is introduced as an intermediary substance to facilitate the separation of 2-ethylhexanol from ethylene glycol. The extractant selectively dissolves 2-ethylhexanol, forming a separate phase that can be easily removed, thereby breaking the azeotropic relationship.
2Productivity
If simple distillation is used to separate ethylene glycol from 2-ethylhexanol, then separation is attempted, but low purity is achieved due to azeotropic nature
Solution Approach 1:
An extractant is used as a mediator to selectively interact with 2-ethylhexanol, forming an extractable complex that separates from the ethylene glycol phase. This intermediary substance enables effective separation despite the azeotropic relationship that would otherwise prevent clean distillation.
Solution Approach 2:
The process utilizes changes in physical parameters (solubility, density, boiling point) by introducing the extractant to alter the phase behavior of the mixture. The extractant changes the distribution coefficients of the components, enabling separation that simple distillation cannot achieve.
3Manufacturing precision
If multi-step purification process is implemented to achieve high purity ethylene glycol, then purity reaches 90% or higher, but process complexity increases
Solution Approach 1:
The complex purification requirement is broken down into three manageable unit operations: evaporation (water removal), extraction (2-ethylhexanol removal), and distillation (final purification). Each unit operation is relatively simple and can be implemented with standard equipment, making the overall complex process manageable.
Solution Approach 2:
The extraction step serves multiple functions simultaneously: it removes 2-ethylhexanol from the mixture, concentrates ethylene glycol in the raffinate phase, and prepares the mixture for efficient distillation. This multi-functionality reduces the need for additional separate processing steps.
4Ease of manufacture
If conventional purification methods are used, then processing is simple, but the recovered ethylene glycol cannot be used as raw material for synthetic polyester due to low purity
Solution Approach 1:
The purification process is segmented into stages that progressively remove different impurities (water first, then 2-ethylhexanol, then other contaminants). This ensures the final ethylene glycol product meets the stringent purity requirements for use as raw material in synthetic polyester production while keeping each processing step relatively simple.
Solution Approach 2:
The process is designed as a continuous flow system where the ethylene glycol moves through evaporation, extraction, and distillation stages without interruption. This continuous processing maintains high purity throughout and ensures the final product consistently meets specifications for reuse as raw material.
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 achieves ethylene glycol purity of not less than 90%, enhancing its application value and allowing for direct treatment of waste streams through wastewater treatment or incineration without environmental pollution.
Implementation Method 1
inputting a hot water stream into the ethylene glycol dehydration tower to mix with the reaction liquid waste stream and to remove the 2-ethylhexanol from the reaction liquid waste stream so that the ethylene glycol is separated from the 2-ethylhexanol
Implementation Method 2
utilizing a reboiler loop with high pressure steam for heat
Implementation Method 3
The reboiler loop is configured to heat the reaction liquid in the ethylene glycol dehydration tower
Implementation Method 4
inputting the crude ethylene glycol stream into an ethylene glycol distillation tower to collect an ethylene glycol solution from a tower top of the ethylene glycol distillation tower
Data Source
AI summary
A method for purifying by-product ethylene glycol of polyester in converting plasticizer includes: inputting a reaction liquid waste stream including ethylene glycol and 2-ethylhexanol into an ethylene glycol dehydration tower; inputting a hot water stream into the ethylene glycol dehydration tower to mix with the reaction liquid waste stream and to remove the 2-ethylhexanol from the reaction liquid waste stream; dehydrating the ethylene glycol via the ethylene glycol dehydration tower to collect a crude ethylene glycol stream including dehydrated ethylene glycol from a tower bottom of the ethylene glycol dehydration tower and to collect an organic liquid waste stream including the 2-ethylhexanol from a tower top of the ethylene glycol dehydration tower; and inputting the crude ethylene glycol stream into an ethylene glycol distillation tower to collect a ethylene glycol solution from a tower top of the ethylene glycol distillation tower.

