CN106927571B - A method for enhancing denitrification of constructed wetlands by using modified biochar with strong carbon secretion - Google Patents
A method for enhancing denitrification of constructed wetlands by using modified biochar with strong carbon secretion Download PDFInfo
- Publication number
- CN106927571B CN106927571B CN201611258520.8A CN201611258520A CN106927571B CN 106927571 B CN106927571 B CN 106927571B CN 201611258520 A CN201611258520 A CN 201611258520A CN 106927571 B CN106927571 B CN 106927571B
- Authority
- CN
- China
- Prior art keywords
- denitrification
- wetland
- biochar
- strong carbon
- modified biochar
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 74
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 238000000034 method Methods 0.000 title claims abstract description 33
- 230000002708 enhancing effect Effects 0.000 title claims 10
- 230000028327 secretion Effects 0.000 title description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 54
- 230000003248 secreting effect Effects 0.000 claims abstract description 44
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 28
- 238000000197 pyrolysis Methods 0.000 claims abstract description 19
- 239000010865 sewage Substances 0.000 claims abstract description 18
- 239000011159 matrix material Substances 0.000 claims abstract description 16
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000000945 filler Substances 0.000 claims abstract description 9
- 238000005728 strengthening Methods 0.000 claims abstract description 8
- 239000002994 raw material Substances 0.000 claims abstract description 7
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 7
- 229960002089 ferrous chloride Drugs 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 claims description 6
- 239000000758 substrate Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000011261 inert gas Substances 0.000 claims description 4
- 239000002699 waste material Substances 0.000 claims description 4
- 239000006004 Quartz sand Substances 0.000 claims description 3
- 239000011449 brick Substances 0.000 claims description 3
- 238000003763 carbonization Methods 0.000 claims description 3
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- 230000004048 modification Effects 0.000 claims description 3
- 238000012986 modification Methods 0.000 claims description 3
- 230000007935 neutral effect Effects 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims 2
- 238000007605 air drying Methods 0.000 claims 1
- 239000003610 charcoal Substances 0.000 claims 1
- 238000004140 cleaning Methods 0.000 claims 1
- 238000011049 filling Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 11
- 238000011068 loading method Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 3
- 238000012546 transfer Methods 0.000 abstract description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract 2
- 241000196324 Embryophyta Species 0.000 description 24
- 238000012856 packing Methods 0.000 description 17
- 229910002651 NO3 Inorganic materials 0.000 description 6
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 5
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 4
- 235000017491 Bambusa tulda Nutrition 0.000 description 4
- 241001330002 Bambuseae Species 0.000 description 4
- 235000014676 Phragmites communis Nutrition 0.000 description 4
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 4
- 239000011425 bamboo Substances 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 230000001737 promoting effect Effects 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- -1 NO 3 - Chemical compound 0.000 description 2
- 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 2
- 239000000370 acceptor Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000005431 greenhouse gas Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 241000124033 Salix Species 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- YYXHRUSBEPGBCD-UHFFFAOYSA-N azanylidyneiron Chemical compound [N].[Fe] YYXHRUSBEPGBCD-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000005067 remediation Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000009919 sequestration Effects 0.000 description 1
- 239000003516 soil conditioner Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Images
Classifications
-
- 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
-
- 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
- C02F3/28—Anaerobic digestion processes
-
- 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Botany (AREA)
- Biotechnology (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种人工湿地脱氮方法,具体是一种利用强泌碳型改性生物炭强化人工湿地化学与微生物反硝化脱氮的方法,属于环境工程污水处理技术领域The invention relates to a method for denitrification of artificial wetlands, in particular to a method for strengthening the chemistry of artificial wetlands and microbial denitrification and denitrification by using modified biochar with strong carbon secretion, and belongs to the technical field of environmental engineering sewage treatment
背景技术Background technique
人工湿地作为一种由植物、基质、微生物等组成的独具特色的复合生态污水处理技术,在发展中地区污水处理厂达标尾水深度治理中具有突出的应用优势,逐步成为污水深度净化常用的新兴方法之一。然而,由于达标尾水中碳氮比低、硝态氮含量高,人工湿地反硝化脱氮效果往往受到抑制。另外,我国每年产生的湿地植物生物质面积达五千余万公顷,湿地植物除了一部分被湿地动物所摄食,进入生物链,大部分植物直接枯萎死亡,大量湿地植物如得不到及时清除,腐败后分解,再次释放到湿地水体中,有的地方甚至采取焚烧的做法,影响了大气环境质量。高价值资源化技术的缺失导致巨大的资源浪费和潜在的二次污染风险。As a unique composite ecological sewage treatment technology composed of plants, substrates, microorganisms, etc., constructed wetlands have outstanding application advantages in the advanced treatment of sewage treatment plants in developing regions. One of the emerging methods. However, due to the low carbon-to-nitrogen ratio and high nitrate nitrogen content in the up-to-standard tail water, the denitrification and denitrification effect of constructed wetlands is often inhibited. In addition, the area of wetland plant biomass produced in my country every year reaches more than 50 million hectares. Except for a part of wetland plants that are ingested by wetland animals and enter the biological chain, most plants directly wither and die. If a large number of wetland plants are not removed in time, they will become corrupt. After decomposing, it is released into the wetland water again, and in some places even incineration is adopted, which affects the quality of the atmospheric environment. The lack of high-value resource technology leads to huge waste of resources and potential secondary pollution risks.
随着污水中总氮排放标准的日益加严,如何将人工湿地高效反硝化脱氮与植物资源化利用有机结合是亟待解决的难题。有研究将湿地植物直接填埋入湿地提供碳源,但是难以控制植物腐烂时间,且极易出现湿地堵塞,出水色度加大等问题;中国专利文献CN103936161A”公开了一种利用植物碳源强化人工湿地对低碳高氮污水脱氮的方法和系统,它利用植物水解液作为湿地有机碳源、强化污水脱氮效率的方法,但该种方法操作复杂,且存在水解废弃物,没有实现植物的最大化利用。With the increasingly stringent emission standards of total nitrogen in sewage, how to organically combine the efficient denitrification and denitrification of constructed wetlands with the utilization of plant resources is an urgent problem to be solved. There are studies that directly bury wetland plants into wetlands to provide carbon sources, but it is difficult to control the decay time of plants, and it is very easy to block the wetlands and increase the chromaticity of the effluent. A method and system for denitrification of low-carbon and high-nitrogen sewage by constructed wetlands. It uses plant hydrolyzate as a wetland organic carbon source to enhance the denitrification efficiency of sewage. maximum utilization.
生物炭(Biochar),是由生物质在低氧环境下炭化产生的一类含碳量极其丰富、紧密堆积的片层状多孔环境功能材料。近年来生物炭在温室气体N2O减排、土壤改良修复、污染物吸附等方面展现出巨大的应用潜力,受到广泛关注。生物炭制备简便,无需活化,成本仅为活性炭的1/6左右。生物炭在人工湿地系统中的引入,能够为同时实现植物资源化利用与湿地效果的提升提供潜在的解决方案。Biochar is a kind of carbon-rich, tightly packed lamellar porous environmental functional material produced by carbonization of biomass in a low-oxygen environment. In recent years, biochar has shown great application potential in the reduction of greenhouse gas N 2 O, soil improvement and remediation, and pollutant adsorption, and has received extensive attention. The preparation of biochar is simple and requires no activation, and the cost is only about 1/6 of that of activated carbon. The introduction of biochar into the constructed wetland system can provide a potential solution for the simultaneous utilization of plant resources and the improvement of wetland effects.
中国专利文献CN 104761057A公开了一种生物炭模块化复合垂直流人工湿地系统,将生物炭添加入垂直流人工湿地的概念,但是该专利没有针对性提出生物炭的制备方法、生物炭碳源释放特性以及微生物——生物炭脱氮机制。当前生物炭多作为吸附剂或土壤改良剂使用,反硝化强化脱氮应用鲜有报道,且当前生物炭大多在高温下制备,大部分有机物气化,提供碳源的能力极为有限。因此,研发新型高泌碳型湿地基质,在促进湿地反硝化脱氮效果的同时实现湿地植物资源化高效利用,具有重要意义。Chinese patent document CN 104761057A discloses a biochar modular composite vertical flow constructed wetland system, the concept of adding biochar to the vertical flow constructed wetland, but the patent does not specifically propose a biochar preparation method, biochar carbon source release Characteristics and mechanisms of microbial-biochar denitrification. Currently, biochar is mostly used as an adsorbent or soil conditioner, and the application of denitrification to enhance denitrification is rarely reported. Currently, biochar is mostly prepared at high temperature, and most organic matter is gasified, so its ability to provide carbon sources is extremely limited. Therefore, it is of great significance to develop a new type of high-carbon-secreting wetland substrate to achieve efficient utilization of wetland plant resources while promoting the denitrification and denitrification effect of wetlands.
发明内容SUMMARY OF THE INVENTION
针对现有技术的不足,本发明提供一种利用强泌碳型改性生物炭强化人工湿地脱氮的方法,处理效率高。Aiming at the deficiencies of the prior art, the present invention provides a method for strengthening the denitrification of constructed wetlands by using the modified biochar with strong carbon secretion, which has high treatment efficiency.
本发明是通过如下技术方案实现的:The present invention is achieved through the following technical solutions:
一种利用强泌碳型改性生物炭强化人工湿地脱氮的方法,强泌碳型改性生物炭作为处理剂强化人工湿地进行反硝化脱氮,将强泌碳型改性生物炭与基质混合填入人工湿地床体中,或直接作为填料柱嵌入人工湿地床体中进行,所述的强泌碳型改性生物炭是以湿地植物为原料,经低温干馏后然后负载亚铁得到;反硝化脱氮处理温度为0-40℃,pH为6-8,人工湿地污水总氮含量为5-60mg/L。A method for strengthening the denitrification of constructed wetlands by using the modified biochar with strong carbon emission type, the modified biochar with strong carbon emission type is used as a treatment agent to strengthen the constructed wetland for denitrification and denitrification, and the modified biochar with strong carbon emission type is combined with a substrate. It is mixed and filled into the constructed wetland bed body, or directly embedded in the constructed wetland bed body as a packing column, and the strong carbon-secreting modified biochar is obtained by using wetland plants as raw materials, and after low-temperature dry distillation and then loading ferrous iron; The denitrification and denitrification treatment temperature is 0-40℃, the pH is 6-8, and the total nitrogen content of the constructed wetland sewage is 5-60mg/L.
本发明优选的,反硝化脱氮处理温度为10-30℃,pH为6-7,人工湿地污水总氮含量为20-40mg/L。Preferably in the present invention, the denitrification and denitrification treatment temperature is 10-30° C., the pH is 6-7, and the total nitrogen content of the constructed wetland sewage is 20-40 mg/L.
本发明优选的,强泌碳型改性生物炭与基质的混合的体积比1:20~1:2,进一步优选的,强泌碳型改性生物炭与基质的混合的体积比1:10~1:3,最为优选的,强泌碳型改性生物炭与基质的混合的体积比1:3。Preferably in the present invention, the volume ratio of the strong carbon-secreting modified biochar and the matrix is 1:20 to 1:2, and further preferably, the volume ratio of the strong carbon-secreting modified biochar and the matrix is 1:10 ~1:3, most preferably, the volume ratio of the mixture of the strong carbon-secreting modified biochar and the substrate is 1:3.
本发明优选的,所述的基质为砾石、建筑废砖或石英砂中的一种或两种以上混合。Preferably in the present invention, the matrix is one or a mixture of two or more of gravel, construction waste bricks or quartz sand.
本发明优选的,强泌碳型改性生物炭与基质混合后的总覆盖面积占湿地总面积的1/3~2/3,强泌碳型改性生物炭与基质混合填充后的孔隙率为20~50%;优选的,强泌碳型改性生物炭与基质混合填充后的孔隙率为30~40%。Preferably in the present invention, the total coverage area of the strong carbon-secreting modified biochar mixed with the matrix accounts for 1/3 to 2/3 of the total area of the wetland, and the porosity of the strong carbon-secreting modified biochar mixed with the matrix is filled. is 20-50%; preferably, the porosity after the strong carbon-secreting modified biochar is mixed and filled with the matrix is 30-40%.
本发明优选的,直接作为填料柱是将生物炭填充至填料柱内,然后将填料柱垂直嵌入人工湿地床体中,生物炭总体积与湿地体积比为1:20~1:4;所述填料柱为穿孔柱,孔径为0.5~1cm,开孔率40%~80%。Preferably in the present invention, as a packing column directly, the biochar is filled into the packing column, and then the packing column is vertically embedded in the constructed wetland bed, and the ratio of the total volume of the biochar to the wetland volume is 1:20 to 1:4; the The packing column is a perforated column, the pore diameter is 0.5-1 cm, and the porosity is 40%-80%.
进一步优选的,填料柱覆盖面积占湿地表面积的1/20~2/3。Further preferably, the covered area of the packing column accounts for 1/20 to 2/3 of the wetland surface area.
本发明优选的,所述的强泌碳型改性生物炭是按以下方法制备得到:Preferably in the present invention, the described strong carbon secretion type modified biochar is prepared by the following method:
(1)、以湿地植物为原料,将湿地植物洗净,粉碎成直径为1~3cm的块状,风干至恒重;(1), take wetland plants as raw materials, wash the wetland plants, pulverize them into blocks with a diameter of 1-3 cm, and air-dry to constant weight;
(2)、将步骤(1)处理后的湿地植物在惰性气体保护下,通过干馏方式,在低温下进行快速碳化处理,得到生物炭;所述干馏温度为250~400℃,升温速率为5~10℃/min,干馏时间30~60min;(2), under the protection of inert gas, the wetland plants treated in step (1) are rapidly carbonized at low temperature by dry distillation to obtain biochar; the dry distillation temperature is 250~400 ℃, and the heating rate is 5 ~10℃/min,
(3)、负载改性处理:将步骤(2)制得的生物炭与0.5~3mol/L的氯化亚铁溶液混合,静置12~16h进行负载亚铁,负载后的生物炭用去离子水洗涤至中性,然后于100~120℃厌氧环境中干燥6~12h,得到强泌碳型改性生物炭。(3), loading modification treatment: mix the biochar obtained in step (2) with 0.5-3 mol/L ferrous chloride solution, let stand for 12-16 hours to load ferrous, and the loaded biochar is used for Ionized water was washed to neutrality, and then dried in an anaerobic environment at 100-120 °C for 6-12 hours to obtain modified biochar with strong carbon secretion.
本发明优选的,步骤(1)中原料的选用湿地植物的根或茎。Preferably in the present invention, the raw materials in step (1) are the roots or stems of wetland plants.
本发明优选的,步骤(1)湿地植物为湿地常用植物芦竹、水织锦、杞柳等中的一种或两种以上混合。Preferably in the present invention, the wetland plants in step (1) are one or a mixture of two or more of the commonly used plants in wetlands such as reed bamboo, water brocade, and willow.
本发明优选的,步骤(2)所述的惰性气体为氮气。Preferably in the present invention, the inert gas described in step (2) is nitrogen.
本发明优选的,步骤(2)干馏温度为250~300℃,升温速率为5~8℃/min,干馏时间40~60min。Preferably in the present invention, the dry distillation temperature in step (2) is 250-300° C., the heating rate is 5-8° C./min, and the dry distillation time is 40-60 min.
最为优选的,步骤(2)干馏温度为300℃,升温速率为5~8℃/min,干馏时间60min。Most preferably, the dry distillation temperature in step (2) is 300° C., the heating rate is 5-8° C./min, and the dry distillation time is 60 minutes.
本发明优选的,步骤(3)氯化亚铁溶液的浓度为1~3mol/L,最为优选的,氯化亚铁溶液的浓度为3mol/L。Preferably in the present invention, the concentration of the ferrous chloride solution in step (3) is 1-3 mol/L, and most preferably, the concentration of the ferrous chloride solution is 3 mol/L.
本发明优选的,步骤(3)负载时间为12h。Preferably in the present invention, the load time of step (3) is 12h.
本发明优选的,步骤(3)厌氧干燥温度100~110℃,干燥时间8~12h,最为优选的,步骤(3)厌氧干燥温度105℃,干燥时间12h。Preferably in the present invention, step (3) anaerobic drying temperature is 100-110°C and drying time is 8-12h, most preferably, step (3) anaerobic drying temperature is 105°C and drying time is 12h.
本发明利用强泌碳型改性生物炭强化人工湿地脱氮的方法取得了意料不到的效果。The present invention achieves an unexpected effect by using the strong carbon-secreting modified biochar to strengthen the denitrification of the constructed wetland.
本发明所用原料及设备均为现有技术。The raw materials and equipment used in the present invention are all in the prior art.
与现有技术相比,本发明具有以下优势:Compared with the prior art, the present invention has the following advantages:
(1)、本发明利用强泌碳型改性生物炭强化人工湿地脱氮取得了意料不到的效果,应用时通过简便的负载Fe(II),Fe(II)可作为电子供体将电子转移给高价氮(如NO3 -,NO2 -),在自身被氧化的同时可以将高价态氮还原为氮气,实现化学反硝化脱氮过程。同时微生物也可以分别以亚铁和硝酸盐作为电子供体和受体,将亚铁氧化为三价铁,同时还原硝酸盐,从而将NO3 -转化为N2。另外,当反应体系中NO3 -消耗完时,微生物还可以利用生物炭释放的有机物将Fe(III)还原为Fe(II),从而实现铁-氮的氧化还原循环。(1) The present invention achieves unexpected effects by using strong carbon-secreting modified biochar to strengthen the denitrification of constructed wetlands. During application, by simply loading Fe(II), Fe(II) can be used as an electron donor to transfer electrons It is transferred to high-valent nitrogen (such as NO 3 - , NO 2 - ), and the high-valent nitrogen can be reduced to nitrogen while being oxidized to realize the chemical denitrification and denitrification process. At the same time, microorganisms can also use ferrous and nitrate as electron donor and acceptor, respectively, to oxidize ferrous iron to ferric iron, and at the same time reduce nitrate, so as to convert NO 3 - into N 2 . In addition, when the NO 3 - in the reaction system is consumed, the microorganisms can also reduce Fe(III) to Fe(II) by utilizing the organic matter released by the biochar, thereby realizing the iron-nitrogen redox cycle.
(2)、本发明使用的强泌碳型改性生物炭在低温下干馏制备,其有机碳溶出能力大大高于当前高温下(>400℃)制备的生物炭。图1是不同温度下干馏法制备的芦竹生物炭有机碳溶出曲线,由图可以看出在低温300℃下制备的芦竹生物炭用去离子水按照1:20的比例进行有机碳溶出测定,其有机碳浓度高达135mg/L(2700mg/kg),是污水处理厂一级A标准COD出水浓度(50mg/L)的近3倍,因此,对于低碳氮比废水的强化脱氮,该部分有机碳将起到重要作用。随着温度升高,生物炭中有机碳溶出量大幅减少,因此高温生物炭对于释放碳源促进反硝化的作用十分有限。(2) The strong carbon-secreting modified biochar used in the present invention is prepared by dry distillation at low temperature, and its organic carbon dissolution capacity is much higher than that of biochar prepared at current high temperature (>400°C). Fig. 1 is the organic carbon dissolution curve of the reed bamboo biochar prepared by dry distillation method at different temperatures, it can be seen from the figure that the reed bamboo biochar prepared at low temperature 300 ℃ carries out the organic carbon dissolution determination according to the ratio of 1:20 with deionized water , its organic carbon concentration is as high as 135mg/L (2700mg/kg), which is nearly three times the COD effluent concentration (50mg/L) of the first-class A standard of the sewage treatment plant. Therefore, for the enhanced denitrification of low-carbon nitrogen ratio wastewater, the Some organic carbon will play an important role. With the increase of temperature, the amount of organic carbon dissolved in biochar is greatly reduced, so the effect of high temperature biochar on releasing carbon source and promoting denitrification is very limited.
(3)、大量报道表明生物炭在土壤中可缓解温室气体N2O释放,本发明中将强泌碳型改性生物炭应用于人工湿地污水深度脱氮处理,既起到固碳减排的作用,又能通过促进反硝化进程缓解人工湿地N2O释放。(3) A large number of reports show that biochar can alleviate the release of greenhouse gas N 2 O in the soil. In the present invention, the strong carbon-secreting modified biochar is applied to the deep denitrification treatment of constructed wetland sewage, which not only plays a role in carbon sequestration and emission reduction It can also alleviate the N 2 O release from constructed wetlands by promoting the denitrification process.
本发明以简单的方法提升了低碳氮比污水中反硝化脱氮的效率,同时为原位解决植物资源化利用难题提供了参考,本方法操作简单、实用性强,对于全面实现污水排放中总氮提质达标、缓解全球温室效应具有重要意义。The invention improves the efficiency of denitrification and denitrification in sewage with a low-carbon nitrogen ratio in a simple method, and at the same time provides a reference for solving the problem of plant resource utilization in situ. It is of great significance to improve the quality of total nitrogen and alleviate the global greenhouse effect.
附图说明Description of drawings
图1是不同温度生物炭溶出有机碳浓度图;Fig. 1 is a graph of the organic carbon concentration of biochar dissolved at different temperatures;
图2是本发明使用的强泌碳型改性生物炭的结构示意图。Figure 2 is a schematic structural diagram of the strong carbon-secreting modified biochar used in the present invention.
图3是本发明强化人工湿地脱氮的方法中水平潜流湿地的结构示意图。FIG. 3 is a schematic structural diagram of a horizontal subsurface wetland in the method for strengthening denitrification of a constructed wetland according to the present invention.
图中:1、进水口,2、填料柱,3、强泌碳型改性生物炭基质,4、湿地主体基质,5、出水口,6、湿地植物,7、湿地床体。In the figure: 1. Water inlet, 2. Packing column, 3. Strong carbon-secreting modified biochar matrix, 4. Wetland main matrix, 5. Water outlet, 6. Wetland plants, 7. Wetland bed.
图4为不同强泌碳型改性生物炭的添加量对总氮去除影响效果柱状图。Figure 4 is a bar graph showing the effect of different strong carbon-secreting modified biochar additions on total nitrogen removal.
具体实施方式Detailed ways
下面通过具体实施例对本发明做进一步说明,但不限于此。The present invention will be further described below through specific embodiments, but not limited thereto.
实施例1Example 1
一种利用强泌碳型改性生物炭强化人工湿地脱氮的方法,强泌碳型改性生物炭作为处理剂强化人工湿地进行反硝化脱氮,具体方法如下:A method for strengthening the denitrification of constructed wetlands by using the modified biochar with strong carbon secretion type, the modified biochar with strong carbon secretion type is used as a treatment agent to strengthen the constructed wetland for denitrification and denitrification, and the specific method is as follows:
将生物炭填充至填料柱内,然后将填料柱垂直嵌入人工湿地床体中,生物炭总体积与湿地体积比为1:6;所述填料柱为穿孔柱,孔径为0.5~1cm,开孔率40%~80%。填料柱为圆形或方形,为方形时填料柱与湿地宽度相同,填料柱顶部设有可拆卸式密封塞,用于密封填料柱或更换本发明中的生物炭填料。填料柱覆盖面积占湿地表面积的1/20~2/3。水平潜流湿地由池体7、湿地植物6、湿地主体基质4、填料柱2、湿地强泌碳型改性生物炭3构成,具体如图3所示。湿地主体基质填料为砾石、建筑废砖、粉煤灰中的一种或任意几种组合,顶部铺设15cm粗沙或石英砂。The biochar is filled into the packing column, and then the packing column is vertically embedded in the bed of the constructed wetland, and the ratio of the total volume of the biochar to the wetland volume is 1:6; The rate is 40% to 80%. The packing column is round or square, and when the packing column is square, the width of the packing column is the same as that of the wetland, and a detachable sealing plug is arranged on the top of the packing column, which is used to seal the packing column or replace the biochar packing in the present invention. The coverage area of the packed column accounts for 1/20 to 2/3 of the wetland surface area. The horizontal subsurface wetland is composed of a pool body 7, wetland plants 6, a wetland main body matrix 4, a packing column 2, and a wetland strong carbon-secreting modified
上述垂直流湿地的具体工作过程为:The specific working process of the above-mentioned vertical flow wetland is as follows:
采用连续进水、推流出水方式运行。当高硝氮污水经过布水管道均匀地进入湿地床体7后,进水中的硝态氮与本发明中的生物炭填料柱接触后,一方面,本发明中的强泌碳型生物炭通过释放有机碳源直接促进污水中的反硝化微生物脱氮作用;另一方面,本发明中的改性生物炭通过表面Fe(II)作为电子供体将电子转移给高价氮(如NO3 -,NO2 -),在自身被氧化的同时可以将高价态氮还原为氮气,实现化学反硝化脱氮过程;同时反硝化微生物也分别以亚铁和硝酸盐作为电子供体和受体,将亚铁氧化为三价铁,同时还原硝酸盐,将NO3 -转化为N2。处理后的水有出水口排出湿地。It operates in the mode of continuous water inflow and push-out water. After the high-nitrate sewage enters the wetland bed 7 evenly through the water distribution pipeline, and the nitrate nitrogen in the influent is in contact with the biochar packing column of the present invention, on the one hand, the strong carbon-secreting biochar of the present invention The denitrifying microbial denitrification in sewage is directly promoted by releasing organic carbon sources; on the other hand, the modified biochar in the present invention transfers electrons to high-valent nitrogen (such as NO 3 − , NO 2 - ), while being oxidized, it can reduce high-valence nitrogen to nitrogen to realize chemical denitrification and denitrification process; at the same time, denitrifying microorganisms also use ferrous and nitrate as electron donors and acceptors, respectively. Ferrous iron is oxidized to ferric iron, while nitrate is reduced, converting NO 3 - to N 2 . The treated water is discharged from the wetland through an outlet.
强泌碳型改性生物炭是按如下方法制备得到:The strong carbon-secreting modified biochar is prepared as follows:
(1)取湿地植物的湿地植物芦竹根洗净并切碎成直径为1~3cm块状,风干,风干至恒重。(1) Take the Wetland plant reed bamboo root of the wetland plant, wash and chop it into a block with a diameter of 1-3 cm, air-dry, and air-dry to constant weight.
(2)、将步骤(1)处理后的湿地植物在氮气保护下,通过干馏方式,在低温下进行快速碳化处理,得到生物炭;所述干馏温度为300℃,升温速率为8℃/min,干馏时间60min;(2), under nitrogen protection, the wetland plants treated in step (1) are subjected to rapid carbonization at low temperature by dry distillation to obtain biochar; the dry distillation temperature is 300 ° C, and the heating rate is 8 ° C/min , dry distillation time 60min;
(3)、负载改性处理:将步骤(2)制得的生物炭与3mol/L的氯化亚铁溶液混合,静置12h进行负载亚铁,负载后的生物炭用去离子水洗涤至中性,然后于105℃厌氧环境中干燥12h,得到强泌碳型改性生物炭,如图2所示。(3), loading modification treatment: mix the biochar obtained in step (2) with 3 mol/L ferrous chloride solution, let stand for 12h to load ferrous, and wash the loaded biochar with deionized water to Neutral, and then dried in an anaerobic environment at 105 °C for 12 h to obtain modified biochar with strong carbon secretion, as shown in Figure 2.
实施例2Example 2
一种利用强泌碳型改性生物炭强化人工湿地脱氮的方法,同实施例1,不同之处在于:A method for strengthening the denitrification of constructed wetlands by utilizing strong carbon-secreting modified biochar, the same as in Embodiment 1, the difference is:
将强泌碳型改性生物炭与基质混合填入人工湿地床体中进行强化脱氮,强泌碳型改性生物炭与基质的体积比1:3,混合填料覆盖面积占湿地总面积的1/3~2/3。其它构造和实施例2相同,污水经过湿地深度反硝化脱氮净化后由出水口流出池体。The strong carbon-secreting modified biochar and the matrix were mixed and filled into the constructed wetland bed for enhanced denitrification. The volume ratio of the strong carbon-secreting modified biochar to the matrix was 1:3, and the coverage area of the mixed filler accounted for 30% of the total wetland area. 1/3 to 2/3. The other structures are the same as in Example 2, and the sewage flows out of the tank from the water outlet after being purified by deep denitrification and denitrification in the wetland.
应用实验例Application experiment example
一、分别将实施例1、实施例2利用强泌碳型改性生物炭强化人工湿地脱氮的方法进行应用实验,分别向实施例1、实施例2的垂直流湿地经布水管道进入高硝氮污水模拟废水,进水总氮含量25mg/L,进水pH为7,进水负荷10L/h,在环境温度8~10℃下进行脱氮处理,每个处理做平行实验,并与不加生物炭做对比,HRT(水力停留时间)5天条件下,总氮去除率可达88%,出水总氮含量小于8mg/L,不同强泌碳型改性生物炭的添加量对总氮去除的效果影响见图4所示。通过图4可以看出,强泌碳型改性生物炭的添加量在30%左右处理效果最强。1. Carry out the application experiment of the method of using strong carbon-secreting modified biochar to strengthen the denitrification of the constructed wetland in Example 1 and Example 2, respectively. Nitrate sewage simulated wastewater, the total nitrogen content of the influent water was 25mg/L, the pH of the influent water was 7, the influent water load was 10L/h, and the denitrification treatment was carried out at an ambient temperature of 8 to 10 °C. Without biochar for comparison, under the condition of HRT (hydraulic retention time) for 5 days, the total nitrogen removal rate can reach 88%, and the total nitrogen content in the effluent is less than 8mg/L. The effect of nitrogen removal is shown in Figure 4. It can be seen from Figure 4 that the treatment effect of the modified biochar with strong carbon secretion is about 30%.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611258520.8A CN106927571B (en) | 2016-12-30 | 2016-12-30 | A method for enhancing denitrification of constructed wetlands by using modified biochar with strong carbon secretion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611258520.8A CN106927571B (en) | 2016-12-30 | 2016-12-30 | A method for enhancing denitrification of constructed wetlands by using modified biochar with strong carbon secretion |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106927571A CN106927571A (en) | 2017-07-07 |
| CN106927571B true CN106927571B (en) | 2020-06-09 |
Family
ID=59444019
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611258520.8A Active CN106927571B (en) | 2016-12-30 | 2016-12-30 | A method for enhancing denitrification of constructed wetlands by using modified biochar with strong carbon secretion |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106927571B (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107720977B (en) * | 2017-09-27 | 2020-12-15 | 浙江海洋大学 | A method for reducing nitrogen and phosphorus non-point source pollution in ecological soil system based on composite biochar |
| CN107824612B (en) * | 2017-11-04 | 2018-09-28 | 江西夏氏春秋环境股份有限公司 | A kind of Fe3O4The preparation method of base charcoal soil passivator |
| CN108101222B (en) * | 2017-12-29 | 2020-07-31 | 华南农业大学 | Constructed wetland for deep denitrification and phosphorus removal of tail water and method for treating tail water |
| CN111943359B (en) * | 2020-07-24 | 2022-06-03 | 山东大学 | Artificial wetland coupled with iron ore enhanced denitrification, operation method and application |
| CN114409089A (en) * | 2022-01-21 | 2022-04-29 | 北京林业大学 | Subsurface flow constructed wetland river water treatment method based on carbon-supplementing columns |
| CN114940564B (en) * | 2022-05-31 | 2023-12-22 | 太原理工大学 | Method for controlling release of nitrogen in bottom mud of landscape water body by coupling iron-type autotrophic denitrification with biochar |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6569321B2 (en) * | 1999-04-16 | 2003-05-27 | Larry Steven Coffman | Method and apparatus for treating stormwater runoff |
| EP2093196B1 (en) * | 2008-02-19 | 2014-10-29 | Erik Meers | Method for controlling a waste water treatment system using a multiple step constructed wetland |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100390079C (en) * | 2006-06-30 | 2008-05-28 | 清华大学 | Ecological denitrification process for photosynthetic carbon supply |
| CN100569670C (en) * | 2007-05-14 | 2009-12-16 | 华南农业大学 | Method and system for treating sewage in composite vertical downflow artificial wetland |
| CN104556377B (en) * | 2014-12-15 | 2017-01-04 | 上海交通大学 | A kind of method of the low stain water body nitric efficiency improving low ratio of carbon to ammonium |
| KR101602129B1 (en) * | 2015-03-24 | 2016-03-21 | (주)새롬환경기술 | Water Purification System of Lake and Marsh |
| CN105000667B (en) * | 2015-06-05 | 2020-01-31 | 南开大学 | A sewage treatment system combining constructed wetland and microbial fuel cell |
| CN105236687B (en) * | 2015-11-02 | 2017-10-10 | 重庆大学 | The micro- vertical baffling wetland sewage-treatment plant of aeration of self-cleaning type and method |
| CN105217797B (en) * | 2015-11-04 | 2017-10-10 | 中国科学院水生生物研究所 | A kind of composite vertical current artificial wetland couples the method and device of microorganism electrolysis cell strengthened denitrification |
-
2016
- 2016-12-30 CN CN201611258520.8A patent/CN106927571B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6569321B2 (en) * | 1999-04-16 | 2003-05-27 | Larry Steven Coffman | Method and apparatus for treating stormwater runoff |
| EP2093196B1 (en) * | 2008-02-19 | 2014-10-29 | Erik Meers | Method for controlling a waste water treatment system using a multiple step constructed wetland |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106927571A (en) | 2017-07-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106927571B (en) | A method for enhancing denitrification of constructed wetlands by using modified biochar with strong carbon secretion | |
| CN107540094B (en) | Constructed wetland sewage treatment system | |
| CN1292999C (en) | Efficient ecological waste water treating apparatus and method | |
| CN103304033A (en) | Artificial wetland system taking oyster shell-waste brick-zeolite as composite filler | |
| CN108217959A (en) | For the intensified denitrification and dephosphorization artificial wet land system of low carbon-nitrogen ratio sewage processing | |
| CN112939187A (en) | Method for treating sewage by combining nitrogen-doped sludge biochar and peroxydisulfate | |
| CN108862574A (en) | Denitrifying artificial wet land system and its sewage denitrification method are cooperateed with based on reduction-state Fe autotrophy/sawdust heterotrophism | |
| CN103406328A (en) | Complex cover material for refuse landfill and application method thereof | |
| CN103130337A (en) | Method utilizing charcoal to achieve rural non-point source pollution denitrogenating | |
| CN106745812B (en) | A kind of preparation method of strong carbon secretion type modified biochar | |
| CN102092856A (en) | Hollow spherical porous filler for artificial wetland and raw materials | |
| Chen et al. | Optimizing agricultural biomass application to enhance nitrogen removal in vertical flow constructed wetlands for treating low-carbon wastewater | |
| CN108101222B (en) | Constructed wetland for deep denitrification and phosphorus removal of tail water and method for treating tail water | |
| CN107486139A (en) | Original position covering suppresses the function soil and its application method of black and odorous water sedimentary phosphate release | |
| CN111533395A (en) | Substrate improvement material for polluted river sediment, preparation method and application thereof | |
| CN101638281A (en) | Aeration oxidizing ecological bed used for waste water treatment | |
| CN107081122A (en) | The method that dephosphorization agent is prepared using copper water-supply pipe | |
| CN102964033B (en) | Covering layer for water quality purification of leachate and enhanced oxidation of methane in landfill and treatment method of leachate | |
| CN101966422B (en) | Method for processing CH4 in landfill site after acclimatizing and mineralizing garbage by utilizing percolate | |
| CN114477355B (en) | Oxygenation and adsorption coupled permeation reaction wall capable of improving river bank pollution cleaning capacity and application | |
| CN106477835B (en) | An in-situ chemically modified barrier agent for highly polluted sediment and its application | |
| CN106517677B (en) | Quality of reclaimed water landscape water body keeps structure | |
| CN113955855B (en) | Ecological blanket for water body restoration and application thereof | |
| CN117263388A (en) | Low-cost baffling type efficient denitrification and dephosphorization wetland combined matrix system | |
| CN202849197U (en) | Deep purification and combined denitrification system for polluted ground water |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200602 Address after: Licheng Alexander Road in Ji'nan City, Shandong province 250199 No. 27 Co-patentee after: NUCLEAR AND RADIATION SAFETY MONITORING CENTER OF SHANDONG PROVINCE Patentee after: SHANDONG University Address before: Licheng Alexander Road in Ji'nan City, Shandong province 250199 No. 27 Patentee before: SHANDONG University |