Soda Ash Production via Bicarbonate Concentration Control

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Conventional processes for producing dense soda ash, sodium bicarbonate, and sodium silicate from bicarbonate-containing solutions are wasteful and inefficient, requiring significant caustic consumption and resulting in high production costs and waste generation.

Innovation Solution

An integrated process that optimizes the production of dense soda ash, sodium bicarbonate, and sodium silicate by minimizing caustic consumption, increasing process flexibility, and recovering waste as final products, involving the use of deca/sesqui crystallization, calcination, and recrystallization to produce diverse alkali products with improved particle size and purity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional monohydrate method is used to produce dense soda ash, then production can be achieved, but significant amount of caustic is consumed and impurities accumulate requiring regular purging

Engineering Contradiction:
Improvedense soda ash productionVSAvoidcaustic consumption and impurity accumulation
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent changes the operating parameters of the crystallization process by controlling bicarbonate concentration to remain below the invariant point throughout the process. This parameter change prevents the formation of sesquicarbonate and enables continuous monohydrate production without caustic consumption and without impurity accumulation, eliminating the need for purging.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements continuous operation of the crystallization process by maintaining stable conditions that prevent impurity accumulation. The continuous crystallization of monohydrate without periodic purging maintains steady-state operation, improving productivity while eliminating waste associated with batch purging operations.

Inventive Principle:
Principle #20Continuity of useful action

2Manufacturing precision

If bicarbonate content is completely neutralized to obtain monohydrate crystals, then product quality is achieved, but significant amount of caustic is consumed

Engineering Contradiction:
Improvemonohydrate crystal purityVSAvoidcaustic consumption
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The patent changes the chemical parameter by controlling bicarbonate concentration to stay below the invariant point rather than complete neutralization. This parameter change achieves the desired monohydrate crystal formation while minimizing caustic consumption, as only enough caustic is added to maintain the concentration below the invariant point rather than complete neutralization.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent applies partial neutralization rather than complete neutralization. By adding only the amount of caustic needed to bring bicarbonate concentration below the invariant point (partial action), the process achieves sufficient monohydrate crystal formation without the excessive caustic consumption required for complete neutralization.

Inventive Principle:
Principle #16Partial or excessive action

3Manufacturing precision

If purge rate is increased to maintain product quality, then impurity concentration is controlled, but product loss increases

Engineering Contradiction:
Improveproduct qualityVSAvoidproduct loss with purge
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The patent eliminates periodic purging operations by implementing continuous operation at controlled bicarbonate concentrations. This continuous stable operation prevents impurity accumulation that would otherwise require purging, thereby eliminating product loss associated with purge operations while maintaining consistent product quality.

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

The patent changes the operational parameter by controlling bicarbonate concentration to remain below the invariant point. This parameter change fundamentally alters the process behavior to prevent impurity accumulation, eliminating the need for quality-compromising purges and associated product losses.

Inventive Principle:
Principle #35Parameter changes

4Loss of substance

If decahydrate process is used to handle purge stream, then some product recovery is achieved, but complex neutralization and additional equipment are required

Engineering Contradiction:
Improveproduct recovery from purgeVSAvoidprocess complexity
Core Design Contradiction:
Loss of substanceVSDevice complexity

Solution Approach 1:

The patent extracts and eliminates the purge stream generation by controlling bicarbonate concentration to remain below the invariant point. By taking out the source of the problem (impurity accumulation requiring purging), the need for complex decahydrate processing equipment and operations is eliminated entirely.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The simplified crystallization process serves multiple functions: it produces monohydrate crystals, controls impurity levels, and eliminates the need for separate decahydrate processing equipment. The single crystallization system performs what would otherwise require multiple specialized processes.

Inventive Principle:
Principle #6Universality (Multi-functionality)

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 process reduces waste generation, decreases production costs, and enhances product diversity by minimizing caustic consumption and optimizing the production of dense soda ash, sodium bicarbonate, and sodium silicate, while improving particle size and product quality.

Implementation Method 1

the bicarbonate concentration is below the invariant point within the feed solution to the monohydrate crystallizer

Methodology Applied
Scientific EffectCrystallization: Crystallisation

Implementation Method 2

The monohydrate cake effluent from the centrifuging process is dried in the rotary or fluidized bed driers

Methodology Applied
Scientific EffectDehydration: Melting

Implementation Method 3

sodium bicarbonate is converted into sodium carbonate in the stripping column

Methodology Applied
Scientific EffectStripping: Distillation

Data Source

PatentUS7507388B2Process for production of dense soda, light soda, sodium bicarbonate and sodium silicate from solutions containing bicarbonate
Publication Date: 2009.03.24 ETI SODA URETIM PAZARLAMA NAKLIYAT & ELEKTRIK URETIM SANAYI & TICARET A S
  • US7507388B2 patent drawing
  • US7507388B2 patent drawing
  • US7507388B2 patent drawing

AI summary

A process related to sodium chemicals production, including the processing of bicarbonate containing solutions obtained by solution mining of trona, nahcolite or wegscheiderite reserves and the lake waters containing bicarbonates, includes the steps of purification, evaporation-decarbonation, crystallization, centrifuging, and drying.