CN110075782A - A kind of novel arsenic adsorbent material and preparation method thereof - Google Patents
A kind of novel arsenic adsorbent material and preparation method thereof Download PDFInfo
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- 239000000463 material Substances 0.000 title claims abstract description 56
- 229910052785 arsenic Inorganic materials 0.000 title claims abstract description 49
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 title claims abstract description 48
- 238000002360 preparation method Methods 0.000 title claims abstract description 13
- 239000003463 adsorbent Substances 0.000 title claims description 19
- 239000003818 cinder Substances 0.000 claims abstract description 52
- 239000002904 solvent Substances 0.000 claims abstract description 20
- 229940037003 alum Drugs 0.000 claims abstract description 18
- 239000002994 raw material Substances 0.000 claims abstract description 17
- 239000004484 Briquette Substances 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 10
- 239000013110 organic ligand Substances 0.000 claims abstract description 7
- 239000000853 adhesive Substances 0.000 claims abstract description 6
- 230000001070 adhesive effect Effects 0.000 claims abstract description 6
- 239000003381 stabilizer Substances 0.000 claims abstract description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 29
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 27
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 18
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical group [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims description 6
- 229910019142 PO4 Inorganic materials 0.000 claims description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 6
- 239000010452 phosphate Substances 0.000 claims description 6
- 229920002635 polyurethane Polymers 0.000 claims description 6
- 239000004814 polyurethane Substances 0.000 claims description 6
- 238000010298 pulverizing process Methods 0.000 claims description 6
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 4
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 claims description 3
- TVQLLNFANZSCGY-UHFFFAOYSA-N disodium;dioxido(oxo)tin Chemical compound [Na+].[Na+].[O-][Sn]([O-])=O TVQLLNFANZSCGY-UHFFFAOYSA-N 0.000 claims description 3
- 229910052943 magnesium sulfate Inorganic materials 0.000 claims description 3
- 235000019341 magnesium sulphate Nutrition 0.000 claims description 3
- 229940079864 sodium stannate Drugs 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 2
- CMPQUABWPXYYSH-UHFFFAOYSA-N phenyl phosphate Chemical compound OP(O)(=O)OC1=CC=CC=C1 CMPQUABWPXYYSH-UHFFFAOYSA-N 0.000 claims description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical group OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims 1
- 239000002253 acid Substances 0.000 claims 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims 1
- 229910052802 copper Inorganic materials 0.000 claims 1
- 239000010949 copper Substances 0.000 claims 1
- 150000002148 esters Chemical class 0.000 claims 1
- 235000019441 ethanol Nutrition 0.000 claims 1
- 238000007654 immersion Methods 0.000 claims 1
- 238000012216 screening Methods 0.000 claims 1
- 238000010792 warming Methods 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 49
- 238000006243 chemical reaction Methods 0.000 abstract description 7
- -1 combines alum Substances 0.000 abstract description 2
- 238000009776 industrial production Methods 0.000 abstract description 2
- 239000011148 porous material Substances 0.000 abstract description 2
- 239000002910 solid waste Substances 0.000 abstract description 2
- 231100000252 nontoxic Toxicity 0.000 abstract 1
- 230000003000 nontoxic effect Effects 0.000 abstract 1
- 238000007873 sieving Methods 0.000 abstract 1
- 239000003245 coal Substances 0.000 description 17
- 239000011259 mixed solution Substances 0.000 description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 230000009286 beneficial effect Effects 0.000 description 6
- 229910021536 Zeolite Inorganic materials 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000010457 zeolite Substances 0.000 description 4
- 241000282414 Homo sapiens Species 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 208000008316 Arsenic Poisoning Diseases 0.000 description 2
- 229910000365 copper sulfate Inorganic materials 0.000 description 2
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 238000005411 Van der Waals force Methods 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007670 carcinogenicity Effects 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- ZJXZSIYSNXKHEA-UHFFFAOYSA-N ethyl dihydrogen phosphate Chemical compound CCOP(O)(O)=O ZJXZSIYSNXKHEA-UHFFFAOYSA-N 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- CAAULPUQFIIOTL-UHFFFAOYSA-N methyl dihydrogen phosphate Chemical group COP(O)(O)=O CAAULPUQFIIOTL-UHFFFAOYSA-N 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4875—Sorbents characterised by the starting material used for their preparation the starting material being a waste, residue or of undefined composition
- B01J2220/4887—Residues, wastes, e.g. garbage, municipal or industrial sludges, compost, animal manure; fly-ashes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/103—Arsenic compounds
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明公开了一种新型砷吸附材料及其制备方法,本发明采用选自固体废弃物的蜂窝煤煤渣作为主原料,结合明矾、稳定剂、有机配体、胶黏剂和溶剂,经浸泡、过筛、搅拌等反应步骤,得到了新型砷吸附材料;本发明的新型砷吸附材料制备工艺简单,原料廉价易得,同时本发明具产品有较大的比表面积和孔体积,具有较好的稳定性及环境友好的特性,能够满足工业化生产的需要。The invention discloses a novel arsenic adsorption material and a preparation method thereof. The invention adopts briquette cinders selected from solid waste as the main raw material, combines alum, stabilizer, organic ligand, adhesive and solvent, and soaks, passes The novel arsenic adsorption material is obtained through reaction steps such as sieving and stirring; the preparation process of the novel arsenic adsorption material of the present invention is simple, the raw material is cheap and easy to obtain, and the product of the present invention has a larger specific surface area and pore volume at the same time, and has better stability Non-toxic and environmentally friendly, it can meet the needs of industrial production.
Description
技术领域technical field
本发明属于吸附材料技术领域,具体的涉及一种新型砷吸附材料及其制备方法。The invention belongs to the technical field of adsorption materials, and in particular relates to a novel arsenic adsorption material and a preparation method thereof.
背景技术Background technique
本发明涉及近年来,随着工农业和采矿、冶金等产业的蓬勃发展,在一定程度上加重了水资源的污染,导致地下水和地表水中砷的含量严重超标。高砷水在满足人类用水的同时也给人们带来了致命的伤害,即所谓的地方性砷中毒,地方性砷中毒长期困扰着人们,并且砷的强致癌性也提醒着人们,为了人类自身的生命健康与安全,必须开发高效经济且环保的饮用水及工业废水除砷工艺。The present invention relates to recent years, with the vigorous development of industry, agriculture, mining, metallurgy and other industries, the pollution of water resources has been aggravated to a certain extent, resulting in serious excess of arsenic content in groundwater and surface water. High-arsenic water not only satisfies human water consumption, but also brings fatal harm to people, which is the so-called endemic arsenic poisoning. Endemic arsenic poisoning has plagued people for a long time, and the strong carcinogenicity of arsenic also reminds people that for the sake of human beings In order to improve the life, health and safety of human beings, it is necessary to develop efficient, economical and environmentally friendly arsenic removal processes for drinking water and industrial wastewater.
因此,近年来各国学者对砷的去除技术进行了大量研究,目前发展较为成熟的砷去除技术主要有以下几种:沉淀法、吸附法、离子交换法、膜技术和生物技术等。吸附法是通过物理作用、化学作用或离子交换等将水中的砷固定在吸附剂的表面,从而将砷去除的方法。吸附法是一种简单易行的水处理技术,在我国应用的最为广泛,目前,在水处理中常用的砷吸附剂有活性氧化铝、活性炭、沸石等。活性氧化铝虽然对As(V)具有良好的去除效果,但通常在pH值为5左右时这种效果才能很好的表现出来,从而限制了其应用;而活性炭和天然沸石对砷的吸附能力又相当有限。因此,研究新型廉价、吸附性能优良的吸附剂是本领域人员亟需解决的技术问题。Therefore, in recent years, scholars from various countries have conducted a lot of research on arsenic removal technology. At present, the relatively mature arsenic removal technology mainly includes the following types: precipitation method, adsorption method, ion exchange method, membrane technology and biotechnology. The adsorption method is a method of fixing arsenic in water on the surface of the adsorbent through physical action, chemical action or ion exchange, so as to remove arsenic. Adsorption is a simple and easy water treatment technology, which is most widely used in our country. At present, the commonly used arsenic adsorbents in water treatment include activated alumina, activated carbon, zeolite and so on. Although activated alumina has a good removal effect on As(V), this effect can only be performed well when the pH value is about 5, which limits its application; while activated carbon and natural zeolite have a good adsorption capacity for arsenic. And quite limited. Therefore, it is an urgent technical problem to be solved by those skilled in the art to research novel and inexpensive adsorbents with excellent adsorption properties.
发明内容SUMMARY OF THE INVENTION
有鉴于此,本发明提供了一种新型砷吸附材料。In view of this, the present invention provides a novel arsenic adsorption material.
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:
新型砷吸附材料,由以下重量份的原料组成:蜂窝煤煤渣30-50份、明矾5-20份、稳定剂5-15份、有机配体10-20份、胶黏剂2-10份、溶剂40-70份。The new arsenic adsorption material is composed of the following raw materials in parts by weight: 30-50 parts of honeycomb cinder, 5-20 parts of alum, 5-15 parts of stabilizer, 10-20 parts of organic ligand, 2-10 parts of adhesive, solvent 40-70 servings.
进一步,上述稳定剂为硫酸镁、硫酸铜、锡酸钠、有机磷酸盐中的一种或几种;Further, the above-mentioned stabilizer is one or more of magnesium sulfate, copper sulfate, sodium stannate, and organic phosphate;
更进一步上述有机磷酸盐为磷酸甲酯、磷酸乙酯或磷酸苯酯。Furthermore, the above-mentioned organic phosphate is methyl phosphate, ethyl phosphate or phenyl phosphate.
采用上述进一步的有益效果在于,本发明采用的稳定剂能够改善蜂窝煤煤渣的空间结构,并且使本发明中的有机配体等物质与蜂窝煤煤渣形成稳定的吸附结构,从而增强了本发明吸附材料的吸附能力,并且还起到了保持原料之间的化学平衡,降低产品的表面张力,有效阻止了光、热分解和氧化分解等作用。The further beneficial effect of adopting the above is that the stabilizer used in the present invention can improve the spatial structure of the briquette cinder, and make the organic ligands and other substances in the present invention form a stable adsorption structure with the briquette cinder, thereby enhancing the adsorption of the present invention. It also plays a role in maintaining the chemical balance between raw materials, reducing the surface tension of products, and effectively preventing light, thermal decomposition and oxidative decomposition.
进一步,上述有机配体为乙二胺或邻苯二甲酸。Further, the above-mentioned organic ligand is ethylenediamine or phthalic acid.
采用上述进一步的有益效果在于,本发明采用的有机配体能够和蜂窝煤煤渣以及明矾产生键结的分子,从而有效提高了本发明吸附材料的吸附能力和吸附容量,同时提高了本发明原料的溶解度,促进了反应速率,有效缩短了制备时间,简化了制备工艺。The further beneficial effect of adopting the above is that the organic ligand used in the present invention can produce bonded molecules with briquette cinder and alum, thereby effectively improving the adsorption capacity and adsorption capacity of the adsorption material of the present invention, and simultaneously improving the solubility of the raw materials of the present invention , promotes the reaction rate, effectively shortens the preparation time, and simplifies the preparation process.
进一步,上述胶黏剂为水性聚氨酯或甲基丙烯酸酯。Further, the above-mentioned adhesive is water-based polyurethane or methacrylate.
采用上述进一步的有益效果在于,本发明利用胶黏剂的优秀理化性能,通过与溶剂的黏附和内聚等作用,增加了溶液的粘稠度,同时增强了物质之间的范德华力的作用,改善了本发明吸附材料的物质结构,进而增强了本发明吸附材料的吸附力。The further beneficial effect of adopting the above is that the present invention utilizes the excellent physical and chemical properties of the adhesive to increase the viscosity of the solution through the adhesion and cohesion with the solvent, and at the same time enhance the effect of the van der Waals force between substances, The substance structure of the adsorption material of the present invention is improved, thereby enhancing the adsorption force of the adsorption material of the present invention.
进一步,上述述溶剂组成为水、乙醇、丙酮、二甲基甲酰胺和异丙醇的任一种或几种混合。Further, the above-mentioned solvent is composed of any one or a mixture of water, ethanol, acetone, dimethylformamide and isopropanol.
更进一步,上述溶剂中水、乙醇、丙酮、二甲基甲酰胺和异丙醇的质量比优选为1:0.5-1.5:0.1-0.5:0.3-0.8:1-2;Further, the mass ratio of water, ethanol, acetone, dimethylformamide and isopropanol in the above solvent is preferably 1:0.5-1.5:0.1-0.5:0.3-0.8:1-2;
更进一步上述溶剂中水、乙醇、丙酮、二甲基甲酰胺和异丙醇的质量比优选为1:1:0.5:0.5:1。Furthermore, the mass ratio of water, ethanol, acetone, dimethylformamide and isopropanol in the above solvent is preferably 1:1:0.5:0.5:1.
采用上述进一步的有益效果在于,本发明以水、乙醇、丙酮、二甲基甲酰胺和异丙醇的混合溶液作为溶剂,本发明采用的溶剂能够任意比例互溶,从而能够充分溶解本发明的溶质,进而扩大了各物质之间的接触面积,对本发明的内部反映起到了有效的催化作用。The further beneficial effect of adopting the above is that the present invention uses a mixed solution of water, ethanol, acetone, dimethylformamide and isopropanol as a solvent, and the solvent used in the present invention can be miscible in any proportion, thereby fully dissolving the solute of the present invention , and then expand the contact area between the various substances, and effectively catalyze the internal reflection of the present invention.
本发明还提供了上述新型砷吸附材料的制备方法,包括以下步骤:The present invention also provides a preparation method for the above-mentioned novel arsenic adsorption material, comprising the following steps:
1)按权利要求1-6任一项所述新型砷吸附材料的重量分数称取各原料,备用;1) take each raw material according to the weight fraction of the novel arsenic adsorption material described in any one of claims 1-6, and set aside;
(2)将称好的煤渣用水浸泡10-60min之后,将浸泡后的煤渣烘干;(2) After soaking the weighed cinder in water for 10-60min, dry the soaked cinder;
(3)将烘干后的煤渣进行过筛,舍去筛下物质,将剩余物质进行超声粉碎之后得到粉碎煤渣;(3) Sieve the dried coal cinder, discard the under-sieve material, and obtain pulverized coal cinder after the remaining material is ultrasonically pulverized;
(4)将步骤(3)中粉碎后的煤渣与其他原料进行搅拌混合之后,得到煤渣浊液,将煤渣浊液以5℃/min的升温速率升温到150℃,保持2-12h,得到负载明矾的多孔结构煤渣;(4) After stirring and mixing the pulverized coal slag in step (3) with other raw materials, the coal slag turbid liquid is obtained, and the coal slag turbid liquid is heated up to 150°C at a heating rate of 5°C/min, and kept for 2-12h to obtain a loaded Porous structure cinder of alum;
(5)将步骤(4)中的负载明矾的多孔结构煤渣过滤之后,在200-240℃下干燥1-5h,得到新型砷吸附材料。(5) After filtering the cinder with a porous structure loaded with alum in step (4), drying at 200-240° C. for 1-5 hours to obtain a novel arsenic adsorption material.
进一步,上述步骤(2)中烘干温度为100-150℃,烘干时间为20-40min。Further, the drying temperature in the above step (2) is 100-150° C., and the drying time is 20-40 minutes.
进一步,上述步骤(3)中过筛粒径为100-250目。Further, the sieved particle size in the above step (3) is 100-250 mesh.
采用上述进一步的有益效果在于,将蜂窝煤煤渣中的灰烬进行筛除,能够有效防止杂质对本发明吸附材料的吸附容量和吸附力的影响,促进了本发明吸附材料的结构形成,有效提高了吸附容量。The further beneficial effect of adopting the above is that the ashes in the briquette cinders are screened out, which can effectively prevent the influence of impurities on the adsorption capacity and adsorption force of the adsorption material of the present invention, promote the formation of the structure of the adsorption material of the present invention, and effectively improve the adsorption capacity. .
进一步,上述步骤(4)中搅拌速率为1500-3000r/min,搅拌时间为10-30min。Further, in the above step (4), the stirring speed is 1500-3000r/min, and the stirring time is 10-30min.
与现有技术相比,本发明的有益效果在于:Compared with the prior art, the beneficial effects of the present invention are:
本发明所得的砷吸附材料具有较大的比表面积和孔体积,具有较好的稳定性及环境友好的特性;本发明产品的主原料选自固体废弃物,所有原料廉价易得,制备工艺简单,无需惰性气体保护,制备成本低廉,能满足工业化生产和使用的需要;本发明的产品的吸附容量大,吸附速率快,能同时去除试样中的三价砷和五价砷。The arsenic adsorption material obtained in the present invention has a large specific surface area and pore volume, and has good stability and environment-friendly characteristics; the main raw material of the product of the present invention is selected from solid waste, all raw materials are cheap and easy to obtain, and the preparation process is simple , without inert gas protection, low preparation cost, and can meet the needs of industrial production and use; the product of the invention has a large adsorption capacity and a fast adsorption rate, and can simultaneously remove trivalent arsenic and pentavalent arsenic in samples.
具体实施方式Detailed ways
下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below. Obviously, the described embodiments are only some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
实施例1Example 1
新型砷吸附材料:New arsenic adsorption materials:
(1)称取蜂窝煤煤渣30g、明矾20g、有机磷酸盐5g、邻苯二甲酸10g、水性聚氨酯2g、溶剂40g,备用,溶剂中水、乙醇、丙酮的质量比为1:1.5:0.5;(1) Weigh 30g of honeycomb briquette cinder, 20g of alum, 5g of organic phosphate, 10g of phthalic acid, 2g of water-based polyurethane, and 40g of solvent for subsequent use. The mass ratio of water, ethanol, and acetone in the solvent is 1:1.5:0.5;
(2)将称好的煤渣用水浸湿,侵泡10min之后,在150℃下烘干20min;(2) Wet the weighed cinders with water, soak them for 10 minutes, and then dry them at 150°C for 20 minutes;
(3)将烘干后的煤渣进行过250目筛,舍去筛下物质,将剩余物质进行超声粉碎,得到粉碎煤渣;(3) passing the dried coal cinder through a 250-mesh sieve, discarding the material under the sieve, and ultrasonically pulverizing the remaining material to obtain pulverized coal cinder;
(4)将步骤(3)中粉碎后的煤渣与其他原料在3000r/min的速率下搅拌10min进行混合反应之后,以5℃/min的升温速率升温到150℃,保持12h,得到负载明矾的多孔结构煤渣;(4) After stirring the pulverized coal cinder and other raw materials at a speed of 3000r/min for 10min for a mixed reaction in step (3), the temperature was raised to 150°C at a heating rate of 5°C/min and kept for 12h to obtain alum-loaded Porous structure cinder;
(5)将步骤(4)中的混合溶液在200℃下干5h之后,过滤得到新型砷吸附材料。(5) After drying the mixed solution in step (4) at 200° C. for 5 hours, filter to obtain a novel arsenic adsorption material.
实施例2Example 2
新型砷吸附材料:New arsenic adsorption materials:
(1)称取蜂窝煤煤渣50g、明矾5g、硫酸镁15g、乙二胺20g、水性聚氨酯10g、溶剂70g,备用,溶剂中水、乙醇、丙酮、二甲基甲酰胺和异丙醇的质量比为1:0.5:0.1:0.3:1;(1) Take by weighing 50g of briquette cinder, 5g of alum, 15g of magnesium sulfate, 20g of ethylenediamine, 10g of water-based polyurethane, and 70g of solvent, for subsequent use, the mass ratio of water, ethanol, acetone, dimethylformamide and isopropanol in the solvent 1:0.5:0.1:0.3:1;
(2)将称好的煤渣用水浸湿,侵泡60min之后,在100℃下烘干40min;(2) Wet the weighed cinders with water, soak them for 60 minutes, and then dry them at 100°C for 40 minutes;
(3)将烘干后的煤渣进行过100目筛,舍去筛下物质,将剩余物质进行超声粉碎,得到粉碎煤渣;(3) passing the dried coal cinder through a 100-mesh sieve, discarding the material under the sieve, and ultrasonically pulverizing the remaining material to obtain pulverized coal cinder;
(4)将步骤(3)中粉碎后的煤渣与其他原料在1500r/min的速率下搅拌130min进行混合反应之后,将混合溶液以5℃/min的升温速率升温到150℃,保持2h,得到负载明矾的多孔结构煤渣;(4) After stirring the pulverized cinder and other raw materials at a rate of 1500r/min for 130min for a mixed reaction in step (3), the mixed solution was heated to 150°C at a heating rate of 5°C/min and kept for 2h to obtain Porous structure cinder loaded with alum;
(5)将步骤(4)中的混合溶液在240℃下干燥1h之后,过滤得到新型砷吸附材料。(5) After the mixed solution in step (4) was dried at 240° C. for 1 hour, it was filtered to obtain a novel arsenic adsorption material.
实施例3Example 3
新型砷吸附材料:New arsenic adsorption materials:
(1)称取蜂窝煤煤渣42g、明矾13g、锡酸钠8g、乙二胺17g、甲基丙烯酸酯6g、溶剂45g,备用,溶剂中水、乙醇、丙酮、二甲基甲酰胺和异丙醇的质量比为1:0.8:0.4:0.8:1;(1) Weigh 42g of briquette cinder, 13g of alum, 8g of sodium stannate, 17g of ethylenediamine, 6g of methacrylate, and 45g of solvent, and set aside, water, ethanol, acetone, dimethylformamide and isopropanol in the solvent The mass ratio is 1:0.8:0.4:0.8:1;
(2)将称好的煤渣用水浸湿,侵泡30min之后,在140℃下烘干25min;(2) Wet the weighed cinders with water, soak them for 30 minutes, and then dry them at 140°C for 25 minutes;
(3)将烘干后的煤渣进行过200目筛,舍去筛下物质,将剩余物质进行超声粉碎,得到粉碎煤渣;(3) passing the dried coal cinder through a 200-mesh sieve, discarding the material under the sieve, and ultrasonically pulverizing the remaining material to obtain pulverized coal cinder;
(4)将步骤(3)中粉碎后的煤渣与其他原料在2500r/min的速率下搅拌15min进行混合反应之后,将混合溶液以5℃/min的升温速率升温到150℃,保持6h,得到负载明矾的多孔结构煤渣;(4) After stirring the pulverized cinder in step (3) and other raw materials for 15 min at a rate of 2500 r/min for a mixed reaction, the mixed solution was heated to 150 °C at a heating rate of 5 °C/min and kept for 6 h to obtain Porous structure cinder loaded with alum;
(5)将步骤(4)中的混合溶液在220℃下干燥3h之后,过滤得到新型砷吸附材料。(5) After the mixed solution in step (4) was dried at 220° C. for 3 hours, it was filtered to obtain a novel arsenic adsorption material.
实施例4Example 4
新型砷吸附材料:New arsenic adsorption materials:
(1)称取蜂窝煤煤渣36g、明矾9g、有机磷酸盐8g、邻苯二甲酸14g、水性聚氨酯4g、溶剂65g,备用,溶剂中水、乙醇、丙酮、二甲基甲酰胺和异丙醇的质量比为1:1:0.5:0.5:1;(1) Weigh 36g of honeycomb coal cinder, 9g of alum, 8g of organic phosphate, 14g of phthalic acid, 4g of water-based polyurethane, 65g of solvent, for subsequent use, the amount of water, ethanol, acetone, dimethylformamide and isopropanol in the solvent The mass ratio is 1:1:0.5:0.5:1;
(2)将称好的煤渣用水浸湿,侵泡45min之后,在120℃下烘干30min;(2) Wet the weighed cinders with water, soak them for 45 minutes, and then dry them at 120°C for 30 minutes;
(3)将烘干后的煤渣进行过250目筛,舍去筛下物质,将剩余物质进行超声粉碎,得到粉碎煤渣;(3) passing the dried coal cinder through a 250-mesh sieve, discarding the material under the sieve, and ultrasonically pulverizing the remaining material to obtain pulverized coal cinder;
(4)将步骤(3)中粉碎后的煤渣与其他原料在2000r/min的速率下搅拌30min进行混合反应之后,将混合溶液以5℃/min的升温速率升温到150℃,保持8h,得到负载明矾的多孔结构煤渣;(4) After stirring the crushed cinder in step (3) and other raw materials for 30 minutes at a rate of 2000 r/min for a mixed reaction, the mixed solution was heated to 150 °C at a heating rate of 5 °C/min and kept for 8 hours to obtain Porous structure cinder loaded with alum;
(5)将步骤(4)中的混合溶液在200℃下干燥3h之后,过滤得到新型砷吸附材料。(5) After the mixed solution in step (4) was dried at 200° C. for 3 hours, it was filtered to obtain a novel arsenic adsorption material.
实施例5Example 5
新型砷吸附材料:New arsenic adsorption materials:
(1)称取蜂窝煤煤渣48g、明矾16g、硫酸铜5-15g、乙二胺15g、水性聚氨酯3g、溶剂50g,备用,溶剂中水、乙醇、丙酮、二甲基甲酰胺和异丙醇的质量比为1:1.5:0.2:0.8:2;(1) Weigh 48g of briquette cinder, 16g of alum, 5-15g of copper sulfate, 15g of ethylenediamine, 3g of water-based polyurethane, and 50g of solvent, and set aside, the amount of water, ethanol, acetone, dimethylformamide and isopropanol in the solvent The mass ratio is 1:1.5:0.2:0.8:2;
(2)将称好的煤渣用水浸湿,侵泡20min之后,在150℃下烘干30min;(2) Wet the weighed cinders with water, soak them for 20 minutes, and then dry them at 150°C for 30 minutes;
(3)将烘干后的煤渣进行过100目筛,舍去筛下物质,将剩余物质进行超声粉碎,得到粉碎煤渣;(3) passing the dried coal cinder through a 100-mesh sieve, discarding the material under the sieve, and ultrasonically pulverizing the remaining material to obtain pulverized coal cinder;
(4)将步骤(3)中粉碎后的煤渣与其他原料在3000r/min的速率下搅拌15min进行混合反应之后,将混合溶液以5℃/min的升温速率升温到150℃,保持10h,得到负载明矾的多孔结构煤渣;(4) After stirring the pulverized cinder in step (3) and other raw materials for 15 minutes at a rate of 3000 r/min for a mixed reaction, the mixed solution was heated to 150 °C at a heating rate of 5 °C/min and kept for 10 h to obtain Porous structure cinder loaded with alum;
(5)将步骤(4)中的混合溶液在200℃下干燥3h之后,过滤得到新型砷吸附材料。(5) After the mixed solution in step (4) was dried at 200° C. for 3 hours, it was filtered to obtain a novel arsenic adsorption material.
试验例Test case
取本发明实施例1-5产品各1g,与1g活性氧化铝、1g活性炭、1g天然沸石和1g市售的MOF材料的吸附容量结果进行对比进行,具体数据如表1所示;Take each 1g of the products of Examples 1-5 of the present invention, and compare them with the adsorption capacity results of 1g of activated alumina, 1g of activated carbon, 1g of natural zeolite and 1g of commercially available MOF materials, and the specific data are as shown in Table 1;
表1本发明与不同类型吸附剂的吸附容量对比Table 1 The present invention compares with the adsorption capacity of different types of adsorbents
由以上数据可见,本发明的新型砷吸附材料的同等条件下对三价As和五价As的吸附量远高于现有技术中的吸附剂,证明本发明是一种具有高效率、大吸附容量的新型砷吸附材料。It can be seen from the above data that the adsorption capacity of the novel arsenic adsorption material of the present invention to trivalent As and pentavalent As under the same conditions is much higher than that of the adsorbents in the prior art, which proves that the present invention is a kind of high-efficiency, large adsorption A new type of arsenic adsorption material with high capacity.
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