Claims
- 1. A coating of about 2 mils to about 60 mils thickness of an hydraulic cement composition which comprises in weight percent a dry component of mineral cement selected from the group of portland and calcium aluminate cement, 100; a mineral aggregate of 100 mesh or finer selected from the group of calcite and silica and mixtures thereof, 15-60; pozzolonic fly ash, 0-15; calcium stearate, 0-1; color pigments, 0-5; and a cement accelerator, 0-3; and a liquid component to be admixed to the dry component, of water, 35-50; a synthetic polymer latex selected from the group of polymers which are film-forming at ambient temperature, 5-30, with an equivalent polymer solids of 2.5-16; a super water reducer selected from the group of polymers comprising the alkali metal salts of melamine sulfonic acid partially condensed with formaldehyde, the alkali metal salt of naphthalene sulfonic acid partially condensed with formaldehyde, and about 30-90 percent of the alkali metal salt of a high molecular weight condensation product of naphthalene-sulfonic acid and the balance 70-10 percent being the alkali salt of gluconic acid, 0.5-3.0; sodium nitrite, 0.1-0.3; a cement accelerator, on a dry basis, 0-3; and a cement retarder, 0.05-0.5.
- 2. A process for the preparation of an improved coating of about 2 mils to about 60 mils thickness suitable for spray application, containing hydraulic cement, which comprises intermixing, in parts by weight, a blended dry component of hydraulic cement, 100, finely divided mineral aggregate, 15-60, pozzolonic fly ash, 0-15, calcium stearate, 0-1.0, and color pigments, 0-5, with a liquid component of water, 35-50, a synthetic polymer latex, 5-30, with equivalent polymer solids, 2.5-16, a super water reducer, 0.5-3.0, sodium nitrite, 0.1-0.3, and a cement retarder, 0.15-0.5, and placing the resulting mixture on a substrate until it sets.
- 3. A process according to claim 2 wherein the hydraulic cement is selected from the group of portland cement and calcium aluminate cement.
- 4. A process according to claim 2 wherein the finely divided mineral aggregate is 100 mesh or finer, and is selected from the group of minerals calcite, silica, aluminum oxide, aluminum trihydrate, and mixtures thereof.
- 5. A process according to claim 2 wherein the synthetic polymer latex is an emulsion of polymers which are film-forming at room temperature.
- 6. A process according to claim 2 wherein the super water reducer is selected from the group of polymers comprising the alkali metal salts of melamine sulfonic acid partially condensed with formaldehyde, the alkli metal salt of naphthalene sulfonic acid partially condensed with formaldehyde, and about 30-90 percent of the alkali metal salt of a high molecular weight condensation product of naphthalene-sulfonic acid and the balance 70-10 percent being the alkali salt of gluconic acid.
- 7. A process according to claim 2 wherein the dry and wet components are metered into a common duct from separate containers, are contacted in measured ratios just before an in-line static mixing device in the duct, the mixture is conveyed through the static mixer by air pressure and is discharged through a spray nozzle unto a substrate.
- 8. A process according to claim 7 wherein one of the components contains a hydraulic cement accelerator.
CROSS REFERENCE TO RELATED APPLICATIONS
This application is a continuation-in-part of our copending applications Ser. No. 610,990, filed Sept. 8, 1975 now U.S. Pat. No. 4,039,170, and Ser. No. 649,895, filed Jan. 16, 1976 now U.S. Pat. No. 4,036,839.
US Referenced Citations (6)
Related Publications (1)
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Date |
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649895 |
Jan 1976 |
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Continuation in Parts (1)
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Number |
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610990 |
Sep 1975 |
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