Peripheral Heat Transfer Tubes for Reactor Temperature Uniformity

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Solution Overview

Problem

In heat exchange reactors, achieving uniform temperature distribution across the radial direction is challenging due to catalyst-free regions near the external reactor wall, leading to uneven flow and temperature distribution, especially in steam reforming processes.

Innovation Solution

Incorporating peripheral heat transfer tubes in the outer periphery of the catalyst bed, which are elongated members or tubes that fit between the outermost heat transfer tubes and the external reactor wall, to maintain a consistent catalyst area to heat transfer area ratio, thereby ensuring uniform temperature distribution.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Power

If heat transfer tubes are arranged in parallel along the major axis of the reactor, then heat exchange efficiency is improved, but uniform temperature distribution across the radial direction deteriorates due to catalyst-free regions near the external reactor wall

Engineering Contradiction:
Improveheat exchange efficiencyVSAvoidtemperature distribution uniformity
Core Design Contradiction:
PowerVSTemperature

Solution Approach 1:

The patent applies local quality by introducing peripheral heat transfer tubes specifically in the outer periphery region where catalyst-free zones create temperature non-uniformity. These peripheral tubes provide localized heat exchange capacity exactly where needed, compensating for the deficiency in the outer regions without affecting the inner regions unnecessarily. This resolves the contradiction by making the heat exchange system non-uniform in a controlled way to achieve overall temperature uniformity.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The heat transfer tube arrangement is segmented into two distinct zones: central heat transfer tubes running along the major axis for primary heat exchange, and peripheral heat transfer tubes positioned in the outer periphery for temperature uniformity. This segmentation allows each zone to perform its specific function optimally, with peripheral tubes addressing the temperature distribution issue in the outer regions.

Inventive Principle:
Principle #1Segmentation

2Device complexity

If catalyst bed is disposed only outside the heat transfer tubes, then reactor simplicity is improved, but temperature control precision deteriorates in the outer periphery regions

Engineering Contradiction:
Improvereactor structure simplicityVSAvoidtemperature control precision
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The catalyst bed configuration is modified locally in the outer periphery by introducing catalyst-containing porous plugs at the ends of peripheral heat transfer tubes. This local modification ensures that catalyst is present exactly where heat transfer occurs in the peripheral regions, enabling precise temperature control in these previously problematic zones without requiring a complete redesign of the catalyst bed structure.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The porous plugs act as intermediaries between the heat transfer tubes and the catalyst bed. They provide a transition zone that allows heat transfer from the peripheral tubes to the catalyst bed while maintaining structural integrity and ensuring proper catalyst distribution in the outer periphery regions.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Temperature

If peripheral heat transfer tubes are added to maintain consistent catalyst area to heat transfer area ratio, then temperature distribution uniformity is improved, but device complexity increases

Engineering Contradiction:
Improvetemperature distribution uniformityVSAvoidheat transfer tube arrangement complexity
Core Design Contradiction:
TemperatureVSDevice complexity

Solution Approach 1:

The peripheral heat transfer tubes serve multiple functions: they provide heat exchange in the outer periphery regions, maintain consistent catalyst area to heat transfer area ratio, and ensure uniform temperature distribution. By making these tubes multi-functional, the patent reduces the need for additional separate components to address each issue, thereby limiting the increase in device complexity.

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

Solution Approach 2:

The patent merges the functions of heat transfer and temperature uniformity maintenance into a single integrated system of peripheral heat transfer tubes. Rather than adding separate components to address temperature uniformity, the heat transfer tube arrangement itself is designed to simultaneously achieve both heat exchange and temperature distribution objectives.

Inventive Principle:
Principle #5Merging (Combining)

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 configuration achieves more even process conditions and higher gas conversion rates by maintaining consistent temperatures across the reactor, minimizing gas channeling, and optimizing the catalyst area and heat transfer area near the external reactor wall.

Implementation Method 1

temperature control is achieved by indirect heat exchanging between a process stream passing through the catalyst bed and said heat-exchanging medium

Methodology Applied
Scientific EffectIndirect heat exchange: Heat Exchanger

Implementation Method 2

The solid catalyst inside the tubes provides a catalyst bed in which the required chemical reactions take place

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS7776285B2Reactor and process for carrying out endothermic or exothermic catalytic reaction
Publication Date: 2010.08.17 HALDOR TOPSOE AS
  • US7776285B2 patent drawing
  • US7776285B2 patent drawing
  • US7776285B2 patent drawing

AI summary

A heat exchange reactor for carrying out endothermic or exothermic reactions comprising: a housing defining an external reactor wall (1), a plurality of heat transfer tubes (2) arranged within said housing for the supply or removal of heat in catalyst beds (3, 3′) disposed at least outside (3) said heat transfer tubes (2), and built-in elements (4) disposed in the outer periphery of said catalyst bed (3).