Porous-Layer Rebalancing Reactor for Redox Flow Battery Electrolytes

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Solution Overview

Problem

Packed bed-type rebalancing reactors for redox flow battery systems exhibit unfavorable reaction kinetics due to two-phase flow, leading to higher mass transport losses and the need for excessive catalyst usage, which is costly and inefficient.

Innovation Solution

A rebalancing reactor design that includes a porous layer separating two sides, one for hydrogen gas flow and the other for electrolyte flow, where the hydrogen gas and electrolyte are fluidly contacted at the porous layer surface, with a pressure drop across the electrolyte side being less than across the porous layer, enhancing efficiency and cost-effectiveness.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If packed bed-type rebalancing reactor is used, then catalyst utilization is improved, but mass transport losses increase and reaction kinetics become unfavorable

Engineering Contradiction:
Improvecatalyst utilizationVSAvoidmass transport losses
Core Design Contradiction:
Quantity of substanceVSLoss of energy

Solution Approach 1:

The patent employs a porous layer as the catalyst support structure instead of traditional packed bed configuration. This porous structure provides high surface area for catalyst deposition while maintaining open channels for efficient fluid transport, thereby achieving both high catalyst utilization and low mass transport losses simultaneously

Inventive Principle:
Principle #31Porous materials

Solution Approach 2:

The patent optimizes the two-phase flow dynamics by designing specific flow channels and pressure distributions. By controlling hydraulic conditions and gas-liquid flow patterns through the porous medium, the system achieves favorable reaction kinetics while maintaining efficient mass transport

Inventive Principle:
Principle #29Pneumatics and hydraulics

2Productivity

If rebalancing reactor is oversized to compensate for mass transport limitations, then reaction completeness is improved, but system cost and complexity increase

Engineering Contradiction:
Improverebalancing completenessVSAvoidreactor size
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent changes key operating parameters including pressure distribution (maintaining lower pressure on electrolyte side), flow rates, and temperature to optimize reaction efficiency. These parameter optimizations enable compact reactor design while achieving complete rebalancing, avoiding the need for oversized equipment

Inventive Principle:
Principle #35Parameter changes

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 design improves the rebalancing of electrolyte charges in redox flow battery systems with increased efficiency and reduced costs compared to conventional packed bed and other designs, while maintaining a simpler system architecture.

Implementation Method 1

a porous layer separating and fluidly coupled to the first side and the second side. The hydrogen gas and the electrolyte are fluidly contacted at a surface of the porous layer

Methodology Applied
Scientific EffectCapillary action: Capillary Action

Implementation Method 2

a pressure drop across the second side may be less than a pressure drop across the porous layer

Methodology Applied
Scientific EffectPressure gradient: Pressure Gradient

Data Source

PatentUS20240030471A1Methods and systems for rebalancing electrolytes for a redox flow battery system
Publication Date: 2024.01.25 ESS TECH INC
  • US20240030471A1 patent drawing
  • US20240030471A1 patent drawing
  • US20240030471A1 patent drawing

AI summary

A rebalancing reactor for a redox flow battery system may include a first side through which hydrogen gas is flowed, a second side through which electrolyte from the redox flow battery system is flowed, and a porous layer separating and fluidly coupled to the first side and the second side, wherein, the hydrogen gas and the electrolyte are fluidly contacted at a surface of the porous layer, and a pressure drop across the second side is less than a pressure drop across the porous layer. In this way, rebalancing of electrolyte charges in a redox flow battery system may be performed with increased efficiency and cost effectiveness as compared to conventional rebalancing reactors.