Multi-stage Wastewater Oxidation Apparatus for Ozone Utilization

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current ozone and hydrogen peroxide oxidation methods for wastewater treatment suffer from low ozone utilization efficiency, uneven mixing, and reduced photocatalytic reaction efficiency, leading to increased treatment costs and inefficiencies.

Innovation Solution

A multi-stage apparatus and process involving a liquid-liquid mixing unit, preheating, gas-liquid mixing, parallel photocatalytic reactors, and an oxidation tower, which ensures optimal mixing and temperature conditions for ozone and hydrogen peroxide, maximizing their utilization and enhancing photocatalytic reactions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If an integrated device combining ozone, ultraviolet radiation and hydrogen peroxide is used for advanced oxidation, then the treatment effect is improved, but the residence time of ozone in the reactor becomes short and the utilization rate of ozone becomes low

Engineering Contradiction:
Improvetreatment effectVSAvoidozone utilization rate
Core Design Contradiction:
ReliabilityVSLoss of energy

Solution Approach 1:

The patent divides the treatment system into separate functional units: a liquid-liquid mixing unit for hydrogen peroxide and wastewater, a preheating unit, a gas-liquid mixing unit for ozone injection, and a photocatalytic reactor. This segmentation allows each component to perform its function optimally, extending ozone residence time and improving utilization rate while maintaining treatment effectiveness.

Inventive Principle:
Principle #1Segmentation

2Reliability

If an integrated device combining ozone, ultraviolet radiation and hydrogen peroxide is used for advanced oxidation, then the treatment effect is improved, but the mixing of hydrogen peroxide, wastewater and ozone becomes uneven

Engineering Contradiction:
Improvetreatment effectVSAvoidmixing uniformity
Core Design Contradiction:
ReliabilityVSStability of the object's composition

Solution Approach 1:

The patent implements separate mixing stages: first a liquid-liquid mixing unit for homogeneous mixing of hydrogen peroxide and wastewater, then a preheating unit, followed by a gas-liquid mixing unit for ozone injection. This segmented approach ensures each mixing stage optimizes for its specific phase combination, achieving uniform overall mixing that enhances reaction efficiency.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent performs preliminary mixing of hydrogen peroxide and wastewater in the liquid-liquid mixing unit before introducing ozone. This preliminary action ensures the liquid phase is homogenized and preheated, creating optimal conditions for subsequent ozone dissolution and reaction, thereby improving overall mixing uniformity.

Inventive Principle:
Principle #10Preliminary action

3Device complexity

If the concentration of ozone in effluent is high, then the treatment process is simpler, but additional energy is needed to decompose ozone and treatment cost increases

Engineering Contradiction:
Improveprocess simplicityVSAvoidenergy consumption
Core Design Contradiction:
Device complexityVSUse of energy by moving object

Solution Approach 1:

The patent segments the treatment process into distinct stages with separate mixing and reaction zones. This allows for controlled ozone injection and extended residence time, ensuring more complete ozone utilization and lower effluent concentration without requiring additional decomposition equipment, thus maintaining process simplicity while reducing energy consumption.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent employs a preheating unit to raise the temperature of the liquid-liquid mixture before ozone injection. This parameter change (temperature increase) accelerates ozone dissolution and decomposition kinetics, improving ozone utilization efficiency and reducing the concentration of ozone in effluent, thereby avoiding additional energy-consuming decomposition steps.

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

The solution significantly increases ozone and hydrogen peroxide utilization rates, reduces treatment costs, and improves wastewater treatment efficiency by optimizing reaction conditions and residence times, achieving ozone utilization efficiencies above 80% and enhanced COD degradation.

Implementation Method 1

the preheating unit is used for preheating a mixed solution of the to-be-treated wastewater and the hydrogen peroxide

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 2

the parallel photocatalytic reactor group is internally provided with several photocatalytic reactors, and an ultraviolet lamp is arranged in the photocatalytic reactor

Methodology Applied
Scientific EffectUltraviolet radiation: Light

Implementation Method 3

the system temperature is in the range when the ozone quickly generates the free radicals

Methodology Applied
Scientific EffectFree radical reaction: Oxidation

Data Source

PatentUS20230002261A1Multi-stage apparatus and process for advanced oxidation treatment of wastewater
Publication Date: 2023.01.05 NANJING UNIV YANCHENG ENVIRONMENTAL PROTECTION TECH & ENG RES INST
  • US20230002261A1 patent drawing
  • US20230002261A1 patent drawing
  • US20230002261A1 patent drawing

AI summary

The present disclosure discloses a multi-stage apparatus and process for advanced oxidation treatment of wastewater, and belongs to the field of wastewater treatment in environmental protection. The apparatus includes a liquid-liquid mixing unit, a preheating unit, a gas-liquid mixing unit, a parallel photocatalytic reactor group and an oxidation tower connected in sequence. According to characteristics of free radical reactions, the parallel photocatalytic reactor group and the oxidation tower in the apparatus are reasonably designed, utilization rates of the ozone and the hydrogen peroxide are increased, and the wastewater treatment cost is reduced.