Two-Step CO2 Conversion System for Formate Production

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Solution Overview

Problem

Existing carbon dioxide conversion technologies face challenges in achieving high energy efficiency and selectivity, particularly when converting carbon dioxide and hydrocarbons with hydroxy groups, due to differing optimal reaction temperatures and the production of by-products in one-pot conversion systems.

Innovation Solution

A two-step simultaneous conversion system where a hydrocarbon with a hydroxy group is dehydrogenated to produce hydrogen, which is then used in a separate process to convert carbon dioxide into formate, optimizing reaction conditions for each step and improving energy efficiency by separating and reusing hydrogen.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If one-pot simultaneous conversion of hydrocarbon and carbon dioxide is performed, then both conversions occur in a single reactor, but the yield decreases and by-products are produced due to incompatible reaction temperatures

Engineering Contradiction:
Improvereactor configurationVSAvoidconversion yield
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The single-reactor system is segmented into two separate reactors: a first reactor for dehydrogenation of hydrocarbon containing at least one hydroxy group at higher temperature, and a second reactor for hydrogenation of carbon dioxide at lower temperature. This segmentation allows each reaction to proceed at its optimal temperature, resolving the temperature incompatibility issue while maintaining high conversion yields.

Inventive Principle:
Principle #1Segmentation

2Device complexity

If one-pot conversion is performed, then the process is simpler, but energy efficiency decreases due to inability to optimize reaction conditions for each step

Engineering Contradiction:
Improveprocess configurationVSAvoidenergy efficiency
Core Design Contradiction:
Device complexityVSUse of energy by moving object

Solution Approach 1:

The conversion process is segmented into two distinct steps in separate reactors, allowing independent optimization of reaction conditions for each step. The first reactor operates at higher temperature for dehydrogenation, while the second reactor operates at lower temperature for hydrogenation, thereby maximizing energy efficiency for each reaction step.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The dehydrogenation reaction is performed first in the first reactor to generate hydrogen in advance, which is then supplied to the second reactor for the hydrogenation of carbon dioxide. This preliminary action ensures that the hydrogenation reaction has sufficient hydrogen available under optimized conditions, improving overall energy efficiency.

Inventive Principle:
Principle #10Preliminary action

3Device complexity

If one-pot conversion is used, then the system is simpler to operate, but hydrogen cannot be directly utilized and energy is wasted

Engineering Contradiction:
Improvesystem configurationVSAvoidhydrogen utilization efficiency
Core Design Contradiction:
Device complexityVSLoss of energy

Solution Approach 1:

The two separate conversion processes are merged into an integrated two-step system where the hydrogen produced in the first reactor is directly utilized in the second reactor. This merging of processes eliminates hydrogen waste and improves energy efficiency by ensuring complete utilization of the generated hydrogen for carbon dioxide conversion.

Inventive Principle:
Principle #5Merging (Combining)

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 increases the yield and efficiency of both hydrocarbon and carbon dioxide conversion processes, reducing by-product formation and enabling the direct use of hydrogen in carbon dioxide conversion, thus enhancing energy efficiency and convenience.

Implementation Method 1

a hydrocarbon conversion step of converting a hydrocarbon containing at least one hydroxy group into a metal salt that is a dehydrogenated form of the hydrocarbon, hydrogen, and water in the presence of water and a metal oxalate

Methodology Applied
Scientific EffectDehydrogenation:

Implementation Method 2

a carbon dioxide conversion step of converting the hydrogen obtained in the hydrogen separation step into formate by reacting with carbon dioxide or carbon dioxide-derived carbonate

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Data Source

PatentUS20230026024A1System and method for two-step simultaneous conversion of carbon dioxide (CO2) and hydrocarbon containing at least one hydroxy group
Publication Date: 2023.01.26 KOREA UNIV RES & BUSINESS FOUND
  • US20230026024A1 patent drawing
  • US20230026024A1 patent drawing
  • US20230026024A1 patent drawing

AI summary

Proposed is a two-pot-two-step simultaneous conversion system for carbon dioxide and a hydrocarbon containing at least one hydroxy group and a method thereof. The system integrates a process of producing a metal salt that is a dehydrogenated form of the hydrocarbon, hydrogen, and water by reacting a hydrocarbon containing at least one hydroxy group in the presence of water and a metal oxalate, and a process of converting carbon dioxide or carbon dioxide-derived carbonate into formate by hydrogenation, thereby increasing energy efficiency while maintaining a higher hydrocarbon conversion rate and a higher carbon dioxide conversion rate than the one-pot conversion system for hydrocarbon and carbon dioxide.