Methanol Production from Logistical Fuel via Segmentation

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Solution Overview

Problem

Conventional methanol production methods are not feasible for small-scale or portable applications, particularly in situations where traditional fuel sources like natural gas or coal are not available, such as in U.S. military operations, which limits the use of methanol-based technologies like direct methanol fuel cells (DMFCs).

Innovation Solution

A system and method for producing methanol from logistical fuels like JP-8, involving a fuel injection system to combine the fuel with ambient air, a synthesis gas production system to convert the mixture into synthesis gas, and a methanol synthesis system to convert the gas into crude methanol, which is then refined and dispensed as a liquid product.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional methanol production methods (steam reformation of natural gas or coal) are used, then large-scale methanol production (1000 metric tons per day) is achieved, but the system is not suitable for small-scale or portable applications and requires infrastructure not available in specialized situations

Engineering Contradiction:
Improvemethanol production scaleVSAvoidapplicability to specialized situations
Core Design Contradiction:
ProductivityVSAdaptability or versatility

Solution Approach 1:

The conventional large-scale methanol production process is segmented into three separate modular systems: (1) a fuel processing system that converts logistical fuel to synthesis gas, (2) a synthesis gas processing system that converts synthesis gas to crude methanol, and (3) a methanol purification system. This segmentation enables the system to be scaled down and deployed in specialized situations while maintaining production capability.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent introduces synthesis gas as an intermediary substance between the logistical fuel (JP-8) and the final methanol product. The fuel processing system converts JP-8 to synthesis gas, which then serves as the feedstock for methanol synthesis. This intermediary approach enables conversion of available logistical fuel to methanol without requiring direct access to natural gas or coal infrastructure.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If conventional methanol production facilities are built, then high methanol output is achieved, but the device complexity and infrastructure requirements increase significantly

Engineering Contradiction:
Improvemethanol production capacityVSAvoidsystem infrastructure requirements
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The production system is divided into distinct functional modules: fuel injection system, synthesis gas production system, methanol synthesis system, and purification system. Each module performs a specific function and can be independently optimized or scaled, reducing overall system complexity while maintaining production capacity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system is designed to use existing logistical fuel (JP-8) as feedstock, making it universally applicable to military operations without requiring specialized fuel infrastructure. The same system architecture can produce methanol at different scales by adjusting operational parameters rather than requiring complete infrastructure redesign.

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

3Ease of operation

If methanol is produced on-site in specialized situations, then transport and delivery constraints are overcome, but the availability of traditional fuel sources (natural gas, coal) is not present

Engineering Contradiction:
Improveon-site production capabilityVSAvoidfuel source availability
Core Design Contradiction:
Ease of operationVSAdaptability or versatility

Solution Approach 1:

The system uses synthesis gas as an intermediary that can be produced from various carbon-containing fuels. By converting logistical fuel (JP-8) to synthesis gas first, the system adapts to situations where natural gas or coal is unavailable, while still enabling methanol production through the intermediate synthesis gas stage.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The system changes the fundamental parameter of fuel input from conventional natural gas or coal to logistical fuel (JP-8). This parameter change is achieved through modified processing conditions in the fuel processing system that are optimized for jet fuel characteristics, enabling on-site production in specialized situations without traditional fuel infrastructure.

Inventive Principle:
Principle #35Parameter changes

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

Enables efficient, on-site production of methanol at small scales (e.g., 0.1 metric tons per day), bridging the gap between available logistical fuels and methanol requirements, and facilitating the use of DMFCs in specialized operations without relying on traditional fuel sources.

Implementation Method 1

The fuel injection system may include a fuel pump, an air compressor, a mass flow controller, an air heater, and a fuel injector. The fuel injector may receive pressurized liquid logistical fuel stream and heated and pressurized air and may force the logistical fuel and air through an atomizing nozzle.

Methodology Applied
Scientific EffectAtomization:

Implementation Method 2

The catalytic partial oxidation system may include a catalytic partial oxidation reactor configured to receive the logistical fuel/air mixture and convert a portion of the mixture to synthesis gas

Methodology Applied
Scientific EffectCatalytic partial oxidation: Catalysis

Implementation Method 3

The catalytic partial oxidation system may include a catalytic partial oxidation reactor configured to receive the logistical fuel/air mixture and convert a portion of the mixture to synthesis gas

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 4

The methanol synthesis system may include a methanol synthesis reactor configured to receive the synthesis gas and convert the synthesis gas to a crude methanol liquid

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 5

The fuel injection system may include a heat exchanger configured to heat the pressurized air and transfer the heat to the liquid logistical fuel stream

Methodology Applied
Scientific EffectThermal conduction: Conduction (thermal)

Implementation Method 6

The fuel injection system may include a fuel pump, an air compressor, a mass flow controller, an air heater, and a fuel injector

Methodology Applied
Scientific EffectCompression: Compression

Data Source

PatentUS8968685B2Fuel processing system and related methods
Publication Date: 2015.03.03 NORTHROP GRUMMAN SYSTEMS CORP
  • US8968685B2 patent drawing
  • US8968685B2 patent drawing
  • US8968685B2 patent drawing

AI summary

A fuel processing system for converting a logistical fuel and air into a liquid product comprising methanol. One such system comprises a fuel injection system configured to combine a logistical fuel and ambient air to produce a logistical fuel and air mixture, a synthesis gas production system configured to convert the logistical fuel and air mixture to synthesis gas, and a methanol synthesis system configured to convert the synthesis gas to a crude methanol liquid. Related methods are additionally disclosed.