US4127641A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the preparation of precipitated silicas having morphology similar to pyrogenic silicas
Assignee: Ineos Silicas Ltd
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Filing: 1977-06-22
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Granted: 1978-11-28
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Expires: 1997-06-22
Abstract
Abstract A multistage precipitation and flocculation production process is disclosed in which primary silica particles are prepared and flocculated useing an alkali metal salt solution and further silica precipitated in the presence of the salt, the pH of the mixture reduced and the silica isolated, purified carefully dried and optionally milled.
Inventors
- 👤 Derek Aldcroft
- 👤 Donald Barby
- 👤 Anthony L. Lovell
- 👤 James P. Quinn
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 21:03
CPC Classifications
C; C09; C09C; C09C1/00; C09C1/28; C09C1/30; C09C1/3009; C09C1/3027; C01; C01B; C01B33/00; C01B33/113; C01B33/12; C01B33/18; C01B33/187; C01B33/193; C08; C08K; C08K3/00; C08K3/34; C08K3/36; C01P; C01P2004/00; C01P2004/50; C01P2004/51; C01P2004/52; C01P2004/60; C01P2004/61; C01P2006/00; C01P2006/10; C01P2006/12; C01P2006/21; C01P2006/90
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
238 words
A process for the preparation of a precipitated silica having an ignition weight loss of at least 3% between 120° C and 1000° C and a strength such that a sample of the silica having a weight mean particle size on a substantially unimodal distribution in the size range 10-20 microns requires less than 6500 joules of ultrasonic energy to reduce the weight mean particle size of the sample to below 3 microns and which silica, after fluid energy milling, has a performance index of at least 7, said process comprising the steps of: (a) reacting an aqueous alkali metal silicate and an acid to form primary silica particles by simultaneously adding to water, under mixing conditions, at a temperature between 85° C and the boiling point of the reaction mixture, the silicate and the acid to a degree of silicate neutralization and a concentration of SiO 2 as indicated in Area A in the drawing, (b) flocculating the primary silica particles produced by the addition of an effective amount of an alkali metal salt flocculant, (c) precipitating secondary silica in the presence of the salt by the addition of more acid or more silicate and acid to obtain a final mixture, (d) reducing the pH of the final mixture to below 7, and (e) isolating the silica so produced and spray drying it at a temperature such that the temperature of the silica never exceeds 450° C.
Claim 2
Dependent Claim
238 words
A process for the preparation of a precipitated silica having an ignition weight loss of at least 3% between 120° C and 1000° C and a strength such that a sample of the silica having a weight mean particle size on a substantially unimodal distribution in the size range 10-20 microns requires less than 6500 joules of ultrasonic energy to reduce the weight mean particle size of the sample to below 3 microns and which silica, after fluid energy milling, has a performance index of at least 7, said process comprising the steps of: (a) reacting an aqueous alkali metal silicate and an acid to form primary silica particles by simultaneously adding to water, under mixing conditions, at a temperature between 85° C and the boiling point of the reaction mixture, the silicate and the acid to a degree of silicate neutralization and a concentration of SiO 2 as indicated in Area A in the drawing, (b) flocculating the primary silica particles produced by the addition of an effective amount of an alkali metal salt flocculant, (c) precipitating secondary silica in the presence of the salt by the addition of more acid or more silicate and acid to obtain a final mixture, (d) reducing the pH of the final mixture to below 7, and (e) isolating the silica so produced and spray drying it at a temperature such that the temperature of the silica never exceeds 450° C.
Claim 3
Dependent Claim
32 words
A process as claimed in claim 1, in which the aqueous alkali metal silicate solution and acid are reacted to a degree of neutralization as indicated in Area B of the drawing.
Claim 4
Dependent Claim
17 words
A process as claimed in claim 1, in which the alkali metal salt used is sodium chloride.
Claim 5
Dependent Claim
26 words
A process as claimed in claim 3, in which the sodium chloride is added to produce a mixture containing 0.3-2.0 gms NaCl/g of SiO 2 .
Claim 6
Dependent Claim
21 words
A process as claimed in claim 1, in which the pH of the final mixture is reduced to 4 or below.
Claim 7
Dependent Claim
17 words
A process as claimed in claim 1, which comprises the additional step of milling the dried silica.
Claim 8
Dependent Claim
21 words
A process for the preparation of a silica as claimed in claim 6 in which the milling is fluid energy milling.
Claim 9
Dependent Claim
14 words
A process as claimed in claim 1 in which the acid is sulphuric acid.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-11-27 | 1982-05-29 | 1982-11-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-11-27 | 1986-05-29 | 1986-11-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-11-27 | 1990-05-29 | 1990-11-28 | $7700.00 | Window Closed / Lapsed |