Beta-Ammonium Tetramolybdate Crystallization via Zonal pH Control

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Solution Overview

Problem

Current methods for preparing β-ammonium tetramolybdate suffer from low yield, poor purity, and inefficient production processes, with existing techniques requiring long cycles, high energy consumption, and difficulty in achieving stable crystallization of the desired β-form.

Innovation Solution

A method involving stepwise pH-adjusting treatment of an ammonium molybdate solution through six zones, with specific pH control at each stage, to facilitate continuous crystallization and improve the purity and crystallinity of β-ammonium tetramolybdate, utilizing a ring-shaped device for efficient processing.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If acid precipitation crystallization is used to prepare ammonium tetramolybdate, then the production process is simple, but the product quality fluctuates greatly due to cocrystallization of various ammonium molybdates and transformation between different crystal forms

Engineering Contradiction:
Improvecrystallization process simplicityVSAvoidproduct quality stability
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The crystallization process is divided into multiple controlled stages with specific pH ranges (pH 1.5-2.5 for nucleation, pH 2.0-3.0 for growth) to prevent cocrystallization and control crystal form transformation, thereby improving product quality stability while maintaining process simplicity

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent controls the pH parameter within specific ranges during different crystallization stages to promote β-crystal form formation and prevent α-crystal form, while controlling ion concentration and temperature to suppress cocrystallization of various ammonium molybdates

Inventive Principle:
Principle #35Parameter changes

2Reliability

If direct drying and sealing at 40°C for 24-48 h is used to transform to β-ammonium tetramolybdate, then the transformation can be achieved, but the production cycle is long and production efficiency is low

Engineering Contradiction:
Improveβ-crystal form transformationVSAvoidproduction efficiency
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The patent performs preliminary pH adjustment to 1.5-2.5 before crystallization to pre-condition the solution for β-crystal form formation, eliminating the need for subsequent long-term thermal transformation and significantly shortening the production cycle

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent uses pH parameter control (pH 1.5-2.5) during crystallization to directly promote β-crystal form formation, replacing the traditional thermal transformation method (40°C for 24-48 h) with a chemical parameter control method that achieves the same result much faster

Inventive Principle:
Principle #35Parameter changes

3Shape

If ultrasonic field is introduced during crystallization to control crystal morphology, then β-ammonium tetramolybdate can be obtained, but the purity needs to be improved and fine control of crystal form transformation is difficult

Engineering Contradiction:
Improvecrystal morphology controlVSAvoidcrystal form transformation control precision
Core Design Contradiction:
ShapeVSManufacturing precision

Solution Approach 1:

The patent uses pH parameter control (pH 1.5-2.5) during crystallization to directly promote β-crystal form formation, providing fine control over crystal form transformation and improving product purity to 95% or higher, surpassing the ultrasonic method

Inventive Principle:
Principle #35Parameter changes

4Speed

If rapid crystallization reaction occurs during acid precipitation, then the process is fast, but cocrystallization of various ammonium molybdates occurs leading to variable polymerization morphology

Engineering Contradiction:
Improvecrystallization reaction speedVSAvoidpolymerization morphology uniformity
Core Design Contradiction:
SpeedVSManufacturing precision

Solution Approach 1:

The patent segments the crystallization process into nucleation (pH 1.5-2.5) and growth (pH 2.0-3.0) stages with controlled pH adjustment rates, preventing rapid uncontrolled crystallization and cocrystallization while maintaining efficient production speed

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent dynamically adjusts the pH parameter during crystallization, starting at pH 1.5-2.5 for nucleation and then adjusting to pH 2.0-3.0 for growth, allowing the process to adapt to different crystallization stages and maintain uniform polymerization morphology

Inventive Principle:
Principle #15Dynamics

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 enables stable and continuous production of high-purity β-ammonium tetramolybdate with uniform morphology, reducing impurity phases and enhancing crystallinity, while minimizing energy consumption and equipment size, thus improving the quality and efficiency of the process.

Implementation Method 1

A method for crystallization of β-ammonium tetramolybdate includes: stepwise pH-adjusting treatment of an ammonium molybdate solution through zoning

Methodology Applied
Scientific EffectCrystallization: Crystallisation

Implementation Method 2

pH1 of a resultant solution in the first zone is adjusted to be 7.0-6.0; pH2 of a resultant solution in the second zone is adjusted to be less than 6 and greater than or equal to 4

Methodology Applied
Scientific EffectpH-adjusting treatment:

Data Source

PatentUS11701600B2Method for crystallization of β-ammonium tetramolybdate
Publication Date: 2023.07.18 CENT SOUTH UNIV
  • US11701600B2 patent drawing
  • US11701600B2 patent drawing
  • US11701600B2 patent drawing

AI summary

A method for crystallization of β-ammonium tetramolybdate includes: performing a stepwise pH-adjusting treatment of an ammonium molybdate solution via zoning to obtain the β-ammonium tetramolybdate. When feeding the ammonium molybdate solution into a reaction system from a first zone and then into second to sixth zones successively, pH1 of a resultant solution in the first zone is 7.0-6.0; pH2 of a resultant solution in the second zone is less than 6 and greater than or equal to 4; pH3 of a resultant solution in the third zone is less than 4 and greater than or equal to 2.5; pH4 of a crystallized slurry in the fourth zone is less than 2.5 and greater than or equal to 1; pH5 of a crystallized slurry in the fifth zone is 2.5-4.0; and pH6 of a crystallized slurry in the sixth zone is less than 2.5 and greater than or equal to 2.0.