Patent US4654172A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4654172A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for processing radioactive waste resin

Assignee: Hitachi Ltd
•
Filing: 1984-05-23
•
Granted: 1987-03-31
•
Expires: 2004-05-23
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A method of processing radioactive waste resin by pyrolyzing radioactive waste ion exchange resin generated in a nuclear plant such as a nuclear power station. First, the ion exchange resin is pyrolyzed at a low temperature, and the resulting decomposition gas is separated. Second, the ion exchange resin at a high temperature, and the resulting decomposition gas is separated. Finally, the residue of the ion exchange resin is hot-pressed into a molded article.

Inventors

  • 👤 Masami Matsuda
  • 👤 Yoshiyuki Aoyama
  • 👤 Fumio Kawamura
  • 👤 Hideo Yusa
  • 👤 Makoto Kikuchi
  • 👤 Shin Tamata
  • 👤 Susumu Horiuchi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 08:31
CPC Classifications
G; G21; G21F; G21F9/00; G21F9/04; G21F9/06; G21F9/14; C; C07; C07C; C07C29/00; C07C29/16; C07C31/00; C07C31/02; C07C31/10; Y; Y10; Y10S; Y10S159/00; Y10S159/12

Claims Analysis

Total Claims: 26
Claim 1
Independent Claim 102 words
A method of processing radioactive waste resin by pyrolyzing radioactive waste ion exchange resin generated in a nuclear plant in a reaction vessel, comprising pyrolyzing said ion exchange resin without the presence of oxygen at low temperatures between 120° C. and 350° C. in the same reaction vessel, separating the resulting decomposition gas, then pyrolyzing said ion exchange resin in the presence of oxygen at high temperatures between 350° C. and 600° C. in the same reaction vessel, separating the resulting decomposition gas, and thereafter hot-pressing the residue of said ion exchange resin into a molded article in the same reaction vessel.
Claim 2
Independent Claim 102 words
A method of processing radioactive waste resin by pyrolyzing radioactive waste ion exchange resin generated in a nuclear plant in a reaction vessel, comprising pyrolyzing said ion exchange resin without the presence of oxygen at low temperatures between 120° C. and 350° C. in the same reaction vessel, separating the resulting decomposition gas, then pyrolyzing said ion exchange resin in the presence of oxygen at high temperatures between 350° C. and 600° C. in the same reaction vessel, separating the resulting decomposition gas, and thereafter hot-pressing the residue of said ion exchange resin into a molded article in the same reaction vessel.
Claim 3
Dependent Claim 26 words
A method of processing radioactive waste resin as defined in claim 1, wherein the pyrolyzing at a high temperature is effected while supplying an oxidizing agent.
Claim 4
Dependent Claim 18 words
A method of processing radioactive waste resin as defined in claim 2, wherein said oxidizing agent is air.
Claim 5
Dependent Claim 31 words
A method of processing radioactive waste resin as defined in claim 3, wherein the average velocity of the air supplied from outside is up to 1.5 cm/s within the reaction vessel.
Claim 6
Dependent Claim 41 words
A method of processing radioactive waste resin as defined in claim 1, wherein said hot-pressing is effected while at least part of said residue is being fused or softened by the pyrolysis at high temperatures between 350° C. and 600° C.
Claim 7
Dependent Claim 33 words
A method of processing radioactive waste resin as defined in claim 5, wherein said hot-pressing is effected immediately after the pyrolysis at a high temperature while the temperature is being kept as such.
Claim 8
Dependent Claim 33 words
A method of processing radioactive waste resin as defined in claim 1, wherein the pyrolysis at a high temperature is effected in the presence of a vitrifying agent which adsorbs volatile radioactive substances.
Claim 9
Dependent Claim 27 words
A method of processing radioactive waste resin as defined in claim 7, wherein said vitrifying agent is added before the pyrolysis at a low temperature is effected.
Claim 10
Dependent Claim 25 words
A method of processing radioactive waste resin as defined in claim 7, wherein said vitrifying agent is glass frit comprising silica as its principal component.
Claim 11
Independent Claim 229 words
A method of processing radioactive ion exchange resins into stable and safely storable forms comprising the steps of: a. introducing a quantity of radioactive ion exchange resin into a sealed reaction vessel; b. heating the radioactive ion exchange resin in the sealed reaction vessel without the presence of oxygen to a temperature sufficient to remove the ion exchange group from the radioactive ion exchange resin but insufficient to decompose the polymer backbone of the radioactive ion exchange resin and insufficient to initiate the spattering of the radioactive material; c. removing the gases produced by the heating of the radioactive ion exchange resin from the reaction vessel and introducing said gases to an exhaust gas processing apparatus; d. inserting an oxygen-containing gas into the reaction vessel at a velocity insufficient to initiate the spattering of the radioactive material; e. heating the remaining radioactive resin and the oxygen-containing gas in the reaction vessel to a temperature sufficient to decompose the polymer backbone of the remaining radioactive resin; f. removing the gases produced by the heating of the radioactive resin and the oxygen containing gas from the reaction vessel; g. hot-pressing the remaining radioactive residue while within the reaction vessel into a molded article at a temperature substantially similar to that of the heating of the radioactive resin; and, h. removing the molded article containing the radioactive residue from the reaction vessel.
Claim 12
Independent Claim 229 words
A method of processing radioactive ion exchange resins into stable and safely storable forms comprising the steps of: a. introducing a quantity of radioactive ion exchange resin into a sealed reaction vessel; b. heating the radioactive ion exchange resin in the sealed reaction vessel without the presence of oxygen to a temperature sufficient to remove the ion exchange group from the radioactive ion exchange resin but insufficient to decompose the polymer backbone of the radioactive ion exchange resin and insufficient to initiate the spattering of the radioactive material; c. removing the gases produced by the heating of the radioactive ion exchange resin from the reaction vessel and introducing said gases to an exhaust gas processing apparatus; d. inserting an oxygen-containing gas into the reaction vessel at a velocity insufficient to initiate the spattering of the radioactive material; e. heating the remaining radioactive resin and the oxygen-containing gas in the reaction vessel to a temperature sufficient to decompose the polymer backbone of the remaining radioactive resin; f. removing the gases produced by the heating of the radioactive resin and the oxygen containing gas from the reaction vessel; g. hot-pressing the remaining radioactive residue while within the reaction vessel into a molded article at a temperature substantially similar to that of the heating of the radioactive resin; and, h. removing the molded article containing the radioactive residue from the reaction vessel.
Claim 13
Dependent Claim 40 words
A method of processing radioactive ion exchange resin as defined in claim 10, wherein the heating of the radioactive ion exchange resin in the reaction vessel without the pressure of oxygen occurs at a temperature of 350° C. or below.
Claim 14
Dependent Claim 37 words
A method of processing radioactive ion exchange resin as defined in claim 10, wherein the heating of the radioactive resin and the oxygen-containing gas in the reaction vessel occurs at a temperature of 350° C. or above.
Claim 15
Independent Claim 33 words
A method of processing radioactive ion exchange resin as defined in claims 10, wherein the inserting of an oxygen-containing gas into the reaction vessel is at a velocity of 1.5 cm/s or below.
Claim 16
Dependent Claim 40 words
A method of processing radioactive ion exchange resin as defined in claim 10, wherein the gases produced by the heating of the radioactive ion exchange resin in the reaction vessel without the pressure of oxygen are sulfur and nitrogen oompounds.
Claim 17
Dependent Claim 35 words
a method of processing radioactive ion exchange resin as defined in claim 14, wherein the gases of the sulfur and nitrogen compounds are SO x , H 2 S, NO x and NH 4 .
Claim 18
Dependent Claim 52 words
A method of processing radioactive ion exchange resin as defined in claim 10, wherein the exhaust gas processing apparatus is an alkali scrubber which converts the gases produced by the heating of the radioactive ion exchange resin in the reaction vessel without the presence of oxygen, into aqueous solutions of sodium salts.
Claim 19
Dependent Claim 43 words
A method of processing radioactive ion exchange resin as defined in claim 10, wherein the gases produced by the heating of the radioactive resin and the oxygen-containing gas in the reaction vessel are CO 2 , CO, H 2 and CH 4 .
Claim 20
Dependent Claim 41 words
A method of processing radioactive ion exchange resin as defined in claim 17, wherein the CO 2 , CO, H 2 and CH 4 gases are introduced to a flame stack and burnt producing CO 2 and H 2 O gases.
Claim 21
Dependent Claim 41 words
A method of processing radioactive ion exchange resin as defined in claim 11, wherein the heating of the radioactive ion exchange resin in the reaction vessel without the presence of oxygen occurs at a temperature between 120° C. and 350° C.
Claim 22
Dependent Claim 36 words
A method of processing radioactive ion exchange resin as defined in claim 19, wherein the heating of the radioactive ion exchange resin in the reaction vessel without the presence of oxygen occurs at about 300° C.
Claim 23
Dependent Claim 38 words
A method of processing radioactive ion exchange resin as defined in claim 12, wherein the heating of the radioactive ion exchange resin and the oxygen-containing gas in the reaction vessel occurs at a temperature of about 600° C.
Claim 24
Dependent Claim 59 words
A method of processing radioactive ion exchange resin as defined in claim 10, wherein said hot-pressing occurs immediately after the heating of the remaining radioactive resin and the oxygen-containing gas in the reaction vessel to a temperature sufficient to decompose the polymer backbone of the remaining radioactive resin, which the temperature of the reaction vessel is maintained as such.
Claim 25
Dependent Claim 56 words
A method of processing radioactive ion exchange resin as defined in claim 10, wherein the heating of the remaining radioactive resin and the oxygen-containing gas in the reaction vessel to a temperature sufficient to decompose the polymer backbone of the remaining radioactive resin occurs in the presence of a vitrifying agent which absorbs volatile radioactive substances.
Claim 26
Dependent Claim 21 words
A method of processing radioactive waste resin as defined in claim 23, wherein said vitrifying agent is added prior to heating.

References Cited (Backward Citations)

GB837967A Cited
US3954661A Cited
US4235738A Cited
US4053432A Cited
US4152287A Cited
DE2753368A1 Cited
US4242220A Cited
JPS5594199A Cited
JPS5730000A Cited
US4460500A Cited
US4499833A Cited
EP0125381A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-03-30 1990-09-29 1991-03-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-03-30 1994-09-29 1995-03-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-03-30 1998-09-29 1999-03-31 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag