Low-Temperature Hydrocarbon Burner for Enclosed Habitats

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Solution Overview

Problem

Enclosed habitable environments experience a gradual buildup of hydrocarbons due to human metabolic processes, personal care products, materials outgassing, and equipment faults, leading to potentially hazardous concentrations over time, which existing air purifiers struggle to manage effectively.

Innovation Solution

A low-temperature hydrocarbon burner system with a regenerative heat exchanger and catalyst reactor that converts hydrocarbons into H2O and CO2, integrated into air recirculation and filtration systems to prevent hazardous buildup, operating below the decomposition temperatures of common refrigerants to avoid generating harmful byproducts.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a conventional catalytic reactor operates at temperatures above 287-315°C to achieve sufficient catalytic activity, then hydrocarbon conversion efficiency is improved, but the risk of refrigerant decomposition and harmful byproduct generation increases

Engineering Contradiction:
Improvehydrocarbon conversion efficiencyVSAvoidrefrigerant decomposition and harmful byproduct generation
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent changes the temperature parameter from conventional high temperatures (287-315°C) to low temperatures (below refrigerant decomposition points), fundamentally altering the operating conditions to avoid harmful effects while maintaining conversion efficiency through catalyst optimization

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs a composite catalyst system combining multiple metal oxides (manganese oxide, copper oxide, zinc oxide, cerium oxide) to achieve effective catalytic activity at low temperatures without causing refrigerant decomposition, resolving the contradiction between conversion efficiency and safety

Inventive Principle:
Principle #40Composite materials

2Object-affected harmful factors

If a low-temperature catalytic reactor is used to avoid refrigerant decomposition, then safety is improved, but catalytic activity and hydrocarbon conversion efficiency may be reduced

Engineering Contradiction:
Improverefrigerant decomposition preventionVSAvoidhydrocarbon conversion efficiency
Core Design Contradiction:
Object-affected harmful factorsVSProductivity

Solution Approach 1:

The patent uses a composite catalyst comprising multiple metal oxides that work synergistically to provide sufficient catalytic activity at low temperatures, overcoming the typical limitation of reduced conversion efficiency at lower operating temperatures

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The catalyst is supported on a porous material with high surface area, increasing the active catalytic sites available for hydrocarbon conversion at low temperatures, thereby maintaining productivity while operating safely below refrigerant decomposition points

Inventive Principle:
Principle #31Porous materials

3Use of energy by moving object

If a regenerative heat exchanger is added to the system to improve energy efficiency, then power consumption is reduced, but device complexity increases

Engineering Contradiction:
Improvepower consumptionVSAvoidsystem structure
Core Design Contradiction:
Use of energy by moving objectVSDevice complexity

Solution Approach 1:

The patent implements a regenerative heat exchanger that recovers thermal energy from the reactor outlet stream and uses it to preheat the incoming air stream, discarding waste heat and recovering useful energy to reduce overall power consumption while integrating smoothly into the existing system

Inventive Principle:
Principle #34Discarding and recovering

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 system effectively reduces hydrocarbon concentrations, maintaining a safe air supply for extended periods with minimal footprint and power consumption, eliminating the need for additional scrubbers and ensuring continuous operation without poisoning the environment.

Implementation Method 1

a regenerative heat exchanger, heating an output of the regenerative heat exchanger in a heater

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

passing an output of the reactor through the regenerative heat exchanger, thereby transferring heat from the output of the reactor to the portion of air

Methodology Applied
Scientific EffectThermal energy transfer: Conduction (thermal)

Implementation Method 3

a catalyst mixture disposed in a reactor bed between the reactor inlet and the reactor outlet, the heater connecting the first heat exchanger outlet to the reactor inlet, and wherein the reactor is a low temperature reactor configured to convert at least one hydrocarbon to at least one of H2O and CO2

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 4

converts hydrocarbons into H2O and CO2

Methodology Applied
Scientific EffectOxidation: Oxidation

Data Source

PatentUS10799830B2Reduced temperature hydrocarbon burner for enclosed environments
Publication Date: 2020.10.13 HAMILTON SUNDSTRAND CORP
  • US10799830B2 patent drawing

AI summary

A hydrocarbon burner for an enclosed environment includes a heat exchanger having a first heat exchanger inlet connected to an inlet of the hydrocarbon burner and a first heat exchanger outlet connected to a heater, and a second heat exchanger inlet connected to a reactor outlet and a second heat exchanger outlet connected to an outlet of the hydrocarbon burner. A reactor includes a reactor inlet, the reactor outlet, and a catalyst mixture disposed in a reactor bed between the reactor inlet and the reactor outlet. The heater connects the first heat exchanger outlet to the reactor inlet. The reactor is a low temperature reactor configured to convert at least one hydrocarbon to at least one of H2O and CO2.