CN106179249A - A kind of preparation method of attapulgite cellulose composite adsorption microsphere - Google Patents
A kind of preparation method of attapulgite cellulose composite adsorption microsphere Download PDFInfo
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- 229920002678 cellulose Polymers 0.000 title claims abstract description 154
- 239000001913 cellulose Substances 0.000 title claims abstract description 154
- 229960000892 attapulgite Drugs 0.000 title claims abstract description 127
- 229910052625 palygorskite Inorganic materials 0.000 title claims abstract description 127
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 83
- 239000004005 microsphere Substances 0.000 title claims abstract description 58
- 239000002131 composite material Substances 0.000 title claims abstract description 48
- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 62
- 239000002608 ionic liquid Substances 0.000 claims abstract description 58
- 238000000034 method Methods 0.000 claims abstract description 7
- 235000010980 cellulose Nutrition 0.000 claims description 147
- 239000000243 solution Substances 0.000 claims description 68
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 49
- 238000003756 stirring Methods 0.000 claims description 41
- 239000003921 oil Substances 0.000 claims description 38
- 235000019198 oils Nutrition 0.000 claims description 38
- 239000008367 deionised water Substances 0.000 claims description 30
- 229910021641 deionized water Inorganic materials 0.000 claims description 30
- 239000004094 surface-active agent Substances 0.000 claims description 26
- 239000003795 chemical substances by application Substances 0.000 claims description 20
- 239000000843 powder Substances 0.000 claims description 20
- 239000006087 Silane Coupling Agent Substances 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 13
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- 239000000725 suspension Substances 0.000 claims description 9
- 239000011259 mixed solution Substances 0.000 claims description 8
- 229920000742 Cotton Polymers 0.000 claims description 6
- PRXRUNOAOLTIEF-ADSICKODSA-N Sorbitan trioleate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OC[C@@H](OC(=O)CCCCCCC\C=C/CCCCCCCC)[C@H]1OC[C@H](O)[C@H]1OC(=O)CCCCCCC\C=C/CCCCCCCC PRXRUNOAOLTIEF-ADSICKODSA-N 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 6
- 235000010482 polyoxyethylene sorbitan monooleate Nutrition 0.000 claims description 6
- 229920000053 polysorbate 80 Polymers 0.000 claims description 6
- FHDQNOXQSTVAIC-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;chloride Chemical compound [Cl-].CCCCN1C=C[N+](C)=C1 FHDQNOXQSTVAIC-UHFFFAOYSA-M 0.000 claims description 5
- 229920000168 Microcrystalline cellulose Polymers 0.000 claims description 5
- 235000019813 microcrystalline cellulose Nutrition 0.000 claims description 5
- 239000008108 microcrystalline cellulose Substances 0.000 claims description 5
- 229940016286 microcrystalline cellulose Drugs 0.000 claims description 5
- PBIDWHVVZCGMAR-UHFFFAOYSA-N 1-methyl-3-prop-2-enyl-2h-imidazole Chemical compound CN1CN(CC=C)C=C1 PBIDWHVVZCGMAR-UHFFFAOYSA-N 0.000 claims description 4
- 239000005662 Paraffin oil Substances 0.000 claims description 4
- 235000019483 Peanut oil Nutrition 0.000 claims description 4
- NKSJNEHGWDZZQF-UHFFFAOYSA-N ethenyl(trimethoxy)silane Chemical compound CO[Si](OC)(OC)C=C NKSJNEHGWDZZQF-UHFFFAOYSA-N 0.000 claims description 4
- PHQOGHDTIVQXHL-UHFFFAOYSA-N n'-(3-trimethoxysilylpropyl)ethane-1,2-diamine Chemical compound CO[Si](OC)(OC)CCCNCCN PHQOGHDTIVQXHL-UHFFFAOYSA-N 0.000 claims description 4
- 239000000312 peanut oil Substances 0.000 claims description 4
- HQYALQRYBUJWDH-UHFFFAOYSA-N trimethoxy(propyl)silane Chemical compound CCC[Si](OC)(OC)OC HQYALQRYBUJWDH-UHFFFAOYSA-N 0.000 claims description 4
- 235000010446 mineral oil Nutrition 0.000 claims description 3
- 239000002480 mineral oil Substances 0.000 claims description 3
- 238000002525 ultrasonication Methods 0.000 claims description 2
- 125000002572 propoxy group Chemical group [*]OC([H])([H])C(C([H])([H])[H])([H])[H] 0.000 claims 1
- 239000003344 environmental pollutant Substances 0.000 abstract description 14
- 231100000719 pollutant Toxicity 0.000 abstract description 14
- 239000003463 adsorbent Substances 0.000 abstract description 10
- 231100000252 nontoxic Toxicity 0.000 abstract description 7
- 230000003000 nontoxic effect Effects 0.000 abstract description 7
- 238000011084 recovery Methods 0.000 abstract description 7
- 238000003912 environmental pollution Methods 0.000 abstract description 5
- 230000004048 modification Effects 0.000 abstract description 2
- 238000012986 modification Methods 0.000 abstract description 2
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 21
- 239000002245 particle Substances 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- 238000000967 suction filtration Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000007822 coupling agent Substances 0.000 description 6
- 239000002957 persistent organic pollutant Substances 0.000 description 6
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 5
- 239000010865 sewage Substances 0.000 description 5
- 229910000077 silane Inorganic materials 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 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 3
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229960000907 methylthioninium chloride Drugs 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 230000002195 synergetic effect Effects 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 description 2
- 230000002860 competitive effect Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000000975 dye Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- STZCRXQWRGQSJD-GEEYTBSJSA-M methyl orange Chemical compound [Na+].C1=CC(N(C)C)=CC=C1\N=N\C1=CC=C(S([O-])(=O)=O)C=C1 STZCRXQWRGQSJD-GEEYTBSJSA-M 0.000 description 2
- 229940012189 methyl orange Drugs 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
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- 238000011069 regeneration method Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000003403 water pollutant Substances 0.000 description 2
- WWVMHGUBIOZASN-UHFFFAOYSA-N 1-methyl-3-prop-2-enylimidazol-1-ium Chemical compound CN1C=C[N+](CC=C)=C1 WWVMHGUBIOZASN-UHFFFAOYSA-N 0.000 description 1
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- 241001464837 Viridiplantae Species 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 150000001555 benzenes Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- WLZRMCYVCSSEQC-UHFFFAOYSA-N cadmium(2+) Chemical compound [Cd+2] WLZRMCYVCSSEQC-UHFFFAOYSA-N 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 229960004337 hydroquinone Drugs 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- -1 lead ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000004627 regenerated cellulose Substances 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing 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
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
-
- 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
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
- B01J20/28021—Hollow particles, e.g. hollow spheres, microspheres or cenospheres
-
- 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
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
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- Chemical & Material Sciences (AREA)
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- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Water Treatment By Sorption (AREA)
Abstract
本发明公开了一种凹凸棒纤维素复合吸附微球的制备方法,该方法包括以下三个步骤:凹凸棒的预处理及表面改性;离子液体纤维素溶液制备;凹凸棒纤维素复合吸附微球的制备。制备过程简单方便,使用的离子液体溶剂安全无毒,制备的凹凸棒纤维素微球多孔,分散性、生物相容性和热稳定性好,对水中污染物具有吸附能力强、吸附容量大、去除效率高、性质稳定,易于回收等优点;解决了凹凸棒吸附能力差、回收难,纤维素吸附剂机械强度弱、热稳定性低等问题,同时原料来源广泛,价格低廉,不产生二次污染,充分利用纤维素、凹凸棒再生资源,实用价值高,可用于水中污染物的深度处理,解决了能源危机和环境污染问题。The invention discloses a preparation method of attapulgite cellulose composite adsorption microspheres. The method comprises the following three steps: pretreatment and surface modification of attapulgite; preparation of ionic liquid cellulose solution; attapulgite cellulose composite adsorption microspheres. Preparation of balls. The preparation process is simple and convenient, the ionic liquid solvent used is safe and non-toxic, the prepared attapulgite cellulose microspheres are porous, have good dispersibility, biocompatibility and thermal stability, and have strong adsorption capacity for pollutants in water, large adsorption capacity, It has the advantages of high removal efficiency, stable properties, and easy recovery; it solves the problems of poor adsorption capacity of attapulgite, difficult recovery, weak mechanical strength of cellulose adsorbent, and low thermal stability. Pollution, making full use of cellulose and attapulgite renewable resources, high practical value, can be used for advanced treatment of pollutants in water, and solves the problems of energy crisis and environmental pollution.
Description
技术领域:Technical field:
本发明涉及污水处理领域,具体涉及一种凹凸棒纤维素复合吸附微球的制备方法。The invention relates to the field of sewage treatment, in particular to a preparation method of attapulgite cellulose composite adsorption microspheres.
背景技术:Background technique:
随着现代社会的高速发展,工业废水和生活污水等引起的环境污染使生态环境遭到严重破坏。如何经济、高效地治理污水中污染物,己成为环保和化学工业迫在眉睫的任务之一。With the rapid development of modern society, environmental pollution caused by industrial wastewater and domestic sewage has seriously damaged the ecological environment. How to treat pollutants in sewage economically and efficiently has become one of the urgent tasks of environmental protection and chemical industry.
凹凸棒具有独特的层链状晶体结构和纳米级的纤维状晶体形态,内孔道发达,比表面积较大,这些赋予了凹凸棒较强的吸附性能和离子交换性能。其对废水中的重金属离子和水中的有机污染物,如苯类化合物、酚类化合物、原油及石油产品等具有很强的吸附作用。另外凹凸棒本身无毒、无害、自然界中储存量高、成本低廉,在水处理过程中工艺操作简便、吸附效率高、无污染性且二次污染少等优点,使凹凸棒在工业污水和生活污水的处理表现出优异的应用潜能。然而凹凸棒作为一种天然粘土,当凹凸棒应用于废水中时,水和有机污染物在凹凸棒表面竞争吸附时,水分子被优先吸附,占据凹凸棒孔道表面的活性位点,使得其对有机污染物去除率低,限制了其在吸附领域的应用。此外由于其表面能高,使得凹凸棒极易聚集成团,聚集后的凹凸棒比表面积有所减小,从而限制了其吸附能力,且它的粉末状形态在使用后的回收问题上也存在一定的难度。The attapulgite has a unique layer chain crystal structure and nano-scale fibrous crystal form, developed internal pores and large specific surface area, which endow the attapulgite with strong adsorption performance and ion exchange performance. It has a strong adsorption effect on heavy metal ions in wastewater and organic pollutants in water, such as benzene compounds, phenol compounds, crude oil and petroleum products. In addition, the attapulgite itself is non-toxic, harmless, with high storage capacity in nature and low cost. It has the advantages of simple process operation, high adsorption efficiency, no pollution and less secondary pollution in the water treatment process, so that the attapulgite can be used in industrial sewage and The treatment of domestic sewage shows excellent application potential. However, attapulgite is a kind of natural clay. When attapulgite is used in wastewater, when water and organic pollutants compete for adsorption on the surface of attapulgite, water molecules are preferentially adsorbed, occupying active sites on the surface of attapulgite pores, making it The low removal rate of organic pollutants limits its application in the field of adsorption. In addition, due to its high surface energy, the attapulgite is easy to aggregate into agglomerates, and the specific surface area of the aggregated attapulgite is reduced, thereby limiting its adsorption capacity, and its powder form also has problems in recycling after use. A certain degree of difficulty.
纤维素是自然界蕴含最丰富的可再生资源,是一种天然的多糖分子,无毒,可生物降解,抗水性强,具有高度的亲水性、良好生物相容性、合适的多孔结构、极低的非特异性吸附性能,其大分子链上含有众多氨基和羟基,对金属离子、极性有机化合物具有吸附、絮凝作用,是一种良好的吸附剂基质材料。用纤维素制备的吸附剂广泛用于各种金属离子的富集分离、蛋白质的分离纯化以及废水中染料的脱除等;但由于天然纤维素分子间强烈的氢键作用,形成非常致密的结构,造成纤维素材料加工的困难,且纤维素吸附剂存在机械强度弱、热稳定性低等问题。Cellulose is the most abundant renewable resource in nature. It is a natural polysaccharide molecule, non-toxic, biodegradable, strong water resistance, highly hydrophilic, good biocompatibility, suitable porous structure, extremely Low non-specific adsorption performance. Its macromolecular chain contains many amino groups and hydroxyl groups. It has adsorption and flocculation effects on metal ions and polar organic compounds. It is a good adsorbent matrix material. Adsorbents prepared from cellulose are widely used in the enrichment and separation of various metal ions, the separation and purification of proteins, and the removal of dyes in wastewater; however, due to the strong hydrogen bonding between natural cellulose molecules, a very dense structure is formed , resulting in difficulties in the processing of cellulose materials, and the cellulose adsorbent has problems such as weak mechanical strength and low thermal stability.
发明内容:Invention content:
本发明的目的是提供一种凹凸棒纤维素复合吸附微球的制备方法,制备过程简单方便,使用的离子液体溶剂安全无毒,制备的凹凸棒纤维素微球多孔,分散性、生物相容性和热稳定性好,对水中污染物具有吸附能力强、吸附容量大、去除效率高、性质稳定,易于回收等优点;解决了凹凸棒吸附能力差、回收难,纤维素吸附剂机械强度弱、热稳定性低等问题,同时原料来源广泛,价格低廉,不产生二次污染,充分利用纤维素、凹凸棒再生资源,实用价值高,可用于水中污染物的深度处理,解决了能源危机和环境污染问题。The purpose of the present invention is to provide a preparation method of attapulgite cellulose composite adsorption microspheres, the preparation process is simple and convenient, the ionic liquid solvent used is safe and non-toxic, and the prepared attapulgite cellulose microspheres are porous, dispersible and biocompatible Good thermal stability, strong adsorption capacity, large adsorption capacity, high removal efficiency, stable properties, and easy recovery of pollutants in water; it solves the problem of poor adsorption capacity of attapulgite, difficult recovery, and weak mechanical strength of cellulose adsorbent , low thermal stability, etc. At the same time, there are wide sources of raw materials, low prices, no secondary pollution, full use of cellulose and attapulgite regeneration resources, high practical value, and can be used for advanced treatment of water pollutants, solving the energy crisis and Environmental Pollution.
本发明是通过以下技术方案予以实现的:The present invention is achieved through the following technical solutions:
一种凹凸棒纤维素复合吸附微球的制备方法,该方法包括以下三个步骤:A preparation method of attapulgite cellulose composite adsorption microspheres, the method comprising the following three steps:
a、凹凸棒的预处理及表面改性:粉体凹凸棒用质量分数为5-10%的稀盐酸浸泡8-12h后洗涤至中性,分散到乙醇和水体积比为9:1的混合溶液中,加入硅烷偶联剂,在40-50℃下超声50min后吸附,吸附产物经分离纯化后110℃下干燥得到硅烷改性凹凸棒土,研磨备用;所述粉体凹凸棒与硅烷偶联剂的质量比为4∶1~6∶1;a. Pretreatment and surface modification of attapulgite: the powder attapulgite is soaked in dilute hydrochloric acid with a mass fraction of 5-10% for 8-12 hours, washed to neutrality, and dispersed into a mixture of ethanol and water with a volume ratio of 9:1 Add a silane coupling agent to the solution, and then adsorb after ultrasonication at 40-50°C for 50 minutes. After separation and purification, the adsorbed product is dried at 110°C to obtain silane-modified attapulgite, which is ground for later use; the powder attapulgite and silane coupling The mass ratio of the joint agent is 4:1~6:1;
b、离子液体纤维素溶液的制备:在100重量份的离子液体中加入2~6重量份的纤维素,90~110℃搅拌混合至纤维素完全溶解,得到离子液体纤维素溶液;b. Preparation of ionic liquid cellulose solution: add 2 to 6 parts by weight of cellulose to 100 parts by weight of ionic liquid, stir and mix at 90 to 110° C. until the cellulose is completely dissolved, and obtain an ionic liquid cellulose solution;
c、凹凸棒纤维素复合吸附微球的制备:步骤b得到的离子液体纤维素溶液中加入步骤a中得到的硅烷改性凹凸棒土,硅烷改性凹凸棒土质量为离子液体纤维素溶液质量的0.2-0.4倍,90~100℃,80~200rpm转速下搅拌20~30分钟后,加入油相和表面活性剂,油相与离子液体纤维素溶液的体积比4∶1~6∶1,表面活性剂与油相的质量比为1∶40~1∶100,搅拌15~20分钟,形成反相悬浮体系,通过程序降温至30~50℃,加入固化剂,固化剂的体积为离子液体纤维素溶液体积的2~3倍,保持搅拌20分钟,形成凹凸棒纤维素复合吸附微球;用去离子水洗涤并浸泡,湿态筛分,得到凹凸棒纤维素复合吸附微球。c. Preparation of attapulgite cellulose composite adsorption microspheres: add the silane-modified attapulgite obtained in step a to the ionic liquid cellulose solution obtained in step b, and the mass of the silane-modified attapulgite is the mass of the ionic liquid cellulose solution 0.2-0.4 times of 0.2-0.4 times, 90-100 ℃, 80-200rpm rotating speed, after stirring for 20-30 minutes, add oil phase and surfactant, the volume ratio of oil phase and ionic liquid cellulose solution is 4:1-6:1, The mass ratio of the surfactant to the oil phase is 1:40-1:100, stirred for 15-20 minutes to form a reverse-phase suspension system, cooled to 30-50°C through a program, and a curing agent is added, the volume of which is ionic liquid 2 to 3 times the volume of the cellulose solution, and keep stirring for 20 minutes to form attapulgite cellulose composite adsorption microspheres; wash with deionized water, soak, and sieve in a wet state to obtain attapulgite cellulose composite adsorption microspheres.
所述程序降温是指每10min降温5℃的速率。The temperature programming refers to the rate of cooling by 5°C every 10 minutes.
所述凹凸棒纤维素复合吸附微球的制备方法,具体包括以下步骤:The preparation method of the attapulgite cellulose composite adsorption microspheres specifically comprises the following steps:
a、凹凸棒经挤压、剪切、粉碎得到粒度为200目的粉体,用质量分数为5-10%的稀盐酸浸泡8-12h再用去离子水洗涤沉淀至中性后分散到乙醇和水体积比为9:1的混合溶液中,搅拌中加入硅烷偶联剂,在40-50℃下超声50min,50℃搅拌吸附4h,吸附产物经抽滤分离后依次用甲苯、无水乙醇和去离子水洗涤去除多余的硅烷偶联剂,于110℃下干燥,得到硅烷改性凹凸棒土,研磨备用;所述粉体凹凸棒与硅烷偶联剂的质量比为4∶1~6∶1;a. The attapulgite is extruded, sheared, and pulverized to obtain a powder with a particle size of 200 mesh, soaked in dilute hydrochloric acid with a mass fraction of 5-10% for 8-12 hours, washed with deionized water and precipitated to neutral, and dispersed in ethanol and In a mixed solution with a water volume ratio of 9:1, add a silane coupling agent during stirring, ultrasonicate at 40-50°C for 50 minutes, stir and adsorb at 50°C for 4 hours, and the adsorbed product is separated by suction filtration and then washed with toluene, absolute ethanol and Washing with deionized water to remove excess silane coupling agent, drying at 110°C to obtain silane-modified attapulgite, which is ground for later use; the mass ratio of the powder attapulgite to the silane coupling agent is 4:1 to 6: 1;
b、离子液体纤维素溶液的制备:在100重量份的离子液体中加入2~6重量份的纤维素,90~110℃搅拌混合至纤维素完全溶解,搅拌转速为80~200rpm,得到离子液体纤维素溶液;b. Preparation of ionic liquid cellulose solution: add 2 to 6 parts by weight of cellulose to 100 parts by weight of ionic liquid, stir and mix at 90 to 110 ° C until the cellulose is completely dissolved, and the stirring speed is 80 to 200 rpm to obtain an ionic liquid Cellulose solution;
c、凹凸棒纤维素复合吸附微球的制备:步骤b得到的离子液体纤维素溶液中加入步骤a中得到的硅烷改性凹凸棒土,硅烷改性凹凸棒土质量为离子液体纤维素溶液质量的0.2-0.4倍,90~100℃,80~200rpm转速下搅拌20~30分钟后,加入油相和表面活性剂,油相与离子液体纤维素溶液的体积比4∶1~6∶1,表面活性剂与油相的质量比为1∶40~1∶100,在300~500rpm转速下搅拌15~20分钟,形成反相悬浮体系,以每10min降温5℃的速率降温至30~50℃,纤维素溶液凝结成球;加入固化剂,固化剂的体积为离子液体纤维素溶液体积的2~3倍;5分钟后转速降为200rpm,保持搅拌20分钟,纤维素溶液迅速固化,形成凹凸棒纤维素复合吸附微球,待降至室温,将凹凸棒纤维素复合吸附微球从反应液中过滤出来,用去离子水洗涤,然后将微球浸泡在去离子水中48小时;湿态筛分,得到凹凸棒纤维素复合吸附微球。c. Preparation of attapulgite cellulose composite adsorption microspheres: add the silane-modified attapulgite obtained in step a to the ionic liquid cellulose solution obtained in step b, and the mass of the silane-modified attapulgite is the mass of the ionic liquid cellulose solution 0.2-0.4 times of 0.2-0.4 times, 90-100 ℃, 80-200rpm rotating speed, after stirring for 20-30 minutes, add oil phase and surfactant, the volume ratio of oil phase and ionic liquid cellulose solution is 4:1-6:1, The mass ratio of surfactant to oil phase is 1:40~1:100, stir at 300~500rpm for 15~20 minutes to form a reverse phase suspension system, and cool down to 30~50℃ at a rate of 5℃ every 10min , the cellulose solution coagulates into a ball; add a curing agent, the volume of the curing agent is 2 to 3 times the volume of the ionic liquid cellulose solution; after 5 minutes, the speed is reduced to 200rpm, keep stirring for 20 minutes, the cellulose solution solidifies rapidly, forming unevenness Rod cellulose composite adsorption microspheres, after cooling down to room temperature, filter the attapulgite rod cellulose composite adsorption microspheres from the reaction solution, wash with deionized water, and then soak the microspheres in deionized water for 48 hours; wet sieve The attapulgite cellulose composite adsorption microspheres were obtained.
步骤a中,所述的硅烷偶联剂选自γ-(2,3-环氧丙氧基)丙基三甲氧基硅烷、N-2(氨乙基)3-氨丙基三甲氧基硅烷、乙烯基三甲氧基硅烷中的一种。In step a, the silane coupling agent is selected from γ-(2,3-glycidoxy)propyltrimethoxysilane, N-2 (aminoethyl) 3-aminopropyltrimethoxysilane , One of vinyltrimethoxysilane.
步骤a中,粒度为200目的粉体凹凸棒用质量分数为5-10%的稀盐酸浸泡8-12h后,凹凸棒石得到活化呈蓬松的类似溶胶形态,洗涤至中性后经硅烷偶联剂进行表面改性处理,凹凸棒表面由完全亲水性变为适度亲油性,增强在有机溶剂中的分散性,减少了凹凸棒的团聚现象,利于有机污染物在凹凸棒表面竞争吸附。In step a, after the attapulgite powder with a particle size of 200 mesh is soaked in dilute hydrochloric acid with a mass fraction of 5-10% for 8-12 hours, the attapulgite is activated into a fluffy sol-like form, washed to neutrality and then coupled with silane The attapulgite surface is modified from completely hydrophilic to moderately lipophilic, which enhances the dispersion in organic solvents, reduces the agglomeration of the attapulgite, and facilitates the competitive adsorption of organic pollutants on the attapulgite surface.
步骤b中,所述的离子液体为1-丁基-3-甲基咪唑氯盐或1-烯丙基-3-甲基咪唑醋酸盐;所述的纤维素选自纸浆、脱脂棉、精制棉或微晶纤维素中的一种。In step b, the ionic liquid is 1-butyl-3-methylimidazolium chloride or 1-allyl-3-methylimidazolium acetate; the cellulose is selected from pulp, absorbent cotton, refined One of cotton or microcrystalline cellulose.
天然纤维素具有结晶度高、分子间和分子内部含有大量氢键的结构特点,使其难溶于水和常见的有机溶剂。离子液体是一种新型纤维素的绿色溶剂,能有效地破坏纤维素晶体结构,降低其结晶度,不仅可以有效溶解纤维素,还可以为纤维素提供良好的反应环境。Natural cellulose has the structural characteristics of high crystallinity and a large number of hydrogen bonds between molecules and inside molecules, making it difficult to dissolve in water and common organic solvents. Ionic liquid is a new type of green solvent for cellulose, which can effectively destroy the crystal structure of cellulose and reduce its crystallinity. It can not only effectively dissolve cellulose, but also provide a good reaction environment for cellulose.
步骤c中,所述的表面活性剂为吐温80、Span 85或其混合物;所述的油相为泵油、矿物油、石蜡油或花生油;所述的固化剂为水、乙醇、丙酮或其混合物。In step c, the surfactant is Tween 80, Span 85 or a mixture thereof; the oil phase is pump oil, mineral oil, paraffin oil or peanut oil; the curing agent is water, ethanol, acetone or its mixture.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
(1)本发明利用离子溶液作为溶剂直接溶解纤维素,工艺简单、无毒、对环境污染小,且可以重新回收利用。(1) The present invention uses an ion solution as a solvent to directly dissolve cellulose, and the process is simple, non-toxic, less polluting to the environment, and can be recycled again.
(2)通过硅烷偶联剂对凹凸棒进行表面改性,使凹凸棒表面极性降低,表面性质由完全亲水性变为适度亲油性,增强在有机溶剂中的分散性,减少了凹凸棒的团聚现象,利于有机污染物在凹凸棒表面竞争吸附。(2) The surface of the attapulgite is modified by a silane coupling agent, so that the surface polarity of the attapulgite is reduced, the surface property is changed from completely hydrophilic to moderately lipophilic, the dispersion in organic solvents is enhanced, and the attapulgite is reduced. The agglomeration phenomenon is conducive to the competitive adsorption of organic pollutants on the surface of the attapulgite.
(3)本发明将改性凹凸棒与离子液体溶解的纤维素两种吸附材料耦合,产生协同效应,增强了凹凸棒与有机纤维素分子间的相容性,提高了分子界面的结合力,促进了纤维素微球成形,有效提高吸附性能;此外凹凸棒组分内嵌入再生纤维素的网状结构,有效提高了微球的机械强度和热稳定性;同时,纤维素为凹凸棒提供良好的载体作用,进一步避免凹凸棒聚集,有利于凹凸棒吸附剂的回收。(3) The present invention couples two adsorption materials of modified attapulgite and ionic liquid-dissolved cellulose to produce a synergistic effect, enhance the compatibility between attapulgite and organic cellulose molecules, and improve the binding force of the molecular interface, It promotes the formation of cellulose microspheres and effectively improves the adsorption performance; in addition, the network structure of regenerated cellulose embedded in the attapulgite components effectively improves the mechanical strength and thermal stability of the microspheres; at the same time, the cellulose provides good support for the attapulgite The carrier function of the attapulgite further avoids the aggregation of the attapulgite, which is beneficial to the recovery of the attapulgite adsorbent.
(4)凹凸棒无毒、无害、储存量高、成本低廉;纤维素广泛存在于绿色植物中,是自然界最丰富的可再生资源,充分利用凹凸棒土、纤维素不仅符合“绿色化学”的要求,还可以解决环境污染带来的影响。通过纤维素与凹凸棒土等基质材料进行配伍,形成兼具多孔结构和较强污染物吸附能力的吸附材料,使得到的吸附剂具有吸附能力强、吸附容量大、去除效率高的优点,性质稳定,易于回收再利用。(4) Attapulgite is non-toxic, harmless, with high storage capacity and low cost; cellulose widely exists in green plants and is the most abundant renewable resource in nature. Making full use of attapulgite and cellulose is not only in line with "green chemistry" It can also solve the impact of environmental pollution. Through the compatibility of cellulose and attapulgite and other matrix materials, an adsorption material with both porous structure and strong pollutant adsorption capacity is formed, so that the obtained adsorbent has the advantages of strong adsorption capacity, large adsorption capacity, and high removal efficiency. Stable and easy to recycle and reuse.
总之,本发明制备过程简单方便,使用的离子液体溶剂安全无毒,将改性凹凸棒与离子液体溶解的纤维素两种吸附材料耦合,产生协同效应,制备的凹凸棒纤维素微球多孔,分散性、生物相容性和热稳定性好,对水中污染物具有吸附能力强、吸附容量大、去除效率高、性质稳定,易于回收等优点;解决了凹凸棒吸附能力差、回收难,纤维素吸附剂机械强度弱、热稳定性低等问题,同时原料来源广泛,价格低廉,不产生二次污染,充分利用纤维素、凹凸棒再生资源,实用价值高,可用于水中污染物的深度处理,解决了能源危机和环境污染问题。In a word, the preparation process of the present invention is simple and convenient, the ionic liquid solvent used is safe and non-toxic, and the modified attapulgite and the cellulose dissolved in the ionic liquid are coupled to produce a synergistic effect, and the prepared attapulgite cellulose microspheres are porous, It has good dispersibility, biocompatibility and thermal stability, and has the advantages of strong adsorption capacity, large adsorption capacity, high removal efficiency, stable properties, and easy recovery of pollutants in water; it solves the problem of poor adsorption capacity of attapulgite, difficult recovery, fiber At the same time, the source of raw materials is wide, the price is low, no secondary pollution occurs, and the regeneration resources of cellulose and attapulgite are fully utilized, which has high practical value and can be used for advanced treatment of pollutants in water , to solve the energy crisis and environmental pollution problems.
具体实施方式:detailed description:
以下是对本发明的进一步说明,而不是对本发明的限制。The following is a further description of the present invention, rather than a limitation of the present invention.
实施例1:Example 1:
将凹凸棒土经挤压、剪切、粉碎,得到粒度为200目的粉体,粉体用质量分数为5%稀盐酸浸泡8h,然后用去离子水反复洗涤沉淀至中性,取20g分散到100mL乙醇和水的混合溶液中,其中乙醇和水体积比为9:1,随后边搅拌边加入5gγ-(2,3-环氧丙氧基)丙基三甲氧基硅烷偶联剂,在40℃下超声50min,然后在50℃搅拌吸附4h,吸附产物经抽滤分离后依次用100ml甲苯、无水乙醇和去离子水洗涤去除多余的硅烷偶联剂,于110℃下干燥,即得硅烷改性凹凸棒土,研磨备用。The attapulgite is extruded, sheared, and crushed to obtain a powder with a particle size of 200 mesh. The powder is soaked in dilute hydrochloric acid with a mass fraction of 5% for 8 hours, then washed and precipitated with deionized water repeatedly to neutrality, and 20 g is dispersed in In the mixed solution of 100mL ethanol and water, wherein the volume ratio of ethanol and water is 9:1, then add 5g gamma-(2,3-glycidoxy) propyltrimethoxysilane coupling agent while stirring, at 40 Ultrasonic at 50°C for 50 minutes, then stirred and adsorbed at 50°C for 4 hours, the adsorbed product was separated by suction filtration, washed with 100ml of toluene, absolute ethanol and deionized water to remove excess silane coupling agent, and dried at 110°C to obtain silane Modified attapulgite, ground for later use.
于烧瓶内加入1-丁基-3-甲基-咪唑氯盐100克,纸浆2克,于90℃下,80rpm转速搅拌,至纤维素完全溶解得到离子液体纤维素溶液。Add 100 grams of 1-butyl-3-methyl-imidazolium chloride salt and 2 grams of pulp into the flask, and stir at 90° C. at 80 rpm until the cellulose is completely dissolved to obtain an ionic liquid cellulose solution.
将上述制备的质量为离子液体纤维素溶液质量0.2倍的改性凹凸棒,分散到离子液体纤维素溶液中,在90℃,80rpm转速下搅拌20分钟后,加入油相和表面活性剂(油相为泵油、表面活性剂为吐温80),油相与离子液体纤维素溶液的体积比为4∶1,表面活性剂与油相的质量比为1∶40,在300rpm转速下搅拌15分钟,形成反相悬浮体系,以每10钟降温5℃的速率降温至30℃,纤维素溶液凝结成球;加入固化剂(固化剂为水,体积为离子液体纤维素溶液体积的2倍),5分钟后转速降为200rpm,保持搅拌20分钟,纤维素溶液迅速固化,形成凹凸棒纤维素复合吸附微球,温度降至室温,将微球从反应液中过滤出来,用1~2倍体积的去离子水洗涤3~6次,然后将凹凸棒纤维素复合吸附微球浸泡在去离子水中48小时;将凹凸棒纤维素复合吸附微球湿态筛分,得到凹凸棒纤维素复合吸附微球。The above-mentioned modified attapulgite whose quality is 0.2 times the mass of the ionic liquid cellulose solution is dispersed in the ionic liquid cellulose solution, and after stirring for 20 minutes at 90° C. at 80 rpm, add the oil phase and surfactant (oil The phase is pump oil, the surfactant is Tween 80), the volume ratio of the oil phase to the ionic liquid cellulose solution is 4:1, the mass ratio of the surfactant to the oil phase is 1:40, and stirred at 300rpm for 15 Minutes, form a reverse suspension system, cool down to 30°C at a rate of 5°C every 10 minutes, and the cellulose solution coagulates into balls; add a curing agent (the curing agent is water, and the volume is twice the volume of the ionic liquid cellulose solution) , after 5 minutes, the rotation speed was reduced to 200rpm, and kept stirring for 20 minutes, the cellulose solution solidified rapidly, forming attapulgite cellulose composite adsorption microspheres, the temperature was lowered to room temperature, and the microspheres were filtered out from the reaction solution, and washed with 1 to 2 times volume of deionized water for 3 to 6 times, and then soak the attapulgite cellulose composite adsorption microspheres in deionized water for 48 hours; sieve the attapulgite cellulose composite adsorption microspheres in a wet state to obtain the attapulgite cellulose composite adsorption Microspheres.
实施例2:Example 2:
将凹凸棒土经挤压、剪切、粉碎,得到粒度为200目的粉体,粉体用质量分数为10%稀盐酸浸泡12h,然后用去离子水反复洗涤沉淀至中性,取20g分散到100mL乙醇和水的混合溶液中,其中乙醇和水体积比为9:1,随后边搅拌边加入4g N-2(氨乙基)3-氨丙基三甲氧基硅烷偶联剂,在50℃下超声50min,然后在50℃搅拌吸附4h,吸附产物经抽滤分离后依次用100ml甲苯、无水乙醇和去离子水洗涤去除多余的硅烷偶联剂,于110℃下干燥,即得硅烷改性凹凸棒土,研磨备用。The attapulgite is extruded, sheared, and crushed to obtain a powder with a particle size of 200 mesh. The powder is soaked in dilute hydrochloric acid with a mass fraction of 10% for 12 hours, then washed and precipitated with deionized water repeatedly until neutral, and 20 g is dispersed in In a mixed solution of 100mL ethanol and water, wherein the volume ratio of ethanol and water is 9:1, then add 4g of N-2(aminoethyl)3-aminopropyltrimethoxysilane coupling agent while stirring, at 50℃ Ultrasonic for 50min, then stirred and adsorbed at 50°C for 4h, the adsorbed product was separated by suction filtration, washed with 100ml of toluene, absolute ethanol and deionized water to remove excess silane coupling agent, and dried at 110°C to obtain silane-modified Sexual attapulgite, ground for later use.
于烧瓶内加入1-烯丙基-3-甲基咪唑醋酸盐100克,脱脂棉6克,于100℃下,200rpm转速搅拌,至纤维素完全溶解得到离子液体纤维素溶液。Add 100 grams of 1-allyl-3-methylimidazole acetate and 6 grams of absorbent cotton into the flask, and stir at 100° C. at 200 rpm until the cellulose is completely dissolved to obtain an ionic liquid cellulose solution.
将上述制备的质量为离子液体纤维素溶液质量0.4倍的改性凹凸棒,分散到离子液体纤维素溶液中,在100℃,200rpm转速下搅拌30分钟后,加入油相和表面活性剂(油相为矿物油、表面活性剂为Span 85),油相与离子液体纤维素溶液的体积比为6∶1,表面活性剂与油相的质量比为1∶100,在500rpm转速下搅拌20分钟,形成反相悬浮体系,以每10钟降温5℃的速率降温至50℃,纤维素溶液凝结成球;加入固化剂(固化剂为乙醇,体积为离子液体纤维素溶液体积的3倍),5分钟后转速降为200rpm,保持搅拌20分钟,纤维素溶液迅速固化,形成凹凸棒纤维素复合吸附微球,温度降至室温,将微球从反应液中过滤出来,用1~2倍体积的去离子水洗涤3~6次,然后将凹凸棒纤维素复合吸附微球浸泡在去离子水中48小时;将凹凸棒纤维素复合吸附微球湿态筛分,得到凹凸棒纤维素复合吸附微球。The above-mentioned modified attapulgite whose quality is 0.4 times the mass of the ionic liquid cellulose solution is dispersed into the ionic liquid cellulose solution, and after stirring for 30 minutes at 100° C. at 200 rpm, add the oil phase and surfactant (oil Phase is mineral oil, surfactant is Span 85), the volume ratio of oil phase and ionic liquid cellulose solution is 6: 1, the mass ratio of surfactant and oil phase is 1: 100, stir 20 minutes under 500rpm rotating speed , forming a reverse suspension system, cooling down to 50°C at a rate of 5°C every 10 minutes, the cellulose solution coagulates into balls; adding a curing agent (the curing agent is ethanol, and the volume is 3 times the volume of the ionic liquid cellulose solution), After 5 minutes, the rotation speed was reduced to 200rpm, and kept stirring for 20 minutes. The cellulose solution solidified rapidly and formed attapulgite cellulose composite adsorption microspheres. Wash with deionized water for 3 to 6 times, then soak the attapulgite cellulose composite adsorption microspheres in deionized water for 48 hours; sieve the attapulgite cellulose composite adsorption microspheres in a wet state to obtain the attapulgite cellulose composite adsorption microspheres ball.
实施例3:Example 3:
将凹凸棒土经挤压、剪切、粉碎,得到粒度为200目的粉体,粉体用质量分数为8%稀盐酸浸泡10h,然后用去离子水反复洗涤沉淀至中性,取20g分散到100mL乙醇和水的混合溶液中,其中乙醇和水体积比为9:1,随后边搅拌边加入3.3g乙烯基三甲氧基硅烷偶联剂,在50℃下超声50min,然后在50℃搅拌吸附4h,吸附产物经抽滤分离后依次用100ml甲苯、无水乙醇和去离子水洗涤去除多余的硅烷偶联剂,于110℃下干燥,即得硅烷改性凹凸棒土,研磨备用。The attapulgite is extruded, sheared, and crushed to obtain a powder with a particle size of 200 mesh. The powder is soaked in dilute hydrochloric acid with a mass fraction of 8% for 10 hours, then washed and precipitated with deionized water repeatedly to neutrality, and 20 g is dispersed in Into a mixed solution of 100mL ethanol and water, wherein the volume ratio of ethanol and water is 9:1, then add 3.3g of vinyltrimethoxysilane coupling agent while stirring, ultrasonicate at 50°C for 50min, then stir and adsorb at 50°C After 4 hours, the adsorption product was separated by suction filtration, washed with 100ml of toluene, absolute ethanol and deionized water to remove excess silane coupling agent, and dried at 110°C to obtain silane-modified attapulgite, which was ground for later use.
于烧瓶内加入1-烯丙基-3-甲基咪唑醋酸盐100克,精制棉5克,于100℃下,150rpm转速搅拌,至纤维素完全溶解得到离子液体纤维素溶液。Add 100 grams of 1-allyl-3-methylimidazole acetate and 5 grams of refined cotton into the flask, and stir at 100° C. at 150 rpm until the cellulose is completely dissolved to obtain an ionic liquid cellulose solution.
将上述制备的质量为离子液体纤维素溶液质量0.3倍的改性凹凸棒,分散到离子液体纤维素溶液中,在95℃,150rpm转速下搅拌25分钟后,加入油相和表面活性剂(油相为石蜡油、表面活性剂为Span 85),油相与离子液体纤维素溶液的体积比为5∶1,表面活性剂与油相的质量比为1∶60,在400rpm转速下搅拌20分钟,形成反相悬浮体系,以每10钟降温5℃的速率降温至40℃,纤维素溶液凝结成球;加入固化剂(固化剂为丙酮,体积为离子液体纤维素溶液体积的3倍),5分钟后转速降为200rpm,保持搅拌20分钟,纤维素溶液迅速固化,形成凹凸棒纤维素复合吸附微球,温度降至室温,将微球从反应液中过滤出来,用1~2倍体积的去离子水洗涤3~6次,然后将凹凸棒纤维素复合吸附微球浸泡在去离子水中48小时;将凹凸棒纤维素复合吸附微球湿态筛分,得到凹凸棒纤维素复合吸附微球。The above-mentioned modified attapulgite whose quality is 0.3 times the mass of the ionic liquid cellulose solution is dispersed in the ionic liquid cellulose solution, and after stirring for 25 minutes at 95° C. at 150 rpm, add the oil phase and surfactant (oil The phase is paraffin oil, the surfactant is Span 85), the volume ratio of the oil phase to the ionic liquid cellulose solution is 5:1, the mass ratio of the surfactant to the oil phase is 1:60, and stirred for 20 minutes at 400 rpm , forming a reverse suspension system, cooling down to 40°C at a rate of 5°C per 10 minutes, the cellulose solution coagulates into balls; adding a curing agent (the curing agent is acetone, and the volume is 3 times the volume of the ionic liquid cellulose solution), After 5 minutes, the rotation speed was reduced to 200rpm, and kept stirring for 20 minutes. The cellulose solution solidified rapidly and formed attapulgite cellulose composite adsorption microspheres. Wash with deionized water for 3 to 6 times, then soak the attapulgite cellulose composite adsorption microspheres in deionized water for 48 hours; sieve the attapulgite cellulose composite adsorption microspheres in a wet state to obtain the attapulgite cellulose composite adsorption microspheres ball.
实施例4:Example 4:
将凹凸棒土经挤压、剪切、粉碎,得到粒度为200目的粉体,粉体用质量分数为7%稀盐酸浸泡11h,然后用去离子水反复洗涤沉淀至中性,取20g分散到100mL乙醇和水的混合溶液中,其中乙醇和水体积比为9:1,随后边搅拌边加入4.4g N-2(氨乙基)3-氨丙基三甲氧基硅烷偶联剂,在45℃下超声50min,然后在50℃搅拌吸附4h,吸附产物经抽滤分离后依次用100ml甲苯、无水乙醇和去离子水洗涤去除多余的硅烷偶联剂,于110℃下干燥,即得硅烷改性凹凸棒土,研磨备用。The attapulgite is extruded, sheared, and crushed to obtain a powder with a particle size of 200 mesh. The powder is soaked in dilute hydrochloric acid with a mass fraction of 7% for 11 hours, and then washed and precipitated with deionized water repeatedly to neutrality. Take 20g and disperse it in In the mixed solution of 100mL ethanol and water, wherein ethanol and water volume ratio are 9:1, then add 4.4g N-2 (aminoethyl) 3-aminopropyltrimethoxysilane coupling agent while stirring, at 45 Ultrasonic at 50°C for 50 minutes, then stirred and adsorbed at 50°C for 4 hours, the adsorbed product was separated by suction filtration, washed with 100ml of toluene, absolute ethanol and deionized water to remove excess silane coupling agent, and dried at 110°C to obtain silane Modified attapulgite, ground for later use.
于烧瓶内加入1-丁基-3-甲基咪唑氯盐100克,微晶纤维素4克,于100℃下,100rpm转速搅拌,至纤维素完全溶解得到离子液体纤维素溶液。Add 100 grams of 1-butyl-3-methylimidazolium chloride salt and 4 grams of microcrystalline cellulose into the flask, and stir at 100° C. at 100 rpm until the cellulose is completely dissolved to obtain an ionic liquid cellulose solution.
将上述制备的质量为离子液体纤维素溶液质量0.4倍的改性凹凸棒,分散到离子液体纤维素溶液中,在95℃,180rpm转速下搅拌25分钟后,加入油相和表面活性剂(油相为花生油、表面活性剂为吐温80),油相与离子液体纤维素溶液的体积比为6∶1,表面活性剂与油相的质量比为1∶40,在450rpm转速下搅拌20分钟,形成反相悬浮体系,以每10钟降温5℃的速率降温至30℃,纤维素溶液凝结成球;加入体积为离子液体纤维素溶液体积的3倍的固化剂(固化剂为体积比为1:3的乙醇与丙酮混合物),5分钟后转速降为200rpm,保持搅拌20分钟,纤维素溶液迅速固化,形成凹凸棒纤维素复合吸附微球,温度降至室温,将微球从反应液中过滤出来,用1~2倍体积的去离子水洗涤3~6次,然后将凹凸棒纤维素复合吸附微球浸泡在去离子水中48小时;将凹凸棒纤维素复合吸附微球湿态筛分,得到凹凸棒纤维素复合吸附微球。The above-mentioned modified attapulgite whose quality is 0.4 times the mass of the ionic liquid cellulose solution is dispersed in the ionic liquid cellulose solution, and after stirring for 25 minutes at 95° C. at 180 rpm, add the oil phase and surfactant (oil Phase is peanut oil, surfactant is Tween 80), the volume ratio of oil phase and ionic liquid cellulose solution is 6: 1, the mass ratio of surfactant and oil phase is 1: 40, stirs 20 minutes under 450rpm rotating speed , form a reverse suspension system, cool down to 30°C at a rate of 5°C per 10 minutes, and the cellulose solution coagulates into balls; add a solidifying agent whose volume is 3 times the volume of the ionic liquid cellulose solution (the solidifying agent has a volume ratio of 1:3 mixture of ethanol and acetone), after 5 minutes, the rotation speed was reduced to 200rpm, and kept stirring for 20 minutes, the cellulose solution solidified rapidly, forming attapulgite cellulose composite adsorption microspheres, the temperature was lowered to room temperature, and the microspheres were removed from the reaction solution Filter out the medium, wash with 1 to 2 times the volume of deionized water for 3 to 6 times, then soak the attapulgite cellulose composite adsorption microspheres in deionized water for 48 hours; sieve the attapulgite cellulose composite adsorption microspheres wet The attapulgite cellulose composite adsorption microspheres were obtained.
实施例5:Example 5:
将凹凸棒土经挤压、剪切、粉碎,得到粒度为200目的粉体,粉体用质量分数为6%稀盐酸浸泡9h,然后用去离子水反复洗涤沉淀至中性,取20g分散到100mL乙醇和水的混合溶液中,其中乙醇和水体积比为9:1,随后边搅拌边加入5g乙烯基三甲氧基硅烷偶联剂,在45℃下超声50min,然后在50℃搅拌吸附4h,吸附产物经抽滤分离后依次用100ml甲苯、无水乙醇和去离子水洗涤去除多余的硅烷偶联剂,于110℃下干燥,即得硅烷改性凹凸棒土,研磨备用。The attapulgite is extruded, sheared, and crushed to obtain a powder with a particle size of 200 mesh. The powder is soaked in dilute hydrochloric acid with a mass fraction of 6% for 9 hours, then washed and precipitated with deionized water repeatedly to neutrality, and 20 g is dispersed in 100mL of ethanol and water mixed solution, wherein the volume ratio of ethanol and water is 9:1, then add 5g of vinyltrimethoxysilane coupling agent while stirring, ultrasonic at 45°C for 50min, then stir and adsorb at 50°C for 4h , the adsorption product was separated by suction filtration, washed with 100ml of toluene, absolute ethanol and deionized water to remove excess silane coupling agent, and dried at 110°C to obtain silane-modified attapulgite, which was ground for later use.
于烧瓶内加入1-烯丙基-3-甲基咪唑醋酸盐100克,微晶纤维素5克,于100℃下,150rpm转速搅拌,至纤维素完全溶解得到离子液体纤维素溶液。Add 100 grams of 1-allyl-3-methylimidazole acetate and 5 grams of microcrystalline cellulose into the flask, and stir at 100° C. at 150 rpm until the cellulose is completely dissolved to obtain an ionic liquid cellulose solution.
将上述制备的质量为离子液体纤维素溶液质量0.3倍的改性凹凸棒,分散到离子液体纤维素溶液中,在100℃,150rpm转速下搅拌20分钟后,加入油相和表面活性剂(油相为花生油、表面活性剂为质量比为1:1的吐温80与Span 85的混合物),油相与离子液体纤维素溶液的体积比为5∶1,表面活性剂与油相的质量比为1∶60,在400rpm转速下搅拌20分钟,形成反相悬浮体系,以每10钟降温5℃的速率降温至30℃,纤维素溶液凝结成球;加入体积为离子液体纤维素溶液体积的3倍的固化剂(固化剂为体积比为1:1的乙醇与丙酮混合物),5分钟后转速降为200rpm,保持搅拌20分钟,纤维素溶液迅速固化,形成凹凸棒纤维素复合吸附微球,温度降至室温,将微球从反应液中过滤出来,用1~2倍体积的去离子水洗涤3~6次,然后将凹凸棒纤维素复合吸附微球浸泡在去离子水中48小时;将凹凸棒纤维素复合吸附微球湿态筛分,得到凹凸棒纤维素复合吸附微球。The above-mentioned modified attapulgite whose quality is 0.3 times the mass of the ionic liquid cellulose solution is dispersed in the ionic liquid cellulose solution, and after stirring for 20 minutes at 100° C. at a speed of 150 rpm, an oil phase and a surfactant (oil The phase is peanut oil, the surfactant is a mixture of Tween 80 and Span 85 with a mass ratio of 1:1), the volume ratio of the oil phase to the ionic liquid cellulose solution is 5:1, and the mass ratio of the surfactant to the oil phase 1:60, stirred at 400 rpm for 20 minutes to form a reverse-phase suspension system, cooled to 30°C at a rate of 5°C every 10 minutes, and the cellulose solution coagulated into balls; the volume of the ionic liquid cellulose solution added was 3 times the curing agent (the curing agent is a mixture of ethanol and acetone with a volume ratio of 1:1), reduce the speed to 200rpm after 5 minutes, keep stirring for 20 minutes, the cellulose solution is rapidly solidified, and attapulgite cellulose composite adsorption microspheres are formed , the temperature is lowered to room temperature, the microspheres are filtered out from the reaction solution, washed with 1 to 2 times the volume of deionized water for 3 to 6 times, and then the attapulgite cellulose composite adsorption microspheres are soaked in deionized water for 48 hours; The attapulgite cellulose composite adsorption microspheres are sieved in a wet state to obtain the attapulgite cellulose composite adsorption microspheres.
实施例6:Embodiment 6:
将凹凸棒土经挤压、剪切、粉碎,得到粒度为200目的粉体,粉体用质量分数为8%稀盐酸浸泡10h,然后用去离子水反复洗涤沉淀至中性,取20g分散到100mL乙醇和水的混合溶液中,其中乙醇和水体积比为9:1,随后边搅拌边加入5gγ-(2,3-环氧丙氧基)丙基三甲氧基硅烷偶联剂,在50℃下超声50min,然后在50℃搅拌吸附4h,吸附产物经抽滤分离后依次用100ml甲苯、无水乙醇和去离子水洗涤去除多余的硅烷偶联剂,于110℃下干燥,即得硅烷改性凹凸棒土,研磨备用。The attapulgite is extruded, sheared, and crushed to obtain a powder with a particle size of 200 mesh. The powder is soaked in dilute hydrochloric acid with a mass fraction of 8% for 10 hours, then washed and precipitated with deionized water repeatedly to neutrality, and 20 g is dispersed in In the mixed solution of 100mL ethanol and water, wherein the volume ratio of ethanol and water is 9:1, then add 5g gamma-(2,3-glycidoxy) propyltrimethoxysilane coupling agent while stirring, at 50 Ultrasonic at 50°C for 50 minutes, then stirred and adsorbed at 50°C for 4 hours, the adsorbed product was separated by suction filtration, washed with 100ml of toluene, absolute ethanol and deionized water to remove excess silane coupling agent, and dried at 110°C to obtain silane Modified attapulgite, ground for later use.
于烧瓶内加入1-丁基-3-甲基咪唑氯盐100克,微晶纤维素5克,于100℃下,180rpm转速搅拌,至纤维素完全溶解得到离子液体纤维素溶液。Add 100 grams of 1-butyl-3-methylimidazolium chloride salt and 5 grams of microcrystalline cellulose into the flask, and stir at 100° C. at 180 rpm until the cellulose is completely dissolved to obtain an ionic liquid cellulose solution.
将上述制备的质量为离子液体纤维素溶液质量0.3倍的改性凹凸棒,分散到离子液体纤维素溶液中,在100℃,180rpm转速下搅拌20分钟后,加入油相和表面活性剂(油相为石蜡油、表面活性剂为质量比为1:1的吐温80与Span 85的混合物),油相与离子液体纤维素溶液的体积比为5∶1,表面活性剂与油相的质量比为1∶80,在400rpm转速下搅拌15分钟,形成反相悬浮体系,以每10钟降温5℃的速率降温至30℃,纤维素溶液凝结成球;加入体积为离子液体纤维素溶液体积的3倍的固化剂(固化剂为体积比为1:1的乙醇与水混合物),5分钟后转速降为200rpm,保持搅拌20分钟,纤维素溶液迅速固化,形成凹凸棒纤维素复合吸附微球,温度降至室温,将微球从反应液中过滤出来,用1~2倍体积的去离子水洗涤3~6次,然后将凹凸棒纤维素复合吸附微球浸泡在去离子水中48小时;将凹凸棒纤维素复合吸附微球湿态筛分,得到凹凸棒纤维素复合吸附微球。The above-mentioned modified attapulgite whose quality is 0.3 times the mass of the ionic liquid cellulose solution is dispersed in the ionic liquid cellulose solution, and after stirring for 20 minutes at 100° C. at a speed of 180 rpm, add the oil phase and surfactant (oil The phase is paraffin oil, the surfactant is a mixture of Tween 80 and Span 85 with a mass ratio of 1:1), the volume ratio of the oil phase to the ionic liquid cellulose solution is 5:1, and the mass ratio of the surfactant to the oil phase The ratio is 1:80, stirred at 400rpm for 15 minutes to form a reverse suspension system, and the temperature is lowered to 30°C at a rate of 5°C every 10 minutes, and the cellulose solution is condensed into balls; the added volume is the volume of the ionic liquid cellulose solution 3 times the curing agent (the curing agent is a mixture of ethanol and water with a volume ratio of 1:1), the rotation speed is reduced to 200rpm after 5 minutes, and the stirring is kept for 20 minutes. The temperature is lowered to room temperature, the microspheres are filtered out from the reaction solution, washed with 1 to 2 times the volume of deionized water for 3 to 6 times, and then the attapulgite cellulose composite adsorption microspheres are soaked in deionized water for 48 hours and sieving the attapulgite cellulose composite adsorption microspheres in a wet state to obtain the attapulgite cellulose composite adsorption microspheres.
实施例7:将本发明制备的凹凸棒纤维素复合吸附微球用于污染物吸附处理:Example 7: Using the attapulgite cellulose composite adsorption microspheres prepared by the present invention for pollutant adsorption treatment:
分别以实施例1-6制备的凹凸棒纤维素复合吸附微球、硅烷改性凹凸棒、天然未改性凹凸棒和天然未改性纤维素为吸附剂,分别以初始浓度为5mg/L的苯酚、邻苯二酚、对苯二酚、亚甲基蓝、甲基橙、铜离子、镉离子、铅离子作为污染物进行吸附处理。具体方法如下:The attapulgite cellulose composite adsorption microspheres, silane-modified attapulgite, natural unmodified attapulgite and natural unmodified cellulose prepared in Examples 1-6 were respectively used as adsorbents, and the initial concentration was 5 mg/L respectively. Phenol, catechol, hydroquinone, methylene blue, methyl orange, copper ions, cadmium ions, and lead ions are used as pollutants for adsorption treatment. The specific method is as follows:
向初始浓度为5mg/L有机污染物中加入吸附剂,固液比为1g:50mL,25℃下以200r/min转速恒温振荡吸附12h,过滤取滤液,测得吸附量,结果参见表1。Add adsorbent to the organic pollutants with an initial concentration of 5 mg/L, the solid-to-liquid ratio is 1 g:50 mL, oscillate at 25 °C at a constant temperature of 200 r/min for 12 h, filter the filtrate, and measure the adsorption amount. The results are shown in Table 1.
表1不同吸附剂对污染物吸附处理Table 1 Adsorption treatment of pollutants by different adsorbents
从表1中可以看出实施例1-6制备的凹凸棒纤维素复合吸附微球与硅烷改性凹凸棒、天然未改性凹凸棒石和天然未改性纤维素相比,对水中酚类染物的脱除率可提高3-5倍以上;对水中亚甲基蓝脱除率最高为97-99%;对甲基橙脱除率也达到了75%以上;对重金属的吸附脱除也具有较好效果,脱除率在55-77%之间;而天然未改性凹凸棒和天然未改性纤维素对污染物的脱除率均为达到35%以上。从以上数据可以看出,本发明制备的凹凸棒纤维素复合吸附微球吸附性能好,对污染物去除效果较好。It can be seen from Table 1 that the attapulgite cellulose composite adsorption microspheres prepared in Examples 1-6, compared with silane-modified attapulgite, natural unmodified attapulgite, and natural unmodified cellulose, are less sensitive to phenolic dyes in water. The removal rate of methylene blue can be increased by more than 3-5 times; the highest removal rate of methylene blue in water is 97-99%; the removal rate of methyl orange has also reached more than 75%; the adsorption and removal of heavy metals also has a good effect , the removal rate is between 55-77%; while the removal rates of natural unmodified attapulgite and natural unmodified cellulose to pollutants are both above 35%. It can be seen from the above data that the attapulgite cellulose composite adsorption microspheres prepared by the present invention have good adsorption performance and good effect on pollutant removal.
本发明将改性凹凸棒与纤维素配伍,得到具有多孔结构,比表面积大的吸附介质,通过取长补短,产生协同效应,提高了对污染物的吸附、富集能力,性质稳定,易于回收再利用;同时原料来源广泛,价格低廉,不产生二次污染,实用价值高,可用于水中污染物的深度处理。In the invention, the modified attapulgite is compatible with cellulose to obtain an adsorption medium with a porous structure and a large specific surface area. By learning from each other, a synergistic effect is produced, and the ability to absorb and enrich pollutants is improved. The properties are stable and easy to recycle and reuse. ; At the same time, the source of raw materials is wide, the price is low, no secondary pollution occurs, the practical value is high, and it can be used for advanced treatment of pollutants in water.
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