Surface-Modified Oxygen Carriers for Low-Temperature Olefin Catalysis

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current methods for converting natural gas liquids and naphtha to olefins, such as steam cracking, are energy-intensive and produce significant emissions, and are not economically viable for small-scale operations due to high energy requirements and environmental impacts.

Innovation Solution

Development of redox catalysts with a core oxygen carrier and a surface-modifying shell, comprising specific metal salts and tungstates, which facilitate low-temperature oxidative dehydrogenation and cracking processes, reducing energy consumption and emissions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If steam cracking is used to convert natural gas liquids and naphtha to olefins, then olefin production is achieved, but energy consumption is excessive and emissions are significant

Engineering Contradiction:
Improveolefin production efficiencyVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent changes the operating temperature parameter from high temperature (steam cracking) to low temperature (oxidative dehydrogenation), fundamentally altering the energy requirements of the process. The core-shell catalyst enables this parameter change by providing active sites for oxidation at lower temperatures while maintaining catalytic activity for olefin production.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs a composite core-shell catalyst structure where the core material (e.g., metal oxide) provides oxygen storage and release capabilities, while the shell material (e.g., zeolite or other catalyst) provides selective cracking activity. This composite structure enables low-temperature oxidative dehydrogenation to produce olefins with high efficiency and reduced energy consumption.

Inventive Principle:
Principle #40Composite materials

2Productivity

If steam cracking is used to convert natural gas liquids and naphtha to olefins, then olefin production is achieved, but CO2 and NOx emissions increase

Engineering Contradiction:
Improveolefin production efficiencyVSAvoidemissions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent changes the temperature parameter to operate below the threshold for significant NOx formation, while using controlled oxidation to achieve olefin production. This parameter change fundamentally reduces the formation of harmful emissions while maintaining productivity.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent converts the harmful combustion process into a beneficial controlled oxidation process. By using the core-shell catalyst to facilitate selective oxidative dehydrogenation, the energy release from oxidation is harnessed to drive the endothermic cracking reaction, reducing the need for external fuel combustion and associated emissions.

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

3Productivity

If high temperature is used for steam cracking, then olefin production is maintained, but the process is not economically viable for small-scale operations

Engineering Contradiction:
Improveolefin productionVSAvoideconomic viability for small-scale operations
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The patent changes the temperature parameter from high to low, which reduces capital equipment requirements, energy infrastructure needs, and operational complexity. This makes the process economically viable for small-scale and distributed operations while maintaining olefin production capability.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent enables distributed small-scale production units to be deployed locally near natural gas liquid sources, segmenting the olefin production process from centralized large-scale steam cracking facilities. This segmentation reduces transportation costs and enables economic viability for small-scale operations.

Inventive Principle:
Principle #1Segmentation

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

The redox catalysts enable efficient conversion of saturated hydrocarbons to unsaturated hydrocarbons at lower temperatures, improving energy efficiency and reducing environmental impact while maintaining high selectivity and stability.

Implementation Method 1

redox catalysts enable efficient conversion of saturated hydrocarbons to unsaturated hydrocarbons

Methodology Applied
Scientific EffectRedox reactions: Redox Reactions

Implementation Method 2

the outer shell comprising a metal salt. The salt can modify the surface of the catalysts

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS20230415124A1Oxygen carrying materials with surface modification for redox-based catalysis and methods of making and uses thereof
Publication Date: 2023.12.28 NORTH CAROLINA STATE UNIV
  • US20230415124A1 patent drawing
  • US20230415124A1 patent drawing
  • US20230415124A1 patent drawing

AI summary

Redox catalysts having surface medication, methods of making redox catalysts with surface modification, and uses of the surface modified redox catalysts are provided. In some aspects, the redox catalysts include a core oxygen carrier region such as CaMnO3, BaMnO3-δ, SrMnO3-δ, Mn2SiO4, Mn2MgO4-δ, La0.8Sr0.2O3-δ, La0.8Sr0.2FeO3-δ, Ca9Ti0.1Mn0.9O3-δ, Pr6O11-δ, manganese ore, or a combination thereof; and an outer shell having an average thickness of about 1-100 monolayers surrounding the outer surface of the core region. The outer shell can include, for example a salt selected such as Li2WO4, Na2WO4, K2WO4, SrWO4, Li2MoO4, Na2MoO4, K2MoO4, CsMoO4, Li2CO3, Na2CO3, K2CO3, or a combination thereof.