Trioxane Production via Liquid-Liquid Extraction and Solvent Recovery

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Solution Overview

Problem

Conventional methods for producing trioxane result in high energy consumption due to the need for large amounts of energy to separate trioxane from mixtures with formaldehyde and water, and inefficient extraction processes lead to significant energy losses and low trioxane yield.

Innovation Solution

A method involving the distillation of a formaldehyde aqueous solution in the presence of an acid catalyst, followed by liquefaction of the gas mixture and subsequent separation using two liquid/liquid extractors connected in series, allowing for energy recovery and reduced trioxane discharge into the aqueous phase, with the option to reuse solvents based on boiling points.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If distillation evaporation is used to separate trioxane from the mixture, then trioxane can be obtained, but a large amount of water is inevitably contained due to vapor-liquid equilibrium, and energy consumption is increased due to evaporation heat loss

Engineering Contradiction:
Improvetrioxane purityVSAvoidevaporation heat loss
Core Design Contradiction:
Manufacturing precisionVSLoss of energy

Solution Approach 1:

The patent utilizes phase transition by condensing the vapor mixture from distillation back into liquid form, then employing liquid-liquid extraction to separate trioxane from water. This approach avoids the energy-intensive process of completely evaporating water while still achieving effective separation through the phase change and subsequent extraction steps.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The patent introduces an organic solvent as an intermediary substance to facilitate the separation of trioxane from water. The solvent acts as a mediator that selectively extracts trioxane from the aqueous phase, enabling separation without requiring complete evaporation of water and thus reducing energy consumption.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Loss of energy

If liquid/liquid extraction is carried out without phase change, then energy consumption is reduced, but a large amount of trioxane is transferred to an aqueous phase, deteriorating processing efficiency

Engineering Contradiction:
Improveenergy consumptionVSAvoidprocessing efficiency
Core Design Contradiction:
Loss of energyVSProductivity

Solution Approach 1:

The organic solvent serves as an intermediary that preferentially dissolves trioxane from the aqueous mixture. By selecting a solvent with appropriate solubility characteristics, the patent achieves effective trioxane extraction into the organic phase while minimizing its transfer to the aqueous phase, thus maintaining high processing efficiency without requiring energy-intensive phase change.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent optimizes extraction parameters such as solvent-to-feed ratio, temperature, and mixing conditions to maximize trioxane transfer to the organic phase while minimizing its presence in the aqueous phase. These parameter adjustments enable efficient separation without phase change, reducing energy consumption while maintaining high productivity.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If a large amount of solvent is employed to extract trioxane, then trioxane solubility in water is overcome, but a large-sized distillation column is required and a great amount of energy is consumed

Engineering Contradiction:
Improvetrioxane extraction efficiencyVSAvoiddistillation column size
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent optimizes the solvent quantity and extraction conditions to achieve effective trioxane separation without requiring excessive solvent. By carefully controlling extraction parameters, the patent reduces the load on subsequent distillation operations, allowing for smaller, more economical distillation columns and lower energy consumption.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements a solvent recovery system where the organic solvent is separated from extracted trioxane and reused in subsequent extraction operations. This recovery approach reduces the total solvent requirement over time, minimizing the size of distillation equipment needed and reducing overall energy consumption while maintaining high extraction efficiency.

Inventive Principle:
Principle #34Discarding and recovering

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 recovers 80-85% of energy consumed in reactors and distillation columns as steam, enhances trioxane yield, and improves extraction efficiency by minimizing trioxane in the aqueous phase, while allowing for flexible solvent selection.

Implementation Method 1

preparing trioxane from a formaldehyde aqueous solution in the presence of an acid catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

distilling a mixture including trioxane

Methodology Applied
Scientific EffectDistillation: Distillation

Implementation Method 3

liquefying the distilled gas mixture

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 4

mixing the liquefied liquid mixture with an extraction solvent and separating the mixture into an aqueous phase and a solvent phase

Methodology Applied
Scientific EffectLiquid-liquid extraction: Liquid-Liquid Extraction

Data Source

PatentUS9598394B2Method of producing trioxane
Publication Date: 2017.03.21 BAEK SUNG YONG
  • US9598394B2 patent drawing
  • US9598394B2 patent drawing
  • US9598394B2 patent drawing

AI summary

Disclosed is a method of producing trioxane, including: (A) preparing trioxane from a high-concentration formaldehyde aqueous solution in the presence of an acid catalyst; (B) distilling a mixture including trioxane; (C) liquefying the distilled gas mixture; (D) mixing the liquefied liquid mixture with an extraction solvent and separating the mixture into an aqueous phase and a solvent phase; (E) distilling the solvent phase to give trioxane, and mixing the aqueous phase with the extraction solvent to give a mixture, which is then separated into an aqueous phase and a solvent phase; and (F) discharging the aqueous phase separated in (E) out of the system, and recirculating the solvent phase so as to be reused in (D) and (E).