Reformer Tubes with Enlarged Outer Surface Area

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Solution Overview

Problem

Current reforming reactors face limitations in achieving high reformer efficiency and methane conversion rates while minimizing the number of tubes, which can lead to increased pressure drop and reduced tube lifetime due to temperature peaks and heat transfer issues.

Innovation Solution

The use of reformer tubes with structured catalysts and elements that enlarge the outer surface area, such as fins, to enhance heat transfer and reduce the number of tubes required, maintaining high efficiency and methane conversion rates while minimizing temperature peaks and pressure drop.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Volume of moving object

If the number of reformer tubes is reduced to achieve a more compact reactor design, then the reactor volume and capital costs are reduced, but the pressure drop increases and tube lifetime decreases due to temperature peaks and heat transfer issues

Engineering Contradiction:
Improvereactor volumeVSAvoidtube lifetime
Core Design Contradiction:
Volume of moving objectVSReliability

Solution Approach 1:

The patent applies this principle by adding external fins to the reformer tubes, which increases the outer surface area available for heat transfer. This dimensional extension allows heat to be transferred more efficiently from the combustion zone to the tube interior, enabling the use of fewer tubes while maintaining adequate heat supply and avoiding temperature peaks that would reduce tube lifetime.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Volume of moving object

If the number of reformer tubes is reduced to achieve a more compact reactor design, then the reactor volume and capital costs are reduced, but the heat transfer efficiency decreases

Engineering Contradiction:
Improvereactor volumeVSAvoidheat transfer efficiency
Core Design Contradiction:
Volume of moving objectVSUse of energy by moving object

Solution Approach 1:

The patent applies this principle by adding external fins to the reformer tubes, which increases the outer surface area available for heat transfer. This dimensional extension allows heat to be transferred more efficiently from the combustion zone to the tube interior, enabling the use of fewer tubes while maintaining adequate heat supply and avoiding temperature peaks that would reduce tube lifetime.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

3Productivity

If elements for enlarging outer surface area (such as fins) are added to reformer tubes, then heat transfer is enhanced and fewer tubes are needed, but the device complexity increases

Engineering Contradiction:
Improvereformer efficiencyVSAvoidtube structure complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent applies this principle by adding external fins to the reformer tubes, which increases the outer surface area available for heat transfer. This dimensional extension allows heat to be transferred more efficiently from the combustion zone to the tube interior, enabling the use of fewer tubes while maintaining adequate heat supply and avoiding temperature peaks that would reduce tube lifetime.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

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 combination allows for a more compact and efficient reforming reactor with improved heat transfer, maintaining high reformer efficiency and methane conversion rates, and reducing the number of tubes, thus lowering capital and maintenance costs.

Implementation Method 1

elements for enlarging the outer surface area of a reformer tube... to enhance heat transfer

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

The conversion reaction needs to be conducted at high temperatures, for example temperatures of at least 700° C. The heat necessary for the endothermic conversion of the process gas

Methodology Applied
Scientific EffectEndothermic reaction: Endothermic Reaction

Implementation Method 3

the reformer tubes contain in their interior a catalyst for the conversion of said hydrocarbons and said at least one further fluid to synthesis gas

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS20230415118A1Reforming reactor comprising reformer tubes with enlarged outer surface area and structured catalyst
Publication Date: 2023.12.28 LAIR LIGUIDE SOCIÉTÉ ANONYME POUR IETUDE & IEXPLOITATION DES PROCÉDÉS GEORGES CLAUDE
  • US20230415118A1 patent drawing
  • US20230415118A1 patent drawing
  • US20230415118A1 patent drawing

AI summary

A reforming reactor for an endothermic process including a plurality of reformer tubes allowing a flow of hydrocarbons and at least one further fluid inside the tubes is provided. Wherein the reformer tubes contain in their interior a catalyst for the conversion of the hydrocarbons and the at least one further fluid to synthesis gas, and a means for heating the reformer tubes. Wherein at least a portion of the plurality of reformer tubes is provided with one or more elements for enlarging the outer surface area of a reformer tube, and the catalyst includes a structured catalyst. Also an endothermic process for the production of synthesis gas, including allowing a flow of hydrocarbons and at least one further fluid inside a plurality of reformer tubes, and heating the plurality of reformer tubes to convert said hydrocarbons and the at least one further fluid to synthesis gas.