US5093093A
Expired / Lapsed
US
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Process for preparing calcium sulfate alpha hemihydrate
Assignee: Sicowa Verfahrenstechnik fuer Baustoffe GmbH and Co KG
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Filing: 1989-05-10
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Granted: 1992-03-03
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Expires: 2009-05-10
Abstract
Abstract In a process for preparing calcium sulphate alpha hemihydrate essentially the form of primary crystals, the hemihydrate is milled to specific surface area of 1200 to 4000 cm 2 /g, the fines are removed by screening, and a retarder and liquefier in the form of at least one fruit acid and/or its or their salt(s) are admixed. The product obtained is characterized by delayed onset of rigidity, rapid development of resistance and high resistance, and is used in particular as an injection mortar.
Inventors
- 👤 Thomas Koslowski
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 00:33
CPC Classifications
E; E04; E04F; E04F15/00; E04F15/12; A; A01; A01K; A01K1/00; A01K1/015; A01K1/0152; A01K1/0154; C; C01; C01F; C01F11/00; C01F11/46; C01F11/466; C04; C04B; C04B11/00; C04B11/02; C04B11/024; C04B11/26; C04B11/268; C04B18/00; C04B18/02; C04B18/027; C04B22/00; C04B22/08; C04B22/14; C04B22/142; C04B22/143; C01P; C01P2006/00; C01P2006/14
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
141 words
A process for preparing calcium sulfate alpha hemihydrate in granular form having a specific surface area of 1200 to 4000 cm 2 /g, which comprises the steps of: (a) milling crystalline calcium sulfate alpha hemihydrate to obtain a granular calcium sulfate alpha hemihydrate having a specific surface area of 1200 to 4000 cm 2 /g; (b) screening the granular calcium sulfate alpha hemihydrate produced during step (a) to eliminate coarser and finer grains, after said screening said product having a specific surface area of 1200 to 4000 cm 2 /g and particle size greater than 0.03 mm; and (c) admixing 0.005 to 0.05% of at least one fruit acid selected from the group consisting of malic acid, tartaric acid, citric acid, and their salts and monohydrates, with the ground and screened calcium sulfate alpha hemihydrate produced during steps (a) and (b).
Claim 2
Dependent Claim
141 words
A process for preparing calcium sulfate alpha hemihydrate in granular form having a specific surface area of 1200 to 4000 cm 2 /g, which comprises the steps of: (a) milling crystalline calcium sulfate alpha hemihydrate to obtain a granular calcium sulfate alpha hemihydrate having a specific surface area of 1200 to 4000 cm 2 /g; (b) screening the granular calcium sulfate alpha hemihydrate produced during step (a) to eliminate coarser and finer grains, after said screening said product having a specific surface area of 1200 to 4000 cm 2 /g and particle size greater than 0.03 mm; and (c) admixing 0.005 to 0.05% of at least one fruit acid selected from the group consisting of malic acid, tartaric acid, citric acid, and their salts and monohydrates, with the ground and screened calcium sulfate alpha hemihydrate produced during steps (a) and (b).
Claim 3
Dependent Claim
24 words
Process according to claim 1, wherein the screening step achieves a hemihydrate having a specific surface approximately between 1500 and 3500 cm 2 /g.
Claim 4
Dependent Claim
21 words
Process according to claim 1, wherein the fruit acids are admixed in an amount of from 0.005 to 0.02% by mass.
Claim 5
Dependent Claim
13 words
Process according to claim 1, wherein the fruit acid is citric acid monohydrate.
Claim 6
Dependent Claim
14 words
Process according to claim 1, wherein the fruit acids are admixed as fine particles.
Claim 7
Dependent Claim
39 words
Process according to claim 1, further comprising adding to the milled calcium sulfate alpha hemihydrate a growth-influencing additive selected from the group consisting of finely ground brown coal, finely ground peat, finely ground wood, humic acid, and wood components.
Claim 8
Dependent Claim
32 words
Process according to claim 1, wherein the crystalline calcium sulfate alpha hemihydrate has been produced from calcium sulfate dihydrate from a flue-gas desulfurization installation of a power plant running on brown coal.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1995-03-03 | 1995-09-02 | 1996-03-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-03-03 | 1999-09-02 | 2000-03-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-03-03 | 2003-09-02 | 2004-03-03 | $7700.00 | Window Closed / Lapsed |