CN106587830B - Waste phosphoric acid tributyl/cement solidification material of kerosene and its preparation method of solidified cement body - Google Patents
Waste phosphoric acid tributyl/cement solidification material of kerosene and its preparation method of solidified cement body Download PDFInfo
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- CN106587830B CN106587830B CN201611145456.2A CN201611145456A CN106587830B CN 106587830 B CN106587830 B CN 106587830B CN 201611145456 A CN201611145456 A CN 201611145456A CN 106587830 B CN106587830 B CN 106587830B
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- 239000004568 cement Substances 0.000 title claims abstract description 106
- 239000002699 waste material Substances 0.000 title claims abstract description 88
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical group CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 title claims abstract description 86
- 239000003350 kerosene Substances 0.000 title claims abstract description 83
- 239000000463 material Substances 0.000 title claims abstract description 57
- 238000007711 solidification Methods 0.000 title claims abstract description 30
- 230000008023 solidification Effects 0.000 title claims abstract description 30
- 238000002360 preparation method Methods 0.000 title claims abstract description 24
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 38
- 239000007787 solid Substances 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 26
- 239000010881 fly ash Substances 0.000 claims abstract description 25
- 239000011398 Portland cement Substances 0.000 claims abstract description 23
- 238000003756 stirring Methods 0.000 claims description 50
- 239000000203 mixture Substances 0.000 claims description 38
- 239000002002 slurry Substances 0.000 claims description 27
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 claims description 10
- 239000011347 resin Substances 0.000 claims description 9
- 229920005989 resin Polymers 0.000 claims description 9
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 4
- 229910052710 silicon Inorganic materials 0.000 claims description 4
- 239000010703 silicon Substances 0.000 claims description 4
- 239000002956 ash Substances 0.000 claims description 3
- BCAARMUWIRURQS-UHFFFAOYSA-N dicalcium;oxocalcium;silicate Chemical compound [Ca+2].[Ca+2].[Ca]=O.[O-][Si]([O-])([O-])[O-] BCAARMUWIRURQS-UHFFFAOYSA-N 0.000 claims description 3
- HFHDHCJBZVLPGP-UHFFFAOYSA-N schardinger α-dextrin Chemical class O1C(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(O)C2O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC2C(O)C(O)C1OC2CO HFHDHCJBZVLPGP-UHFFFAOYSA-N 0.000 claims description 3
- 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 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 241000771208 Buchanania arborescens Species 0.000 claims 4
- 230000008961 swelling Effects 0.000 claims 3
- 239000002253 acid Substances 0.000 claims 2
- 239000005864 Sulphur Substances 0.000 claims 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- 239000004411 aluminium Substances 0.000 claims 1
- UFLSLGGVXPPUDQ-UHFFFAOYSA-N dicalcium oxygen(2-) Chemical compound [O--].[O--].[Ca++].[Ca++] UFLSLGGVXPPUDQ-UHFFFAOYSA-N 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- 239000003469 silicate cement Substances 0.000 claims 1
- 238000002386 leaching Methods 0.000 abstract description 21
- 229910021487 silica fume Inorganic materials 0.000 abstract description 15
- 239000000126 substance Substances 0.000 abstract description 5
- 239000003921 oil Substances 0.000 description 32
- 239000002901 radioactive waste Substances 0.000 description 18
- 238000000034 method Methods 0.000 description 13
- 238000004537 pulping Methods 0.000 description 10
- 238000012360 testing method Methods 0.000 description 9
- 230000007774 longterm Effects 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000007654 immersion Methods 0.000 description 6
- 238000011056 performance test Methods 0.000 description 6
- 239000000292 calcium oxide Substances 0.000 description 5
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000004567 concrete Substances 0.000 description 4
- 229920005646 polycarboxylate Polymers 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical group [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 230000002285 radioactive effect Effects 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 239000000440 bentonite Substances 0.000 description 2
- 229910000278 bentonite Inorganic materials 0.000 description 2
- 238000006056 electrooxidation reaction Methods 0.000 description 2
- 239000002925 low-level radioactive waste Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000004438 BET method Methods 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052768 actinide Inorganic materials 0.000 description 1
- 150000001255 actinides Chemical class 0.000 description 1
- -1 bentonite modified cyclodextrin Chemical class 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 230000002925 chemical effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 229910052681 coesite Inorganic materials 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- HOOWDPSAHIOHCC-UHFFFAOYSA-N dialuminum tricalcium oxygen(2-) Chemical compound [O--].[O--].[O--].[O--].[O--].[O--].[Al+3].[Al+3].[Ca++].[Ca++].[Ca++] HOOWDPSAHIOHCC-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000002927 high level radioactive waste Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052747 lanthanoid Inorganic materials 0.000 description 1
- 150000002602 lanthanoids Chemical class 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000000191 radiation effect Effects 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000002915 spent fuel radioactive waste Substances 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 235000019976 tricalcium silicate Nutrition 0.000 description 1
- 229910021534 tricalcium silicate Inorganic materials 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/02—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
- C04B28/04—Portland cements
-
- 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
- G21F9/165—Cement or cement-like matrix
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00017—Aspects relating to the protection of the environment
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00241—Physical properties of the materials not provided for elsewhere in C04B2111/00
- C04B2111/00258—Electromagnetic wave absorbing or shielding materials
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
- C04B2111/00767—Uses not provided for elsewhere in C04B2111/00 for waste stabilisation purposes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Ceramic Engineering (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明是关于一种废磷酸三丁酯/煤油的水泥固化材料及其水泥固化体的制备方法,废磷酸三丁酯/煤油的水泥固化材料以重量百分比计,其包括:硅酸盐水泥:45.0‑65.0%;粉煤灰:17.0‑38.0%;硅灰:4.0‑6.0%;膨胀剂:4.0‑6.0%;粉状减水剂:0.8‑1.2%;相容性改善剂:5.0‑6.0%;固油材料:2.5‑3.0%。本发明水泥固化材料具有废物包容量大、机械性能稳定、核素离子浸出率低等特点,水泥固化体的制备过程无化学污染、无放射性、无光污染、低噪声。The present invention relates to a kind of cement solidification material of waste tributyl phosphate/kerosene and the preparation method of cement solidification body thereof, the cement solidification material of waste tributyl phosphate/kerosene is calculated by weight percentage, and it comprises: Portland cement: 45.0‑65.0%; fly ash: 17.0‑38.0%; silica fume: 4.0‑6.0%; expansion agent: 4.0‑6.0%; powdered water reducer: 0.8‑1.2%; compatibility improver: 5.0‑6.0 %; solid oil materials: 2.5‑3.0%. The cement solidified material of the invention has the characteristics of large waste storage capacity, stable mechanical properties, low nuclide ion leaching rate and the like, and the preparation process of the cement solidified body has no chemical pollution, no radioactivity, no light pollution and low noise.
Description
技术领域technical field
本发明涉及一种放射性废物处理技术领域,特别是涉及一种废磷酸三丁酯/煤油的水泥固化材料及其水泥固化体的制备方法。The invention relates to the technical field of radioactive waste treatment, in particular to a cement solidification material of waste tributyl phosphate/kerosene and a preparation method of the cement solidification body thereof.
背景技术Background technique
废磷酸三丁酯/煤油(TBP/OK)是萃取处理乏燃料和高放废液中的锕系和镧系元素过程中产生的,是核工业产生的重要的放射性废液,按照GB9133-1995《放射性废物分类标准》规定,其属于中、低放废液。磷酸三丁酯(TBP)作为萃取剂多次循环使用后,受到化学和辐射的作用,发生降解反应性能变差,需要作为放射性废物进行处置。因其放射性核素的化学组成复杂并且易燃、易挥发,处理和整备都需要特殊考虑。Waste tributyl phosphate/kerosene (TBP/OK) is produced during the extraction and treatment of actinides and lanthanides in spent fuel and high-level waste liquid. It is an important radioactive waste liquid produced by the nuclear industry. According to GB9133-1995 The "Radioactive Waste Classification Standard" stipulates that it belongs to medium and low level radioactive waste. After repeated use of tributyl phosphate (TBP) as an extractant, it is subjected to chemical and radiation effects, and its degradation reaction performance deteriorates, so it needs to be disposed of as radioactive waste. Due to the complex chemical composition of radionuclides and their flammability and volatility, special considerations are required for handling and conditioning.
目前,国内外对废磷酸三丁酯/煤油的处置方法主要有焚烧或热解、水解固化、间接电化学氧化、塑料固化和水泥固化等。其中,焚烧或热解需要在高温环境下运行,废液中的磷、硫和氯对设备腐蚀严重且尾气净化复杂,使设施的建造和维护困难。水解固化、间接电化学氧化处理后废物依然需要进行后期水泥固化处置,工艺复杂,处理成本也较高。塑料固化体遇明火容易燃烧、不耐高温,易造成放射性泄露。美国Nochar公司研制的N910聚合物等N系列产品用于固化有机废液,固化体稳定性较好,但同样不耐高温,并且Nochar价格昂贵,其吸收废液之后的固化体是松散的颗粒或者小块,目前国内没有相关的废物体接收标准。水泥固化法广泛用于固化中、低放射性废物,但由于水泥与废磷酸三丁酯/煤油相容性差,导致水泥固化体中废磷酸三丁酯/煤油体积包容量低(小于24%),固化体强度差,单位体积增容大,固化处置效率、安全性和经济性不佳。At present, the disposal methods of waste tributyl phosphate/kerosene at home and abroad mainly include incineration or pyrolysis, hydrolysis solidification, indirect electrochemical oxidation, plastic solidification and cement solidification. Among them, incineration or pyrolysis needs to be operated in a high temperature environment. The phosphorus, sulfur and chlorine in the waste liquid seriously corrode the equipment and the exhaust gas purification is complicated, which makes the construction and maintenance of the facilities difficult. After hydrolytic solidification and indirect electrochemical oxidation treatment, the waste still needs to be treated with cement solidification in the later stage. The process is complicated and the treatment cost is also high. The cured plastic body is easy to burn when exposed to an open flame, is not resistant to high temperature, and may easily cause radioactive leakage. N series products such as N910 polymer developed by Nochar Company in the United States are used to solidify organic waste liquid. The solidified body has good stability, but it is also not resistant to high temperature, and Nochar is expensive. The solidified body after absorbing waste liquid is loose particles or Small pieces, currently there is no relevant waste body acceptance standard in China. The cement solidification method is widely used to solidify medium and low radioactive wastes, but due to the poor compatibility between cement and waste tributyl phosphate/kerosene, the volume inclusion capacity of waste tributyl phosphate/kerosene in the cement solidified body is low (less than 24%), The strength of the cured body is poor, the volume increase per unit volume is large, and the curing disposal efficiency, safety and economy are not good.
发明内容Contents of the invention
本发明的主要目的在于,提供一种新型的废磷酸三丁酯/煤油的水泥固化材料及其水泥固化体的制备方法,所要解决的技术问题是使其水泥基固化材料具有核废物包容量大,核废物处置工艺简单,处理成本低,处理过程无化学污染,从而更加适于实用。The main purpose of the present invention is to provide a new type of waste tributyl phosphate/kerosene cement solidified material and its cement solidified body preparation method, the technical problem to be solved is to make its cement-based solidified material have a large nuclear waste containment capacity , The nuclear waste disposal process is simple, the treatment cost is low, and there is no chemical pollution in the treatment process, so it is more suitable for practical use.
本发明的目的及解决其技术问题是采用以下技术方案来实现的。依据本发明提出的一种废磷酸三丁酯/煤油的水泥固化材料,以重量百分比计,其包括:The purpose of the present invention and the solution to its technical problems are achieved by adopting the following technical solutions. According to the cement solidification material of a kind of waste tributyl phosphate/kerosene that the present invention proposes, by weight percentage, it comprises:
硅酸盐水泥:45.0-65.0%;Portland cement: 45.0-65.0%;
粉煤灰:17.0-38.0%;Fly ash: 17.0-38.0%;
硅灰:4.0-6.0%;Silica fume: 4.0-6.0%;
膨胀剂:4.0-6.0%;Expanding agent: 4.0-6.0%;
粉状减水剂:0.8-1.2%;Powdered water reducer: 0.8-1.2%;
相容性改善剂:5.0-6.0%;Compatibility improver: 5.0-6.0%;
固油材料:2.5-3.0%。Solid oil material: 2.5-3.0%.
本发明的目的及解决其技术问题还可采用以下技术措施进一步实现。The purpose of the present invention and its technical problems can also be further realized by adopting the following technical measures.
优选的,前述的废磷酸三丁酯/煤油的水泥固化材料,其中所述的硅酸盐水泥为高阿利特硅酸盐水泥;所述的粉煤灰为粉煤灰精细沉珠;所述的膨胀剂为硫铝酸钙-氧化钙类混凝土膨胀剂;所述的粉状减水剂为聚羧酸系高性能粉状减水剂;所述的相容性改善剂为钠质蒙脱石;所述的固油材料为有机膨润土改性环糊精基高吸油树脂。Preferably, the cement solidified material of the aforementioned waste tributyl phosphate/kerosene, wherein the Portland cement is a high-alite Portland cement; the fly ash is a fine sinking bead of fly ash; the The expansion agent is calcium sulfoaluminate-calcium oxide concrete expansion agent; the powder water reducer is polycarboxylate high-performance powder water reducer; the compatibility improver is sodium montmorillonite stone; the oil-fixing material is organobentonite modified cyclodextrin-based high oil-absorbing resin.
本发明的目的及解决其技术问题还采用以下的技术方案来实现。依据本发明提出的一种废磷酸三丁酯/煤油的水泥固化体的制备方法,其包括:The purpose of the present invention and the solution to its technical problems are also achieved by the following technical solutions. According to the preparation method of the cement solidified body of a kind of waste tributyl phosphate/kerosene proposed by the present invention, it comprises:
1)将固油材料和废磷酸三丁酯/煤油按重量比1:14-16混合静置,加入相容性改善剂,搅拌,得到固油材料-废磷酸三丁酯/煤油混合料;1) Mix the solid oil material and waste tributyl phosphate/kerosene at a weight ratio of 1:14-16 and let it stand, add a compatibility improving agent and stir to obtain the solid oil material-waste tributyl phosphate/kerosene mixture;
2)将水泥基固化浆体材料和水按重量比1:0.16-0.20混合,搅拌,制得水泥基固化浆体;其中,水泥基固化浆体材料包括硅酸盐水泥、粉煤灰、硅灰、膨胀剂、粉状减水剂;2) Mix the cement-based solidified slurry material and water at a weight ratio of 1:0.16-0.20, and stir to obtain the cement-based solidified slurry; wherein, the cement-based solidified slurry material includes Portland cement, fly ash, silicon Ash, expansion agent, powdered water reducer;
3)将所述的水泥基固化浆体与固油材料-废磷酸三丁酯/煤油混合料混合,搅拌,得到废磷酸三丁酯/煤油的水泥固化体;3) Mix the cement-based solidified slurry with the solid oil material-waste tributyl phosphate/kerosene mixture, and stir to obtain a cement solidified body of waste tributyl phosphate/kerosene;
其中,硅酸盐水泥、粉煤灰、硅灰、膨胀剂、粉状减水剂、相容性改善剂和固油材料为废磷酸三丁酯/煤油的水泥固化材料,其重量百分比为:Wherein, Portland cement, fly ash, silica fume, expansion agent, powdery water reducing agent, compatibility improving agent and solid oil material are cement solidified materials of waste tributyl phosphate/kerosene, and its weight percentage is:
硅酸盐水泥:45.0-65.0%;Portland cement: 45.0-65.0%;
粉煤灰:17.0-38.0%;Fly ash: 17.0-38.0%;
硅灰:4.0-6.0%;Silica fume: 4.0-6.0%;
膨胀剂:4.0-6.0%;Expanding agent: 4.0-6.0%;
粉状减水剂:0.8-1.2%;Powdered water reducer: 0.8-1.2%;
相容性改善剂:5.0-6.0%;Compatibility improver: 5.0-6.0%;
固油材料:2.5-3.0%。Solid oil material: 2.5-3.0%.
本发明的目的及解决其技术问题还可采用以下技术措施进一步实现。The purpose of the present invention and its technical problems can also be further realized by adopting the following technical measures.
优选的,前述的废磷酸三丁酯/煤油的水泥固化体的制备方法,其中所述的硅酸盐水泥为高阿利特硅酸盐水泥;所述的粉煤灰为粉煤灰精细沉珠;所述的膨胀剂为硫铝酸钙-氧化钙类混凝土膨胀剂;所述的粉状减水剂为聚羧酸系高性能粉状减水剂;所述的相容性改善剂为钠质蒙脱石;所述的固油材料为有机膨润土改性环糊精基高吸油树脂。Preferably, the aforementioned preparation method of waste tributyl phosphate/kerosene solidified body of cement, wherein said Portland cement is high-alite Portland cement; said fly ash is fly ash fine pellets The expansion agent is calcium sulfoaluminate-calcium oxide concrete expansion agent; the powdered water reducer is polycarboxylate high-performance powdered water reducer; the compatibility improving agent is sodium quality montmorillonite; the oil-fixing material is organobentonite modified cyclodextrin-based high oil-absorbing resin.
优选的,前述的废磷酸三丁酯/煤油的水泥固化体的制备方法,其中步骤1)中所述的搅拌的速度为6-8m/s。Preferably, the aforementioned method for preparing waste tributyl phosphate/kerosene cement solidified body, wherein the stirring speed in step 1) is 6-8m/s.
优选的,前述的废磷酸三丁酯/煤油的水泥固化体的制备方法,其中步骤2)中所述的搅拌的速度为14-18m/s。Preferably, the aforementioned method for preparing waste tributyl phosphate/kerosene cement solidified body, wherein the stirring speed in step 2) is 14-18m/s.
优选的,前述的废磷酸三丁酯/煤油的水泥固化体的制备方法,其中步骤3)中所述的搅拌的速度为9-12m/s。Preferably, the aforementioned method for preparing waste tributyl phosphate/kerosene cement solidified body, wherein the stirring speed in step 3) is 9-12m/s.
优选的,前述的废磷酸三丁酯/煤油的水泥固化体的制备方法,其中所述的废磷酸三丁酯/煤油的水泥固化体的体积包容量为42-50%。Preferably, the aforementioned method for preparing waste tributyl phosphate/kerosene solidified cement body, wherein the volume inclusion capacity of the waste tributyl phosphate/kerosene cement solidified body is 42-50%.
借由上述技术方案,本发明废磷酸三丁酯/煤油的水泥固化材料及其水泥固化体的制备方法至少具有下列优点:By means of the above-mentioned technical scheme, the preparation method of the cement solidified material of waste tributyl phosphate/kerosene and its cement solidified body of the present invention has the following advantages at least:
1)本发明采用固油材料和相容性改善剂,提高了废磷酸三丁酯/煤油与水泥的相容性,包容量提高为42-50%,极大减少了固化过程中的体积增容,降低了后期处理所占的空间和费用,具有重大的经济效益;1) The present invention adopts solid oil material and compatibility improving agent, has improved the compatibility of waste tributyl phosphate/kerosene and cement, and the inclusion capacity is improved to 42-50%, greatly reduces the volume increase in solidification process It reduces the space and cost of post-processing, and has significant economic benefits;
2)本发明的水泥固化体核素离子浸出率低,Cs(42d)浸出率为1.5-4.9×10-4cm/d,Ce(42d)浸出率为0.76-4.5×10-6cm/d;抗压强度为13.2-17.2MPa;抗冲击性、抗浸泡性、抗冻融性能满足GB14569.1-2011《低、中水平放射性废物固化体性能要求-水泥固化体》与GB7023-86《放射性废物固化体长期浸出试验》的各项指标,具有优良的性能;2) The cement solidified body of the present invention has a low leaching rate of nuclide ions, the leaching rate of Cs(42d) is 1.5-4.9×10 -4 cm/d, and the leaching rate of Ce(42d) is 0.76-4.5×10 -6 cm/d The compressive strength is 13.2-17.2MPa; the impact resistance, immersion resistance and freeze-thaw resistance performance meet GB14569.1-2011 "performance requirements for low and medium level radioactive waste solidified body - cement solidified body" and GB7023-86 "radioactive The various indicators of the long-term leaching test of waste solidified body have excellent performance;
3)本发明的制备方法简单,过程无化学污染、无放射性、无光污染、低噪声,适用于实际生产过程。3) The preparation method of the present invention is simple, the process has no chemical pollution, no radioactivity, no light pollution, and low noise, and is applicable to the actual production process.
上述说明仅是本发明技术方案的概述,为了能够更清楚了解本发明的技术手段,并可依照说明书的内容予以实施,以下以本发明的较佳实施例详细说明如后。The above description is only an overview of the technical solutions of the present invention. In order to understand the technical means of the present invention more clearly and implement them according to the contents of the description, the preferred embodiments of the present invention will be described in detail below.
具体实施方式Detailed ways
为更进一步阐述本发明为达成预定发明目的所采取的技术手段及功效,以下结合较佳实施例,对依据本发明提出的废磷酸三丁酯/煤油的水泥固化材料及其水泥固化体的制备方法其具体实施方式、结构、特征及其功效,详细说明如后。在下述说明中,不同的“一实施例”或“实施例”指的不一定是同一实施例。此外,一或多个实施例中的特定特征、结构、或特点可由任何合适形式组合。For further elaborating the technical means and effect that the present invention takes for reaching the predetermined invention purpose, below in conjunction with preferred embodiment, to the preparation of the cement solidification material of waste tributyl phosphate/kerosene and cement solidification body thereof according to the present invention The specific implementation, structure, features and effects of the method are described in detail below. In the following description, different "one embodiment" or "embodiment" do not necessarily refer to the same embodiment. Furthermore, the particular features, structures, or characteristics of one or more embodiments may be combined in any suitable manner.
本发明的一个实施例提出的一种废磷酸三丁酯/煤油的水泥固化材料,以重量百分比计,其包括:A kind of cement solidified material of waste tributyl phosphate/kerosene that one embodiment of the present invention proposes, in weight percent, it comprises:
硅酸盐水泥:45.0-65.0%;Portland cement: 45.0-65.0%;
粉煤灰:17.0-38.0%;Fly ash: 17.0-38.0%;
硅灰:4.0-6.0%;Silica fume: 4.0-6.0%;
膨胀剂:4.0-6.0%;Expanding agent: 4.0-6.0%;
粉状减水剂:0.8-1.2%;Powdered water reducer: 0.8-1.2%;
相容性改善剂:5.0-6.0%;Compatibility improver: 5.0-6.0%;
固油材料:2.5-3.0%。Solid oil material: 2.5-3.0%.
其中,硅酸盐水泥、粉煤灰、硅灰、膨胀剂、粉状减水剂为水泥基固化浆体材料;水泥基固化浆体材料、相容性改善剂和固油材料三大组分单独包装。Among them, Portland cement, fly ash, silica fume, expansion agent, and powdered water reducer are cement-based solidified slurry materials; three major components are cement-based solidified slurry material, compatibility improver and solid oil material Individually packaged.
优选的,硅酸盐水泥为P·Ⅰ52.5高阿利特硅酸盐水泥,硅酸三钙重量含量68-71%,铝酸三钙重量含量6-7%,游离氧化钙重量含量低于0.8%,氧化镁重量含量低于3.5%,勃氏比表面积为(420±10)m2/kg。Preferably, the Portland cement is P·I52.5 High Alite Portland cement, the weight content of tricalcium silicate is 68-71%, the weight content of tricalcium aluminate is 6-7%, and the weight content of free calcium oxide is less than 0.8%, the weight content of magnesium oxide is less than 3.5%, and the Blaine specific surface area is (420±10)m 2 /kg.
优选的,粉煤灰为粉煤灰精细沉珠,细度d50≤3μm,d95≤10μm,需水量小于90%,28天活性指数大于110%,90天活性指数大于120%。Preferably, the fly ash is fly ash fine pellets, fineness d 50 ≤ 3 μm, d 95 ≤ 10 μm, water demand less than 90%, 28-day activity index greater than 110%, 90-day activity index greater than 120%.
优选的,硅灰符合GB/T 27690-2011标准要求,SiO2重量含量不低于96%,烧失量小于1.0wt%,比表面积(BET法)(23±2)m2/g,需水量小于115%,28d活性指数97-98%。Preferably, the silica fume meets the requirements of the GB/T 27690-2011 standard, the SiO2 weight content is not less than 96%, the ignition loss is less than 1.0wt%, and the specific surface area (BET method) is (23± 2 )m2/g. The water content is less than 115%, and the 28d activity index is 97-98%.
优选的,膨胀剂为符合GB 23439-2009标准要求的硫铝酸钙-氧化钙类混凝土膨胀剂,主要矿物成分为:(以重量百分比计)f-CaO:40-45%;CaSO4:15-20%,绝湿膨胀,水中7天限制膨胀率0.08-0.12%,优选0.10%。充分利用该膨胀剂的绝湿膨胀特性,用于解决水泥固化体的体积收缩,防止水泥固化体与处置桶脱离。Preferably, the expansion agent is a calcium sulfoaluminate-calcium oxide concrete expansion agent that meets the requirements of the GB 23439-2009 standard, and the main mineral components are: (by weight percentage) f-CaO: 40-45%; CaSO 4 : 15 -20%, Absolute moisture expansion, 7 days limit expansion rate in water 0.08-0.12%, preferably 0.10%. Make full use of the moisture-absolute expansion characteristics of the expansion agent to solve the volume shrinkage of the cement solidified body and prevent the cement solidified body from detaching from the disposal bucket.
优选的,粉状减水剂为聚羧酸系高性能粉状减水剂,优选为减缩-早强复合型聚羧酸系减水剂,减水率重量含量大于35%,减少混凝土收缩大于等于30%,室温养护12h抗压强度比大于等于300%。Preferably, the powdery water reducer is a polycarboxylate high-performance powdery water reducer, preferably a shrinkage reduction-early strength composite polycarboxylate water reducer, the water reducing rate is greater than 35% by weight, and the shrinkage of concrete is reduced by more than Equal to 30%, room temperature curing 12h compressive strength ratio is greater than or equal to 300%.
相容性改善剂为钠质蒙脱石,吸蓝量42-43,二氧化硅重量含量不低60%,三氧化铝重量含量不低于15%,细度600-800目,优选700目。钠质蒙脱石在改善固油材料、废磷酸三丁酯/煤油与水泥相容性同时,对核素离子Cs、Ce具有较强的选择性物理吸附能力,增加水泥基固化材料的核素离子固化能力。The compatibility improving agent is sodium montmorillonite, the blue absorption amount is 42-43, the weight content of silica is not less than 60%, the weight content of aluminum oxide is not less than 15%, and the fineness is 600-800 mesh, preferably 700 mesh . Sodium montmorillonite improves the compatibility of solid oil materials, waste tributyl phosphate/kerosene and cement, and has strong selective physical adsorption capacity for nuclide ions Cs and Ce, increasing the nuclide content of cement-based solidified materials. Ionic curing ability.
固油材料为有机膨润土改性环糊精基高吸油树脂,粒径分布0.3-0.6mm,半透明珠状,对煤油和磷酸三丁酯的吸油倍率分别为22克/克和16克/克,保油率95%以上(重量含量)。通过有机膨润土改性,除了增加固油能力外,对核素离子Cs、Ce同样具有较强的物理吸附能力。The oil-fixing material is organic bentonite modified cyclodextrin-based high oil-absorbing resin, particle size distribution 0.3-0.6mm, translucent beads, oil absorption ratios for kerosene and tributyl phosphate are 22 g/g and 16 g/g respectively , The oil retention rate is above 95% (weight content). Modified by organic bentonite, in addition to increasing the oil-fixing capacity, it also has a strong physical adsorption capacity for nuclide ions Cs and Ce.
本发明的另一实施例提出一种废磷酸三丁酯/煤油的水泥固化体的制备方法,其包括:Another embodiment of the present invention proposes a kind of preparation method of the cement solidification body of waste tributyl phosphate/kerosene, it comprises:
1)将固油材料和废磷酸三丁酯/煤油按重量比1:14-16加入处置桶中混合静置3h,加入相容性改善剂,搅拌4-6min,得到固油材料-废磷酸三丁酯/煤油混合料;1) Put the solid oil material and waste tributyl phosphate/kerosene into the disposal barrel at a weight ratio of 1:14-16, mix and stand for 3 hours, add a compatibility improver, stir for 4-6 minutes, and obtain the solid oil material-waste phosphoric acid Tributyl ester/kerosene blend;
2)将水泥基固化浆体材料和水按重量比1:0.16-0.20混合,置于高速制浆机中,搅拌4-6min,制得水泥基固化浆体;其中,水泥基固化浆体材料包括硅酸盐水泥、粉煤灰、硅灰、膨胀剂、粉状减水剂;2) Mix the cement-based solidified slurry material and water at a weight ratio of 1:0.16-0.20, place it in a high-speed pulper, and stir for 4-6 minutes to obtain a cement-based solidified slurry; wherein, the cement-based solidified slurry material Including Portland cement, fly ash, silica fume, expansion agent, powdered water reducer;
3)将所述的水泥基固化浆体加入处置桶,与固油材料-废磷酸三丁酯/煤油混合料混合,搅拌3-5min,得到废磷酸三丁酯/煤油的水泥固化体;3) Add the cement-based solidified slurry into the disposal barrel, mix it with the solid oil material-waste tributyl phosphate/kerosene mixture, and stir for 3-5 minutes to obtain a cement solidified body of waste tributyl phosphate/kerosene;
硅酸盐水泥、粉煤灰、硅灰、膨胀剂、粉状减水剂、相容性改善剂和固油材料为废磷酸三丁酯/煤油的水泥固化材料,其重量百分比为:Portland cement, fly ash, silica fume, expansion agent, powdery water reducing agent, compatibility improving agent and solid oil material are the cement solidified material of waste tributyl phosphate/kerosene, and its weight percentage is:
硅酸盐水泥:45.0-65.0%;Portland cement: 45.0-65.0%;
粉煤灰:17.0-38.0%;Fly ash: 17.0-38.0%;
硅灰:4.0-6.0%;Silica fume: 4.0-6.0%;
膨胀剂:4.0-6.0%;Expanding agent: 4.0-6.0%;
粉状减水剂:0.8-1.2%;Powdered water reducer: 0.8-1.2%;
相容性改善剂:5.0-6.0%;Compatibility improver: 5.0-6.0%;
固油材料:2.5-3.0%。Solid oil material: 2.5-3.0%.
优选的,步骤1)中的搅拌叶线速度6-8m/s,优选为7m/s。Preferably, the linear velocity of the stirring blade in step 1) is 6-8m/s, preferably 7m/s.
优选的,步骤2)中高速制浆机的搅拌叶线速度14-18m/s,优选为16m/s。Preferably, the linear velocity of the stirring blades of the high-speed pulper in step 2) is 14-18m/s, preferably 16m/s.
优选的,步骤3)中搅拌机转速600-800转/min,搅拌叶线速度9-12m/s,优选为10m/s。Preferably, in step 3), the rotational speed of the agitator is 600-800 rpm, and the linear velocity of the stirring blade is 9-12m/s, preferably 10m/s.
本实施例中废磷酸三丁酯/煤油为非放射性模拟中、低放废磷酸三丁酯/煤油,由分析纯试剂磷酸三丁酯和无水煤油按体积比3:7混合制成,并且掺有活度当量为105-6Bq的Cs和Ce,其中Ce用于模拟核素239Pu。The waste tributyl phosphate/kerosene in this example is non-radioactive simulated medium and low-level waste tributyl phosphate/kerosene, which is made by mixing the analytical reagent tributyl phosphate and anhydrous kerosene at a volume ratio of 3:7, and Doped with Cs and Ce with an activity equivalent of 10 5-6 Bq, among which Ce is used to simulate nuclide 239 Pu.
本发明的一个实施例提出一种废磷酸三丁酯/煤油的水泥固化材料,实施例1-12废磷酸三丁酯/煤油的水泥固化材料组分如表1所示。An embodiment of the present invention proposes a cement-cured material of waste tributyl phosphate/kerosene, and the components of the cement-cured material of waste tributyl phosphate/kerosene in Examples 1-12 are shown in Table 1.
表1废磷酸三丁酯/煤油的水泥固化材料的组分(重量百分比%)The component (weight percentage %) of the cement solidification material of table 1 waste tributyl phosphate/kerosene
实施例1Example 1
本发明的一个实施例提出一种废磷酸三丁酯/煤油的水泥固化体的制备方法,其包括:One embodiment of the present invention proposes a kind of preparation method of the cement solidification body of waste tributyl phosphate/kerosene, it comprises:
1)将2.5kg固油材料高吸油树脂和35.0kg废磷酸三丁酯/煤油加入处置桶中混合静置3h,加入5.0kg相容性改善剂钠质蒙脱石,搅拌5min,搅拌叶线速度8m/s,得到固油材料-废磷酸三丁酯/煤油混合料;1) Add 2.5kg of solid oil material super oil-absorbing resin and 35.0kg of waste tributyl phosphate/kerosene into the disposal barrel, mix and let stand for 3 hours, add 5.0kg of compatibility improving agent sodium montmorillonite, stir for 5 minutes, stir the blade line Speed 8m/s, obtain solid oil material-waste tributyl phosphate/kerosene mixture;
2)将45.0kg硅酸盐水泥、35.7kg粉煤灰、6.0kg硅灰、5.0kg膨胀剂和0.8kg粉状减水剂混合均匀制成92.5kg水泥基固化浆体材料,和18.5kg水置于高速制浆机中,搅拌4min,高速制浆机搅拌叶线速度18m/s,制得水泥基固化浆体;2) Mix 45.0kg Portland cement, 35.7kg fly ash, 6.0kg silica fume, 5.0kg expansion agent and 0.8kg powdered water reducing agent to make 92.5kg cement-based solidified slurry material, and 18.5kg water Place in a high-speed pulping machine, stir for 4 minutes, and the linear speed of the stirring blade of the high-speed pulping machine is 18m/s, to obtain a cement-based solidified slurry;
3)将所述的水泥基固化浆体加入处置桶,与固油材料-废磷酸三丁酯/煤油混合料混合,搅拌叶线速度10m/s,搅拌4min,养护固化得到废磷酸三丁酯/煤油的水泥固化体。3) Add the cement-based solidified slurry into the disposal barrel, mix it with the solid oil material-waste tributyl phosphate/kerosene mixture, stir the blade at a linear speed of 10m/s, stir for 4min, and cure and solidify to obtain waste tributyl phosphate / Kerosene cement solidification body.
制备Φ50mm×50mm试样,在温度为25±5℃的环境下养护至相应龄期,按照GB14569.1-2011《低、中水平放射性废物固化体性能要求-水泥固化体》与GB 7023-86《放射性废物固化体长期浸出试验》进行各项性能测试。在42%体积包容量下,抗压强度16.5MPa,抗冲击性、抗冻融性和抗浸泡性合格,Cs(42d)浸出率2.5×10-4cm/d,Ce(42d)浸出率7.6×10-7cm/d。Prepare a Φ50mm×50mm sample, and maintain it to the corresponding age at a temperature of 25±5°C, in accordance with GB14569.1-2011 "Performance Requirements for Low and Medium Level Radioactive Waste Solidified Body-Cement Solidified Body" and GB 7023-86 "Long-term leaching test of solidified radioactive waste" conducts various performance tests. Under 42% volume inclusion capacity, the compressive strength is 16.5 MPa, the impact resistance, freeze-thaw resistance and immersion resistance are qualified, the leaching rate of Cs(42d) is 2.5×10 -4 cm/d, and the leaching rate of Ce(42d) is 7.6 ×10 -7 cm/d.
实施例2Example 2
本发明的一个实施例提出一种废磷酸三丁酯/煤油的水泥固化体的制备方法,其包括:One embodiment of the present invention proposes a kind of preparation method of the cement solidification body of waste tributyl phosphate/kerosene, it comprises:
1)将2.6kg固油材料高吸油树脂和39.0kg废磷酸三丁酯/煤油加入处置桶中混合静置3h,加入5.2kg相容性改善剂钠质蒙脱石,搅拌4min,搅拌叶线速度7m/s,得到固油材料-废磷酸三丁酯/煤油混合料;1) Add 2.6kg of solid oil material high oil-absorbing resin and 39.0kg of waste tributyl phosphate/kerosene into the disposal barrel and mix for 3 hours, add 5.2kg of compatibility improving agent sodium montmorillonite, stir for 4 minutes, and stir the blade line Speed 7m/s, obtain solid oil material-waste tributyl phosphate/kerosene mixture;
2)将50.0kg硅酸盐水泥、32.3kg粉煤灰、5.0kg硅灰、4.0kg膨胀剂和0.9kg粉状减水剂混合均匀制成92.2kg水泥基固化浆体材料,和17.5kg水置于高速制浆机中,搅拌4min,高速制浆机搅拌叶线速度16m/s,制得水泥基固化浆体;2) Mix 50.0kg Portland cement, 32.3kg fly ash, 5.0kg silica fume, 4.0kg expansion agent and 0.9kg powdered water reducing agent to make 92.2kg cement-based solidified slurry material, and 17.5kg water Place in a high-speed pulping machine, stir for 4 minutes, and the linear speed of the stirring blade of the high-speed pulping machine is 16m/s, to obtain a cement-based solidified slurry;
3)将所述的水泥基固化浆体加入处置桶,与固油材料-废磷酸三丁酯/煤油混合料混合,搅拌叶线速度12m/s,搅拌3min,养护固化得到废磷酸三丁酯/煤油的水泥固化体。3) Add the cement-based solidified slurry to the disposal barrel, mix it with the solid oil material-waste tributyl phosphate/kerosene mixture, stir the stirring blade at a linear speed of 12m/s, stir for 3min, and cure and solidify to obtain waste tributyl phosphate / Kerosene cement solidification body.
制备成Φ50mm×50mm试样,在温度为25±5℃的环境下养护至相应龄期,按照GB14569.1-2011《低、中水平放射性废物固化体性能要求-水泥固化体》与GB 7023-86《放射性废物固化体长期浸出试验》进行各项性能测试。在44%体积包容量下,抗压强度14.5MPa,抗冲击性、抗冻融性和抗浸泡性合格,Cs(42d)浸出率2.7×10-4cm/d,Ce(42d)浸出率8.6×10-7cm/d。Prepare a Φ50mm×50mm sample, and maintain it to the corresponding age at a temperature of 25±5°C, in accordance with GB14569.1-2011 "Performance Requirements for Low and Medium Level Radioactive Waste Solidified Body - Cement Solidified Body" and GB 7023- 86 "Long-term leaching test of solidified radioactive waste" conducts various performance tests. Under 44% volume inclusion capacity, the compressive strength is 14.5 MPa, the impact resistance, freeze-thaw resistance and immersion resistance are qualified, the leaching rate of Cs(42d) is 2.7×10 -4 cm/d, and the leaching rate of Ce(42d) is 8.6 ×10 -7 cm/d.
实施例3Example 3
本发明的一个实施例提出一种废磷酸三丁酯/煤油的水泥固化体的制备方法,其包括:One embodiment of the present invention proposes a kind of preparation method of the cement solidification body of waste tributyl phosphate/kerosene, it comprises:
1)将2.7kg固油材料高吸油树脂和43.2kg废磷酸三丁酯/煤油加入处置桶中混合静置3h,加入5.4kg相容性改善剂钠质蒙脱石,搅拌4min,搅拌叶线速度7m/s,得到固油材料-废磷酸三丁酯/煤油混合料;1) Add 2.7kg of solid oil material super oil-absorbing resin and 43.2kg of waste tributyl phosphate/kerosene into the disposal barrel and mix for 3 hours, add 5.4kg of compatibility improving agent sodium montmorillonite, stir for 4 minutes, and stir Speed 7m/s, obtain solid oil material-waste tributyl phosphate/kerosene mixture;
2)将55.0kg硅酸盐水泥、25.9kg粉煤灰、4.0kg硅灰、6.0kg膨胀剂和1.0kg粉状减水剂混合均匀制成91.9kg水泥基固化浆体材料,和17.5kg水置于高速制浆机中,搅拌6min,高速制浆机搅拌叶线速度18m/s,制得水泥基固化浆体;2) Mix 55.0kg Portland cement, 25.9kg fly ash, 4.0kg silica fume, 6.0kg expansion agent and 1.0kg powdered water reducing agent to make 91.9kg cement-based solidified slurry material, and 17.5kg water Place in a high-speed pulping machine, stir for 6 minutes, and the linear speed of the stirring blade of the high-speed pulping machine is 18m/s, to obtain a cement-based solidified slurry;
3)将所述的水泥基固化浆体加入处置桶,与固油材料-废磷酸三丁酯/煤油混合料混合,搅拌叶线速度9m/s,搅拌5min,养护固化得到废磷酸三丁酯/煤油的水泥固化体。3) Add the cement-based solidified slurry into the disposal barrel, mix it with the solid oil material-waste tributyl phosphate/kerosene mixture, stir the stirring blade at a linear speed of 9m/s, stir for 5min, and cure and solidify to obtain waste tributyl phosphate / Kerosene cement solidification body.
制备Φ50mm×50mm试样,在温度为25±5℃的环境下养护至相应龄期,按照GB14569.1-2011《低、中水平放射性废物固化体性能要求-水泥固化体》与GB 7023-86《放射性废物固化体长期浸出试验》进行各项性能测试。在47%体积包容量下,抗压强度16.2MPa,抗冲击性、抗冻融性和抗浸泡性合格,Cs(42d)浸出率3.8×10-4cm/d,Ce(42d)浸出率1.1×10-6cm/d。Prepare a Φ50mm×50mm sample, and maintain it to the corresponding age at a temperature of 25±5°C, in accordance with GB14569.1-2011 "Performance Requirements for Low and Medium Level Radioactive Waste Solidified Body-Cement Solidified Body" and GB 7023-86 "Long-term leaching test of solidified radioactive waste" conducts various performance tests. Under 47% volume inclusion capacity, the compressive strength is 16.2MPa, the impact resistance, freeze-thaw resistance and immersion resistance are qualified, the leaching rate of Cs(42d) is 3.8×10 -4 cm/d, and the leaching rate of Ce(42d) is 1.1 ×10 -6 cm/d.
实施例4Example 4
本发明的一个实施例提出一种废磷酸三丁酯/煤油的水泥固化体的制备方法,其包括:One embodiment of the present invention proposes a kind of preparation method of the cement solidification body of waste tributyl phosphate/kerosene, it comprises:
1)将2.8kg固油材料高吸油树脂和44.8kg废磷酸三丁酯/煤油加入处置桶中混合静置3h,加入5.6kg相容性改善剂钠质蒙脱石,搅拌5min,搅拌叶线速度7m/s,得到固油材料-废磷酸三丁酯/煤油混合料;1) Add 2.8kg of solid oil material high oil-absorbing resin and 44.8kg of waste tributyl phosphate/kerosene into the disposal barrel, mix and let stand for 3 hours, add 5.6kg of compatibility improving agent sodium montmorillonite, stir for 5 minutes, and stir the blade line Speed 7m/s, obtain solid oil material-waste tributyl phosphate/kerosene mixture;
2)将60.0kg硅酸盐水泥、20.0kg粉煤灰、5.5kg硅灰、5.0kg膨胀剂和1.1kg粉状减水剂混合均匀制成91.6kg水泥基固化浆体材料,和15.6kg水置于高速制浆机中,搅拌5min,高速制浆机搅拌叶线速度15m/s,制得水泥基固化浆体;2) Mix 60.0kg Portland cement, 20.0kg fly ash, 5.5kg silica fume, 5.0kg expansion agent and 1.1kg powdered water reducing agent to make 91.6kg cement-based solidified slurry material, and 15.6kg water Place in a high-speed pulping machine, stir for 5 minutes, and the linear speed of the stirring blade of the high-speed pulping machine is 15m/s, to obtain a cement-based solidified slurry;
3)将所述的水泥基固化浆体加入处置桶,与固油材料-废磷酸三丁酯/煤油混合料混合,搅拌叶线速度10m/s,搅拌4min,养护固化得到废磷酸三丁酯/煤油的水泥固化体。3) Add the cement-based solidified slurry into the disposal barrel, mix it with the solid oil material-waste tributyl phosphate/kerosene mixture, stir the blade at a linear speed of 10m/s, stir for 4min, and cure and solidify to obtain waste tributyl phosphate / Kerosene cement solidification body.
制备Φ50mm×50mm试样,在温度为25±5℃的环境下养护至相应龄期,按照GB14569.1-2011《低、中水平放射性废物固化体性能要求-水泥固化体》与GB 7023-86《放射性废物固化体长期浸出试验》进行各项性能测试。在48%体积包容量下,抗压强度13.9MPa,抗冲击性、抗冻融性和抗浸泡性合格,Cs(42d)浸出率4.9×10-4cm/d,Ce(42d)浸出率4.5×10-6cm/d。Prepare a Φ50mm×50mm sample, and maintain it to the corresponding age at a temperature of 25±5°C, in accordance with GB14569.1-2011 "Performance Requirements for Low and Medium Level Radioactive Waste Solidified Body-Cement Solidified Body" and GB 7023-86 "Long-term leaching test of solidified radioactive waste" conducts various performance tests. Under 48% volume inclusion capacity, the compressive strength is 13.9MPa, the impact resistance, freeze-thaw resistance and immersion resistance are qualified, the leaching rate of Cs(42d) is 4.9×10 -4 cm/d, and the leaching rate of Ce(42d) is 4.5 ×10 -6 cm/d.
实施例5Example 5
本发明的一个实施例提出一种废磷酸三丁酯/煤油的水泥固化体的制备方法,其包括:One embodiment of the present invention proposes a kind of preparation method of the cement solidification body of waste tributyl phosphate/kerosene, it comprises:
1)将3.0kg固油材料高吸油树脂和48.0kg废磷酸三丁酯/煤油加入处置桶中混合静置3h,加入5.8kg相容性改善剂钠质蒙脱石,搅拌5min,搅拌叶线速度7m/s,得到固油材料-废磷酸三丁酯/煤油混合料;1) Add 3.0kg of solid oil material high oil-absorbing resin and 48.0kg of waste tributyl phosphate/kerosene into the disposal barrel, mix and let stand for 3 hours, add 5.8kg of compatibility improving agent sodium montmorillonite, stir for 5 minutes, stir the blade line Speed 7m/s, obtain solid oil material-waste tributyl phosphate/kerosene mixture;
2)将65.0kg硅酸盐水泥、17.0kg粉煤灰、4.0kg硅灰、4.0kg膨胀剂和1.2kg粉状减水剂混合均匀制成91.2kg水泥基固化浆体材料,和14.6kg水置于高速制浆机中,搅拌6min,高速制浆机搅拌叶线速度16m/s,制得水泥基固化浆体;2) Mix 65.0kg Portland cement, 17.0kg fly ash, 4.0kg silica fume, 4.0kg expansion agent and 1.2kg powdered water reducing agent to make 91.2kg cement-based solidified slurry material, and 14.6kg water Place in a high-speed pulping machine, stir for 6 minutes, and the linear speed of the stirring blade of the high-speed pulping machine is 16m/s, to obtain a cement-based solidified slurry;
3)将所述的水泥基固化浆体加入处置桶,与固油材料-废磷酸三丁酯/煤油混合料混合,搅拌叶线速度10m/s,搅拌4min,养护固化得到废磷酸三丁酯/煤油的水泥固化体。3) Add the cement-based solidified slurry into the disposal barrel, mix it with the solid oil material-waste tributyl phosphate/kerosene mixture, stir the blade at a linear speed of 10m/s, stir for 4min, and cure and solidify to obtain waste tributyl phosphate / Kerosene cement solidification body.
制备Φ50mm×50mm试样,在温度为25±5℃的环境下养护至相应龄期,按照GB14569.1-2011《低、中水平放射性废物固化体性能要求-水泥固化体》与GB 7023-86《放射性废物固化体长期浸出试验》进行各项性能测试。在50%体积包容量下,抗压强度17.8MPa,抗冲击性、抗冻融性和抗浸泡性合格,Cs(42d)浸出率4.4×10-4cm/d,Ce(42d)浸出率3.8×10-6cm/d。Prepare a Φ50mm×50mm sample, and maintain it to the corresponding age at a temperature of 25±5°C, in accordance with GB14569.1-2011 "Performance Requirements for Low and Medium Level Radioactive Waste Solidified Body-Cement Solidified Body" and GB 7023-86 "Long-term leaching test of solidified radioactive waste" conducts various performance tests. Under 50% volume inclusion capacity, the compressive strength is 17.8 MPa, the impact resistance, freeze-thaw resistance and immersion resistance are qualified, the leaching rate of Cs(42d) is 4.4×10 -4 cm/d, and the leaching rate of Ce(42d) is 3.8 ×10 -6 cm/d.
实施例6-12的废磷酸三丁酯/煤油的水泥固化体的制备方法步骤如实施例1-5,废磷酸三丁酯/煤油的水泥固化材料组分如表1所示,水泥固化体的制备工艺参数如表2所示。The preparation method step of the cement solidified body of waste tributyl phosphate/kerosene of embodiment 6-12 is as embodiment 1-5, and the cement solidified material component of waste tributyl phosphate/kerosene is as shown in Table 1, cement solidified body The preparation process parameters are shown in Table 2.
表2废磷酸三丁酯/煤油水泥固化体的制备工艺参数Table 2 The preparation process parameters of waste tributyl phosphate/kerosene cement solidified body
按照GB14569.1-2011《低、中水平放射性废物固化体性能要求-水泥固化体》与GB7023-86《放射性废物固化体长期浸出试验》进行各项性能测试,实施例1-12废磷酸三丁脂/煤油的水泥固化体测试结果见表3。Perform various performance tests according to GB14569.1-2011 "Performance Requirements for Low and Medium Level Radioactive Waste Solidified Body-Cement Solidified Body" and GB7023-86 "Long-term Leaching Test of Radioactive Waste Solidified Body", Example 1-12 waste tributyl phosphate Table 3 shows the test results of grease/kerosene cement solidified body.
表3废磷酸三丁脂/煤油的水泥固化体测试结果Table 3 waste tributyl phosphate/kerosene cement solidified body test results
以上所述,仅是本发明的较佳实施例而已,并非对本发明作任何形式上的限制,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明技术方案的范围内。The above are only preferred embodiments of the present invention, and are not intended to limit the present invention in any form. Any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention still belong to the present invention. within the scope of the technical solution of the invention.
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