METHOD FOR PROCESSING LIQUID RADIOACTIVE WASTE AND FOR THE RECOVERY THEREOF

Abstract

The invention relates to a technique for handling liquid radioactive waste from a nuclear fuel-energy cycle, and may be used in a process for processing liquid radioactive waste for maximally reducing the volume thereof and removing radionuclides by concentrating same in a solid phase. The aim is achieved by means of a method for processing liquid radioactive waste and for the recovery thereof, including waste oxidation, separating sludge, colloids and suspended particles from a liquid phase, and removing, from the liquid phase, radionuclides to be subsequently recovered using selective sorbents and filters; the method is characterized in that, prior to the stage for separating sludge, colloids and suspended particles from the liquid phase of the radioactive waste, selective sorbents in the form of powders are added and mixed into the liquid waste.

Claims

1. A method of processing of a liquid radioactive waste and its utilization, comprising: oxidizing of the waste, separating of a sludge, colloids and suspended particles from a liquid phase, and removing, from the liquid phase, radionuclides to be subsequently recovered using selective sorbents and filters; the method is characterized in that, prior to a stage of the sludge, colloids and suspended particles separating from the liquid phase of the radioactive waste, the selective sorbents in a form of powders are added and mixed into the liquid waste and then an obtained suspension is filtered by pumping through, at least one waste disposal container and provided with at least one filter element at its exit; the filter element separating insoluble substances from the liquid phase; then a filtrate is passed through at least one waste disposal reservoir with granulated selective sorbents; with said container and reservoir placed in concrete blocks.

2. The method of claim 1, wherein one or several selective sorbents are used in the liquid radioactive waste processing.

3. The method of claim 1, wherein the waste disposal container has two or more filter element.

4. The method of claim 1, wherein the obtained suspension passed through two or more waste disposal containers with the filter elements.

5. The method of claim 1, wherein the filtrate passed through two or more sequentially connected reservoirs with the granulated selective sorbents.

6. The method of claim 1, further comprising filling the reservoir containing the granulated selective sorbents with a high-penetrating cement mortar after the end of its use.

7. The method of claim 1, further comprising filling the containing insoluble substances removed from the liquid phase, with a high-penetrating cement mortar after the end of its use.

8. The method of claim 6, wherein prior to pouring the cement mortar the reservoir is vacuumized and/or heated with a hot air or an inert gas.

9. The method of claim 1, wherein a size of granules of the selective sorbents is in a range from 1 to 3 mm.

10. The method of claim 1, wherein a size of particles of the selective sorbents added in the form of powder is in a range from 0.1 to 0.7 mm.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0018] The principle of the invention is explained in FIG. 1 that presents a scheme of implementing the proposed method.

[0019] FIG. 1 shows:

[0020] 1. Tank for mixing LRW with inorganic selective sorbents in powder form.

[0021] 2. COREBRICK-F with 2 filter elements (50 microns and 5 microns).

[0022] 3. Ozone treatment unit.

[0023] 4. COREBRICK-F with 2 filter elements (5 microns and 0.5 microns).

[0024] 5. COREBRICK-C filled with selective sorbent.

[0025] 6. COREBRICK-C filled with selective sorbent.

[0026] COREBRICK-F is a concrete 1500×1500×1500 mm block containing a hollow 200 liter chamber and also featuring two filter elements sequentially installed at its exit.

[0027] COREBRICK-C is a concrete 1500×1500×1500 mm block containing a cylinder 40 liter reservoir with a selective sorbent.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

[0028] The suggested method mainly uses a composition comprising amorphous silicon dioxide from the Sukholozhsky deposit (with size of particles varying up to 500 microns). One or several selective sorbents and a coagulating substance (f.e. nickel sulfate) can be placed in its pores. Such composition helps to handle several challenges: [0029] remove part of radionuclides from the liquid phase and evenly distribute activity in filter elements and sorption blocks. [0030] mold suspended particles and colloids into solid fractions that can be separated easily, which simplifies the process of separating liquid LRW components from the solid ones and reduces the costs. [0031] Amorphous silicon dioxide is a rather light material (0.6 g/cm3). Its mesopores have a large volume and can hold one or several selective sorbents, which provide high availability of the sorption centers.

[0032] Practical implementation of this method implies the use of reservoirs with simple filter elements (grids, ceramic filters, etc.), which are placed in concrete casings that are, essentially, concrete blocks themselves. This rules out personnel's radiation exposure. The filtered high-level waste remain inside the concrete blocks, instead of being removed as sludge at the stage of flushing filter elements, as is the case with the prototype and all other known methods. Concrete blocks are safe for transportation and storage. They can be used as elements in special purpose structural units (e.g. for construction of warehouses, radioactive waste storage facilities etc.)

[0033] The filtrate is passed through reservoirs with granulated sorbent, since a certain height of sorbent layer is necessary for effective sorption (that ensures optimal time for a filtrate-sorbent contact). Using sorbents in powder forms and at such high level will create high hydrodynamic resistance, thus decreasing filtration speed and making it close to zero.

[0034] The set interval (0.1-0.7 mm) in sizes of particles of the powder sorbents is based on the fact that larger particles (more than 0.7 mm) have a smaller surface of absorbing material and, respectively, smaller absorption efficiency, while smaller particles (less than 0.1 mm) are more difficult to separate from the filtrate.

[0035] The set interval (1 to 3 mm) in sizes of particles of the granulated sorbents is based on the fact that larger granules (more than 3 mm) have a smaller surface of absorbing material and, respectively, smaller absorption efficiency, while smaller granules (less than 1 mm) create high hydrodynamic resistance and can reduce efficacy of LRW processing.

IMPLEMENTATION EXAMPLE 1

[0036] The described method was used to process LRW (pH of 12.1) containing: [0037] solids content (after drying at 105° C.)-285 g/l; [0038] suspended particles (separated on the filter with a blue belt), 5.1 g/l; [0039] specific activity of Cs-137: 1.1.10-3 Ci/l [0040] specific activity cobalt-60: 1.4.10-6 Ci/l

[0041] Tank 1 was pumped with 5M3 of LRW of the aforesaid composition. Then a composition consisting of nickel ferrocyanide selective sorbent (5 kg), applied to the powder of amorphous silicon dioxide from the Sukholozhsky deposit, that had particles sized 200 to 500 microns, and of nickel sulfate (0.5 kg) as a coagulant was stirred in. The combination of amorphous silicon dioxide and agglomerates, which forms during the interaction process between nickel-based coagulant and LRW suspended particles, makes separation of liquid components from the solid ones inside COREBRICK F very easy.

[0042] After a two-hour stirring, the suspension comprising sorbent, LRW-derived suspended particles and a coagulant, was pumped into COREBRICK F 2 equipped with two filter elements. Afterwards, a solution, which was purified from the suspension, was directed for the ozone treatment 3, where the destruction of organic compounds and complexes took place. Suspended solids obtained during the oxidation were mixed with 5kg of the same sorbent that was stirred into the tank, and a resulting suspension was directed to COREBRICK F 4 equipped with two filter elements. Filtrate purified from the suspended solids was passed through sequentially connected COREBRICKs C 5&6 with granular selective sorbent based on nickel ferrocyanide. The purified filtrate, containing less than 10 Bq/l of Cs-137 and Co-60, was sent to evaporation and crystallization. The final product can be placed at the non-radioactive waste storage site.

[0043] COREBRICKs F containing sludge were filled with high-penetrating cement mortar that embeds the inside chamber. COREBRICKs C containing selective sorbents were blasted with hot air and also built in with high-penetrating cement mortar.

[0044] Activity registered in COREBRICKs F amounted to 5 Ci each, while in COREBRICKs C it amounted to 9.8 Ci in the first one and 0.2 Ci in the second.

IMPLEMENTATION EXAMPLE 2

[0045] The tank was pumped with 25M.sup.3 of LRW comprising sea water of the following composition: [0046] total salt content −30 g/l; pH of 7.9; specific activity of Cs-137: 2.4*105 Ci/l.

[0047] Fifty kilograms of selective sorbent, based on “Prussian Blue” (Iron (III) hexacyanoferrate (II)) in a form of a dry powder with a particle size of 0.2 to 0.5 mm, was stirred into LRW. After eight hours of mixing, LRW and the sorbent were directed to COREBRICK F featuring one filter element with a pore size of 0.1 mm. Filtrate separated from the sorbent was passed through COREBRICK C, comprising one hundred kilograms of granular selective sorbent based on iron ferrocyanide with a granule size of 1-2 mm. Sea water scrubbed of cesium radionuclides contains less than 5 Bq/l of cesium-137 and may be dumped back into the sea. Used-up sorbents that are in COREBRICKs C and F are built in with high-penetrating cement mortar.

IMPLEMENTATION EXAMPLE 3

[0048] The proposed method was used to process LRW containing: [0049] total salt content—−228 g/l; pH=10.9; [0050] specific activity of strontium—90, 4.2*104 Bq/l; [0051] specific activity of cobalt—60:1.5*104 Bq/l.

[0052] The tank was pumped with 12M.sup.3 of LRW of the aforementioned composition, and then thirty kilograms of selective sorbent in a form of dry powder based on manganese dioxide were added, and after that 30 kg of powder sorbent based on copper sulfide. The particle size of the powder sorbents did not exceed 0.5 mm. After a three-hour mixing, LRW was directed to COREBRICK F equipped with two filter elements with a pore size of 0.4 and 0.1 mm. Afterwards, filtrate separated from the powder sorbent was passed through COREBRICK C, comprising fifty kilograms of granular selective sorbent, based on manganese dioxide. The total specific activity of isotopes remaining in LRW accounted for no more than 10 Bq/l.

IMPLEMENTATION EXAMPLE 4

[0053] The suggested method was used to process LRW containing: [0054] Boric acid g/L, pH=4; [0055] Cs-137 5.2*106 Bq/l; Co-60 3.1*104 Bq/l; [0056] Ag-110 8.1*103 Bq/l; Sr-90 1.9*105 Bq/l.

[0057] The tank containing 10M.sup.3 of LRW was consecutively pumped with twenty kilograms of selective sorbents in a form of dry powder (with a particle size of less than 0.3 mm) and of the following composition: copper ferrocyanide, magnesium phosphate, zirconium hydroxide.

[0058] After a five-hour mixing, LRW was pumped through two COREBRICKs F with a pore size of 0.2 mm in the first filter and 0.1 mm in the second one. Afterwards, filtrate was passed through three consecutively connected COREBRICKs C, comprising sixty liters of mechanical mixture of selective sorbents with granular size of 3 mm.

[0059] Mechanical mixture consisted of homogeneously mixed sorbents: [0060] 20 L of copper ferrocyanide, [0061] 20 L of magnesium phosphate, [0062] 20 L of zirconium hydroxide.

[0063] The total specific activity of isotopes remaining in LRW made up not more than 10 Bq/l.

[0064] The use of the described method can decrease radiation exposure of personnel processing LRW, streamline the technological procedures of LRW processing, delivering a final product—a block that is safe to transport and use and that doesn't require any radiation safety precautions.