U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Recovery of anhydrous hydrogen fluoride from depleted uranium hexafluoride

Patent 5346684 Issued on September 13, 1994. Estimated Expiration Date: Icon_subject January 21, 2013. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

3168369

3333930

3765844

3845193

3906081

Method of recovering HF from mixtures containing C1 -C3 halocarbon compounds
Patent #: 3947558
Issued on: 03/30/1976
Inventor: van Eijl

Production of sized particles of uranium oxides and uranium oxyfluorides
Patent #: 3978194
Issued on: 08/31/1976
Inventor: Knudsen ,   et al.

Production of uranium dioxide
Patent #: 4020146
Issued on: 04/26/1977
Inventor: Knudsen

Production of uranium dioxide
Patent #: 4053559
Issued on: 10/11/1977
Inventor: Hart ,   et al.

Conversion of uranium hexafluoride to oxides of uranium
Patent #: 4397824
Issued on: 08/09/1983
Inventor: Butler ,   et al.

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Inventor

Assignee

Application

No. 007016 filed on 01/21/1993

US Classes:

423/488, Recovery or purification423/472, Ternary compound423/483, Hydrogen fluoride423/484, From impure starting material423/489Binary fluorine containing compound

Examiners

Primary: Fuller, Benjamin R.
Assistant: Lund, Valerie

Attorney, Agent or Firm

International Classes

C01B 007/19
C01B 009/08

Abstract

A method is provided for recovering an anhydrous hydrogen fluoride product from uranium hexafluoride gas by initially reacting the uranium hexafluoride in a primary reactor with steam to produce a uranyl fluoride intermediate and a gaseous mixture of hydrogen fluoride and water. The uranyl fluoride intermediate is fed to a secondary reactor and reacted with water to produce a triuranium octoxide product for disposal, and a gaseous mixture of water, hydrogen fluoride and oxygen. The two mixtures from the primary and secondary reactors are combined and subsequently separated in a distillation column to obtain an anhydrous hydrogen fluoride product stream and an aqueous azeotropic recycle stream containing water and hydrogen fluoride which is vaporized and returned to the primary reactor as the steam feed.

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