Ethanol Production from Lignocellulosic Biomass via Low-Dose Xylose Fermentation

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Solution Overview

Problem

Current methods for producing ethanol from biomass, particularly cellulosic feedstocks, face inefficiencies in preparing and treating biomass to maximize ethanol yield, often due to inhibitory components and the limited ability of conventional yeast strains to ferment xylose effectively.

Innovation Solution

A method involving pre-treatment and separation of biomass into a liquid and solids component, followed by fed batch fermentation with a low yeast dose, where the pH is adjusted to 4.5-6.5 and temperature maintained between 25-37°C, using an ethanologen capable of fermenting xylose into ethanol, with additional xylose supplied at a controlled rate to achieve high conversion efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional yeast strains are used for fermentation, then the fermentation process is simpler to operate, but the ability to ferment xylose effectively is limited

Engineering Contradiction:
Improvexylose fermentation capabilityVSAvoidyeast strain adaptability
Core Design Contradiction:
ReliabilityVSAdaptability or versatility

Solution Approach 1:

The patent changes the fundamental parameter of yeast strain selection by using engineered yeast strains (such as Saccharomyces cerevisiae modified with xylose utilization pathways) instead of conventional strains. This parameter change enables effective xylose fermentation while maintaining operational simplicity, resolving the contradiction between fermentation capability and strain adaptability.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If high yeast dose is used in fed batch fermentation, then the fermentation speed increases, but the cost and complexity of the process increases

Engineering Contradiction:
Improvefermentation speedVSAvoidfermentation process complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent implements dynamic control of the fed batch fermentation process by gradually adding substrate (xylose-containing hydrolysate) at controlled rates rather than using all-at-once addition. This dynamic approach allows the yeast population to grow and adapt progressively, achieving high productivity with lower overall yeast doses and reduced process complexity.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent applies preliminary action by conducting a growth phase before the production phase in the fed batch fermentation. During this preliminary growth phase, yeast cells are allowed to acclimate and multiply on the substrate, preparing them for efficient ethanol production in the subsequent phase. This preliminary preparation enables higher productivity with reduced yeast requirements.

Inventive Principle:
Principle #10Preliminary action

3Productivity

If pH is not adjusted during fermentation, then the process is simpler to operate, but the fermentation efficiency and yield decrease

Engineering Contradiction:
Improveethanol yieldVSAvoidfermentation operation simplicity
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

The patent implements feedback control by monitoring pH during fermentation and making adjustments based on measured values. The pH is maintained within an optimal range (typically 4.0-6.0) through automated or manual addition of base or acid as needed. This feedback mechanism ensures high ethanol yield while the automation reduces operational complexity.

Inventive Principle:
Principle #23Feedback

4Reliability

If all xylose is supplied at the beginning of fermentation, then the process is simpler to operate, but the conversion efficiency decreases due to inhibitory components

Engineering Contradiction:
Improvexylose to ethanol conversion efficiencyVSAvoidsubstrate addition complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent applies periodic action by dividing the substrate addition into multiple stages or batches throughout the fermentation process. Instead of adding all xylose at once, the substrate is added periodically at controlled intervals or rates. This periodic addition allows the yeast population to process inhibitory components progressively and maintain high conversion efficiency, while the standardized feeding protocol keeps operational complexity manageable.

Inventive Principle:
Principle #19Periodic 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 approach achieves a fermentation product with at least 75% conversion of xylose to ethanol, improving the efficiency and yield of cellulosic ethanol production from lignocellulosic biomass, such as corn cobs and stalks, compared to previous methods.

Implementation Method 1

The ethanologen is capable of fermenting xylose into ethanol

Methodology Applied
Scientific EffectFermentation: Fermentation

Implementation Method 2

adjusting the pH of the slurry to a range of about 4.5 to about 6.5

Methodology Applied
Scientific EffectpH adjustment:

Implementation Method 3

maintaining the first component and the ethanologen in the fermentation system at a temperature of between about 25 and about 37 degrees Celsius

Methodology Applied
Scientific EffectTemperature control:

Data Source

PatentEP2582822B1Method for producing ethanol from biomass
Publication Date: 2015.05.06 POET RESEARCH INC
  • EP2582822B1 patent drawingFigure 1A
  • EP2582822B1 patent drawingFigure 1B
  • EP2582822B1 patent drawingFigure 2

AI summary

A method for producing a fermentation product in a fermentation system from biomass that has been pre-treated and separated into a first component and a second component is provided. The method comprises preparing a slurry comprising: supplying the first component to the fermentation system; and providing an ethanologen to the fermentation system. The method also comprises adjusting the pH of the slurry to a range of about 4.5 to about 6.5, maintaining the first component and ethanologen in the fermentation system at a temperature of between about 25 and about 37 degrees Celsius, and recovering fermentation product from the fermentation system. The ethanologen is supplied to the fermentation system in a concentration of less than 2 grams of ethanologen on a dry basis per liter of slurry. The biomass comprises lignocellulosic material. The first component comprises pentose, which can comprise xylose. The ethanologen is capable of fermenting xylose into ethanol.