CN110526642A - A kind of cement solidification method of mixed burning waste residue - Google Patents
A kind of cement solidification method of mixed burning waste residue Download PDFInfo
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- CN110526642A CN110526642A CN201910747183.6A CN201910747183A CN110526642A CN 110526642 A CN110526642 A CN 110526642A CN 201910747183 A CN201910747183 A CN 201910747183A CN 110526642 A CN110526642 A CN 110526642A
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- 239000002699 waste material Substances 0.000 title claims abstract description 50
- 238000000034 method Methods 0.000 title claims abstract description 30
- 239000004568 cement Substances 0.000 title claims abstract description 24
- 238000007711 solidification Methods 0.000 title claims abstract description 21
- 230000008023 solidification Effects 0.000 title claims abstract description 21
- 238000002386 leaching Methods 0.000 claims abstract description 17
- 239000002028 Biomass Substances 0.000 claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000011973 solid acid Substances 0.000 claims abstract description 12
- 239000011268 mixed slurry Substances 0.000 claims abstract description 8
- 239000003381 stabilizer Substances 0.000 claims abstract description 8
- 239000007800 oxidant agent Substances 0.000 claims abstract description 7
- 239000010881 fly ash Substances 0.000 claims abstract description 6
- 230000001590 oxidative effect Effects 0.000 claims abstract description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-L Phosphate ion(2-) Chemical compound OP([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-L 0.000 claims abstract description 5
- 239000003365 glass fiber Substances 0.000 claims abstract description 5
- 239000011398 Portland cement Substances 0.000 claims abstract description 4
- YDEXUEFDPVHGHE-GGMCWBHBSA-L disodium;(2r)-3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Na+].[Na+].COC1=CC=CC(C[C@H](CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O YDEXUEFDPVHGHE-GGMCWBHBSA-L 0.000 claims abstract 2
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 6
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 claims description 5
- 235000019345 sodium thiosulphate Nutrition 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims description 3
- 238000012423 maintenance Methods 0.000 claims description 3
- 239000012286 potassium permanganate Substances 0.000 claims description 3
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Chemical compound [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 claims description 3
- 230000002378 acidificating effect Effects 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 239000002480 mineral oil Substances 0.000 claims description 2
- 235000010446 mineral oil Nutrition 0.000 claims description 2
- 239000003960 organic solvent Substances 0.000 claims description 2
- 239000003973 paint Substances 0.000 claims description 2
- ZOCLAPYLSUCOGI-UHFFFAOYSA-M potassium hydrosulfide Chemical compound [SH-].[K+] ZOCLAPYLSUCOGI-UHFFFAOYSA-M 0.000 claims description 2
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims description 2
- DPLVEEXVKBWGHE-UHFFFAOYSA-N potassium sulfide Chemical compound [S-2].[K+].[K+] DPLVEEXVKBWGHE-UHFFFAOYSA-N 0.000 claims description 2
- HYHCSLBZRBJJCH-UHFFFAOYSA-M sodium hydrosulfide Chemical compound [Na+].[SH-] HYHCSLBZRBJJCH-UHFFFAOYSA-M 0.000 claims description 2
- DCERHCFNWRGHLK-UHFFFAOYSA-N C[Si](C)C Chemical compound C[Si](C)C DCERHCFNWRGHLK-UHFFFAOYSA-N 0.000 claims 1
- 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 1
- 230000037396 body weight Effects 0.000 claims 1
- 239000003921 oil Substances 0.000 claims 1
- 235000019394 potassium persulphate Nutrition 0.000 claims 1
- 239000011734 sodium Substances 0.000 claims 1
- 229910052708 sodium Inorganic materials 0.000 claims 1
- 239000000758 substrate Substances 0.000 claims 1
- 239000002920 hazardous waste Substances 0.000 abstract description 29
- 238000001723 curing Methods 0.000 abstract description 14
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 9
- 239000002893 slag Substances 0.000 abstract description 6
- 239000000654 additive Substances 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 238000004056 waste incineration Methods 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229920005552 sodium lignosulfonate Polymers 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- LCPVQAHEFVXVKT-UHFFFAOYSA-N 2-(2,4-difluorophenoxy)pyridin-3-amine Chemical compound NC1=CC=CN=C1OC1=CC=C(F)C=C1F LCPVQAHEFVXVKT-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- ZODDGFAZWTZOSI-UHFFFAOYSA-N nitric acid;sulfuric acid Chemical compound O[N+]([O-])=O.OS(O)(=O)=O ZODDGFAZWTZOSI-UHFFFAOYSA-N 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 238000006277 sulfonation reaction Methods 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 239000012756 surface treatment agent Substances 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc 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
- C04B20/00—Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
- C04B20/02—Treatment
- C04B20/023—Chemical treatment
-
- 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
-
- 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
- C04B2111/00784—Uses not provided for elsewhere in C04B2111/00 for waste stabilisation purposes for disposal only
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明公开了一种混合焚烧废渣的水泥固化方法,包括以下步骤:(1)取一定质量的混合焚烧废渣,加入氧化剂和水,搅拌一定时间,然后加入稳定剂,继续搅拌一定时间;(2)向步骤(1)中得到混合浆料中分别加入若干份粉煤灰、双三甲基硅基磷酸氢酯,搅拌一定时间;(3)向步骤(2)中得到混合浆料中加入若干份硅酸盐水泥、木质素磺酸钠、生物质基固体酸和玻璃纤维,然后加适量水,搅拌至均匀后在室温环境放置一定时间后得到固化体;(4)取水对固化体进行浇淋养护;通过该固化方法制备的固化体重金属浸出率低,满足《危险废物填埋污染控制标准》中规定的危险废物允许进入填埋区的限值,实现了混合焚烧废渣的集中处理,具有重要的意义。The invention discloses a cement solidification method for mixed incineration waste slag, which comprises the following steps: (1) Take a certain quality of mixed incineration waste slag, add oxidant and water, stir for a certain period of time, then add a stabilizer, and continue stirring for a certain period of time; (2) ) Add several parts of fly ash and bistrimethylsilyl hydrogen phosphate to the mixed slurry obtained in step (1), and stir for a certain period of time; (3) Add some parts to the mixed slurry obtained in step (2) Portland cement, sodium lignin sulfonate, biomass-based solid acid and glass fiber, then add appropriate amount of water, stir until uniform, and place it at room temperature for a certain period of time to obtain a solidified body; (4) Take water to pour the solidified body The leaching rate of solidified heavy metals prepared by this curing method is low, which meets the limit value of hazardous waste allowed to enter the landfill specified in the "Hazardous Waste Landfill Pollution Control Standard", and realizes the centralized treatment of mixed incineration waste residues. Significance.
Description
技术领域technical field
本发明涉及焚烧废渣处理领域,具体为一种混合焚烧废渣的水泥固化方法。The invention relates to the field of incineration waste residue treatment, in particular to a cement solidification method for mixing incineration waste residue.
背景技术Background technique
焚烧法处理危险废物即能够降低危险废物在环境中所占体积,又可以转化和减少危险废物中的有害组分,是目前国内外普遍使用的一种处理危险废物的方法。可是,焚烧处理危险废物可能会产生一系列的再生污染,例如焚烧过程中产生的烟尘、氮氧化物、硫氧化物、焚烧废渣等。水泥固化危险废物焚烧废渣是国内外处理危险废物焚烧废渣的普遍方法。Incineration treatment of hazardous wastes can not only reduce the volume of hazardous wastes in the environment, but also transform and reduce the harmful components in hazardous wastes. It is a method commonly used at home and abroad to treat hazardous wastes. However, the incineration of hazardous waste may produce a series of secondary pollution, such as smoke, nitrogen oxides, sulfur oxides, and incineration residues generated during the incineration process. Cement solidification of hazardous waste incineration residues is a common method for treating hazardous waste incineration residues at home and abroad.
按照国家标准,鉴别出的一类至少具备有腐蚀性、毒性、易燃性、反应性、感染性五大危险特性之一的或者列入国家危险废物名录上的,可能危害环境或人体健康的废物被称之为危险废物。危险废物焚烧废渣是指经过挑选的可以用来焚烧处理的危险废物,在控制氧气、危险废物量等焚烧条件下燃烧,发生氧化反应,生成的剩余物质就叫做危险废物焚烧废渣。水泥固化危险废物焚烧废渣,不仅能够降低有害组分浓度,而且运行费用较低,操作过程较为简单,固化块稳定。但是目前而言,水泥固化焚烧废渣仍存在一些技术问题。例如,水泥固化废渣由于废渣成分的不同,需要合理调配固化剂的成分,否则会造成固化体的固化强度不高,造成固化体在一定的情况下,如高压出现二次崩塌,造成污染物的二次扩散。由于焚烧废渣中常常存在一些重金属残留,在固化体的堆放过程中存在重金属浸出的问题。此外,由于水泥固化法中需要采用大量的水泥进行固化,水泥具有较大的碱性,且水泥固化添加剂中常添加一些碱性添加剂以对重金属进行处理,常常导致废渣的浸出液碱性超标,不符合相应的废物填埋标准《危险废物填埋污染控制标准(GB18598-2001)》。对于水泥固化添加剂而言,目前采用的复合添加剂通常是一次性加入,对添加剂功能的有效发挥造成了一定的影响。In accordance with national standards, a class of wastes identified that have at least one of the five hazardous characteristics of corrosiveness, toxicity, flammability, reactivity, and infectivity or that are included in the national list of hazardous wastes and may endanger the environment or human health called hazardous waste. Hazardous waste incineration slag refers to selected hazardous waste that can be used for incineration treatment. It is burned under incineration conditions such as controlled oxygen and hazardous waste, and an oxidation reaction occurs. The resulting residue is called hazardous waste incineration slag. Cement solidification of hazardous waste incineration residue can not only reduce the concentration of harmful components, but also lower operating costs, the operation process is relatively simple, and the solidified block is stable. But for now, there are still some technical problems in cement solidification of incineration waste. For example, due to the different components of cement solidified waste residue, it is necessary to reasonably adjust the composition of the curing agent, otherwise the solidified body will have low curing strength, causing the solidified body to collapse twice under certain circumstances, such as high pressure, resulting in pollution. secondary diffusion. Since there are often some heavy metal residues in the incineration waste residue, there is a problem of heavy metal leaching during the stacking process of the solidified body. In addition, because the cement curing method needs to use a large amount of cement for curing, the cement has a large alkalinity, and some alkaline additives are often added to the cement curing additives to treat heavy metals, which often leads to the alkalinity of the leachate of the waste residue exceeding the standard, which does not meet the requirements. Corresponding waste landfill standard "Hazardous Waste Landfill Pollution Control Standard (GB18598-2001)". For cement curing additives, the currently used composite additives are usually added at one time, which has a certain impact on the effective function of the additive.
发明内容Contents of the invention
本发明的发明目的在于解决现有技术中存在的上述技术问题,The purpose of the invention of the present invention is to solve the above-mentioned technical problems existing in the prior art,
为了实现上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种混合焚烧废渣的水泥固化方法,包括以下步骤:A cement solidification method for mixing incineration waste slag, comprising the following steps:
(1)按照质量份数计,取混合焚烧废渣100份,加入氧化剂1-8份,加入水80-160份,搅拌5-20分钟,然后加入稳定剂5-20份,继续搅拌20-60分钟;(1) According to the number of parts by mass, take 100 parts of mixed incineration waste residue, add 1-8 parts of oxidant, add 80-160 parts of water, stir for 5-20 minutes, then add 5-20 parts of stabilizer, continue stirring for 20-60 minute;
(2)向步骤(1)中得到混合浆料中继续加入粉煤灰20-50份、双三甲基硅基磷酸氢酯1-3份,搅拌5-10分钟;(2) Continue to add 20-50 parts of fly ash and 1-3 parts of bistrimethylsilyl hydrogen phosphate to the mixed slurry obtained in step (1), and stir for 5-10 minutes;
(3)向步骤(2)中得到混合浆料中加入硅酸盐水泥30-60份、木质素磺酸钠5-15份、生物质基固体酸10-25份和玻璃纤维5-12份,然后加水30-70份,搅拌至均匀后在室温环境放置10-24h后得到固化体;(3) Add 30-60 parts of Portland cement, 5-15 parts of sodium lignosulfonate, 10-25 parts of biomass-based solid acid and 5-12 parts of glass fiber to the mixed slurry obtained in step (2) , then add 30-70 parts of water, stir until evenly placed at room temperature for 10-24 hours to obtain a cured body;
(4)按照固化体重量的10-15%取水对固化体进行浇淋养护,每日两次,养护周期为5-15天。(4) Take water according to 10-15% of the weight of the solidified body to carry out pouring maintenance on the solidified body, twice a day, and the curing period is 5-15 days.
进一步的,所述氧化剂选自高锰酸钾、过硫酸钾、过硫酸钠或过硫酸铵。Further, the oxidizing agent is selected from potassium permanganate, potassium persulfate, sodium persulfate or ammonium persulfate.
进一步的,所述混合焚烧废渣为有机溶剂焚烧废渣、矿物油焚烧废渣、表面处理剂焚烧废渣、医疗垃圾焚烧废渣和废油漆焚烧废渣的混合物。Further, the mixed incineration waste is a mixture of organic solvent incineration waste, mineral oil incineration waste, surface treatment agent incineration waste, medical waste incineration waste and waste paint incineration waste.
进一步的,所述稳定剂选自硫氢化钠,硫化钾、硫化钠、硫代硫酸钠或硫氢化钾中的一种或几种。Further, the stabilizer is selected from one or more of sodium hydrosulfide, potassium sulfide, sodium sulfide, sodium thiosulfate or potassium hydrosulfide.
进一步的,所述稳定剂为硫代硫酸钠。Further, the stabilizer is sodium thiosulfate.
进一步的,所述生物质基固体酸的酸味位点不小于0.5mol/g。对于生物质基固体酸催化剂,可采用的多种方法制备,如热解-磺化法,将经破碎的生物质原料,如木材,秸秆等烘干处理,然后在惰性气体下高温热解形成生物质炭化物,将上述生物质炭化物至于浓硫酸中磺化处理,经去离子水洗涤后烘干即得到所需的生物质固体酸。当然,也可通过其他现有技术中公开的方法处理生物质材料获得相应的生物质固体酸。Further, the sour sites of the biomass-based solid acid are not less than 0.5 mol/g. For biomass-based solid acid catalysts, a variety of methods can be used to prepare, such as pyrolysis-sulfonation method, the crushed biomass raw materials, such as wood, straw, etc. are dried, and then pyrolyzed at high temperature under inert gas to form Biomass charcoal, sulfonate the above biomass charcoal in concentrated sulfuric acid, wash with deionized water and then dry to obtain the desired biomass solid acid. Of course, the corresponding biomass solid acid can also be obtained by treating the biomass material through other methods disclosed in the prior art.
本发明的有益效果在于:The beneficial effects of the present invention are:
为了实现对焚烧废渣中重金属的固定,通过对氧化剂对废渣中进行充分氧化,一方面有利于废渣本身与后续添加剂,如粉煤灰和水泥与废渣之间的固化,更主要的是,有利于后续添加的重金属稳定剂与废渣中重金属发生相应的氢氧化物络合物,这对防止废渣中重金属的浸出是十分有力的。通过添加生物质固体酸,可以在固化体氧化过程中,有效调控固化体的浸出液的pH值,通过探索添加剂的添加顺序并且优化了添加剂的添加比例,达到水泥固化的国家堆放标准的要求。In order to achieve the fixation of heavy metals in the incineration waste residue, the oxidant is fully oxidized in the waste residue, on the one hand, it is beneficial to the solidification between the waste residue itself and subsequent additives, such as fly ash and cement, and the waste residue, and more importantly, It is beneficial to The heavy metal stabilizer added later will form corresponding hydroxide complexes with the heavy metals in the waste residue, which is very effective in preventing the leaching of heavy metals in the waste residue. By adding biomass solid acid, the pH value of the leaching solution of the solidified body can be effectively regulated during the oxidation process of the solidified body. By exploring the order of adding additives and optimizing the proportion of additives added, the requirements of the national stacking standard for cement curing can be met.
具体实施方式Detailed ways
下面将通过具体实施例对本发明进行进一步说明The present invention will be further described below by specific embodiment
本发明处理的混合焚烧废渣取自马鞍山危险废物集中处置中心。The mixed incineration waste treated by the present invention is taken from Ma'anshan Hazardous Waste Centralized Disposal Center.
实施例1Example 1
一种混合焚烧废渣的水泥固化方法,包括以下步骤:A cement solidification method for mixing incineration waste slag, comprising the following steps:
(1)按照质量份数计,取混合焚烧废渣100份,加入高锰酸钾1份,加入水100份,搅拌5-20分钟,然后加入硫代硫酸钠5份,继续搅拌20分钟;(1) According to the number of parts by mass, take 100 parts of mixed incineration waste residue, add 1 part of potassium permanganate, add 100 parts of water, stir for 5-20 minutes, then add 5 parts of sodium thiosulfate, and continue stirring for 20 minutes;
(2)向步骤(1)中得到混合浆料中继续加入粉煤灰20份、双三甲基硅基磷酸氢酯2份,搅拌5-10分钟;(2) Continue to add 20 parts of fly ash and 2 parts of bistrimethylsilyl hydrogen phosphate to the mixed slurry obtained in step (1), and stir for 5-10 minutes;
(3)向步骤(2)中得到混合浆料中加入硅酸盐水泥30份、木质素磺酸钠5份、酸性位点为0.5mol/g的生物质基固体酸10份和玻璃纤维8份,然后加水50份,搅拌至均匀后在室温环境放置10h后得到固化体;(3) Add 30 parts of Portland cement, 5 parts of sodium lignosulfonate, 10 parts of biomass-based solid acid with an acid site of 0.5 mol/g and 8 parts of glass fiber to the mixed slurry obtained in step (2). part, then add 50 parts of water, stir until uniform, and place it at room temperature for 10 hours to obtain a cured body;
(4)按照固化体重量的10%取水对固化体进行浇淋养护,每日两次,养护周期为5天。(4) Take water according to 10% of the weight of the solidified body to carry out pouring maintenance on the solidified body, twice a day, and the curing period is 5 days.
考虑到将混合焚烧废渣的固化体运至垃圾填埋厂进行填埋,其在酸性条件下的浸出毒性,并分析该种固化工艺所形成的固化块在酸雨等条件下是否会产生二次污染。这里采用硫酸—硝酸法对原样,固化后样,养护后样,水泥等进行浸出实验,将预先配置好的浓硫酸和浓硝酸混和液加入到超纯水中,调节pH,使pH在3.15-3.25之间。称取5g相关的样品,按液固比为10:1加入所需要的浸提剂后,旋紧瓶盖后固定在翻转振荡器上,设置振荡时间为18 h。振荡结束后,取下瓶子在0.6-0.8um滤膜上采用高压过滤装置进行过滤,得到澄清液体即为浸出液。将浸提出来的液体立即用直径为0.45 um滤膜过滤,用pH计测定其pH值。将浸提出来的溶液加入适量硝酸调节pH<2.0,然后直接用等离子体发射光谱仪进行测定各浸出液中金属的含量。Considering the leaching toxicity of the solidified body of mixed incineration waste residues transported to landfills for landfill under acidic conditions, and analyze whether the solidified blocks formed by this solidification process will produce secondary pollution under conditions such as acid rain . Here, the sulfuric acid-nitric acid method is used to carry out the leaching experiment on the original sample, the sample after curing, the sample after curing, cement, etc., and add the pre-configured concentrated sulfuric acid and concentrated nitric acid mixture into the ultrapure water to adjust the pH to make the pH between 3.15- Between 3.25. Weigh 5 g of the relevant sample, add the required extractant according to the liquid-solid ratio of 10:1, tighten the cap of the bottle and fix it on an inversion oscillator, and set the oscillation time to 18 h. After the shaking is over, remove the bottle and filter it on a 0.6-0.8um filter membrane using a high-pressure filter device to obtain a clear liquid that is the leachate. Immediately filter the leached liquid through a filter membrane with a diameter of 0.45 um, and measure its pH value with a pH meter. An appropriate amount of nitric acid is added to the leached solution to adjust the pH<2.0, and then the metal content in each leached solution is directly measured with a plasma emission spectrometer.
通过上述方法对浸出液进行检测可知,经实施例1的方法固化后,浸出液的各金属原始浸出值满足《危险废物填埋污染控制标准(GB18598-2001)》中规定的危险废物允许进入填埋区的控制限值,其中浸出的pH值为10。It can be known from the detection of the leachate by the above method that after solidification by the method of Example 1, the original leaching value of each metal in the leachate meets the requirements in the "Hazardous Waste Landfill Pollution Control Standard (GB18598-2001)" that hazardous waste is allowed to enter the landfill area The control limit of which the pH value of leaching is 10.
实施例2Example 2
参照实施例1中步骤制备对混合焚烧废渣进行固化,所不同的在于,步骤(1)中氧化剂采用过硫酸铵2份,步骤(3)中采用生物质固体酸的酸性位点为1.3mol/g。Refer to the steps in Example 1 to solidify the mixed incineration waste residue. The difference is that the oxidant in step (1) uses 2 parts of ammonium persulfate, and the acid site of biomass solid acid in step (3) is 1.3 mol/ g.
经实施例2方法的固化后,浸出液的各金属原始浸出值满足《危险废物填埋污染控制标准(GB18598-2001)》中规定的危险废物允许进入填埋区的控制限值,其中pH的浸出值为9。After solidification by the method in Example 2, the original leaching value of each metal in the leach solution meets the control limit for hazardous wastes allowed to enter the landfill specified in the "Hazardous Waste Landfill Pollution Control Standard (GB18598-2001)", wherein the leaching of pH The value is 9.
实施例3Example 3
参照实施例1中步骤制备对混合焚烧废渣进行固化,所不同的在于,步骤(3)中玻璃纤维的加入量为12份。The mixed incineration waste residue was solidified with reference to the steps in Example 1, except that the amount of glass fiber added in step (3) was 12 parts.
经实施例3方法的固化后,浸出液的各金属原始浸出值满足《危险废物填埋污染控制标准(GB18598-2001)》中规定的危险废物允许进入填埋区的控制限值,其中pH的浸出值为10,与实施例1相比,本实施例中的固化体的强度提升了23%,可以满足填埋场的填埋要求。After solidification by the method in Example 3, the original leaching value of each metal in the leach solution meets the control limit for hazardous wastes allowed to enter the landfill specified in the "Hazardous Waste Landfill Pollution Control Standard (GB18598-2001)", wherein the leaching of pH The value is 10. Compared with Example 1, the strength of the cured body in this example has been improved by 23%, which can meet the landfill requirements of the landfill.
实施例4Example 4
参照实施例1中步骤制备对混合焚烧废渣进行固化,所不同的在于,步骤(4)中养护周期为10天。The mixed incineration waste was solidified with reference to the steps in Example 1, except that the curing period in step (4) was 10 days.
经实施例2方法的固化后,浸出液的各金属原始浸出值满足《危险废物填埋污染控制标准(GB18598-2001)》中规定的危险废物允许进入填埋区的控制限值,其中pH的浸出值为9。可见,随着养护时间的加长,有利于固化体的酸碱性平衡。After solidification by the method in Example 2, the original leaching value of each metal in the leach solution meets the control limit for hazardous wastes allowed to enter the landfill specified in the "Hazardous Waste Landfill Pollution Control Standard (GB18598-2001)", wherein the leaching of pH The value is 9. It can be seen that as the curing time increases, it is beneficial to the acid-base balance of the cured body.
对比例1Comparative example 1
参照实施例1中步骤制备对混合焚烧废渣进行固化,所不同的在于,在步骤(3)中不添加生物质基固体酸。The mixed incineration waste residue was solidified with reference to the steps in Example 1, except that no biomass-based solid acid was added in step (3).
经对比例1方法的固化后,其固化体浸出液的各金属原始浸出值满足《危险废物填埋污染控制标准(GB18598-2001)》中规定的危险废物允许进入填埋区的控制限值,但是pH的浸出值为13,超过了填埋入场标准(7-12)。After being solidified by the method of Comparative Example 1, the original leaching value of each metal in the leachate of the solidified body meets the control limit for hazardous wastes allowed to enter the landfill specified in the "Hazardous Waste Landfill Pollution Control Standard (GB18598-2001)", but The pH leach value was 13, exceeding the landfill entry criteria (7-12).
对比例2Comparative example 2
参照实施例1中步骤制备对混合焚烧废渣进行固化,所不同的在于,省去步骤(2),将粉煤灰20份和双三甲基硅基磷酸氢酯2份与步骤(3)硅酸盐水泥等原料同时加入。Refer to the steps in Example 1 to solidify the mixed incineration waste residue, the difference is that step (2) is omitted, and 20 parts of fly ash and 2 parts of bistrimethylsilyl hydrogen phosphate are mixed with step (3) silicon Salt cement and other raw materials are added at the same time.
经对比例2方法的固化后,其固化体浸出液的铅、锌、铬的浸出值分别超出了《危险废物填埋污染控制标准(GB18598-2001)》中规定的各重金属限值的23%,65和34%。After solidification by the method of Comparative Example 2, the leaching values of lead, zinc and chromium in the leachate of the cured body exceeded 23% of the heavy metal limits stipulated in the "Hazardous Waste Landfill Pollution Control Standard (GB18598-2001)", 65 and 34%.
以上所述,仅为本发明较佳的具体实施方式,这些具体实施方式都是基于本发明整 体构思下的不同实现方式,而且本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应该以权利要求书的保护范围为准。The above are only preferred specific implementations of the present invention. These specific implementations are all based on different implementations under the overall concept of the present invention, and the scope of protection of the present invention is not limited thereto. Anyone familiar with the technical field Within the technical scope disclosed in the present invention, any changes or substitutions that can be easily conceived by a skilled person shall fall within the protection scope of the present invention. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.
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