Microreactor Auto-Oxidation for Hydrogen Peroxide Production

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Solution Overview

Problem

Conventional hydrogen peroxide production processes face challenges such as large reactor volumes, long liquid residence times, high equipment costs, fire risks, and unwanted byproduct formation, which lead to inefficiencies and increased operating costs.

Innovation Solution

The use of a microreactor for the oxidation step in the auto-oxidation process, which provides a high surface-to-volume ratio, enhancing mass and heat transfer rates, and allowing for optimized operating conditions, reduced byproduct formation, and improved oxygen utilization.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional large-volume reactors are used for oxidation, then sufficient reaction capacity is achieved, but reactor volume and liquid residence time increase leading to higher equipment costs and fire risks

Engineering Contradiction:
Improvereaction capacityVSAvoidreactor volume
Core Design Contradiction:
ProductivityVSVolume of stationary object

Solution Approach 1:

The invention divides the oxidation reaction into multiple stages using a multi-stage packed bed reactor system. Each stage contains packing material that facilitates mass transfer and reaction, allowing the overall reaction capacity to be achieved through sequential stages rather than a single large-volume reactor. This segmentation reduces the volume required for each stage while maintaining total productivity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention employs packed bed reactors with porous packing material to facilitate mass transfer between gas and liquid phases. The porous structure increases the effective surface area for reaction within a compact volume, enabling high reaction capacity without requiring large reactor volumes. The packing material provides numerous pathways for oxygen transfer to the liquid stream, enhancing reaction efficiency per unit volume.

Inventive Principle:
Principle #31Porous materials

2Productivity

If conventional large-volume reactors are used for oxidation, then sufficient reaction capacity is achieved, but liquid residence time increases leading to unwanted byproduct formation

Engineering Contradiction:
Improvereaction capacityVSAvoidliquid residence time
Core Design Contradiction:
ProductivityVSLoss of time

Solution Approach 1:

The oxidation process is divided into multiple sequential stages, each with its own packed bed reactor. This segmentation allows the liquid stream to pass through a series of compact reaction zones rather than a single large reactor, reducing the total residence time while maintaining sufficient reaction capacity. Each stage processes a portion of the liquid, preventing excessive accumulation time that would lead to byproduct formation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention maintains continuous flow through the multi-stage packed bed reactor system, ensuring that the liquid stream is constantly refreshed and moved through reaction zones. This continuous action prevents prolonged residence times that would cause unwanted side reactions. The system operates at steady state with continuous oxygen transfer and product formation, eliminating the delays and stagnation associated with batch processing in large volumes.

Inventive Principle:
Principle #20Continuity of useful action

3Productivity

If conventional oxidation processes are used, then hydrogen peroxide production is achieved, but oxygen utilization is incomplete leading to high equipment costs and operating expenses

Engineering Contradiction:
Improvehydrogen peroxide productionVSAvoidoxygen utilization
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The packed bed reactors utilize porous packing material that maximizes the gas-liquid contact surface area. This porous structure ensures complete oxygen dissolution and utilization by providing numerous pathways for oxygen transfer from the gas phase to the liquid phase. The high surface area to volume ratio of the packing material ensures that oxygen is fully exploited in the oxidation reaction, minimizing unreacted oxygen in the outlet stream.

Inventive Principle:
Principle #31Porous materials

Solution Approach 2:

The multi-stage packed bed reactor system incorporates feedback mechanisms where the outlet stream from each stage is fed to the next stage, allowing progressive oxidation. The system monitors and adjusts operating conditions to ensure optimal oxygen utilization at each stage. Any unreacted oxygen or intermediate products are carried forward to subsequent stages for further reaction, maximizing overall oxygen efficiency.

Inventive Principle:
Principle #23Feedback

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 approach results in higher volumetric reactor productivity, minimized byproduct formation, reduced hydrogen peroxide loss, and increased energy efficiency, while also reducing the risk of fires and equipment costs.

Implementation Method 1

oxidizing the hydrogenated working compound in an oxidation microreactor to produce hydrogen peroxide

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 2

provides a high surface-to-volume ratio, enhancing mass and heat transfer rates

Methodology Applied
Scientific EffectMass transfer: Diffusion

Implementation Method 3

provides a high surface-to-volume ratio, enhancing mass and heat transfer rates

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Data Source

PatentUS7416718B2Auto-oxidation production of hydrogen peroxide via oxidation in a microreactor
Publication Date: 2008.08.26 PEROXYCHEM LLC

AI summary

Hydrogen peroxide is prepared by an auto-oxidation method via oxidation in a microreactor. A working solution containing a reactive carrier compound is hydrogenated with hydrogen in a first step and is subsequently oxidized in a microreactor to produce hydrogen peroxide.