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US4285830A Expired / Lapsed US ⏱️ 0.0 years remaining

Method and apparatus for reconditioning waste solutions of the nuclear industry which contain ammonium nitrate

Assignee: Forschungszentrum Jülich
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Filing: 1978-11-30
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Granted: 1981-08-25
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Expires: 1998-11-30
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Abstract

Abstract A method and apparatus for reconditioning waste solutions of the nuclear ustry which contain ammonium nitrate. The waste solution is continuously sprayed from above into a 300° to 600° C. hot zone, from the lower end of which the decomposition products are withdrawn and are separated into condensate and exhaust gas. The NO content is reduced by adding oxygen, especially at the exit of the decomposition zone. By the presence of reducing agents, such as CO(NH 2 ) 2 or preferably NH 3 , in the solution to be sprayed, the NO 2 content of the decomposition products and the NH 4 NO 3 residue in the condensate can be practically eliminated and an additional precipitation in the condensate which can be filtered off can be obtained. Optimal contents are 0.25-0.4 Mol NH 3 and 0.15-0.25 Mol CO(NH 2 ) 2 per Mol NH 4 NO 3 . Prior to the thermal decomposition, the waste solution is preferably concentrated, cooled off, and filtered to about 60% or (if a solution containing reducing agents is to be sprayed) about 48% NH 4 NO 3 at about 60° C. in a thin layer evaporator, and is temporarily stored at room temperature. The addition of ammonia to the concentrate offers a precipitation which can be filtered off.

Inventors

  • 👤 Burkhardt Muller

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 22:37
CPC Classifications
G; G21; G21F; G21F9/00; G21F9/04; G21F9/06; Y; Y10; Y10S; Y10S159/00; Y10S159/12

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 100 words
A method of treating waste solutions which are produced during the production of fuel and breeder material for nuclear reactors and which contain about 60 weight percent ammonium nitrate which method comprises the steps of: continuously spraying waste solution containing about 60% ammonium nitrate into an ammonium nitrate decomposition furnace for essential decomposition; and subjecting the decomposition products formed during said spraying step to condensation to enable separation of said decompositions products into a liquid and a gaseous phase; and supplying a quantity of oxygen, equivalent to the NO content of the decomposition products, to the ammonium nitrate decomposition zone.
Claim 2
Independent Claim 100 words
A method of treating waste solutions which are produced during the production of fuel and breeder material for nuclear reactors and which contain about 60 weight percent ammonium nitrate which method comprises the steps of: continuously spraying waste solution containing about 60% ammonium nitrate into an ammonium nitrate decomposition furnace for essential decomposition; and subjecting the decomposition products formed during said spraying step to condensation to enable separation of said decompositions products into a liquid and a gaseous phase; and supplying a quantity of oxygen, equivalent to the NO content of the decomposition products, to the ammonium nitrate decomposition zone.
Claim 3
Dependent Claim 40 words
A method according to claim 1, in which said decomposition furnace is vertically oriented, said waste solution is sprayed from above, into said furnace, and said decomposition products are removed through an exit in a lower region of said furnace.
Claim 4
Dependent Claim 19 words
A method according to claim 2, in which said oxygen is added at the exit of the decomposition furnace.
Claim 5
Dependent Claim 20 words
A method according to claim 1, in which the decomposition furnace operates at temperatures ranging from 300° to 600° C.
Claim 6
Dependent Claim 20 words
A method according to claim 4, in which the decomposition furnace operates at temperatures ranging from 350° to 450° C.
Claim 7
Dependent Claim 40 words
A method according to claim 1, which includes the step of adding 0.2 to 0.6 mole of ammonia per mole of ammonium nitrate or 0.1 to 0.5 mole of urea per mole of ammonium nitrate prior to said spraying step.
Claim 8
Dependent Claim 45 words
A method according to claim 1, which includes the steps of distilling off water from the liquid condensate phase of the condensed decomposition products, and selectively supplying the remainder of said condensate for fuel production and to said waste solution which is to be sprayed.
Claim 9
Dependent Claim 25 words
A method according to claim 1, which includes the step of concentrating said waste solution prior to said spraying step at temperatures below 100° C.
Claim 10
Dependent Claim 17 words
A method according to claim 12, in which said concentration step takes place at about 60° C.
Claim 11
Dependent Claim 25 words
A method according to claim 8, which includes the step of concentrating said waste solution in a thin layer evaporator prior to said spraying step.
Claim 12
Dependent Claim 23 words
A method according to claim 8, which includes the steps of concentrating and then filtering said waste solution prior to said spraying step.
Claim 13
Dependent Claim 27 words
A method according to claim 8, which includes the steps of concentrating said waste solution and then storing it at room temperature prior to said spraying step.

References Cited (Backward Citations)

US2968719A Cited
US3101258A Cited
US3191662A Cited
US3361649A Cited
DE1299610B Cited
US3862296A Cited
US3950216A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-08-24 1985-02-23 1985-08-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-08-24 1989-02-23 1989-08-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-08-24 1993-02-23 1993-08-25 $7700.00 Window Closed / Lapsed

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