Submitted:
23 September 2023
Posted:
25 September 2023
You are already at the latest version
Abstract
Keywords:
1. Introduction
- Technical or cost difficulties exist in the current utilization process for PG, and the comprehensive utilization rate remains low at less than 25%[15].
- The large stock of PG piles necessitates a corresponding market for its extensive consumption.
- Downstream products derived from PG have low added value and suffer from serious homogenization.
2. Dihydrate Gypsum
3. Hemihydrate Gypsum
3.1. α-Hemihydrate Gypsum
3.2. β-Hemihydrate Gypsum
| Process | Experiment Condition | Crystal Morphology | Flexural Strength | Compressive Strength |
|---|---|---|---|---|
| Pre-grinding + calcination[55] |
Temperature: 150℃ Calcination time: 2 hours |
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— | 6.0 |
| Calcination[50] | Temperature: 130℃ Autoclave time: 3 hours Polycarboxylate superplasticizer: 0.5 % |
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3.8 | 14.8 |
| Washing + calcination[51] | Temperature: 130℃ Calcination time: 1 hours |
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3.0 | 5.7 |
| Calcination[56] | Temperature: 180℃ Calcination time: 4 hours |
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— | 9.2 |
4. Anhydrite

5. Conclusions
- the harmless treatment of PG for producing dihydrate gypsum can serve as a cement retarder. The process is straightforward and supported by well-developed technologies. However, due to its non-competitive price, the cement industry heavily relies on natural gypsum, resulting in saturated market demand. Therefore, national and local policies are needed to promote the application's development.
- The use of hemihydrate gypsum is predominantly observed in the construction industry. In comparison to β-hemihydrate gypsum, α-hemihydrate gypsum exhibits superior physical and mechanical properties. In comparison to anhydrous gypsum, α-hemihydrate gypsum consumes less energy and facilitates scaling, thereby promoting the high-quality development of PG building materials. Consequently, the production of α-hemihydrate gypsum from PG is expected to become the dominant trend in the comprehensive utilization of PG for building materials in the future.
- type II anhydrous gypsum exhibits high strength, excellent water resistance, chemical corrosion resistance, and toughness. Moreover, its production capacity is significantly higher than that of β-semi-water gypsum. It can be utilized not only in road construction and mine filling materials to achieve significant consumption of PG, but also in the preparation of gypsum whiskers for applications such as paper fillers, rubber compounds, paints, and other advanced processing of novel materials. However, the production of type II anhydrous gypsum is constrained by the high calcination temperature involved in the preparation process. Moreover, type II anhydrous gypsum exhibits limited hydration activity and slow setting and hardening characteristics, necessitating careful consideration of modification treatments during its application.
Author Contributions
Funding
Conflicts of Interest
References
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| Process | Experiment Condition | Crystal Morphology |
|---|---|---|
| Modified water washing[29] | Mechanical activation + Water phase grinding Micellar agent:CH3COOH,Al2O3 |
![]() |
| Mechanical grinding[30] | PG: fly ash: lime mass ratio of 50:30:20 mixed Grinding time: 15min Sample preparation additives: 5% cement, 3% AC reinforcer and 0.5% polycarboxylic acid water reducer |
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| Modification[31] | Modifier: 6wt% calcium carbide slag and 4wt%CFB fly ash | ![]() |
| Reverse direct flotation[32] | Collector: Kerosene Foaming agent: industrial grade pine oil |
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| Process | Principle | Advantage | Disadvantage | |
|---|---|---|---|---|
| Autoclave | Process of heating and pressurization in saturated water vapor removing of 1.5 molecules of water |
|
|
|
| Aqueous solution method |
Pressurized water solution method | Crystallization reaction of PG and water solution under pressure | High product quality |
|
| Atmospheric salt solution method | Crystallization reaction between PG and salt solution at atmospheric pressure |
|
|
|
| Process | Experiment Condition | Crystal Morphology | Flexural Strength | Compressive Strength | L/D ratio |
|---|---|---|---|---|---|
| Ball milling + Autoclave [43] | pH: 5 Temperature: 140℃ Autoclave time: 2 hours Crystal modifier: Maleic acid |
![]() |
8.2 | 25.4 | — |
| Flotation + Autoclave [44] | Temperature: 140℃ Autoclave time: 2 hours Crystal modifier: 0.13wt% Maleic acid 2.0wt% Aluminum sulfate |
![]() |
6.09 | 40.96 | 0.7: 1 |
| Atmospheric salt solution [45] | Temperature: 97±1℃ Time: 2 hours Crystal modifier: maleic acid |
![]() |
4.7 | 37.6 | 1.0: 1 |
| Pressurized aqueous solution [46] | Temperature: 130℃ pH: 7.0 Autoclave time: 4 hours Crystal modifier: EDTA |
![]() |
— | — | 1.5: 1 |
| Process | Experiment Condition | Crystal Morphology | Flexural Strength | Compressive Strength |
|---|---|---|---|---|
| Calcination + grinding[61] | Temperature: 800℃ Calcination time: 1.6 hours Potassium alum + LA-1 |
![]() |
>6.5 | 36.5 |
| Calcination[62] | Complexing agent (β-hemihydrate gypsum 6%、Modified steel slag 3%、K2SO4 2%、Calcium aluminate cement 0.5% ) | ![]() |
> 5 | 15.4 |
| Calcination [63] | Temperature: 800℃ Calcination time: 1 hours Addition: Ca (H2PO4) ·H2O and NaF |
![]() |
> 6 | > 20 |
| Calcination[64] | Temperature: 600℃ Calcination time: 1.5 hours |
![]() |
7-12 | 25-100 |
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