CN105597681B - A kind of preparation method for the NCC/PVA/PVP carbon blended sponges that can efficiently remove Heavy Metals in Waters ion and organic dyestuff - Google Patents
A kind of preparation method for the NCC/PVA/PVP carbon blended sponges that can efficiently remove Heavy Metals in Waters ion and organic dyestuff Download PDFInfo
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 69
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 67
- 238000002360 preparation method Methods 0.000 title claims abstract description 51
- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 39
- 239000000975 dye Substances 0.000 title claims abstract description 28
- 239000003643 water by type Substances 0.000 title 1
- 239000000725 suspension Substances 0.000 claims abstract description 103
- 229920000036 polyvinylpyrrolidone Polymers 0.000 claims abstract description 99
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims abstract description 99
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims abstract description 98
- 239000004372 Polyvinyl alcohol Substances 0.000 claims abstract description 89
- 229920002451 polyvinyl alcohol Polymers 0.000 claims abstract description 89
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 47
- 150000002500 ions Chemical class 0.000 claims abstract description 35
- 229920001046 Nanocellulose Polymers 0.000 claims abstract description 18
- 229920000168 Microcrystalline cellulose Polymers 0.000 claims abstract description 14
- 238000000137 annealing Methods 0.000 claims abstract description 14
- 235000019813 microcrystalline cellulose Nutrition 0.000 claims abstract description 14
- 239000008108 microcrystalline cellulose Substances 0.000 claims abstract description 14
- 229940016286 microcrystalline cellulose Drugs 0.000 claims abstract description 14
- 239000000243 solution Substances 0.000 claims description 43
- 238000001179 sorption measurement Methods 0.000 claims description 39
- 239000002243 precursor Substances 0.000 claims description 30
- 239000000843 powder Substances 0.000 claims description 23
- 239000002245 particle Substances 0.000 claims description 21
- 238000006243 chemical reaction Methods 0.000 claims description 20
- 239000008367 deionised water Substances 0.000 claims description 20
- 229910021641 deionized water Inorganic materials 0.000 claims description 20
- 238000002156 mixing Methods 0.000 claims description 10
- 238000012546 transfer Methods 0.000 claims description 9
- -1 polyethylene Polymers 0.000 claims description 8
- 238000006136 alcoholysis reaction Methods 0.000 claims description 7
- 229920002678 cellulose Polymers 0.000 claims description 5
- 239000001913 cellulose Substances 0.000 claims description 5
- 239000007795 chemical reaction product Substances 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 239000011259 mixed solution Substances 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 4
- 238000001132 ultrasonic dispersion Methods 0.000 claims description 4
- 239000003431 cross linking reagent Substances 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims 5
- 229920000573 polyethylene Polymers 0.000 claims 5
- 235000010980 cellulose Nutrition 0.000 claims 2
- 229920006316 polyvinylpyrrolidine Polymers 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 25
- 239000003960 organic solvent Substances 0.000 abstract description 4
- 239000002121 nanofiber Substances 0.000 abstract 1
- 238000010521 absorption reaction Methods 0.000 description 11
- 229920000642 polymer Polymers 0.000 description 10
- KMUONIBRACKNSN-UHFFFAOYSA-N potassium dichromate Chemical compound [K+].[K+].[O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O KMUONIBRACKNSN-UHFFFAOYSA-N 0.000 description 10
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 9
- 239000003575 carbonaceous material Substances 0.000 description 9
- 229960000907 methylthioninium chloride Drugs 0.000 description 9
- 239000000047 product Substances 0.000 description 9
- 230000008859 change Effects 0.000 description 8
- 239000000835 fiber Substances 0.000 description 7
- 239000002114 nanocomposite Substances 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000011651 chromium Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 4
- 238000002835 absorbance Methods 0.000 description 4
- 238000001354 calcination Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 238000001228 spectrum Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000003763 carbonization Methods 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 2
- 238000001157 Fourier transform infrared spectrum Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910021389 graphene Inorganic materials 0.000 description 2
- 229940046892 lead acetate Drugs 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229960002523 mercuric chloride Drugs 0.000 description 2
- LWJROJCJINYWOX-UHFFFAOYSA-L mercury dichloride Chemical compound Cl[Hg]Cl LWJROJCJINYWOX-UHFFFAOYSA-L 0.000 description 2
- 239000002086 nanomaterial Substances 0.000 description 2
- 239000002105 nanoparticle Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000001338 self-assembly Methods 0.000 description 2
- UOFGSWVZMUXXIY-UHFFFAOYSA-N 1,5-Diphenyl-3-thiocarbazone Chemical compound C=1C=CC=CC=1N=NC(=S)NNC1=CC=CC=C1 UOFGSWVZMUXXIY-UHFFFAOYSA-N 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 239000004966 Carbon aerogel Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000004964 aerogel Substances 0.000 description 1
- 238000003321 atomic absorption spectrophotometry Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 230000009920 chelation Effects 0.000 description 1
- 229910001430 chromium ion Inorganic materials 0.000 description 1
- JOPOVCBBYLSVDA-UHFFFAOYSA-N chromium(6+) Chemical compound [Cr+6] JOPOVCBBYLSVDA-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007850 degeneration Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 229940077449 dichromate ion Drugs 0.000 description 1
- SOCTUWSJJQCPFX-UHFFFAOYSA-N dichromate(2-) Chemical compound [O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O SOCTUWSJJQCPFX-UHFFFAOYSA-N 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000001523 electrospinning Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229910021432 inorganic complex Inorganic materials 0.000 description 1
- 238000009830 intercalation Methods 0.000 description 1
- 230000002687 intercalation Effects 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 230000005389 magnetism Effects 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 150000002843 nonmetals Chemical class 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 238000006053 organic reaction Methods 0.000 description 1
- 239000013339 polymer-based nanocomposite Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 235000019422 polyvinyl alcohol Nutrition 0.000 description 1
- 239000012217 radiopharmaceutical Substances 0.000 description 1
- 229940121896 radiopharmaceutical Drugs 0.000 description 1
- 230000002799 radiopharmaceutical effect Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000002336 sorption--desorption measurement Methods 0.000 description 1
- 238000002798 spectrophotometry method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 238000003911 water pollution 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
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- 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
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
-
- 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
- C02F2101/20—Heavy metals or heavy metal compounds
-
- 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
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/22—Chromium or chromium compounds, e.g. chromates
-
- 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
- C02F2101/30—Organic compounds
- C02F2101/308—Dyes; Colorants; Fluorescent agents
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明提供了一种通过微波退火法制备高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵的制备方法,包括步骤:1)用硫酸法将微晶纤维素制备纳米纤维素悬浊液;2)将聚乙烯醇加入步骤1)所得到的悬浊液;3)将聚乙烯吡咯烷酮加入步骤1)所得到的悬浊液;4)将步骤2)和3)中得到的悬浊液按比例混合,然后在微波下退火处理即可得到纳米纤维素/聚乙烯醇/聚乙烯吡咯烷酮共混碳海绵。根据本发明的制备方法制备的共混碳海绵具有稳定的形态,产物纯度高,且对重金属离子和有机溶剂的去除率高。
The invention provides a method for preparing an NCC/PVA/PVP blended carbon sponge capable of efficiently removing heavy metal ions and organic dyes in water by a microwave annealing method, comprising steps: 1) preparing nanofibers from microcrystalline cellulose by a sulfuric acid method plain suspension; 2) polyvinyl alcohol is added to the suspension obtained in step 1); 3) polyvinylpyrrolidone is added to the suspension obtained in step 1); 4) steps 2) and 3) are obtained in The suspensions are mixed in proportion, and then annealed under microwave to obtain nanocellulose/polyvinyl alcohol/polyvinylpyrrolidone blended carbon sponge. The blended carbon sponge prepared by the preparation method of the present invention has a stable shape, high product purity, and high removal rate of heavy metal ions and organic solvents.
Description
技术领域technical field
本发明涉及一种纳米纤维素/聚乙烯醇/聚乙烯吡咯烷酮(NCC/PVA/PVP)共混碳海绵的制备方法,特别涉及一种微波退火法制备高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵的制备方法。The present invention relates to a preparation method of nano-cellulose/polyvinyl alcohol/polyvinylpyrrolidone (NCC/PVA/PVP) blended carbon sponge, in particular to a microwave annealing method to prepare NCC for efficiently removing heavy metal ions and organic dyes in water Preparation method of /PVA/PVP blended carbon sponge.
背景技术Background technique
由相互贯通或封闭的孔洞构成网络结构的多孔炭材料在具备炭材料性质(如化学稳定性高、导电性好、价廉等)优点的同时,还具有比表面积大等特点。因此,多孔炭材料可应用于分离净化、催化、光学器件、能量存储、生物分离薄膜及纳米反应器等领域。由三维网络结构形成的大孔结构使多孔炭材料具有优异的吸附性能。目前,随着多孔炭材料研究的深入,制备多孔炭材料不仅需要控制其介观结构、孔径及孔道排列,而且对其微米级的宏观形貌也有要求。现已成功合成了球、纤维、棒、单晶和块体材料等多种形貌的介孔炭材料。使得多孔碳材料在污水处理,水体净化领域有重要的作用。Porous carbon materials with a network structure composed of interpenetrating or closed pores not only have the advantages of carbon material properties (such as high chemical stability, good electrical conductivity, low price, etc.), but also have the characteristics of large specific surface area. Therefore, porous carbon materials can be used in the fields of separation and purification, catalysis, optical devices, energy storage, bioseparation membranes, and nanoreactors. The macroporous structure formed by the three-dimensional network structure makes the porous carbon material have excellent adsorption performance. At present, with the deepening of research on porous carbon materials, the preparation of porous carbon materials not only needs to control its mesoscopic structure, pore size and pore arrangement, but also requires its micron-scale macroscopic morphology. Mesoporous carbon materials with various shapes such as spheres, fibers, rods, single crystals and bulk materials have been successfully synthesized. This makes porous carbon materials play an important role in the fields of sewage treatment and water purification.
聚合物基纳米复合材料是指以高聚物为基体,与金属、无机非金属以及有机物纳米粒子等进行复合而得到的一种性能优异的材料。这种复合材料既有高聚物本身的优点,又兼备了纳米粒子的特异属性,因而使其在力学、催化、功能材料(光、电、磁、敏感)等领域内得到应用,甚至出现全新的性能和功能,例如高强度、高模量、高韧性、高耐热性、高透明性、高导电性、对油类和气体的高阻隔性等,因而有着广阔的发展前景。聚合物纳米复合材料可分为聚合物/无机物纳米复合材料和聚合物/聚合物纳米复合材料。近年来大量的研究集中于制备单一组分的不同形貌和结构的碳纤维、碳气凝胶等对水体中重金属离子和有机染料的去除,对于多组分共混,纳米材料与高聚物共混制备碳材料研究很少。目前制备的重金属离子和有机染料的吸附材料有多孔纤维、石墨烯气凝胶、碳纳米复合纤维、淀粉-碳膜材料等。如由Zhao等提出的以聚苯乙烯为基体,通过电纺丝技术制备了具有多空隙结构的纤维对油有很高的吸附率(Jing Wu,Nu Wang,Li Wang,Hua Dong,Yong Zhao,and LeiJing ACS Appl.Mater.Interfaces,2012,4,3207-3212);由Li等提出的以自组装方法制备的可压缩石墨烯气凝胶对有机溶剂的去除可循环使用(Jihao Li,Jingye Li,Hu Meng,Siyuan Xie,Bowu Zhang,Linfan Li,Hongjuan Ma,Jianyong Zhang and Ming Yu,J.Mater.Chem.A,2014,2,2934–2941;由Guo等提出的以棉纤维为原料通过微波退火和煅烧等方法制备的具有多孔的可磁性吸附重金属离子的碳纳米复合纤维(Jiahua Zhu,HongboGu,Jiang Guo,Minjiao Chen,Huige Wei,Zhiping Luo,Henry A.Colorado,NarendranathYerra,Daowei Ding,Thomas C.Ho,Neel Haldolaarachchige,Jack Hopper,DavidP.Young,Zhanhu Guo and Suying Wei,J.Mater.Chem.A,2014,2,2256–2265);由Mezzenga等提出的用淀粉和碳杂化制备用于净化水的膜可去除重金属离子和有机溶剂(SreenathBolisetty and Raffaele Mezzenga,Nature Nanotechnology,2016,DOI:10.1038/NNANO.2015.310。Polymer-based nanocomposites refer to materials with excellent performance obtained by compounding polymers with metals, inorganic non-metals, and organic nanoparticles. This kind of composite material not only has the advantages of polymer itself, but also has the specific properties of nanoparticles, so it can be applied in the fields of mechanics, catalysis, functional materials (light, electricity, magnetism, sensitivity), etc., and even new Its properties and functions, such as high strength, high modulus, high toughness, high heat resistance, high transparency, high conductivity, high barrier to oil and gas, etc., thus have broad development prospects. Polymer nanocomposites can be divided into polymer/inorganic nanocomposites and polymer/polymer nanocomposites. In recent years, a large number of studies have focused on the preparation of carbon fibers with different shapes and structures of single components, carbon aerogels, etc. to remove heavy metal ions and organic dyes in water. For multi-component blending, nanomaterials and polymers There are few studies on hybrid carbon materials. The currently prepared adsorption materials for heavy metal ions and organic dyes include porous fibers, graphene aerogels, carbon nanocomposite fibers, and starch-carbon membrane materials. For example, based on polystyrene as the matrix proposed by Zhao et al., the fiber with multi-void structure was prepared by electrospinning technology, which has a high adsorption rate for oil (Jing Wu, Nu Wang, Li Wang, Hua Dong, Yong Zhao, and LeiJing ACS Appl.Mater.Interfaces,2012,4,3207-3212); the compressible graphene airgel prepared by self-assembly method proposed by Li et al. can be recycled for the removal of organic solvents (Jihao Li, Jingye Li ,Hu Meng,Siyuan Xie,Bowu Zhang,Linfan Li,Hongjuan Ma,Jianyong Zhang and Ming Yu,J.Mater.Chem.A,2014,2,2934–2941; Cotton fiber as raw material proposed by Guo et al. Porous carbon nanocomposite fibers that can magnetically adsorb heavy metal ions prepared by annealing and calcination (Jiahua Zhu, HongboGu, Jiang Guo, Minjiao Chen, Huige Wei, Zhiping Luo, Henry A.Colorado, Narendranath Yerra, Daowei Ding, Thomas C .Ho, Neel Haldolaarachchige, Jack Hopper, DavidP.Young, Zhanhu Guo and Suying Wei, J.Mater.Chem.A, 2014, 2, 2256–2265); proposed by Mezzenga et al. Membranes for water purification can remove heavy metal ions and organic solvents (Sreenath Bolisetty and Raffaele Mezzenga, Nature Nanotechnology, 2016, DOI: 10.1038/NNANO.2015.310.
近年来微波已经被广泛地应用于化学领域,包括分子筛制备、放射性药物的合成、无机配合物的合成与嵌入反应、干燥条件下的有机反应、等离子体化学、分析化学中的样品预处理及催化等。近年来,微波法因其具有特殊效应已引起了材料科学界的极大关注。与传统方法相比,微波法具有反应速度快、反应条件温和及反应效率高等优点,而且产品具有较高的纯度、窄的粒径分布和均一的形态,并适于推广到大规模的工业生产中去,因而在纳米材料合成领域中显示了良好的发展态势和广阔的应用前景。由Guo等提出的以棉纤维为原料通过微波退火方法制备的具有多孔的可磁性吸附重金属离子的碳纳米复合纤维(JiahuaZhu,Hongbo Gu,Jiang Guo,Minjiao Chen,Huige Wei,Zhiping Luo,Henry A.Colorado,Narendranath Yerra,Daowei Ding,Thomas C.Ho,Neel Haldolaarachchige,JackHopper,David P.Young,Zhanhu Guo and Suying Wei,J.Mater.Chem.A,2014,2,2256–2265);但是关于NCC/PVA/PVP共混碳海绵鲜有报道,开展这方面的研究发明,对水体污染的处理,以及规模化生产有很重要的意义。In recent years, microwave has been widely used in the field of chemistry, including preparation of molecular sieves, synthesis of radiopharmaceuticals, synthesis and intercalation reactions of inorganic complexes, organic reactions under dry conditions, plasma chemistry, sample pretreatment and catalysis in analytical chemistry. Wait. In recent years, the microwave method has attracted great attention in the material science community because of its special effects. Compared with the traditional method, the microwave method has the advantages of fast reaction speed, mild reaction conditions and high reaction efficiency, and the product has higher purity, narrow particle size distribution and uniform shape, and is suitable for large-scale industrial production Therefore, it shows a good development trend and broad application prospects in the field of nanomaterial synthesis. Porous carbon nanocomposite fibers that can magnetically absorb heavy metal ions were prepared from cotton fibers by microwave annealing method proposed by Guo et al. (JiahuaZhu, Hongbo Gu, Jiang Guo, Minjiao Chen, Huige Wei, Zhiping Luo, Henry A. Colorado, Narendranath Yerra, Daowei Ding, Thomas C.Ho, Neel Haldolaarachchige, JackHopper, David P.Young, Zhanhu Guo and Suying Wei, J.Mater.Chem.A, 2014, 2, 2256–2265); but regarding NCC/ There are few reports on PVA/PVP blended carbon sponges. Research and invention in this area is of great significance for the treatment of water pollution and large-scale production.
发明内容Contents of the invention
针对现在水体中重金属离子和有机染料超标和现有技术存在的问题,本发明的一个目的是提供了一种通过微波退火法制备能够高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵的制备方法。Aiming at the existing problems of excessive heavy metal ions and organic dyes in water bodies and existing technologies, an object of the present invention is to provide a NCC/PVA/PVP co-polymer that can efficiently remove heavy metal ions and organic dyes in water bodies by microwave annealing. Preparation method of carbon-mixed sponge.
根据本发明的所述通过微波退火法制备高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵的制备方法,包括如下步骤:According to the preparation method of the NCC/PVA/PVP blended carbon sponge for efficiently removing heavy metal ions and organic dyes in water by microwave annealing method of the present invention, the method comprises the following steps:
1)将微晶纤维素(MCC)用质量百分比浓度为40-70%的硫酸在35-80℃的反应温度下处理10-80min,以制备纳米纤维素(NCC),其中所述微晶纤维素与所述硫酸的质量百分比1:5-20,然后将制得的纳米纤维素分散在水中,在超声波条件下配制成均匀悬浊液,所得悬浊液先经机械搅拌1-3小时,然后再在超声细胞粉碎机中进一步分散30分钟,超声波的强度为500-1200W,其中相对于1重量份的制得的纳米纤维素,用100-500重量份的去离子水分散,从而制成质量百分比为0.2-1%的悬浊液;1) Microcrystalline cellulose (MCC) is treated with sulfuric acid with a mass percentage concentration of 40-70% at a reaction temperature of 35-80°C for 10-80min to prepare nanocellulose (NCC), wherein the microcrystalline fiber The mass percentage of the element and the sulfuric acid is 1:5-20, and then the prepared nanocellulose is dispersed in water, and prepared into a uniform suspension under ultrasonic conditions, and the obtained suspension is first mechanically stirred for 1-3 hours, Then further disperse in an ultrasonic cell pulverizer for 30 minutes, the intensity of the ultrasonic wave is 500-1200W, wherein 100-500 parts by weight of deionized water is dispersed with respect to 1 part by weight of the prepared nanocellulose, thereby making Suspension with a mass percentage of 0.2-1%;
2)将聚乙烯醇(PVA)颗粒加步骤1)所得到的均匀悬浊液,使悬浊液中聚乙烯醇的质量百分比浓度为5-20%,然后在超声波细胞粉碎机下继续分散2小时,配制成悬浊液A;2) Add polyvinyl alcohol (PVA) particles to the homogeneous suspension obtained in step 1), so that the mass percentage concentration of polyvinyl alcohol in the suspension is 5-20%, and then continue to disperse under the ultrasonic cell pulverizer for 2 Hours, prepared into a suspension A;
3)将聚乙烯吡咯烷酮(PVP)粉末加入步骤1)所得到的均匀悬浊液,使悬浊液中聚乙烯吡咯烷酮的质量百分比浓度为5-40%,在磁力搅拌器下或超声细胞粉碎机下继续分散2小时,配制成悬浊液B;3) Add polyvinylpyrrolidone (PVP) powder to the homogeneous suspension obtained in step 1), so that the mass percentage concentration of polyvinylpyrrolidone in the suspension is 5-40%, under a magnetic stirrer or an ultrasonic cell pulverizer Continue to disperse for 2 hours, and prepare suspension B;
4)将步骤2)、3)中得到的悬浊液A和B按照体积比为5:1至1:1的比例混合得到前驱体溶液,加入占前驱体溶液体积为1%的质量浓度为10%的硫酸在微波下退火处理即可得到具有NCC/PVA/PVP共混碳海绵,其中所述微波退火处理是在600W微波下反应5min,然后再将微波调至900W继续反应10min。4) Mix the suspensions A and B obtained in steps 2) and 3) according to the volume ratio of 5:1 to 1:1 to obtain a precursor solution, and add a mass concentration of 1% of the volume of the precursor solution to The NCC/PVA/PVP blended carbon sponge can be obtained by annealing 10% sulfuric acid under microwave, wherein the microwave annealing is to react under 600W microwave for 5 minutes, and then adjust the microwave to 900W to continue the reaction for 10 minutes.
优选地,步骤1)中所述硫酸的质量百分比浓度为50-60%,进一步优选为58-60%,更进一步优选为58%;反应温度为40-60℃,进一步优选为50-60℃,更进一步优选为50℃;反应时间为30-50min,进一步优选为35-40min,更进一步优选为35min;MCC与硫酸的质量百分比为1:8-15,进一步优选为1:10-15,更进一步优选为1:10。Preferably, the mass percent concentration of sulfuric acid described in step 1) is 50-60%, more preferably 58-60%, even more preferably 58%; the reaction temperature is 40-60°C, more preferably 50-60°C , more preferably 50°C; the reaction time is 30-50min, more preferably 35-40min, even more preferably 35min; the mass percentage of MCC and sulfuric acid is 1:8-15, more preferably 1:10-15, More preferably, it is 1:10.
优选地,步骤1)中相对于1重量份的制得的纳米纤维素,优选用150-300重量份,进一步优选为200-250重量份,更进一步优选为200重量份的去离子水分散,从而制成质量百分比为0.33-0.66%,进一步优选为0.4-0.5%,更进一步优选为0.5%的悬浊液。Preferably, relative to 1 part by weight of the prepared nanocellulose in step 1), it is preferably dispersed with 150-300 parts by weight, more preferably 200-250 parts by weight, and even more preferably 200 parts by weight of deionized water, Thus, a suspension with a mass percentage of 0.33-0.66%, more preferably 0.4-0.5%, and even more preferably 0.5% is prepared.
优选地,步骤1)中所述超声波分散中的超声波的强度为700-1000W,进一步优选为800-1000W,更进一步优选为800W。Preferably, the intensity of the ultrasonic waves in the ultrasonic dispersion in step 1) is 700-1000W, more preferably 800-1000W, even more preferably 800W.
优选地,步骤2)中所述PVA颗粒为重均分子量为17-22万且醇解度约为88%的PVA颗粒,进一步优选为PVA17-88。将所述PVA颗粒加入1)所得到的均匀悬浊液中,使悬浊液中聚乙烯醇的质量百分比浓度为7-15%,进一步优选为8-10%,更进一步优选为8%。Preferably, the PVA particles in step 2) are PVA particles with a weight average molecular weight of 170,000-220,000 and an alcoholysis degree of about 88%, more preferably PVA17-88. Add the PVA particles into the homogeneous suspension obtained in 1), so that the mass percent concentration of polyvinyl alcohol in the suspension is 7-15%, more preferably 8-10%, and even more preferably 8%.
优选地,步骤3)中所述PVP粉末为重均分子量为1-7万的PVP粉末,优选为PVP粉末K-30,将所述PVP粉末加入步骤1)所得到的均匀悬浊液中,使悬浊液中的聚乙烯吡咯烷酮的质量百分比浓度为10-25%;进一步优选为20-25%,更进一步优选为20%。Preferably, the PVP powder described in step 3) is a PVP powder with a weight average molecular weight of 10,000 to 70,000, preferably PVP powder K-30, and the PVP powder is added to the homogeneous suspension obtained in step 1), The mass percent concentration of the polyvinylpyrrolidone in the suspension is 10-25%; more preferably 20-25%, even more preferably 20%.
优选地,步骤4)中所述步骤2)、3)中得到的悬浊液A和B的混合体积比为3:1至2:1,进一步优选为7-5:3,更进一步优选为7:3。Preferably, the mixing volume ratio of suspensions A and B obtained in steps 2) and 3) in step 4) is 3:1 to 2:1, more preferably 7-5:3, even more preferably 7:3.
根据本发明的所述制备方法,其包括如下步骤:According to the preparation method of the present invention, it comprises the following steps:
1)取配制好的质量百分比浓度为58%硫酸50mL置于圆底烧瓶中,加入5g MCC在50℃条件下反应35min,反应完成后把反应产物转移到烧杯中用去离子水稀释至800mL静置4h,然后在3000转条件下离心30min,透析24h,-50℃条件下真空冷冻36h得到的1g的NCC,超声波条件下将得到的NCC加入200mL去离子水中配制成悬浊液,所得悬浊液再经机械搅拌2小时,然后再在800W的超声细胞粉碎机中进一步分散30分钟,最终得到0.5%的均匀悬浊液;1) Take 50mL of sulfuric acid with a concentration of 58% prepared in a round bottom flask, add 5g of MCC and react for 35min at 50°C. After the reaction is completed, transfer the reaction product to a beaker and dilute to 800mL with deionized water. Place for 4 hours, then centrifuge at 3000 rpm for 30 minutes, dialyze for 24 hours, vacuum freeze 1 g of NCC obtained at -50°C for 36 hours, and add 200 mL of deionized water to prepare a suspension under ultrasonic conditions. The solution was mechanically stirred for 2 hours, and then further dispersed in an 800W ultrasonic cell pulverizer for 30 minutes to finally obtain a 0.5% uniform suspension;
2)将35g PVA颗粒(PVA17-88,分子量为17-22万,醇解度约为88%)加入300mL步骤1)所得到的均匀悬浊液中在超声波条件下配制成悬浊液中聚乙烯醇的质量百分比浓度为8%的PVA悬浊液;2) Add 35g of PVA granules (PVA17-88, molecular weight 170,000-220,000, degree of alcoholysis about 88%) to 300mL of the homogeneous suspension obtained in step 1), and prepare a suspension in the suspension under ultrasonic conditions. The mass percent concentration of vinyl alcohol is 8% PVA suspension;
3)将5g PVP粉末(PVP粉末K-30,分子量1-7万)加入到20mL步骤1)所得到的均匀悬浊液中在超声波条件下配制成悬浊液中的聚乙烯吡咯烷酮的质量百分比浓度为20%的PVP悬浊液;3) Add 5g of PVP powder (PVP powder K-30, molecular weight 1-70,000) to 20mL of the homogeneous suspension obtained in step 1), and prepare the mass percentage of polyvinylpyrrolidone in the suspension under ultrasonic conditions 20% PVP suspension;
4)前驱体溶液制备4) Preparation of precursor solution
将步骤2)所得到的PVA悬浊液和步骤3)所得到的PVP悬浊液按体积比7:3的比例混合搅拌均匀后,加入占混合溶液体积1%的质量百分比浓度为10%的硫酸得到前驱体溶液;After mixing and stirring the PVA suspension obtained in step 2) and the PVP suspension obtained in step 3) in a ratio of 7:3 by volume, add 1% of the volume of the mixed solution with a mass percentage concentration of 10%. Sulfuric acid obtains precursor solution;
5)微波退火5) Microwave annealing
将步骤4)中得到的前驱体溶液在600W微波下反应5min,使前驱体溶液中NCC、PVA和PVP反应,然后再将微波调至900W继续反应10min,使前驱体退火碳化得到能够高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵。React the precursor solution obtained in step 4) under 600W microwave for 5 minutes to react NCC, PVA and PVP in the precursor solution, and then adjust the microwave to 900W to continue the reaction for 10 minutes to anneal and carbonize the precursor to obtain an efficient removal of water NCC/PVA/PVP blended carbon sponge with medium heavy metal ions and organic dyes.
根据本发明的所述制备方法中不采用任何交联剂。No crosslinking agent is used in the preparation method according to the present invention.
根据本发明的另一个方面,提供了一种能够高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵,所述共混碳海绵通过上述根据本发明的制备方法制备,其对Cr6+的吸附达到了9.3948mg/g以上。According to another aspect of the present invention, a kind of NCC/PVA/PVP blended carbon sponge capable of efficiently removing heavy metal ions and organic dyes in water is provided, and the blended carbon sponge is prepared by the above-mentioned preparation method according to the present invention, which The adsorption of Cr 6+ reached above 9.3948mg/g.
有益效果Beneficial effect
1、根据本发明的NCC/PVA/PVP共混碳海绵的制备方法中,PVA和PVP都是简单易得的高聚物,而且碳海绵环保可降解;NCC/PVA/PVP三者共混就可得到高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵;1. According to the preparation method of NCC/PVA/PVP blended carbon sponge of the present invention, PVA and PVP are all simple and easy-to-get high polymers, and the carbon sponge is environmentally friendly and degradable; the blending of NCC/PVA/PVP is just NCC/PVA/PVP blended carbon sponge that can efficiently remove heavy metal ions and organic dyes in water can be obtained;
2、根据本发明的方法制备的高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵具有稳定的形态,在吸附水体中重金属离子和有机染料后可回收利用,不对水体形成二次污染;2. The NCC/PVA/PVP blended carbon sponge prepared according to the method of the present invention to efficiently remove heavy metal ions and organic dyes in water has a stable shape, and can be recycled after absorbing heavy metal ions and organic dyes in water. Secondary pollution;
3、根据本发明的方法制备的NCC/PVA/PVP共混碳海绵傅里叶红外图谱显示产物在波数1500cm-1之前没有峰出现,说明NCC/PVA/PVP共混碳海绵具有高纯度的碳骨架,微波退火得到的产物纯度很高;3, according to the NCC/PVA/PVP blended carbon sponge Fourier transform infrared spectra that prepares according to the method of the present invention shows that product does not have peak to appear before wave number 1500cm -1 , illustrates that NCC/PVA/PVP blended carbon sponge has the carbon of high purity Skeleton, the purity of the product obtained by microwave annealing is very high;
4、根据本发明的方法制备出的NCC/PVA/PVP共混碳海绵对重金属离子和有机溶剂的去除率更高;4. The NCC/PVA/PVP blended carbon sponge prepared according to the method of the present invention has a higher removal rate of heavy metal ions and organic solvents;
6、根据本发明方法制备的NCC/PVA/PVP共混碳海绵,原料来源广泛,价格便宜,降低产品的生产成本,利于工业化推广使用。6. The NCC/PVA/PVP blended carbon sponge prepared by the method of the present invention has a wide range of raw material sources and low price, which reduces the production cost of the product and is conducive to industrialization and popularization.
附图说明Description of drawings
图1为根据本发明的NCC/PVA/PVP共混碳海绵制备工艺流程图。Fig. 1 is a flow chart of the preparation process of NCC/PVA/PVP blended carbon sponge according to the present invention.
图2为根据实施例1制备的NCC/PVA/PVP共混碳海绵及反应物NCC、PVA和PVP的傅里叶红外图谱图。Fig. 2 is the Fourier transform infrared spectrogram of the NCC/PVA/PVP blended carbon sponge prepared according to Example 1 and the reactants NCC, PVA and PVP.
图3为根据实验实施例1的NCC/PVA/PVP共混碳海绵对重铬酸钾吸附过程的紫外分光光度谱图。Fig. 3 is the ultraviolet spectrophotometric spectrum diagram of the NCC/PVA/PVP blended carbon sponge to potassium dichromate adsorption process according to Experimental Example 1.
图4为根据实验实施例1的NCC/PVA/PVP共混碳海绵对重铬酸钾吸附前后的浓度变化。Fig. 4 is the concentration change before and after adsorption of potassium dichromate by the NCC/PVA/PVP blended carbon sponge according to Experimental Example 1.
图5为根据实验实施例2的NCC/PVA/PVP共混碳海绵对铅离子吸附前后的浓度变化。Fig. 5 shows the concentration change of the NCC/PVA/PVP blended carbon sponge before and after adsorption of lead ions according to Experimental Example 2.
图6为根据实验实施例3的NCC/PVA/PVP共混碳海绵对汞离子吸附前后的浓度变化。Fig. 6 shows the concentration change of the NCC/PVA/PVP blended carbon sponge before and after adsorption of mercury ions according to Experimental Example 3.
图7为根据实验实施例4的NCC/PVA/PVP共混碳海绵对亚甲基蓝吸附过程的紫外分光光度谱图。Fig. 7 is an ultraviolet spectrophotometric spectrum diagram of the methylene blue adsorption process of the NCC/PVA/PVP blended carbon sponge according to Experimental Example 4.
图8为根据实验实施例4的NCC/PVA/PVP共混碳海绵对亚甲基蓝吸附前后的浓度变化。Fig. 8 is the concentration change of the NCC/PVA/PVP blended carbon sponge before and after the adsorption of methylene blue according to Experimental Example 4.
图9为根据实施例1、2和3得到的产物的孔隙率对比图。Fig. 9 is a comparison chart of porosity of products obtained according to Examples 1, 2 and 3.
图10为根据实施例1、2和3得到的产物对重金属离子和有机染料去除率对比图。Figure 10 is a comparison chart of the removal rates of heavy metal ions and organic dyes obtained according to Examples 1, 2 and 3.
具体实施方式detailed description
在根据本发明的制备方法中以高聚物PVA和PVP以及MCC制备而来的NCC,先有MCC以硫酸法制备NCC,然后再将NCC分散到水中在超声的作用下配制成均匀统一的悬浊液,然后以NCC悬浊液为溶剂分别配制PVA和PVP溶液,将PVA溶液和PVP溶液按照一定的比例在酸性条件下混合成前驱体溶液,在微波下反应生成碳海绵,此过程无需任何复杂实验设备,不添加任何交联剂,组分内部通过自组装形成稳定的网络结构后微波退化碳化就形成了高孔隙率的碳海绵,绿色无污染,工艺简洁,操作方便,得率较高,是一种高效快捷环境友好的制备高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵的制备方法。According to the preparation method of the present invention, the NCC prepared from high polymer PVA, PVP and MCC firstly has MCC to prepare NCC with sulfuric acid method, and then disperses NCC into water and prepares a uniform and uniform suspension under the action of ultrasound. Then use NCC suspension as solvent to prepare PVA and PVP solutions respectively, mix PVA solution and PVP solution according to a certain ratio under acidic conditions to form a precursor solution, and react under microwave to form carbon sponge. This process does not require any Complex experimental equipment without adding any cross-linking agent, the internal components form a stable network structure through self-assembly, and then microwave degeneration carbonization forms a high-porosity carbon sponge, green and pollution-free, simple process, convenient operation, and high yield , is an efficient, quick and environmentally friendly preparation method for preparing NCC/PVA/PVP blended carbon sponges that can efficiently remove heavy metal ions and organic dyes in water.
根据本发明的制备方法中,所述PVA颗粒为分子量为17-22万且醇解度约为88%的PVA颗粒,优选为PVA17-88。当PVA的分子量过高时,PVA的价格越高,成本上升,且由于容易固化而不易配制成悬浊液;而当PVA的分子量过低时,虽然价格可能便宜,但由于分子链过短,不能与PVP和NCC构建具有强效吸附作用的三维网络结构。因此根据本发明的制备方法中所述PVA颗粒的分子量优选为17-22万。According to the preparation method of the present invention, the PVA particles are PVA particles with a molecular weight of 170,000-220,000 and an alcoholysis degree of about 88%, preferably PVA17-88. When the molecular weight of PVA is too high, the price of PVA is higher, the cost rises, and it is difficult to prepare a suspension because it is easy to solidify; and when the molecular weight of PVA is too low, although the price may be cheap, but because the molecular chain is too short, A three-dimensional network structure with strong adsorption cannot be constructed with PVP and NCC. Therefore, the molecular weight of the PVA particles according to the preparation method of the present invention is preferably 170,000-220,000.
根据本发明的制备方法中,所述PVP粉末可以是K-30PVP粉末,其重均分子量约为1-7万,较为合适,同时PVP K-30已获得国家医药管理部门的批准正式上市,环保无污染。In the preparation method according to the present invention, the PVP powder can be K-30PVP powder, and its weight average molecular weight is about 10,000-70,000, which is more suitable. No pollution.
在根据本发明的制备方法制备的高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵,PVA和PVP都是简单易得聚合物是的生产成本大大降低,而且由于PVA和PVP本身就是长分子链结构,对于构建碳海绵中网状结构有利,进而提升了碳海绵的吸附性能。In the NCC/PVA/PVP blended carbon sponge of heavy metal ions and organic dyes in the efficient removal of water prepared by the preparation method of the present invention, PVA and PVP are all simple and easy to obtain polymers, so the production cost is greatly reduced, and because PVA and PVP itself has a long molecular chain structure, which is beneficial to the construction of the network structure in the carbon sponge, thereby improving the adsorption performance of the carbon sponge.
以下,将详细地描述本发明。在进行描述之前,应当理解的是,在本说明书和所附的权利要求书中使用的术语不应解释为限制于一般含义和字典含义,而应当在允许发明人适当定义术语以进行最佳解释的原则的基础上,根据与本发明的技术方面相应的含义和概念进行解释。因此,这里提出的描述仅仅是出于举例说明目的的优选实例,并非意图限制本发明的范围,从而应当理解的是,在不偏离本发明的精神和范围的情况下,可以由其获得其他等价方式或改进方式。Hereinafter, the present invention will be described in detail. Before proceeding with the description, it should be understood that the terms used in this specification and appended claims should not be construed as limited to ordinary and dictionary meanings, but should be best interpreted while allowing the inventor to properly define the terms On the basis of the principles of the present invention, explanations are made based on meanings and concepts corresponding to the technical aspects of the present invention. Accordingly, the descriptions set forth herein are preferred examples for illustrative purposes only and are not intended to limit the scope of the invention, so that it should be understood that other, etc. price or improvement.
实施例1Example 1
1)取配制好的质量百分比浓度为58%硫酸50mL置于圆底烧瓶中,加入5g MCC在50℃条件下反应35min,反应完成后把反应产物转移到烧杯中用去离子水稀释至800mL静置4h,然后在3000转条件下离心30min,透析24h,-50℃条件下真空冷冻36h得到的1g的NCC,超声波条件下将得到的NCC加入200mL去离子水中配制成悬浊液,所得悬浊液再经机械搅拌2小时,然后再在800W的超声细胞粉碎机中进一步分散30分钟,最终得到0.5%的均匀悬浊液;可以按照文献(Shan Liu,Yan-Jun Liu,Fu Deng,Ming-Guo Ma and Jing Bian,RSCAdv.,2015,5,74198–74205)记载的方法进行。1) Take 50mL of sulfuric acid with a concentration of 58% prepared in a round bottom flask, add 5g of MCC and react for 35min at 50°C. After the reaction is completed, transfer the reaction product to a beaker and dilute to 800mL with deionized water. Place for 4 hours, then centrifuge at 3000 rpm for 30 minutes, dialyze for 24 hours, vacuum freeze 1 g of NCC obtained at -50°C for 36 hours, and add 200 mL of deionized water to prepare a suspension under ultrasonic conditions. The solution was mechanically stirred for 2 hours, and then further dispersed in an 800W ultrasonic cell pulverizer for 30 minutes to finally obtain a 0.5% uniform suspension; according to the literature (Shan Liu, Yan-Jun Liu, Fu Deng, Ming- Guo Ma and Jing Bian, RSCAdv., 2015, 5, 74198-74205).
2)将35g PVA颗粒(PVA17-88,分子量为17-22万,醇解度约为88%)加入300mL步骤1)所得到的均匀悬浊液中在超声波条件下配制成悬浊液中聚乙烯醇的质量百分比浓度为8%的PVA悬浊液;2) Add 35g of PVA granules (PVA17-88, molecular weight 170,000-220,000, degree of alcoholysis about 88%) to 300mL of the homogeneous suspension obtained in step 1), and prepare a suspension in the suspension under ultrasonic conditions. The mass percent concentration of vinyl alcohol is 8% PVA suspension;
3)将5g PVP粉末(PVP粉末K-30,分子量1-7万)加入到20mL步骤1)所得到的均匀悬浊液中在超声波条件下配制成悬浊液中的聚乙烯吡咯烷酮的质量百分比浓度为20%的PVP悬浊液;3) Add 5g of PVP powder (PVP powder K-30, molecular weight 1-70,000) to 20mL of the homogeneous suspension obtained in step 1), and prepare the mass percentage of polyvinylpyrrolidone in the suspension under ultrasonic conditions 20% PVP suspension;
4)前驱体溶液制备4) Preparation of precursor solution
将步骤2)所得到的PVA悬浊液和步骤3)所得到的PVP悬浊液按体积比7:3的比例混合搅拌均匀后,加入占混合溶液体积1%的质量百分比浓度为10%的硫酸得到前驱体溶液;After mixing and stirring the PVA suspension obtained in step 2) and the PVP suspension obtained in step 3) in a ratio of 7:3 by volume, add 1% of the volume of the mixed solution with a mass percentage concentration of 10%. Sulfuric acid obtains precursor solution;
5)微波退火5) Microwave annealing
将前驱体溶液在600W微波下反应5min,使前驱体溶液中NCC、PVA和PVP反应,使前驱体溶液变得粘稠,然后再将微波调至900W继续反应10min,使前驱体退火碳化得到高效去除水体中重金属离子和有机染料的NCC/PVA/PVP共混碳海绵。React the precursor solution under 600W microwave for 5 minutes to make NCC, PVA and PVP in the precursor solution react to make the precursor solution viscous. NCC/PVA/PVP blended carbon sponge for removing heavy metal ions and organic dyes in water.
采用傅里叶红外谱图对NCC、PVA、PVP以及反应后的NCC/PVA/PVP共混碳海绵的结构变化进行分析,如图2所示。在傅里叶红外光谱图中4000-1500cm-1碳海绵没有吸收峰出现,说明经过退火之后前驱体溶液基本只剩下了多孔状的碳骨架。The structural changes of NCC, PVA, PVP and the NCC/PVA/PVP blended carbon sponge after the reaction were analyzed by Fourier transform infrared spectroscopy, as shown in Figure 2. There is no absorption peak in the 4000-1500cm -1 carbon sponge in the Fourier transform infrared spectrum, indicating that after annealing, only the porous carbon skeleton remains in the precursor solution.
实验实施例1:重金属铬的吸附Experimental example 1: Adsorption of heavy metal chromium
采用紫外吸收分光光度计对实施例1中制备的NCC/PVA/PVP共混碳海绵对重金属离子的吸附性能进行研究。用分析天平准确秤取500mg重铬酸钾溶于500mL去离子水中,配制成含有六价铬离子浓度为372ppm(mg/L)的溶液待用。用量筒量取40mL重铬酸钾溶液于烧杯中,加入1g实施例1中所制备的碳海绵,转移到温度设定为30℃的摇床中,每隔3min用紫外吸收分光光度计(Techcomp UV2310)测量一次。图3为根据Cr6+吸附过程的紫外分光光度谱图,图中曲线自上而下依次为未吸附(0min)时、3min、6min、9min、12min、15min、18min、21min、24min、27min、30min和40min吸附时的紫外吸收曲线,从结果可以看出随着时间延长,吸光度降低,这意味着水体中的重铬酸根离子逐渐减少,当吸附40分钟时吸光度变化不大,说明水体中的重铬酸根离子基本已去除干净。图4为根据实施例1制备的NCC/PVA/PVP共混碳海绵对重铬酸钾吸附前后浓度变化,如图4所示,吸附前Cr6+浓度为372ppm,吸附后浓度为0.012ppm,去除率达到了99.99%,吸附之后的水体中重金属铬的含量为0.012ppm,几乎达到了一类饮用水的标准(GB7467-87)。The adsorption performance of the NCC/PVA/PVP blended carbon sponge prepared in Example 1 on heavy metal ions was studied by using an ultraviolet absorption spectrophotometer. Accurately weigh 500 mg of potassium dichromate with an analytical balance and dissolve it in 500 mL of deionized water to prepare a solution containing hexavalent chromium ions at a concentration of 372 ppm (mg/L) for use. Measure 40mL of potassium dichromate solution in a beaker with a graduated cylinder, add 1g of the carbon sponge prepared in Example 1, transfer to a shaker whose temperature is set at 30°C, and use a UV absorption spectrophotometer (Techcomp UV2310) measurement once. Figure 3 is the UV spectrophotometric spectrum according to the Cr 6+ adsorption process. The curves in the figure are from top to bottom when not adsorbed (0min), 3min, 6min, 9min, 12min, 15min, 18min, 21min, 24min, 27min, The ultraviolet absorption curves of 30min and 40min adsorption, it can be seen from the results that as time goes on, the absorbance decreases, which means that the dichromate ion in the water gradually decreases, and the absorbance does not change much when adsorbed for 40 minutes. The dichromate ions have been basically removed. Fig. 4 is the NCC/PVA/PVP blended carbon sponge prepared according to embodiment 1 concentration change before and after potassium dichromate adsorption, as shown in Fig. 4, Cr before adsorption Concentration is 372ppm , after adsorption concentration is 0.012ppm, The removal rate reaches 99.99%, and the content of heavy metal chromium in the water body after adsorption is 0.012ppm, almost reaching the standard of class I drinking water (GB7467-87).
实验实施例2:重金属铅的吸附Experimental Example 2: Adsorption of heavy metal lead
采用紫外吸收分光光度计对实施例1中制备的NCC/PVA/PVP共混碳海绵对重金属离子的吸附性能进行研究。用分析天平准确秤取170mg醋酸铅溶于500mL去离子水中,配制成含有二价铅离子浓度为128ppm(mg/L)的溶液待用。用量筒量取40mL醋酸铅溶液于烧杯中,加入1g实施例1中所制备的碳海绵,转移到温度设定为30℃的摇床中,每隔3min用紫外吸收分光光度计(Techcomp UV2310)测量一次。结果如图5所示,吸附前Pb2+浓度为128ppm,吸附后Pb2+浓度为0.015ppm,去除率达到了99.98%,吸附之后水体中的重金属铅的含量优于国家标准(实验原子吸收分光光度法(螯合萃取法)GB7475-87或双硫腙分光光度法GB7470-87)。The adsorption performance of the NCC/PVA/PVP blended carbon sponge prepared in Example 1 on heavy metal ions was studied by using an ultraviolet absorption spectrophotometer. Accurately weigh 170 mg of lead acetate with an analytical balance and dissolve it in 500 mL of deionized water to prepare a solution containing divalent lead ions at a concentration of 128 ppm (mg/L) for use. Measure 40mL of lead acetate solution in a beaker with a graduated cylinder, add 1g of the carbon sponge prepared in Example 1, transfer to a shaker with a temperature setting of 30°C, and measure it with an ultraviolet absorption spectrophotometer (Techcomp UV2310) every 3min once. Result as shown in Figure 5, before adsorption, Pb 2+ concentration is 128ppm, and after adsorption, Pb 2+ concentration is 0.015ppm, and removal rate has reached 99.98%. After adsorption, the content of heavy metal lead in water is better than national standard (experimental atomic absorption Spectrophotometry (chelation extraction method) GB7475-87 or dithizone spectrophotometry GB7470-87).
实验实施例3:重金属汞的吸附Experimental Example 3: Adsorption of Heavy Metal Mercury
采用紫外吸收分光光度计对实施例1中制备的NCC/PVA/PVP共混碳海绵对重金属离子的吸附性能进行研究。用分析天平准确秤取180mg氯化汞溶于500mL去离子水中,配制成含有二价汞离子浓度为76ppm(mg/L)的溶液待用。用量筒量取40mL氯化汞溶液于烧杯中,加入1g实施例1中所制备的碳海绵,转移到温度设定为30℃的摇床中,每隔3min用紫外吸收分光光度计(Techcomp UV2310)测量一次。结果如图6所示,吸附前Hg2+浓度为76ppm,吸附之后的浓度为0.3ppm,去除率达到了99.6%。The adsorption performance of the NCC/PVA/PVP blended carbon sponge prepared in Example 1 on heavy metal ions was studied by using an ultraviolet absorption spectrophotometer. Accurately weigh 180 mg of mercuric chloride with an analytical balance and dissolve it in 500 mL of deionized water to prepare a solution containing divalent mercury ions at a concentration of 76 ppm (mg/L) for use. Measure 40mL of mercuric chloride solution in a beaker with a graduated cylinder, add 1g of the carbon sponge prepared in Example 1, transfer to a shaker whose temperature is set at 30°C, and use a UV absorption spectrophotometer (Techcomp UV2310 ) is measured once. The results are shown in Figure 6, the concentration of Hg 2+ before adsorption was 76ppm, the concentration after adsorption was 0.3ppm, and the removal rate reached 99.6%.
实验实施例4:有机染料的吸附Experimental Example 4: Adsorption of Organic Dyes
采用紫外吸收分光光度计对实施例1中制备的NCC/PVA/PVP共混碳海绵对有机染料的吸附性能进行研究。用分析天平准确秤取6.4mg亚甲基蓝溶于500mL去离子水中,配制成含有亚甲基蓝浓度为12.8ppm(mg/L)的溶液待用。用量筒量取40mL亚甲基蓝溶液于烧杯中,加入1g实施例1中所制备的碳海绵,转移到温度设定为30℃的摇床中,每隔3min用紫外吸收分光光度计(Techcomp UV2310)测量一次。图7为根据亚甲基蓝吸附过程的紫外分光光度谱图,图中曲线自上而下依次为未吸附(0min)时、3min、6min、9min、12min、15min、18min、21min、24min、27min、30min和40min吸附时的紫外吸收曲线,从结果可以看出随着时间延长,吸光度降低,这意味着水体中的亚甲基蓝逐渐减少,当吸附40分钟时吸光度变化不大,说明水体中的亚甲基蓝基本已去除干净。图8为根据实施例1制备的NCC/PVA/PVP共混碳海绵对亚甲基蓝吸附前后浓度变化,如图8所示,吸附前浓度为12.8ppm,吸附后浓度为0.02ppm,去除率达到了99.84%。The adsorption performance of the NCC/PVA/PVP blended carbon sponge prepared in Example 1 on organic dyes was studied by means of an ultraviolet absorption spectrophotometer. Use an analytical balance to accurately weigh 6.4 mg of methylene blue and dissolve it in 500 mL of deionized water to prepare a solution containing methylene blue at a concentration of 12.8 ppm (mg/L) for use. Measure 40mL of methylene blue solution in a beaker with a graduated cylinder, add 1g of the carbon sponge prepared in Example 1, transfer to a shaker with a temperature set at 30°C, and measure with a UV absorption spectrophotometer (Techcomp UV2310) every 3min once. Fig. 7 is the ultraviolet spectrophotometric spectrum diagram according to the methylene blue adsorption process, and the curves in the figure are sequentially from top to bottom when not adsorbed (0min), 3min, 6min, 9min, 12min, 15min, 18min, 21min, 24min, 27min, 30min and The UV absorption curve during 40 minutes of adsorption shows that the absorbance decreases with time, which means that the methylene blue in the water gradually decreases, and the absorbance does not change much after 40 minutes of adsorption, indicating that the methylene blue in the water has basically been removed. . Figure 8 is the concentration change of the NCC/PVA/PVP blended carbon sponge prepared according to Example 1 before and after the adsorption of methylene blue, as shown in Figure 8, the concentration before adsorption is 12.8ppm, the concentration after adsorption is 0.02ppm, and the removal rate reaches 99.84 %.
实施例2Example 2
1)取配制好的质量百分比浓度为58%硫酸50mL置于圆底烧瓶中,加入5g MCC在50℃条件下反应35min,反应完成后把反应产物转移到烧杯中用去离子水稀释至800mL静置4h,然后在3000转条件下离心30min,透析24h,-50℃条件下真空冷冻36h得到的1g的NCC,超声波条件下将得到的NCC加入200mL去离子水中配制成悬浊液,所得悬浊液再经机械搅拌2小时,然后再在800W的超声细胞粉碎机中进一步分散30分钟,最终得到0.5%的均匀悬浊液;1) Take 50mL of sulfuric acid with a concentration of 58% prepared in a round bottom flask, add 5g of MCC and react for 35min at 50°C. After the reaction is completed, transfer the reaction product to a beaker and dilute to 800mL with deionized water. Place for 4 hours, then centrifuge at 3000 rpm for 30 minutes, dialyze for 24 hours, vacuum freeze 1 g of NCC obtained at -50°C for 36 hours, and add 200 mL of deionized water to prepare a suspension under ultrasonic conditions. The solution was mechanically stirred for 2 hours, and then further dispersed in an 800W ultrasonic cell pulverizer for 30 minutes to finally obtain a 0.5% uniform suspension;
2)将35g PVA颗粒(PVA17-88,分子量为17-22万,醇解度约为88%)加入300mL步骤1)所得到的均匀悬浊液中在超声波条件下配制成悬浊液中聚乙烯醇的质量百分比浓度为8%的PVA悬浊液;2) Add 35g of PVA granules (PVA17-88, molecular weight 170,000-220,000, degree of alcoholysis about 88%) to 300mL of the homogeneous suspension obtained in step 1), and prepare a suspension in the suspension under ultrasonic conditions. The mass percent concentration of vinyl alcohol is 8% PVA suspension;
3)将5g PVP粉末(PVP粉末K-30,分子量1-7万)加入到20mL步骤1)所得到的均匀悬浊液中在超声波条件下配制成悬浊液中的聚乙烯吡咯烷酮的质量百分比浓度为20%的PVP悬浊液;3) Add 5g of PVP powder (PVP powder K-30, molecular weight 1-70,000) to 20mL of the homogeneous suspension obtained in step 1), and prepare the mass percentage of polyvinylpyrrolidone in the suspension under ultrasonic conditions 20% PVP suspension;
4)前驱体溶液制备4) Preparation of precursor solution
将步骤2)所得到的PVA悬浊液和步骤3)所得到的PVP悬浊液按体积比7:3的比例混合搅拌均匀后,加入占混合溶液体积1%的质量百分比浓度为10%的硫酸得到前驱体溶液;After mixing and stirring the PVA suspension obtained in step 2) and the PVP suspension obtained in step 3) in a ratio of 7:3 by volume, add 1% of the volume of the mixed solution with a mass percentage concentration of 10%. Sulfuric acid obtains precursor solution;
5)管式炉煅烧碳化5) Calcination and carbonization in tube furnace
将前驱体溶液在氮气氛围中,800℃条件下管式炉中碳化3h,使前驱体溶液完全碳化,得到粉末状黑色颗粒。The precursor solution was carbonized in a tube furnace at 800° C. for 3 h in a nitrogen atmosphere to completely carbonize the precursor solution to obtain powdery black particles.
实施例2得到粉末状黑色颗粒,得到粉末原因是因为NCC/PVA/PVP之间没有预先反应构建互相交叉的网状结构,所以煅烧后不是海绵状。虽然得到粉末状颗粒对重金属离子和有机染料也具有一定的去除效果,但是去除率不如实施例1中碳海绵去除率高,根据孔隙率计算,孔隙率越高,去除率越高,且不易回收处理。Example 2 obtained powdery black particles, and the reason for obtaining the powder was that there was no pre-reaction between NCC/PVA/PVP to build an intersecting network structure, so it was not spongy after calcination. Although the obtained powdery particles also have a certain removal effect on heavy metal ions and organic dyes, the removal rate is not as high as that of the carbon sponge in Example 1. According to the porosity calculation, the higher the porosity, the higher the removal rate, and it is not easy to recycle. deal with.
实施例3Example 3
1)取配制好的质量百分比浓度为58%硫酸50mL置于圆底烧瓶中,加入5g MCC在50℃条件下反应35min,反应完成后把反应产物转移到烧杯中用去离子水稀释至800mL静置4h,然后在3000转条件下离心30min,透析24h,-50℃条件下真空冷冻36h得到的1g的NCC,超声波条件下将得到的NCC加入200mL去离子水中配制成悬浊液,所得悬浊液再经机械搅拌2小时,然后再在800W的超声细胞粉碎机中进一步分散30分钟,最终得到0.5%的均匀悬浊液;1) Take 50mL of sulfuric acid with a concentration of 58% prepared in a round bottom flask, add 5g of MCC and react for 35min at 50°C. After the reaction is completed, transfer the reaction product to a beaker and dilute to 800mL with deionized water. Place for 4 hours, then centrifuge at 3000 rpm for 30 minutes, dialyze for 24 hours, vacuum freeze 1 g of NCC obtained at -50°C for 36 hours, and add 200 mL of deionized water to prepare a suspension under ultrasonic conditions. The solution was mechanically stirred for 2 hours, and then further dispersed in an 800W ultrasonic cell pulverizer for 30 minutes to finally obtain a 0.5% uniform suspension;
2)将35g PVA颗粒(PVA17-88,分子量为17-22万,醇解度约为88%)加入300mL步骤1)所得到的均匀悬浊液中在超声波条件下配制成悬浊液中聚乙烯醇的质量百分比浓度为8%的PVA悬浊液;2) Add 35g of PVA granules (PVA17-88, molecular weight 170,000-220,000, degree of alcoholysis about 88%) to 300mL of the homogeneous suspension obtained in step 1), and prepare a suspension in the suspension under ultrasonic conditions. The mass percent concentration of vinyl alcohol is 8% PVA suspension;
3)将5g PVP粉末(PVP粉末K-30,分子量1-7万)加入到20mL步骤1)所得到的均匀悬浊液中在超声波条件下配制成悬浊液中的聚乙烯吡咯烷酮的质量百分比浓度为20%的PVP悬浊液;3) Add 5g of PVP powder (PVP powder K-30, molecular weight 1-70,000) to 20mL of the homogeneous suspension obtained in step 1), and prepare the mass percentage of polyvinylpyrrolidone in the suspension under ultrasonic conditions 20% PVP suspension;
4)前驱体溶液制备4) Preparation of precursor solution
将步骤2)所得到的PVA悬浊液和步骤3)所得到的PVP悬浊液按体积比7:3的比例混合搅拌均匀后,加入占混合溶液体积1%的质量百分比浓度为10%的硫酸得到前驱体溶液;After mixing and stirring the PVA suspension obtained in step 2) and the PVP suspension obtained in step 3) in a ratio of 7:3 by volume, add 1% of the volume of the mixed solution with a mass percentage concentration of 10%. Sulfuric acid obtains precursor solution;
5)微波反应5) Microwave reaction
将前驱体溶液在600W微波下反应5min,使前驱体溶液中NCC/PVA/PVP反应,前驱体溶液变为粘稠状;React the precursor solution under 600W microwave for 5 minutes to make the NCC/PVA/PVP in the precursor solution react, and the precursor solution becomes viscous;
6)管式炉煅烧碳化6) Calcination and carbonization in tube furnace
将5)所得到的粘稠状液体在氮气氛围中,800℃条件下管式炉中碳化3h,使其完全碳化,得到碳海绵。The viscous liquid obtained in 5) was carbonized in a tube furnace at 800° C. for 3 hours in a nitrogen atmosphere to make it completely carbonized to obtain a carbon sponge.
实施例3所得到的碳海绵虽然对重金属离子和有机染料也具有一定的去除效果,但是去除率不如实施例1中碳海绵去除率高,因为实施例3得到的碳海绵颗粒孔隙率不如实施例1碳海绵高,导致去除率降低,且脆性大易碎,也不易回收处理。Although the carbon sponge obtained in embodiment 3 also has a certain removal effect on heavy metal ions and organic dyes, the removal rate is not as high as that of the carbon sponge in embodiment 1, because the carbon sponge particle porosity obtained in embodiment 3 is not as good as that of embodiment 3. 1 The carbon sponge is high, resulting in a lower removal rate, and it is brittle and brittle, and it is not easy to recycle.
实验实施例5:氮吸附脱附测试Experimental example 5: Nitrogen adsorption and desorption test
利用常规氮吸附脱附曲线通过BJH孔径分布计算模型检测实施例1至3中制备的碳海绵或颗粒的孔径。图9为根据实施例1、2和3得到的产物的孔隙率对比图。从图中可以看出根据实施例1制备的碳海绵的孔隙率远高于根据实施例2和3制备的产物的孔隙率,前者是后者的约3至6倍,因此根据本发明的制备方法制备的碳海绵可有效去除重金属离子和有机染料等。The pore diameters of the carbon sponges or particles prepared in Examples 1 to 3 were detected through the BJH pore size distribution calculation model using conventional nitrogen adsorption-desorption curves. Fig. 9 is a comparison chart of porosity of products obtained according to Examples 1, 2 and 3. It can be seen from the figure that the porosity of the carbon sponge prepared according to Example 1 is much higher than that of the products prepared according to Examples 2 and 3, the former is about 3 to 6 times that of the latter, so the preparation according to the present invention The carbon sponge prepared by the method can effectively remove heavy metal ions and organic dyes.
实验实施例6:去除率对比实验Experimental Example 6: Comparative Experiment of Removal Rate
分别根据实验实施例1至4的方法测试根据实施例2和3得到的产物对重金属离子和有机染料率的对比。图10为根据实施例1、2和3得到的产物对重金属离子和有机染料去除率对比图。从图中可以看出根据本发明的实施例1的制备方法制备的碳海绵对重金属离子和有机染料的去除率均可以达到99%以上,甚至达到99.99%,远高于根据实施例2和3得到的产物的去除率。According to the methods of Experimental Examples 1 to 4, the products obtained according to Examples 2 and 3 were tested for comparison of heavy metal ion and organic dye rates. Figure 10 is a comparison chart of the removal rates of heavy metal ions and organic dyes obtained according to Examples 1, 2 and 3. It can be seen from the figure that the carbon sponge prepared according to the preparation method of Example 1 of the present invention can achieve more than 99% removal rate of heavy metal ions and organic dyes, even 99.99%, which is much higher than that according to Examples 2 and 3. The removal rate of the obtained product.
以上实施例仅是作为本发明的实施方案的例子列举,并不对本发明构成任何限制,本领域技术人员可以理解在不偏离本发明的实质和构思的范围内的修改均落入本发明的保护范围。Above embodiment is only enumerated as the example of embodiment of the present invention, does not constitute any restriction to the present invention, and those skilled in the art can understand that the modification in the scope of not departing from the spirit and design of the present invention all falls into the protection of the present invention. scope.
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