Ethionic Acid Production in Falling Film Reactor

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Solution Overview

Problem

Existing methods for producing ethionic acid using sulfur trioxide are economically disadvantageous due to the need for toxic sulfur dioxide as a reaction medium, high costs associated with using pure sulfur trioxide, and inefficiencies in heat management and scalability, particularly in industrial-scale implementations.

Innovation Solution

A process involving the reaction of ethanol and sulfur trioxide in a falling film reactor with a molar ratio of 1:2, where the reactor is cooled, using ethionic acid as the reaction medium and sulfur trioxide diluted with inert gases, allowing for controlled exothermic reactions and scalable production without additional solvents, utilizing contact gas to reduce costs.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If liquid sulfur dioxide is used as reaction solvent, then quantitative yield of ethionic acid is obtained, but toxic sulfur dioxide must be recovered and recompressed which represents major operational expense

Engineering Contradiction:
ImproveyieldVSAvoidoperational expense
Core Design Contradiction:
Manufacturing precisionVSEase of manufacture

Solution Approach 1:

The patent extracts and eliminates the toxic sulfur dioxide solvent from the process by using ethionic acid itself as the reaction medium. This removes the need for sulfur dioxide recovery and compression operations, eliminating the major operational expense while maintaining quantitative yield through the self-solvating property of ethionic acid.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent applies self-service by using the product itself (ethionic acid) as the reaction medium. This self-solvating approach eliminates the need for separate solvent recovery systems and reduces operational expenses while maintaining high yield, as the product serves dual purposes: as both reactant and solvent.

Inventive Principle:
Principle #25Self-service

2Manufacturing precision

If pure sulfur trioxide is used, then quantitative yield is achieved, but it is much more costly than contact gas

Engineering Contradiction:
ImproveyieldVSAvoidcost
Core Design Contradiction:
Manufacturing precisionVSEase of manufacture

Solution Approach 1:

The patent changes the parameter of sulfur trioxide concentration by using diluted contact gas (containing inert gases) instead of pure sulfur trioxide. The ethionic acid solvent compensates for the dilution, allowing quantitative yield to be maintained while using cheaper contact gas as the sulfonating agent.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces ethionic acid as an intermediary solvent that enables the use of diluted sulfur trioxide. This intermediary medium allows contact gas to function effectively as the sulfonating agent, bridging the gap between cost reduction and maintaining quantitative yield.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If two stage process is used for direct sulfonation, then reaction can be carried out, but the reaction heat is inherently difficult to remove in the first stage at temperature of 0-5° C.

Engineering Contradiction:
Improvereaction completionVSAvoidheat removal difficulty
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent segments the reaction system into multiple zones within a single stage: a reaction zone where sulfonation occurs and a cooling zone where heat is removed. This spatial segmentation allows the exothermic reaction to proceed while heat is continuously removed, eliminating the need for two-stage temperature control.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent implements continuous cooling throughout the reaction process rather than allowing temperature buildup. The cooling means operates continuously to maintain optimal temperature, enabling single-stage operation while managing the exothermic heat effectively.

Inventive Principle:
Principle #20Continuity of useful action

4Ease of manufacture

If contact gas is used as sulfonating agent, then cost is reduced, but productivity is limited by contact time and absorption efficiency

Engineering Contradiction:
ImprovecostVSAvoidproductivity
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent uses a falling film reactor that utilizes gravity-driven liquid flow to create intimate contact between the gas-phase contact gas and liquid-phase ethionic acid. This hydraulic arrangement maximizes mass transfer and absorption efficiency, overcoming the limitations of gas-liquid contact time while maintaining low cost through use of contact gas.

Inventive Principle:
Principle #29Pneumatics and hydraulics

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 a practically quantitative yield of high-purity ethionic acid, simplifies heat management, and enables easy scaling of production capacity while eliminating the need for toxic solvents and reducing operational expenses.

Implementation Method 1

reacting ethanol and sulfur trioxide in a molar ratio of 1:2 in a falling film reactor while cooling the reactor with a cooling means

Methodology Applied
Scientific EffectCooling: Cooling

Implementation Method 2

falling film reactor

Methodology Applied
Scientific EffectGravity-driven flow: Gravitation

Data Source

PatentUS9061978B1Process for the production of ethionic acid
Publication Date: 2015.06.23 LIBRE HLDG
  • US9061978B1 patent drawing

AI summary

The present invention discloses a process for the production of ethionic acid by reacting ethanol with sulfur trioxide in a molar ratio of 1:2 at a temperature from 40 to 100° C. in a falling film reactor while cooling the reactor with a cooling means.