Acetic Acid Recovery via Extractive Distillation
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Solution Overview
Problem
Conventional distillation systems for recovering acetic acid from aqueous solutions in terephthalic acid production are energy-intensive and inefficient, leading to high operating costs and environmental concerns due to acetic acid losses and wastewater treatment burdens.
Innovation Solution
An integrated extraction and distillation apparatus comprising a liquid-liquid extraction column and an azeotropic distillation column, with a guard bed to manage alcohol buildup and separate water-poor and water-rich streams for optimized energy use, using selective esters as extraction solvents to reduce acetic acid concentration and improve separation efficiency.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Quantity of substance
If conventional distillation is used to separate acetic acid from water, then acetic acid can be recovered, but high energy consumption and high operating costs occur due to close-boiling characteristics requiring high number of theoretical stages and high reflux ratio
Solution Approach 1:
The patent introduces an extractive agent (entrainer) as an intermediary substance that forms an azeotrope with water. This mediator changes the relative volatility between acetic acid and water, enabling separation at lower energy consumption. The entrainer selectively interacts with water to form a low-boiling azeotrope that can be easily separated from acetic acid, thus resolving the close-boiling problem without requiring high reflux ratios or numerous theoretical stages.
Solution Approach 2:
The patent changes the physical-chemical parameters of the separation system by introducing a third component (entrainer) that modifies the vapor-liquid equilibrium relationships. This parameter change transforms the difficult separation of close-boiling acetic acid-water into an easier separation involving an azeotropic mixture, thereby reducing the number of theoretical stages and reflux ratio requirements while maintaining effective acetic acid recovery.
2Quantity of substance
If conventional distillation is used to separate acetic acid from water, then acetic acid can be recovered, but large size equipment and high investment cost are required
Solution Approach 1:
By introducing an extractive agent as a mediator, the patent enables more efficient mass transfer and separation. The entrainer's selective interaction with water creates a more favorable separation scenario, allowing the use of fewer and smaller distillation columns while achieving the same recovery efficiency. This reduces both the number of theoretical stages required and the physical size of equipment needed.
Solution Approach 2:
The introduction of the entrainer changes the separation parameters, improving relative volatility and enabling more compact equipment design. The modified vapor-liquid equilibrium allows for smaller column diameters, fewer trays, and reduced overall equipment footprint while maintaining the required separation performance and acetic acid recovery rates.
3Quantity of substance
If conventional distillation is used to separate acetic acid from water, then acetic acid can be recovered, but high operating costs occur due to high steam consumption
Solution Approach 1:
The extractive agent acts as a mediator that facilitates separation at lower energy input. By forming an azeotrope with water, the entrainer enables the distillation process to proceed at lower reflux ratios and with fewer theoretical stages, directly reducing steam consumption. The mediator's presence creates a more energy-efficient separation pathway that maintains effective acetic acid recovery while minimizing thermal energy requirements.
Solution Approach 2:
The patent changes the thermodynamic parameters of the system by introducing the entrainer, which modifies the energy requirements of the distillation process. This parameter change reduces the heat duty required per unit of acetic acid recovered, lowering steam consumption and associated operating costs while maintaining the necessary separation efficiency and recovery rates.
4Quantity of substance
If conventional distillation is used to separate acetic acid from water, then acetic acid can be recovered, but environmental problems occur due to acetic acid losses and wastewater treatment burdens
Solution Approach 1:
The entrainer serves as a mediator that improves separation efficiency, enabling more complete acetic acid recovery and reducing losses to the effluent stream. By achieving lower acetic acid concentrations in the overhead water stream through the azeotropic mechanism, the system reduces the burden on downstream wastewater treatment facilities and minimizes environmental discharge of acetic acid, thus resolving the harmful effects associated with conventional distillation.
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 apparatus significantly reduces energy consumption and waste production, enhancing the separation efficiency of acetic acid while maintaining compatibility with existing terephthalic acid manufacturing systems, thereby lowering capital and operational costs and environmental impact.
Implementation Method 1
The extraction column is a liquid-liquid contacting device and is located upstream from and in fluid communication with the azeotropic distillation column
Implementation Method 2
an azeotropic distillation column for dehydration of the extractant
Implementation Method 3
The entrainer forms a low boiling azeotrope with water and therefore improves the relative volatility for the separation between the acetic acid containing stream and the alkyl-acetate/water azeotrope
Implementation Method 4
the new apparatus further comprises a pre-concentrator for providing more concentrated aqueous acetic solutions to both the liquid-liquid extractor and the azeotropic distillation column
Data Source
AI summary
The invention disclosed relates to an apparatus and method for recovering acetic acid from an aqueous feed stream containing acetic acid, in particular a stream generated during terephthalic acid production. The apparatus includes: a liquid-liquid extraction column to which water-rich feed streams are fed, having a guard bed situated near the top and within the extraction column for conversion by reaction with acetic acid of alcohol within the mixture to the corresponding ester; and an azeotropic distillation column to remove residual water from acetic acid, to which water-poor feed streams are fed directly at a height of the azeotropic distillation column at which the mixture therein has a similar water concentration. The liquid-liquid extraction column produces an extract comprising an extraction solvent and acetic acid which is sent to the azeotropic distillation column to separate residual water and acetic acid.


