CN111499000B - A kind of artificial wetland filler and preparation method thereof - Google Patents
A kind of artificial wetland filler and preparation method thereof Download PDFInfo
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- 239000000945 filler Substances 0.000 title claims description 43
- 238000002360 preparation method Methods 0.000 title claims description 35
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 78
- 239000003463 adsorbent Substances 0.000 claims description 73
- 239000000243 solution Substances 0.000 claims description 51
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 42
- 229910052698 phosphorus Inorganic materials 0.000 claims description 42
- 239000011574 phosphorus Substances 0.000 claims description 42
- 229910052757 nitrogen Inorganic materials 0.000 claims description 39
- 239000002893 slag Substances 0.000 claims description 34
- 238000003756 stirring Methods 0.000 claims description 30
- 239000010802 sludge Substances 0.000 claims description 27
- 241000609240 Ambelania acida Species 0.000 claims description 26
- 239000010905 bagasse Substances 0.000 claims description 26
- 239000000203 mixture Substances 0.000 claims description 24
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 239000000440 bentonite Substances 0.000 claims description 17
- 229910000278 bentonite Inorganic materials 0.000 claims description 17
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims description 17
- 239000010881 fly ash Substances 0.000 claims description 17
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 15
- 239000011324 bead Substances 0.000 claims description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
- 239000012190 activator Substances 0.000 claims description 12
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 10
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims description 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 10
- 238000000227 grinding Methods 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 10
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims description 10
- 239000007974 sodium acetate buffer Substances 0.000 claims description 10
- BHZOKUMUHVTPBX-UHFFFAOYSA-M sodium acetic acid acetate Chemical compound [Na+].CC(O)=O.CC([O-])=O BHZOKUMUHVTPBX-UHFFFAOYSA-M 0.000 claims description 10
- 238000001179 sorption measurement Methods 0.000 claims description 10
- 238000001035 drying Methods 0.000 claims description 9
- 241000894006 Bacteria Species 0.000 claims description 8
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 7
- 229920005552 sodium lignosulfonate Polymers 0.000 claims description 7
- ICAKDTKJOYSXGC-UHFFFAOYSA-K lanthanum(iii) chloride Chemical compound Cl[La](Cl)Cl ICAKDTKJOYSXGC-UHFFFAOYSA-K 0.000 claims description 6
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 5
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 5
- 229920002472 Starch Polymers 0.000 claims description 5
- 229930003270 Vitamin B Natural products 0.000 claims description 5
- VYLVYHXQOHJDJL-UHFFFAOYSA-K cerium trichloride Chemical compound Cl[Ce](Cl)Cl VYLVYHXQOHJDJL-UHFFFAOYSA-K 0.000 claims description 5
- 239000008103 glucose Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 5
- 239000008107 starch Substances 0.000 claims description 5
- 235000019698 starch Nutrition 0.000 claims description 5
- 235000019156 vitamin B Nutrition 0.000 claims description 5
- 239000011720 vitamin B Substances 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 4
- 235000021355 Stearic acid Nutrition 0.000 claims description 2
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 2
- 239000008117 stearic acid Substances 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 230000003213 activating effect Effects 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 230000000052 comparative effect Effects 0.000 description 8
- 238000001914 filtration Methods 0.000 description 6
- 239000010865 sewage Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 241000233866 Fungi Species 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000008394 flocculating agent Substances 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000009920 chelation Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003653 coastal water Substances 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Classifications
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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
- C02F3/32—Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
-
- 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
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
-
- 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
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
- C02F2003/003—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms using activated carbon or the like
-
- 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
- C02F2101/105—Phosphorus compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
-
- 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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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Botany (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明公开了一种人工湿地填料及其制备方法,属于环境保护技术领域。其包括:按重量份计,活性污泥50‑100份、高炉渣10‑40份、碳渣1‑20份、膨润土1‑10份、氮吸附剂1‑5份和磷吸附剂1‑5份。本发明原料价格低廉,容易获得,制备简单、制成的填料具有强度大,硬度高、不易分解,透水性好,对磷和氮的吸附性强的优点。The invention discloses a constructed wetland filler and a preparation method thereof, belonging to the technical field of environmental protection. It includes: by weight, 50-100 parts of activated sludge, 10-40 parts of blast furnace slag, 1-20 parts of carbon slag, 1-10 parts of bentonite, 1-5 parts of nitrogen adsorbent and 1-5 parts of phosphorus adsorbent share. The raw material of the invention is cheap, easy to obtain, simple to prepare, and the prepared filler has the advantages of high strength, high hardness, not easy to decompose, good water permeability, and strong adsorption to phosphorus and nitrogen.
Description
技术领域technical field
本发明涉及环境保护技术领域,具体涉及一种人工湿地填料及其制备方法。The invention relates to the technical field of environmental protection, in particular to a constructed wetland filler and a preparation method thereof.
背景技术Background technique
目前我国水环境状况日趋恶化,出现了湖泊富营养化、近岸海域赤潮、河流和水库的有机污染等问题,威胁到居民的引水安全和人民群众的健康。人工湿地填料处理由于其具有水质净化效果好、基建运行费用低、能耗低、维护管理简单、抗冲击负荷能力强等特点,而且能够为野生动物提供栖息地、提高生态景观的美学价值,所以在生活污水、工业废水、农业面源污水、城市暴雨径流和富营养化水体等方面均得到了广泛的应用。但是,从已有的工程实践来看,人工湿地填料脱氮脱磷能力弱。At present, my country's water environment is deteriorating day by day, with problems such as eutrophication of lakes, red tides in coastal waters, and organic pollution of rivers and reservoirs, threatening the safety of water diversion for residents and the health of the people. Constructed wetland filler treatment has the characteristics of good water purification effect, low infrastructure operation cost, low energy consumption, simple maintenance and management, strong shock load resistance, etc., and can provide habitat for wild animals and improve the aesthetic value of ecological landscape, so It has been widely used in domestic sewage, industrial wastewater, agricultural non-point source sewage, urban storm runoff and eutrophic water bodies. However, according to the existing engineering practice, the denitrification and dephosphorization ability of constructed wetland packing is weak.
发明内容SUMMARY OF THE INVENTION
本发明的目的是提供一种人工湿地填料及其制备方法,以解决现有人工湿地填料脱氮脱磷能力弱的问题。The purpose of the present invention is to provide a constructed wetland filler and a preparation method thereof, so as to solve the problem of weak denitrification and dephosphorization capability of the existing constructed wetland filler.
本发明解决上述技术问题的技术方案如下:The technical scheme that the present invention solves the above-mentioned technical problems is as follows:
一种人工湿地填料,包括:按重量份计,活性污泥50-100份、高炉渣10-40份、粉煤灰1-20份、膨润土1-10份、氮吸附剂1-5份和磷吸附剂1-5份。A constructed wetland filler, comprising: by weight, 50-100 parts of activated sludge, 10-40 parts of blast furnace slag, 1-20 parts of fly ash, 1-10 parts of bentonite, 1-5 parts of nitrogen adsorbent and Phosphorus adsorbent 1-5 parts.
本发明采用的活性污泥为污水处理厂的污泥脱水环节留下来的,其中含有大量的絮凝剂,主要有PAM和PAC,这些絮凝剂保留在污泥中。因此,本发明采用的活性污泥中含有大量残留的有效絮凝成分,这些活性成分可以对人工湿地起到吸附污染物和净化污水的作用。并且将污水处理厂中残留下的污泥废渣支撑填料,对剩余污泥难处理问题,实现了“以废治废”、“变废为宝”的环境治理理念。The activated sludge used in the present invention is left over from the sludge dewatering process of the sewage treatment plant, and contains a large amount of flocculants, mainly PAM and PAC, and these flocculants are retained in the sludge. Therefore, the activated sludge used in the present invention contains a large amount of residual effective flocculation components, and these active components can play the role of adsorbing pollutants and purifying sewage on the constructed wetland. In addition, the sludge residue left in the sewage treatment plant is used to support the filler, which is difficult to deal with the remaining sludge, and realizes the environmental governance concept of "treating waste with waste" and "turning waste into treasure".
在本申请的填料中,活性污泥含有的大量的有效絮凝成分,能够高效截留水体中的氮、磷元素,供种植在其上方土壤层植物生长所用。并通过高炉渣、膨润土和粉煤灰作为辅助填料,使得填料具有表面粗糙、孔隙率高、微孔结构分布均匀、比表面积大、机械强度较高的优点,可以改善人工湿地的水力学性能,为微生物提供更大的附着面积,增强系统对污染物去除效率的同时,也能防止湿地堵塞。并通过加入氮吸附剂和磷吸附剂,优化填料对氮磷的吸附效果,其除磷除氮吸附容量远远大于目前常用吸附材料,延长了填料的使用寿命,降低了因需置换带来的高额成本。In the filler of the present application, the activated sludge contains a large amount of effective flocculation components, which can efficiently retain nitrogen and phosphorus elements in the water body for the growth of plants planted in the soil layer above it. By using blast furnace slag, bentonite and fly ash as auxiliary fillers, the fillers have the advantages of rough surface, high porosity, uniform distribution of microporous structure, large specific surface area and high mechanical strength, which can improve the hydraulic performance of constructed wetlands. Provides a larger attachment area for microorganisms, enhances the system's removal efficiency of pollutants, and also prevents wetland clogging. And by adding nitrogen adsorbent and phosphorus adsorbent, the adsorption effect of the filler on nitrogen and phosphorus is optimized. high cost.
进一步地,在本发明较佳的实施例中,上述人工湿地填料,包括:按重量份计,活性污泥60-80份、高炉渣20-30份、粉煤灰5-15份、膨润土3-7份、氮吸附剂1-5份和磷吸附剂1-5份。Further, in a preferred embodiment of the present invention, the above-mentioned constructed wetland fillers include: by weight, 60-80 parts of activated sludge, 20-30 parts of blast furnace slag, 5-15 parts of fly ash, and 3 parts of bentonite. -7 parts, 1-5 parts nitrogen adsorbent and 1-5 parts phosphorus adsorbent.
进一步地,在本发明较佳的实施例中,上述活性污泥含水量低于60%。Further, in a preferred embodiment of the present invention, the water content of the activated sludge is lower than 60%.
进一步地,在本发明较佳的实施例中,上述氮吸附剂的制备方法包括以下步骤:Further, in a preferred embodiment of the present invention, the preparation method of the above-mentioned nitrogen adsorbent comprises the following steps:
(ⅰ)将木质素磺酸钠和活性炭按质量为(80-100):1溶解在乙酸溶液中配制成1-10wt%溶液后,滴加到浓度为10-20wt%氢氧化钠溶液中,搅拌、过滤得到珠体;(i) Dissolve sodium lignosulfonate and activated carbon in an acetic acid solution with a mass of (80-100):1 to prepare a 1-10wt% solution, and then add dropwise to a sodium hydroxide solution with a concentration of 10-20wt%, Stir and filter to obtain beads;
(ⅱ)将珠体加入浓度为1-5g/mL氯化镧水溶液中浸泡,并在30-50℃下充分吸附,过滤后加入到环氧氯丙烷中,调节pH至8-10,再加入过硫酸钾,在50-70℃温度下反应3-5h,制得氮吸附剂;(ii) Soak the beads in an aqueous solution of lanthanum chloride with a concentration of 1-5g/mL, fully absorb them at 30-50°C, filter and add them to epichlorohydrin, adjust the pH to 8-10, and then add Potassium persulfate, react at 50-70℃ for 3-5h to obtain nitrogen adsorbent;
其中,珠体、环氧氯丙烷和过硫酸钾的质量比为:1:(6-8):(0.01-0.02)。Wherein, the mass ratio of beads, epichlorohydrin and potassium persulfate is: 1:(6-8):(0.01-0.02).
进一步地,在本发明较佳的实施例中,上述磷吸附剂的制备方法包括以下步骤:Further, in a preferred embodiment of the present invention, the preparation method of the above-mentioned phosphorus adsorbent comprises the following steps:
(ⅰ)将活化甘蔗渣在浓度为3-7g/mL的氯化铈溶液中浸渍,调节pH至10-12,搅拌反应1-2h,经乙醇清洗烘干后,制得初始吸附剂;(i) immersing the activated bagasse in a cerium chloride solution with a concentration of 3-7g/mL, adjusting the pH to 10-12, stirring and reacting for 1-2h, washing and drying with ethanol to obtain the initial adsorbent;
(ⅱ)将初始吸附剂浸渍在浓度为1-2g/mL的纳米二氧化锆水溶液中,经过滤、洗涤、干燥后,在300-600℃温度下焙烧2-3h,制得磷吸附剂。(ii) Immerse the initial adsorbent in an aqueous solution of nano-zirconia with a concentration of 1-2 g/mL, filter, wash and dry, and then calcinate at a temperature of 300-600 °C for 2-3 hours to obtain a phosphorus adsorbent.
进一步地,在本发明较佳的实施例中,上述步骤(ⅰ)中活化甘蔗渣的制备步骤包括:将甘蔗渣加入培养液中,向培养液中加入乙酸-乙酸钠缓冲液,调节pH至3后加入白腐菌,于30℃-35℃温度下反应36h-45h,取出、烘干并粉碎至粒径为50目,得到改性甘蔗渣;其中甘蔗渣、培养液以及白腐菌的质量比为1:(10-12):(3-5);乙酸-乙酸钠缓冲液的加入量为培养液的10wt%-20wt%;培养液包括以下重量份的组分:酵母粉2份、维生素B10.4份、葡萄糖1.5份、可溶性淀粉1.5份、KH2PO40.2份和MgSO4·7H2O0.5份。Further, in a preferred embodiment of the present invention, the preparation step of the activated bagasse in the above step (i) includes: adding the bagasse into the culture solution, adding acetic acid-sodium acetate buffer to the culture solution, and adjusting the pH to 3. After adding white rot fungi, react at 30°C-35°C for 36h-45h, take out, dry and pulverize to a particle size of 50 meshes to obtain modified bagasse; among them, the bagasse, culture solution and white rot fungi are The mass ratio is 1:(10-12):(3-5); the addition amount of acetic acid-sodium acetate buffer is 10wt%-20wt% of the culture solution; the culture solution includes the following components by weight: 2 parts of yeast powder , 10.4 parts of vitamin B, 1.5 parts of glucose, 1.5 parts of soluble starch, 0.2 part of KH 2 PO 4 and 0.5 part of MgSO 4 ·7H 2 O.
上述的人工湿地填料的制备方法,包括以下步骤:The preparation method of the above-mentioned constructed wetland filler, comprises the following steps:
(1)对粒径小于200nm的高炉渣进行充分研磨后,加入活化剂搅拌混合均匀后,在400-600℃下焙烧0.5-1h;高炉渣与活化剂加入的质量比为(100-150):1;(1) After fully grinding the blast furnace slag with a particle size of less than 200nm, add the activator and stir and mix evenly, then roast at 400-600 ℃ for 0.5-1h; the mass ratio of blast furnace slag and activator added is (100-150) :1;
(2)将煅烧后的高炉渣再次研磨后,加水混合均匀,从室温升温至80-90℃后保温1-3h后,再在70-90℃温度下烘干;(2) After grinding the calcined blast furnace slag again, add water to mix evenly, heat up from room temperature to 80-90 °C, keep it for 1-3 hours, and then dry it at 70-90 °C;
(3)将硬酸脂溶解在乙醚中,水浴加热使其完全溶解配制成0.01-0.05g/mL的溶液,加入步骤(2)烘干后的高炉渣、膨润土和粉煤灰搅拌混合均匀,制得混合料;(3) Dissolving stearic acid in ether, heating it in a water bath to make it completely dissolved to prepare a solution of 0.01-0.05g/mL, adding the blast furnace slag, bentonite and fly ash after drying in step (2), stirring and mixing evenly, prepared mixture;
(4)向混合料中加入氮吸附剂和磷吸附剂充分搅拌混合均匀后,与活动污泥搅拌混合均匀,经压制成型后风干,制得人工湿地填料。(4) Add nitrogen adsorbent and phosphorus adsorbent to the mixture, stir and mix evenly, and stir and mix with activated sludge evenly, press and shape, and then air-dry to obtain a constructed wetland filler.
进一步地,在本发明较佳的实施例中,上述步骤(1)中的活化剂为氢氧化钠。Further, in a preferred embodiment of the present invention, the activator in the above step (1) is sodium hydroxide.
本发明具有以下有益效果:The present invention has the following beneficial effects:
1、本发明的氮吸附剂中加入的活性炭,具有较强的吸附性和催化性能,对水中溶解的有机污染物和某些有毒的重金属具有较强的吸附能力;加入的木质素磺酸钠含有大量的直链和极性基团,可提高对氨氮的吸附。并且还通过加入氯化镧作为改性剂,辅助提高活性碳和木质素磺酸钠对氮的吸附能力,从而提高氮吸附剂提高对氮的吸附效果。1. The activated carbon added in the nitrogen adsorbent of the present invention has strong adsorption and catalytic performance, and has strong adsorption capacity to organic pollutants dissolved in water and some toxic heavy metals; the added sodium lignosulfonate Contains a large number of linear and polar groups, which can improve the adsorption of ammonia nitrogen. In addition, by adding lanthanum chloride as a modifier, the adsorption capacity of activated carbon and sodium lignosulfonate for nitrogen is assisted to improve, thereby improving the nitrogen adsorption effect of the nitrogen adsorbent.
2、本发明通过制成生物炭基的磷吸附剂,提供磷吸附剂对环境的适应性,加入纳米二氧化锆,纳米二氧化锆主要通过螯合作用、共价键或配位键与磷酸根结合固定在磷吸附剂表面,提高对磷的吸附效果。2. The present invention provides the adaptability of the phosphorus adsorbent to the environment by making a biochar-based phosphorus adsorbent, adding nano zirconium dioxide, and the nano zirconium dioxide mainly interacts with phosphoric acid through chelation, covalent bonds or coordination bonds. The roots are bound and fixed on the surface of the phosphorus adsorbent to improve the adsorption effect of phosphorus.
3、本发明原料价格低廉,容易获得,制备简单、制成的填料具有强度大,硬度高、不易分解,透水性好,对磷和氮的吸附性强的优点。3. The raw materials of the present invention are cheap, easy to obtain, simple to prepare, and the prepared filler has the advantages of high strength, high hardness, not easy to decompose, good water permeability, and strong adsorption to phosphorus and nitrogen.
具体实施方式Detailed ways
以下结合实施例对本发明的原理和特征进行描述,所举实例只用于解释本发明,并非用于限定本发明的范围。实施例中未注明具体条件者,按照常规条件或制造商建议的条件进行。所用试剂或仪器未注明生产厂商者,均为可以通过市售购买获得的常规产品。The principles and features of the present invention will be described below with reference to the embodiments. The examples are only used to explain the present invention, but not to limit the scope of the present invention. If the specific conditions are not indicated in the examples, it is carried out according to the conventional conditions or the conditions suggested by the manufacturer. The reagents or instruments used without the manufacturer's indication are conventional products that can be purchased from the market.
实施例1:Example 1:
本实施例的人工湿地填料包括:按重量份计,活性污泥50份、高炉渣10份、粉煤灰1份、膨润土1份、氮吸附剂1份和磷吸附剂1份。The constructed wetland filler in this embodiment includes: by weight, 50 parts of activated sludge, 10 parts of blast furnace slag, 1 part of fly ash, 1 part of bentonite, 1 part of nitrogen adsorbent and 1 part of phosphorus adsorbent.
其中,氮吸附剂的制备方法包括以下步骤:Wherein, the preparation method of nitrogen adsorbent comprises the following steps:
(ⅰ)将木质素磺酸钠和活性炭按质量为80:1溶解在乙酸溶液中配制成1wt%溶液后,滴加到浓度为10wt%氢氧化钠溶液中,搅拌、过滤得到珠体;(i) dissolving sodium lignosulfonate and activated carbon in an acetic acid solution at a mass ratio of 80:1 to prepare a 1wt% solution, then adding dropwise to a sodium hydroxide solution with a concentration of 10wt%, stirring and filtering to obtain beads;
(ⅱ)将珠体加入浓度为1g/mL氯化镧水溶液中浸泡,并在30℃下充分吸附,过滤后加入到环氧氯丙烷中,调节pH至8,再加入过硫酸钾,在50℃温度下反应3-5h,制得氮吸附剂;(ii) The beads were soaked in an aqueous solution of lanthanum chloride with a concentration of 1 g/mL, and fully adsorbed at 30 °C. After filtration, they were added to epichlorohydrin, adjusted to pH 8, and then potassium persulfate was added. React at ℃ temperature for 3-5h to obtain nitrogen adsorbent;
其中,珠体、环氧氯丙烷和过硫酸钾的质量比为:1:6:0.01。Wherein, the mass ratio of beads, epichlorohydrin and potassium persulfate is: 1:6:0.01.
磷吸附剂的制备方法包括以下步骤:The preparation method of phosphorus adsorbent comprises the following steps:
(ⅰ)将活化甘蔗渣在浓度为3g/mL的氯化铈溶液中浸渍,调节pH至10,搅拌反应1h,经乙醇清洗烘干后,制得初始吸附剂;活化甘蔗渣的制备步骤包括:将甘蔗渣加入培养液中,向培养液中加入乙酸-乙酸钠缓冲液,调节pH至3后加入白腐菌,于30℃温度下反应36h,取出、烘干并粉碎至粒径为50目,得到改性甘蔗渣;其中甘蔗渣、培养液以及白腐菌的质量比为1:10:3;乙酸-乙酸钠缓冲液的加入量为培养液的10wt%;培养液包括以下重量份的组分:酵母粉2份、维生素B10.4份、葡萄糖1.5份、可溶性淀粉1.5份、KH2PO40.2份和MgSO4·7H2O0.5份。(i) Immerse the activated bagasse in a cerium chloride solution with a concentration of 3 g/mL, adjust the pH to 10, stir and react for 1 hour, wash and dry with ethanol to obtain an initial adsorbent; the preparation steps of the activated bagasse include: : Add bagasse into the culture solution, add acetic acid-sodium acetate buffer to the culture solution, adjust the pH to 3, add white rot bacteria, react at 30°C for 36h, take out, dry and pulverize until the particle size is 50 To obtain modified bagasse; wherein the mass ratio of bagasse, culture solution and white rot bacteria is 1:10:3; the addition of acetic acid-sodium acetate buffer is 10wt% of the culture solution; the culture solution includes the following parts by weight Ingredients: 2 parts of yeast powder, 10.4 parts of vitamin B, 1.5 parts of glucose, 1.5 parts of soluble starch, 0.2 part of KH 2 PO 4 and 0.5 part of MgSO 4 ·7H 2 O .
(ⅱ)将初始吸附剂浸渍在浓度为1g/mL的纳米二氧化锆水溶液中,经过滤、洗涤、干燥后,在300℃温度下焙烧2h,制得磷吸附剂。(ii) The initial adsorbent was immersed in an aqueous solution of nano-zirconia with a concentration of 1 g/mL, filtered, washed and dried, and then calcined at 300°C for 2 hours to obtain a phosphorus adsorbent.
本实施例的人工湿地填料的制备方法的制备方法,包括以下步骤:The preparation method of the preparation method of the constructed wetland filler of the present embodiment comprises the following steps:
(1)对粒径为150nm的高炉渣进行充分研磨后,加入活化剂搅拌混合均匀后,在400℃下焙烧0.5h;高炉渣与活化剂加入的质量比为100:1;(1) After fully grinding the blast furnace slag with a particle size of 150nm, adding an activator and stirring to mix it uniformly, roasting at 400 ° C for 0.5h; the mass ratio of blast furnace slag and activator added is 100:1;
(2)将煅烧后的高炉渣再次研磨后,加水混合均匀,从室温升温至80℃后保温1h后,再在70℃温度下烘干;(2) After grinding the calcined blast furnace slag again, add water to mix evenly, heat it up from room temperature to 80°C, hold it for 1 hour, and then dry it at 70°C;
(3)将硬酸脂溶解在乙醚中,水浴加热使其完全溶解配制成0.01g/mL的溶液,加入步骤(2)烘干后的高炉渣、膨润土和粉煤灰搅拌混合均匀,制得混合料;(3) Dissolving stearate in ether, heating it in a water bath to make it completely dissolved to prepare a solution of 0.01 g/mL, adding the blast furnace slag, bentonite and fly ash after drying in step (2), stirring and mixing evenly to obtain the Mixture;
(4)向混合料中加入氮吸附剂和磷吸附剂充分搅拌混合均匀后,与活动污泥搅拌混合均匀,经压制成型后风干,制得人工湿地填料。(4) Add nitrogen adsorbent and phosphorus adsorbent to the mixture, stir and mix evenly, and stir and mix with activated sludge evenly, press and shape, and then air-dry to obtain a constructed wetland filler.
实施例2:Example 2:
本实施例的人工湿地填料包括:按重量份计,活性污泥60份、高炉渣20份、粉煤灰5份、膨润土3份、氮吸附剂2份和磷吸附剂2份。The constructed wetland filler in this embodiment includes: by weight, 60 parts of activated sludge, 20 parts of blast furnace slag, 5 parts of fly ash, 3 parts of bentonite, 2 parts of nitrogen adsorbent and 2 parts of phosphorus adsorbent.
其中,氮吸附剂的制备方法包括以下步骤:Wherein, the preparation method of nitrogen adsorbent comprises the following steps:
(ⅰ)将木质素磺酸钠和活性炭按质量为90:1溶解在乙酸溶液中配制成5wt%溶液后,滴加到浓度为15wt%氢氧化钠溶液中,搅拌、过滤得到珠体;(i) dissolving sodium lignosulfonate and activated carbon in an acetic acid solution at a mass ratio of 90:1 to prepare a 5wt% solution, then adding dropwise to a sodium hydroxide solution with a concentration of 15wt%, stirring and filtering to obtain beads;
(ⅱ)将珠体加入浓度为3g/mL氯化镧水溶液中浸泡,并在40℃下充分吸附,过滤后加入到环氧氯丙烷中,调节pH至9,再加入过硫酸钾,在60℃温度下反应4h,制得氮吸附剂;(ii) Soak the beads in an aqueous solution of lanthanum chloride with a concentration of 3g/mL, and fully absorb them at 40°C. After filtration, add them to epichlorohydrin, adjust the pH to 9, and then add potassium persulfate at 60°C. Reaction at ℃ temperature for 4h to obtain nitrogen adsorbent;
其中,珠体、环氧氯丙烷和过硫酸钾的质量比为:1:7:0.015。Wherein, the mass ratio of beads, epichlorohydrin and potassium persulfate is: 1:7:0.015.
磷吸附剂的制备方法包括以下步骤:The preparation method of phosphorus adsorbent comprises the following steps:
(ⅰ)将活化甘蔗渣在浓度为5g/mL的氯化铈溶液中浸渍,调节pH至11,搅拌反应1.5h,经乙醇清洗烘干后,制得初始吸附剂;活化甘蔗渣的制备步骤包括:将甘蔗渣加入培养液中,向培养液中加入乙酸-乙酸钠缓冲液,调节pH至3后加入白腐菌,于32℃温度下反应40h,取出、烘干并粉碎至粒径为50目,得到改性甘蔗渣;其中甘蔗渣、培养液以及白腐菌的质量比为1:11:4;乙酸-乙酸钠缓冲液的加入量为培养液的15wt%;培养液包括以下重量份的组分:酵母粉2份、维生素B10.4份、葡萄糖1.5份、可溶性淀粉1.5份、KH2PO40.2份和MgSO4·7H2O0.5份。(i) Immerse the activated bagasse in a cerium chloride solution with a concentration of 5 g/mL, adjust the pH to 11, stir and react for 1.5 hours, wash and dry with ethanol to obtain the initial adsorbent; the preparation steps of the activated bagasse The method includes: adding bagasse into the culture solution, adding acetic acid-sodium acetate buffer to the culture solution, adjusting the pH to 3, adding white rot bacteria, reacting at 32°C for 40 hours, taking out, drying and crushing to a particle size of 50 meshes to obtain modified bagasse; wherein the mass ratio of bagasse, culture solution and white rot bacteria is 1:11:4; the addition of acetic acid-sodium acetate buffer is 15wt% of the culture solution; the culture solution includes the following weights The components of the serving: 2 parts of yeast powder, 10.4 parts of vitamin B, 1.5 parts of glucose, 1.5 parts of soluble starch, 0.2 part of KH 2 PO 4 and 0.5 part of MgSO 4 ·7H 2 O.
(ⅱ)将初始吸附剂浸渍在浓度为1.5g/mL的纳米二氧化锆水溶液中,经过滤、洗涤、干燥后,在450℃温度下焙烧3h,制得磷吸附剂。(ii) The initial adsorbent was immersed in an aqueous solution of nano-zirconia with a concentration of 1.5 g/mL, filtered, washed and dried, and then calcined at 450°C for 3 hours to obtain a phosphorus adsorbent.
本实施例的人工湿地填料的制备方法的制备方法,包括以下步骤:The preparation method of the preparation method of the constructed wetland filler of the present embodiment comprises the following steps:
(1)对粒径为150nm的高炉渣进行充分研磨后,加入活化剂搅拌混合均匀后,在500℃下焙烧1h;高炉渣与活化剂加入的质量比为120:1;(1) After fully grinding the blast furnace slag with a particle size of 150nm, adding an activator and stirring to mix it uniformly, roasting at 500 °C for 1 hour; the mass ratio of blast furnace slag and activator added is 120:1;
(2)将煅烧后的高炉渣再次研磨后,加水混合均匀,从室温升温至85℃后保温2h后,再在80℃温度下烘干;(2) After grinding the calcined blast furnace slag again, add water to mix evenly, heat it up from room temperature to 85°C, keep it for 2 hours, and then dry it at 80°C;
(3)将硬酸脂溶解在乙醚中,水浴加热使其完全溶解配制成0.03g/mL的溶液,加入步骤(2)烘干后的高炉渣、膨润土和粉煤灰搅拌混合均匀,制得混合料;(3) Dissolving stearate in ether, heating it in a water bath to make it completely dissolved to prepare a solution of 0.03 g/mL, adding the blast furnace slag, bentonite and fly ash after drying in step (2), stirring and mixing evenly to obtain the Mixture;
(4)向混合料中加入氮吸附剂和磷吸附剂充分搅拌混合均匀后,与活动污泥搅拌混合均匀,经压制成型后风干,制得人工湿地填料。(4) Add nitrogen adsorbent and phosphorus adsorbent to the mixture, stir and mix evenly, and stir and mix with activated sludge evenly, press and shape, and then air-dry to obtain a constructed wetland filler.
实施例3:Example 3:
本实施例的人工湿地填料包括:按重量份计,活性污泥70份、高炉渣25份、粉煤灰10份、膨润土5份、氮吸附剂3份和磷吸附剂3份。The constructed wetland filler in this embodiment includes: 70 parts by weight of activated sludge, 25 parts of blast furnace slag, 10 parts of fly ash, 5 parts of bentonite, 3 parts of nitrogen adsorbent and 3 parts of phosphorus adsorbent.
其中,氮吸附剂的制备方法包括以下步骤:Wherein, the preparation method of nitrogen adsorbent comprises the following steps:
(ⅰ)将木质素磺酸钠和活性炭按质量为100:1溶解在乙酸溶液中配制成10wt%溶液后,滴加到浓度为20wt%氢氧化钠溶液中,搅拌、过滤得到珠体;(i) dissolving sodium lignosulfonate and activated carbon in an acetic acid solution with a mass of 100:1 to prepare a 10wt% solution, then adding dropwise to a sodium hydroxide solution with a concentration of 20wt%, stirring and filtering to obtain beads;
(ⅱ)将珠体加入浓度为5g/mL氯化镧水溶液中浸泡,并在50℃下充分吸附,过滤后加入到环氧氯丙烷中,调节pH至10,再加入过硫酸钾,在70℃温度下反应5h,制得氮吸附剂;(ii) Soak the beads in an aqueous solution of lanthanum chloride with a concentration of 5g/mL, and fully absorb them at 50°C. After filtration, add them to epichlorohydrin, adjust the pH to 10, and then add potassium persulfate, at 70 The nitrogen adsorbent was prepared by reacting at ℃ for 5h;
其中,珠体、环氧氯丙烷和过硫酸钾的质量比为:1:8:0.02。Wherein, the mass ratio of beads, epichlorohydrin and potassium persulfate is: 1:8:0.02.
磷吸附剂的制备方法包括以下步骤:The preparation method of phosphorus adsorbent comprises the following steps:
(ⅰ)将活化甘蔗渣在浓度为3-7g/mL的氯化铈溶液中浸渍,调节pH至12,搅拌反应2h,经乙醇清洗烘干后,制得初始吸附剂;甘蔗渣的制备步骤包括:将甘蔗渣加入培养液中,向培养液中加入乙酸-乙酸钠缓冲液,调节pH至3后加入白腐菌,于35℃温度下反应45h,取出、烘干并粉碎至粒径为50目,得到改性甘蔗渣;其中甘蔗渣、培养液以及白腐菌的质量比为1:12:5;乙酸-乙酸钠缓冲液的加入量为培养液的20wt%;培养液包括以下重量份的组分:酵母粉2份、维生素B10.4份、葡萄糖1.5份、可溶性淀粉1.5份、KH2PO40.2份和MgSO4·7H2O0.5份。(i) Immerse the activated bagasse in a cerium chloride solution with a concentration of 3-7g/mL, adjust the pH to 12, stir and react for 2 hours, wash and dry with ethanol to obtain an initial adsorbent; the preparation steps of bagasse Including: adding bagasse into the culture solution, adding acetic acid-sodium acetate buffer to the culture solution, adjusting the pH to 3, adding white rot bacteria, reacting at 35°C for 45 hours, taking out, drying and pulverizing to a particle size of 50 meshes to obtain modified bagasse; wherein the mass ratio of bagasse, culture solution and white rot bacteria is 1:12:5; the addition of acetic acid-sodium acetate buffer is 20wt% of the culture solution; the culture solution includes the following weights The components of the serving: 2 parts of yeast powder, 10.4 parts of vitamin B, 1.5 parts of glucose, 1.5 parts of soluble starch, 0.2 part of KH 2 PO 4 and 0.5 part of MgSO 4 ·7H 2 O.
(ⅱ)将初始吸附剂浸渍在浓度为2g/mL的纳米二氧化锆水溶液中,经过滤、洗涤、干燥后,在600℃温度下焙烧3h,制得磷吸附剂。(ii) The initial adsorbent was immersed in an aqueous solution of nano-zirconia with a concentration of 2 g/mL, filtered, washed and dried, and then calcined at 600°C for 3 hours to obtain a phosphorus adsorbent.
本实施例的人工湿地填料的制备方法的制备方法,包括以下步骤:The preparation method of the preparation method of the constructed wetland filler of the present embodiment comprises the following steps:
(1)对粒径为100nm的高炉渣进行充分研磨后,加入活化剂搅拌混合均匀后,在600℃下焙烧1h;高炉渣与活化剂加入的质量比为150:1;(1) After fully grinding the blast furnace slag with a particle size of 100 nm, add the activator and stir and mix evenly, and then roast at 600 °C for 1 hour; the mass ratio of blast furnace slag and activator added is 150:1;
(2)将煅烧后的高炉渣再次研磨后,加水混合均匀,从室温升温至90℃后保温3h后,再在90℃温度下烘干;(2) After grinding the calcined blast furnace slag again, add water and mix it uniformly, heat it up from room temperature to 90 °C, keep it for 3 hours, and then dry it at 90 °C;
(3)将硬酸脂溶解在乙醚中,水浴加热使其完全溶解配制成0.05g/mL的溶液,加入步骤(2)烘干后的高炉渣、膨润土和粉煤灰搅拌混合均匀,制得混合料;(3) Dissolving stearate in ether, heating it in a water bath to make it completely dissolved to prepare a solution of 0.05 g/mL, adding the blast furnace slag, bentonite and fly ash after drying in step (2), stirring and mixing evenly to obtain the Mixture;
(4)向混合料中加入氮吸附剂和磷吸附剂充分搅拌混合均匀后,与活动污泥搅拌混合均匀,经压制成型后风干,制得人工湿地填料。(4) Add nitrogen adsorbent and phosphorus adsorbent to the mixture, stir and mix evenly, and stir and mix with activated sludge evenly, press and shape, and then air-dry to obtain a constructed wetland filler.
实施例4:Example 4:
本实施例的人工湿地填料包括:按重量份计,活性污泥80份、高炉渣30份、粉煤灰15份、膨润土7份、氮吸附剂4份和磷吸附剂4份。其中,氮吸附剂和磷吸附剂的制备方法与实施例1中的制备方法一致。The constructed wetland filler in this embodiment includes: 80 parts by weight of activated sludge, 30 parts of blast furnace slag, 15 parts of fly ash, 7 parts of bentonite, 4 parts of nitrogen adsorbent and 4 parts of phosphorus adsorbent. Among them, the preparation methods of nitrogen adsorbent and phosphorus adsorbent are the same as those in Example 1.
本实施例的人工湿地填料的制备方法与实施例1相同。The preparation method of the constructed wetland filler in this example is the same as that in Example 1.
实施例5:Example 5:
本实施例的人工湿地填料包括:按重量份计,活性污泥100份、高炉渣40份、粉煤灰20份、膨润土10份、氮吸附剂5份和磷吸附剂5份。其中,氮吸附剂和磷吸附剂的制备方法与实施例1中的制备方法一致。The constructed wetland filler in this embodiment includes: by weight, 100 parts of activated sludge, 40 parts of blast furnace slag, 20 parts of fly ash, 10 parts of bentonite, 5 parts of nitrogen adsorbent and 5 parts of phosphorus adsorbent. Among them, the preparation methods of nitrogen adsorbent and phosphorus adsorbent are the same as those in Example 1.
本实施例的人工湿地填料的制备方法与实施例1相同。The preparation method of the constructed wetland filler in this example is the same as that in Example 1.
对照例1Comparative Example 1
本对照例的人工湿地填料包括:按重量份计,活性污泥70份、高炉渣25份、粉煤灰10份和膨润土5份。The constructed wetland filler in this comparative example includes: by weight, 70 parts of activated sludge, 25 parts of blast furnace slag, 10 parts of fly ash and 5 parts of bentonite.
本对照例的人工湿地填料的制备方法与实施例3的人工湿地填料的制备方法一致。The preparation method of the constructed wetland filler of this comparative example is consistent with the preparation method of the constructed wetland filler of Example 3.
对照例2Comparative Example 2
本对照例的人工湿地填料的配方与实施例3的配方一致,区别在于,制备方法不同。The formula of the constructed wetland filler of this comparative example is the same as that of Example 3, except that the preparation method is different.
本对照例的人工湿地填料的制备方法包括以下步骤:The preparation method of the constructed wetland filler of this comparative example comprises the following steps:
将高炉渣进行研磨,将研磨后的高炉渣、活性污泥、粉煤灰、膨润土、氮吸附剂和磷吸附剂搅拌混合均匀后,经压制成型后风干,制得人工湿地填料。The blast furnace slag is ground, and the ground blast furnace slag, activated sludge, fly ash, bentonite, nitrogen adsorbent and phosphorus adsorbent are stirred and mixed uniformly, and then compressed and formed, and then air-dried to obtain a constructed wetland filler.
将上述实施例1-5以及对照制备的填料进行氮磷吸附测试。测试条件为取填料模块10g加入含100mg/L氮和25mg/L磷的溶液15mL,静置1天后。Nitrogen and phosphorus adsorption tests were performed on the fillers prepared in the above examples 1-5 and the control. The test condition is to take 10 g of the packing module and add 15 mL of a solution containing 100 mg/L nitrogen and 25 mg/L phosphorus, and let it stand for 1 day.
表1 实施例和对照例制得人工湿地填料的氮磷去除率Table 1 Nitrogen and phosphorus removal rates of constructed wetland fillers prepared in Examples and Comparative Examples
通过上述表格可以看出,本发明的实施例中加入氮吸附剂和磷吸附剂,可以看出氨氮和磷的去除率明显高于对照例1中没加的情况。并且与对照例2相比,对高炉渣活化处理也提高了氨氮和磷的去除率。It can be seen from the above table that nitrogen adsorbent and phosphorus adsorbent are added in the embodiment of the present invention, and it can be seen that the removal rate of ammonia nitrogen and phosphorus is significantly higher than that in Comparative Example 1 without adding it. And compared with the control example 2, the activation treatment of blast furnace slag also improved the removal rate of ammonia nitrogen and phosphorus.
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 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 the range.
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