Synthetic Pozzolans
US-2017320781-A1 · Nov 9, 2017 · US
US2023339814A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023339814-A1 |
| Application number | US-202318216368-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 29, 2023 |
| Priority date | May 5, 2016 |
| Publication date | Oct 26, 2023 |
| Grant date | — |
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Synthetic pozzolans are produced using local materials to provide a cementitious material that is uniform in chemistry and properties independent of the location where the materials are obtained. Two methods of production are described. One is a high temperature process in which materials are processed in a semi-molten or molten state. The second process is a low temperature aqueous process.
Opening claim text (preview).
What is claimed is: 1 . A synthetic pozzolan comprising: at least 10% by mass of an activatable amorphous phase comprised of one or more of siliceous, aluminosiliceous and aluminous material, said activatable amorphous phase configured to be activated by conducting a chemical reaction to form a cementitious compound. 2 . The synthetic pozzolan of claim 1 , further comprising a crystalline phase. 3 . The synthetic pozzolan of claim 2 , wherein said crystalline phase comprises in its majority crystalline melilite. 4 . The synthetic pozzolan of claim 2 , wherein said crystalline phase comprises in its majority crystalline plagioclase feldspar. 5 . The synthetic pozzolan of claim 2 , wherein said crystalline phase comprises in its majority crystalline alkali feldspar. 6 . A method of making a synthetic pozzolan, said synthetic pozzolan comprising at least 10% by mass of an activatable amorphous phase, the method comprising the step of performing a solid state reaction in a high temperature process to produce a clinker. 7 . The method of making a synthetic pozzolan of claim 6 , wherein said step of performing a solid state reaction in a high temperature process comprises the steps of: selecting one or more precursor raw materials; analyzing the chemical compositions of said one or more precursor raw materials; blending said one or more precursor raw materials to obtain a blended precursor composition with a bulk molar ratio of Ca to the sum of Al, Fe, Mg, Si of 0.5-1.0 and a sum of metal oxides of Al, Fe and Mg of at least 14% by weight; and heating said blended precursor composition to a temperature between 800° C. and 1400° C. for a time sufficient to react said blended precursor composition to produce a melilite based clinker. 8 . The method of making a synthetic pozzolan of claim 6 , wherein said step of performing a solid state reaction in a high temperature process comprises the steps of: selecting one or more precursor raw materials; analyzing the chemical compositions of said one or more precursor raw materials; blending said one or more precursor raw materials to obtain a blended precursor composition with a bulk chemistry of AlSi 2 O 8 with the addition of a one or more of CaAl (anorthite end member), NaSi (albite end member), or KAl (orthoclase end member) with a molar ratio of the CaAl+NaSi+KAl components to AlSi 2 O 8 of 0.8-1.2 to 1; and heating the blended precursor composition to a temperature between 800° C. and 1400° C. for a time sufficient to react said blended precursor composition to produce a plagioclase feldspar based clinker. 9 . The method of making a synthetic pozzolan of claim 6 , further comprising the step of using of a pretreatment chemical to improve a reaction rate or a maximum extent of reaction of said solid state reaction over said reaction rate or said maximum extent of reaction that is observed in the absence of said pretreatment chemical. 10 . The method of making a synthetic pozzolan of claim 9 , wherein said pretreatment chemical is an organic acid solution containing at least one of acetic acid, citric acid, tartaric acid, gluconic acid, and oxalic acid. 11 . The method of making a synthetic pozzolan of claim 6 , comprising the step of introducing said pretreatment chemical during grinding of the clinkers. 12 . The method of making a synthetic pozzolan of claim 6 , comprising the step of introducing said pretreatment chemical to a ground clinker. 13 . A method of making a synthetic pozzolan, said synthetic pozzolan comprising at least 10% by mass of an activatable amorphous phase, the method comprising the step of performing an aqueous reaction in a low temperature process. 14 . The method of making a synthetic pozzolan of claim 13 , wherein said step of performing an aqueous reaction in a low temperature process comprises using a precursor comprising a silicate mineral configured to decompose or incongruently dissolve to form an activatable amorphous phase and a precursor chemical configured to aid in the decomposition or dissolution of the precursor mineral. 15 . The method of making a synthetic pozzolan of claim 13 , further comprising the step of percolating a CO 2 containing waste gas through a reactor. 16 . The method of making a synthetic pozzolan of claim 13 , wherein said precursor chemical is an acid. 17 . The method of making a synthetic pozzolan of claim 13 , wherein said precursor chemical is derived from CO 2 gas. 18 . The method of making a synthetic pozzolan of claim 13 , wherein said precursor chemical is synthesized from CO 2 gas. 19 . The method of making a synthetic pozzolan of claim 13 , wherein said precursor mineral is selected from a naturally obtained mineral, a siliceous limestone, a clay, wollastonite, olivine, and feldspar. 20 . The method of making a synthetic pozzolan of claim 13 , wherein said precursor mineral is a manmade material selected from ordinary Portland cement, a calcium sulfoaluminate cement, a calcium aluminate cement, a carbonateable calcium silicate cement, and synthetic foundry sand. 21 . The method of making a synthetic pozzolan of claim 13 , wherein said precursor mineral is a synthetically produced pozzolan. 22 . The method of making a synthetic pozzolan of claim 13 , wherein said precursor mineral is selected from a waste material, slag and fly ash. 23 . The method of making a synthetic pozzolan of claim 13 , wherein said activatable amorphous phase comprises SiO 2 and Al 2 O 3 . 24 . A composite material produced by the blending of a synthetic pozzolan of claim 1 with an activator and water. 25 . The composite material of claim 24 wherein the activator is selected from hydraulic cement (1-70 wt %), free lime (1-20 wt %), calcium hydroxide (1-20 wt %), and alkali hydroxides (NaOH, KOH 1 to 10 wt %), individually or in combination.
the Ca-silicates being present in the starting mixture · CPC title
containing mineral polymers, e.g. geopolymers of the Davidovits type · CPC title
Aluminium-containing silicates {, i.e. silico-aluminates} · CPC title
Hydraulic cements not provided for in one of the groups C04B7/02 - C04B7/34 · CPC title
Natural pozzuolanas; Natural pozzuolana cements; {Artificial pozzuolanas or artificial pozzuolana cements other than those obtained from waste or combustion residues, e.g. burned clay; Treating inorganic materials to improve their pozzuolanic characteristics (cements containing slag C04B7/14)} · CPC title
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