Composite gypsum board and methods related thereto
US-10421250-B2 · Sep 24, 2019 · US
US11834374B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11834374-B2 |
| Application number | US-201816126953-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 10, 2018 |
| Priority date | Apr 19, 2018 |
| Publication date | Dec 5, 2023 |
| Grant date | Dec 5, 2023 |
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An accelerator for accelerating the rate of hydration of calcined gypsum is disclosed. The accelerator comprises calcium sulfate dihydrate particles and a starch. The starch has a cold water solubility of at least about 25% (e.g., at least about 35%) and a viscosity of about 25 Brabender Units (BU) or less when the starch is in a 30% aqueous slurry at 92° C. Also disclosed are a method of preparing an accelerator, method of hydrating stucco to form set gypsum, slurry, and method of making gypsum board.
Opening claim text (preview).
The invention claimed is: 1. An accelerator for use in accelerating the rate of hydration of calcined gypsum to set gypsum in gypsum slurries for producing gypsum wallboard panels, said accelerator comprising: particles of calcium sulfate dihydrate having an average particle size of from 20 μm to 50 μm, and starch having a cold water solubility of at least about 25% and a viscosity of 25 Brabender Units (BU) or less when the starch is in a 30% solids aqueous slurry at 92° C., wherein the starch is an acid-hydrolyzed starch, and wherein said accelerator has a time to 50% hydration of between 2.42 and 3.83 minutes. 2. The accelerator of claim 1 , wherein the starch has a cold water solubility of at least about 35%. 3. The accelerator of claim 2 , wherein the accelerator is prepared by co-grinding the calcium sulfate dihydrate in the presence of the starch. 4. The accelerator of claim 3 , wherein the starch has an average particle size of from about 20 μm to about 100 μm prior to co-grinding. 5. The accelerator of claim 3 , wherein the starch is present in an amount from about 1% to about 10% by weight of the accelerator. 6. The accelerator of claim 3 , wherein the co-grinding occurs in a ball mill. 7. The accelerator of claim 3 , wherein the co-grinding occurs for a period of from about 10 minutes to about 90 minutes. 8. A method of preparing gypsum board comprising: (a) providing a first cover sheet; (b) mixing a first slurry comprising stucco, water, and an accelerator comprising calcium sulfate dihydrate particles having an average particle size of from 20 μm to 50 μm and starch having a cold water solubility of at least about 25%, and a viscosity of about 25 Brabender Units (BU) or less when the starch is in a 30% solids aqueous starch slurry at 92° C., wherein the starch is an acid-hydrolyzed starch, and wherein said accelerator has a time to 50% hydration of between 2.42 and 3.83 minutes; (c) disposing the first μslurry between the first cover sheet and a second cover sheet to form an assembly; (d) cutting the assembly into a board; and (e) drying the board. 9. The method of claim 8 , wherein the first slurry further comprises polyphosphate. 10. The method of claim 8 , wherein the first slurry further includes a pregelatinized starch. 11. The method of claim 10 , wherein the pregelatinized starch has a viscosity of from about 20 centipoise to about 500 centipoise, as measured according to the VMA method. 12. The method of claim 8 , wherein the first slurry further includes uncooked starch having a peak viscosity of from about 100 Brabender Units to about 900 Brabender units when the viscosity is measured by putting the uncooked starch in a second slurry with water at an uncooked starch concentration of 15% solids, and using a Viscograph-E instrument set at 75 rpm and 700 cmg, where the uncooked starch is heated from 25° C. to 95° C. at a rate of 3° C./minute, the second slurry is held at 95° C. for ten minutes, and the starch in the second slurry is cooled to 50° C. at a rate of −3° C./minute.
containing calcium sulfate cements {(gypsum-paper plates E04C)} · CPC title
Ingredients added before, or during, the calcining process, e.g. calcination modifiers · CPC title
for the wet process, e.g. dehydrating in solution or under saturated vapour conditions, {i.e. to obtain alpha-hemihydrate (C04B11/0281 - C04B11/0288 take precedence)} · CPC title
pelletizing of the material before starting the manufacture · CPC title
Polysaccharides or derivatives thereof {(C04B24/243 takes precedence)} · CPC title
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