Power Battery Vacuum Cracking With Staged Pyrolysis

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Solution Overview

Problem

Traditional high-temperature treatment methods for recycling power batteries face issues such as dioxin production in aerobic pyrolysis, tar and coke generation in anaerobic cracking, leading to secondary pollution, acid and alkali consumption, and difficulties in wastewater treatment, which hinder effective recycling and resource recovery.

Innovation Solution

A vacuum cracking method that combines battery cracking and pyrolysis, where waste power batteries are preheated, cracked under an inert atmosphere, and then pyrolyzed in an aerobic environment, allowing for the recovery of heat and avoidance of secondary pollution, with cracked gas used as fuel for pyrolysis, and the apparatus includes sequential sealing units for material and gas isolation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If traditional aerobic pyrolysis method is used, then battery treatment is achieved, but dioxin is produced causing secondary pollution

Engineering Contradiction:
Improvebattery treatment processVSAvoiddioxin production
Core Design Contradiction:
Ease of manufactureVSObject-generated harmful factors

Solution Approach 1:

The treatment process is divided into two separate stages: first anaerobic cracking to decompose organic substances without producing dioxin, then aerobic pyrolysis to burn remaining materials. This segmentation prevents the formation of harmful dioxins by avoiding direct aerobic decomposition of chlorinated compounds.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Anaerobic cracking is performed as a preliminary step before aerobic pyrolysis. This preliminary action removes organic substances that would otherwise react with oxygen during pyrolysis to form dioxins, thereby preventing secondary pollution.

Inventive Principle:
Principle #10Preliminary action

2Ease of manufacture

If traditional anaerobic cracking method is used, then battery cracking is achieved, but tar and cokes are produced affecting subsequent processes

Engineering Contradiction:
Improvebattery cracking processVSAvoidtar and cokes production
Core Design Contradiction:
Ease of manufactureVSObject-generated harmful factors

Solution Approach 1:

The process separates cracking and pyrolysis into distinct stages with different atmospheric conditions. Anaerobic cracking breaks down organic materials into gas, liquid, and solid products, followed by aerobic pyrolysis that combusts tar and cokes, converting them into CO2 and H2O.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The atmospheric parameter (oxygen presence) is changed between stages: anaerobic conditions during cracking to preserve valuable gases, then aerobic conditions during pyrolysis to eliminate tar and cokes. This parameter change resolves the contradiction between cracking efficiency and byproduct formation.

Inventive Principle:
Principle #35Parameter changes

3Ease of manufacture

If traditional high-temperature treatment is used, then battery decomposition is achieved, but heat cannot be recovered making temperature control difficult

Engineering Contradiction:
Improvebattery decompositionVSAvoidheat recovery
Core Design Contradiction:
Ease of manufactureVSLoss of energy

Solution Approach 1:

The heat generated during aerobic pyrolysis, which would normally be wasted energy, is captured and used to preheat the feed material entering the cracking unit. This converts the harmful heat loss into a beneficial preheating function, improving energy efficiency and simplifying temperature control.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Solution Approach 2:

The pyrolysis unit and cracking unit are thermally coupled through heat exchange. The high-temperature aerobic pyrolysis process is merged with the lower-temperature anaerobic cracking process via heat recovery, allowing the exothermic pyrolysis to supply heat for the endothermic cracking operation.

Inventive Principle:
Principle #5Merging (Combining)

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 method effectively decomposes tar and cokes, reduces acid and alkali consumption, simplifies wastewater treatment, and increases the yield of valuable metal recoveries, while avoiding dioxin production and enhancing resource utilization by using cracked gas as fuel.

Implementation Method 1

heated and cracked under an inert atmosphere or vacuum to obtain cracked gas, solid cracked products and non-crackable products

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Implementation Method 2

the crushed material is transported to a cracking unit through a first sealing unit for preheating, then heated and cracked

Methodology Applied
Scientific EffectThermal decomposition: Decomposition (biological)

Implementation Method 3

the solid cracked products and non-crackable products are transported to a pyrolysis unit through a second sealing unit for pyrolysis in an aerobic atmosphere to obtain pyrolysis gas and non-pyrolysis products

Methodology Applied
Scientific EffectAerobic oxidation: Oxidation

Implementation Method 4

pyrolysis in an aerobic atmosphere to obtain pyrolysis gas mainly composed of carbon dioxide and water vapor

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 5

the cracked gas is used as a fuel for pyrolysis in the step (3)

Methodology Applied
Scientific EffectCombustion: Combustion

Data Source

PatentUS11850640B2Vacuum cracking method and cracking apparatus for power battery
Publication Date: 2023.12.26 GUANGDONG BRUNP RECYCLING TECH CO LTD
  • US11850640B2 patent drawing
  • US11850640B2 patent drawing
  • US11850640B2 patent drawing

AI summary

A vacuum cracking method and a cracking apparatus for a power battery are disclosed. The vacuum cracking method includes the following steps that: waste power batteries are fed from a feed hopper and then enter a rolling unit for rolling treatment to obtain a crushed material; the crushed material is transported to a cracking unit for preheating, then heated and cracked under an inert atmosphere or vacuum to obtain cracked gas, solid cracked products and non-crackable products; and the solid cracked products and the non-crackable products are transported to a pyrolysis unit for pyrolysis at an aerobic atmosphere to obtain pyrolysis gas and non-pyrolysis products.