CN114891273A - Modified overhaul slag based on tannic acid and preparation method and application thereof - Google Patents
Modified overhaul slag based on tannic acid and preparation method and application thereof Download PDFInfo
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- 239000002893 slag Substances 0.000 title claims abstract description 103
- 238000002360 preparation method Methods 0.000 title claims abstract description 10
- TUSDEZXZIZRFGC-UHFFFAOYSA-N 1-O-galloyl-3,6-(R)-HHDP-beta-D-glucose Natural products OC1C(O2)COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC1C(O)C2OC(=O)C1=CC(O)=C(O)C(O)=C1 TUSDEZXZIZRFGC-UHFFFAOYSA-N 0.000 title claims description 48
- 239000001263 FEMA 3042 Substances 0.000 title claims description 48
- LRBQNJMCXXYXIU-PPKXGCFTSA-N Penta-digallate-beta-D-glucose Natural products OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-PPKXGCFTSA-N 0.000 title claims description 48
- LRBQNJMCXXYXIU-NRMVVENXSA-N tannic acid Chemical compound OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-NRMVVENXSA-N 0.000 title claims description 48
- 229940033123 tannic acid Drugs 0.000 title claims description 48
- 235000015523 tannic acid Nutrition 0.000 title claims description 48
- 229920002258 tannic acid Polymers 0.000 title claims description 48
- FFUAGWLWBBFQJT-UHFFFAOYSA-N hexamethyldisilazane Chemical compound C[Si](C)(C)N[Si](C)(C)C FFUAGWLWBBFQJT-UHFFFAOYSA-N 0.000 claims abstract description 44
- 238000000034 method Methods 0.000 claims abstract description 42
- 239000000843 powder Substances 0.000 claims abstract description 40
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- 239000000126 substance Substances 0.000 claims abstract description 12
- REYJJPSVUYRZGE-UHFFFAOYSA-N Octadecylamine Chemical compound CCCCCCCCCCCCCCCCCCN REYJJPSVUYRZGE-UHFFFAOYSA-N 0.000 claims abstract description 11
- 125000000524 functional group Chemical group 0.000 claims abstract description 10
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 6
- 229920001864 tannin Polymers 0.000 claims abstract description 6
- 239000001648 tannin Substances 0.000 claims abstract description 6
- 235000018553 tannin Nutrition 0.000 claims abstract description 6
- 239000011241 protective layer Substances 0.000 claims abstract description 5
- 229920000642 polymer Polymers 0.000 claims abstract description 3
- 239000010426 asphalt Substances 0.000 claims description 71
- 229910052731 fluorine Inorganic materials 0.000 claims description 26
- 239000011737 fluorine Substances 0.000 claims description 26
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 25
- 238000001556 precipitation Methods 0.000 claims description 24
- 239000000243 solution Substances 0.000 claims description 21
- -1 hexamethyldisilane amine Chemical class 0.000 claims description 14
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- 238000001035 drying Methods 0.000 claims description 7
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- LRBQNJMCXXYXIU-YIILYMKVSA-N tannic acid Chemical compound OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)C(OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-YIILYMKVSA-N 0.000 abstract description 2
- 239000010865 sewage Substances 0.000 abstract 1
- 238000004065 wastewater treatment Methods 0.000 abstract 1
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 description 34
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 27
- 239000000047 product Substances 0.000 description 20
- 238000006243 chemical reaction Methods 0.000 description 15
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 11
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 10
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- 238000012986 modification Methods 0.000 description 8
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 238000003860 storage Methods 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
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- QKNYBSVHEMOAJP-UHFFFAOYSA-N 2-amino-2-(hydroxymethyl)propane-1,3-diol;hydron;chloride Chemical compound Cl.OCC(N)(CO)CO QKNYBSVHEMOAJP-UHFFFAOYSA-N 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000000872 buffer Substances 0.000 description 4
- 239000011575 calcium Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 125000001165 hydrophobic group Chemical group 0.000 description 4
- 229910017053 inorganic salt Inorganic materials 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000012467 final product Substances 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
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- 150000004753 Schiff bases Chemical class 0.000 description 2
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- 239000002253 acid Substances 0.000 description 2
- 150000003973 alkyl amines Chemical class 0.000 description 2
- 125000003277 amino group Chemical group 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
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- 238000000576 coating method Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
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- 238000011084 recovery Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- 238000006845 Michael addition reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 1
- 229910001634 calcium fluoride Inorganic materials 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 230000009920 chelation Effects 0.000 description 1
- 239000011258 core-shell material Substances 0.000 description 1
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- 125000001153 fluoro group Chemical group F* 0.000 description 1
- 238000007306 functionalization reaction Methods 0.000 description 1
- 231100000086 high toxicity Toxicity 0.000 description 1
- 125000000879 imine group Chemical group 0.000 description 1
- 229910001506 inorganic fluoride Inorganic materials 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 231100001252 long-term toxicity Toxicity 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
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- 230000009919 sequestration Effects 0.000 description 1
- FZHAPNGMFPVSLP-UHFFFAOYSA-N silanamine Chemical compound [SiH3]N FZHAPNGMFPVSLP-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K9/00—Use of pretreated ingredients
- C08K9/04—Ingredients treated with organic substances
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K11/00—Use of ingredients of unknown constitution, e.g. undefined reaction products
- C08K11/005—Waste materials, e.g. treated or untreated sewage sludge
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K9/00—Use of pretreated ingredients
- C08K9/04—Ingredients treated with organic substances
- C08K9/06—Ingredients treated with organic substances with silicon-containing compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
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- 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
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- Polymers & Plastics (AREA)
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Abstract
Description
技术领域technical field
本发明属于固废物绿色资源化再利用技术领域,具体涉及一种基于单宁酸的改性大修渣及其制备方法和应用。The invention belongs to the technical field of green resource recycling of solid waste, and particularly relates to a modified overhaul slag based on tannic acid and a preparation method and application thereof.
背景技术Background technique
铝电解生产行业在生产过程中无法避免的会产生各种废弃物,大修渣(OverhaulWaste Residues,OWRs)为各种废弃物中产量较大的一种。近年,大修渣因为其所携带的污染成分毒性高、含量高等特点被国家列为危险废弃物,按照国家危险废弃物标准对其进行无害化处理会极大增加铝工业生产行业的成本。因此,为降低大修渣的处理成本以缓解铝电解生产工业成本上升对行业发展造成的压力,对大修渣的回收再利用途径的研究成为当今环境、化工等研究领域的热点。大修渣资源化再利用工艺较少,尤其是在湿法工艺类别中,在早期多为直接生成无机盐以达到令大修渣无害化以及进一步再利用的目的。此类方法得到的资源化大修渣为无机盐材料,氟化物中的氟元素以离子形式存在,易于水溶液侵蚀条件下快速溶出,稳定性不佳。因此,要探究新的氟化物资源化工艺,应优化大修渣资源化工艺加强固化氟化物的长期稳定性,并在使用过程中既发挥大修渣无机盐自身良好的力学性能,同时保证大修渣产物不会直接与环境接触,最终达成资源化大修渣长期稳定、有效利用的目的。The aluminum electrolysis production industry will inevitably generate various wastes in the production process, and Overhaul Waste Residues (OWRs) is the one with the largest output among various wastes. In recent years, overhaul slag has been classified as hazardous waste by the state because of the high toxicity and high content of the pollutants it carries. The harmless treatment of it according to the national hazardous waste standard will greatly increase the cost of the aluminum industry production industry. Therefore, in order to reduce the processing cost of the overhaul slag and relieve the pressure on the industry development caused by the rising industrial cost of aluminum electrolysis production, the research on the recovery and reuse of the overhaul slag has become a hot spot in the research fields of environment and chemical industry. There are few overhaul slag recycling processes, especially in the wet process category. In the early stage, inorganic salts are directly generated to achieve the purpose of making overhaul slag harmless and further reused. The resource-recycling overhaul slag obtained by such a method is an inorganic salt material, and the fluorine element in the fluoride exists in the form of ions, which is easy to dissolve rapidly under the condition of aqueous solution erosion, and has poor stability. Therefore, in order to explore a new fluoride recycling process, the overhaul slag recycling process should be optimized to strengthen the long-term stability of the solidified fluoride, and in the process of use, the good mechanical properties of the inorganic salt of the overhaul slag itself should be exerted, and the overhaul slag product should be guaranteed. It will not directly contact the environment, and finally achieve the purpose of long-term stable and effective utilization of resource-based overhaul slag.
铝工业大修渣湿法资源化处理工艺早期方法主要是使用各种无机氟离子固化剂,例如氟化钙、氯化钙、氧化钙等钙剂,通过离子反应生成沉淀以固化游离的氟离子。该种方式虽可以达成将大修渣资源化的目的,但是在实际使用过程中具有以下几个问题:The early methods of the wet recycling process of aluminum industry overhaul slag are mainly to use various inorganic fluoride ion curing agents, such as calcium fluoride, calcium chloride, calcium oxide and other calcium agents, through ion reaction to generate precipitation to solidify free fluoride ions. Although this method can achieve the purpose of recycling the overhaul slag, it has the following problems in the actual use process:
(1)固化氟化物稳定性差。无机沉降氟化物在短时间实际使用中,其固化的氟离子会因空气、雨水等自然环境侵蚀而溶出至自然环境中。(1) The cured fluoride has poor stability. In the actual use of the inorganic precipitated fluoride in a short time, the solidified fluoride ions will be dissolved into the natural environment due to the erosion of the natural environment such as air and rain.
(2)氟化物回收成本高。湿法处理的大修渣废液中氟离子含量无法直接达到国家废水排放标准,氟化物沉降后的废水仍需使用其他工艺进行除氟。(2) The cost of fluoride recovery is high. The fluoride ion content in the overhaul slag waste liquid treated by the wet method cannot directly meet the national wastewater discharge standard, and the wastewater after fluoride sedimentation still needs to be defluorinated by other processes.
(3)再利用途径少。现今资源化工艺得到的大修渣活性较低,在实际使用中性能表现不佳。(3) There are few ways of reuse. The overhaul slag obtained by the current recycling process has low activity and poor performance in actual use.
因此,需探究一种经济、简便的改性工艺,以解决资源化大修渣过程中废水以及产品化学活性低的问题,将改性大修渣作为工程材料改性剂用以增加建材的使用性能。Therefore, it is necessary to explore an economical and simple modification process to solve the problem of low chemical activity of waste water and products in the process of overhauling the slag, and using the modified overhaul slag as an engineering material modifier to increase the performance of building materials.
发明内容SUMMARY OF THE INVENTION
为解决上述技术问题,本发明提供一种基于单宁酸的改性大修渣及其制备方法和应用,通过加入单宁酸,将作为无机物的大修渣表面转化为具有羟基及亚氨基的有机表面,同时借由这些活性基团将疏水基团接枝在大修渣粉末表面上,最终得到产物十八烷基胺/单宁酸复合改性大修渣(ODA/T-OWRs)或六甲基二硅烷胺/单宁酸复合改性大修渣(HMDS/T-OWRs)。该产品作为改性剂应用于沥青路面,可达到提高改性沥青的粘弹性、抗形变能力的作用。In order to solve the above-mentioned technical problems, the present invention provides a modified overhaul slag based on tannic acid and a preparation method and application thereof. At the same time, the hydrophobic groups are grafted on the surface of the overhaul slag powder by these active groups, and finally the product octadecylamine/tannic acid composite modified overhaul slag (ODA/T-OWRs) or hexamethyl is obtained. Disilazane/tannic acid composite modified overhaul residues (HMDS/T-OWRs). The product is used as a modifier in asphalt pavement, which can improve the viscoelasticity and deformation resistance of modified asphalt.
为实现上述目的,本发明提出如下技术方案:To achieve the above object, the present invention proposes the following technical solutions:
技术方案一:一种基于单宁酸的改性大修渣,通过单宁酸的自聚反应在大修渣粉末表面形成单宁酸聚合物包覆层,然后通过化学接枝法将具有疏水功能的官能团接枝于包覆层表面形成疏水保护层,得到的产品即为基于单宁酸的改性大修渣;其中,所述具有疏水功能的官能团的物质为十八烷基胺或六甲基二硅烷胺。Technical scheme 1: A modified overhaul slag based on tannic acid, through the self-polymerization reaction of tannic acid, a tannic acid polymer coating layer is formed on the surface of the overhaul slag powder, and then the hydrophobic function is formed by chemical grafting. The functional group is grafted on the surface of the coating layer to form a hydrophobic protective layer, and the obtained product is the modified overhaul slag based on tannic acid; wherein, the substance with the functional group with hydrophobic function is octadecylamine or hexamethyldicarbonate Silylamine.
技术方案二:一种基于单宁酸的改性大修渣的制备方法,包括以下步骤:Technical scheme 2: a method for preparing a modified overhaul slag based on tannic acid, comprising the following steps:
1)将大修渣粉末进行沉氟处理,过滤,烘干,研磨,得到沉氟大修渣粉末;1) carry out precipitation fluorine treatment to the overhaul slag powder, filter, dry, and grind to obtain overhaul slag powder with precipitation;
2)将沉氟大修渣粉末与缓冲溶液混合,得到大修渣溶液;2) Mixing the fluorine overhaul slag powder with a buffer solution to obtain an overhaul slag solution;
3)在大修渣溶液中加入单宁酸后超声处理,加热搅拌,过滤,洗涤,干燥,重新研磨,得到的产品直接浸泡在十八烷基胺或六甲基二硅烷胺中并进行热拌处理,静置,得到的产品进行清洗、干燥并研磨,即得基于单宁酸的改性大修渣。3) After adding tannic acid to the overhaul slag solution, ultrasonic treatment, heating and stirring, filtration, washing, drying, and regrinding, the obtained product is directly immersed in octadecylamine or hexamethyldisilazane and hot-mixed Treatment, standing, and the obtained product is washed, dried and ground to obtain a modified overhaul slag based on tannic acid.
操作过程中,每次研磨粒径均与大修渣粉末粒径相同。During the operation, the particle size of each grinding is the same as that of the overhauled slag powder.
进一步地,步骤1)中,所述沉氟大修渣粉末粒径为100-200目。Further, in step 1), the particle size of the precipitation fluorine overhaul slag powder is 100-200 mesh.
进一步地,步骤2)中,所述缓冲溶液的pH为8-9,沉氟大修渣粉末与缓冲溶液的固液比为1g:(3-10)mL。Further, in step 2), the pH of the buffer solution is 8-9, and the solid-to-liquid ratio of the precipitation fluoride overhaul slag powder to the buffer solution is 1 g: (3-10) mL.
进一步地,步骤3)中,所述单宁酸与沉氟大修渣粉末的质量比为(0.5-1.0):5。Further, in step 3), the mass ratio of the tannic acid to the precipitating fluorine overhaul slag powder is (0.5-1.0):5.
所述沉氟处理是将大修渣中的可溶性氟化物沉降为不可溶性氟化物的沉氟方法,主要是使用可以与氟离子发生沉降反应的无机、有机物作为沉降剂,得到沉氟大修渣应具有较为稳定、坚硬的性质;沉降剂可选无水氯化钙,其可提供Ca2+改变反应过程中的沉降反应方向,同时借助与单宁酸进行的螯合反应,加速单宁酸的聚合速率。The fluorine precipitation treatment is a fluorine precipitation method in which the soluble fluoride in the overhaul slag is precipitated into insoluble fluoride, mainly using inorganic and organic substances that can precipitate and react with fluoride ions as the sedimentation agent. Relatively stable and hard properties; the precipitation agent can be selected from anhydrous calcium chloride, which can provide Ca 2+ to change the direction of the precipitation reaction during the reaction, and at the same time accelerate the polymerization of tannic acid by means of the chelation reaction with tannic acid. rate.
进一步地,步骤3)中,所述超声处理时间为15-30min,所述加热温度为25-60℃,搅拌时间为12-24h,转速为350-450rpm。Further, in step 3), the ultrasonic treatment time is 15-30min, the heating temperature is 25-60°C, the stirring time is 12-24h, and the rotational speed is 350-450rpm.
进一步地,步骤3)中,所述十八烷基胺或六甲基二硅烷胺与沉氟大修渣粉末用量比为(5-7)mL:5g。Further, in step 3), the dosage ratio of the octadecylamine or hexamethyldisilazane to the heavy fluorine overhaul slag powder is (5-7) mL:5g.
进一步地,步骤3)中,所述热拌处理温度为60℃,热拌处理时间为1-2h,静置温度为25-60℃,静置时间为12-18h。Further, in step 3), the hot-mixing treatment temperature is 60°C, the hot-mixing treatment time is 1-2h, the standing temperature is 25-60°C, and the standing time is 12-18h.
技术方案三:一种复合改性沥青,利用基于单宁酸的改性大修渣改性剂与SBS(苯乙烯-丁二烯-苯乙烯嵌段共聚物)共同对沥青进行改性,得到复合改性沥青(OWRs/SBS)。将改性大修渣掺入沥青中时,保持150-200℃恒温,在350-450rpm转速下分散改性大修渣,使大修渣粉末均匀分散在沥青中。Technical solution 3: a composite modified asphalt, which uses a tannic acid-based modified overhaul slag modifier and SBS (styrene-butadiene-styrene block copolymer) to jointly modify the asphalt to obtain a composite modified asphalt. Modified bitumen (OWRs/SBS). When the modified overhaul slag is mixed into the asphalt, keep a constant temperature of 150-200 ℃, and disperse the modified overhaul slag at a speed of 350-450rpm, so that the overhaul slag powder is evenly dispersed in the asphalt.
所述改性大修渣掺入量为沥青总质量的1.0-2.0%,所述SBS掺入量为沥青总质量的5%。The mixing amount of the modified overhaul slag is 1.0-2.0% of the total mass of the asphalt, and the mixing amount of the SBS is 5% of the total mass of the asphalt.
本发明反应原理:The reaction principle of the present invention:
基于氟离子自身性质使用钙剂或其他金属离子与之发生反应形成硬质沉淀,之后通过单宁酸的自聚合反应在沉氟大修渣粉末表面黏附单宁酸包裹层,这个过程中由于已有氟化物沉淀粉末也会被包裹,导致溶液中直接接触溶液的沉降物变少,促进溶液中的氟离子继续沉降。最后通过单宁酸包裹大修渣表面的大量羟基与改性剂的氨基发生迈克尔加成和席夫碱反应,将亲油疏水基团接枝于大修渣粉末表面。Based on the nature of the fluoride ion itself, calcium or other metal ions are used to react with it to form a hard precipitate, and then the tannic acid coating layer is adhered to the surface of the fluoride overhaul slag powder through the self-polymerization reaction of tannic acid. The fluoride precipitation powder is also encapsulated, resulting in less sediment in the solution directly contacting the solution, and promoting the continued sedimentation of fluoride ions in the solution. Finally, a large number of hydroxyl groups on the surface of the overhaul slag wrapped by tannic acid undergo Michael addition and Schiff base reaction with the amino group of the modifier, and the lipophilic and hydrophobic groups are grafted on the surface of the overhaul slag powder.
本发明采用单宁酸作为包覆层保护大修渣的内核,保证大修渣在使用过程中不会直接与环境接触:单宁酸包覆层作为有机聚合物,具有很好的稳定性、包覆性。在改性过程中可以以大修渣粉末为核形成核壳结构,同时还使用化学接枝法在单宁酸包裹层外接枝疏水基团,进一步形成疏水保护层,既保留了大修渣作为无机盐所具有的优秀力学性能,又大大提升了资源化大修渣的长期稳定性。The invention adopts tannic acid as the coating layer to protect the inner core of the overhaul slag, and ensures that the overhaul slag will not directly contact the environment during use: the tannic acid coating layer, as an organic polymer, has good stability and coating sex. In the modification process, the core-shell structure can be formed with the overhaul slag powder as the core, and the hydrophobic group can be grafted outside the tannic acid coating layer by chemical grafting method to further form a hydrophobic protective layer, which not only retains the overhaul slag as an inorganic The excellent mechanical properties of salt have greatly improved the long-term stability of the resource-based overhaul slag.
本发明利用单宁酸自聚合反应,在沉降过程中包裹已沉降的氟化物,改变沉降反应过程中沉淀在溶液中的数量,促进废水中的游离氟离子进一步沉降,同时全工艺步骤少,因此成本较低:在资源化大修渣工艺中,单宁酸自聚合形成包覆层包裹溶液中的固体粉末,隔绝其与溶液的接触。离子沉降反应作为可逆反应,最终溶液里氟离子浓度受反应环境下溶度积控制。通过单宁酸的包裹可以减少沉淀在溶液中的数量,从而令溶液中的氟离子进一步与钙离子沉淀,突破了常规工艺中无机钙剂直接沉降氟离子的极限能力,令本工艺产生的废水中氟离子含量可以达到直接排放的浓度,大大降低了资源化成本。The invention utilizes the self-polymerization reaction of tannic acid, wraps the settled fluoride in the sedimentation process, changes the amount of sedimentation in the solution in the sedimentation reaction process, and promotes further sedimentation of free fluoride ions in the waste water. At the same time, the whole process has few steps, so Low cost: In the process of overhauling the slag with resources, tannic acid self-polymerizes to form a coating layer to wrap the solid powder in the solution and isolate it from contact with the solution. The ion precipitation reaction is a reversible reaction, and the fluoride ion concentration in the final solution is controlled by the solubility product under the reaction environment. The coating of tannic acid can reduce the number of precipitates in the solution, so that the fluoride ions in the solution are further precipitated with calcium ions, which breaks through the limit ability of inorganic calcium agents to directly precipitate fluoride ions in the conventional process, and makes the wastewater produced by this process. The content of fluoride ions in the medium can reach the concentration of direct discharge, which greatly reduces the cost of resource utilization.
将在大修渣表面进行化学接枝,使其适用于在沥青中作为改性剂:沥青与无机盐粉末的相容性差,无机盐粉末中的金属阳离子会降低沥青的使用寿命。因此选择在单宁酸包裹层上进行疏水基团的接枝,改善资源化大修渣与沥青的相容性,同时进一步防止水直接与资源化大修渣粉末接触导致其电离出金属阳离子损害沥青使用寿命。同时,沥青作为油性有机物可以很好的保护资源化大修渣,进一步加强其稳定性。Chemical grafting will be carried out on the surface of the overhaul slag, making it suitable for use as a modifier in asphalt: asphalt has poor compatibility with inorganic salt powder, and metal cations in inorganic salt powder will reduce the service life of asphalt. Therefore, the grafting of hydrophobic groups on the tannic acid coating layer is chosen to improve the compatibility of the recyclable overhaul slag and asphalt, and at the same time further prevent the water from directly contacting the recyclable overhaul slag powder, resulting in the ionization of metal cations and damage to the use of asphalt. life. At the same time, bitumen, as an oily organic matter, can well protect the recyclable overhaul slag and further strengthen its stability.
与现有技术相比,本发明的有益效果为:Compared with the prior art, the beneficial effects of the present invention are:
1、本发明反应过程中加入单宁酸,于大修渣粉末表面粘附,迅速沉积、聚集在其表面而形成聚单宁酸包覆层,该包覆层稳定性持久,能够作为纽带增加无机的大修渣粉末与沥青的结合力;且沉积的聚单宁酸层还具有羟基、亚胺基等官能团,为进一步功能化提供大量的活性基团,易与十八烷基胺、六甲基二硅烷胺等物质中的胺基发生席夫碱等反应,进一步促进疏水官能团高效接枝于大修渣粉末表面。1. Tannic acid is added in the reaction process of the present invention, which adheres to the surface of the overhauled slag powder, and is rapidly deposited and aggregated on its surface to form a polytannic acid coating layer. The coating layer has long-lasting stability and can be used as a link to increase inorganic and the deposited polytannic acid layer also has functional groups such as hydroxyl and imine groups, which provide a large number of active groups for further functionalization, which are easy to be combined with octadecylamine, hexamethyl group and other functional groups. The amine groups in the disilazine and other substances undergo reactions such as Schiff bases, which further promotes the efficient grafting of hydrophobic functional groups on the surface of the overhaul slag powder.
2、本发明很好的改善了大修渣粉末作为无机材料与沥青的低相容性,帮助大修渣粉末更好更均匀的分散在沥青中,从而提供立体的力学支撑,加强沥青的弹性。同时大修渣粉末二次改性得到的疏水官能团可以提高沥青的疏水性能,以提升沥青的抗水损能力,且对于大修渣本身而言也可以很好的保证氟化物沉淀无法与水直接接触,导致氟化物电离生成氟离子流入环境中。2. The present invention improves the low compatibility of the overhaul slag powder as an inorganic material with asphalt, and helps the overhaul slag powder to be better and more uniformly dispersed in the asphalt, thereby providing three-dimensional mechanical support and enhancing the elasticity of the asphalt. At the same time, the hydrophobic functional groups obtained by the secondary modification of the overhaul slag powder can improve the hydrophobic performance of the asphalt, so as to improve the water damage resistance of the asphalt, and for the overhaul slag itself, it can also ensure that the fluoride precipitation cannot be directly contacted with water. Causes the ionization of fluoride to generate fluoride ions that flow into the environment.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the accompanying drawings required in the embodiments will be briefly introduced below. Obviously, the drawings in the following description are only some of the present invention. In the embodiments, for those of ordinary skill in the art, other drawings can also be obtained according to these drawings without any creative effort.
图1为本发明应用实施例4和对比例1的大修渣/SBS复合改性沥青复数剪切模量G*(10Hz)随温度的变化对比图;Fig. 1 is a graph showing the variation of the overhaul slag/SBS composite modified asphalt complex shear modulus G * (10Hz) with temperature of Application Example 4 and Comparative Example 1 of the present invention;
图2为本发明应用实施例5和对比例2的大修渣/SBS复合改性沥青复数剪切模量G*(10Hz)随温度的变化对比图;Fig. 2 is a graph showing the variation of the overhaul slag/SBS composite modified asphalt complex shear modulus G * (10Hz) with temperature of Application Example 5 and Comparative Example 2 of the present invention;
图3为本发明应用实施例6和对比例3的大修渣/SBS复合改性沥青复数剪切模量G*(10Hz)随温度的变化对比图;Fig. 3 is a graph showing the variation of the overhaul slag/SBS composite modified asphalt complex shear modulus G * (10Hz) with temperature of Application Example 6 and Comparative Example 3 of the present invention;
图4为单宁酸加入量对大修渣中氟离子浓度的影响;Figure 4 shows the effect of tannic acid addition on fluoride ion concentration in overhaul slag;
图5为大修渣改性前后毒性浸泡实验。Figure 5 shows the toxicity immersion experiment before and after modification of the overhaul slag.
具体实施方式Detailed ways
现详细说明本发明的多种示例性实施方式,该详细说明不应认为是对本发明的限制,而应理解为是对本发明的某些方面、特性和实施方案的更详细的描述。Various exemplary embodiments of the present invention will now be described in detail, which detailed description should not be construed as a limitation of the invention, but rather as a more detailed description of certain aspects, features, and embodiments of the invention.
应理解本发明中所述的术语仅仅是为描述特别的实施方式,并非用于限制本发明。另外,对于本发明中的数值范围,应理解为还具体公开了该范围的上限和下限之间的每个中间值。在任何陈述值或陈述范围内的中间值以及任何其他陈述值或在所述范围内的中间值之间的每个较小的范围也包括在本发明内。这些较小范围的上限和下限可独立地包括或排除在范围内。It should be understood that the terms described in the present invention are only used to describe particular embodiments, and are not used to limit the present invention. Additionally, for numerical ranges in the present disclosure, it should be understood that each intervening value between the upper and lower limits of the range is also specifically disclosed. Every smaller range between any stated value or intervening value in a stated range and any other stated value or intervening value in that stated range is also encompassed within the invention. The upper and lower limits of these smaller ranges may independently be included or excluded in the range.
除非另有说明,否则本文使用的所有技术和科学术语具有本发明所述领域的常规技术人员通常理解的相同含义。虽然本发明仅描述了优选的方法和材料,但是在本发明的实施或测试中也可以使用与本文所述相似或等同的任何方法和材料。本说明书中提到的所有文献通过引用并入,用以公开和描述与所述文献相关的方法和/或材料。在与任何并入的文献冲突时,以本说明书的内容为准。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention relates. Although only the preferred methods and materials are described herein, any methods and materials similar or equivalent to those described herein can also be used in the practice or testing of the present invention. All documents mentioned in this specification are incorporated by reference for the purpose of disclosing and describing the methods and/or materials in connection with which the documents are referred. In the event of conflict with any incorporated document, the content of this specification controls.
在不背离本发明的范围或精神的情况下,可对本发明说明书的具体实施方式做多种改进和变化,这对本领域技术人员而言是显而易见的。由本发明的说明书得到的其他实施方式对技术人员而言是显而易见的。本申请说明书和实施例仅是示例性的。It will be apparent to those skilled in the art that various modifications and variations can be made in the specific embodiments of the present invention without departing from the scope or spirit of the invention. Other embodiments will be apparent to those skilled in the art from the description of the present invention. The description and examples of the present application are only exemplary.
关于本文中所使用的“包含”、“包括”、“具有”、“含有”等等,均为开放性的用语,即意指包含但不限于。As used herein, "comprising," "including," "having," "containing," and the like, are open-ended terms, meaning including but not limited to.
试验过程中各批次大修渣中氟离子浓度不同,需对处理样品进行测试得出沉氟理论量。本发明所用大修渣通过标准浸泡流程测试在固液比为10g:100mL条件下,浸出溶液中氟离子浓度为2523.75mg/L。通过摩尔数计算理论无水氯化钙加入量为7.38g/L,工艺流程中无水氯化钙实际加入量为理论值的5倍,即36.9g/L。During the test, the concentration of fluoride ions in each batch of overhaul slag was different, and it was necessary to test the treated samples to obtain the theoretical amount of precipitation fluoride. The overhaul slag used in the present invention is tested by a standard soaking process under the condition that the solid-liquid ratio is 10g:100mL, and the fluoride ion concentration in the leaching solution is 2523.75mg/L. The theoretical addition amount of anhydrous calcium chloride is 7.38g/L calculated by the number of moles, and the actual addition amount of anhydrous calcium chloride in the technological process is 5 times the theoretical value, namely 36.9g/L.
Tris-HCl缓冲液的制备:将0.6057g的Tris(三羟甲基氨基甲烷)溶于100mL水中,用1mol HCl溶液滴定至pH即可。Preparation of Tris-HCl buffer: Dissolve 0.6057 g of Tris (tris (trishydroxymethylaminomethane) in 100 mL of water, and titrate to pH with 1 mol of HCl solution.
实施例1Example 1
(1)称取5g筛至100目的大修渣于50mL水溶液中,在50℃恒温加热磁力搅拌器中溶出30min,将总量为36.9g/L的无水氯化钙分两次加入,每次加入无水氯化钙后沉氟10min,真空抽滤得到产物放入60℃烘箱中8h,备用;(1) Weigh 5g of overhaul slag sieved to 100 mesh in 50mL of aqueous solution, dissolve in a magnetic stirrer with constant temperature heating at 50°C for 30min, and add anhydrous calcium chloride with a total amount of 36.9g/L in two times, each time After adding anhydrous calcium chloride, fluorine was precipitated for 10 minutes, and the product obtained by vacuum filtration was placed in an oven at 60 °C for 8 hours, for use;
(2)将步骤(1)所得沉氟大修渣重新研磨至100目,再于60℃烘箱中除水2h,得到大修渣粉末;(2) regrinding the precipitation fluorine overhaul slag obtained in step (1) to 100 mesh, and then dewatering in a 60° C. oven for 2 hours to obtain overhaul slag powder;
(3)将步骤(2)中得到的5g大修渣粉末置于50mLpH为8.5的Tris-HCl缓冲液中,加入单宁酸0.5g于超声细胞破碎仪中超声15min,超声温度通过暂停超声或物理散热方式控制在60℃以下,完成后在35℃下以350rpm的转速搅拌12h;(3) 5g of overhaul slag powder obtained in step (2) was placed in 50mL of Tris-HCl buffer with pH 8.5, 0.5g of tannic acid was added, and sonicated for 15min in an ultrasonic cell disruptor. The heat dissipation method is controlled below 60 °C, and after completion, it is stirred at 350 rpm for 12 hours at 35 °C;
(4)反应完成后的产物过滤,使用无水乙醇和水反复洗涤3次,在60℃烘箱中干燥12h,得到产物重新研磨至100目,将其直接浸泡在5mL ODA或HMDS溶液中热拌1h,热拌温度为60℃,之后于45℃下恒温放置12h,最终产物使用无水乙醇和水反复洗涤3次,烘干并研磨成100目,即得到改性大修渣,记为十八烷基胺/单宁酸复合改性大修渣(ODA/T-OWRs)或六甲基二硅烷胺/单宁酸复合改性大修渣(HMDS/T-OWRs)。(4) Filtration of the product after the completion of the reaction, repeated washing with absolute ethanol and water for 3 times, drying in an oven at 60°C for 12 hours, the obtained product was re-ground to 100 mesh, and directly immersed in 5 mL of ODA or HMDS solution for hot mixing 1h, the hot mixing temperature was 60°C, and then placed at a constant temperature of 45°C for 12h. The final product was repeatedly washed 3 times with absolute ethanol and water, dried and ground to 100 mesh to obtain modified overhaul slag, denoted as 18 Alkylamine/tannic acid composite modified overhaul residues (ODA/T-OWRs) or hexamethyldisilazane/tannic acid composite modified overhaul residues (HMDS/T-OWRs).
实施例2Example 2
(1)称取5g筛至150目的大修渣于50mL水溶液中,在55℃恒温加热磁力搅拌器中溶出30min,将总量为36.9g/L的无水氯化钙分两次加入,每次加入无水氯化钙后沉氟10min,真空抽滤得到产物放入60℃烘箱中8h,备用;(1) Weigh 5g sieve to 150 mesh overhaul slag in 50mL aqueous solution, dissolve in 55°C constant temperature heating magnetic stirrer for 30min, add anhydrous calcium chloride with a total amount of 36.9g/L in two times, each time After adding anhydrous calcium chloride, fluorine was precipitated for 10 minutes, and the product obtained by vacuum filtration was placed in an oven at 60 °C for 8 hours, for use;
(2)将步骤(1)所得沉氟大修渣重新研磨至150目,再于60℃烘箱中除水2h,得到大修渣粉末;(2) regrinding the precipitation fluorine overhaul slag obtained in step (1) to 150 mesh, and then dewatering in a 60° C. oven for 2 hours to obtain overhaul slag powder;
(3)将步骤(2)中得到的5g大修渣粉末置于50mLpH为8.0的Tris-HCl缓冲液中,加入单宁酸0.75g于超声细胞破碎仪中超声20min,超声温度通过暂停超声或物理散热方式控制在60℃以下,完成后在40℃下以400rpm的转速搅拌18h;(3) 5g of overhaul slag powder obtained in step (2) was placed in 50mL of Tris-HCl buffer with a pH of 8.0, 0.75g of tannic acid was added, and sonicated for 20min in an ultrasonic cell disruptor, and the ultrasonic temperature was adjusted by suspending ultrasonic or physical The heat dissipation method is controlled below 60 °C, and after completion, it is stirred at 400 rpm for 18 hours at 40 °C;
(4)反应完成后的产物过滤,使用无水乙醇和水反复洗涤3次,在60℃烘箱中干燥12h,得到产物重新研磨至150目,将其直接浸泡在6.5mL ODA或HMDS溶液中热拌1.5h,热拌温度为60℃,之后于50℃下恒温放置13h,最终产物使用无水乙醇和水反复洗涤3次,烘干并研磨成150目,即得到改性大修渣,记为十八烷基胺/单宁酸复合改性大修渣(ODA/T-OWRs)或六甲基二硅烷胺/单宁酸复合改性大修渣(HMDS/T-OWRs)。(4) Filtration of the product after the completion of the reaction, repeated washing with absolute ethanol and water for 3 times, drying in an oven at 60°C for 12h, the obtained product was re-ground to 150 mesh, and directly soaked in 6.5mL ODA or HMDS solution to heat Mixed for 1.5 hours, the hot mixing temperature was 60 °C, and then placed at a constant temperature of 50 °C for 13 hours. The final product was washed 3 times with absolute ethanol and water, dried and ground to 150 mesh, that is, the modified overhaul slag was obtained, recorded as Octadecylamine/tannic acid composite modified overhaul residues (ODA/T-OWRs) or hexamethyldisilazane/tannic acid composite modified overhaul residues (HMDS/T-OWRs).
实施例3Example 3
(1)称取5g筛至200目的大修渣于50mL水溶液中,在55℃恒温加热磁力搅拌器中溶出30min,将总量为36.9g/L的无水氯化钙分两次加入,每次加入无水氯化钙后沉氟10min,真空抽滤得到产物放入60℃烘箱中8h,备用;(1) Weigh 5g sieve to 200 mesh overhaul slag in 50mL aqueous solution, dissolve in 55 ℃ constant temperature heating magnetic stirrer for 30min, add anhydrous calcium chloride with a total amount of 36.9g/L in two times, each time After adding anhydrous calcium chloride, fluorine was precipitated for 10 minutes, and the product obtained by vacuum filtration was placed in an oven at 60 °C for 8 hours, for use;
(2)将步骤(1)所得沉氟大修渣重新研磨至200目,再于60℃烘箱中除水2h,得到大修渣粉末;(2) regrinding the precipitation fluorine overhaul slag obtained in step (1) to 200 mesh, and then dewatering in a 60° C. oven for 2 hours to obtain overhaul slag powder;
(3)将步骤(2)中得到的5g大修渣粉末置于50mLpH为8.5的Tris-HCl缓冲液中,加入单宁酸1.0g于超声细胞破碎仪中超声30min,超声温度通过暂停超声或物理散热方式控制在60℃以下,完成后在45℃下以450rpm的转速搅拌12h;(3) 5g of overhaul slag powder obtained in step (2) was placed in 50mL of Tris-HCl buffer with a pH of 8.5, 1.0g of tannic acid was added, and sonicated for 30min in an ultrasonic cell disruptor. The heat dissipation method is controlled below 60 °C, and after completion, it is stirred at 450 rpm for 12 hours at 45 °C;
(4)反应完成后的产物过滤,使用无水乙醇和水反复洗涤3次,在60℃烘箱中干燥12h,得到产物重新研磨至200目,将其直接浸泡在5mL ODA或HMDS溶液中热拌1h,热拌温度为60℃,之后于45℃下恒温放置14h,最终产物使用无水乙醇和水反复洗涤3次,烘干并研磨成200目,即得到改性大修渣,记为十八烷基胺/单宁酸复合改性大修渣(ODA/T-OWRs)或六甲基二硅烷胺/单宁酸复合改性大修渣(HMDS/T-OWRs)。(4) Filtration of the product after the completion of the reaction, repeated washing with absolute ethanol and water for 3 times, drying in an oven at 60°C for 12 hours, the obtained product was re-ground to 200 mesh, and directly immersed in 5 mL of ODA or HMDS solution for hot mixing 1h, the hot mixing temperature was 60°C, and then placed at a constant temperature of 45°C for 14h. The final product was repeatedly washed 3 times with absolute ethanol and water, dried and ground to 200 mesh, that is, the modified overhaul slag was obtained, denoted as 18 Alkylamine/tannic acid composite modified overhaul residues (ODA/T-OWRs) or hexamethyldisilazane/tannic acid composite modified overhaul residues (HMDS/T-OWRs).
应用实施例4Application Example 4
称取150g的SK-70A沥青在135℃烘箱中烘干2h以除去多余的水分,将实施例1得到的HMDS/T-OWRs或ODA/T-OWRs与SBS加入沥青中,保持150℃恒温,在5000rpm高速剪切机下剪切2h,并在400rpm高速剪切机下分散2h,即得到HMDS/T-OWRs/SBS或ODA/T-OWRs/SBS复合改性的沥青;HMDS/T-OWRs或ODA/T-OWRs掺入量为沥青总质量的1%,SBS掺入量为沥青总质量的5%。Weigh 150 g of SK-70A asphalt and dry it in an oven at 135 °C for 2 hours to remove excess water. Add the HMDS/T-OWRs or ODA/T-OWRs and SBS obtained in Example 1 into the asphalt, and keep a constant temperature of 150 °C. After shearing for 2h under 5000rpm high-speed shearing machine, and dispersing under 400rpm high-speed shearing machine for 2h, the composite modified asphalt of HMDS/T-OWRs/SBS or ODA/T-OWRs/SBS was obtained; HMDS/T-OWRs Or the dosage of ODA/T-OWRs is 1% of the total mass of asphalt, and the dosage of SBS is 5% of the total mass of asphalt.
应用实施例5Application Example 5
称取150g的SK-70A沥青在135℃烘箱中烘干2h以除去多余的水分,将实施例2得到的HMDS/T-OWRs或ODA/T-OWRs与SBS加入沥青中,保持165℃恒温,在5000rpm高速剪切机下剪切2h,并在450rpm高速剪切机下分散2h,即得到HMDS/T-OWRs/SBS或ODA/T-OWRs/SBS复合改性的沥青;HMDS/T-OWRs或ODA/T-OWRs掺入量为沥青总质量的1.5%,SBS掺入量为沥青总质量的5%。Weigh 150 g of SK-70A asphalt and dry it in an oven at 135 °C for 2 hours to remove excess water. Add the HMDS/T-OWRs or ODA/T-OWRs and SBS obtained in Example 2 into the asphalt, and keep a constant temperature of 165 °C. After shearing for 2h under 5000rpm high-speed shearing machine, and dispersing under 450rpm high-speed shearing machine for 2h, the composite modified asphalt of HMDS/T-OWRs/SBS or ODA/T-OWRs/SBS was obtained; HMDS/T-OWRs Or the dosage of ODA/T-OWRs is 1.5% of the total mass of asphalt, and the dosage of SBS is 5% of the total mass of asphalt.
应用实施例6Application Example 6
称取150g的SK-70A沥青在135℃烘箱中烘干2h以除去多余的水分,将实施例3得到的HMDS/T-OWRs或ODA/T-OWRs与SBS加入沥青中,保持175℃恒温,在在5000rpm高速剪切机下剪切2h,并在450rpm高速剪切机下分散2h,即得到HMDS/T-OWRs/SBS或ODA/T-OWRs/SBS复合改性的沥青;HMDS/T-OWRs或ODA/T-OWRs掺入量为沥青总质量的2.0%,SBS掺入量为沥青总质量的5%。Weigh 150 g of SK-70A asphalt and dry it in an oven at 135 °C for 2 hours to remove excess moisture. Add the HMDS/T-OWRs or ODA/T-OWRs and SBS obtained in Example 3 into the asphalt, and keep a constant temperature of 175 °C. After shearing under 5000rpm high-speed shearing machine for 2h, and dispersing under 450rpm high-speed shearing machine for 2h, the composite modified asphalt of HMDS/T-OWRs/SBS or ODA/T-OWRs/SBS was obtained; HMDS/T- The content of OWRs or ODA/T-OWRs was 2.0% of the total mass of asphalt, and the content of SBS was 5% of the total mass of asphalt.
对比例1Comparative Example 1
同应用实施例4,区别在于,将实施例1中的HMDS/T-OWRs或ODA/T-OWRs替换成仅沉氟处理的OWRs,得到OWRs/SBS复合改性沥青。The same as application example 4, the difference is that the HMDS/T-OWRs or ODA/T-OWRs in example 1 are replaced with OWRs treated with precipitation only to obtain OWRs/SBS composite modified asphalt.
对比例2Comparative Example 2
同应用实施例5,区别在于,将实施例1中的HMDS/T-OWRs或ODA/T-OWRs替换成仅沉氟处理的OWRs,得到OWRs/SBS复合改性沥青。Same as Application Example 5, the difference is that the HMDS/T-OWRs or ODA/T-OWRs in Example 1 are replaced with OWRs treated with fluorine only to obtain OWRs/SBS composite modified asphalt.
对比例3Comparative Example 3
同应用实施例6,区别在于,将实施例1中的HMDS/T-OWRs或ODA/T-OWRs替换成仅沉氟处理的OWRs,得到OWRs/SBS复合改性沥青。The same as in Application Example 6, the difference is that the HMDS/T-OWRs or ODA/T-OWRs in Example 1 are replaced with only fluorine-treated OWRs to obtain OWRs/SBS composite modified asphalt.
试验例1Test Example 1
将应用实施例4-6、对比例1-3以及对照组(只添加SBS的改性沥青,SBS掺入量为沥青总质量的5%)进行DSR测试,具体是将1.0g沥青浇注在直径为25mm的试验板中心,移动试验板将挤压两个试验板间的沥青,加热试件修整器,修正周边多余的沥青,然后调整间隙到1mm的试验间隙。温度平衡时,设备将自动以10rad/s的频率和选择的应力目标值进行试验,记录和计算均由数据采集系统完成(需要说明,附图1-3中的HMDS-TA-OWRs和ODA-TA-OWRs/SBS即为实施例中的HMDS/T-OWRs和ODA/T-OWRs/SBS)。The DSR test was carried out for application examples 4-6, comparative examples 1-3 and the control group (modified asphalt with only SBS added, and the SBS content was 5% of the total mass of the asphalt). Specifically, 1.0 g of asphalt was poured on a diameter of For the center of the 25mm test board, moving the test board will squeeze the asphalt between the two test boards, heat the test piece conditioner, correct the excess asphalt around the perimeter, and then adjust the gap to a test gap of 1mm. When the temperature is equilibrated, the equipment will automatically conduct the test at the frequency of 10rad/s and the selected stress target value, and the recording and calculation are completed by the data acquisition system (it needs to be explained, HMDS-TA-OWRs and ODA- TA-OWRs/SBS are HMDS/T-OWRs and ODA/T-OWRs/SBS in the embodiment).
图1是应用实施例4、对比例1所得产物的测试的储能模量对比图。从图1可知,两种改性沥青的复数剪切模量G*在相同温度时,应用实施例4中HMDS/T-OWRs或ODA/T-OWRs/SBS复合改性沥青的复数剪切模量G*均大于对比例1中仅沉氟处理OWRs/SBS改性沥青的复数剪切模量G*,证明经过单宁酸和六甲基二硅烷胺、十八烷基氨改性过后的大修渣,在加入到沥青中后,会使得沥青变硬,从而提高了其抵抗形变的能力。FIG. 1 is a comparison diagram of the storage modulus of the products obtained by applying Example 4 and Comparative Example 1. It can be seen from Figure 1 that when the complex shear modulus G* of the two modified asphalts is at the same temperature, the complex shear modulus of the HMDS/T-OWRs or ODA/T-OWRs/SBS composite modified asphalt in Example 4 is applied. The amount G* is greater than the complex shear modulus G* of the OWRs/SBS modified asphalt treated with only fluorine in Comparative Example 1, which proves that the modified asphalt after modification with tannic acid, hexamethyldisilazane and octadecylamine Overhaul slag, when added to asphalt, hardens the asphalt, thereby increasing its resistance to deformation.
图2是应用实施例5、对比例2所得产物的测试的储能模量对比图。从图2可知,两种改性沥青的储能G'在相同温度时,HMDS/T-OWRs或ODA/T-OWRs/SBS复合改性沥青的储能模量G'均大于仅沉氟处理OWRs/SBS改性沥青的储能模量G',说明HMDS/T-OWRs或ODA/T-OWRs改性沥青的弹性性能增强。2 is a comparison diagram of the storage modulus of the products obtained by applying Example 5 and Comparative Example 2. It can be seen from Figure 2 that the storage modulus G' of the HMDS/T-OWRs or ODA/T-OWRs/SBS composite modified asphalt is greater than that of the fluorine precipitation only at the same temperature. The storage modulus G' of OWRs/SBS modified asphalt indicates the enhanced elastic properties of HMDS/T-OWRs or ODA/T-OWRs modified asphalt.
图3是应用实施例6、对比例3所得产物的测试的储能模量对比图。从图3可知,两种改性沥青在相同温度时HMDS/T-OWRs或ODA/T-OWRs/SBS复合改性沥青的损失模量G”均大于仅沉氟处理OWRs/SBS改性沥青的损失模量G”,说明HMDS/T-OWRs或ODA/T-OWRs改性沥青的粘性性能增强。3 is a comparison diagram of the storage modulus of the products obtained by applying Example 6 and Comparative Example 3. It can be seen from Fig. 3 that the loss modulus G” of the HMDS/T-OWRs or ODA/T-OWRs/SBS composite modified asphalt of the two modified asphalts at the same temperature is greater than that of the OWRs/SBS modified asphalt only treated with fluorine precipitation. Loss modulus G”, indicating the enhanced viscous properties of HMDS/T-OWRs or ODA/T-OWRs modified asphalt.
由图1-3可知,HMDS/T-OWRs或ODA/T-OWRs/SBS复合改性沥青的复数剪切模量G*、储能模量G'和损失模量G”均大于仅沉氟处理OWRs/SBS改性沥青。这说明在粘性得到提高的同时,弹性也得到了一定的提高。证明经过改性后的大修渣粉末加入沥青后能有效提高沥青的粘弹性能及抗形变能力。It can be seen from Figure 1-3 that the complex shear modulus G*, storage modulus G' and loss modulus G" of HMDS/T-OWRs or ODA/T-OWRs/SBS composite modified asphalt are all larger than those of only precipitation fluorine. Treating OWRs/SBS modified asphalt. This shows that while the viscosity is improved, the elasticity is also improved to a certain extent. It proves that the modified overhaul slag powder can effectively improve the viscoelastic performance and deformation resistance of asphalt after adding asphalt.
试验例2Test Example 2
探讨单宁酸加入量对大修渣中氟离子浓度的影响,方法同实施例3,区别在于,单宁酸加入量分别为0g、0.25g、0.5g、0.75g、1.0g、1.25g,结果如图4所示。The effect of the amount of tannic acid added on the fluoride ion concentration in the overhaul slag was discussed. The method was the same as that in Example 3. As shown in Figure 4.
从图4中可以看出,随着单宁酸加入量的增加,氟离子浓度逐渐降低,加入量为1.0g时氟离子浓度达到最低,但是当继续增加单宁酸用量时,氟离子浓度略有增加,这证明在0.75g时单宁酸已将大修渣完全包裹,0.75g是性能达标的最低加入点。It can be seen from Figure 4 that with the increase of the amount of tannic acid added, the concentration of fluoride ions gradually decreased, and the concentration of fluoride ions reached the lowest when the amount of tannic acid was 1.0 g. There is an increase, which proves that the tannins have completely wrapped the overhaul residue at 0.75g, and 0.75g is the lowest addition point to meet the performance standards.
试验例3Test Example 3
将实施例3得到的六甲基二硅烷胺/单宁酸复合改性大修渣与改性前的大修渣进行毒性浸泡实验,结果如图5所示。The hexamethyldisilazane/tannic acid composite modified overhaul slag obtained in Example 3 and the overhaul slag before modification were subjected to a toxicity soaking test, and the results are shown in FIG. 5 .
从图5中可以看出,改性大修渣在长时间毒性浸泡实验中表现出明显的氟化物封存能力,虽然在前期会出现一定的浸出情况,但是可以看到平稳后的氟离子浓度具有很好的稳定性,50多天的浸泡过程中氟离子浓度几乎不变。As can be seen from Figure 5, the modified overhaul slag showed obvious fluoride sequestration ability in the long-term toxicity immersion test. Although there will be a certain leaching situation in the early stage, it can be seen that the fluoride ion concentration after stabilization has a very high fluoride ion concentration. Good stability, the fluoride ion concentration is almost unchanged during the soaking process of more than 50 days.
将实施例3得到的改性大修渣作为改性剂加入沥青之后,沥青自身会形成改性剂表面的保护层,改性后的改性剂在沥青中分布均匀,表界面力强,沥青会均匀且严密的包覆改性剂表面,因此在实际使用过程中会表现出更好的保护效果。After the modified overhaul slag obtained in Example 3 is added to the asphalt as a modifier, the asphalt itself will form a protective layer on the surface of the modifier, the modified modifier is evenly distributed in the asphalt, the surface interface is strong, and the asphalt will The surface of the modifier is uniformly and tightly coated, so it will show better protection during actual use.
以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present invention shall be included in the protection scope of the present invention. within.
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