CN116813197A - A kind of borosilicate glass curing aid for the treatment of medium and low radioactive waste liquid and its use method - Google Patents
A kind of borosilicate glass curing aid for the treatment of medium and low radioactive waste liquid and its use method Download PDFInfo
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- 239000002901 radioactive waste Substances 0.000 title claims abstract description 39
- 239000007788 liquid Substances 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 32
- 239000005388 borosilicate glass Substances 0.000 title claims abstract description 11
- 239000011521 glass Substances 0.000 claims abstract description 71
- 239000000203 mixture Substances 0.000 claims abstract description 37
- 239000011734 sodium Substances 0.000 claims abstract description 27
- 238000007711 solidification Methods 0.000 claims abstract description 17
- 230000008023 solidification Effects 0.000 claims abstract description 17
- 229910052708 sodium Inorganic materials 0.000 claims abstract description 15
- 239000000654 additive Substances 0.000 claims abstract description 12
- 229910052746 lanthanum Inorganic materials 0.000 claims abstract description 7
- 229910052727 yttrium Inorganic materials 0.000 claims abstract description 7
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims abstract description 6
- 229910052779 Neodymium Inorganic materials 0.000 claims abstract description 6
- 229910052788 barium Inorganic materials 0.000 claims abstract description 6
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 6
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims abstract description 6
- 229910052712 strontium Inorganic materials 0.000 claims abstract description 6
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims abstract description 3
- 239000000156 glass melt Substances 0.000 claims description 19
- 238000000137 annealing Methods 0.000 claims description 18
- 238000002386 leaching Methods 0.000 claims description 15
- 230000000996 additive effect Effects 0.000 claims description 7
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims description 7
- 239000004327 boric acid Substances 0.000 claims description 7
- 239000008367 deionised water Substances 0.000 claims description 7
- 229910021641 deionized water Inorganic materials 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 3
- PPQREHKVAOVYBT-UHFFFAOYSA-H dialuminum;tricarbonate Chemical class [Al+3].[Al+3].[O-]C([O-])=O.[O-]C([O-])=O.[O-]C([O-])=O PPQREHKVAOVYBT-UHFFFAOYSA-H 0.000 claims description 3
- 238000002844 melting Methods 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 150000002823 nitrates Chemical class 0.000 claims description 3
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052796 boron Inorganic materials 0.000 claims description 2
- 229910052710 silicon Inorganic materials 0.000 claims description 2
- 239000010703 silicon Substances 0.000 claims description 2
- 229910018626 Al(OH) Inorganic materials 0.000 claims 1
- -1 alkaline earth metal carbonates Chemical class 0.000 claims 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 abstract description 19
- 229910001948 sodium oxide Inorganic materials 0.000 abstract description 19
- 239000002699 waste material Substances 0.000 abstract description 14
- 230000008569 process Effects 0.000 abstract description 7
- 230000002285 radioactive effect Effects 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 229910004298 SiO 2 Inorganic materials 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 16
- 239000000126 substance Substances 0.000 description 16
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 14
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 12
- 238000012360 testing method Methods 0.000 description 11
- PLDDOISOJJCEMH-UHFFFAOYSA-N neodymium(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Nd+3].[Nd+3] PLDDOISOJJCEMH-UHFFFAOYSA-N 0.000 description 10
- 239000000463 material Substances 0.000 description 8
- 239000000377 silicon dioxide Substances 0.000 description 8
- 229910001220 stainless steel Inorganic materials 0.000 description 8
- 239000010935 stainless steel Substances 0.000 description 8
- 229910000029 sodium carbonate Inorganic materials 0.000 description 7
- 238000003860 storage Methods 0.000 description 7
- 238000003723 Smelting Methods 0.000 description 6
- 238000012512 characterization method Methods 0.000 description 6
- 238000007654 immersion Methods 0.000 description 6
- 239000012212 insulator Substances 0.000 description 6
- MRELNEQAGSRDBK-UHFFFAOYSA-N lanthanum(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[La+3].[La+3] MRELNEQAGSRDBK-UHFFFAOYSA-N 0.000 description 6
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 6
- 230000003068 static effect Effects 0.000 description 6
- 239000011787 zinc oxide Substances 0.000 description 6
- 229910001928 zirconium oxide Inorganic materials 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- 235000012239 silicon dioxide Nutrition 0.000 description 5
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 238000007496 glass forming Methods 0.000 description 3
- BDAGIHXWWSANSR-NJFSPNSNSA-N hydroxyformaldehyde Chemical compound O[14CH]=O BDAGIHXWWSANSR-NJFSPNSNSA-N 0.000 description 3
- 239000002925 low-level radioactive waste Substances 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 3
- SIWVEOZUMHYXCS-UHFFFAOYSA-N oxo(oxoyttriooxy)yttrium Chemical compound O=[Y]O[Y]=O SIWVEOZUMHYXCS-UHFFFAOYSA-N 0.000 description 3
- 229910000018 strontium carbonate Inorganic materials 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 150000001342 alkaline earth metals Chemical class 0.000 description 2
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 2
- AYJRCSIUFZENHW-DEQYMQKBSA-L barium(2+);oxomethanediolate Chemical compound [Ba+2].[O-][14C]([O-])=O AYJRCSIUFZENHW-DEQYMQKBSA-L 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 2
- 238000009375 geological disposal Methods 0.000 description 2
- 239000003758 nuclear fuel Substances 0.000 description 2
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 1
- 229940118662 aluminum carbonate Drugs 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000006121 base glass Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000003181 co-melting Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000002927 high level radioactive waste Substances 0.000 description 1
- 239000002926 intermediate level radioactive waste Substances 0.000 description 1
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000012857 radioactive material Substances 0.000 description 1
- 229910001404 rare earth metal oxide Inorganic materials 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 230000010512 thermal transition Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000004017 vitrification Methods 0.000 description 1
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
- C03C3/095—Glass compositions containing silica with 40% to 90% silica, by weight containing rare earths
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/04—Treating liquids
- G21F9/06—Processing
- G21F9/16—Processing by fixation in stable solid media
- G21F9/162—Processing by fixation in stable solid media in an inorganic matrix, e.g. clays, zeolites
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Glass Compositions (AREA)
Abstract
一种用于中、低放射性废液处理的硼硅酸盐玻璃固化助剂及其使用方法,其组成范围为:SiO245~65,B2O312~25,Al2O30.6~20,ZnO 0.6~6.5,ZrO20.6~2.5,RE2O30.6~6.5,MO 0.6~12,其中,RE2O3(RE是La、Nd、Y的一种或几种),M是Mg、Ca、Sr、Ba中的一种或几种。制备的固化玻璃中Na2O的质量百分数可达20~30%,且固化玻璃产品满足O/(Si+B+Al)的摩尔比为2.0~2.5,(2ΣM+Na)/(Si+B+Al)的摩尔比为0.5~1.0。其使用方法是将助剂和氧化钠的原材料按照配方的比例称量、混匀,电熔炉中熔融、浇注、退火,制得高钠固化玻璃,该产品符合固化玻璃生产工艺要求,粘度、电导率等工艺参数适中,适合高钠中、低放蒸残废液的固化处理。
A borosilicate glass curing aid for the treatment of medium and low radioactive waste liquids and its use method. Its composition range is: SiO 2 45~65, B 2 O 3 12~25, Al 2 O 3 0.6~ 20. ZnO 0.6~6.5, ZrO 2 0.6~2.5, RE 2 O 3 0.6~6.5, MO 0.6~12, among which, RE 2 O 3 (RE is one or more of La, Nd, Y), M is One or more of Mg, Ca, Sr and Ba. The mass percentage of Na 2 O in the prepared cured glass can reach 20-30%, and the cured glass product satisfies the molar ratio of O/(Si+B+Al) of 2.0-2.5, (2ΣM+Na)/(Si+B +Al) molar ratio is 0.5 to 1.0. The method of use is to weigh and mix the raw materials of additives and sodium oxide according to the proportion of the formula, melt, pour, and anneal in an electric furnace to produce high-sodium solidified glass. This product meets the requirements of the solidified glass production process, and its viscosity and conductivity The process parameters such as rate are moderate, and it is suitable for the solidification treatment of high sodium, medium and low radioactive steam waste liquids.
Description
技术领域Technical field
本发明属于中、低放射性核废料的处理方法,涉及一种高氧化钠包容率的硼硅酸盐固化玻璃助剂及其使用方法,适用于核工业等领域所排放的高钠中、低放射性核废料的固化处理。The invention belongs to a method for processing medium and low radioactive nuclear waste. It relates to a borosilicate curing glass additive with high sodium oxide containment rate and a method of using it. It is suitable for high sodium, medium and low radioactive materials discharged from the nuclear industry and other fields. Solidification of nuclear waste.
背景技术Background technique
核能发电过程中不产生任何大气污染,作为清洁能源高效、实用。然而,核燃料循环中产生的放射性废物具有极高的毒性,会对生态环境造成极大的破坏,其安全处置一直是国内外关注的焦点。根据核废物的放射性水平不同,核废料分为高放废物、中放废物和低放废物。其中,中、低放射性核废液来源于核燃料循环的三个阶段(前端、中端或运行、后端),占比最大,达到97%。玻璃固化技术是目前国际上较为广泛使用的一种对中低放射性核废液进行处理处置的可行方法。通过将中低放废液与基础玻璃原料共熔成玻璃体,可以实现对中低放废物的原子尺度固化,从而在玻璃固化体处置年限内起到阻止放射性核素向外界环境迁移的作用。Nuclear energy does not produce any air pollution during power generation and is efficient and practical as a clean energy source. However, the radioactive waste produced in the nuclear fuel cycle is extremely toxic and can cause great damage to the ecological environment. Its safe disposal has always been the focus of domestic and foreign attention. According to the different radioactivity levels of nuclear waste, nuclear waste is divided into high-level waste, intermediate-level waste and low-level waste. Among them, medium- and low-level radioactive nuclear waste liquids originate from the three stages of the nuclear fuel cycle (front-end, middle-end or operation, back-end), accounting for the largest proportion, reaching 97%. Vitrification technology is currently a feasible method widely used in the world to treat and dispose of medium and low radioactive nuclear waste liquid. By co-melting liquid low- and medium-level radioactive waste with basic glass raw materials into a glass body, atomic-scale solidification of low-level and medium-level radioactive waste can be achieved, thereby preventing the migration of radionuclides to the external environment within the disposal life of the solidified glass body.
目前,美国、韩国、意大利和俄罗斯等对中低放废液都采用了玻璃固化方法进行处理并拟进行地质处置。我国核废物后处理厂迫切需要处置固化的酸性中低放蒸残液和碱性中低放蒸残液中,主要含有UO2(NO3)2和NaNO3等源项,其中NaNO3的质量占比达到99%以上,固化中低放射性废液的配方研究主要体现在固化高含量质量百分比的氧化钠上。氧化钠属于活泼性强的碱金属氧化物,玻璃固化体中如果含有大量的氧化钠,势必影响固化体的化学稳定性,而中低放废液玻璃固化体的贮存需保持几百年以上,因而对含有高质量百分比含量的氧化钠的固化玻璃配方的化稳性提出了较高要求。At present, the United States, South Korea, Italy and Russia have all used glass solidification methods to treat low- and medium-level radioactive waste liquids and plan to conduct geological disposal. China's nuclear waste reprocessing plants urgently need to dispose of the solidified acidic low-medium radioactive vapor residue and alkaline medium-low radioactive vapor residue, which mainly contain source items such as UO 2 (NO 3 ) 2 and NaNO 3. The mass of NaNO 3 The proportion reaches more than 99%. The research on the formula of solidifying medium and low radioactive waste liquid is mainly reflected in solidifying high content mass percentage of sodium oxide. Sodium oxide is a highly reactive alkali metal oxide. If the solidified glass contains a large amount of sodium oxide, it will inevitably affect the chemical stability of the solidified body. The storage of solidified glassware of medium and low radioactive waste liquids needs to be maintained for more than hundreds of years. Therefore, higher requirements are placed on the chemical stability of cured glass formulations containing high mass percentages of sodium oxide.
硼硅酸盐玻璃固化基材具有热力学稳定性好、化学稳定性好、放射性核素浸出率低、热膨胀系数小等优点,因此,在国外大型玻璃固化设施中优先选择硼硅酸盐玻璃作为固化基材。中国专利200980153530.7公布了一种铝硼硅酸盐固化玻璃,用于处理中等放射性的废液,所制备的玻璃固化体中氧化钠的最高百分之质量含量仅为15%。文献刘丽君等,核化学与放射化学,2014,Vol.36,No3:163-168.公布了一种高硫高钠的硼硅酸盐固化玻璃配方,其中基础玻璃中氧化钠的含量为5.21%,源项中氧化钠的含量为45.103%,按照源项的包容率为16%来计算,该固化玻璃配方的氧化钠总含量仅为12.37%。Borosilicate glass curing substrate has the advantages of good thermodynamic stability, good chemical stability, low radionuclide leaching rate, and small thermal expansion coefficient. Therefore, borosilicate glass is preferred as the curing material in large foreign glass curing facilities. base material. Chinese patent 200980153530.7 discloses an aluminoborosilicate solidified glass for treating moderately radioactive waste liquids. The maximum mass content of sodium oxide in the prepared glass solidified body is only 15%. Literature Liu Lijun et al., Nuclear Chemistry and Radiochemistry, 2014, Vol. 36, No3: 163-168. published a high-sulfur and high-sodium borosilicate cured glass formula, in which the sodium oxide content in the base glass is 5.21% , the content of sodium oxide in the source term is 45.103%. Calculated based on the containment rate of the source term of 16%, the total sodium oxide content of this cured glass formula is only 12.37%.
鉴于固化玻璃低质处置的成本极高,需要提高氧化钠的包容率,因此有必要开发一种对氧化钠包容率较高,固化产品的化稳性符合地质处置条件要求,适合连续熔融生产的固化玻璃助剂。In view of the extremely high cost of disposal of low-quality solidified glass, it is necessary to increase the containment rate of sodium oxide. Therefore, it is necessary to develop a method that has a high containment rate of sodium oxide, and the chemical stability of the solidified product meets the requirements of geological disposal conditions, and is suitable for continuous melting production. Curing glass additives.
发明内容Contents of the invention
针对上述现有中、低放射性废液的固化处置需要包容较高氧化钠含量的要求,提出一种高氧化钠包容率的硼硅酸盐固化玻璃助剂及其使用方法。制备的高钠固化玻璃成玻璃性能好、化学稳定性高、适合中低放废物连续固化处理。In view of the above requirements that the solidification and disposal of existing medium and low radioactive waste liquids need to contain higher sodium oxide content, a borosilicate curing glass additive with high sodium oxide containment rate and its use method are proposed. The prepared high-sodium solidified glass has good glass-forming properties and high chemical stability, and is suitable for the continuous solidification treatment of medium and low-level radioactive waste.
本发明的技术方案如下:The technical solution of the present invention is as follows:
用于固化Na2O的硼硅酸盐固化玻璃助剂的氧化物质量百分比组分范围为:The oxide mass percentage component range of borosilicate curing glass additives used to cure Na 2 O is:
其中,RE2O3(RE是La、Nd、Y的一种或几种),M是Mg、Ca、Sr、Ba中的一种或几种。Among them, RE 2 O 3 (RE is one or more of La, Nd, Y), and M is one or more of Mg, Ca, Sr, and Ba.
用上述固化玻璃助剂固化高氧化钠含量的固化玻璃产品,具有基于固化玻璃总质量的质量百分比为:Using the above curing glass additives to cure cured glass products with high sodium oxide content, the mass percentage based on the total mass of the cured glass is:
其中,RE2O3(RE是La、Nd、Y的一种或几种),M是Mg、Ca、Sr、Ba中的一种或几种,并满足O/(Si+B+Al)的摩尔比为2.0~2.5,(2ΣM+Na)/(Si+B+Al)的摩尔比为0.5~1.0。Among them, RE 2 O 3 (RE is one or more of La, Nd, Y), M is one or more of Mg, Ca, Sr, Ba, and satisfies O/(Si+B+Al) The molar ratio of (2ΣM+Na)/(Si+B+Al) is 0.5-1.0.
本发明还提供了一种上述的硼硅酸盐固化玻璃助剂包容高氧化钠的使用方法,包括以下步骤:The invention also provides a method for using the above-mentioned borosilicate curing glass additive to contain high sodium oxide, which includes the following steps:
(1)、按照玻璃助剂和氧化钠的质量百分比称取原材料,并且混合均匀,得到混合料;(1) Weigh the raw materials according to the mass percentage of glass additives and sodium oxide, and mix them evenly to obtain a mixture;
(2)、把混合料盛入坩埚,放入温度在1150~1200℃不等的熔炉中熔化,澄清1~3小时,得到澄清均匀的玻璃熔体;(2) Put the mixture into a crucible, put it into a furnace with a temperature ranging from 1150 to 1200°C, melt it, and clarify it for 1 to 3 hours to obtain a clear and uniform glass melt;
(3)、将澄清均匀的玻璃熔体浇注在预热至350~450℃的不锈钢模具中成型,随后转移到预热到450~500℃的退火炉中;(3) Pour the clear and uniform glass melt into a stainless steel mold preheated to 350-450°C, and then transfer it to an annealing furnace preheated to 450-500°C;
(4)、在退火炉中保温1~5小时,然后降至室温,得到高硼硅酸盐固化玻璃。(4) Keep the temperature in the annealing furnace for 1 to 5 hours, and then lower to room temperature to obtain high borosilicate solidified glass.
上述制备方法中,步骤(1)所述的按照玻璃组分及质量百分比称取原材料时,B2O3来自B2O3、硼酸中的一种或多种;Al2O3来自Al(OH)3、铝的碳酸盐、铝的硝酸盐中的一种或多种;Na2O来自钠的碳酸盐、硝酸盐中的一种或多种;所述MO来自碱土金属的碳酸盐、硝酸盐中的一种或多种。In the above preparation method, when the raw materials are weighed according to the glass composition and mass percentage as described in step (1), B 2 O 3 comes from one or more of B 2 O 3 and boric acid; Al 2 O 3 comes from Al( OH) 3 , one or more of aluminum carbonate, aluminum nitrate; Na 2 O comes from one or more of sodium carbonate, nitrate; the MO comes from the carbon of alkaline earth metal One or more of acid salts and nitrates.
下面对本发明作进一步说明,本发明要求O/(Si+B+Al)的摩尔比控制在2.0~2.5,(2ΣM+Na)/(Si+B+Al)的摩尔比为0.5~1.0。制备的固化玻璃在浇注、退火后,呈玻璃无定形态。玻璃中的主要网络体为硅、硼、铝,当O/(Si+B+Al)及(2ΣM+Na)/(Si+B+Al)的摩尔比值较高,玻璃网络体不足,容易析晶,且会降低玻璃的化学稳定性;较低时,玻璃修饰体不足,同样会导致分相及析晶。The present invention will be further described below. The present invention requires that the molar ratio of O/(Si+B+Al) be controlled at 2.0-2.5, and the molar ratio of (2ΣM+Na)/(Si+B+Al) be controlled at 0.5-1.0. The prepared solidified glass takes on the amorphous form of glass after casting and annealing. The main network bodies in glass are silicon, boron, and aluminum. When the molar ratios of O/(Si+B+Al) and (2ΣM+Na)/(Si+B+Al) are high, the glass network body is insufficient and it is easy to analyze. crystallization, and will reduce the chemical stability of the glass; when it is lower, the glass modifier is insufficient, which will also lead to phase separation and crystallization.
少量的ZrO2也参与玻璃网络,有利于玻璃化学稳定性的提高,但超过2%,容易产生晶核,导致析晶,降低玻璃的成玻璃性能。氧化镧、氧化钕及氧化钇等稀土氧化物有提高玻璃热转变温度、改善玻璃成玻璃性能,提高玻璃粘度的作用。碱土金属作为玻璃的修饰体,有调节玻璃配位数、电导率、粘度的作用。A small amount of ZrO 2 also participates in the glass network, which is beneficial to improving the chemical stability of the glass, but if it exceeds 2%, it is easy to produce crystal nuclei, leading to crystallization and reducing the glass-forming properties of the glass. Rare earth oxides such as lanthanum oxide, neodymium oxide and yttrium oxide can increase the thermal transition temperature of glass, improve the glass-forming properties of glass, and increase the viscosity of glass. As a modification of glass, alkaline earth metals can adjust the coordination number, conductivity, and viscosity of glass.
本发明的有益效果在于:The beneficial effects of the present invention are:
本发明提供的玻璃助剂可以包容高质量百分比含量的氧化钠,制备的固化玻璃透明无析晶,化学稳定性优异,满足核工业标准EJ1186-2005中对固化体化学稳定性的要求。且固化玻璃的粘度、电导率适合连续熔炉的焦耳陶瓷电熔炉的固化生产工艺,适合于高钠含量的中、低放废液的固化处理。The glass additive provided by the invention can contain sodium oxide with a high-quality percentage content, and the cured glass prepared is transparent without crystallization and has excellent chemical stability, meeting the requirements for the chemical stability of the solidified body in the nuclear industry standard EJ1186-2005. The viscosity and conductivity of the solidified glass are suitable for the solidification production process of the Joule ceramic electric furnace of the continuous furnace, and are suitable for the solidification treatment of medium and low-level radioactive waste liquids with high sodium content.
附图说明Description of the drawings
图1是本发明6个实施例的28天化稳性的元素浸出率图。Figure 1 is a graph of elemental leaching rates of 28-day chemical stability of six embodiments of the present invention.
具体实施方式Detailed ways
实施例中提供的用于中、低放射性废液处理的高钠硼硅酸盐固化玻璃产品的组分质量百分比为:The component mass percentage of the high-sodium borosilicate cured glass product provided in the embodiment for the treatment of medium and low radioactive waste liquids is:
其中,RE2O3(RE是La、Nd、Y的一种或几种),M是Mg、Ca、Sr、Ba中的一种或几种,且O/(Si+B+Al)的摩尔比为2.0~2.5,(2ΣM+Na)/(Si+B+Al)的摩尔比为0.5~1.0。Among them, RE 2 O 3 (RE is one or more of La, Nd, Y), M is one or more of Mg, Ca, Sr, Ba, and O/(Si+B+Al) The molar ratio is 2.0 to 2.5, and the molar ratio of (2ΣM+Na)/(Si+B+Al) is 0.5 to 1.0.
实施例中上述玻璃助剂包容高含量氧化钠的使用方法包括以下步骤:In the embodiment, the method of using the above-mentioned glass additive to contain high content of sodium oxide includes the following steps:
(1)、按照玻璃组分及质量百分比称取原材料,并且混合均匀,得到混合料;(1) Weigh the raw materials according to the glass components and mass percentage, and mix them evenly to obtain a mixture;
(2)、把混合料盛入坩埚,并根据组成及质量百分比的不同放入温度在1150~1200℃不等的熔炉中熔化,澄清1~3小时,得到澄清均匀的玻璃熔体;(2) Put the mixture into a crucible, put it into a furnace with a temperature ranging from 1150 to 1200°C according to the composition and mass percentage, and melt it, and then clarify it for 1 to 3 hours to obtain a clear and uniform glass melt;
(3)、将澄清均匀的玻璃熔体浇注在预热至350~450℃的不锈钢模具中成型,随后快速转移到预热到450~500℃的退火炉中;(3) Pour the clear and uniform glass melt into a stainless steel mold preheated to 350-450°C and then quickly transfer it to an annealing furnace preheated to 450-500°C;
(4)、在退火炉中保温1~5小时,然后以1℃/分钟的速率降至室温,得到所述硼硅酸盐固化玻璃。(4) Keep the temperature in an annealing furnace for 1 to 5 hours, and then lower it to room temperature at a rate of 1°C/minute to obtain the borosilicate solidified glass.
以下结合具体实施例对本发明作进一步说明。The present invention will be further described below in conjunction with specific examples.
表1给出本发明的6个实施例的固化玻璃产品组成、O/(Si+B+Al)及(2ΣM+Na)/(Si+B+Al)的摩尔比值:Table 1 shows the composition of cured glass products, the molar ratios of O/(Si+B+Al) and (2ΣM+Na)/(Si+B+Al) of six embodiments of the present invention:
表1Table 1
实施例1:Example 1:
按照表1中实施例1配方中氧化物的质量百分组成:称取碳酸钠44克、二氧化硅42克、三氧化二硼17.7克、氧化铝4克、氧化锌3克、氧化锆1克、氧化镧1克、氧化钕1克、氧化钇2克、轻质氧化镁4克、碳酸钡1.29克,混合均匀,得到混合料,把混合料盛入二氧化硅坩埚,在1200℃的熔炉中熔化,澄清1小时,得到澄清均匀的玻璃熔体;将澄清均匀的玻璃熔体浇注在预热至390℃的不锈钢模具中成型,随后快速转移到预热至500℃的退火炉中;在退火炉中保温2.5小时消除应力,然后以1℃/分钟的速率降至室温,得到用于中低放射性废液固化处理的高钠硼硅酸盐玻璃。用Orton公司RSV-16RT型高温旋转法粘度仪测得玻璃在1150℃高温粘度为23Poise。依据GB/T 10581-2006《绝缘体材料在高温下电阻和电阻率的试验方案》提供的方法测试电阻率,并计算在1150℃的电导率为0.56S/cm。依据标准EJ 1186-2005《放射性废物体和废物包的特性鉴定》,在90℃±1℃去离子水中,静态浸泡28天的归一化元素浸出率入图所示,单一元素浸出率均小于0.2g/m2。化学稳定性与粘度、电导率等工艺参数均适合中低放废液固化玻璃的连续熔炼与地质存储。According to the mass percentage composition of the oxides in the formula of Example 1 in Table 1: weigh 44 grams of sodium carbonate, 42 grams of silicon dioxide, 17.7 grams of diboron trioxide, 4 grams of aluminum oxide, 3 grams of zinc oxide, and 1 gram of zirconium oxide. g, 1 g of lanthanum oxide, 1 g of neodymium oxide, 2 g of yttrium oxide, 4 g of light magnesium oxide, and 1.29 g of barium carbonate, mix evenly to obtain a mixture, put the mixture into a silica crucible, and heat it at 1200°C Melt in the furnace and clarify for 1 hour to obtain a clear and uniform glass melt; pour the clear and uniform glass melt into a stainless steel mold preheated to 390°C and then quickly transfer it to an annealing furnace preheated to 500°C; Keep the temperature in the annealing furnace for 2.5 hours to eliminate stress, and then lower it to room temperature at a rate of 1°C/minute to obtain high-sodium borosilicate glass for solidification treatment of medium and low radioactive waste liquids. The high-temperature viscosity of glass at 1150°C was measured to be 23 Poise using Orton's RSV-16RT high-temperature rotational viscometer. The resistivity was measured according to the method provided in GB/T 10581-2006 "Test Plan for Resistance and Resistivity of Insulator Materials at High Temperatures" and the conductivity at 1150°C was calculated to be 0.56S/cm. According to the standard EJ 1186-2005 "Characterization of Radioactive Waste Bodies and Waste Packages", the normalized element leaching rate of static immersion in deionized water at 90℃±1℃ for 28 days is shown in the figure. The leaching rates of single elements are less than 0.2g/m 2 . The chemical stability, viscosity, conductivity and other process parameters are suitable for the continuous smelting and geological storage of solidified glass for medium and low radioactive waste liquids.
实施例2:Example 2:
按照表1中实施例2配方中氧化物的质量百分组成:称取碳酸钠51.3克、二氧化硅50克、硼酸26.6克、氧化铝0.5克、氧化锌2克、氧化锆2克、氧化镧0.5克、碳酸锶7.1克,混合均匀,得到混合料,把混合料盛入二氧化硅坩埚,在1200℃的熔炉中熔化,澄清1小时,得到澄清均匀的玻璃熔体;将澄清均匀的玻璃熔体浇注在预热至390℃的不锈钢模具中成型,随后快速转移到预热至500℃的退火炉中;在退火炉中保温2.5小时消除应力,然后以1℃/分钟的速率降至室温,得到用于中低放射性废液固化处理的高钠硼硅酸盐玻璃。用Orton公司RSV-16RT型高温旋转法粘度仪测得玻璃在1150℃高温粘度为40Poise。依据GB/T 10581-2006《绝缘体材料在高温下电阻和电阻率的试验方案》提供的方法测试电阻率,并计算在1150℃的电导率为0.13S/cm。依据标准EJ 1186-2005《放射性废物体和废物包的特性鉴定》,在90℃±1℃去离子水中,静态浸泡28天的归一化元素浸出率入图所示,单一元素浸出率均小于0.2g/m2。化学稳定性与粘度、电导率等工艺参数均适合中低放废液固化玻璃的连续熔炼与地质存储。According to the mass percentage composition of the oxide in the formula of Example 2 in Table 1: weigh 51.3 grams of sodium carbonate, 50 grams of silicon dioxide, 26.6 grams of boric acid, 0.5 grams of aluminum oxide, 2 grams of zinc oxide, 2 grams of zirconium oxide, 0.5 grams of lanthanum and 7.1 grams of strontium carbonate are mixed evenly to obtain a mixture. Put the mixture into a silica crucible, melt it in a furnace at 1200°C, and clarify it for 1 hour to obtain a clear and uniform glass melt; The glass melt is poured into a stainless steel mold preheated to 390°C and then quickly transferred to an annealing furnace preheated to 500°C. It is kept in the annealing furnace for 2.5 hours to eliminate stress, and then reduced to a temperature of 1°C/min at a rate of 1°C/min. At room temperature, high-sodium borosilicate glass for solidification treatment of medium and low radioactive waste liquids was obtained. The high-temperature viscosity of glass at 1150°C was measured to be 40 Poise using Orton's RSV-16RT high-temperature rotational viscometer. Test the resistivity according to the method provided in GB/T 10581-2006 "Test Plan for Resistance and Resistivity of Insulator Materials at High Temperatures", and calculate the conductivity at 1150°C to be 0.13S/cm. According to the standard EJ 1186-2005 "Characterization of Radioactive Waste Bodies and Waste Packages", the normalized element leaching rate of static immersion in deionized water at 90℃±1℃ for 28 days is shown in the figure. The leaching rates of single elements are less than 0.2g/m 2 . The chemical stability, viscosity, conductivity and other process parameters are suitable for the continuous smelting and geological storage of solidified glass for medium and low radioactive waste liquids.
实施例3:Example 3:
按照表1中实施例3配方中氧化物的质量百分组成:称取碳酸钠34.2克、二氧化硅55克、硼酸23.1克、氢氧化铝15.3克、氧化锌0.5克、氧化锆2克、氧化镧1克、氧化钕1克、氧化钇3克、轻质氧化镁2克、碳酸钙7克。混合均匀,得到混合料,把混合料盛入氧化铝坩埚,在1200℃的熔炉中熔化,澄清1小时,得到澄清均匀的玻璃熔体;将澄清均匀的玻璃熔体浇注在预热至390℃的不锈钢模具中成型,随后快速转移到预热至500℃的退火炉中;在退火炉中保温2.5小时消除应力,然后以1℃/分钟的速率降至室温,得到用于中低放射性废液固化处理的高钠硼硅酸盐玻璃。用Orton公司RSV-16RT型高温旋转法粘度仪测得玻璃在1150℃高温粘度为33Poise。依据GB/T 10581-2006《绝缘体材料在高温下电阻和电阻率的试验方案》提供的方法测试电阻率,并计算在1150℃的电导率为0.7S/cm。依据标准EJ 1186-2005《放射性废物体和废物包的特性鉴定》,在90℃±1℃去离子水中,静态浸泡28天的归一化元素浸出率入图所示,单一元素浸出率均小于0.17g/m2。化学稳定性与粘度、电导率等工艺参数均适合中低放废液固化玻璃的连续熔炼与地质存储。According to the mass percentage composition of the oxides in the formula of Example 3 in Table 1: weigh 34.2 grams of sodium carbonate, 55 grams of silicon dioxide, 23.1 grams of boric acid, 15.3 grams of aluminum hydroxide, 0.5 grams of zinc oxide, 2 grams of zirconium oxide, 1 gram of lanthanum oxide, 1 gram of neodymium oxide, 3 grams of yttrium oxide, 2 grams of light magnesium oxide, and 7 grams of calcium carbonate. Mix evenly to obtain a mixture, put the mixture into an alumina crucible, melt it in a furnace at 1200°C, and clarify it for 1 hour to obtain a clear and uniform glass melt; pour the clear and uniform glass melt into a furnace preheated to 390°C Formed in a stainless steel mold, and then quickly transferred to an annealing furnace preheated to 500°C; kept in the annealing furnace for 2.5 hours to eliminate stress, and then lowered to room temperature at a rate of 1°C/min to obtain medium and low radioactive waste liquid Cured high sodium borosilicate glass. The high-temperature viscosity of glass at 1150°C was measured to be 33 Poise using Orton's RSV-16RT high-temperature rotational viscometer. Test the resistivity according to the method provided in GB/T 10581-2006 "Test Plan for Resistance and Resistivity of Insulator Materials at High Temperatures", and calculate the conductivity at 1150°C to be 0.7S/cm. According to the standard EJ 1186-2005 "Characterization of Radioactive Waste Bodies and Waste Packages", the normalized element leaching rate of static immersion in deionized water at 90℃±1℃ for 28 days is shown in the figure. The leaching rates of single elements are less than 0.17g/m 2 . The chemical stability, viscosity, conductivity and other process parameters are suitable for the continuous smelting and geological storage of solidified glass for medium and low radioactive waste liquids.
实施例4:Example 4:
按照表1中实施例4配方中氧化物的质量百分组成:称取碳酸钠41、二氧化硅35克、硼酸35.5克、氢氧化铝18.3克、氧化锌5克、氧化锆1.5克、氧化钇2克、氢氧化镁3.7克,混合均匀,得到混合料,把混合料盛入氧化铝坩埚,在1200℃的熔炉中熔化,澄清1小时,得到澄清均匀的玻璃熔体;将澄清均匀的玻璃熔体浇注在预热至390℃的不锈钢模具中成型,随后快速转移到预热至500℃的退火炉中;在退火炉中保温2.5小时消除应力,然后以1℃/分钟的速率降至室温,得到用于中低放射性废液固化处理的高钠硼硅酸盐玻璃。用Orton公司RSV-16RT型高温旋转法粘度仪测得玻璃在1150℃高温粘度为22Poise。依据GB/T 10581-2006《绝缘体材料在高温下电阻和电阻率的试验方案》提供的方法测试电阻率,并计算在1150℃的电导率为0.6S/cm。依据标准EJ 1186-2005《放射性废物体和废物包的特性鉴定》,在90℃±1℃去离子水中,静态浸泡28天的归一化元素浸出率入图所示,单一元素浸出率均小于0.18g/m2。化学稳定性与粘度、电导率等工艺参数均适合中低放废液固化玻璃的连续熔炼与地质存储。According to the mass percentage composition of the oxides in the formula of Example 4 in Table 1: weigh 41 grams of sodium carbonate, 35 grams of silicon dioxide, 35.5 grams of boric acid, 18.3 grams of aluminum hydroxide, 5 grams of zinc oxide, 1.5 grams of zirconium oxide, 2 grams of yttrium and 3.7 grams of magnesium hydroxide are mixed evenly to obtain a mixture. Put the mixture into an alumina crucible, melt it in a furnace at 1200°C, and clarify it for 1 hour to obtain a clear and uniform glass melt; The glass melt is poured into a stainless steel mold preheated to 390°C and then quickly transferred to an annealing furnace preheated to 500°C. It is kept in the annealing furnace for 2.5 hours to eliminate stress, and then reduced to a temperature of 1°C/min at a rate of 1°C/min. At room temperature, high-sodium borosilicate glass for solidification treatment of medium and low radioactive waste liquids was obtained. The high-temperature viscosity of glass at 1150°C was measured to be 22 Poise using Orton's RSV-16RT high-temperature rotational viscometer. Test the resistivity according to the method provided in GB/T 10581-2006 "Test Plan for Resistance and Resistivity of Insulator Materials at High Temperatures", and calculate the conductivity at 1150°C to be 0.6S/cm. According to the standard EJ 1186-2005 "Characterization of Radioactive Waste Bodies and Waste Packages", the normalized element leaching rate of static immersion in deionized water at 90℃±1℃ for 28 days is shown in the figure. The leaching rates of single elements are less than 0.18g/m 2 . The chemical stability, viscosity, conductivity and other process parameters are suitable for the continuous smelting and geological storage of solidified glass for medium and low radioactive waste liquids.
实施例5:Example 5:
按照表1中实施例5中配方氧化物的质量百分组成:称取碳酸钠34.2、二氧化硅55克、硼酸28.9克、氧化铝0.5克、氧化锌1克、氧化锆0.5克、氧化钕2克、碳酸锶4.3克、碳酸钡5.2克,混合均匀,得到混合料,把混合料盛入氧化铝坩埚,在1200℃的熔炉中熔化,澄清1小时,得到澄清均匀的玻璃熔体;将澄清均匀的玻璃熔体浇注在预热至390℃的不锈钢模具中成型,随后快速转移到预热至500℃的退火炉中;在退火炉中保温2.5小时消除应力,然后以1℃/分钟的速率降至室温,得到用于中低放射性废液固化处理的高钠硼硅酸盐玻璃。用Orton公司RSV-16RT型高温旋转法粘度仪测得玻璃在1150℃高温粘度为75Poise。依据GB/T10581-2006《绝缘体材料在高温下电阻和电阻率的试验方案》提供的方法测试电阻率,并计算在1150℃的电导率为0.55S/cm。依据标准EJ 1186-2005《放射性废物体和废物包的特性鉴定》,在90℃±1℃去离子水中,静态浸泡28天的归一化元素浸出率入图所示,单一元素浸出率均小于0.16g/m2。化学稳定性与粘度、电导率等工艺参数均适合中低放废液固化玻璃的连续熔炼与地质存储。According to the mass percentage composition of the formula oxide in Example 5 in Table 1: weigh 34.2 g of sodium carbonate, 55 g of silica, 28.9 g of boric acid, 0.5 g of alumina, 1 g of zinc oxide, 0.5 g of zirconium oxide, and neodymium oxide. 2 grams, 4.3 grams of strontium carbonate, and 5.2 grams of barium carbonate, mix evenly to obtain a mixture, put the mixture into an alumina crucible, melt it in a furnace at 1200°C, and clarify it for 1 hour to obtain a clear and uniform glass melt; The clear and uniform glass melt is poured into a stainless steel mold preheated to 390°C and then quickly transferred to an annealing furnace preheated to 500°C. It is kept in the annealing furnace for 2.5 hours to eliminate stress, and then heated to 1°C/min. The rate is reduced to room temperature, and high-sodium borosilicate glass is obtained for solidification treatment of medium and low radioactive waste liquids. The high-temperature viscosity of glass at 1150°C was measured to be 75 Poise using Orton's RSV-16RT high-temperature rotational viscometer. Test the resistivity according to the method provided by GB/T10581-2006 "Test Plan for Resistance and Resistivity of Insulator Materials at High Temperatures", and calculate the conductivity at 1150°C to be 0.55S/cm. According to the standard EJ 1186-2005 "Characterization of Radioactive Waste Bodies and Waste Packages", the normalized element leaching rate of static immersion in deionized water at 90℃±1℃ for 28 days is shown in the figure. The leaching rates of single elements are less than 0.16g/m 2 . The chemical stability, viscosity, conductivity and other process parameters are suitable for the continuous smelting and geological storage of solidified glass for medium and low radioactive waste liquids.
实施例6:Example 6:
按照表1中实施例6中氧化物的质量百分组成:称取碳酸钠39.2克、二氧化硅42克、硼酸19.5克、氧化铝15克、氧化锌3克、氧化锆1克、氧化钕3克、轻质氧化镁2克、碳酸锶1.42克。混合均匀,得到混合料,把混合料盛入氧化铝坩埚,在1200℃的熔炉中熔化,澄清1小时,得到澄清均匀的玻璃熔体;将澄清均匀的玻璃熔体浇注在预热至390℃的不锈钢模具中成型,随后快速转移到预热至500℃的退火炉中;在退火炉中保温2.5小时消除应力,然后以1℃/分钟的速率降至室温,得到用于中低放射性废液固化处理的高钠硼硅酸盐玻璃。用Orton公司RSV-16RT型高温旋转法粘度仪测得玻璃在1150℃高温粘度为25Poise。依据GB/T10581-2006《绝缘体材料在高温下电阻和电阻率的试验方案》提供的方法测试电阻率,并计算在1150℃的电导率为0.45S/cm。依据标准EJ 1186-2005《放射性废物体和废物包的特性鉴定》,在90℃±1℃去离子水中,静态浸泡28天的归一化元素浸出率入图所示,单一元素浸出率均小于0.18g/m2。化学稳定性与粘度、电导率等工艺参数均适合中低放废液固化玻璃的连续熔炼与地质存储。According to the mass percentage composition of the oxide in Example 6 in Table 1: weigh 39.2 grams of sodium carbonate, 42 grams of silicon dioxide, 19.5 grams of boric acid, 15 grams of aluminum oxide, 3 grams of zinc oxide, 1 gram of zirconium oxide, and neodymium oxide. 3 grams, light magnesium oxide 2 grams, strontium carbonate 1.42 grams. Mix evenly to obtain a mixture, put the mixture into an alumina crucible, melt it in a furnace at 1200°C, and clarify it for 1 hour to obtain a clear and uniform glass melt; pour the clear and uniform glass melt into a furnace preheated to 390°C Formed in a stainless steel mold, and then quickly transferred to an annealing furnace preheated to 500°C; kept in the annealing furnace for 2.5 hours to eliminate stress, and then lowered to room temperature at a rate of 1°C/min to obtain medium and low radioactive waste liquid Cured high sodium borosilicate glass. The high-temperature viscosity of glass at 1150°C was measured to be 25 Poise using Orton's RSV-16RT high-temperature rotational viscometer. Test the resistivity according to the method provided by GB/T10581-2006 "Test Plan for Resistance and Resistivity of Insulator Materials at High Temperatures", and calculate the conductivity at 1150°C to be 0.45S/cm. According to the standard EJ 1186-2005 "Characterization of Radioactive Waste Bodies and Waste Packages", the normalized element leaching rate of static immersion in deionized water at 90℃±1℃ for 28 days is shown in the figure. The leaching rates of single elements are less than 0.18g/m 2 . The chemical stability, viscosity, conductivity and other process parameters are suitable for the continuous smelting and geological storage of solidified glass for medium and low radioactive waste liquids.
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