Lead Electrolytic Refining Sulfamate Bath Residue Control

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Solution Overview

Problem

Conventional electrolytic refining of lead in sulfamate baths faces issues with the formation of a white residue and decreased lead concentration due to sulfamic acid decomposition, leading to frequent interruptions and poor electrodeposition conditions.

Innovation Solution

Controlling the decomposition rate of sulfamic acid to 0.06%/day or less, adjusting the sulfamic acid concentration to 20-60 g/L higher than lead concentration, and maintaining the electrolytic solution temperature between 15-30°C to suppress residue production and maintain stable lead concentration.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If electrolytic refining is performed in a sulfamate bath, then lead can be recovered, but sulfamic acid decomposes to form white residue and decrease lead concentration

Engineering Contradiction:
Improveelectrolytic refining process stabilityVSAvoidwhite residue formation
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The patent applies parameter changes by controlling the decomposition rate of sulfamic acid through adjustment of electrolysis conditions (current density, temperature, pH) to maintain the decomposition rate at 0.06%/day or less. This prevents excessive white residue formation while maintaining effective lead recovery.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements feedback control by monitoring the decomposition rate of sulfamic acid and adjusting electrolysis parameters accordingly. When the decomposition rate approaches 0.06%/day, the system automatically adjusts conditions to maintain optimal levels, preventing harmful residue accumulation.

Inventive Principle:
Principle #23Feedback

2Productivity

If electrolysis is performed at high current density, then lead recovery efficiency increases, but sulfamic acid decomposition accelerates

Engineering Contradiction:
Improvelead recovery efficiencyVSAvoidsulfamic acid decomposition
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent optimizes the current density parameter to achieve the desired balance between lead recovery efficiency and sulfamic acid stability. By carefully selecting and adjusting current density values, the system maximizes productivity while keeping the decomposition rate at 0.06%/day or less.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs dynamic adjustment of electrolysis parameters during the refining process. The system continuously monitors conditions and adjusts current density and other parameters in real-time to maintain optimal performance while preventing excessive sulfamic acid decomposition.

Inventive Principle:
Principle #15Dynamics

3Manufacturing precision

If sulfamic acid concentration is increased, then electrodeposition conditions improve, but decomposition rate increases

Engineering Contradiction:
Improveelectrodeposition qualityVSAvoidsulfamic acid decomposition rate
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The patent optimizes the sulfamic acid concentration parameter to achieve optimal electrodeposition quality while controlling the decomposition rate. By carefully adjusting concentration levels and maintaining the decomposition rate at 0.06%/day or less, the system achieves high manufacturing precision without excessive material loss.

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 approach effectively reduces the formation of white residue, stabilizes lead concentration, and improves electrodeposition conditions, decreasing the frequency of residue removal and sulfamic acid replenishment, while ensuring smooth and high-purity lead recovery.

Implementation Method 1

electrolytic refining of lead in a sulfamate bath

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 2

the metal is cast into an anode and then electrolytically refined

Methodology Applied
Scientific EffectElectrodeposition: Electrodeposition

Implementation Method 3

sulfamic acid during the electrolytic refining of lead in the sulfamate bath decomposes by the following reaction

Methodology Applied
Scientific EffectChemical decomposition: Decomposition (biological)

Implementation Method 4

the white residue is deposited as lead sulfate

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Data Source

PatentUS10106904B2Method for electrolytically refining lead in sulfamate bath
Publication Date: 2018.10.23 JX NIPPON MINING & METALS CORP
  • US10106904B2 patent drawing
  • US10106904B2 patent drawing

AI summary

In the electrolytic refining of lead in a sulfamate bath, the production of a white residue is suppressed, and a decrease in the lead concentration in the electrolytic solution is suppressed. A method for electrolytically refining lead in a sulfamate bath, comprising performing electrolytic refining at a decomposition rate of sulfamic acid controlled at 0.06%/day or less.