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US3647420A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing high-purity niobium and tantalum

Assignee: H.C. Starck GmbH
•
Filing: 1969-06-04
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Granted: 1972-03-07
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Expires: 1989-06-04
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Abstract

Abstract A process for producing high-purity niobium and tantalum wherein the oxide of the metal is intimately mixed with carbon, e.g., fine graphite, in an amount such that the oxygen is present in a slight excess beyond the quantity of carbon required to react stoichiometrically with the metal oxide. In the first stage, the mixture is subjected to a high vacuum at the order of 10 4 torr. at a temperature of about 1,800* C. to carry out an initial reduction, the reduced material containing about 500 to 10,000 parts per million (p.p.m.) of oxygen. In an intermediate stage, the partly reduced product is combined with finely divided carbon pyrolytically precipitated from a hydrocarbon in a retort permeable to hydrogen (at elevated temperature), so that the carbon is uniformly distributed over the surface of the partly reduced product. In the second state, the mixture of the partially reduced product and the finely divided pyrolytically precipitated carbon is subjected to a temperature below to 2,000* C. and nevertheless sufficient to effect a final reduction. Preferably the latter temperature is about 1,700* C. The resulting high-purity metal (i.e., tantalum or niobium), may be used in electrolytic capacitors.

Inventors

  • 👤 Attilio Restelli

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 20:36
CPC Classifications
C; C22; C22B; C22B34/00; C22B34/20; C22B34/24; B; B22; B22F; B22F9/00; B22F9/16; B22F9/18; B22F9/20

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 23 words
The process defined in claim 1 wherein said prereduced product is reacted with said hydrocarbon at a temperature between 700* and 1,000* C.
Claim 2
Dependent Claim 32 words
The process defined in claim 2 wherein said prereduced product is reacted with said hydrocarbon in a sealed reaction vessel having a hydrogen-permeable wall at a temperature of 700* to 1,000* C.
Claim 3
Dependent Claim 15 words
The process defined in claim 3 wherein said reaction vessel is composed of nickel-chromium-iron alloy.
Claim 4
Dependent Claim 29 words
The process defined in claim 3 wherein said hydrocarbon is a paraffinic alkane of the general formula CnH(2n 2) where n is an integer ranging between 1 and 8.
Claim 5
Dependent Claim 47 words
The process defined in claim 5 wherein steps (a) and (c) are each carried out at a temperature below 2,000* C. 7 The process defined in claim 6 wherein steps (a) and (c) are each carried out at a pressure of the order of 10 4 torr.
Claim 6
Dependent Claim 19 words
The process defined in claim 7 wherein step (c) is carried out at a temperature of about 1,700* C.

References Cited (Backward Citations)

US26294A Cited
US3231408A Cited
US3144328A Cited
US3114629A Cited
US3415639A Cited
US3499753A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-03-07 1975-09-06 1976-03-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-03-07 1979-09-06 1980-03-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-03-07 1983-09-06 1984-03-07 $7700.00 Window Closed / Lapsed

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