Cu/Zn Catalyst Methanol Synthesis from CO2

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Solution Overview

Problem

Current methods for converting hydrocarbon feedstock into syngas result in high carbon dioxide emissions and energy-intensive processes with limited selectivity to methanol, requiring severe reaction conditions and separate oxygen generation, which increases environmental concerns and operational costs.

Innovation Solution

An integrated process utilizing a Cu/Zn-based catalyst system for CO2 hydrogenation, where syngas from gasified hydrocarbon feedstock is used for power generation, and the CO2 exhaust is recycled for methanol synthesis, with oxygen produced from an electrolyzer used as a gasifying and combustion agent, eliminating the need for separate oxygen generation and CO2 capture systems.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Power

If hydrocarbon feedstock is converted into syngas for power generation, then electricity production is achieved, but carbon dioxide emissions increase and environmental harm worsens

Engineering Contradiction:
Improveelectricity productionVSAvoidcarbon dioxide emissions
Core Design Contradiction:
PowerVSObject-generated harmful factors

Solution Approach 1:

The patent converts the harmful CO2 emissions from syngas power generation into a useful resource by recycling them to the gasification unit for further syngas production and to the methanol synthesis unit for methanol production. This transforms the waste product CO2 into valuable chemical feedstock, thereby converting the harmful emission into a beneficial output.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Solution Approach 2:

The patent recovers and reuses CO2 that would otherwise be discarded as waste. The CO2 from the power generation exhaust is captured and redirected to multiple units including gasification and methanol synthesis, maximizing resource utilization and minimizing waste discharge.

Inventive Principle:
Principle #34Discarding and recovering

2Reliability

If separate oxygen generation system is used for gasification and combustion, then sufficient oxygen supply is achieved, but device complexity and operational costs increase

Engineering Contradiction:
Improveoxygen supplyVSAvoidprocess complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent merges the oxygen generation function with the electrolyzer unit that produces hydrogen. The electrolyzer simultaneously generates both H2 and O2, eliminating the need for separate oxygen generation equipment and simplifying the overall process configuration.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The electrolyzer unit performs multiple functions: it produces hydrogen for methanol synthesis and simultaneously generates oxygen for gasification and combustion processes. This multi-functional approach reduces the number of dedicated units required and lowers overall system complexity.

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

3Productivity

If severe reaction conditions are used for methanol synthesis from syngas, then methanol production is achieved, but energy consumption increases

Engineering Contradiction:
Improvemethanol productionVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent changes the approach from using syngas (which requires severe conditions) to using CO2 hydrogenation with adjusted parameters. By modifying the reactant type and corresponding reaction conditions, the process achieves methanol production under more energy-efficient parameters while maintaining productivity.

Inventive Principle:
Principle #35Parameter changes

4Object-generated harmful factors

If CO2 capture system is added to utilize CO2, then CO2 utilization is achieved, but device complexity and capital costs increase

Engineering Contradiction:
ImproveCO2 utilizationVSAvoidprocess complexity
Core Design Contradiction:
Object-generated harmful factorsVSDevice complexity

Solution Approach 1:

The patent merges CO2 utilization functions with existing process units. The CO2 from power generation exhaust is directly fed to the gasification unit and methanol synthesis unit without requiring separate capture and storage infrastructure, thereby achieving CO2 utilization while minimizing additional complexity.

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 process achieves high methanol yield and selectivity while reducing CO2 emissions, utilizing waste CO2 for fuel production, and simplifying the process by integrating oxygen production and recycling, thus reducing capital and operational costs and environmental impact.

Implementation Method 1

a Cu/Zn-based catalyst system is used inside the methanol reactor for methanol synthesis through direct hydrogenation of CO2

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

methanol synthesis through direct hydrogenation of CO2

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 3

operating an electrolyzer to produce hydrogen

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 4

gasifying the hydrocarbon feedstock and oxygen inside a gasification unit to produce a syngas

Methodology Applied
Scientific EffectGasification:

Implementation Method 5

utilizing the produced syngas inside a power generation unit for electrical power generation

Methodology Applied
Scientific EffectCombustion: Combustion

Data Source

PatentUS11773039B2Integrated process and Cu/Zn-based catalyst for synthesizing methanol utilizing CO2, generating electricity from hydrocarbon feedstock
Publication Date: 2023.10.03 INDIAN OIL CORP LTD
  • US11773039B2 patent drawing
  • US11773039B2 patent drawing
  • US11773039B2 patent drawing

AI summary

The present disclosure provides an integrated process and a Cu/Zn-based catalyst system for synthesizing methanol from CO2 and generating electricity from hydrocarbon feedstock. The process includes steps of gasifying hydrocarbon feedstock into syngas by using oxygen and using the produced syngas as a fuel in a power generation unit, reusing a first part of an exhaust stream of the power generation unit as a reactant in the gasification unit. Using a second part of the said exhaust stream as a reactant for methanol synthesis in a methanol reactor, wherein, the second part is treated to separate CO2 and water, and CO2 is used as the reactant for methanol synthesis. Operating an electrolyzer during non-peak hours to produce hydrogen, wherein, a required stoichiometric ratio of the produced hydrogen is transferred into the methanol reactor for methanol synthesis, wherein, a Cu/Zn-based catalyst system is used for methanol synthesis through a direct hydrogenation reaction of CO2.