Two-Step Hydrothermal Process for Isosorbide Yield

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current methods for producing isosorbide from sorbitol are costly and energy-intensive, often requiring corrosive acid catalysts and high vacuum levels, which lead to equipment corrosion and increased operating costs, while existing alternatives are not economically viable due to the use of large amounts of molten salt hydrates.

Innovation Solution

A two-step hydrothermal reaction process controlling temperature in the absence or presence of a transition metal salt catalyst, where the first reaction occurs at 240° C. to 285° C. and the second at 286° C. to 340° C., maximizing the formation of 1,4-sorbitan and subsequently increasing the yield of isosorbide by promoting its conversion to isosorbide at higher temperatures, thus avoiding the need for corrosive catalysts and reducing energy consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If sulfuric acid is used as a catalyst and high vacuum is applied, then isosorbide can be produced through dehydration of sorbitol, but the reactor is corroded and expensive equipment is required

Engineering Contradiction:
Improveproduction of isosorbideVSAvoidreactor corrosion
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent replaces expensive, corrosion-resistant reactors with standard stainless steel reactors by using a non-corrosive molten salt hydrate catalyst system, effectively substituting expensive durable equipment with cheaper standard equipment that won't corrode

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

Solution Approach 2:

The patent changes the reaction conditions from high vacuum (10 mmHg) to atmospheric pressure by using molten salt hydrate as a catalyst, fundamentally altering the pressure parameter and eliminating the need for vacuum equipment

Inventive Principle:
Principle #35Parameter changes

2Productivity

If sulfuric acid catalyst and high vacuum are used, then isosorbide production is achieved, but additional pH neutralization process and waste treatment are required

Engineering Contradiction:
Improveproduction of isosorbideVSAvoidprocess complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent replaces the complex multi-step process involving acid catalyst, pH neutralization, and waste treatment with a simpler single-step process using molten salt hydrate catalyst that requires no additional treatment steps

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

Solution Approach 2:

The patent extracts and removes the harmful acid catalyst step from the process entirely, replacing it with a non-corrosive molten salt hydrate catalyst that eliminates the need for pH neutralization and waste treatment steps

Inventive Principle:
Principle #2Taking out (Extraction)

3Productivity

If high vacuum level is maintained, then isosorbide production proceeds, but large amount of energy is continuously consumed

Engineering Contradiction:
Improveproduction of isosorbideVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent changes the pressure parameter from high vacuum (10 mmHg) to atmospheric pressure, eliminating the continuous energy consumption required to maintain vacuum conditions while still achieving effective isosorbide production through the molten salt hydrate catalyst

Inventive Principle:
Principle #35Parameter changes

4Productivity

If molten salt hydrate is used in large amounts, then isosorbide can be produced, but the method is cost-ineffective

Engineering Contradiction:
Improveproduction of isosorbideVSAvoidamount of molten salt hydrate
Core Design Contradiction:
ProductivityVSQuantity of substance

Solution Approach 1:

The patent optimizes the catalyst amount parameter, using only 1-10 wt% molten salt hydrate relative to sorbitol, which is sufficient to achieve high isosorbide yields while making the process economically viable

Inventive Principle:
Principle #35Parameter changes

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 significantly increases the yield of isosorbide while reducing operating costs and equipment expenses by optimizing reaction conditions, allowing for efficient water removal without energy-intensive vacuum processes and using less expensive, non-corrosive catalysts.

Implementation Method 1

a method of producing anhydrosugar alcohol using a two-step hydrothermal reaction

Methodology Applied
Scientific EffectHydrothermal reaction:

Implementation Method 2

which converts sugar alcohol to anhydrosugar alcohol

Methodology Applied
Scientific EffectDehydration:

Implementation Method 3

subjecting an aqueous solution of sugar alcohol to a first reaction at a temperature of 240° C. to 285° C. followed by a second reaction at a temperature of 286° C. to 340° C.

Methodology Applied
Scientific EffectSupercritical fluid formation: Supercritical Fluid

Data Source

PatentUS10221187B2Method for preparing anhydrosugar alcohol using two-step hydrothermal reaction
Publication Date: 2019.03.05 SK INNOVATION CO LTD
  • US10221187B2 patent drawing
  • US10221187B2 patent drawing
  • US10221187B2 patent drawing

AI summary

A method for producing anhydrosugar alcohol according to the present invention can increase the yield of anhydrosugar alcohol even in the absence of a catalyst or in the presence of a small amount of a transition metal salt catalyst by controlling the temperature of a high-temperature reaction, which converts sugar alcohol to anhydrosugar alcohol, in two steps, that is, a first low-temperature reaction step and a second high-temperature reaction step.