CN104326574A - Horizontal subsurface wetland system for intensifying denitrification of micro-polluted water in winter - Google Patents

Horizontal subsurface wetland system for intensifying denitrification of micro-polluted water in winter Download PDF

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CN104326574A
CN104326574A CN201410683823.9A CN201410683823A CN104326574A CN 104326574 A CN104326574 A CN 104326574A CN 201410683823 A CN201410683823 A CN 201410683823A CN 104326574 A CN104326574 A CN 104326574A
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water
matrix bed
bed body
layer
matrix
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CN104326574B (en
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于鲁冀
陈涛
柏义生
范鹏宇
晋凯迪
章显
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Zhengzhou University
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/32Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
    • C02F3/327Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae characterised by animals and plants
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/301Aerobic and anaerobic treatment in the same reactor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/004Apparatus and plants for the biological treatment of water, waste water or sewage comprising a selector reactor for promoting floc-forming or other bacteria
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
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  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
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  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

本发明涉及强化冬季微污染水体脱氮的水平潜流湿地系统,有效解决低BOD5/NO3 -、溶解氧、基质堵塞等影响冬季湿地脱氮效果的问题,方法是,基质床体的进水端内面设置的布水板与进水端内面间构成布水间,出水端内面设置的收水板与出水端内面间构成收水间,布水板与收水板之间基质床体内的前段和中段有多道取样管,每个取样管上开有通气孔,基质床体内后段有玉米芯层,布水板和收水板上均布有通水孔,布水板和收水板之间的基质床体内由上至下填充有砂石层、沸石层、砾石铁屑层,基质床体进水端的端面上装有进水管,出水端的端面有调节水位的出水管,湿地系统表面覆盖有薄膜,本发明维护简单,基质堵塞频率低,脱氮率不低于40%,运行费用低。

The invention relates to a horizontal subsurface flow wetland system that strengthens denitrification of micro-polluted water bodies in winter, and effectively solves problems such as low BOD 5 /NO 3 - , dissolved oxygen, matrix clogging, etc. that affect the denitrification effect of winter wetlands. The method is to inject water into the matrix bed The water distribution room is formed between the water distribution plate installed on the inner surface of the end and the inner surface of the water inlet end. The water collection room is formed between the water collecting plate provided on the inner surface of the water outlet end and the inner surface of the water outlet end. The front section of the matrix bed is between the water distribution plate and the water collecting plate. There are multiple sampling tubes in the middle section, and each sampling tube has a vent hole. There is a corncob layer in the rear section of the matrix bed. There are water holes on the water distribution plate and the water collection plate. The water distribution plate and the water collection plate are The matrix bed is filled from top to bottom with a sand and gravel layer, a zeolite layer, and a gravel and iron filing layer. The water inlet end of the matrix bed is equipped with a water inlet pipe, and the water outlet end is equipped with an outlet pipe to adjust the water level. The surface of the wetland system is covered With the membrane, the invention has simple maintenance, low substrate clogging frequency, denitrification rate of not less than 40%, and low operating costs.

Description

强化冬季微污染水体脱氮的水平潜流湿地系统Horizontal subsurface flow wetland system to strengthen denitrification of slightly polluted water in winter

技术领域 technical field

本发明涉及污水处理系统,特别是一种强化冬季微污染水体脱氮的水平潜流湿地系统。 The invention relates to a sewage treatment system, in particular to a horizontal subsurface flow wetland system that strengthens denitrification of slightly polluted water bodies in winter.

背景技术 Background technique

世界上水源被污染是普遍存在的问题,尤其我国是世界上水资源严重短缺的国家之一,人均水资源占有量少,而水污染却很严重。近年来,由于不断加强污水处理厂建设,使污水直接排放的问题得到一定程度遏制,但是污水处理厂即使执行最严格的排放标准,其出水指标与地表水环境质量标准仍存在一定的差距。河流作为各种处理后废水的收纳水体,经常也受到有机物及氮磷的污染,但相对污染较轻,被称为微污染水体。虽然此类水体污染并不严重,但大多数河流生态环境质量较差,无法满足水环境功能要求,尤其在北方,由于大部分地区河流缺乏天然径流、水资源严重短缺,导致天然水体纳污能力非常有限,保障及维持地表水环境功能区划要求具有相当大难度。 Pollution of water sources is a common problem in the world, especially my country is one of the countries with serious shortage of water resources in the world. The per capita water resources are small, but the water pollution is very serious. In recent years, due to the continuous strengthening of the construction of sewage treatment plants, the problem of direct sewage discharge has been curbed to a certain extent. However, even if the sewage treatment plants implement the most stringent discharge standards, there is still a certain gap between the effluent indicators and the surface water environmental quality standards. As the receiving water body of various treated wastewater, rivers are often polluted by organic matter and nitrogen and phosphorus, but the pollution is relatively light, and they are called slightly polluted water bodies. Although the pollution of such water bodies is not serious, the quality of the ecological environment of most rivers is poor and cannot meet the functional requirements of the water environment. Especially in the north, due to the lack of natural runoff and serious shortage of water resources in most areas, the pollution-holding capacity of natural water bodies has been reduced. It is very difficult to guarantee and maintain the functional zoning requirements of the surface water environment.

目前,国内外学者已经研究出一些技术手段对污染河流微污染水体进行净化。(1)常用的物理净化方法包括河道曝气、引水稀释和底泥疏竣。这类方法需要消耗较高的能量才能达到曝气、疏浚、冲污等预期效果,并且没有从根本上去除污染物,治标不治本。(2)化学净化法有化学除藻、絮凝沉淀和重金属的化学固定等。此类方法也没有将氮、磷或重金属从水体中清除,并且由于化学试剂的应用,容易导致二次污染。另外,针对流量极大的河水而言,投加的药量也很大,经济性较差。(3)生物净化法常用的有投菌法、生物膜法及曝气充氧法。总的来说,生物净化具有处理效果好、投资省、能耗低且能够恢复或增强水体的自净能力的优点,但投菌法中应用的高效微生物的选育需要较长时间,净化效果持续时间短,且易受外部条件的制约;生物膜法和曝气充氧法投入的资金都较大,在资金有限的前提下,不宜大规模采用。(4)生态技术主要有植物净化技术、土地处理技术、稳定塘技术及人工湿地净化技术。生态治理措施具有治理效果好、能耗低、运行费用低、维护简单的优点,尤其是人工湿地净化法,还具有一定的生态效益和经济效益。 At present, scholars at home and abroad have developed some technical means to purify the slightly polluted water bodies of polluted rivers. (1) The commonly used physical purification methods include river aeration, water diversion dilution and sediment dredging. Such methods require high energy consumption to achieve the expected effects of aeration, dredging, and flushing, and do not remove pollutants fundamentally, treating the symptoms but not the root cause. (2) Chemical purification methods include chemical algae removal, flocculation and sedimentation, and chemical fixation of heavy metals. Such methods also do not remove nitrogen, phosphorus or heavy metals from water bodies, and easily lead to secondary pollution due to the application of chemical reagents. In addition, for the river water with a large flow rate, the amount of dosing is also large, and the economy is poor. (3) The commonly used methods of biological purification include the method of bacteriostasis, biofilm and aeration and oxygenation. In general, biological purification has the advantages of good treatment effect, low investment, low energy consumption, and the ability to restore or enhance the self-purification ability of water bodies. However, it takes a long time for the breeding of high-efficiency microorganisms used in the bacterial injection method, and the purification effect lasts. The time is short, and it is easily restricted by external conditions; the investment of biofilm method and aeration and oxygenation method is relatively large, and it is not suitable for large-scale adoption under the premise of limited funds. (4) Ecological technologies mainly include plant purification technology, land treatment technology, stabilization pond technology and artificial wetland purification technology. Ecological management measures have the advantages of good governance effects, low energy consumption, low operating costs, and simple maintenance, especially the artificial wetland purification method, which also has certain ecological and economic benefits.

人工湿地技术虽在南方广泛应用,但在北方推广应用受到很大限制,主要原因有:(1)北方寒冷的气候条件抑制了微生物活性,导致去除效果差;(2)冬季植物枯萎或死亡,光合作用复氧能力减弱,基质床内溶解氧不足;(3)河流收纳的处理后废水,BOD5/NO3 -较低,可生化性较差,限制了人工湿地的处理效果;(4)冬季微生物活性受限,加速了基质床堵塞频率。 Although constructed wetland technology is widely used in the south, its promotion and application in the north is greatly restricted. The main reasons are: (1) the cold climate in the north inhibits the activity of microorganisms, resulting in poor removal effect; (2) plants wither or die in winter, The reoxygenation ability of photosynthesis is weakened, and the dissolved oxygen in the matrix bed is insufficient; (3) the treated wastewater collected by the river has low BOD 5 /NO 3 - and poor biodegradability, which limits the treatment effect of the constructed wetland; (4) Microbial activity is limited in winter, which accelerates the frequency of substrate bed clogging.

虽然认识到BOD5/NO3 -、溶解氧、基质堵塞问题影响冬季湿地脱氮效果,但目前国内外尚无得到公认的解决技术方案。 Although it is recognized that BOD 5 /NO 3 - , dissolved oxygen, and matrix clogging affect the denitrification effect of wetlands in winter, there is no recognized technical solution at home and abroad.

发明内容 Contents of the invention

针对上述情况,为克服现有技术之缺陷,本发明之目的就是提供一种强化冬季微污染水体脱氮的水平潜流湿地系统,可有效解决低BOD5/NO3 -、溶解氧、基质堵塞等影响冬季湿地脱氮效果的问题。 In view of the above situation, in order to overcome the defects of the prior art, the purpose of the present invention is to provide a horizontal subsurface flow wetland system that strengthens the denitrification of slightly polluted water in winter, which can effectively solve the problems of low BOD 5 /NO 3 - , dissolved oxygen, matrix clogging, etc. Problems affecting the denitrification effect of wetlands in winter.

本发明解决的技术方案是,该系统包括布水板、基质床体和收水板,基质床体沿长向的进水端内面设置有向上平行于基质床体端面的布水板,布水板与进水端内面间构成布水间,基质床体沿长向的出水端内面设置有向上平行于基质床体端面的收水板,收水板与出水端内面间构成收水间,布水板与收水板之间构成的基质床体内的前段和中段垂直向上放置有多道通气的取样管,每个取样管上开有通气孔,基质床体内后段垂直向上放置有平行于收水板内面作为纤维素碳源的玉米芯层(所述的前段、中段、后段是以进水端为前、出水端为后定义的),布水板和收水板结构相同,布水板和收水板上均布有通水孔,布水板和收水板之间的基质床体内由上至下依次填充有砂石层、沸石层、砾石铁屑层,砂石层和沸石层之间、沸石层和砾石铁屑层之间均设置有用于防止基质层坍塌或下渗的土工透水布,基质床体进水端的端面上装有进水管,出水端的端面自上至下设置有用于调节水位的第一出水管、第二出水管、第三出水管,湿地系统表面覆盖有薄膜,与调节水位的出水管构成床体内水的保温结构,通过布水板上的通水孔,水体均匀的在基质床体中曲折流动,同玉米芯层充分接触,提高水体的BOD5/NO3 -,通过第一出水管、第二出水管、第三出水管调节基质床体内的水位,将水位调节同基质床体表面覆盖薄膜措施相结合,保证基质床体内的水温,进而强化水平潜流湿地系统的冬季脱氮效果,取样管的布设密度由进水端至出水端依次降低,基质床体前端复氧能力高于后端,使富氧水体主要集中在基质床体前端,为基质床体前端好氧硝化作用和末端厌氧反硝化作用创造条件,有利湿地对氮的去除效果,益于基质床体前端硝化作用和末端反硝化作用的进行。 The technical solution solved by the present invention is that the system includes a water distribution plate, a matrix bed body and a water collection plate, and the inner surface of the water inlet end of the matrix bed body along the long direction is provided with a water distribution plate parallel to the end surface of the matrix bed body upwards, and the water distribution plate The water distribution room is formed between the plate and the inner surface of the water inlet end, and the inner surface of the water outlet end of the matrix bed is provided with a water collection plate parallel to the end surface of the matrix bed body, and the water collection room is formed between the water collection plate and the inner surface of the water outlet end. The front section and the middle section of the matrix bed formed between the water plate and the water collection plate are vertically placed with multi-channel ventilation sampling tubes, each sampling tube is provided with air holes, and the rear section of the matrix bed body is vertically placed with a tube parallel to the collection tube. The inner surface of the water board is the corn cob layer as the cellulose carbon source (the front section, middle section, and rear section are defined by the water inlet end as the front and the water outlet end as the back), the structure of the water distribution board and the water collection board are the same, and the water distribution board The water distribution plate and the water collection plate are evenly distributed with water holes, and the matrix bed between the water distribution plate and the water collection plate is filled with sandstone layer, zeolite layer, gravel iron filings layer, sandstone layer and zeolite layer from top to bottom. Between the layers, between the zeolite layer and the gravel iron filings layer, there are geotechnical permeable cloths used to prevent the matrix layer from collapsing or seeping down. The end surface of the water inlet end of the matrix bed is equipped with a water inlet pipe, and the end surface of the water outlet end is arranged from top to bottom. The first water outlet pipe, the second water outlet pipe, and the third water outlet pipe for adjusting the water level. The surface of the wetland system is covered with a film, and the water outlet pipe for adjusting the water level constitutes the heat preservation structure of the water in the bed. Through the water hole on the water distribution plate, The water body evenly flows zigzagging in the matrix bed, fully contacts with the corn cob layer, increases the BOD 5 /NO 3 - of the water body, and adjusts the water level in the matrix bed through the first water outlet pipe, the second water outlet pipe, and the third water outlet pipe. Combining the water level adjustment with the film covering the surface of the matrix bed body ensures the water temperature in the matrix bed body, and then strengthens the denitrification effect of the horizontal subsurface flow wetland system in winter. The reoxygenation capacity of the front end of the body is higher than that of the back end, so that the oxygen-enriched water is mainly concentrated in the front end of the matrix bed, creating conditions for the aerobic nitrification at the front end of the matrix bed and anaerobic denitrification at the end, which is beneficial to the nitrogen removal effect of the wetland and benefits Nitrification at the front end of the matrix bed and denitrification at the end.

本发明是针对湿地在北方推广受限而提供的一种结构设计合理、复氧措施和保温措施得当的水平潜流湿地系统,该系统的基质配置与分布可以显著提高冬季水平潜流湿地系统的脱氮能力,并且维护简单,基质堵塞频率低,可以强化冬季湿地床的脱氮能力,脱氮率不低于40%,并且维护简单,运行费用低,有效解决水污染问题,经济和社会效益巨大。 The present invention provides a horizontal subsurface flow wetland system with reasonable structure design, appropriate reoxygenation measures and heat preservation measures in view of the limited promotion of wetlands in the north. The matrix configuration and distribution of the system can significantly improve the denitrification of the horizontal subsurface flow wetland system in winter capacity, and simple maintenance, low frequency of matrix clogging, can strengthen the denitrification capacity of the wetland bed in winter, the denitrification rate is not less than 40%, and simple maintenance, low operating costs, effectively solve the problem of water pollution, huge economic and social benefits.

附图说明 Description of drawings

图1为本发明的剖面结构主视图。 Fig. 1 is the front view of the sectional structure of the present invention.

图2为本发明的布水板(或收水板)的结构主视图。 Fig. 2 is a structural front view of the water distribution plate (or water collection plate) of the present invention.

图3为本发明的基质床体底面结构剖面主视图。 Fig. 3 is a sectional front view of the substrate bed bottom structure of the present invention.

具体实施方式 Detailed ways

以下结合附图对本发明的具体实施方式作详细说明。 The specific implementation manners of the present invention will be described in detail below in conjunction with the accompanying drawings.

由图1所示,本发明包括布水板、基质床体和收水板,基质床体沿长向的进水端内面设置有向上平行于基质床体端面的布水板3,布水板与进水端内面间构成布水间13,基质床体沿长向的出水端内面设置有向上平行于基质床体端面的收水板11,收水板与出水端内面间构成收水间14,布水板与收水板之间构成的基质床体内的前段和中段垂直向上放置有多道通气的取样管4,每个取样管上开有通气孔5,基质床体内后段垂直向上放置有平行于收水板内面作为纤维素碳源的玉米芯层9(所述的前段、中段、后段是以进水端为前、出水端为后定义的),布水板和收水板结构相同,布水板和收水板上均布有通水孔3-1,布水板和收水板之间的基质床体内由上至下依次填充有砂石层6、沸石层7、砾石铁屑层8,砂石层6和沸石层7之间、沸石层7和砾石铁屑层8之间均设置有用于防止基质层坍塌或下渗的土工透水布10,基质床体进水端的端面上装有进水管2,出水端的端面自上至下设置有用于调节水位的第一出水管12-1、第二出水管12-2、第三出水管12-3,湿地系统表面覆盖有薄膜,与调节水位的出水管构成床体内水的保温结构,通过布水板上的通水孔,水体均匀的在基质床体中曲折流动,同玉米芯层9充分接触,提高水体的BOD5/NO3 -,通过第一出水管12-1、第二出水管12-2、第三出水管12-3调节基质床体内的水位,将水位调节同基质床体表面覆盖薄膜措施相结合,保证基质床体内的水温,进而强化水平潜流湿地系统的冬季脱氮效果,取样管的布设密度由进水端至出水端依次降低,基质床体前端复氧能力高于后端,使富氧水体主要集中在基质床体前端,为基质床体前端好氧硝化作用和末端厌氧反硝化作用创造条件,有利湿地对氮的去除效果,益于基质床体前端硝化作用和末端反硝化作用的进行。 As shown in Figure 1, the present invention includes a water distribution plate, a matrix bed body and a water collection plate, and the inner surface of the water inlet end of the matrix bed body along the long direction is provided with a water distribution plate 3 parallel to the end surface of the matrix bed body upwards, and the water distribution plate The water distribution room 13 is formed between the inner surface of the water inlet end, and the inner surface of the water outlet end of the matrix bed along the length is provided with a water collection plate 11 parallel to the end surface of the matrix bed body, and a water collection room 14 is formed between the water collection plate and the inner surface of the water outlet end. , the front section and the middle section of the matrix bed formed between the water distribution plate and the water collection plate are placed vertically upwards with multi-channel ventilation sampling tubes 4, each sampling tube is provided with air holes 5, and the rear section of the matrix bed body is placed vertically upwards There is a corn cob layer 9 parallel to the inner surface of the water collecting plate as the cellulose carbon source (the front section, middle section, and rear section are defined by the water inlet end as the front and the water outlet end as the rear), the water distribution plate and the water collection plate The structure is the same, the water distribution plate and the water collection plate are evenly distributed with water holes 3-1, and the matrix bed between the water distribution plate and the water collection plate is filled with sandstone layer 6, zeolite layer 7, The gravel iron filings layer 8, between the sandstone layer 6 and the zeolite layer 7, and between the zeolite layer 7 and the gravel iron filings layer 8 are provided with a geotechnical permeable cloth 10 for preventing the matrix layer from collapsing or infiltrating, and the matrix bed is infiltrated with water. The water inlet pipe 2 is installed on the end surface of the water end, and the first water outlet pipe 12-1, the second water outlet pipe 12-2, and the third water outlet pipe 12-3 for adjusting the water level are arranged on the end surface of the water outlet end from top to bottom. The surface of the wetland system is covered with The film and the water outlet pipe for adjusting the water level constitute the heat preservation structure of the water in the bed body. Through the water holes on the water distribution plate, the water body evenly flows in the matrix bed body in a zigzag way, fully contacts with the corn cob layer 9, and increases the BOD 5 of the water body /NO 3 - , through the first water outlet pipe 12-1, the second water outlet pipe 12-2, and the third water outlet pipe 12-3 to adjust the water level in the matrix bed, and combine the water level adjustment with the film covering the matrix bed surface, Ensure the water temperature in the matrix bed, and then strengthen the denitrification effect of the horizontal submerged wetland system in winter. The layout density of the sampling pipes decreases from the water inlet to the water outlet. It is mainly concentrated at the front end of the matrix bed, creating conditions for aerobic nitrification at the front end of the matrix bed and anaerobic denitrification at the end, which is beneficial to the removal of nitrogen by wetlands, and is beneficial to the nitrification at the front end of the matrix bed and denitrification at the end .

所述的基质床体是由砖砌筑成的长方形的周边墙体1-1和周边墙体底部的底面1-2构成,基质床体长宽比为2︰1,高1.2米,底面是由自下向上的夯实20cm厚的素土层1-2-3、1.5mm厚的高密度聚乙烯防渗布层1-2-2和夯实10cm厚的粘土层1-2-1构成的复合结构。 The matrix bed body is composed of a rectangular peripheral wall 1-1 made of bricks and a bottom surface 1-2 at the bottom of the peripheral wall body. The matrix bed body has an aspect ratio of 2:1, a height of 1.2 meters, and a bottom surface of Composite consisting of tamped 20cm-thick plain soil layer 1-2-3, 1.5mm-thick high-density polyethylene anti-seepage cloth layer 1-2-2 and rammed 10cm-thick clay layer 1-2-1 from bottom to top structure.

所述的取样管4是由PVC制成的直径1.5cm的圆形空心管,空心管上每间隔8.0cm开有0.3cm的通气孔5。 The sampling tube 4 is a circular hollow tube with a diameter of 1.5 cm made of PVC, and the hollow tube has a ventilation hole 5 of 0.3 cm at intervals of 8.0 cm.

所述的玉米芯层9,玉米芯的粒径为0.5-3cm,在基质床体中后段竖向放置,铺设厚度1.0~3.0cm,高度80cm,宽度与基质床体的宽度相同。 The corncob layer 9 has a corncob particle size of 0.5-3 cm, is placed vertically in the middle and back of the matrix bed, has a thickness of 1.0-3.0 cm, a height of 80 cm, and the same width as the matrix bed.

所述的砂石层厚度为20cm、沸石层厚度为40cm、砾石铁屑层厚度为30cm,砂石粒径0.5~1.0cm、沸石粒径1.0~2.0cm、砾石粒径2.0~4.0cm,铁屑粒径0.5~1.0cm,铁屑与砾石的体积比1︰8~10。 The thickness of the sandstone layer is 20cm, the thickness of the zeolite layer is 40cm, the thickness of the gravel iron filings layer is 30cm, the particle size of the sandstone is 0.5~1.0cm, the particle size of the zeolite is 1.0~2.0cm, the particle size of the gravel is 2.0~4.0cm, iron The chip particle size is 0.5~1.0cm, and the volume ratio of iron filings and gravel is 1︰8~10.

所述的土工透水布为厚度1.5mm的涤纶布;所述的薄膜为厚度0.2mm的TPU防水透气膜。 The geotechnical permeable fabric is a polyester cloth with a thickness of 1.5mm; the film is a TPU waterproof and breathable membrane with a thickness of 0.2mm.

所述的布水板3、收水板11的顶部低于长向两端的基质床体的上沿,取样管4的上顶部高于基质床体的上沿,取样管最上部的通气孔要低于砂石层6的上平面,玉米芯层9的顶部要高于砂石层6的上平面,以保证使用效果。 The tops of the water distribution plate 3 and the water collection plate 11 are lower than the upper edge of the matrix bed at both ends of the lengthwise direction, the upper top of the sampling pipe 4 is higher than the upper edge of the matrix bed, and the vent hole at the top of the sampling pipe must be Lower than the upper plane of the gravel layer 6, the top of the corn cob layer 9 will be higher than the upper plane of the gravel layer 6 to ensure the use effect.

所述的砂石层表面可覆盖有砂土,并种植有芦苇、香蒲或黄花鸢尾等植物。 The surface of the sandstone layer can be covered with sandy soil, and plants such as reeds, cattails or yellow iris are planted.

由上述可知,本发明由布水板、基质床体、收水板以及复氧结构和保温结构共同构成强化冬季微污染水体脱氮的水平潜流湿地系统。 It can be seen from the above that the present invention consists of water distribution board, substrate bed, water collection board, reoxygenation structure and heat preservation structure to form a horizontal subsurface flow wetland system that strengthens the denitrification of slightly polluted water in winter.

所述的复氧结构(措施)为通气取样管和水位调节相结合,通气取样管纵向放置密度由大到小,水位根据基质床体内水中溶解氧浓度而调节; The reoxygenation structure (measure) is a combination of ventilation sampling tube and water level adjustment, the vertical density of the ventilation sampling tube is placed from large to small, and the water level is adjusted according to the concentration of dissolved oxygen in the water in the matrix bed;

所述保温结构(措施)为覆盖薄膜和水位调节相结合的方式,薄膜为厚度0.2mm的TPU透气薄膜,水位根据基质床体内水温而调节。 The heat preservation structure (measure) is a combination of covering film and water level adjustment. The film is a TPU breathable film with a thickness of 0.2 mm, and the water level is adjusted according to the water temperature in the matrix bed.

通气取样管材质为PVC,耐酸碱、耐腐蚀。通气取样管不规则布设、布设密度沿基质床体纵向由大到小,基质床体前端复氧能力高于后端,使得富氧水体主要集中在基质床体前端,为基质床体前端好氧硝化作用和末端厌氧反硝化作用创造了适宜条件,有利湿地对氮的去除效果。 The ventilation sampling tube is made of PVC, which is resistant to acid, alkali and corrosion. The ventilation sampling tubes are irregularly arranged, and the arrangement density is from large to small along the longitudinal direction of the matrix bed. The reoxygenation capacity of the front end of the matrix bed is higher than that of the rear end, so that the oxygen-enriched water is mainly concentrated at the front end of the matrix bed, which is aerobic for the front end of the matrix bed. Nitrification and terminal anaerobic denitrification create suitable conditions, which are beneficial to the nitrogen removal effect of wetlands.

纤维素碳源选用玉米芯,材料具备来源广泛、价格低廉、供碳能力强、不易堵塞基质床等优点。玉米芯在基质床体中后段竖向放置,水体水平曲折流动过程中同玉米芯充分接触,玉米芯浸出物的释放,提高废水的可生化性(BOD5/NO3 -),为反硝化作用创造有利条件,进而促进湿地对氮的去除效果。 The cellulose carbon source is corn cob, which has the advantages of wide source, low price, strong carbon supply capacity, and not easy to block the matrix bed. The corn cob is placed vertically in the middle and back of the matrix bed, and the water body fully contacts with the corn cob during the horizontal tortuous flow process, and the release of the corn cob extract improves the biodegradability of the wastewater (BOD 5 /NO 3 - ), which is denitrification The effect creates favorable conditions, and then promotes the removal effect of wetland on nitrogen.

将铁屑等工业废弃物应用于水平潜流湿地构建当中,综合运用电化学原理(铁屑/碳组成的内电解技术)提高微污染水体的可生化性,在微生物、植物、基质的共同作用下,实现对微污染水体的强化净化。 Apply iron filings and other industrial wastes to the construction of horizontal subsurface flow wetlands, and comprehensively use electrochemical principles (internal electrolysis technology composed of iron filings/carbon) to improve the biodegradability of micro-polluted water bodies. Under the joint action of microorganisms, plants, and substrates , to achieve enhanced purification of slightly polluted water.

并经实际试验,取得了非常满意的有益技术效果,其技术优势主要在于: And through actual tests, very satisfactory beneficial technical effects have been obtained, and its technical advantages mainly lie in:

通气取样管的不规则合理布设,在达到去污效果的同时,避免了曝气系统的动力消耗,节约运行成本,吨水处理费用不高于0.05元,而常规污水处理成本不低于0.4元/吨,污水处理费用仅是原处理费用的1/8,经济效果非常巨大; The irregular and reasonable layout of the ventilation and sampling pipes, while achieving the decontamination effect, avoids the power consumption of the aeration system and saves operating costs. The cost of water treatment per ton is not higher than 0.05 yuan, while the cost of conventional sewage treatment is not less than 0.4 yuan / ton, the sewage treatment cost is only 1/8 of the original treatment cost, and the economic effect is very huge;

工业废弃物、农作废弃物等材料应用于湿地构建当中,不但为废弃物处置提供场所,而且提高了废水可生化性,微污染水体的BOD5/NO3 -由起初的1.0左右可提升至2.0以上,进而促进湿地的去污效果; Industrial waste, agricultural waste and other materials are used in wetland construction, which not only provides a place for waste disposal, but also improves the biodegradability of wastewater. The BOD 5 /NO 3 of slightly polluted water can be increased from about 1.0 at the beginning to 2.0 or above, thereby promoting the decontamination effect of the wetland;

薄膜覆盖、水位调节(降水位利用地热保温)等不同保温措施同复氧措施的有机结合在解决保温(阻隔基质床体同外界的气体交换)和复氧矛盾的同时,湿地床内的水温可保持在10℃以上,溶解氧浓度不低于2mg/L,保证冬季该湿地系统的脱氮率不低于40%,正常情况下水平潜流湿地对TN的去除率仅维持在20%左右,本发明脱氮率远高于现有技术,并经实际应用得到了充分证明。 The organic combination of different heat preservation measures such as film covering, water level adjustment (precipitation level using geothermal heat preservation) and reoxygenation measures solves the contradiction between heat preservation (blocking the gas exchange between the matrix bed and the outside world) and reoxygenation, and the water temperature in the wetland bed can be adjusted. Keep the temperature above 10°C and the concentration of dissolved oxygen not lower than 2mg/L to ensure that the nitrogen removal rate of the wetland system in winter is not lower than 40%. Under normal circumstances, the removal rate of TN in horizontal subsurface flow wetlands is only maintained at about 20%. The denitrification rate of the invention is much higher than that of the prior art, and has been fully proved by practical application.

例1 example 1

如在辽宁某河口湿地工程采用本发明所述技术对湿地周边生活污水和部分工业废水进行处理,工程由污水预处理区、水平潜流湿地处理区(主体工艺)、表流湿地景观区组成,水平潜流湿地共铺设三种基质,种植层0.3m、小粒径砾石层0.5m、大粒径砾石层0.4m。水平潜流湿地配水采用PVC管道多点进水,有高、中、低三个水位,通过开启三个水位阀门进行水量调节。为保证湿地系统冬季正常运行,现场人员通过覆盖塑料膜、草帘子等材料对湿地系统进行保温,湿地系统内水温可维持在10~15℃,出水满足《城镇污水处理厂污染物排放标准》(GB18918-2002)一级标准的A标准。 For example, a estuary wetland project in Liaoning adopts the technology described in the present invention to treat domestic sewage and some industrial wastewater around the wetland. The project consists of a sewage pretreatment area, a horizontal subsurface flow wetland treatment area (main process), and a surface flow wetland landscape area. Three kinds of substrates are laid in the subsurface wetland, the planting layer is 0.3m, the small-size gravel layer is 0.5m, and the large-size gravel layer is 0.4m. The water distribution of the horizontal submerged wetland adopts PVC pipes for multi-point water intake, with three water levels of high, medium and low, and the water volume is adjusted by opening the three water level valves. In order to ensure the normal operation of the wetland system in winter, the on-site personnel covered the wetland system with plastic film, straw curtains and other materials to keep the wetland system warm. The water temperature in the wetland system can be maintained at 10-15°C, and the effluent meets the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" ( GB18918-2002) A standard of the first class standard.

例2: Example 2:

再如,在山西某河滩湿地工程采用本发明所述技术对上游河水、周边工业废水及生活污水进行处理,湿地主体处理工艺为“预处理沉淀池+表面流湿地+垂直流湿地”,垂直流湿地床内铺设1.5m厚不同规格的碎石填层,共分五层,从上到下,碎石粒径由小到大(3mm~100mm),通过基质层内的微生物吸收净化水质。表面层覆有砂土,其上种植有芦苇、香蒲、黄花鸢尾等植物。垂直流湿地中均匀布设有导气管,单根导气管总长1.8m,管壁上间隔30cm均匀开通气孔(孔径约5mm)。冬季芦苇等植物收割后,将植物秸秆、透气薄膜覆盖在潜流湿地表面,由于冬季处理水量小、水力停留时间长,冬季湿地对COD、氨氮的处理效率同其他季节相差不大,湿地出水主要污染物浓度达到地表水Ⅳ类水质标准。 For another example, a river beach wetland project in Shanxi adopts the technology described in the present invention to treat upstream river water, surrounding industrial wastewater and domestic sewage. The main treatment process of the wetland is "pretreatment sedimentation tank + surface flow wetland + vertical flow wetland". The wetland bed is paved with 1.5m thick gravel fill of different specifications, which is divided into five layers. From top to bottom, the gravel particle size ranges from small to large (3mm~100mm), and the water quality is purified through the absorption of microorganisms in the matrix layer. The surface layer is covered with sandy soil, on which plants such as reeds, cattails, and yellow iris are planted. Air ducts are evenly distributed in the vertical flow wetland. The total length of a single air duct is 1.8m, and the air holes (aperture diameter is about 5mm) are evenly opened on the pipe wall at intervals of 30cm. After reeds and other plants are harvested in winter, plant stalks and breathable films are covered on the surface of the subsurface wetland. Due to the small amount of water treated in winter and the long hydraulic retention time, the treatment efficiency of COD and ammonia nitrogen in winter wetlands is not much different from that in other seasons, and the wetland effluent is mainly polluted The concentration of pollutants meets the water quality standard of Class IV of surface water.

由上述资料可以清楚的看出,本发明可以强化冬季湿地床的脱氮能力,脱氮率不低于40%,并且维护简单,运行费用低,具有很强的实用性,是治理水污染上的一大创新,经济和社会效益巨大。 It can be clearly seen from the above data that the present invention can strengthen the denitrification capacity of the wetland bed in winter, the denitrification rate is not lower than 40%, and the maintenance is simple, the operation cost is low, and it has strong practicability. It is a major innovation with huge economic and social benefits.

Claims (9)

1. strengthen the horizontal subsurface flow wetland system of micropollutant water denitrogenation in winter for one kind, comprise water distribution board, matrix bed body and water collecting plate, it is characterized in that, matrix bed body along long to feed-water end inner face be provided with the water distribution board (3) being upwards parallel to matrix bed body end face, form between water distribution board and feed-water end inner face (13) between water distribution, matrix bed body along long to water side inner face be provided with the water collecting plate (11) being upwards parallel to matrix bed body end face, form between water collecting plate and water side inner face and receive (14) between water, leading portion in the matrix bed body formed between water distribution board and water collecting plate and stage casing are placed with the stopple coupon (4) of multiple tracks ventilation vertically upward, each stopple coupon has ventilating pit (5), in matrix bed body, back segment is placed with vertically upward and is parallel to the corn sandwich layer (9) of water collecting plate inner face as Mierocrystalline cellulose carbon source, water distribution board is identical with water collecting plate structure, water distribution board and water collecting plate are evenly equipped with limbers (3-1), sand stone layer (6) is filled with from top to bottom successively in matrix bed body between water distribution board and water collecting plate, zeolite layer (7), gravel iron filings layer (8), between sand stone layer (6) and zeolite layer (7), be provided with between zeolite layer (7) and gravel iron filings layer (8) for prevent hypothallus from caving in or under the permeable cloth of geotechnique (10) that oozes, the end face of matrix bed body feed-water end is equipped with water inlet pipe (2), the end face of water side is provided with the first rising pipe (12-1) for regulating water level from top to bottom, second rising pipe (12-2), 3rd rising pipe (12-3), wet land system surface coverage has film, with the insulation construction regulating the rising pipe of water level to form water in bed body, by the limbers on water distribution board, water body is Tortuous flow in matrix bed body uniformly, fully contact with corn sandwich layer (9), improve the BOD of water body 5/ NO 3 -, by the first rising pipe (12-1), second rising pipe (12-2), 3rd rising pipe (12-3) regulates the water level in matrix bed body, regulation of level is combined with the coating film measure of matrix bed surface, ensure the water temperature in matrix bed body, and then strengthen the denitrification effect in winter of horizontal subsurface flow wetland system, the layout density of stopple coupon is reduced to water side successively by feed-water end, matrix bed body front end reoxygenation ability is higher than rear end, oxygen enrichment water body is made mainly to concentrate on matrix bed body front end, for the aerobic nitrification effect of matrix bed body front end and the effect of end anaerobic denitrifying create conditions, favourable wetland is to the removal effect of nitrogen, benefit the carrying out of matrix bed body front end nitrification and end denitrification.
2. the horizontal subsurface flow wetland system of strengthening micropollutant water denitrogenation in winter according to claim 1, it is characterized in that, described matrix bed body be by the brick rectangular periphery body of wall (1-1) that builds up and periphery body of wall bottom bottom surface (1-2) form, matrix bed body long-width ratio is 2 ︰ 1, high 1.2 meters, bottom surface is the composite structure be made up of the thick high density polyethylene(HDPE) antiseepage layer of cloth (1-2-2) of the thick plain soil layer (1-2-3) of bottom-up compacting 20cm, 1.5mm and the thick clay seam (1-2-1) of compacting 10cm.
3. the horizontal subsurface flow wetland system of strengthening micropollutant water denitrogenation in winter according to claim 1, it is characterized in that, described stopple coupon (4) is the circular hollow tube of the diameter 1.5cm be made up of PVC, open tube has the ventilating pit (5) of 0.3cm at interval of 0.8cm.
4. the horizontal subsurface flow wetland system of strengthening micropollutant water denitrogenation in winter according to claim 1, it is characterized in that, described corn sandwich layer (9), the particle diameter of corn cob is 0.5-3cm, vertically place in matrix bed body posterior segment, laying depth 1.0 ~ 3.0cm, height 80cm, width is identical with the width of matrix bed body.
5. the horizontal subsurface flow wetland system of strengthening micropollutant water denitrogenation in winter according to claim 1, it is characterized in that, described sand stone layer thickness is 20cm, zeolite layer thickness is 40cm, gravel iron filings layer thickness is 30cm, gravel size 0.5 ~ 1.0cm, sized zeolite particles 1.0 ~ 2.0cm, grain size of gravel 2.0 ~ 4.0cm, iron filings particle diameter 0.5 ~ 1.0cm, volume ratio 1 ︰ 8 ~ 10 of iron filings and gravel.
6. the horizontal subsurface flow wetland system of strengthening micropollutant water denitrogenation in winter according to claim 1, it is characterized in that, the permeable cloth of described geotechnique is the woven dacron of thickness 1.5mm.
7. the horizontal subsurface flow wetland system of strengthening micropollutant water denitrogenation in winter according to claim 1, it is characterized in that, described film is the TPU waterproof ventilated membrane of thickness 0.2mm.
8. the horizontal subsurface flow wetland system of strengthening micropollutant water denitrogenation in winter according to claim 1, it is characterized in that, described water distribution board (3), the top of water collecting plate (11) are lower than the long upper edge to the matrix bed body at two ends, the upper top of stopple coupon (4) is higher than the upper edge of matrix bed body, the ventilating pit of stopple coupon topmost will lower than the upper plane of sand stone layer (6), and the top of corn sandwich layer (9) is higher than the upper plane of sand stone layer (6).
9. the horizontal subsurface flow wetland system of strengthening micropollutant water denitrogenation in winter according to claim 1, it is characterized in that, described sand stone layer surface coverage has sand, and kind is implanted with reed, cattail or wilson iris plant.
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CN107151056A (en) * 2017-06-27 2017-09-12 郑州大学环境技术咨询工程有限公司 It is a kind of to strengthen the horizontal drowned flow artificial wet land system of denitrification
CN107540086A (en) * 2017-09-22 2018-01-05 中国科学院武汉植物园 Handle the denitrification denitrogenation bed system of nitrate nitrogen sewage
CN108640416A (en) * 2018-04-28 2018-10-12 江西怡杉环保股份有限公司 A kind of wetland ventilating system

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CN105399208A (en) * 2015-11-20 2016-03-16 云南大学 Enhanced constructed wetland denitration system and method
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CN107540086A (en) * 2017-09-22 2018-01-05 中国科学院武汉植物园 Handle the denitrification denitrogenation bed system of nitrate nitrogen sewage
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