CN113213632B - Nano-hydroxyapatite loofah sponge composite filler and preparation method and application thereof - Google Patents
Nano-hydroxyapatite loofah sponge composite filler and preparation method and application thereof Download PDFInfo
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- 244000280244 Luffa acutangula Species 0.000 title claims abstract description 79
- 235000009814 Luffa aegyptiaca Nutrition 0.000 title claims abstract description 79
- 239000000945 filler Substances 0.000 title claims abstract description 40
- 229910052588 hydroxylapatite Inorganic materials 0.000 title claims abstract description 39
- 239000002131 composite material Substances 0.000 title claims abstract description 37
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- 239000000149 chemical water pollutant Substances 0.000 claims abstract description 23
- 238000000034 method Methods 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 10
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910000388 diammonium phosphate Inorganic materials 0.000 claims abstract description 8
- 235000019838 diammonium phosphate Nutrition 0.000 claims abstract description 8
- 238000003756 stirring Methods 0.000 claims abstract description 6
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 5
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 5
- 238000002791 soaking Methods 0.000 claims abstract description 5
- XYJRXVWERLGGKC-UHFFFAOYSA-D pentacalcium;hydroxide;triphosphate Chemical compound [OH-].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O XYJRXVWERLGGKC-UHFFFAOYSA-D 0.000 claims description 12
- 239000000725 suspension Substances 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 2
- 239000005696 Diammonium phosphate Substances 0.000 claims 1
- 238000007605 air drying Methods 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 17
- 230000000694 effects Effects 0.000 abstract description 15
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 13
- 229910052791 calcium Inorganic materials 0.000 abstract description 3
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 3
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract 1
- 239000011575 calcium Substances 0.000 description 9
- 239000002994 raw material Substances 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 6
- 239000010802 sludge Substances 0.000 description 5
- 230000001360 synchronised effect Effects 0.000 description 5
- 229910052804 chromium Inorganic materials 0.000 description 4
- 229910052745 lead Inorganic materials 0.000 description 4
- 229920005610 lignin Polymers 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000001546 nitrifying effect Effects 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 2
- 229920002488 Hemicellulose Polymers 0.000 description 2
- 229910001424 calcium ion Inorganic materials 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 230000002503 metabolic effect Effects 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 239000002910 solid waste Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000003956 Luffa Nutrition 0.000 description 1
- 241000219138 Luffa Species 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000002306 biochemical method Methods 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/302—Nitrification and denitrification treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
-
- 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
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- 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
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/06—Contaminated groundwater or leachate
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Hydrology & Water Resources (AREA)
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- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
本发明公开了一种纳米羟基磷灰石丝瓜络复合填料及其制备方法和应用,涉及废水处理技术领域;所述方法包括以下步骤:取含水率为5‑10%的丝瓜络浸泡于质量浓度为30%的过氧化氢中,浸泡2h后取出晾干;将晾干后的丝瓜络在Ca(NO3)2·4H2O溶液中浸泡8h;按Ca、P的摩尔比为1.67:1向Ca(NO3)2·4H2O溶液中滴加磷酸氢二铵,然后采用体积浓度为10‑15%的氨水调节pH至9‑9.5,搅拌4‑5h;将上步获得的丝瓜络洗干净后在75‑78℃下烘干24h;重复上述步骤三次后获得纳米羟基磷灰石丝瓜络复合填料。采用本发明的纳米羟基磷灰石丝瓜络复合填料对垃圾渗滤液中的重金属进行吸附,Pb的最佳吸附率高达59%,Cr的最佳吸附率高达92.31%,吸附效果显著。
The invention discloses a nano-hydroxyapatite loofah composite filler and its preparation method and application, and relates to the technical field of wastewater treatment; the method comprises the following steps: taking loofah with a water content of 5-10% and soaking it in a mass concentration In 30% hydrogen peroxide, soak it for 2 hours and take it out to dry; soak the dried loofah in Ca(NO 3 ) 2 4H 2 O solution for 8 hours; the molar ratio of Ca and P is 1.67:1 Add diammonium hydrogen phosphate dropwise to the Ca(NO 3 ) 2 4H 2 O solution, then use ammonia water with a volume concentration of 10-15% to adjust the pH to 9-9.5, and stir for 4-5h; the loofah obtained in the previous step After washing, dry at 75-78°C for 24 hours; repeat the above steps three times to obtain nano-hydroxyapatite loofah composite filler. The nano-hydroxyapatite loofah composite filler of the present invention is used to adsorb heavy metals in landfill leachate, and the optimal adsorption rate of Pb is as high as 59%, and the optimal adsorption rate of Cr is as high as 92.31%, and the adsorption effect is remarkable.
Description
技术领域technical field
本发明涉及废水处理技术领域,具体涉及一种纳米羟基磷灰石丝瓜络复合填料及其制备方法和应用。The invention relates to the technical field of wastewater treatment, in particular to a nano-hydroxyapatite loofah composite filler and a preparation method and application thereof.
背景技术Background technique
2000年左右,我国城市生活垃圾增长迅速,为此,国家大力建设垃圾填埋场。至今大部分垃圾填埋场使用年限已达20年,随填埋时间的增加,垃圾渗滤液中的重金属含量呈增加趋势,As、Mn、Zn、Pb、Cd、Cr和Ni等重金属含量较高。Around 2000, my country's urban domestic waste increased rapidly. For this reason, the country vigorously built waste landfills. So far, most landfills have been used for 20 years. With the increase of landfill time, the content of heavy metals in landfill leachate shows an increasing trend, and the content of heavy metals such as As, Mn, Zn, Pb, Cd, Cr and Ni is relatively high. .
为解决这一问题,有人采用生化法对垃圾渗滤液进行处理,但由于垃圾渗滤液的可生化性较差,且大部分重金属对硝化反硝化菌群存在抑制作用,导致CMBR运维后期逐渐出现微生物菌群活性差、出水不稳定等情况。In order to solve this problem, some people use biochemical methods to treat landfill leachate. However, due to the poor biodegradability of landfill leachate, and most heavy metals have an inhibitory effect on the nitrifying and denitrifying bacteria, leading to the gradual emergence of CMBR in the later stage of operation and maintenance. Poor microbial flora activity, unstable effluent, etc.
针对高氨氮、高重金属有机废水的处理,由于大部分重金属对硝化反硝化菌群有一定的抑制作用,采用生化法A2/O工艺处理垃圾渗滤液是目前主要的应用技术。为提高微生物的处理效果,大部分项目现场施工在O池内采用普通填料,起到增大微生物与废水的接触面积,提高污水处理效果的作用,但其作用单一。For the treatment of high ammonia nitrogen and high heavy metal organic wastewater, since most heavy metals have a certain inhibitory effect on nitrification and denitrification bacteria, the biochemical A2/O process is currently the main application technology for landfill leachate treatment. In order to improve the treatment effect of microorganisms, most of the project site construction uses ordinary fillers in the O pool to increase the contact area between microorganisms and wastewater and improve the effect of sewage treatment, but its effect is single.
而丝瓜络作为环境友好、低成本材料已作为生物膜载体或碳源被广泛应用于多种水处理领域,涉及的方向包括重金属吸附、纤维改性、石油类污染物吸附、生物接触氧化床载体、多孔微生物载体等。有学者采用高温烘干法对丝瓜络进行羟基磷灰石改性,制成粉磨状,有一定的重金属吸附效果,但破坏了丝瓜络原有的多孔形态,不能实现生物填料为活性污泥挂网的效果。As an environmentally friendly and low-cost material, loofah has been widely used in various water treatment fields as a biofilm carrier or carbon source. The directions involved include heavy metal adsorption, fiber modification, petroleum pollutant adsorption, and biological contact oxidation bed carrier. , porous microbial carrier, etc. Some scholars use the high-temperature drying method to modify the loofah with hydroxyapatite and make it into a powdered form, which has a certain heavy metal adsorption effect, but destroys the original porous shape of the loofah, and cannot realize the biological filler as activated sludge. The effect of hanging the net.
发明内容Contents of the invention
为了解决上述问题,本发明提供一种纳米羟基磷灰石丝瓜络复合填料及其制备方法和应用。In order to solve the above problems, the present invention provides a nano-hydroxyapatite loofah composite filler and its preparation method and application.
为了实现上述目的,本发明采用的技术方案之一为:提供一种纳米羟基磷灰石丝瓜络复合填料的制备方法,所述方法包括以下步骤:In order to achieve the above object, one of the technical solutions adopted in the present invention is to provide a preparation method of nano-hydroxyapatite loofah composite filler, said method comprising the following steps:
S1:取含水率为5-10%的丝瓜络浸泡于质量浓度为30%的过氧化氢中,浸泡2h后取出晾干;S1: Take the loofah with a water content of 5-10% and soak it in hydrogen peroxide with a mass concentration of 30%, take it out and dry it after soaking for 2 hours;
S2:将步骤S1中晾干后的丝瓜络在Ca(NO3)2·4H2O溶液中浸泡8h;S2: Soak the dried loofah in step S1 in Ca(NO 3 ) 2 ·4H 2 O solution for 8 hours;
S3:按Ca、P的摩尔比为1.67:1向步骤S2的溶液中滴加磷酸氢二铵,然后采用体积浓度为10-15%的氨水调节pH至9-9.5,搅拌4-5h;S3: Add diammonium hydrogen phosphate dropwise to the solution in step S2 according to the molar ratio of Ca and P of 1.67:1, then adjust the pH to 9-9.5 with ammonia water with a volume concentration of 10-15%, and stir for 4-5h;
S4:将步骤S3获得的丝瓜络洗干净后在75-78℃下烘干24h;S4: Wash the loofah obtained in step S3 and dry it at 75-78°C for 24 hours;
S5:重复步骤S2-S4三次后获得纳米羟基磷灰石丝瓜络复合填料。S5: Repeat steps S2-S4 three times to obtain nano-hydroxyapatite loofah composite filler.
进一步地,所述Ca(NO3)2·4H2O溶液的浓度为0.0334moL/L。Further, the concentration of the Ca(NO 3 ) 2 ·4H 2 O solution is 0.0334moL/L.
更进一步地,磷酸氢二铵的浓度为0.02moL/L。Furthermore, the concentration of diammonium hydrogen phosphate is 0.02moL/L.
为了实现上述目的,本发明采用的技术方案之二为:提供一种本发明所述方法制备的纳米羟基磷灰石丝瓜络复合填料。In order to achieve the above object, the second technical solution adopted by the present invention is to provide a nano-hydroxyapatite loofah composite filler prepared by the method of the present invention.
为实现上述目的,本发明采用的技术方案之三为:将本发明制备的纳米羟基磷灰石丝瓜络复合填料应用但不限于垃圾渗滤液的处理之中。In order to achieve the above purpose, the third technical solution adopted by the present invention is: the nano-hydroxyapatite loofah composite filler prepared by the present invention is applied to but not limited to the treatment of landfill leachate.
为实现上述目的,本发明采用的技术方案之四为:提供一种用于处理垃圾渗滤液的生物反应器,所述反应器采用的填料为本发明制备的纳米羟基磷灰石丝瓜络复合填料。In order to achieve the above object, the fourth technical solution adopted by the present invention is to provide a bioreactor for treating landfill leachate, the filler used in the reactor is the nano-hydroxyapatite loofah composite filler prepared by the present invention .
进一步地,所述生物反应器内还设置有多个多孔悬浮球,所述纳米羟基磷灰石丝瓜络复合填料填充在多孔悬浮球内。Further, the bioreactor is also provided with a plurality of porous suspension balls, and the nano-hydroxyapatite loofah composite filler is filled in the porous suspension balls.
本发明的有益效果:Beneficial effects of the present invention:
以本发明方法制备的纳米羟基磷灰石丝瓜络复合材料作为生物反应器的填料,有效解决了垃圾渗滤液中重金属预处理的问题,减少了工程设备,缩短了水力停留时间(HRT);解决了传统吸附法处理重金属会产生大量含重金属污泥,污泥处理成本高的难题。The nano-hydroxyapatite loofah composite material prepared by the method of the present invention is used as the filler of the bioreactor, which effectively solves the problem of heavy metal pretreatment in landfill leachate, reduces engineering equipment, and shortens the hydraulic retention time (HRT); It solves the problem that the traditional adsorption method will produce a large amount of heavy metal-containing sludge and the cost of sludge treatment is high.
本发明利用丝瓜络的多孔多级结构,实现了一体化同步硝化反硝化,用一个反应池代替了传统的A2/O池,不仅减少了池体大小,简化了设备,还减少了能耗,降低了成本,另外,同步硝化反硝化的脱氮效果较好,规避了老旧垃圾填埋场渗滤液C/N比不足问题,避免了运行难或需加入C源的问题,同时,丝瓜络由65.5%的纤维素、17.5%的半纤维素和15.2%的木质素构成,可作为部分C源供给硝化菌和反硝化菌代谢繁殖;丝瓜络为农村固体废物,价格低,以此作为原材料制备的复合材料为环境友好型、低成本材料。且微生物降解丝瓜络中的木质素,能实的丝瓜络的资源化和减量化。The invention utilizes the porous multi-level structure of loofah to realize integrated synchronous nitrification and denitrification, and replaces the traditional A2/O pool with one reaction pool, which not only reduces the size of the pool, simplifies the equipment, but also reduces energy consumption. The cost is reduced. In addition, the denitrification effect of simultaneous nitrification and denitrification is better, which avoids the problem of insufficient C/N ratio of leachate in old landfills, and avoids the problem of difficult operation or the need to add C sources. At the same time, loofah Composed of 65.5% cellulose, 17.5% hemicellulose and 15.2% lignin, it can be used as part of the C source to supply nitrifying bacteria and denitrifying bacteria for metabolic reproduction; loofah is a rural solid waste with low price, so it can be used as a raw material The prepared composite material is an environment-friendly and low-cost material. Moreover, microorganisms degrade the lignin in the loofah, which can realize the resource utilization and reduction of the loofah.
除了上面所描述的目的、特征和优点之外,本发明还有其它的目的、特征和优点。下面将对本发明作进一步详细的说明。In addition to the objects, features and advantages described above, the present invention has other objects, features and advantages. The present invention will be described in further detail below.
附图说明Description of drawings
构成本申请的一部分的附图用来提供对本发明的进一步理解,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。The accompanying drawings constituting a part of this application are used to provide further understanding of the present invention, and the schematic embodiments and descriptions of the present invention are used to explain the present invention, and do not constitute an improper limitation of the present invention.
图1是本发明实施例的丝瓜络原料的外观形貌图;Fig. 1 is the outward appearance figure of the luffa raw material of the embodiment of the present invention;
图2是本发明实施例的丝瓜络原料的扫描电镜图;Fig. 2 is the scanning electron micrograph of the loofah raw material of the embodiment of the present invention;
图3是本发明实施例的纳米羟基磷灰石丝瓜络复合填料的扫描电镜图;Fig. 3 is the scanning electron micrograph of the nano-hydroxyapatite loofah composite filler of the embodiment of the present invention;
图4是本发明实施例的纳米羟基磷灰石丝瓜络复合填料填充于多孔悬浮球的示意图;4 is a schematic diagram of nano-hydroxyapatite loofah composite filler filled in porous suspension balls according to an embodiment of the present invention;
图5是本发明实施例的纳米羟基磷灰石丝瓜络复合填料表面形成的外部厌氧、中间缺氧、内部好氧的同步硝化反硝化生物脱氮系统图;Fig. 5 is the synchronous nitrification and denitrification biological denitrification system diagram of the external anaerobic, intermediate anoxic and internal aerobic synchronous nitrification and denitrification formed on the surface of the nano-hydroxyapatite loofah composite filler of the embodiment of the present invention;
图6是本发明实施例的生物反应器的结构示意图;Fig. 6 is the structural representation of the bioreactor of the embodiment of the present invention;
图7是经本发明方法处理前后的丝瓜络对垃圾渗滤液中Pb的去除效果图;Fig. 7 is the figure of removal effect of Pb in landfill leachate by loofah before and after the process of the inventive method;
图8是经本发明方法处理前后的丝瓜络对垃圾渗滤液中Cr的去除效果图。Fig. 8 is a graph showing the removal effect of Cr in landfill leachate by loofah before and after treatment by the method of the present invention.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅用以解释本发明,并不用于限定本发明。In order to make the object, technical solution and advantages of the present invention more clear, the present invention will be further described in detail below in conjunction with the examples. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.
实施例1Example 1
一种纳米羟基磷灰石丝瓜络复合填料的制备方法,所述方法包括以下步骤:A preparation method of nano-hydroxyapatite loofah composite filler, said method comprising the following steps:
参考图1,S1:取含水率为5-10%的丝瓜络浸泡于质量浓度为30%的过氧化氢中,浸泡2h后取出晾干;具体的,可以直接买成品丝瓜络,晾晒至含水率为5-10%,也可以将摘取的丝瓜晾晒至含水率为5-10%后去皮,去籽,去两端后获得丝瓜络;然后将含水率为5-10%的丝瓜络浸泡于质量浓度为30%的过氧化氢中,其目的是去除丝瓜络内的胶质,提升丝瓜络的纤维含量,浸泡2h后取出晾干。Refer to Figure 1, S1: Take a loofah with a water content of 5-10% and soak it in hydrogen peroxide with a mass concentration of 30%, soak it for 2 hours, take it out and dry it; specifically, you can directly buy the finished loofah and dry it until it contains water The water content of the loofah is 5-10%, and the picked loofah can also be dried until the water content is 5-10%, then peeled, removed the seeds, and the two ends are removed to obtain the loofah; then the loofah with the water content of 5-10% Soak in hydrogen peroxide with a mass concentration of 30%. The purpose is to remove the colloid in the loofah and increase the fiber content of the loofah. After soaking for 2 hours, take it out and dry it.
S2:将步骤S1中晾干后的丝瓜络在Ca(NO3)2·4H2O溶液中浸泡8h;具体的,首先,称取Ca(NO3)2·4H2O并用纯净水调至糊状,随后加入温度为60-65℃的水进行搅拌,至Ca(NO3)2·4H2O的浓度为0.0334moL/L;然后将步骤S1中晾干的丝瓜络浸泡在Ca(NO3)2·4H2O溶液中,其目的是使钙离子均匀分布在丝瓜络官能团周围,从而定位生成羟基磷灰石的位点,浸泡8h。S2: Soak the dried loofah in step S1 in Ca(NO 3 ) 2 ·4H 2 O solution for 8 hours; specifically, first, weigh Ca(NO 3 ) 2 ·4H 2 O and adjust to paste, then add water at a temperature of 60-65°C and stir until the concentration of Ca(NO 3 ) 2 4H 2 O is 0.0334moL/L; then soak the dried loofah in step S1 in Ca(NO 3 ) 2 ·4H 2 O 3 ) In 2 ·4H 2 O solution, the purpose is to make the calcium ions evenly distributed around the functional groups of the loofah, so as to locate the site where hydroxyapatite is formed, and soak for 8 hours.
S3:按Ca、P的摩尔比为1.67:1向步骤S2的溶液中滴加磷酸氢二铵,然后采用体积浓度为10-15%的氨水调节pH至9-9.5,搅拌4-5h;具体的,首先配置浓度为0.02moL/L的磷酸氢二铵溶液,然后将配置好的磷酸氢二铵溶液按n(Ca)/n(P)=1.67的比例加入浸泡有丝瓜络的Ca(NO3)2·4H2O溶液中,使磷酸根离子与丝瓜络表面的钙离子结合生成羟基磷灰石,再采用体积浓度为10-15%的氨水调节pH至9-9.5,进行低速搅拌4-4.5h。S3: Add diammonium hydrogen phosphate dropwise to the solution in step S2 according to the molar ratio of Ca and P of 1.67:1, then adjust the pH to 9-9.5 with ammonia water with a volume concentration of 10-15%, and stir for 4-5h; specifically Yes, first prepare the diammonium hydrogen phosphate solution with a concentration of 0.02moL/L, and then add the prepared diammonium hydrogen phosphate solution to the Ca(NO 3 ) In 2.4H 2 O solution, combine phosphate ions with calcium ions on the surface of the loofah to form hydroxyapatite, then use ammonia water with a volume concentration of 10-15% to adjust the pH to 9-9.5, and stir at a low speed for 4 -4.5h.
S4:将步骤S3获得的丝瓜络洗干净后在75-78℃下干燥24h;具体的,清洗丝瓜络所用水为纯净水,烘干是在烘箱中进行。S4: Wash the loofah obtained in step S3 and dry it at 75-78° C. for 24 hours; specifically, the water used for cleaning the loofah is pure water, and the drying is performed in an oven.
S5:重复步骤S2-S4三次后获得纳米羟基磷灰石丝瓜络复合填料。S5: Repeat steps S2-S4 three times to obtain nano-hydroxyapatite loofah composite filler.
为验证本发明方法对丝瓜络的改性效果,将丝瓜络原料及本发明制备的纳米羟基磷灰石丝瓜络复合填料在SEM下进行观察,结果见图2和图3,从图中可以看出,通过本发明方法改性后的纳米羟基磷灰石丝瓜络复合填料表面已明显形成了多孔的羟基磷灰石附着材料,孔径清晰,大小分布均匀,大幅度增加了吸附的比表面积。For verifying the modification effect of the inventive method to loofah, the nano-hydroxyapatite loofah composite filler prepared by the loofah raw material and the present invention is observed under SEM, the results are shown in Fig. 2 and Fig. 3, as can be seen from the figure It is found that porous hydroxyapatite attachment material has been obviously formed on the surface of the nano-hydroxyapatite loofah composite filler modified by the method of the present invention, the pore diameter is clear, the size distribution is uniform, and the specific surface area for adsorption is greatly increased.
实施例2Example 2
采用图6所示的生物反应器对某垃圾焚烧厂的垃圾渗滤液进行处理,生物反应器中所用填料为实施例1制备的纳米羟基磷灰石丝瓜络复合填料,首先将纳米羟基磷灰石丝瓜络复合填料裁剪为边长为80mm的正方形,然后填入φ100的PP多孔悬浮球中,各多孔悬浮球之间采用纱线连接,如图4所示。The bioreactor shown in Figure 6 is used to treat the landfill leachate of a waste incineration plant. The filler used in the bioreactor is the nano-hydroxyapatite loofah composite filler prepared in Example 1. First, the nano-hydroxyapatite The loofah composite filler is cut into a square with a side length of 80mm, and then filled into PP porous suspension balls of φ100, and the porous suspension balls are connected by yarn, as shown in Figure 4.
经分析,垃圾渗滤液中COD值较高,B/C比为0.22,可生化性较差,水质如表1。After analysis, the COD value in the landfill leachate is high, the B/C ratio is 0.22, and the biodegradability is poor. The water quality is shown in Table 1.
表1 垃圾渗滤液水质情况表Table 1 Water quality of landfill leachate
从表1可以看出,垃圾渗滤液中主要的重金属污染为Cr和Pb,故采用本发明的纳米羟基磷灰石丝瓜络复合填料和为未经过本发明方法处理的丝瓜络原料,分别填充相同数量的多孔悬浮球,对垃圾渗滤液中的Cr和Pb进行对比吸附实验。As can be seen from Table 1, the main heavy metal pollution in the landfill leachate is Cr and Pb, so the nano-hydroxyapatite loofah composite filler of the present invention and the loofah raw material not processed by the method of the present invention are used to fill the same Quantity of porous suspension balls for comparative adsorption experiments on Cr and Pb in landfill leachate.
调节垃圾渗滤液的pH为6.5-7.5,在连续曝气下分别吸附30min、1h、2h、4h、8h、12h、24h、48h下,考察经过本发明方法处理前后的丝瓜络对垃圾渗滤液中Cr和Pb的吸附效果,实验效果如图7所示,从图7中可以看出,采用本发明方法制备的纳米羟基磷灰石丝瓜络复合填料对垃圾渗滤液中Pb的最佳吸附率高达59%,较丝瓜络原料的最佳吸附率17.15%,提高了41.85%;经吸附后的出水中,Pb浓度低至0.098mg/L。能满足《城镇污水处理厂污染物排放标准》(GB 18918-2002 )一级A标准。Adjust the pH of landfill leachate to be 6.5-7.5, under continuous aeration, absorb respectively 30min, 1h, 2h, 4h, 8h, 12h, 24h, 48h, investigate the effect of loofah before and after the process of the inventive method on landfill leachate The adsorption effect of Cr and Pb, the experimental effect is as shown in Figure 7, as can be seen from Figure 7, the nano-hydroxyapatite loofah composite filler prepared by the method of the present invention has an optimal adsorption rate of Pb in landfill leachate up to 59%, which is 41.85% higher than the best adsorption rate of loofah raw material 17.15%; the concentration of Pb in the effluent after adsorption is as low as 0.098mg/L. It can meet the first-level A standard of "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002).
从图8中可以看出,采用本发明方法制备的纳米羟基磷灰石丝瓜络复合填料对垃圾渗滤液中Cr的最佳吸附率高达92.31%,较丝瓜络原料的最佳吸附率57.69%,提高了34.7%;经吸附后的出水Cr浓度低至0.02mg/L。能满足《城镇污水处理厂污染物排放标准》(GB 18918-2002 )一级A标准。As can be seen from Figure 8, the nano-hydroxyapatite loofah composite filler prepared by the method of the present invention has an optimal adsorption rate of Cr in landfill leachate up to 92.31%, which is 57.69% higher than the optimal adsorption rate of the loofah raw material. Increased by 34.7%; the concentration of Cr in the effluent after adsorption is as low as 0.02mg/L. It can meet the first-level A standard of "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002).
以本发明方法制备的纳米羟基磷灰石丝瓜络复合材料作为生物反应器的填料,有效解决了垃圾渗滤液中重金属预处理的问题,减少了工程设备,缩短了水力停留时间(HRT);解决了传统吸附法处理重金属会产生大量含重金属污泥,污泥处理成本高的难题。The nano-hydroxyapatite loofah composite material prepared by the method of the present invention is used as the filler of the bioreactor, which effectively solves the problem of heavy metal pretreatment in landfill leachate, reduces engineering equipment, and shortens the hydraulic retention time (HRT); It solves the problem that the traditional adsorption method will produce a large amount of heavy metal-containing sludge and the cost of sludge treatment is high.
如图5所示,本发明利用丝瓜络的多孔多级结构,实现了一体化同步硝化反硝化,用一个反应池代替了传统的A2/O池,不仅减少了池体大小,简化了设备,还减少了能耗,降低了成本,另外,同步硝化反硝化的脱氮效果较好,规避了老旧垃圾填埋场渗滤液C/N比不足问题,避免了运行难或需加入C源的问题,同时,丝瓜络由65.5%的纤维素、17.5%的半纤维素和15.2%的木质素构成,可作为部分C源供给硝化菌和反硝化菌代谢繁殖;丝瓜络为农村固体废物,价格低,以此作为原材料制备的复合材料为环境友好型、低成本材料。且微生物降解丝瓜络中的木质素,能实的丝瓜络的资源化和减量化。As shown in Figure 5, the present invention utilizes the porous multi-level structure of loofah to realize integrated synchronous nitrification and denitrification, and replaces the traditional A2/O pool with a reaction pool, which not only reduces the pool size, simplifies the equipment, It also reduces energy consumption and cost. In addition, the denitrification effect of synchronous nitrification and denitrification is better, avoiding the problem of insufficient C/N ratio of leachate in old landfills, and avoiding difficult operation or the need to add C source Problem, at the same time, loofah is composed of 65.5% cellulose, 17.5% hemicellulose and 15.2% lignin, which can be used as part of the C source to supply nitrifying bacteria and denitrifying bacteria for metabolic reproduction; loofah is rural solid waste, the price Low, the composite material prepared as a raw material is environmentally friendly and low-cost material. Moreover, microorganisms degrade the lignin in the loofah, which can realize the resource utilization and reduction of the loofah.
以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the protection of the present invention. within range.
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