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US4710266A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus for subjecting a radioactive sodium borate waste solution to volume reduction and solidification

Assignee: Ebara Corp
•
Filing: 1986-03-20
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Granted: 1987-12-01
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Expires: 2006-03-20
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Abstract

Abstract An apparatus is disclosed for producing a vitric solid solution comprising mainly the solid content of a radioactive waste solution of sodium borate discharged from a pressurized water reactor, the apparatus comprising a waste solution feed tank equipped with a hopper for stabilizing agent in water, a thin film evaporator, a heating type dehydrator, a powder drier connected with a microwave generator through a microwave guide tube and equipped with a stirrer, and a melting furnace connected with a microwave generator through a microwave guide tube, the above units being combined by pipes or a powder-transferring means.

Inventors

  • 👤 Tadamasa Hayashi
  • 👤 Toyoshi Mizushima

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 08:00
CPC Classifications
C; C03; C03C; C03C1/00; C03C1/002; G; G21; G21F; G21F9/00; G21F9/28; G21F9/30; G21F9/301; G21F9/302; G21F9/305; Y; Y10; Y10S; Y10S159/00; Y10S159/12; Y10S422/00; Y10S422/903

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 399 words
An apparatus for producing a vitric solid solution comprising (a) the solid content of a radioactive waste solution of sodium borate discharged from a pressurized water reactor, having a Na 2 O to B 2 O 3 molar ratio of 0.1 to 0.06 and (b) 10 to 40 mole % of ZnO or 10 to 40 mole % of ZnO plus 3 to 10 mole % of Al 2 O 3 and/or CaO so that the total content of ZnO plus Al 2 O 3 and/or CaO does not exceed 43 mole %, the apparatus comprising: (A) a waste solution feed tank equipped with a hopper for stabilizing agent in water, a stirrer for stirring the sodium borate waste solution and the stabilizing agent in water added thereto from said hopper; (B) a waste solution circulation pump for circulating a part of the resulting mixture to the waste solution feed tank and another part of the resulting mixture to an evaporator through a waste solution supply pump; (C) the evaporator for evaporating and concentrating the waste solution fed from the pump to remove water by a heating fluid so as to form an evaporator residue; (D) a heating type dehydrator for heating the evaporator residue sent from the evaporator by a heating fluid while being stirred by a stirrer, for further evaporation; (E) a powder dryer for removing the crystal water of the evaporation residue, thereby rendering said residue as a porous lump, by heating with a microwave generator through a microwave guide tube, and a stirrer for grinding the lump into a powder provided therein; (F) discharger means for forcible batch delivery of said residue to said powder dryer; (G) a melting furnace for melting into a vitric melt the dried power sent from the powder dryer by irradiation with microwaves transmitted from a microwave generator through a microwave guide tube, said melt being charged in a solid solution container; (H) a condenser for condensing the evaporated water generated from the evaporator and the heating type dehydrator; (I) a prefilter for filtering the off-gas from the powder dryer and the melting furnace to remove solids; (J) an off-gas cooler for removing the residual water of the off-gas from the waste solution feed tank, the condenser and the prefilter; (K) an off-gas treater for purifying the off-gas from the off-gas cooler to discharge it from an off-gas exhaust fan.
Claim 2
Independent Claim 399 words
An apparatus for producing a vitric solid solution comprising (a) the solid content of a radioactive waste solution of sodium borate discharged from a pressurized water reactor, having a Na 2 O to B 2 O 3 molar ratio of 0.1 to 0.06 and (b) 10 to 40 mole % of ZnO or 10 to 40 mole % of ZnO plus 3 to 10 mole % of Al 2 O 3 and/or CaO so that the total content of ZnO plus Al 2 O 3 and/or CaO does not exceed 43 mole %, the apparatus comprising: (A) a waste solution feed tank equipped with a hopper for stabilizing agent in water, a stirrer for stirring the sodium borate waste solution and the stabilizing agent in water added thereto from said hopper; (B) a waste solution circulation pump for circulating a part of the resulting mixture to the waste solution feed tank and another part of the resulting mixture to an evaporator through a waste solution supply pump; (C) the evaporator for evaporating and concentrating the waste solution fed from the pump to remove water by a heating fluid so as to form an evaporator residue; (D) a heating type dehydrator for heating the evaporator residue sent from the evaporator by a heating fluid while being stirred by a stirrer, for further evaporation; (E) a powder dryer for removing the crystal water of the evaporation residue, thereby rendering said residue as a porous lump, by heating with a microwave generator through a microwave guide tube, and a stirrer for grinding the lump into a powder provided therein; (F) discharger means for forcible batch delivery of said residue to said powder dryer; (G) a melting furnace for melting into a vitric melt the dried power sent from the powder dryer by irradiation with microwaves transmitted from a microwave generator through a microwave guide tube, said melt being charged in a solid solution container; (H) a condenser for condensing the evaporated water generated from the evaporator and the heating type dehydrator; (I) a prefilter for filtering the off-gas from the powder dryer and the melting furnace to remove solids; (J) an off-gas cooler for removing the residual water of the off-gas from the waste solution feed tank, the condenser and the prefilter; (K) an off-gas treater for purifying the off-gas from the off-gas cooler to discharge it from an off-gas exhaust fan.
Claim 3
Dependent Claim 55 words
An apparatus for producing a vitric solid solution according to claim 1, wherein a cooler is attached to the melting furnace for cooling the melt successively discharged from the melting furnace to the vitric solid solution and wherein the off-gas from the cooler is sent to the prefilter for filtering said off-gas to remove solids.
Claim 4
Dependent Claim 55 words
An apparatus for producing a vitric solid solution according to claim 1, wherein, at the outlet side of the melting furnace for a vitric solid solution melt, there are provided a heater for prevention of rapid cooling of containers filled with the vitric melt as well as a slow cooling chamber for the containers 24.
Claim 5
Dependent Claim 28 words
An apparatus for producing a vitric solid solution according to claim 1, wherein the melting furnace includes a container as a lower half for receiving said vitric melt.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-11-30 1991-06-01 1991-12-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-11-30 1995-06-01 1995-12-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-11-30 1999-06-01 1999-12-01 $7700.00 Window Closed / Lapsed

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