CN115636507B - Constructed Wetland Slow Release Filler Based on Sulfur Autotrophic Denitrification - Google Patents
Constructed Wetland Slow Release Filler Based on Sulfur Autotrophic Denitrification Download PDFInfo
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- 239000000945 filler Substances 0.000 title claims abstract description 62
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 229910052717 sulfur Inorganic materials 0.000 title claims abstract description 28
- 239000011593 sulfur Substances 0.000 title claims abstract description 28
- 230000001651 autotrophic effect Effects 0.000 title claims abstract description 23
- 239000002245 particle Substances 0.000 claims abstract description 64
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 claims abstract description 43
- 235000019345 sodium thiosulphate Nutrition 0.000 claims abstract description 43
- 239000004568 cement Substances 0.000 claims abstract description 31
- 239000012188 paraffin wax Substances 0.000 claims abstract description 28
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000010902 straw Substances 0.000 claims abstract description 26
- 239000011398 Portland cement Substances 0.000 claims abstract description 10
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims abstract description 10
- 239000000920 calcium hydroxide Substances 0.000 claims abstract description 10
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims abstract description 10
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 7
- 238000011049 filling Methods 0.000 claims abstract description 6
- 239000010865 sewage Substances 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 235000021355 Stearic acid Nutrition 0.000 claims description 14
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 14
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 14
- 239000008117 stearic acid Substances 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 13
- 239000011268 mixed slurry Substances 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 9
- 239000002775 capsule Substances 0.000 claims description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 235000021307 Triticum Nutrition 0.000 claims description 3
- 240000007594 Oryza sativa Species 0.000 claims description 2
- 235000007164 Oryza sativa Nutrition 0.000 claims description 2
- 240000006394 Sorghum bicolor Species 0.000 claims description 2
- 235000011684 Sorghum saccharatum Nutrition 0.000 claims description 2
- 240000008042 Zea mays Species 0.000 claims description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 claims description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims description 2
- 235000005822 corn Nutrition 0.000 claims description 2
- 235000009566 rice Nutrition 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims 2
- 244000098338 Triticum aestivum Species 0.000 claims 1
- 239000002131 composite material Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 239000008236 heating water Substances 0.000 claims 1
- 239000003469 silicate cement Substances 0.000 claims 1
- 238000002791 soaking Methods 0.000 claims 1
- 239000008187 granular material Substances 0.000 abstract description 24
- 230000008901 benefit Effects 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 235000014113 dietary fatty acids Nutrition 0.000 abstract description 2
- 239000000194 fatty acid Substances 0.000 abstract description 2
- 229930195729 fatty acid Natural products 0.000 abstract description 2
- 150000004665 fatty acids Chemical class 0.000 abstract description 2
- 238000013268 sustained release Methods 0.000 description 17
- 239000012730 sustained-release form Substances 0.000 description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 235000011116 calcium hydroxide Nutrition 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 229910002651 NO3 Inorganic materials 0.000 description 4
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 241000209140 Triticum Species 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000012851 eutrophication Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- MXZRMHIULZDAKC-UHFFFAOYSA-L ammonium magnesium phosphate Chemical compound [NH4+].[Mg+2].[O-]P([O-])([O-])=O MXZRMHIULZDAKC-UHFFFAOYSA-L 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000035587 bioadhesion Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000013265 extended release Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 231100000405 induce cancer Toxicity 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000012464 large buffer Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000002572 peristaltic effect Effects 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
Classifications
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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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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
本发明公开了一种基于硫自养反硝化的人工湿地缓释填料,由填料颗粒和硫代硫酸钠缓释颗粒组成,填料颗粒与硫代硫酸钠缓释颗粒的填充比为1:0.8~1.2;所述填料颗粒是由以下组分组成的:30%~50%的秸秆,10%~20%的氢氧化钙,20%~40%的硅酸盐水泥,10%~20%的活性炭。所述硫代硫酸钠缓释颗粒,是包裹有石蜡的水泥缓释颗粒,水泥缓释颗粒是由以下组分组成的:35%~45%的硫代硫酸钠,15%~25%的硬脂酸,35%~45%的硅酸盐水泥。本发明的人工湿地缓释填料,具有去除效率高、机械强度高、无需外加碳源、节约资源、环境友好等优点,在生物脱氮、污水处理等方面具有良好的应用前景。
The invention discloses an artificial wetland slow-release filler based on sulfur autotrophic denitrification, which is composed of filler particles and sodium thiosulfate slow-release particles, and the filling ratio of the filler particles to sodium thiosulfate slow-release particles is 1:0.8~ 1.2; the filler particles are composed of the following components: 30% to 50% of straw, 10% to 20% of calcium hydroxide, 20% to 40% of Portland cement, and 10% to 20% of activated carbon . The sodium thiosulfate slow-release granules are cement slow-release granules wrapped with paraffin, and the cement slow-release granules are composed of the following components: 35% to 45% of sodium thiosulfate, 15% to 25% of hard Fatty acid, 35% to 45% Portland cement. The artificial wetland slow-release filler of the present invention has the advantages of high removal efficiency, high mechanical strength, no need to add carbon source, resource saving, environmental friendliness, etc., and has good application prospects in biological denitrification, sewage treatment and the like.
Description
技术领域technical field
本发明涉及一种基于硫自养反硝化的人工湿地缓释填料,属于水处理技术领域。The invention relates to an artificial wetland slow-release filler based on sulfur autotrophic denitrification, which belongs to the technical field of water treatment.
背景技术Background technique
随着我国经济的快速发展,城市化进程的加快,生活及工业废水的排放量不断增加,导致水体中氮的含量超标,从而引起水体富营养化。水体富营养化会导致藻类过度生长,使水体的透明度和溶解氧降低,甚至还会释放出有毒物质破坏水生生态环境。同时硝酸盐还会转换成亚硝酸盐,亚硝酸盐会危害人体健康,甚至诱发癌症。因此,开发一套经济、高效,同时具有良好生态效益的脱氮处理工艺迫在眉睫。With the rapid development of my country's economy and the acceleration of urbanization, the discharge of domestic and industrial wastewater continues to increase, resulting in excessive nitrogen content in water bodies, resulting in eutrophication of water bodies. Eutrophication of the water body will lead to excessive growth of algae, reduce the transparency and dissolved oxygen of the water body, and even release toxic substances to damage the aquatic ecological environment. At the same time, nitrate will also be converted into nitrite, which will endanger human health and even induce cancer. Therefore, it is imminent to develop an economical, efficient, and ecologically beneficial denitrification process.
目前常用的脱氮处理方法有物理法、生物法和化学法。物理脱氮法有气提脱氮法和离子交换法,但是这种方法不能从根本上解决问题。化学脱氮法有折点加氯法和磷酸铵镁沉淀法,但是成本高而且会生成大量的副产物,易造成二次污染。生物法则是利用微生物的反硝化作用将硝酸盐转化成氮气,这种方法理论上可以彻底去除硝酸盐,并且有去除效率高、运行成本低和生态效果良好的优点,因此生物脱氮法是当前最主流的脱氮方法。At present, the commonly used denitrification treatment methods include physical, biological and chemical methods. Physical denitrification methods include air stripping denitrification method and ion exchange method, but this method cannot fundamentally solve the problem. Chemical denitrification methods include breakpoint chlorine addition method and ammonium magnesium phosphate precipitation method, but the cost is high and a large number of by-products are generated, which is easy to cause secondary pollution. The biological method is to use the denitrification of microorganisms to convert nitrate into nitrogen. This method can completely remove nitrate in theory, and has the advantages of high removal efficiency, low operating cost and good ecological effect. Therefore, biological denitrification is the current method. The most mainstream denitrification method.
生物脱氮法根据微生物所需电子供体的不同,可以分为自养反硝化和异养反硝化。我国废水普遍具有高氮低碳的特点,使用自养反硝化来处理废水,无需投加外来碳源,可以有效的降低处理成本,而且自养型细菌生长周期长、污泥产量低,可以减少污泥处理成本。其中使用硫源作为反硝化电子供体的硫自养反硝化脱氮法更为安全。Biological denitrification can be divided into autotrophic denitrification and heterotrophic denitrification according to the different electron donors required by microorganisms. Wastewater in my country generally has the characteristics of high nitrogen and low carbon. Using autotrophic denitrification to treat wastewater does not need to add external carbon sources, which can effectively reduce treatment costs. Moreover, autotrophic bacteria have a long growth cycle and low sludge production, which can reduce Sludge treatment costs. Among them, the sulfur autotrophic denitrification denitrification method using sulfur source as the electron donor for denitrification is safer.
在生物脱氮中,由于传统的活性污泥法运行管理复杂、投资高、能量消耗大,因此工艺简单、缓冲容量大、运行费用低并且生态效益良好的人工湿地系统便得到了越来越广泛的应用。若是将人工湿地法与硫自养反硝化法结合起来,便可以兼顾两者的优点。可以作为硫源供体的物质有很多,其中硫代硫酸钠的去除效率最高,但是硫代硫酸钠易溶于水,因此制备一种可以实现硫代硫酸钠缓释、能够释放碱度物质用于平衡脱氮过程中产生的酸度、有多孔性以有利于微生物附着且同时具有一定机械强度的人工湿地填料成为当前研究热点。In biological denitrification, due to the complex operation and management of the traditional activated sludge method, high investment and high energy consumption, the constructed wetland system with simple process, large buffer capacity, low operating cost and good ecological benefits has been more and more widely used. Applications. If the artificial wetland method is combined with the sulfur autotrophic denitrification method, the advantages of both can be taken into account. There are many substances that can be used as sulfur source donors, among which sodium thiosulfate has the highest removal efficiency, but sodium thiosulfate is easily soluble in water, so preparing a kind of material that can realize sodium thiosulfate sustained release and release alkalinity Constructed wetland fillers that balance the acidity generated during the denitrification process, are porous to facilitate microbial attachment, and have a certain mechanical strength have become current research hotspots.
发明内容Contents of the invention
针对上述现有技术,本发明提供了一种基于硫自养反硝化的人工湿地缓释填料。本发明的人工湿地缓释填料具有去除效率高、机械强度高、无需外加碳源、节约资源、环境友好等优点,在生物脱氮、污水处理等方面具有良好的应用前景。Aiming at the above prior art, the present invention provides a slow-release filler for artificial wetlands based on sulfur autotrophic denitrification. The artificial wetland slow-release filler of the present invention has the advantages of high removal efficiency, high mechanical strength, no need for additional carbon source, resource saving, environmental friendliness, etc., and has good application prospects in biological denitrification, sewage treatment and the like.
本发明是通过以下技术方案实现的:The present invention is achieved through the following technical solutions:
一种基于硫自养反硝化的人工湿地缓释填料,由填料颗粒和硫代硫酸钠缓释颗粒组成,填料颗粒与硫代硫酸钠缓释颗粒的填充比为1:0.8~1.2,按重量比计。A slow-release filler for artificial wetlands based on sulfur autotrophic denitrification, composed of filler particles and sodium thiosulfate slow-release particles, the filling ratio of filler particles and sodium thiosulfate slow-release particles is 1:0.8 to 1.2, by weight ratio.
所述填料颗粒、硫代硫酸钠缓释颗粒的粒径均为4~8 mm,优选6mm。The particle diameters of the filler particles and the sodium thiosulfate slow-release particles are both 4-8 mm, preferably 6 mm.
所述填料颗粒是由以下组分组成的:30%~50%的秸秆,10%~20%的氢氧化钙,20%~40%的硅酸盐水泥,10%~20%的活性炭,按重量百分比计。The filler particles are composed of the following components: 30% to 50% of straw, 10% to 20% of calcium hydroxide, 20% to 40% of Portland cement, 10% to 20% of activated carbon, according to Percentage by weight.
所述硫代硫酸钠缓释颗粒,是包裹有石蜡的水泥缓释颗粒,水泥缓释颗粒是由以下组分组成的:35%~45%的硫代硫酸钠,15%~25%的硬脂酸,35%~45%的硅酸盐水泥,按重量百分比计;石蜡占水泥缓释颗粒重量的15%~25%,包裹的石蜡层的厚度为0.8~1.2 mm。The sodium thiosulfate slow-release granules are cement slow-release granules wrapped with paraffin, and the cement slow-release granules are composed of the following components: 35% to 45% of sodium thiosulfate, 15% to 25% of hard Fatty acid, 35% to 45% Portland cement, calculated by weight percentage; paraffin accounts for 15% to 25% of the weight of cement slow-release particles, and the thickness of the wrapped paraffin layer is 0.8 to 1.2 mm.
进一步地,所述填料颗粒是通过以下方法制备得到的:将秸秆粉末、氢氧化钙、水泥、活性炭与水混合,料水比为1:0.8~1.2,搅拌均匀(20~40分钟),得混合浆;将混合浆倒入球形模具中,干燥,得到填料颗粒。在填料颗粒上覆盖一层麻布,并用喷壶保持麻布潮湿,持续养护一周,以提高填料的机械强度。所述秸秆粉末是通过以下方法制备得到的:将秸秆打碎(使用破碎机),用80~120目的筛网筛分,得秸秆粉末。Further, the filler particles are prepared by the following method: mixing straw powder, calcium hydroxide, cement, activated carbon and water, the ratio of material to water is 1:0.8-1.2, stirring evenly (20-40 minutes), to obtain Mixed slurry; pour the mixed slurry into a spherical mold and dry to obtain filler particles. Cover the filler particles with a layer of burlap, and use a watering can to keep the burlap moist for a week to improve the mechanical strength of the filler. The straw powder is prepared by the following method: crush the straw (using a crusher), and sieve with a sieve of 80-120 meshes to obtain the straw powder.
进一步地,所述秸秆选自小麦秸秆、玉米秸秆、高粱秸秆、水稻秸秆等。Further, the straw is selected from wheat straw, corn straw, sorghum straw, rice straw and the like.
进一步地,所述硫代硫酸钠缓释颗粒是通过以下方法制备得到的:Further, the sodium thiosulfate slow-release granules are prepared by the following method:
(1)将硬脂酸与无水乙醇混合,水浴加热至70~80℃,搅拌至硬脂酸完全熔化,加入硫代硫酸钠,充分搅拌使其均匀分散,在搅拌中自然冷却至30~35℃,待固体析出完全;将析出的固体烘干(无水乙醇完全挥发),80~120目筛网筛分,得缓释胶囊;(1) Mix stearic acid with absolute ethanol, heat in a water bath to 70-80°C, stir until the stearic acid is completely melted, add sodium thiosulfate, stir well to make it evenly dispersed, and naturally cool to 30-80°C while stirring. 35°C, wait until the solids are completely precipitated; dry the precipitated solids (absolute ethanol is completely volatilized), sieve with a sieve of 80-120 meshes, and obtain sustained-release capsules;
所述硬脂酸、无水乙醇与硫代硫酸钠的重量比为1:1:(2~3);The weight ratio of stearic acid, absolute ethanol and sodium thiosulfate is 1:1:(2-3);
(2)将缓释胶囊、水泥与适量水混合(料水比1:0.8~1.2),得混合浆料;将混合浆倒入球形模具中,干燥,得水泥缓释颗粒;(2) Mix slow-release capsules, cement and appropriate amount of water (material-to-water ratio 1:0.8-1.2) to obtain a mixed slurry; pour the mixed slurry into a spherical mold and dry to obtain cement sustained-release granules;
(3)固体石蜡水浴加热至65~75℃,待石蜡完全熔化后,将水泥缓释颗粒浸泡在石蜡中,浸泡5~10秒,取出,冷却至室温,即得包裹有一层石蜡的硫代硫酸钠缓释颗粒。(3) Heat the solid paraffin in a water bath to 65-75°C. After the paraffin is completely melted, soak the cement slow-release granules in the paraffin for 5-10 seconds, take it out, and cool it to room temperature to obtain a thiosulfate coated with a layer of paraffin. Sodium sulfate sustained release granules.
所述基于硫自养反硝化的人工湿地缓释填料,作为填料在生物脱氮、污水处理中的应用。The artificial wetland slow-release filler based on sulfur autotrophic denitrification is used as filler in biological denitrification and sewage treatment.
本发明的基于硫自养反硝化的人工湿地缓释填料,由填料颗粒和硫代硫酸钠缓释颗粒组成。单独使用填料颗粒时,由于缺少硫源,细菌生长速率慢;单独使用硫代硫酸钠缓释颗粒时,由于缓释颗粒表面光滑,不利于微生物附着。因此这两种颗粒单独使用时,脱氮效果较差。将两种填料按一定比例(控制硫代硫酸钠、熟石灰的比例)耦合使用,则填料颗粒中的熟石灰可以完美中和掉微生物因降解硫代硫酸钠缓释颗粒中的硫源而产生的碱度,从而维持微生物生长所需的中性环境;两者相辅相成,相互协作。The artificial wetland slow-release filler based on sulfur autotrophic denitrification of the present invention is composed of filler particles and sodium thiosulfate slow-release particles. When the filler particles are used alone, the bacterial growth rate is slow due to the lack of sulfur source; when the sodium thiosulfate slow-release particles are used alone, the surface of the slow-release particles is smooth, which is not conducive to microbial attachment. Therefore, when the two particles are used alone, the denitrification effect is poor. When the two fillers are used together in a certain ratio (controlling the ratio of sodium thiosulfate and hydrated lime), the hydrated lime in the filler particles can perfectly neutralize the alkali produced by microorganisms due to the degradation of the sulfur source in the sodium thiosulfate slow-release granules To maintain the neutral environment required for microbial growth; the two complement each other and cooperate with each other.
本发明的基于硫自养反硝化的人工湿地缓释填料,具有以下有益效果:The artificial wetland slow-release filler based on sulfur autotrophic denitrification of the present invention has the following beneficial effects:
(1)本发明选用硫代硫酸钠作为提供硫源物质,处理效率比目前主流的使用硫磺作为硫源的人工湿地填料高。(1) The present invention uses sodium thiosulfate as the sulfur source material, and its treatment efficiency is higher than that of the current mainstream artificial wetland fillers that use sulfur as the sulfur source.
(2)本发明在人工湿地填料的原材料中添加了活性炭,活性炭可以吸附水中的硝酸盐,增加水力停留时间,提升处理效果。(2) In the present invention, activated carbon is added to the raw materials of the artificial wetland filler, and the activated carbon can absorb nitrate in water, increase the hydraulic retention time, and improve the treatment effect.
(3)本发明使用熟石灰作为提供碱度物质,硅酸盐水泥作为粘结剂,两者混合后,机械强度更高,同时硅酸盐水泥还具有弱碱性,可以中和掉一部分硫自养反硝化产生的酸。并且钙离子还可以与水中的磷酸根结合成不溶性物质,使得填料兼具有除磷功能。(3) The present invention uses hydrated lime as the alkalinity-providing substance and Portland cement as the binder. After the two are mixed, the mechanical strength is higher. At the same time, Portland cement also has weak alkalinity, which can neutralize part of the sulfur acid produced by denitrification. And calcium ions can also combine with phosphate in water to form insoluble substances, so that the filler has the function of phosphorus removal.
(4)免烧结,低碳环保。(4) No sintering, low carbon and environmental protection.
(5)本发明在人工湿地填料的原材料中添加了秸秆,不但可以使填料呈现出多孔性,增加生物附着面积,而且还能释放碳源,提高硫自养异养反硝化的效率,增加了秸秆的利用新途径。(5) In the present invention, straw is added to the raw materials of artificial wetland filler, which not only makes the filler more porous, increases the bio-adhesion area, but also releases carbon sources, improves the efficiency of sulfur autotrophic heterotrophic denitrification, and increases the New ways to utilize straw.
附图说明Description of drawings
图1:填料颗粒的照片。Figure 1: Photograph of filler particles.
图2:硫代硫酸钠缓释颗粒的照片。Figure 2: Photograph of sodium thiosulfate extended-release granules.
图3:不同缓释工艺制备的缓释颗粒的缓释性能对比图。Figure 3: Comparison chart of sustained-release performance of sustained-release granules prepared by different sustained-release processes.
图4:连续实验硝酸氮去除率示意图。Figure 4: Schematic diagram of the removal rate of nitrate nitrogen in continuous experiments.
具体实施方式Detailed ways
下面结合实施例对本发明作进一步的说明。然而,本发明的范围并不限于下述实施例。本领域技术人员能够理解,在不背离本发明的精神和范围的前提下,可以对本发明进行各种变化和修饰。The present invention will be further described below in conjunction with embodiment. However, the scope of the present invention is not limited to the following examples. Those skilled in the art can understand that various changes and modifications can be made to the present invention without departing from the spirit and scope of the present invention.
下述实施例中所涉及的仪器、试剂、材料,若无特别说明,均为现有技术中已有的常规仪器、试剂、材料,可通过正规商业途径获得。下述实施例中所涉及的实验方法、检测方法等,若无特别说明,均为现有技术中已有的常规实验方法、检测方法。The instruments, reagents, and materials involved in the following examples, unless otherwise specified, are conventional instruments, reagents, and materials in the prior art, and can be obtained through formal commercial channels. The experimental methods and detection methods involved in the following examples, unless otherwise specified, are conventional experimental methods and detection methods in the prior art.
本发明所采用的水泥为购自山水集团的po42.5的硅酸盐水泥。本发明所采用的活性炭,购自康德牌粉末活性炭。本发明所采用的秸秆为小麦秸秆。The cement used in the present invention is Portland cement of po42.5 purchased from Shanshui Group. The activated carbon used in the present invention is purchased from Kangde brand powdered activated carbon. The straw used in the present invention is wheat straw.
实施例1基于硫自养反硝化的人工湿地缓释填料Example 1 Constructed Wetland Slow Release Filler Based on Sulfur Autotrophic Denitrification
由填料颗粒和硫代硫酸钠缓释颗粒组成,二者的填充比为1:1,按重量比计。所述填料颗粒、硫代硫酸钠缓释颗粒的粒径均为6mm。It is composed of filler particles and sodium thiosulfate slow-release particles, and the filling ratio of the two is 1:1, by weight. The particle diameters of the filler particles and the sodium thiosulfate slow-release particles are both 6mm.
制备方法如下:The preparation method is as follows:
(一)制备填料颗粒:(1) Preparation of filler particles:
(1)把秸秆放在破碎机中打碎运行5min,然后用100目的筛网筛选出秸秆粉末,备用;(1) Put the straw in the crusher and run it for 5 minutes, then use a 100-mesh screen to screen out the straw powder and set aside;
(2)将40 g秸秆粉末、15 g熟石灰、30 g水泥、15 g活性炭与100 ml水混合,搅拌30分钟,得混合浆;将混合浆倒入球形模具(直径6mm)中,干燥,得到填料颗粒。在填料颗粒上覆盖一层麻布,并用喷壶保持麻布潮湿,持续养护一周。所得填料颗粒的照片如图1所示,经检测,比表面积为0.0048㎡/g,孔隙率为47%,粒径为6mm,密度为0.78g/cm³,堆积密度为0.368g/cm³。(2) Mix 40 g of straw powder, 15 g of slaked lime, 30 g of cement, 15 g of activated carbon and 100 ml of water, and stir for 30 minutes to obtain a mixed slurry; pour the mixed slurry into a spherical mold (6 mm in diameter), and dry to obtain filler particles. Cover the filler particles with a layer of burlap and keep the burlap moist with a watering can for a week. The photo of the obtained filler particles is shown in Figure 1. After testing, the specific surface area is 0.0048㎡/g, the porosity is 47%, the particle size is 6mm, the density is 0.78g/cm³, and the bulk density is 0.368g/cm³.
(二)制备硫代硫酸钠缓释颗粒:(2) Preparation of sodium thiosulfate sustained-release granules:
(1)将20 g硬脂酸放入烧杯中,加入20 ml无水乙醇,恒温水浴锅水浴加热至75℃,搅拌至硬脂酸完全熔化,加入40 g硫代硫酸钠,充分搅拌使其均匀分散,在搅拌中自然冷却至30℃,待固体析出完全;将析出的固体放入烘箱烘干(40℃),100目筛网筛分,得缓释胶囊;(1) Put 20 g of stearic acid into a beaker, add 20 ml of absolute ethanol, heat it in a constant temperature water bath to 75°C, stir until the stearic acid is completely melted, add 40 g of sodium thiosulfate, and stir fully to make it Disperse evenly, cool naturally to 30°C while stirring, and wait until the solids are completely precipitated; put the precipitated solids into an oven for drying (40°C), and sieve through a 100-mesh sieve to obtain sustained-release capsules;
(2)将60 g缓释胶囊、40 g水泥与100 ml水混合,搅拌均匀,得混合浆料;将混合浆倒入球形模具(直径6mm)中,干燥,得水泥缓释颗粒;(2) Mix 60 g of sustained-release capsules, 40 g of cement and 100 ml of water, and stir evenly to obtain a mixed slurry; pour the mixed slurry into a spherical mold (6 mm in diameter), and dry to obtain cement sustained-release granules;
(3)20 g固体石蜡,恒温水浴锅水浴加热至70℃,待石蜡完全熔化后,将水泥缓释颗粒浸泡在石蜡中,浸泡8秒,取出,冷却至室温,即得表面包裹了一层石蜡的硫代硫酸钠缓释颗粒(石蜡层的厚度约为1.0mm)(经计算,包裹的石蜡的重量为水泥缓释颗粒的18%,这里采用20 g石蜡,为了使融化后的石蜡可以完全包裹住水泥缓释颗粒),照片如图2所示。(3) Heat 20 g of solid paraffin in a constant-temperature water bath to 70°C. After the paraffin is completely melted, soak the cement slow-release granules in the paraffin for 8 seconds, take it out, and cool it to room temperature to obtain a layer coated on the surface. Sodium thiosulfate slow-release granules of paraffin (the thickness of the paraffin layer is about 1.0mm) (by calculation, the weight of the wrapped paraffin is 18% of the cement slow-release granules, 20 g of paraffin is used here, in order to make the paraffin after melting can be Completely wrap the cement slow-release particles), the photo is shown in Figure 2.
对照1:石蜡加水泥制备的缓释颗粒(简称石蜡加水泥),制备方法同上(二),不同之处在于:不进行步骤(1),步骤(2)中采用硫代硫酸钠替换缓释胶囊。Control 1: Sustained-release granules prepared from paraffin plus cement (referred to as paraffin plus cement), the preparation method is the same as above (2), the difference is that step (1) is not performed, and sodium thiosulfate is used in step (2) to replace the slow-release capsule.
对照2:硬脂酸加水泥制备的缓释颗粒(简称硬脂酸加水泥),制备方法同上(二),不同之处在于:不进行步骤(3),步骤(2)得到的水泥缓释颗粒即为最终产品。Control 2: slow-release granules prepared by adding stearic acid and cement (referred to as stearic acid plus cement), the preparation method is the same as above (2), the difference is that step (3) is not carried out, and the cement slow-release obtained in step (2) The pellets are the final product.
取两颗上述制备的硫代硫酸钠缓释颗粒,浸泡在250 ml水中,其缓释速率如表1所示。同时,以石蜡加水泥制备的缓释颗粒、硬脂酸加水泥制备的缓释颗粒作为对照,结果如图3所示。由表1、图3可知,本发明的硫代硫酸钠缓释颗粒,具有良好的缓释效果;不加石蜡或不加硬脂酸时,缓释效果有明显差异。Take two sodium thiosulfate sustained-release granules prepared above and soak them in 250 ml of water. The sustained-release rate is shown in Table 1. At the same time, the slow-release granules prepared by adding paraffin wax and cement, and the slow-release granules prepared by adding stearic acid and cement were used as controls, and the results are shown in Figure 3. As can be seen from Table 1 and Figure 3, the sodium thiosulfate sustained-release granules of the present invention have a good sustained-release effect; when no paraffin or stearic acid is added, the sustained-release effect is significantly different.
表1Table 1
将上述制备的填料颗粒和硫代硫酸钠缓释颗粒填充在升流式厌氧污泥反应器中(二者填充重量比为1:1),通过蠕动泵进行稳定持续的进水,HRT为9.6h,进水硝氮浓度为130mg/L。其硝氮去除效率如表2、图4所示。由表2、图4可知,本发明的基于硫自养反硝化的人工湿地缓释填料具有良好的脱氮效果。The filler particles and sodium thiosulfate slow-release particles prepared above were filled in an upflow anaerobic sludge reactor (the filling weight ratio of the two was 1:1), and the water was fed stably and continuously through a peristaltic pump. The HRT was At 9.6 hours, the concentration of nitrate nitrogen in the influent was 130mg/L. The removal efficiency of nitrate nitrogen is shown in Table 2 and Figure 4. It can be seen from Table 2 and Figure 4 that the artificial wetland slow-release filler based on sulfur autotrophic denitrification of the present invention has a good denitrification effect.
表2Table 2
给本领域技术人员提供上述实施例,以完全公开和描述如何实施和使用所主张的实施方案,而不是用于限制本文公开的范围。对于本领域技术人员而言显而易见的修饰将在所附权利要求的范围内。The above examples are provided to those skilled in the art to fully disclose and describe how to make and use the claimed embodiments and not to limit the scope of the disclosure herein. Modifications obvious to those skilled in the art are intended to be within the scope of the appended claims.
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