Biomass derived grinding aids
View Patent ↗Compositions and methods for increasing grinding efficiency of cement, cement clinker, raw materials for cement, and other inorganic particles. Use of biomass-derived polyols such as diols, triols, or mixtures thereof, optionally with a conventional grinding aid, cement quality improver, and/or hexavalent chromium reducer, are believed to provide less risk of sludging when compared to glycerides obtained from fossil fuel sources.
1. A method for grinding particles, comprising:
introducing to cement clinker particles and limestone particles, in a ball mill or roller mill whereby said particles are ground to have finer average particle size, an aqueous additive composition comprising:
at least one grinding additive selected from the group consisting of triethanolamine, triisopropanolamine, diethanolisopropanolamine, tetrahyroxyethylthylene diamine, an acetic acid or salt thereof, or mixtures thereof; and
a crude glycerin obtained derived from biofuel production; and
wherein the amount of said at least one grinding additive and said crude glycerin derived from biofuel production are in the ratio of 90:10 to 10:90 by weight.
2. The method of claim 1 wherein the crude glycerin comprises glycerin, methanol, water moisture, fatty acid, sodium chloride, sulfate, phosphate, and ash, said ash being present in an amount not exceeding 10% by weight of the aqueous additive composition.
3. The method of claim 1 further comprising introducing a water reducing additive, a chromium reducing additive, or mixture thereof into the ball mill or roller mill.
4. The method of claim 1 wherein the crude glycerin is reacted with a monobasic carboxylic acid.
5. The method of claim 1 wherein the wherein the crude glycerin has one or more substituted OH groups.
6. The method of claim 1 wherein the aqueous additive composition comprising at least one grinding additive and the crude glycerin derived from biofuel production are introduced together as a single additive composition, the additive composition comprising water in the amount of 10%-30% and triethanolamine in an amount of 10%-80%, and said crude glycerin derived from biofuel production comprising 1,2,3-propane triol.
7. The method of claim 1 wherein the aqueous additive composition comprising at least one grinding additive and said crude glycerin derived from biofuel production are introduced together as an additive composition, the additive composition comprising water in the amount of 10%-30% and triisopropanolamine in an amount of 10%-80%, and biofuel derived 1,2,3-propane triol.
8. The method of claim 1 wherein the at least one grinding additive further comprises a glycol.
9. The method of claim 1 wherein the cement clinker and limestone particles are introduced to acetic acid or salt thereof.
10. The method of claim 1 wherein the cement clinker particles and limestone particles are introduced to triethanolamine, triisopropanolamine, diethanolisopropanolamine, tetrahyroxyethylthylene diamine, or a mixture thereof.
11. A method for grinding particles, comprising:
introducing to limestone particles in a ball mill or roller mill whereby said particles are ground to have finer average particle size, an aqueous additive composition comprising:
at least one grinding additive comprising an acetic acid or salt thereof; and
a crude glycerin obtained derived from biofuel production; and
wherein the amount of said at least one grinding additive and said crude glycerin derived from biofuel production are in the ratio of 90:10 to 10:90 by weight.
12. A method for grinding particles, comprising:
introducing to limestone particles in a ball mill or roller mill whereby said particles are ground to have finer average particle size, an aqueous additive composition comprising:
at least one grinding additive comprising triethanolamine, triisopropanolamine, diethanolisopropanolamine, tetrahyroxyethylthylene diamine, or mixture thereof; and
a crude glycerin obtained derived from biofuel production; and
wherein the amount of said at least one grinding additive and said crude glycerin derived from biofuel production are in the ratio of 90:10 to 10:90 by weight.