CN106215862A - A kind of preparation method and applications of iron oxyhydroxide/graphenoxide oxide composite material - Google Patents
A kind of preparation method and applications of iron oxyhydroxide/graphenoxide oxide composite material Download PDFInfo
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- 229910021519 iron(III) oxide-hydroxide Inorganic materials 0.000 title claims abstract description 45
- CUPCBVUMRUSXIU-UHFFFAOYSA-N [Fe].OOO Chemical compound [Fe].OOO CUPCBVUMRUSXIU-UHFFFAOYSA-N 0.000 title claims abstract description 35
- 239000002131 composite material Substances 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 66
- 229910021389 graphene Inorganic materials 0.000 claims abstract description 47
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 239000002351 wastewater Substances 0.000 claims abstract description 27
- 239000000725 suspension Substances 0.000 claims abstract description 25
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000001179 sorption measurement Methods 0.000 claims abstract description 14
- WXNZTHHGJRFXKQ-UHFFFAOYSA-N 4-chlorophenol Chemical compound OC1=CC=C(Cl)C=C1 WXNZTHHGJRFXKQ-UHFFFAOYSA-N 0.000 claims abstract description 13
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 7
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 5
- 238000006243 chemical reaction Methods 0.000 claims abstract description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 239000008367 deionised water Substances 0.000 claims description 15
- 229910021641 deionized water Inorganic materials 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 15
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 10
- 229910002804 graphite Inorganic materials 0.000 claims description 10
- 239000010439 graphite Substances 0.000 claims description 10
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 5
- 239000012286 potassium permanganate Substances 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 4
- 238000001514 detection method Methods 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 229910002588 FeOOH Inorganic materials 0.000 claims 5
- 239000006185 dispersion Substances 0.000 claims 2
- 238000001035 drying Methods 0.000 claims 2
- 239000007788 liquid Substances 0.000 claims 2
- 229940090668 parachlorophenol Drugs 0.000 claims 2
- 238000001914 filtration Methods 0.000 claims 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 claims 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims 1
- 238000006396 nitration reaction Methods 0.000 claims 1
- 238000003672 processing method Methods 0.000 claims 1
- 239000001117 sulphuric acid Substances 0.000 claims 1
- 235000011149 sulphuric acid Nutrition 0.000 claims 1
- IEECXTSVVFWGSE-UHFFFAOYSA-M iron(3+);oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Fe+3] IEECXTSVVFWGSE-UHFFFAOYSA-M 0.000 description 11
- 239000012528 membrane Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- VGVRPFIJEJYOFN-UHFFFAOYSA-N 2,3,4,6-tetrachlorophenol Chemical class OC1=C(Cl)C=C(Cl)C(Cl)=C1Cl VGVRPFIJEJYOFN-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000011259 mixed solution Substances 0.000 description 4
- 150000004045 organic chlorine compounds Chemical class 0.000 description 4
- 150000002989 phenols Chemical class 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 231100000331 toxic Toxicity 0.000 description 3
- 230000002588 toxic effect Effects 0.000 description 3
- -1 Chlorophenol aromatic compounds Chemical class 0.000 description 2
- 241000282414 Homo sapiens Species 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000003651 drinking water Substances 0.000 description 2
- 235000020188 drinking water Nutrition 0.000 description 2
- 231100000049 endocrine disruptor Toxicity 0.000 description 2
- 239000000598 endocrine disruptor Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000013067 intermediate product Substances 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 239000002086 nanomaterial Substances 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000001699 photocatalysis Effects 0.000 description 2
- 239000002352 surface water Substances 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- HFZWRUODUSTPEG-UHFFFAOYSA-N 2,4-dichlorophenol Chemical compound OC1=CC=C(Cl)C=C1Cl HFZWRUODUSTPEG-UHFFFAOYSA-N 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 229920001661 Chitosan Polymers 0.000 description 1
- 208000017701 Endocrine disease Diseases 0.000 description 1
- 239000012028 Fenton's reagent Substances 0.000 description 1
- 231100000570 acute poisoning Toxicity 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 1
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 231100000025 genetic toxicology Toxicity 0.000 description 1
- 230000001738 genotoxic effect Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- ACGUYXCXAPNIKK-UHFFFAOYSA-N hexachlorophene Chemical compound OC1=C(Cl)C=C(Cl)C(Cl)=C1CC1=C(O)C(Cl)=CC(Cl)=C1Cl ACGUYXCXAPNIKK-UHFFFAOYSA-N 0.000 description 1
- 229910001701 hydrotalcite Inorganic materials 0.000 description 1
- 229960001545 hydrotalcite Drugs 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000004005 microsphere Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000005180 public health Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 231100000901 systemic toxic effect Toxicity 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
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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
-
- 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
- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
-
- 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
-
- 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
- C02F2101/34—Organic compounds containing oxygen
- C02F2101/345—Phenols
-
- 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
- C02F2101/36—Organic compounds containing halogen
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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)
- Water Treatment By Sorption (AREA)
Abstract
本发明涉及一种羟基氧化铁/氧化石墨烯复合材料的制备方法及其应用。羟基氧化铁/氧化石墨烯复合材料是由氧化石墨烯的悬浊液和羟基氧化铁的悬浊液在按照体积比1:1~2混合、分散后通过水热法复合而成。将制得的羟基氧化铁/氧化石墨烯复合材料用于含酚废水的处理,取羟基氧化铁/氧化石墨烯复合吸附材料0.5~5g投入1000ml的含有对氯酚浓度为10~60mg/l的废水中,在恒温摇床上充分震荡,控制水温在25℃,反应3h后将废水过滤,检测对氯酚去除率为87~93.2%,出水氯酚浓度在1.3~5.2mg/l,吸附量为11~17.4mg/l。The invention relates to a preparation method and application of an iron oxyhydroxide/graphene oxide composite material. The iron oxyhydroxide/graphene oxide composite material is composed of a suspension of graphene oxide and a suspension of iron oxyhydroxide in a volume ratio of 1:1-2, mixed and dispersed, and compounded by a hydrothermal method. The obtained iron oxyhydroxide/graphene oxide composite material is used for the treatment of phenol-containing wastewater, and 0.5-5 g of the iron oxyhydroxide/graphene oxide composite adsorption material is put into 1000 ml of 10-60 mg/l p-chlorophenol In the wastewater, shake fully on a constant temperature shaker, control the water temperature at 25°C, and filter the wastewater after 3 hours of reaction. The removal rate of p-chlorophenol is detected to be 87-93.2%, the concentration of chlorophenol in the effluent is 1.3-5.2mg/l, and the adsorption capacity is 11~17.4mg/l.
Description
技术领域technical field
本发明涉及水污染控制技术领域,具体涉及一种羟基氧化铁/氧化石墨烯复合材料的制备方法及其在水处理中的应用。The invention relates to the technical field of water pollution control, in particular to a preparation method of an iron oxyhydroxide/graphene oxide composite material and its application in water treatment.
背景技术Background technique
随着化学工业的飞速发展,有机氯化合物在医药、农用品、纺织品、日用化学品及公共卫生等领域得到了广泛应用的同时也造成了严重的环境污染。许多有机氯化合物毒性大、难生物降解、半衰期长、具有“三致效应”和遗传毒性,这些有机氯化合物在环境中长期残留会对环境造成影响进而危害各种生物及人体的健康。With the rapid development of the chemical industry, organochlorine compounds have been widely used in the fields of medicine, agricultural supplies, textiles, daily chemicals, and public health, but they have also caused serious environmental pollution. Many organochlorine compounds are highly toxic, difficult to biodegrade, have a long half-life, have "three effects" and genotoxicity, and the long-term residue of these organochlorine compounds in the environment will affect the environment and endanger the health of various organisms and human beings.
氯酚类芳香族化合物是一类典型有机氯化合物,进入环境中后会对各种生物产生毒害作用,严重时会导致整个生态系统的破坏。同时近几年研究表明,大多数氯酚类化合物是内分泌干扰物或者是潜在的内分泌干扰物,当它们长期存在于生物体内时,会造成生物体的内分泌紊乱,能对各种生物及人体生殖系统造成毒害影响,即使在较低浓度也会对生物体造成危害。研究表明氯酚会对水生生物产生毒害作用。当淡水或海洋中的浓度达1~10μg/L时便会对水生生物产生急性毒害作用。Chlorophenol aromatic compounds are a type of typical organochlorine compounds, which can cause poisonous effects on various organisms after entering the environment, and even lead to the destruction of the entire ecosystem in severe cases. At the same time, studies in recent years have shown that most chlorophenol compounds are endocrine disruptors or potential endocrine disruptors. When they exist in organisms for a long time, they will cause endocrine disorders of organisms and can affect various organisms and human reproduction. Systemic toxic effects that can be harmful to organisms even at low concentrations. Studies have shown that chlorophenols can have toxic effects on aquatic organisms. When the concentration in fresh water or ocean reaches 1-10μg/L, it will cause acute poisoning to aquatic organisms.
环境中氯酚类物质主要来自环境中自然合成产生、含氯有机物的降解、加工或净化工艺中的副产品以及人工合成的含氯化合物。Chlorophenols in the environment mainly come from natural synthesis in the environment, degradation of chlorinated organic substances, by-products in processing or purification processes, and artificially synthesized chlorinated compounds.
目前我国对氯酚的控制主要控制在水污染控制领域。根据我国《地表水环境质量标准》(GB‐3838‐2002)的规定,地表水V类水体中挥发酚的最高允许浓度为0.1mg/L;我国《生活饮用水水质标准》(GB5749‐2006)中规定生活饮用水中挥发酚类浓度不超过0.002mg/L;我国《城市供水水质标准》(CJ/T206‐2005)规定氯酚总量(包括2一氯酚、2,4一二氯酚、2,4,6一三氯酚)不得超过0.01mg/L。At present, the control of p-chlorophenol in my country is mainly in the field of water pollution control. According to my country's "Surface Water Environmental Quality Standards" (GB-3838-2002), the maximum allowable concentration of volatile phenols in surface water V water bodies is 0.1mg/L; my country's "Drinking Water Quality Standards" (GB5749-2006) The concentration of volatile phenols in drinking water shall not exceed 0.002mg/L; my country's "Urban Water Supply Quality Standard" (CJ/T206-2005) stipulates that the total amount of chlorophenols (including 2-chlorophenol, 2,4-dichlorophenol , 2,4,6-trichlorophenol) shall not exceed 0.01mg/L.
目前常规控制氯酚类污染物方法有化学氧化法、光催化、膜分离法、生物降解法、吸附法等。化学氧化法采用强氧化剂如O3、Fenton试剂等进行氧化处理,处理含酚废水效果明显但是氧化剂成本高且技术设备要求高;光催化氧化法通过催化产生羟基自由基来氧化氯酚,此法虽然处理效果好且反应时间短,但在某些处理过程中可能会产生毒性更大的中间产物,使得化学法处理氯代酚难以得到广泛应用;膜分离法是通过合成膜过滤处理含酚废水,但是膜在长时间运行后易被堵塞,导致膜的通透量下降,膜组件要经常更换,导致运行成本高,这些问题使得膜分离技术在实际应用中有一定的局限性;生物法处理含酚废水虽然成本低、无二次污染,但是生物系统处理效率低,运行的稳定性差限制了生物法处理含酚废水的应用。吸附法处理含酚废水不会受到水量、冲击的影响,具有运行成本低、无中间产物生产、高效的优点,运用吸附法处理含酚废水能克服以上众多缺点。At present, conventional methods for controlling chlorophenol pollutants include chemical oxidation, photocatalysis, membrane separation, biodegradation, and adsorption. The chemical oxidation method uses strong oxidants such as O 3 , Fenton reagent, etc. for oxidation treatment. The treatment of phenol-containing wastewater has obvious effects, but the oxidant cost is high and the technical equipment requirements are high; the photocatalytic oxidation method oxidizes chlorophenols by catalyzing the generation of hydroxyl radicals. Although the treatment effect is good and the reaction time is short, more toxic intermediate products may be produced in some treatment processes, making it difficult for chemical treatment of chlorinated phenols to be widely used; membrane separation method is to treat phenol-containing wastewater through synthetic membrane filtration , but the membrane is easy to be blocked after long-term operation, resulting in a decrease in the permeability of the membrane, and frequent replacement of the membrane module, resulting in high operating costs. These problems make the membrane separation technology have certain limitations in practical application; biological treatment Although the cost of phenol-containing wastewater is low and there is no secondary pollution, the biological system has low treatment efficiency and poor operation stability, which limits the application of biological methods to treat phenol-containing wastewater. Adsorption treatment of phenol-containing wastewater will not be affected by water volume and impact, and has the advantages of low operating cost, no intermediate product production, and high efficiency. Using adsorption method to treat phenol-containing wastewater can overcome many of the above shortcomings.
目前吸附法处理氯酚的材料种类很多,如碳基质为主的活性炭、碳纤维等,有机物/高聚物为主的树脂、壳聚糖微球等以及以无机矿物基质为主的蒙脱石、水滑石等。At present, there are many kinds of materials for treating chlorophenol by adsorption method, such as activated carbon and carbon fiber based on carbon matrix, resins based on organic matter/polymer, chitosan microspheres, etc., and montmorillonite based on inorganic mineral matrix, Hydrotalcite etc.
本法提供一种由羟基氧化铁与氧化石墨烯复合材料来处理含酚废水的方法,氧化石墨烯是一种石墨烯衍生物,是一种新型的二维纳米材料,巨大的比表面积和大量的含氧官能团使其成为性能良好的吸附剂。二维的纳米材料在实际应用中容易发生不可逆的堆叠而发生聚团,本法通过羟基氧化铁对氧化石墨烯的进行改性,使其成为性能稳定的优良的水处理吸附剂,有效处理含酚废水。This method provides a method for treating phenol-containing wastewater by iron oxyhydroxide and graphene oxide composite materials. Graphene oxide is a graphene derivative and a new type of two-dimensional nanomaterial with a huge specific surface area and a large amount of The oxygen-containing functional groups make it a good adsorbent. Two-dimensional nanomaterials are prone to irreversible stacking and agglomeration in practical applications. This method modifies graphene oxide through iron oxyhydroxide to make it an excellent water treatment adsorbent with stable performance and effectively treat Phenol wastewater.
发明内容:Invention content:
本发明的目的是提供一种羟基氧化铁/氧化石墨烯复合材料的制备方法并将其应用于处理含酚废水。The purpose of the present invention is to provide a preparation method of iron oxyhydroxide/graphene oxide composite material and apply it to treat phenolic wastewater.
本发明采取的技术方案通过以下步骤实现:The technical scheme that the present invention takes is realized through the following steps:
一种羟基氧化铁/氧化石墨烯复合材料是由氧化石墨烯的悬浊液和羟基氧化铁的悬浊液在按照体积比1:1~2混合、分散后通过水热法复合而成。An iron oxyhydroxide/graphene oxide composite material is formed by mixing and dispersing graphene oxide suspension and iron oxyhydroxide suspension at a volume ratio of 1:1 to 2 and compounding them by a hydrothermal method.
一种羟基氧化铁/氧化石墨烯复合材料中的羟基氧化铁组分是利用水热法将Fe(NO3)3`2H2O与NaOH按照质量比0.5~1.2:1加入100ml去离子水中混合30min,在120~150℃的烘箱中保持24小时,离心干燥后制得。An iron oxyhydroxide component in an iron oxyhydroxide/graphene oxide composite material is obtained by adding Fe(NO 3 ) 3` 2H 2 O and NaOH into 100ml deionized water according to a mass ratio of 0.5-1.2:1 and mixing them by hydrothermal method 30min, kept in an oven at 120-150°C for 24 hours, centrifuged and dried.
一种羟基氧化铁/氧化石墨烯复合材料中的氧化石墨是石墨粉与高锰酸钾按照质量比1:1~3,加入浓硫酸与浓磷酸体积比为6~8:1的混酸,50℃水浴加热2h,制得。Graphite oxide in an iron oxyhydroxide/graphene oxide composite material is graphite powder and potassium permanganate according to the mass ratio of 1:1 to 3, adding concentrated sulfuric acid and concentrated phosphoric acid with a volume ratio of 6 to 8:1 mixed acid, 50 ℃ water bath heating 2h, the system.
一种羟基氧化铁/氧化石墨烯复合材料的复合步骤:A composite step of iron oxyhydroxide/graphene oxide composite material:
(1)取1g的氧化石墨固体,加入50ml去离子水,分散5~10min,即制得质量体积分数约为0.02g/ml的氧化石墨烯悬浊液;(1) Take 1 g of graphite oxide solid, add 50 ml of deionized water, and disperse for 5 to 10 minutes to obtain a graphene oxide suspension with a mass volume fraction of about 0.02 g/ml;
(2)将取0.5~1g的羟基氧化铁于50ml去离子水中,分散5min,即制得质量体积分数0.1~0.2g/ml羟基氧化铁的悬浊液;(2) Disperse 0.5-1 g of ferric oxyhydroxide in 50 ml of deionized water for 5 minutes to obtain a suspension with a mass volume fraction of 0.1-0.2 g/ml of ferric oxyhydroxide;
(3)将分散均匀的羟基氧化铁悬浊液加入到已经分散的氧化石墨烯悬浊液中,并将混合液分散5~10min,在120℃的烘箱中保持12~24h,离心干燥后即制得所述复合材料。(3) Add the uniformly dispersed ferric oxyhydroxide suspension to the dispersed graphene oxide suspension, and disperse the mixed solution for 5-10 minutes, keep it in an oven at 120°C for 12-24 hours, and centrifuge and dry it. The composite material is produced.
上述氧化石墨烯通过石墨烯上基团与羟基氧化铁基团间的静电力结合而形成羟基氧化铁/氧化石墨烯复合材料。The above-mentioned graphene oxide is combined by the electrostatic force between the group on the graphene and the iron oxyhydroxide group to form an iron oxyhydroxide/graphene oxide composite material.
将制得的羟基氧化铁/氧化石墨烯复合材料用于含酚废水的处理,具体步骤如下:取羟基氧化铁/氧化石墨烯复合吸附材料0.5~5g投入1000ml的含有对氯酚浓度为10~60mg/l的废水中,在恒温摇床上充分震荡,控制水温在25℃,反应3h后将废水过滤,检测对氯酚去除率为87~93.2%,出水氯酚浓度在1.3~5.2mg/l,吸附量为11~17.4mg/l。The obtained ferric oxyhydroxide/graphene oxide composite material is used for the treatment of phenol-containing wastewater, and the specific steps are as follows: Take 0.5-5 g of ferric oxyhydroxide/graphene oxide composite adsorption material and put it into 1000 ml of p-chlorophenol containing 10-5 g In the 60mg/l waste water, fully shake it on a constant temperature shaker, control the water temperature at 25°C, filter the waste water after 3 hours of reaction, and detect that the removal rate of p-chlorophenol is 87-93.2%, and the concentration of chlorophenol in the effluent is 1.3-5.2mg/l , the adsorption capacity is 11-17.4mg/l.
本发明制备的羟基氧化铁/氧化石墨烯复合材料具有如下优点:The iron oxyhydroxide/graphene oxide composite material prepared by the present invention has the following advantages:
1、本发明羟基氧化铁/氧化石墨烯复合材料中氧化石墨烯与羟基氧化铁的复合能有效避免氧化石墨烯的聚团,氧化石墨烯能有效的保持二维结构;1. The composite of graphene oxide and iron oxyhydroxide in the iron oxyhydroxide/graphene oxide composite material of the present invention can effectively avoid the agglomeration of graphene oxide, and graphene oxide can effectively maintain a two-dimensional structure;
2、本发明使用的氧化石墨烯是中度氧化的石墨烯,具有丰富的含氧基团和较大的比表面积,能高效吸附氯酚;2. The graphene oxide used in the present invention is moderately oxidized graphene, which has abundant oxygen-containing groups and a large specific surface area, and can efficiently adsorb chlorophenols;
3、羟基氧化铁/氧化石墨烯复合材料中羟基氧化铁作为基底,具有一定吸附和氧化作用,能吸附并氧化部分氯酚。3. The iron oxyhydroxide in the iron oxyhydroxide/graphene oxide composite material is used as the substrate, which has a certain adsorption and oxidation effect, and can absorb and oxidize part of chlorophenol.
具体实施方式detailed description
实施例1Example 1
石墨粉与高锰酸钾按照质量比1:1,加入硫酸与磷酸体积比为8:1的混酸,50℃水浴加热2h。将氧化后的石墨过滤、烘干、研磨成粉备用。Graphite powder and potassium permanganate are in a mass ratio of 1:1, add sulfuric acid and phosphoric acid with a volume ratio of 8:1 mixed acid, and heat in a water bath at 50°C for 2 hours. The oxidized graphite is filtered, dried and ground into powder for later use.
将氧化石墨质量与去离子水体积按1g:50ml,混合、分散5~10min制得0.02g/ml的氧化石墨烯的悬浊液。The mass of graphite oxide and the volume of deionized water are 1g:50ml, mixed and dispersed for 5-10min to prepare a 0.02g/ml graphene oxide suspension.
将Fe(NO3)3`2H2O与NaOH按照物质量比1.2:1加入100ml去离子水中混合30min,在150℃的烘箱中保持24小时制得。Fe(NO 3 ) 3` 2H 2 O and NaOH were added into 100ml deionized water according to the mass ratio of 1.2:1, mixed for 30 minutes, and kept in an oven at 150°C for 24 hours.
将制得羟基氧化铁质量与去离子水体积按照0.5g:50ml混合,分散5min制得0.1g/ml的羟基氧化铁悬浊液。将分散均匀的羟基氧化铁悬浊液加入到已经分散的氧化石墨烯悬浊液中,并将混合液分散5~10min,在120℃的烘箱中保持24h。Mix the obtained iron oxyhydroxide mass with deionized water volume according to 0.5g:50ml, and disperse for 5 minutes to prepare 0.1g/ml iron oxyhydroxide suspension. The uniformly dispersed iron oxyhydroxide suspension was added to the dispersed graphene oxide suspension, and the mixed solution was dispersed for 5-10 minutes, and kept in an oven at 120° C. for 24 hours.
将制得的羟基氧化铁/氧化石墨烯复合材料用于含酚废水的处理,具体步骤如下:取羟基氧化铁/氧化石墨烯复合吸附材料0.5g投入1000ml的含有对氯酚浓度为10mg/l的废水中,在恒温摇床上充分震荡,控制水温在25℃,反应3h后将废水过滤过滤,,出水氯酚浓度在1.3mg/l,吸附量为17.4mg/g。检测对氯酚去除率为87%The obtained ferric oxyhydroxide/graphene oxide composite material is used for the treatment of phenol-containing wastewater, and the specific steps are as follows: 0.5 g of ferric oxyhydroxide/graphene oxide composite adsorption material is dropped into 1000 ml containing p-chlorophenol with a concentration of 10 mg/l In the waste water, shake fully on a constant temperature shaker, control the water temperature at 25°C, and filter the waste water after reacting for 3 hours. The concentration of chlorophenol in the effluent is 1.3 mg/l, and the adsorption capacity is 17.4 mg/g. Detection of p-chlorophenol removal rate of 87%
实施例2Example 2
石墨粉与高锰酸钾按照质量比1:2,加入硫酸与磷酸体积比为7:1的混酸,50℃水浴加热2h。将氧化后的石墨过滤、烘干、研磨成粉备用。Graphite powder and potassium permanganate are in a mass ratio of 1:2, add sulfuric acid and phosphoric acid with a volume ratio of 7:1 mixed acid, and heat in a water bath at 50°C for 2 hours. The oxidized graphite is filtered, dried and ground into powder for later use.
将氧化石墨质量与去离子水体积按1g:50ml混合、分散5~10min制得0.02g/ml的氧化石墨烯的悬浊液。The mass of graphite oxide and the volume of deionized water were mixed according to 1g:50ml, and dispersed for 5-10min to prepare a 0.02g/ml graphene oxide suspension.
将Fe(NO3)3`2H2O与NaOH按照物质量比1:1加入100ml去离子水中混合30min,在120℃的烘箱中保持24小时制得。Fe(NO 3 ) 3` 2H 2 O and NaOH were added into 100ml deionized water according to the mass ratio of 1:1, mixed for 30 minutes, and kept in an oven at 120°C for 24 hours.
将制得羟基氧化铁质量与去离子水体积按照1g:50ml混合,分散5min制得0.2g/ml的羟基氧化铁悬浊液。将分散均匀的羟基氧化铁悬浊液加入到已经分散的氧化石墨烯悬浊液中,并将混合液分散5~10min,在120℃的烘箱中保持24h。The mass of the obtained iron oxyhydroxide and the volume of deionized water were mixed according to 1g:50ml, and dispersed for 5 minutes to prepare a 0.2g/ml iron oxyhydroxide suspension. The uniformly dispersed iron oxyhydroxide suspension was added to the dispersed graphene oxide suspension, and the mixed solution was dispersed for 5-10 minutes, and kept in an oven at 120° C. for 24 hours.
将制得的羟基氧化铁/氧化石墨烯复合材料用于含酚废水的处理,具体步骤如下:取羟基氧化铁/氧化石墨烯复合吸附材料3g投入1000ml的含有对氯酚浓度为50mg/l的废水中,在恒温摇床上充分震荡,控制水温在25℃,反应3h后将废水过滤过滤,,出水氯酚浓度在3.4mg/l,吸附量为15.5mg/g。检测对氯酚去除率为93.2%The obtained ferric oxyhydroxide/graphene oxide composite material is used for the treatment of phenol-containing wastewater, and the specific steps are as follows: get 3 g of ferric oxyhydroxide/graphene oxide composite adsorbent material and drop into 1000 ml of chlorophenol containing p-chlorophenol concentration of 50 mg/l In the wastewater, shake fully on a constant temperature shaker, control the water temperature at 25°C, and filter the wastewater after reacting for 3 hours. The concentration of chlorophenol in the effluent is 3.4mg/l, and the adsorption capacity is 15.5mg/g. Detection of p-chlorophenol removal rate of 93.2%
实施例3Example 3
石墨粉与高锰酸钾按照质量比1:3,加入硫酸与磷酸体积比为6:1的混酸,50℃水浴2h。将氧化后的石墨过滤、烘干、研磨成粉备用。Graphite powder and potassium permanganate are in a mass ratio of 1:3, add sulfuric acid and phosphoric acid with a volume ratio of 6:1 mixed acid, and bathe in water at 50°C for 2 hours. The oxidized graphite is filtered, dried and ground into powder for later use.
将氧化石墨质量与去离子水体积按1g:50ml,混合、分散5~10min制得0.02g/ml的氧化石墨烯的悬浊液。The mass of graphite oxide and the volume of deionized water are 1g:50ml, mixed and dispersed for 5-10min to prepare a 0.02g/ml graphene oxide suspension.
将Fe(NO3)3`2H2O与NaOH按照物质量比0.5:1加入100ml去离子水中混合30min,在120℃的烘箱中保持24小时制得。Fe(NO 3 ) 3` 2H 2 O and NaOH were added into 100ml deionized water according to the mass ratio of 0.5:1, mixed for 30 minutes, and kept in an oven at 120°C for 24 hours.
将制得羟基氧化铁质量与去离子水体积按照1g:50ml混合,分散5min制得0.2g/ml的羟基氧化铁悬浊液。将分散均匀的羟基氧化铁悬浊液加入到已经分散的氧化石墨烯悬浊液中,并将混合液分散5~10min,在120℃的烘箱中保持24h。The mass of the obtained iron oxyhydroxide and the volume of deionized water were mixed according to 1g:50ml, and dispersed for 5 minutes to prepare a 0.2g/ml iron oxyhydroxide suspension. The uniformly dispersed iron oxyhydroxide suspension was added to the dispersed graphene oxide suspension, and the mixed solution was dispersed for 5-10 minutes, and kept in an oven at 120° C. for 24 hours.
将制得的羟基氧化铁/氧化石墨烯复合材料用于含酚废水的处理,具体步骤如下:取羟基氧化铁/氧化石墨烯复合吸附材料5g投入1000ml的含有对氯酚浓度为60mg/l的废水中,在恒温摇床上充分震荡,控制水温在25℃,反应3h后将废水过滤过滤,,出水氯酚浓度在5.2mg/l,吸附量为11mg/g。检测对氯酚去除率为91.3%。The obtained ferric oxyhydroxide/graphene oxide composite material is used for the treatment of phenol-containing wastewater, and the specific steps are as follows: get 5 g of ferric oxyhydroxide/graphene oxide composite adsorbent material and drop into 1000 ml of 60 mg/l p-chlorophenol In the wastewater, shake fully on a constant temperature shaker, control the water temperature at 25°C, and filter the wastewater after reacting for 3 hours. The concentration of chlorophenol in the effluent is 5.2mg/l, and the adsorption capacity is 11mg/g. The removal rate of p-chlorophenol was detected to be 91.3%.
本发明公开和提出的一种羟基氧化铁/氧化石墨烯复合材料的制备方法及其在水处理中的应用,本领域技术人员可通过借鉴本文内容,适当改变条件路线等环节实现,尽管本发明的方法和制备技术已通过较佳实施例子进行了描述,相关技术人员明显能在不脱离本发明内容、精神和范围内对本文所述的方法和技术路线进行改动或重新组合,来实现最终的制备技术。特别需要指出的是,所有相类似的替换和改动对本领域技术人员来说是显而易见的,他们都被视为包括在本发明精神、范围和内容中。The preparation method of an iron oxyhydroxide/graphene oxide composite material disclosed and proposed by the present invention and its application in water treatment can be realized by those skilled in the art by referring to the content of this article and appropriately changing the conditions and routes. Although the present invention The methods and preparation techniques have been described through preferred implementation examples, and those skilled in the art can obviously modify or recombine the methods and technical routes described herein without departing from the content, spirit and scope of the present invention to achieve the final Preparation technology. In particular, it should be pointed out that all similar substitutions and modifications will be obvious to those skilled in the art, and they are all considered to be included in the spirit, scope and content of the present invention.
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| CN119524555A (en) * | 2024-11-20 | 2025-02-28 | 中国人民解放军火箭军工程大学 | A graphene-doped/iron oxyhydroxide pressed agent and its preparation method and application |
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