Porous Structure with Porosity Gradient for Heat Transfer

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Solution Overview

Problem

Existing reactor designs, such as packed-bed reactors, face challenges with hot-spot formation, catalyst deactivation, and inefficient heat and mass transfer, which limit the efficiency of exothermic and endothermic processes, and heat exchangers struggle to maximize heat transfer per unit volume.

Innovation Solution

A device with a porous structure having a porosity gradient, where the porosity decreases from the center to the periphery, is used to enhance conductive heat transfer between the fluid and the vessel wall, minimizing flow resistance and promoting uniform temperature profiles.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If a packed-bed reactor with conventional catalytic materials is used, then catalytic reactions can be performed, but hot spots form and heat transfer is limited

Engineering Contradiction:
Improvetemperature uniformityVSAvoidheat transfer limitation
Core Design Contradiction:
TemperatureVSLoss of energy

Solution Approach 1:

The patent applies local quality by creating a porous structure with spatially varying porosity - higher porosity in the center region and lower porosity at the periphery. This non-uniform porosity distribution optimizes heat transfer locally: the lower porosity at the periphery enhances thermal contact with the reactor wall for efficient heat removal, while the higher porosity in the center maintains adequate flow channels and catalytic activity zones.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent implements parameter changes by systematically varying the porosity parameter throughout the porous structure. The porosity transitions from approximately 40-50% at the periphery to 60-70% in the center, creating a gradient that balances heat conduction pathways with fluid flow requirements. This parameter optimization directly addresses the heat transfer limitation while maintaining reaction efficiency.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If porosity is increased to improve mass transfer, then flow resistance increases and pressure drop increases

Engineering Contradiction:
Improvemass transfer efficiencyVSAvoidpressure drop
Core Design Contradiction:
ProductivityVSStress or pressure

Solution Approach 1:

The patent applies local quality by assigning different porosity values to different spatial regions. The central region has higher porosity (60-70%) to facilitate mass transfer and reduce flow resistance where catalytic reactions occur, while the peripheral region has lower porosity (40-50%) to maintain structural integrity and reduce pressure drop at the boundaries. This localized optimization resolves the contradiction between mass transfer efficiency and pressure drop.

Inventive Principle:
Principle #3Local quality

3Ease of manufacture

If homogeneous porosity is used, then manufacturing is simpler, but heat transfer between center and periphery is inefficient

Engineering Contradiction:
Improvemanufacturing simplicityVSAvoidheat transfer efficiency
Core Design Contradiction:
Ease of manufactureVSTemperature

Solution Approach 1:

The patent resolves this contradiction by implementing local quality through a controlled porosity gradient. The porous structure is manufactured with deliberately non-uniform porosity distribution - achieved through techniques like 3D printing or controlled foaming - where the porosity varies systematically from center to periphery. This controlled complexity enables superior heat transfer from the reaction zone at the center to the cooling surfaces at the periphery, justifying the increased manufacturing sophistication.

Inventive Principle:
Principle #3Local quality

4Stress or pressure

If peripheral porosity is increased to reduce pressure drop, then hot spot formation increases

Engineering Contradiction:
Improvepressure dropVSAvoidhot spot formation
Core Design Contradiction:
Stress or pressureVSTemperature

Solution Approach 1:

The patent applies inversion by reversing the conventional approach: instead of increasing porosity at the periphery to reduce pressure drop (which would worsen heat transfer), it decreases peripheral porosity to enhance heat transfer. The inverted porosity profile - low at periphery, high at center - simultaneously achieves acceptable pressure drop through the high-flow central region while maximizing heat removal efficiency at the thermally active peripheral zones adjacent to reactor walls.

Inventive Principle:
Principle #13The other way round (Inversion)

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 porosity gradient structure improves heat transfer efficiency, reduces catalyst deactivation, and maintains high reaction conversion rates while minimizing pressure drop, effectively addressing the limitations of traditional reactor designs.

Implementation Method 1

The porous structure is advantageously (thermally) coupled to the wall. This advantageously provides for heat conduction between the porous structure and the wall.

Methodology Applied
Scientific EffectThermal conduction: Conduction (thermal)

Implementation Method 2

The porosity gradient structure improves heat transfer efficiency, reduces catalyst deactivation, and maintains high reaction conversion rates while minimizing pressure drop

Methodology Applied
Scientific EffectDarcy's law:

Data Source

PatentUS10695743B2Devices for through-flow of fluids comprising graded porous structures
Publication Date: 2020.06.30 VLAAMSE INSTELLING VOOR TECHNOLOGISCH ONDERZOEK NV (VITO)
  • US10695743B2 patent drawing
  • US10695743B2 patent drawing
  • US10695743B2 patent drawing

AI summary

A device for the through-flow of a fluid may include a fluid inlet and a fluid outlet. A porous structure with interconnected pores is arranged between the fluid inlet and the fluid outlet, and the fluid inlet and the fluid outlet define an overall flow direction. The porous structure is coupled to a wall to provide for heat conduction between the porous structure and the wall. The porous structure has a porosity gradient along a first direction, which is cross to the overall flow direction. The porosity gradient develops along the first direction between a first porosity at a first location proximal to the wall and a second porosity larger than the first porosity at a second location remote from the wall. The difference between the second porosity and the first porosity may be at least 4%.