Trioxane Production via Gas-Phase Formaldehyde Trimerization

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Solution Overview

Problem

Current methods for producing trioxane from formaldehyde are inefficient, leading to low conversion rates and high energy consumption, with complex and costly separation processes, and the formation of significant side products.

Innovation Solution

A process involving a liquid reaction mixture composed of a formaldehyde source, an aprotic compound with a boiling point of 140 °C or higher, and a catalyst, which increases the conversion of formaldehyde to cyclic acetals like trioxane while reducing energy consumption and simplifying separation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If aqueous formaldehyde solution is used with concentrated sulfuric acid catalyst, then trioxane production is achieved, but conversion rate is low (less than 10%) and side products are high

Engineering Contradiction:
Improveconversion rateVSAvoidside products
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent changes the physical state parameter of formaldehyde from aqueous solution to gas phase, and modifies the catalyst system from concentrated sulfuric acid to solid acid catalysts or ion-exchange resins. These parameter changes enable higher conversion rates (excess of 10%, preferably 20-80%) and significantly reduce side product formation by eliminating the aqueous environment that promotes Cannizzaro reaction

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent replaces the liquid-phase chemical system with concentrated sulfuric acid with a gas-phase reaction system using solid acid catalysts or ion-exchange resins. This substitution eliminates the need for complex extraction and solvent recovery steps, directly reducing side products and simplifying the process

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

2Productivity

If conventional liquid system with sulfuric acid is used, then trioxane is produced, but energy consumption is high due to distillation and extraction steps

Engineering Contradiction:
Improveproduction efficiencyVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The patent utilizes phase transition by conducting the reaction in the gas phase rather than liquid phase. This enables direct vapor-phase reaction and simplifies product separation through condensation, eliminating the need for energy-intensive distillation and extraction steps required in conventional liquid-phase processes

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The patent extracts and eliminates the water component from the formaldehyde feedstock by using gas-phase formaldehyde or paraformaldehyde decomposition, thereby removing the need for subsequent extraction and solvent recovery steps that consume significant energy in conventional processes

Inventive Principle:
Principle #2Taking out (Extraction)

3Productivity

If gas phase trimerization is used with solid catalyst, then reaction control is difficult and equipment costs are high, but conversion can be achieved

Engineering Contradiction:
Improveconversion achievementVSAvoidequipment complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent optimizes reaction parameters including temperature (60-150°C), pressure (1-20 bar), and catalyst selection (solid acid catalysts or ion-exchange resins) to achieve controlled gas-phase reaction. These parameter changes enable the use of simpler, less expensive equipment compared to high-temperature gas-phase processes while maintaining effective conversion

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs inexpensive solid acid catalysts and ion-exchange resins that can be easily handled and replaced, avoiding the need for expensive pressure-resistant vessels and complex reaction equipment required in conventional high-temperature gas-phase processes

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

4Quantity of substance

If aqueous formaldehyde solution is concentrated by distillation, then water is removed, but energy consumption increases and azeotrope formation complicates separation

Engineering Contradiction:
Improveformaldehyde concentrationVSAvoiddistillation energy
Core Design Contradiction:
Quantity of substanceVSLoss of energy

Solution Approach 1:

The patent bypasses the need for water removal by directly using gas-phase formaldehyde or decomposing paraformaldehyde in the gas phase. This eliminates the distillation step entirely, avoiding both the high energy consumption and the azeotrope formation problems inherent in concentrating aqueous formaldehyde solutions

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The patent performs preliminary decomposition of paraformaldehyde to generate gas-phase formaldehyde before the trimerization reaction. This preliminary action eliminates the need for subsequent distillation and concentration steps, directly avoiding energy consumption and separation complications

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 process achieves higher conversion rates of formaldehyde to cyclic acetals, such as trioxane, with reduced energy consumption and fewer side products, facilitating easier and less complex separation.

Implementation Method 1

converting the formaldehyde source in the reaction mixture to cyclic acetals

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentEP2782905B1Process for the production of trioxane
Publication Date: 2020.01.01 CELANESE SALES GERMANY
  • EP2782905B1 patent drawing
  • EP2782905B1 patent drawing
  • EP2782905B1 patent drawing

AI summary

The present invention relates to a process for producing cyclic acetal comprising i) preparing a liquid reaction mixture comprising a) formaldehyde source, b) an aprotic compound and c) a catalyst; and ii) converting the formaldehyde source into cyclic acetals.