AU2015255159B2 - Method of producing gypsum binder - Google Patents
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- AU2015255159B2 AU2015255159B2 AU2015255159A AU2015255159A AU2015255159B2 AU 2015255159 B2 AU2015255159 B2 AU 2015255159B2 AU 2015255159 A AU2015255159 A AU 2015255159A AU 2015255159 A AU2015255159 A AU 2015255159A AU 2015255159 B2 AU2015255159 B2 AU 2015255159B2
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Abstract
METHOD OF PRODUCING GYPSUM BINDER Abstract The method of producing gypsum binders is aimed at achieving the technical result of providing opportunities for producing a-modifications of calcium sulfate hemihydrate and multiphase gypsum binders, obtained on its basis, at atmospheric pressure. The technical result is achieved due to the fact that the new method, involving dehydration of gypsum raw material lumps, stipulates heating of gypsum raw material lumps at atmospheric pressure by placing them in thermal shock conditions and during a period required for completion of the dehydration reaction with development of a-modification of calcium sulfate hemihydrate and with further drying, cooling and milling. (10674816_1):JJC
Description
METHOD OF PRODUCING GYPSUM BINDER
The invention pertains to the construction material industry and it can be used for producing gypsum binders and products made on their basis.
The principle of obtaining gypsum binders is founded on capacity of calcium sulfate dihydrate, when heated, undergo dehydration accompanied by changes in the crystal lattice structure (recrystallization).
Natural gypsum stone, recycled gypsum and synthetic gypsum, which is a co-product of the chemical, power, food, wood chemical and other industries (phosphogypsum, borogypsum, chlorogypsum, cytrogypsum, etc.), are used as raw materials for production of gypsum binders.
The industry of low-roasted gypsum binders with a treatment temperature up to 900°C produces several types of products: a- and β-modifications of calcium sulfate hemihydrate, dehydrated hemihydrate, soluble and insoluble anhydrite. Dehydrated hemihydrate and soluble anhydrite are unstable in the air and develop into hemihydrate. The major production volume falls on a- and β-hemihydrates (a- and β-gypsum) or their mixtures. There is a segment of insoluble anhydrites.
Obtained by roasting, a- and β-modifications of gypsum are characterized by the same crystal lattice type. Their difference is that the first has a better structure with well-defined large-size crystals, while the second consists of smallest aggregates of defective crystals with developed inner surface. As a result, a-gypsum products show much better characteristics of strength and moisture resistance than β-gypsum products. However, the main production volume of gypsum binders falls on β-hemihydrate owing to its simpler and cheaper production technology.
The applied flow charts for producing α-modification of gypsum can be subdivided into three key groups: - Heat treatment of lumpy gypsum raw material with saturated steam under pressure using various methods of drying the dehydrated product and subsequent milling; - Heat treatment of powdered gypsum raw material in aqueous suspension under pressure with mechanical dehydration, drying, and milling; - Heat treatment of powdered gypsum raw materials at atmospheric pressure in salt solutions followed by washing, dehydration, drying, and milling.
The main disadvantage of the first two flow charts is that the process requires high pressurization and it is, normally, realized periodically. This significantly increases the cost of both the plant for their realization and the resulting product.
The last two flow charts relate to processing in liquid medium and use additional steps of washing and drying. This will consume a large amount of water and additional heat. This is a significant disadvantage of these methods. Therefore of great practical importance is the method of processing in gaseous medium, eliminating the need for washing and further drying.
At temperatures 105-135°C, these flow charts provide, mostly, α-hemihydrate; at 200-210°C - α-dehydrated hemihydrate; at 220-250°C - a-soluble anhydrite. Higher temperatures produce insoluble anhydrite.
Construction gypsum (β-gypsum) is obtained using a simple technology by heat treatment of gypsum raw material at normal pressure within the temperature range 100°C-160°C. The applied flow charts can be subdivided into three key groups: - Roasting lumpy raw material in drying drums or rotary kilns using flue gases at a relatively low rate of raw material dehydration and, as a consequence, with roasting duration of several hours and flue gas components getting into the product; - Roasting of pre-milled raw material in kettles with non-contact heating through the wall of a heating unit and roasting duration not exceeding 2 hours; - Roasting of milled raw material, contacting with heat medium, in suspension (in mills, “fluidized bed” machines, etc.) at a high rate of the dehydration processes - up to 1 hour.
The advantage of the flow charts for producing β-modification of gypsum is the technology simplicity that does not require high pressurization and its low cost. Nevertheless, β-modification of gypsum, obtained using these methods, is characterized by poor strength properties, no moisture resistance and short mixing time.
In order to improve gypsum binder properties, depending on required characteristics, multiphase (from diverse modifications of gypsum) and/or composite (with adding external nongypsum components) gypsum-based mixtures are produced. Their production involves varying the composition, granulometry, and the component ratio for regulating functional properties: durability, setting time, water resistance, etc. There are great many various additives affecting properties of gypsum binders. All this greatly increases the cost of the finished product.
The closest technical solution is a method of making the gypsum binder described in RU patent No. 2023699 published on 30.11.1994, which suggests a method of producing a binder with predominating calcium sulfate α-hemihydrate. The method consists in gypsum dehydration carried out in lumps at atmospheric pressure in gaseous medium, what is its important advantage, in electromagnetic super-high-frequency field (SHF field). Due to volumetric heating affected by SHF radiation, pressure is increased directly within a gypsum lump. Dehydration with development of predominantly α-modification of gypsum occurs in the proper volume of a lump, which becomes a sort of “mini autoclave” for itself, β- modification of gypsum develops in the near-surface layer.
The disadvantage of this technical solution is applying, during its implementation, a very uneconomic method of heating with SHF radiation generated due to using electric power and, consequently, its high cost.
The technical result of the present invention is providing an opportunity to obtain a-modification of gypsum and multiphase gypsum binders, based on it using lumpy raw material, at the atmospheric pressure in gaseous medium.
The technical result is achieved due to the fact that, in the suggested method involving dehydration of gypsum raw material lumps by heating at atmospheric pressure, heating of gypsum raw material lumps is carried out by placing them in thermal shock conditions and for a period required for completion of the dehydration reaction with predominating formation of a-modification of calcium sulfate hemihydrate, with further drying, cooling, and milling. Thermal shock conditions, or fast external heating by placing the lumps in a high-temperature environment and/or by ensuring high growth rate of ambient temperature around the lumps, the favour growth of water vapor pressure within a lump, which is necessary for dehydration with formation of, mainly, gypsum a-hemihydrate.
In the technical science, the thermal shock is understood as the processes characterized either by treating at high temperatures or high speed of temperature growth, or fast growth of temperature to the values above normally used values.
The thermal shock suggests that the amount of energy, applied to raw material for the process, is greater than energy required for transformation processes in used raw materials at every instant, i.e. energy is supplied in advance of its consumption.
When heated using the thermal shock method, the conditions for dehydration with developing α-modification of gypsum are established within a lump, i.e., each lump becomes mini autoclave for itself and conditions for dehydration with formation of gypsum a-modification are created within every gypsum lump. Such conditions are not established in the near-surface layer of a lump, and β-modification of gypsum develops there.
Each particular raw material allows its own thermal shock conditions. Thus, in our case, the thermal shock must be understood as such conditions of heat treatment of raw material lumps at the atmospheric pressure, under which the dehydration process occurs with a-recrystallization.
Thermal shock parameters and time of the process are determined in advance, depending on properties of a specific raw material, size of lumps, and requirements to the end product as regards the relation of a- and β-hemihydrates or other gypsum modifications in the end product.
Dividing the process into heating, drying and cooling stages is conventional. The heating stage implies dehydration and recrystallization, the drying stage - product dewatering, cooling -product cooldown. At the same time, it's difficult to draw distinct borders between the stages. So, during the heating stage, moisture evaporates through lump surface and drying of processed raw material occurs. During lump drying and water evaporation, processed raw material cools down. This method is flexible and allows many modifications of operation sequence: - heating, drying, cooling, crushing; - heating and drying in one device, cooling, crushing; - heating and drying in one device, crushing, cooling; - heating, crushing, drying, cooling; - heating, crushing and drying in one device, cooling; - and other similar options.
The temperature of gaseous media for thermal shock, drying, and cooling is selected from a technically rational range so that this technological stage can be carried out. The process conditions - temperature and time - can vary within a wide range.
Thus, the thermal shock temperature can be from 140°C to 1200°C and above. The process of dehydration with a-recrystallization must progress within a lump at a specific temperature during a specific time period. The drying temperature can range from the ambient temperature to the thermal shock temperature. The only thing that matters is that, at this temperature and during this time period, a dehydrated product should lose moisture and no rehydration process should occur.
The process time can vary from 15 minutes to 5 hours.
This method can be used for processing raw material with naturally developed temperature and does not require preheating or cooling of the raw material.
Gypsum raw material lumps can be formed by both crushing natural gypsum rock and by agglomerating powders and/or fine fractions of natural, synthetic, or recycled gypsum.
Lumpy raw materials of sizes customary for the gypsum industry are processed; meanwhile, other process conditions, leading towards the needed result, are adjusted to specific raw material parameters.
The production can be both continuous and periodic.
The thermal shock and drying stages can be united in one device.
The drying and/or cooling, and/or milling stages can be combined simultaneously and/or in one device.
Blowing of raw materials during dehydration process increases the content of gypsum β-modification in the near-surface layer of the lumpy gypsum.
Using smaller raw material fractions accelerates the dehydration process but, by doing so, leads to increasing content of calcium sulfate hemihydrate β-modification in the end product.
Milling using the surface abrasion method allows separating the product from the nearsurface layer with an increased content of gypsum β-modification and the product from the middle of a lump with predominating content of gypsum a-modification.
Increasing humidity of thermal shock medium accelerates the rate of material heating.
Decreasing humidity of the medium at the drying and/or cooling stages accelerates these processing stages.
Wetting of lump surface accelerates the thermal shock stage of the process.
When special additives that influence gypsum recrystallization are added to water which is used for wetting of lump surface and/or introduced into the agglomerated raw material, it affects the composition, structure and characteristics of the end product.
Over-pressurizing at the thermal shock stage and/or under-pressurizing at the drying and cooling stages contribute to the production process, but they are not mandatory and cannot be regarded as method modifications.
Preliminary surface treatment of gypsum raw material lumps to modify the pore structure, e.g. extra coating, will change the process modes and properties of the resulting product.
It is possible to carry out the process under non-isothermal conditions: e.g. increasing temperature in a set range at a certain rate at the thermal shock stage and decreasing it at the subsequent stages or vice versa. It is also possible to introduce temperature oscillating processes in order to affect functional properties of the resulting product.
Both indirectly heated air and direct flue gases can be used for the process.
Additional exposure to SHF radiation at the moment of recrystallization will change properties of the end product.
The suggested method can also be used for production of dehydrated a-hemihydrate of gypsum or soluble α-anhydrite with their subsequent reduction to α-hemihydrate of gypsum. Insoluble anhydrite can also be produced. The process parameters can be chosen so that the finished product contains the active lime.
Application of this method is possible when producing finished products directly from gypsum. For this purpose, a pre-molded product is placed in the medium and conditions of thermal shock, under which formation of gypsum a-modification occurs within the product followed by further cooling and drying completion stages.
Varying the process parameters allows obtaining gypsum binders with diverse compositions and changing the ratio of a- and β-modifications, hemihydrate, and anhydrite in a wide concentration range directly within the production process.
The method was realized in the examples as follows.
As a source raw material, samples of natural gypsum lumps, agglomerated in lumps and dried calcium sulfate dihydrate powder were used. The size of the lumps was 3-6 cm.
The treatment process using the thermal shock method was carried out at atmospheric pressure by placing the gypsum raw material in a medium with the hot air under isothermal conditions at temperatures ranging from 160°C to 360°C. The roasting time was varying from 45 minutes to 3.5 hours. Cooling of the finished samples was at room temperature and humidity, followed by milling of the material to powder.
Table 1 summarizes the data of the Rietveld method for quantitative X-ray phase analysis and assessment results of calcium sulfate hemihydrate α-modification for several samples obtained by combining the thermal shock and drying processes. The treated samples represent hemihydrate gypsum with a certain content of impurities inherent with the source raw material; and presence of small amounts of anhydrite and calcium sulfate dihydrate was observed in some particular cases.
It was found that diffraction lines of the calcium sulfate hemihydrate were not broadened, what is evidence of low crystallite microstress values typical of a-gypsum. No amorphous phase was found in the samples.
Table 1
1 Study was performed for the fraction obtained from the central part of a gypsum lump. 2 Anhydrite sample was made.
It is evident that the content of gypsum α-modification for the fraction, taken from the middle of the sample lump, is slightly higher against the volume-averaged fraction.
Heating the sample with the medium temperature 360°C resulted in formation of anhydrite. Whereas, the sample processing under the same conditions but with earlier stopping of the process allowed obtaining a product with a sufficiently high concentration of a-gypsum 75% and the soluble anhydrite content 2.5% during the roasting period of 45 minutes.
Thus, the announced technical result of the invention is achieved. The obtained end product samples represent hemihydrate gypsum with the ratio of α-modification to β-modification up to 95%.
An essential advantage of this invention is its environmental importance.
Firstly, applying the new technology allows significant reduction of energy consumption in contrast to other methods of α-gypsum production, what will allow both reducing material costs and lowering the environmental impact of harmful technological factors associated with energy generation.
Secondly, the suggested method is easily applicable for processing of gypsum raw material, being a by-product of many industries implemented, largely, to reduce sulfur emissions.
Thirdly, the recommended method does not require the stage of washing using lots of clean water, as needed for the solution technology of obtaining α-gypsum in the presence of an electrolyte.
Fourthly, using such a simple and inexpensive technology for producing extra strong gypsum will allow expanding its application and displacing cement-based binders that, both in terms of their properties and production conditions, show inferior environmental characteristics.
Fifthly, it is important that application of gypsum in construction allows its multiple recycling, what makes it different from currently popular concretes and cements that can be used one time only.
Claims (15)
- CLAIMS:1. A method of producing a gypsum binder including dehydrating of gypsum raw material lumps by heating in gaseous medium with further drying, cooling, and milling stages, wherein heating gypsum raw material lumps is performed either by: placing the lumps in a heating medium set to a temperature exceeding the temperature under which dehydration and formation of gypsum a-hemihydrate occurs; and/or placing the lumps in a heating medium having a high rate of temperature increase such that a temperature higher than the temperature under which dehydration and formation of gypsum α-hemihydrate occurs is reached; and under the chosen heating technique, a heating time is selected sufficient for completion of the process of gypsum a -modification formation within the gypsum lumps, wherein the heating is performed under atmospheric pressure through lump surface.
- 2. The method according to claim 1, wherein natural gypsum stone and/or synthetic gypsum and/or recycled gypsum are used as the gypsum raw material.
- 3. The method according to claim 1 or claim 2, wherein the gypsum raw material lumps are formed by crushing and/or agglomerating.
- 4. The method according to any one of claims 1 to 3, wherein the heating medium temperature and heating time are determined experimentally for a particular raw material, depending on the size of lumps, properties of gypsum raw material, more specifically, the pore structure, and the required characteristics of the end product.
- 5. The method according to any one of claims 1 to 4, wherein the heating medium temperature is at least 140°C.
- 6. The method according to any one of claims 1 to 5, wherein the temperature of the medium for the drying stage is between ambient temperature and thermal shock temperature.
- 7. The method according to any one of claims 1 to 6, wherein the heating and drying stages are combined.
- 8. The method according to any one of claims 1 to 7, wherein the drying and/or cooling and/or milling stages are combined.
- 9. The method according to any one of claims 1 to 8, wherein the heating time is from 20 minutes to 5 hours.
- 10. The method according to any one of claims 1 to 9, wherein humidity of the heating medium is varied.
- 11. The method according to any one of claims 1 to 10, wherein the surface of the gypsum raw material lumps is pre-moistened.
- 12. The method according to any one of claims 1 to 11, wherein indirectly heated air or direct flue gases are used as a heating medium.
- 13. The method according to any one of claims 1 to 12, wherein milling is carried out such that a near-surface layer of the lumps is separated from a central part of the lumps rich in gypsum a-modification.
- 14. The method according to any one of claims 1 to 13, wherein the method is carried out until dehydrated gypsum a-hemihydrate is obtained or wherein soluble α-anhydrite is obtained subsequently reduce to gypsum a-hemihydrate.
- 15. The method according to any one of claims 1 to 14, wherein process parameters are chosen so that the finished product contains active lime.
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| AU2015255159A AU2015255159B2 (en) | 2014-10-13 | 2015-11-09 | Method of producing gypsum binder |
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| AU2014246630 | 2014-10-13 | ||
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| AU2015255159A AU2015255159B2 (en) | 2014-10-13 | 2015-11-09 | Method of producing gypsum binder |
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| AU2015255159B2 true AU2015255159B2 (en) | 2016-09-22 |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2616789A (en) * | 1951-03-19 | 1952-11-04 | Certain Teed Prod Corp | Method of producing gypsum plaster |
| AU447777B2 (en) * | 1969-01-09 | 1974-04-10 | Unitedstates Gypsum Company | Calcined gypsum and its preparation |
| DE3522495A1 (en) * | 1985-06-24 | 1987-01-02 | Heinrich Quante | Process for the unpressurised preparation of alpha-gypsum hemihydrate and equipment for carrying out the process |
| RU2023699C1 (en) * | 1990-11-26 | 1994-11-30 | Уральский научно-исследовательский и проектный институт строительных материалов | Process for manufacture of gypsum binder |
| WO2001079116A1 (en) * | 2000-04-14 | 2001-10-25 | The Research Foundation Of State University Of New York | Alpha calcium sulfate hemihydrate and a method of making alpha calcium sulfate hemihydrate |
-
2015
- 2015-11-09 AU AU2015255159A patent/AU2015255159B2/en not_active Ceased
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2616789A (en) * | 1951-03-19 | 1952-11-04 | Certain Teed Prod Corp | Method of producing gypsum plaster |
| AU447777B2 (en) * | 1969-01-09 | 1974-04-10 | Unitedstates Gypsum Company | Calcined gypsum and its preparation |
| DE3522495A1 (en) * | 1985-06-24 | 1987-01-02 | Heinrich Quante | Process for the unpressurised preparation of alpha-gypsum hemihydrate and equipment for carrying out the process |
| RU2023699C1 (en) * | 1990-11-26 | 1994-11-30 | Уральский научно-исследовательский и проектный институт строительных материалов | Process for manufacture of gypsum binder |
| WO2001079116A1 (en) * | 2000-04-14 | 2001-10-25 | The Research Foundation Of State University Of New York | Alpha calcium sulfate hemihydrate and a method of making alpha calcium sulfate hemihydrate |
Non-Patent Citations (1)
| Title |
|---|
| McAdie, H. G., "The Effect of Water Vapor upon the Dehydration of CaSO4.2H2O", Canadian J. Chem., (1964), Vol 42, pages 792-801 * |
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| AU2015255159A1 (en) | 2016-04-28 |
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