Higher Alcohol Production via Methanol Recycle Loop

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Solution Overview

Problem

Current methods for producing higher alcohols like ethanol and propanol on an industrial scale rely heavily on plant feedstock and lack efficient systems for recycling methanol to increase yield, leading to suboptimal production and reliance on single feedstock sources.

Innovation Solution

A system and method that involves reacting carbonaceous materials to produce synthesis gas, which is then processed to generate higher alcohols, with a methanol recycle loop to increase production of higher-order alcohols while minimizing methanol in downstream products, using a CO2 removal unit to optimize the process.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If fermentation processes are used to produce ethanol on an industrial scale, then ethanol production is achieved, but significant amounts of plant feedstock are required

Engineering Contradiction:
Improveplant feedstock consumptionVSAvoidethanol production efficiency
Core Design Contradiction:
Quantity of substanceVSProductivity

Solution Approach 1:

The patent changes the fundamental parameter of feedstock type from plant-based to carbonaceous materials (coal, biomass, waste), enabling ethanol and higher alcohol production without relying on agricultural crops. This parameter change resolves the contradiction by eliminating plant feedstock consumption while maintaining industrial-scale production capability through gasification and catalytic conversion processes

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces synthesis gas (syngas) as an intermediary substance produced from carbonaceous materials through gasification. This syngas serves as the intermediate feedstock that is subsequently converted to ethanol and higher alcohols via catalytic reactions, thereby mediating between the carbonaceous feedstock and the desired alcohol products while avoiding direct plant feedstock requirements

Inventive Principle:
Principle #24Intermediary (Mediator)

2Adaptability or versatility

If standard reformer and auto-reformer processes are used, then syngas production is achieved, but the process is limited to natural gas (methane) as feedstock

Engineering Contradiction:
Improvefeedstock flexibilityVSAvoidsyngas production capability
Core Design Contradiction:
Adaptability or versatilityVSProductivity

Solution Approach 1:

The patent applies universality by developing a gasification system that can process multiple types of carbonaceous materials (coal, biomass, waste) through a single integrated process flow. This multi-functional approach replaces the limitation to natural gas feedstock, enabling the system to adapt to various carbon-based feedstocks while maintaining syngas production capability and alcohol synthesis functionality

Inventive Principle:
Principle #6Universality (Multi-functionality)

3Quantity of substance

If methanol is produced in the alcohol stream, then alcohol production is achieved, but methanol accumulates in downstream products

Engineering Contradiction:
Improvehigher alcohol yieldVSAvoidmethanol content in product
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

The patent implements a feedback mechanism by recycling a portion of the methanol stream back to the reactor inlet. This feedback loop continuously converts accumulated methanol into higher-order alcohols through catalytic reactions, thereby maintaining high yields of desired products while preventing methanol buildup in the final product stream. The recycled methanol serves as an additional reactant that drives the formation of higher alcohols

Inventive Principle:
Principle #23Feedback

4Device complexity

If single feedstock sources are used, then production process is simplified, but economic viability and regulatory compliance are compromised

Engineering Contradiction:
Improveprocess simplicityVSAvoideconomic viability
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The patent applies dynamics by designing a flexible feedstock intake system that can dynamically adjust to process different carbonaceous materials (coal, biomass, waste) based on availability, cost, and regulatory requirements. This dynamic capability allows the process to adapt to changing market conditions and resource availability, thereby enhancing economic viability and regulatory compliance while maintaining operational flexibility

Inventive Principle:
Principle #15Dynamics

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 reduces the cost of producing higher alcohols by utilizing a wide range of non-plant feedstocks, enhances production efficiency, and allows for independence from single feedstock sources, improving economic viability and compliance with regulations.

Implementation Method 1

a reactor configured to receive the syngas feed and produce an alcohol stream and CO2

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

the alcohol stream can then be separated to produce a net reactor product and a methanol stream

Methodology Applied
Scientific EffectPhase separation: Phase Change

Data Source

PatentUS9149739B2Production of higher alcohols with minimum methanol content from the gasification of carbonaceous materials
Publication Date: 2015.10.06 FLUOR TECH CORP
  • US9149739B2 patent drawing
  • US9149739B2 patent drawing
  • US9149739B2 patent drawing

AI summary

Systems and methods for generating higher alcohols from synthesis gas produced from carbonaceous materials are described, which can include a reactor configured to produce an alcohol stream and CO2 from a syngas feed. The alcohol stream can be separated in one or more downstream separators to produce a net reactor product and a methanol stream that can recycled into the reactor. The net reactor product preferably comprises higher-order alcohols such as ethanol, propanol, and butanol.