Freeze-thaw durable geopolymer compositions and methods for making same
US-2017166481-A1 · Jun 15, 2017 · US
US10800703B1 · US · B1
| Field | Value |
|---|---|
| Publication number | US-10800703-B1 |
| Application number | US-201816172043-A |
| Country | US |
| Kind code | B1 |
| Filing date | Oct 26, 2018 |
| Priority date | Oct 26, 2018 |
| Publication date | Oct 13, 2020 |
| Grant date | Oct 13, 2020 |
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A rapid-setting composition includes fly ash and an activator solution for mixing with the fly ash. The activator solution has a silicate solution including a monovalent hydroxide. The activator solution when mixed with the fly ash produces a composition that has a final set time of no more than about 65 minutes.
Opening claim text (preview).
We claim: 1. A method of providing a rapid-setting cementitious composition of adjustable set time, comprising the steps of: providing an amount of fly ash; providing an activator solution comprising a silicate solution including a monovalent hydroxide having a molarity; adjusting the temperature of the activator solution to a temperature of from about 4.5° C. to about 60° C.; providing an amount of inert material comprising sand, soil, clay, gravel and combinations thereof, the amount of the inert material being selected relative to the amount of fly ash to provide a ratio of the inert material to the fly ash; mixing the activator solution with the fly ash and the inert material to provide a rapid-setting cementitious composition that has a final set time that ranges from about 5 minutes to about 65 minutes; and adjusting the molarity of the monovalent hydroxide in the activator solution or the ratio of the inert material to the fly ash or both the molarity of the monovalent hydroxide in the activator solution and the ratio of the inert material to the fly ash to provide a final set time within the range, wherein the final set time is determined by the molarity of the monovalent hydroxide in the activator solution or the ratio of the inert material to the fly ash or both the molarity of the monovalent hydroxide in the activator solution and the ratio of the inert material to the fly ash, wherein the final set time varies further within the range based on the temperature of the activator solution. 2. The method of claim 1 , wherein the fly ash comprises Class C fly ash and the silicate solution comprises a potassium silicate solution or a sodium silicate solution. 3. The method of claim 1 , wherein the monovalent hydroxide comprises Group I alkali metal hydroxides, potassium hydroxide, sodium hydroxide, cesium hydroxide, or lithium hydroxide. 4. The method of claim 1 , wherein the ratio of the inert material to the fly ash ranges from about 0.05 to about 4 by weight. 5. The method of claim 1 , wherein the monovalent hydroxide has a molar concentration that is adjusted between about 5.5 M to about 8.0 M to vary the final set time.
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