Low Temperature SWCNT Synthesis Using Fe:Mo Catalyst

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Solution Overview

Problem

Current methods for synthesizing single-wall carbon nanotubes (SWCNTs) at lower temperatures are limited by the decomposition of carbon feedstocks, with high temperatures still required for endothermic carbon sources, hindering large-scale production and understanding of growth mechanisms.

Innovation Solution

A method involving an Fe and Mo-containing catalyst composition supported on alumina, heated to a high temperature and then cooled, with an endothermic carbon-containing feedstock like methane, allowing for SWCNT growth at a lower temperature of 560°C by optimizing the decomposition process through plasma exposure and reducing atmosphere.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If endothermic carbon feedstock (methane) is used for SWCNT synthesis, then the synthesis temperature must be high (above 900°C), but this increases energy consumption and process complexity

Engineering Contradiction:
Improvesynthesis temperatureVSAvoidenergy consumption
Core Design Contradiction:
TemperatureVSUse of energy by moving object

Solution Approach 1:

The catalyst is pre-reduced at high temperature (900-1000°C) before the actual SWCNT growth step. This preliminary reduction action prepares the catalyst in an active state that enables lower temperature synthesis during the actual production phase, resolving the contradiction between achieving sufficient catalytic activity and minimizing energy consumption

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The invention changes the catalyst's chemical state through reduction treatment, transforming it from an oxidized state to an active metallic state. This parameter change in catalyst composition enables the system to operate at lower temperatures during the actual SWCNT synthesis, reducing energy requirements while maintaining synthesis effectiveness

Inventive Principle:
Principle #35Parameter changes

2Adaptability or versatility

If endothermic carbon feedstock is used, then the decomposition temperature limits the growth temperature, but this restricts the range of usable feedstocks

Engineering Contradiction:
Improvefeedstock flexibilityVSAvoidgrowth temperature
Core Design Contradiction:
Adaptability or versatilityVSTemperature

Solution Approach 1:

The reduced catalyst acts as an intermediary that mediates between the endothermic decomposition of methane and the SWCNT growth process. By providing a lower activation energy pathway for carbon incorporation, the reduced catalyst enables growth at temperatures below the methane decomposition threshold, effectively decoupling the feedstock decomposition temperature from the growth temperature constraint

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The invention changes the catalyst's oxidation state from oxidized to reduced, which fundamentally alters the temperature requirements for the synthesis process. This parameter change enables the use of endothermic feedstocks like methane at lower growth temperatures, expanding feedstock versatility without being constrained by the feedstock's decomposition temperature

Inventive Principle:
Principle #35Parameter changes

3Reliability

If high temperature is used for catalyst reduction, then the catalyst becomes more active, but this increases process complexity and energy requirements

Engineering Contradiction:
Improvecatalyst activityVSAvoidprocess complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The catalyst reduction is performed as a preliminary step before the actual SWCNT growth. This separation of reduction and growth into distinct stages allows the system to achieve high catalyst activity through high-temperature reduction, then maintain simpler, lower-temperature conditions during the production phase, reducing overall process complexity

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The invention segments the overall process into two distinct stages: (1) catalyst reduction at high temperature to achieve active catalyst state, and (2) SWCNT growth at lower temperature using the reduced catalyst. This segmentation allows each stage to be optimized independently, achieving high catalyst activity without permanently increasing process complexity

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

Achieves the lowest reported temperature for SWCNT growth with this catalyst composition and methane as the carbon source, indicating that endothermic feedstock decomposition is the limiting factor, and suggests potential for even lower temperature synthesis with more active feedstocks or plasma-assisted decomposition.

Implementation Method 1

catalytic decomposition of carbon feedstock gas yielding C atoms

Methodology Applied
Scientific EffectCatalytic decomposition: Catalysis

Implementation Method 2

diffusion of these C atoms to the tube end that is strongly attached to the catalyst surface

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 3

heating the catalyst composition in a reducing atmosphere to a first temperature of greater than about 900° C.

Methodology Applied
Scientific EffectReduction: Reduction

Implementation Method 4

optimizing the decomposition process through plasma exposure

Methodology Applied
Scientific EffectPlasma: Plasma

Data Source

PatentUS8728430B2Low temperature single-wall carbon nanotube synthesis
Publication Date: 2014.05.20 HONDA MOTOR CO LTD
  • US8728430B2 patent drawing
  • US8728430B2 patent drawing
  • US8728430B2 patent drawing

AI summary

The present disclosure is directed to a method for producing SWCNT from endothermic carbon-containing feedstock, such as, methane gas, using an activated alumina supported Fe:Mo catalyst. The SWCNT growth temperature is less than about 560° C., and the catalyst is activated by exposure to a reducing atmosphere at a temperature greater than about 900° C.