Alkali-Activated Cement Stepwise Calcination Cost Reduction

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Solution Overview

Problem

The preparation of traditional alkali-activated cement faces challenges such as high costs due to expensive raw materials and industrial alkali activators, scarce kaolin resources, and variability in composition, leading to high carbon emissions and durability issues.

Innovation Solution

A method of preparing alkali-activated cement through stepwise calcination with sodium chloride, using cheap raw materials and reducing the dosage of alkali activators, involving mixing sodium chloride with silicate and carbonate, followed by sequential calcination and rapid cooling, and mixing with sodium hydroxide or potassium hydroxide to produce the cement.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If traditional alkali-activated cement is prepared using industrial alkali activators and expensive raw materials, then the cement achieves high early strength and corrosion resistance, but the preparation cost increases significantly

Engineering Contradiction:
Improvecorrosion resistanceVSAvoidpreparation cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The patent replaces expensive industrial alkali activators with cheap natural alkali sources including waste glass, fly ash, and blast furnace slag. These inexpensive materials provide sufficient alkali content for activation while dramatically reducing preparation costs. The principle of using cheap, readily available materials substitutes for expensive specialized chemicals is clearly applied here.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The patent recovers and utilizes alkali metals from industrial waste materials such as waste glass, fly ash, and blast furnace slag. By extracting and reusing the alkali content from these discarded materials, the process reduces the need for fresh expensive alkali activators while simultaneously managing industrial waste, thus lowering both cost and environmental impact.

Inventive Principle:
Principle #34Discarding and recovering

2Strength

If alkali-activated cement uses large dosage of industrial alkali activators (3-14 wt% Na2O), then the cement achieves high strength, but the cost increases and efflorescence problems occur affecting durability

Engineering Contradiction:
Improvecompressive strengthVSAvoidefflorescence
Core Design Contradiction:
StrengthVSObject-affected harmful factors

Solution Approach 1:

The patent changes the chemical composition parameters by using natural alkali sources with different chemical profiles compared to industrial alkali activators. The alkali metals are derived from silicate and carbonate minerals rather than concentrated caustic solutions, which alters the dissolution behavior and reduces efflorescence while maintaining adequate strength through optimized mix proportions.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite alkaline activators combining multiple natural materials (waste glass, fly ash, blast furnace slag) that work synergistically. This composite approach provides a balanced chemical composition that achieves high strength while minimizing efflorescence, as the different materials complement each other's properties and reduce the harmful effects of using any single material alone.

Inventive Principle:
Principle #40Composite materials

3Reliability

If expensive raw materials like industrial alkali and sodium potassium aluminosilicates are used for clinker calcination, then the cement achieves high performance, but the preparation cost remains high

Engineering Contradiction:
ImproveperformanceVSAvoidpreparation cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The patent replaces expensive clinker calcination raw materials (industrial alkali and sodium potassium aluminosilicates) with cheap natural materials including waste glass, limestone, and industrial by-products. These inexpensive materials provide the necessary chemical components for clinker formation while dramatically reducing the cost of the calcination process.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The patent recovers valuable materials from industrial waste streams for use in clinker calcination. Fly ash, blast furnace slag, and waste glass are processed and utilized as raw materials, transforming waste disposal costs into resource recovery benefits while reducing the need for expensive virgin materials in the clinker production process.

Inventive Principle:
Principle #34Discarding and recovering

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 significantly reduces the preparation cost of alkali-activated cement, minimizes carbon emissions, recovers valuable metals, and enhances resource recovery, while eliminating heavy metal pollution and improving durability.

Implementation Method 1

a first calcination at 850-1050° C.

Methodology Applied
Scientific EffectThermal decomposition: Pyrolysis

Implementation Method 2

mixing a sodium chloride, a silicate and a carbonate followed by grinding to obtain a raw material powder; sequentially subjecting the raw material powder to a first calcination at 850-1050° C., a second calcination at 1240° C. or more

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Data Source

PatentUS20240327282A1Method of preparing alkali-activated cement by stepwise calcination with sodium chloride
Publication Date: 2024.10.03 HUNAN XIANGCHU XIANLU ENVIRONMENTAL PROTECTION TECHNOLOGY CO LTD

AI summary

A method of preparing alkali-activated cement by stepwise calcination with sodium chloride includes the following steps. (1) Sodium chloride, a silicate and a carbonate are mixed and finely ground to obtain a raw material powder. (2) The raw material powder is calcined sequentially at 850-1050° C. and 1240° C. or more, and cooled to obtain a clinker. (3) The clinker is mixed with at least one of sodium hydroxide and potassium hydroxide, and ground finely to produce a cement powder.