Honeycomb Reactor Pore Layout for Uniform CO2 Gas Recovery

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Solution Overview

Problem

Existing honeycomb structures for CO2 recovery exhibit uneven gas flow and adsorbent degradation, leading to reduced recovery rates and shorter lifespan, particularly in larger reactors or those with multiple structures.

Innovation Solution

Incorporating communication pore groups at specific positions in the honeycomb structure, with varying pore diameters and locations to enhance gas flow uniformity and reduce adsorbent deterioration.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If a simple honeycomb structure is used, then the device complexity is reduced, but the gas flow uniformity deteriorates causing central region flow dominance and peripheral region flow difficulty

Engineering Contradiction:
Improvehoneycomb structure complexityVSAvoidgas flow uniformity
Core Design Contradiction:
Device complexityVSStability of the object's composition

Solution Approach 1:

The invention segments the honeycomb structure by introducing communication pore groups that divide and redirect gas flow paths. These communication pores create additional flow channels that segment the dominant central flow into distributed paths, enabling gas to reach peripheral regions more effectively and achieving uniform flow distribution without complex structural modifications.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The communication pore group acts as an intermediary element within the honeycomb structure. It mediates between the main gas inlet and the peripheral cells by providing intermediate flow paths through the partition walls, allowing gas to progressively reach peripheral regions and balance the flow distribution across the entire structure.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Quantity of substance

If the honeycomb structure diameter is increased or multiple structures are arranged, then the recovery capacity is improved, but the flow uniformity deteriorates and peripheral region adsorbent performance decreases

Engineering Contradiction:
ImproveCO2 recovery capacityVSAvoidflow uniformity
Core Design Contradiction:
Quantity of substanceVSStability of the object's composition

Solution Approach 1:

By segmenting the flow paths through communication pores distributed across the honeycomb structure, the invention enables large-diameter or multi-structure reactors to maintain uniform flow distribution. The communication pores create multiple parallel flow segments that prevent flow dominance in central regions, ensuring all adsorbent surfaces are effectively utilized even at large scales.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention applies local quality by positioning communication pore groups at specific locations within the honeycomb structure to address local flow distribution issues. This targeted approach modifies flow characteristics in specific regions without requiring complete structural redesign, maintaining overall system capacity while improving peripheral flow uniformity.

Inventive Principle:
Principle #3Local quality

3Productivity

If adsorbent is supported on partition walls, then the CO2 recovery function is achieved, but the adsorbent deteriorates unevenly with central region adsorbent degrading faster, reducing reactor lifespan

Engineering Contradiction:
ImproveCO2 recovery rateVSAvoidreactor lifespan
Core Design Contradiction:
ProductivityVSDuration of action of stationary object

Solution Approach 1:

The communication pore group segments the gas flow to distribute it uniformly across all partition walls, preventing concentration of flow and adsorption stress in central regions. This segmentation ensures even utilization and aging of adsorbent throughout the structure, extending reactor lifespan while maintaining recovery productivity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

By creating uniform flow distribution through communication pores, the invention achieves homogeneous adsorbent utilization across the entire honeycomb structure. All adsorbent regions experience similar flow conditions and degradation rates, preventing the uneven aging that previously occurred with central region dominance and extending overall system durability.

Inventive Principle:
Principle #33Homogeneity

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

Enhances gas flow through peripheral regions, increases recovery rates, and extends the lifespan of the reactor by minimizing adsorbent degradation and reducing heating requirements.

Implementation Method 1

a first communication pore group comprising a plurality of first communication pores provided in the partition walls so as to be positioned on one straight line orthogonal to an extending direction of the cells

Methodology Applied
Scientific EffectGas flow:

Implementation Method 2

an adsorbent capable of adsorbing CO2, desorb the CO2 by changing a temperature, pressure, humidity, and the like, recover it as highly concentrated CO2

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS20250387744A1Reactor and gas recovery device
Publication Date: 2025.12.25 NGK INSULATORS LTD
  • US20250387744A1 patent drawing
  • US20250387744A1 patent drawing
  • US20250387744A1 patent drawing

AI summary

A reactor including at least one honeycomb structure having an outer peripheral wall and partition walls provided on an inner side of the outer peripheral wall, the partition walls defining a plurality of cells through which a process gas containing a capturing target gas can flow, each of the cells extending from an inflow end face to an outflow end face of the honeycomb structure. The honeycomb structure has at least one communication pore group composed of a plurality of communication pores provided at the outer peripheral wall and the partition walls so as to be positioned on one straight line L1 orthogonal to an extending direction of the cells. The communication pore group is located closer to the outflow end face side than a center C1 in the extending direction of the cells.