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US3940261A
Expired / Lapsed
US
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Process for preparing crystalline silver particles having electrically conductive surfaces and product
Assignee: Permabond International Corp
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Filing: 1975-02-03
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Granted: 1976-02-24
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Expires: 1995-02-03
Abstract
Abstract Processes are disclosed for preparing large crystalline silver particles having exceptionally conductive surfaces. The particles may be prepared by the reduction of a water soluble silver salt in an acidified aqueous solution by a redox reaction. Silver particles having conductive surfaces may also be prepared by treating commercial silver powder with a phenolic reducing compound such as hydroquinone dissolved in a polar solvent such as a lower alcohol. The silver powders obtained by the processes have very low electrical contact resistance and furthermore retain this low contact resistance even though the powders are exposed to air and airborne contaminants.
Inventors
- 👤 Clarence C. Dannelly
- 👤 John M. McIntire
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 22:27
CPC Classifications
C; C01; C01G; C01G5/00; C01G5/003; B; B22; B22F; B22F9/00; B22F9/16; B22F9/18; B22F9/24; C22; C22B; C22B11/00; C22B11/04; C22B3/00; C22B3/20; C22B3/26; C22B3/262; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
165 words
Process for the reduction of water soluble silver salts to prepare crystalline silver particles ranging in size from about 10-100 microns, the silver particles being characterized by exceptionally clean, bright, electrically conductive surfaces, said process comprising reducing a water soluble silver salt in a redox reaction at a temperature of about 0° to about 50°C. for about 2 to 24 hours, said silver salt being present as an aqueous solution in a concentration of about 0.25-1.0 mole per liter of water, dilute nitric acid being present in the amount of 0.1 to 3 ml. per liter of silver salt solution, and a reducing agent characterized by an oxidation potential within -0.150 volts of the silver salt under the conditions of the reaction solution, solubility of about 0.025 or more moles per liter of water at 25°C., and being present in a concentration of 1 to 1.25 molar equivalents, based on the silver ion to be reduced, dissolved in about 0.5 to 2 liters of water.
Claim 2
Dependent Claim
165 words
Process for the reduction of water soluble silver salts to prepare crystalline silver particles ranging in size from about 10-100 microns, the silver particles being characterized by exceptionally clean, bright, electrically conductive surfaces, said process comprising reducing a water soluble silver salt in a redox reaction at a temperature of about 0° to about 50°C. for about 2 to 24 hours, said silver salt being present as an aqueous solution in a concentration of about 0.25-1.0 mole per liter of water, dilute nitric acid being present in the amount of 0.1 to 3 ml. per liter of silver salt solution, and a reducing agent characterized by an oxidation potential within -0.150 volts of the silver salt under the conditions of the reaction solution, solubility of about 0.025 or more moles per liter of water at 25°C., and being present in a concentration of 1 to 1.25 molar equivalents, based on the silver ion to be reduced, dissolved in about 0.5 to 2 liters of water.
Claim 3
Dependent Claim
11 words
Process of claim 1, wherein said silver salt is silver nitrate.
Claim 4
Dependent Claim
8 words
Product produced by the process of claim 1.
Claim 5
Dependent Claim
201 words
Process for the reduction of silver nitrate to prepare crystalline silver particles ranging in size from about 10-100 microns, the silver particles being characterized by exceptionally clean, bright, electrically conductive surfaces, said process comprising: a. preparing an aqueous solution of silver nitrate, the concentration of said silver nitrate being in the range of about 0.25-1.0 mole per liter of water; b. adding dilute nitric acid in the ratio of about 0.1 to 3.0 ml. per liter of said aqueous solution; c. preparing an aqueous solution of reducing agent characterized by a oxidation within -0.150 of the silver salt under the conditions of the reaction solution, solubility of at least about 0.25 mole per liter at 25°C., and being present in the concentration of 1 to 1.25 molar equivalents, based on the silver nitrate, dissolved in about 0.5 to 2 liters of water; d. blending said aqueous solution of reducing agent and said aqueous solution of silver nitrate to thereby reduce said silver nitrate in a redox reaction, said reaction being at a temperature of about 0-50°C. for about 2 to 24 hours; e. filtering and washing said silver particles until the filtrate is essentially clear, and f. drying said silver particles.
Claim 6
Dependent Claim
201 words
Process for the reduction of silver nitrate to prepare crystalline silver particles ranging in size from about 10-100 microns, the silver particles being characterized by exceptionally clean, bright, electrically conductive surfaces, said process comprising: a. preparing an aqueous solution of silver nitrate, the concentration of said silver nitrate being in the range of about 0.25-1.0 mole per liter of water; b. adding dilute nitric acid in the ratio of about 0.1 to 3.0 ml. per liter of said aqueous solution; c. preparing an aqueous solution of reducing agent characterized by a oxidation within -0.150 of the silver salt under the conditions of the reaction solution, solubility of at least about 0.25 mole per liter at 25°C., and being present in the concentration of 1 to 1.25 molar equivalents, based on the silver nitrate, dissolved in about 0.5 to 2 liters of water; d. blending said aqueous solution of reducing agent and said aqueous solution of silver nitrate to thereby reduce said silver nitrate in a redox reaction, said reaction being at a temperature of about 0-50°C. for about 2 to 24 hours; e. filtering and washing said silver particles until the filtrate is essentially clear, and f. drying said silver particles.
Claim 7
Dependent Claim
8 words
Product produced by the process of claim 4.
Claim 8
Dependent Claim
41 words
Process for preparing silver powder having bright electrically conductive surfaces comprising treating silver powder with a phenolic reducing compound dissolved in a polar organic solvent, the solute/solvent ratio being in the range of 0.1/1.00 to 10/100, and collecting the treated silver.
Claim 9
Dependent Claim
41 words
Process for preparing silver powder having bright electrically conductive surfaces comprising treating silver powder with a phenolic reducing compound dissolved in a polar organic solvent, the solute/solvent ratio being in the range of 0.1/1.00 to 10/100, and collecting the treated silver.
Claim 10
Dependent Claim
18 words
Process of claim 6 wherein said phenolic reducing compound is hydroquinone and said polar organic solvent is methanol.
Claim 11
Dependent Claim
8 words
Product produced by the process of claim 6.
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) | 1979-02-23 | 1979-08-25 | 1980-02-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-02-23 | 1983-08-25 | 1984-02-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-02-23 | 1987-08-25 | 1988-02-24 | $7700.00 | Window Closed / Lapsed |