WO2020133553A1 - Method for treating high ammonia-nitrogen wastewater of the coal chemical industry with reinforced sbr process pool - Google Patents

Method for treating high ammonia-nitrogen wastewater of the coal chemical industry with reinforced sbr process pool Download PDF

Info

Publication number
WO2020133553A1
WO2020133553A1 PCT/CN2019/000245 CN2019000245W WO2020133553A1 WO 2020133553 A1 WO2020133553 A1 WO 2020133553A1 CN 2019000245 W CN2019000245 W CN 2019000245W WO 2020133553 A1 WO2020133553 A1 WO 2020133553A1
Authority
WO
WIPO (PCT)
Prior art keywords
sbr
tank
ammonia nitrogen
pool
coal chemical
Prior art date
Application number
PCT/CN2019/000245
Other languages
French (fr)
Chinese (zh)
Inventor
赵美丽
曲涛
王伟
陈永献
韩嘉
孔环
蒋娜
孙秀英
Original Assignee
兖矿国宏化工有限责任公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 兖矿国宏化工有限责任公司 filed Critical 兖矿国宏化工有限责任公司
Priority to KR1020217007768A priority Critical patent/KR20210036407A/en
Publication of WO2020133553A1 publication Critical patent/WO2020133553A1/en

Links

Images

Classifications

    • 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
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1263Sequencing batch reactors [SBR]
    • 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
    • C02F3/006Regulation methods for biological treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/16Nitrogen compounds, e.g. ammonia
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/07Alkalinity
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/08Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/14NH3-N
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/22O2
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/44Time
    • 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

Abstract

The present application belongs to the field of industrial wastewater treatments, and relates to a method for treating wastewater of the coal chemical industry, specifically a method for treating high ammonia-nitrogen wastewater of the coal chemical industry with a reinforced SBR process pool. The method involves (1) controlling and adjusting the indicators of water quality in an adjusting pool: an ammonia nitrogen concentration, a COD concentration, an alkalinity and a C:N ratio; (2) adjusting the dissolved oxygen degree, a high inlet water load, and sludge concentration of the SBR pool, wherein the sludge concentration is determined according to the water quality conditions of the high ammonia-nitrogen wastewater of the coal chemical industry and the season; (3) alternatively charging the SBR pool with water, using a sequence batch reactor, and flowing the effluent water back into the adjusting pool through a return pipe, wherein the amount of the water flowed back is determined according to the concentration of the high ammonia-nitrogen wastewater of the coal chemical industry; and (4) adjusting the inlet and outlet valves of a circulating water pump on the SBR pool, so as to adjust the mixing degree of sludge, water and oxygen in the pool and to adjust the dissolved oxygen efficiency.

Description

一种强化SBR工艺池处理煤化工高氨氮废水的方法Method for strengthening SBR process pool to treat coal chemical industry high ammonia nitrogen wastewater 技术领域Technical field
本申请属于工业废水处理领域,涉及一种煤化工废水处理方法,具体地说是一种强化SBR工艺池处理煤化工高氨氮废水的方法。The present application belongs to the field of industrial wastewater treatment, and relates to a method for treating coal chemical wastewater, in particular to a method for treating high ammonia nitrogen wastewater in coal chemical industry by using enhanced SBR process pool.
背景技术Background technique
煤化工废水是指各种煤加工过程中产生的生产废水,包括焦化废水、煤气化废水、煤制油废水、合成废水等。该类废水的水质极其复杂,含有酚类、烷烃类、多环芳烃类、氨氮等有毒、难降解的物质,属于典型的难生物降解的工业废水。长期以来,高浓度氨氮在工业废水中一直是一大难题,其主要原因有以下两个方面矛盾,一方面是煤化工废水中污染物毒性大,污染物浓度高,抑制硝化细菌的生长,并极易受污泥物质抑制而硝化能力降低。另一方面处理这部分废水中难降解的污泥物含量高,好氧菌处理周期长,造成菌群结构的变化不利于硝化细菌的繁殖。Coal chemical wastewater refers to production wastewater generated during various coal processing processes, including coking wastewater, coal gasification wastewater, coal-to-oil wastewater, and synthetic wastewater. The water quality of this type of wastewater is extremely complex, containing toxic, refractory substances such as phenols, alkanes, polycyclic aromatic hydrocarbons, ammonia nitrogen, etc. It is a typical industrial wastewater that is difficult to biodegrade. For a long time, high concentration of ammonia nitrogen has been a big problem in industrial wastewater. The main reasons are the contradiction of the following two aspects. On the one hand, the pollutants in coal chemical wastewater are highly toxic and the concentration of pollutants is high, which inhibits the growth of nitrifying bacteria, and It is extremely easy to be inhibited by sludge material and the nitrification ability is reduced. On the other hand, the treatment of this part of wastewater has a high content of non-degradable sludge, and the aerobic bacteria treatment cycle is long, resulting in a change in the structure of the bacterial community is not conducive to the reproduction of nitrifying bacteria.
A-O法、氧化沟法处理的煤化工废水已经取得良好的有机污染物去除效果,但是A-O、氧化沟法耐冲击能力较差,经常会受到进水污染物的毒害造成氨氮脱出率大幅度降低,甚至出水氨氮超标。由于现在环保标准提高,煤化工废水的排放标准相应提高,由于煤质变化以及生产环节工艺调整、生化系统自身波动等因素的影响,A-O、氧化沟法很难实现高氨氮废水中有机污染物和氨氮的高效去除。近几年,新提起的厌氧氨氧化技术虽然在城市污水厂已用研究和应用,但是由于厌氧氨氧化的‘主角’-红菌对环境要求比较苛刻,煤化工废水的复杂性和高浓度让有特殊需求的优势菌种红菌难以适应和生存。SBR法的独特运行方式能在同一个反应池内交替进行好氧、缺氧和厌氧的反应环境,池内共存多样化的菌群,菌群数量和菌群结构造就了很强的耐冲击能力和对有毒有害物质的降解能力。目前,SBR工艺在越来越多的煤化工企业工程中应用。值得注意的是,单纯的SBR工艺控制在进水负荷和抗冲击能力上无法满足煤化工废水的处理需求。因此,采用简洁、高效的技术手段加强SBR工艺高氨氮处理能力是煤化工废水生物处理技术领域新的发展方向。The coal chemical wastewater treated by the AO method and oxidation ditch method has achieved good organic pollutant removal effect, but the AO and oxidation ditch method has poor impact resistance and is often poisoned by the influent pollutants, which greatly reduces the ammonia nitrogen removal rate. Even the ammonia nitrogen in the effluent exceeds the standard. Due to the improvement of environmental protection standards, the discharge standards of coal chemical wastewater have been increased accordingly. Due to the influence of coal quality changes, production process adjustments, and biochemical system fluctuations, AO and oxidation ditch methods are difficult to achieve organic pollutants and Efficient removal of ammonia nitrogen. In recent years, although the newly introduced anaerobic ammonia oxidation technology has been used and researched and applied in urban sewage treatment plants, due to the severe environmental requirements of anaerobic ammonia oxidation'protagonist'-Rhodobacter, coal chemical wastewater is complicated and high The concentration makes it difficult to adapt and survive the dominant strain Rhodobacter with special needs. The unique operating mode of the SBR method can alternately carry out aerobic, anoxic and anaerobic reaction environments in the same reaction tank. A variety of bacterial groups coexist in the tank, and the number and structure of the bacterial groups create a strong impact resistance and The ability to degrade toxic and harmful substances. At present, the SBR process is used in more and more coal chemical enterprise projects. It is worth noting that the simple SBR process control cannot meet the treatment requirements of coal chemical wastewater in terms of influent load and impact resistance. Therefore, the use of concise and efficient technical means to enhance the high ammonia nitrogen treatment capacity of the SBR process is a new development direction in the field of coal chemical wastewater biological treatment technology.
发明内容Summary of the invention
为了解决上述问题,本申请提供了一种强化SBR工艺池处理煤化工高氨氮废水的方法,本申请是通过下述方案实现的:In order to solve the above problems, this application provides an enhanced SBR process tank to treat coal chemical industry high ammonia nitrogen wastewater. This application is achieved through the following scheme:
一种强化SBR工艺池处理煤化工高氨氮废水的装置,包括通过管路依次连接的调节池、SBR池组和蓄水池,所述SBR池组包括至少2个SBR池,所述SBR池并联设置,所述蓄水池通过回流管与调节池相连接,所述回流管上设有回流泵,所述调节池上设有煤化工生产生活废水进水管,所述调节池内设有在线氨氮分析仪器,所述SBR池内设有在线溶氧仪器,所述在线溶氧仪器与曝气装置相连接,所述曝气装置上设有相配套的风机。A device for strengthening SBR process pool to treat high ammonia nitrogen wastewater of coal chemical industry includes a regulating tank, an SBR pool group and a storage tank connected in sequence through a pipeline. The SBR pool group includes at least two SBR pools, and the SBR pools are connected in parallel The storage tank is connected to the adjustment tank through a return pipe, a return pump is provided on the return pipe, a coal chemical production and domestic wastewater inlet pipe is provided on the adjustment tank, and an online ammonia nitrogen analysis instrument is provided in the adjustment tank The SBR tank is equipped with an online dissolved oxygen instrument. The online dissolved oxygen instrument is connected to an aeration device, and a matching fan is provided on the aeration device.
一种强化SBR工艺池处理煤化工高氨氮废水的方法,(1)控制调节池内水质的指标:氨氮浓度、COD浓度、碱度和C∶N比;(2)调节SBR池的溶氧度、高进水负荷和污泥浓度,污泥浓度根据煤化工高氨氮废水的水质条件和季节而定;(3)SBR池采用序批式反应器交替进 水,出水通过回流管回流进入调节池,回流的水量根据煤化工高氨氮废水的浓度来决定;(4)通过调整SBR池上循环水泵的进出口阀门,调整池内污泥、水、氧气的混合程度调节溶氧效率。A method for enhancing the treatment of high ammonia nitrogen wastewater in coal chemical industry by the SBR process tank, (1) controlling the indicators of the water quality in the adjusting tank: ammonia nitrogen concentration, COD concentration, alkalinity and C:N ratio; (2) adjusting the dissolved oxygen level of the SBR tank, High influent load and sludge concentration, the sludge concentration is determined according to the water quality conditions and seasons of coal chemical industry high ammonia nitrogen wastewater; (3) SBR tank uses sequential batch reactors to alternately enter water, and the effluent returns to the regulating tank through the return pipe. The water volume is determined according to the concentration of high ammonia nitrogen wastewater in coal chemical industry; (4) By adjusting the inlet and outlet valves of the circulating water pump on the SBR tank, the mixing degree of sludge, water and oxygen in the tank is adjusted to adjust the dissolved oxygen efficiency.
优选的,所述SBR池的出水量与调节池内煤化工废水的体积比为1/6-4/3。Preferably, the ratio of the water output of the SBR tank to the volume of the coal chemical wastewater in the adjusting tank is 1/6-4/3.
优选的,所述SBR池的溶氧的高限为2.0mg/L,低溶氧控制通过SBR池内在线溶氧仪器和曝气装置得已实现。Preferably, the upper limit of the dissolved oxygen in the SBR tank is 2.0 mg/L, and the control of low dissolved oxygen is achieved by the on-line dissolved oxygen instrument and aeration device in the SBR tank.
优选的,所述SBR池内污泥的污泥龄为5-40天,通过SBR池内剩余污泥的排放量控制SBR池内污泥量的停留时间。Preferably, the sludge age of the sludge in the SBR pool is 5-40 days, and the residence time of the sludge volume in the SBR pool is controlled by the discharge amount of the remaining sludge in the SBR pool.
优选的,所述调节池内池水的氨氮浓度为300mg/L,通过在线氨氮分析仪器,调整煤化工高氨氮废水和SBR出水的比例来控制氨氮浓度。Preferably, the ammonia nitrogen concentration of the water in the adjustment tank is 300 mg/L, and the ammonia nitrogen concentration can be controlled by adjusting the ratio of coal chemical high ammonia nitrogen wastewater and SBR effluent through an online ammonia nitrogen analysis instrument.
优选的,所述调节池内池水的COD浓度低于1200mg/L,C∶N比为4;通过手动分析,调整调节池的含醇废水量;调节池设置含醇废水专用管线,调整调节池的COD,稳定调节池的氨氮、COD、C∶N比,保持SBR池的进水稳定;SBR池通过曝气装置、风机和在线溶氧仪器的协同作用,实时控制SBR池内溶氧值。Preferably, the COD concentration of the pool water in the regulating tank is lower than 1200mg/L, and the C:N ratio is 4; by manual analysis, the amount of alcohol-containing wastewater in the regulating tank is adjusted; COD, stabilizing the ratio of ammonia nitrogen, COD and C:N in the tank to keep the water in the SBR tank stable; the SBR tank controls the dissolved oxygen value in the SBR tank in real time through the synergy of the aeration device, fan and online dissolved oxygen instrument.
优选的,所述调节池内的碱度低于1000mg/L,通过调整液碱的投加量控制调节池的碱度在需求值。Preferably, the alkalinity in the adjustment tank is lower than 1000 mg/L, and the alkalinity of the adjustment tank is controlled at a required value by adjusting the amount of liquid alkali added.
优选的,所述SBR池内的曝气量是指通过SBR池内进气阀门开度和风机变频频率进而改变池内曝气量的大小,控制曝气方式采用连续曝气,曝气量为70m 3/min-80m 3/min。 Preferably, the aeration amount in the SBR pool refers to the size of the aeration amount in the pool is changed by the opening of the intake valve in the SBR pool and the frequency conversion frequency of the fan, the continuous aeration is used to control the aeration mode, the aeration amount is 70m 3 / min-80m 3 /min.
优选的,所述SBR池内污泥浓度为3500-5500mg/L;优选的冬季污泥浓度为5000-5500mg/L,夏季污泥浓度为3500-4000mg/L。Preferably, the sludge concentration in the SBR tank is 3500-5500 mg/L; the preferred winter sludge concentration is 5000-5500 mg/L, and the summer sludge concentration is 3500-4000 mg/L.
优选的,所述SBR池的水力停留时间为6-8h,水力停留时间根据进水负荷变化调整,进水负荷稳定,停留时间为6小时,进水增加波动,在线溶氧值未达到2mg/L,依据溶氧值延长停留时间,直至出水合格。Preferably, the hydraulic retention time of the SBR pool is 6-8h, the hydraulic retention time is adjusted according to the change of the inlet water load, the inlet water load is stable, the residence time is 6 hours, the inlet water increases and fluctuates, and the online dissolved oxygen value does not reach 2mg/ L, extend the residence time according to the dissolved oxygen value until the effluent is qualified.
优选的,通过蓄水池回流出水调整调节池的氨氮浓度。Preferably, the ammonia nitrogen concentration of the adjustment tank is adjusted through the backflow water from the storage tank.
本申请的有益效果:本发明是以多效调节池和SBR池强化煤化工高氨氮废水的氨氮处理效率,同时促进有毒高浓度难降解有机物的分解,从而有助于拓展SBR工艺在煤化工高氨氮废水处理中的实际应用。本发明的特点是借助于SBR池内多功能反应池和序批式处理器的多样菌群结构和SBR池的强效耐冲击的优势,利用好氧菌对煤化工废水的抗抑制原理,通过多效调节池的调节对多组SBR池交替进行序批式废水处理,SBR池低氧、高污泥浓度、低污泥龄来抵抗煤化工高浓度氨氮废水中氨氮的高效降解脱除。本发明具有抗负荷冲击能力强、氨氮脱除效率高,运行成本低的优点。The beneficial effects of the present application: The present invention is to strengthen the ammonia nitrogen treatment efficiency of coal chemical industry high ammonia nitrogen wastewater with multi-effect adjustment tank and SBR tank, and at the same time promote the decomposition of toxic high concentration refractory organic matter, thereby helping to expand the SBR process in coal chemical industry. Practical application in ammonia nitrogen wastewater treatment. The feature of the present invention is to utilize the multi-bacterial structure of the multifunctional reaction tank and sequential batch processor in the SBR tank and the advantages of the strong impact resistance of the SBR tank. The adjustment of the effect adjustment tank alternately performs sequential batch-type wastewater treatment on multiple groups of SBR tanks. The SBR tank has low oxygen, high sludge concentration and low sludge age to resist the efficient degradation and removal of ammonia nitrogen in coal chemical industry high concentration ammonia nitrogen wastewater. The invention has the advantages of strong resistance to load impact, high ammonia nitrogen removal efficiency, and low operating cost.
附图说明BRIEF DESCRIPTION
图1为本发明的技术方案的工艺流程图;Figure 1 is a process flow diagram of the technical solution of the present invention;
图中,1、调节池,2、蓄水池,3、SBR池,4、回流管。In the picture, 1, adjustment tank, 2, reservoir, 3, SBR pool, 4, return pipe.
具体实施方式detailed description
实施例1Example 1
一种强化SBR工艺池处理煤化工高氨氮废水的装置,包括通过管路依次连接的调节池 1、SBR池组和蓄水池2,所述SBR池组包括至少2个SBR池3,所述SBR池3并联设置,所述蓄水池2通过回流管4与调节池1相连接,所述回流管4上设有回流泵,所述调节池1上设有煤化工生产生活废水进水管,所述调节池内设有在线氨氮分析仪器,所述SBR池内设有在线溶氧仪器,所述在线溶氧仪器与曝气装置相连接,所述曝气装置上设有相配套的风机。A device for strengthening SBR process pool to treat high ammonia nitrogen wastewater in coal chemical industry, including regulating tank 1, SBR pool group and storage tank 2 connected in sequence through pipelines, the SBR pool group includes at least 2 SBR pools 3, SBR tanks 3 are arranged in parallel. The storage tank 2 is connected to the adjustment tank 1 through a return pipe 4. The return pipe 4 is provided with a return pump. The adjustment tank 1 is provided with a coal chemical production domestic wastewater inlet pipe. The regulating tank is provided with an online ammonia nitrogen analysis instrument, and the SBR tank is provided with an online dissolved oxygen instrument. The online dissolved oxygen instrument is connected to an aeration device, and a matching fan is provided on the aeration device.
实施例2Example 2
下面结合附图1对本发明的技术方案的流程工艺图详细说明,本实施例强化SBR工艺处理煤化工高氨氮废水氨氮处理效率的方法是这样实现的:The flow chart of the technical solution of the present invention will be described in detail below with reference to FIG. 1. The method for enhancing the ammonia nitrogen treatment efficiency of the SBR process for treating coal chemical industry high ammonia nitrogen wastewater is implemented as follows:
一种强化SBR工艺池处理煤化工高氨氮废水的方法,(1)控制调节池内水质的指标:氨氮浓度、COD浓度、碱度和C∶N比;(2)调节SBR池的溶氧度、高进水负荷和污泥浓度,污泥浓度根据煤化工高氨氮废水的水质条件和季节而定;(3)SBR池采用序批式反应器交替进水,出水通过回流管回流进入调节池,回流的水量根据煤化工高氨氮废水的浓度来决定;(4)通过调整SBR池上循环水泵的进出口阀门,调整池内污泥、水、氧气的混合程度调节溶氧效率;A method for enhancing the treatment of high ammonia nitrogen wastewater in coal chemical industry by the SBR process tank, (1) controlling the indicators of the water quality in the adjusting tank: ammonia nitrogen concentration, COD concentration, alkalinity and C:N ratio; (2) adjusting the dissolved oxygen level of the SBR tank, High influent load and sludge concentration, the sludge concentration is determined according to the water quality conditions and seasons of coal chemical industry high ammonia nitrogen wastewater; (3) SBR tank uses sequential batch reactors to alternately enter water, and the effluent returns to the regulating tank through the return pipe. The amount of water is determined according to the concentration of high ammonia nitrogen wastewater in coal chemical industry; (4) By adjusting the inlet and outlet valves of the circulating water pump on the SBR tank, the mixing degree of sludge, water and oxygen in the tank is adjusted to adjust the dissolved oxygen efficiency;
优选的,所述SBR池的出水量与调节池内煤化工废水的体积比为1/6-4/3;Preferably, the ratio of the water output of the SBR tank to the volume of the coal chemical wastewater in the adjusting tank is 1/6-4/3;
优选的,所述SBR池的溶氧的高限为2.0mg/L,低溶氧控制通过SBR池内在线溶氧仪器和曝气装置得已实现;Preferably, the high limit of dissolved oxygen in the SBR tank is 2.0 mg/L, and the control of low dissolved oxygen is achieved by the online dissolved oxygen instrument and aeration device in the SBR tank;
优选的,所述SBR池内污泥的污泥龄为5-40天,通过SBR池内剩余污泥的排放量控制SBR池内污泥量的停留时间,如,对SBR池进行排泥,每次排泥时间30~60min,保持SBR池污泥龄5天-40天,同时向SBR-A/B/C/D池补充活性良好污泥;Preferably, the sludge age of the sludge in the SBR pool is 5-40 days, and the residence time of the sludge volume in the SBR pool is controlled by the discharge amount of the remaining sludge in the SBR pool, for example, the sludge in the SBR pool is discharged every time The sludge time is 30~60min, to keep the sludge age of the SBR tank from 5 days to 40 days, and to supplement the SBR-A/B/C/D pool with good activated sludge;
优选的,所述调节池内池水的氨氮浓度为300mg/L,通过在线氨氮分析仪器,调整煤化工高氨氮废水和SBR出水的比例来控制氨氮浓度;Preferably, the ammonia nitrogen concentration of the water in the adjusting tank is 300 mg/L, and the ammonia nitrogen concentration can be controlled by adjusting the ratio of coal chemical industry high ammonia nitrogen wastewater and SBR effluent through an online ammonia nitrogen analysis instrument;
优选的,所述调节池内池水的COD浓度低于1200mg/L,C∶N比为4;通过手动分析,调整调节池的含醇废水量;调节池设置含醇废水专用管线,调整调节池的COD,稳定调节池的氨氮、COD、C∶N比,保持SBR池的进水稳定;SBR池通过曝气装置、风机和在线溶氧仪器的协同作用,实时控制SBR池内溶氧值;Preferably, the COD concentration of the pool water in the regulating tank is lower than 1200mg/L, and the C:N ratio is 4; by manual analysis, the amount of alcohol-containing wastewater in the regulating tank is adjusted; COD, stable adjustment of ammonia nitrogen, COD, C:N ratio in the tank to keep the water inlet of the SBR tank stable; the SBR tank controls the dissolved oxygen value in the SBR tank in real time through the cooperative action of the aeration device, fan and online dissolved oxygen instrument;
优选的,所述调节池内的碱度低于1000mg/L,通过调整液碱的投加量控制调节池的碱度在需求值;Preferably, the alkalinity in the adjusting tank is lower than 1000mg/L, and the alkalinity of the adjusting tank is controlled at a required value by adjusting the amount of liquid alkali added;
优选的,所述SBR池内的曝气量是指通过SBR池内进气阀门开度和风机变频频率进而改变池内曝气量的大小,控制曝气方式采用连续曝气,曝气量为70m 3/min-80m 3/min,连续曝气3小时,曝气完后继续搅拌1小时,沉淀1小时,滗水1小时,而后通过池内在线溶氧值≤2mg/L控制曝气时间; Preferably, the aeration amount in the SBR pool refers to the size of the aeration amount in the pool is changed by the opening of the intake valve in the SBR pool and the frequency conversion frequency of the fan, the continuous aeration is used to control the aeration mode, the aeration amount is 70m 3 / min-80m 3 /min, continuous aeration for 3 hours, continue stirring for 1 hour after aeration, settling for 1 hour, decanting for 1 hour, and then control the aeration time by the online dissolved oxygen value in the tank ≤ 2mg/L;
优选的,所述SBR池内污泥浓度为3500-5500mg/L;优选的冬季污泥浓度为5000-5500mg/L,夏季污泥浓度为3500-4000mg/L;Preferably, the sludge concentration in the SBR tank is 3500-5500mg/L; the preferred winter sludge concentration is 5000-5500mg/L, and the summer sludge concentration is 3500-4000mg/L;
优选的,所述SBR池的水力停留时间为6-8h,水力停留时间根据进水负荷变化调整,进水负荷稳定,停留时间为6小时,进水增加波动,在线溶氧值未达到2mg/L,依据溶氧值延长停留时间,直至出水合格;Preferably, the hydraulic retention time of the SBR pool is 6-8h, the hydraulic retention time is adjusted according to the change of the inlet water load, the inlet water load is stable, the residence time is 6 hours, the inlet water increases and fluctuates, and the online dissolved oxygen value does not reach 2mg/ L, extend the residence time according to the dissolved oxygen value until the effluent is qualified;
优选的,通过蓄水池回流出水调整调节池的氨氮浓度。Preferably, the ammonia nitrogen concentration of the adjustment tank is adjusted through the backflow water from the storage tank.
Figure PCTCN2019000245-appb-000001
Figure PCTCN2019000245-appb-000001

Claims (10)

  1. 一种强化SBR工艺池处理煤化工高氨氮废水的装置,其特征在于,包括通过管路依次连接的调节池、SBR池组和蓄水池,所述SBR池组包括至少2个SBR池,所述SBR池并联设置,所述蓄水池通过回流管与调节池相连接,所述回流管上设有回流泵,所述调节池上设有煤化工生产生活废水进水管,所述调节池内设有在线氨氮分析仪器,所述SBR池内设有在线溶氧仪器,所述在线溶氧仪器与曝气装置相连接,所述曝气装置上设有相配套的风机。A device for strengthening SBR process pool to treat high ammonia nitrogen wastewater in coal chemical industry is characterized in that it includes a regulating tank, an SBR pool group and a storage tank connected in sequence through a pipeline. The SBR pool group includes at least two SBR pools. The SBR tanks are arranged in parallel, the storage tank is connected to the adjustment tank through a return pipe, a return pump is provided on the return pipe, a water inlet pipe for coal chemical production and domestic wastewater is provided on the adjustment tank, and the adjustment tank is provided with An online ammonia nitrogen analysis instrument, an online dissolved oxygen instrument is provided in the SBR tank, the online dissolved oxygen instrument is connected to an aeration device, and a matching fan is provided on the aeration device.
  2. 如权利要求1所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,(1)控制调节池内水质的指标:氨氮浓度、COD浓度、碱度和C∶N比;(2)调节SBR池的溶氧度、高进水负荷和污泥浓度,污泥浓度根据煤化工高氨氮废水的水质条件和季节而定;(3)SBR池采用序批式反应器交替进水,出水通过回流管回流进入调节池,回流的水量根据煤化工高氨氮废水的浓度来决定;(4)通过调整SBR池上循环水泵的进出口阀门,调整池内污泥、水、氧气的混合程度调节溶氧效率。The method for enhancing the treatment of high-nitrogen nitrogen wastewater in coal chemical industry by the SBR process tank according to claim 1, characterized in that: (1) the indicators for controlling the water quality in the adjusting tank: ammonia nitrogen concentration, COD concentration, alkalinity and C:N ratio; (2) Adjust the dissolved oxygen level, high influent load and sludge concentration of the SBR tank, the sludge concentration is determined according to the water quality conditions and seasons of the high ammonia nitrogen wastewater of the coal chemical industry; (3) The SBR pool adopts sequential batch reactors to alternately feed water, The effluent flows back into the adjustment tank through the return pipe, and the amount of returned water is determined according to the concentration of high ammonia nitrogen wastewater in coal chemical industry; (4) By adjusting the inlet and outlet valves of the circulating water pump on the SBR tank, the mixing degree of sludge, water and oxygen in the tank is adjusted to adjust the solution Oxygen efficiency.
  3. 如权利要求2所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,所述SBR池的出水量与调节池内煤化工废水的体积比为1/6-4/3。The method for enhancing the treatment of coal chemical industry high ammonia nitrogen wastewater by the SBR process pool according to claim 2, characterized in that the volume ratio of the water output of the SBR tank to the volume of coal chemical industry wastewater in the regulating tank is 1/6-4/3 .
  4. 如权利要求2所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,所述SBR池的溶氧的高限为2.0mg/L,低溶氧控制通过SBR池内在线溶氧仪器和曝气装置得已实现。The method for enhancing the treatment of high ammonia nitrogen wastewater in coal chemical industry by the SBR process tank according to claim 2, characterized in that the high limit of dissolved oxygen in the SBR tank is 2.0 mg/L, and the low dissolved oxygen is controlled online through the SBR tank Dissolved oxygen instruments and aeration devices have been realized.
  5. 如权利要求2所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,所述SBR池内污泥的污泥龄为5-40天,通过SBR池内剩余污泥的排放量控制SBR池内污泥量的停留时间。The method for enhancing the treatment of coal chemical industry high ammonia nitrogen wastewater by the SBR process tank according to claim 2, characterized in that the sludge age of the sludge in the SBR tank is 5-40 days, and is discharged through the remaining sludge in the SBR tank The amount controls the residence time of the amount of sludge in the SBR tank.
  6. 如权利要求2所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,所述调节池内池水的氨氮浓度为300mg/L,通过在线氨氮分析仪器调整煤化工高氨氮废水和SBR出水的比例来控制氨氮浓度。The method for enhancing the treatment of coal chemical industry high ammonia nitrogen wastewater by the SBR process pool according to claim 2, characterized in that the ammonia nitrogen concentration of the pool water in the adjusting tank is 300mg/L, and the coal chemical industry high ammonia nitrogen wastewater is adjusted by an online ammonia nitrogen analysis instrument And SBR effluent ratio to control the concentration of ammonia nitrogen.
  7. 如权利要求2所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,所述调节池内池水的COD浓度低于1200mg/L,C∶N比为4;通过手动分析,调整调节池的含醇废水量;调节池设置含醇废水专用管线,调整调节池的COD,稳定调节池的氨氮、COD、C∶N比,保持SBR池的进水稳定;SBR池通过曝气装置、风机和在线溶氧仪器的协同作用,实时控制SBR池内溶氧值。The method for enhancing the treatment of coal chemical industry high ammonia nitrogen wastewater by the SBR process tank according to claim 2, characterized in that the COD concentration of the pool water in the adjusting tank is lower than 1200mg/L, and the C:N ratio is 4; by manual analysis , Adjust the volume of alcohol-containing wastewater in the regulating tank; set up a special pipeline for alcohol-containing wastewater in the regulating tank, adjust the COD of the regulating tank, stabilize the ratio of ammonia nitrogen, COD, and C:N in the regulating tank, and keep the inflow of the SBR pool stable; The synergistic effect of the gas device, fan and online dissolved oxygen instrument can control the dissolved oxygen value in the SBR tank in real time.
  8. 如权利要求2所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,所述调节池内的碱度低于1000mg/L,通过调整液碱的投加量控制调节池的碱度在需求值。An enhanced SBR process tank for treating coal chemical industry high ammonia nitrogen wastewater as claimed in claim 2, wherein the alkalinity in the adjustment tank is lower than 1000mg/L, and the adjustment tank is controlled by adjusting the amount of liquid alkali added The alkalinity is at the demand value.
  9. 如权利要求2所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,所述SBR池内的曝气量是指通过SBR池内进气阀门开度和风机变频频率进而改变池内曝气量的大小,控制曝气方式采用连续曝气,曝气量为70m 3/min-80m 3/min。 The method for enhancing the treatment of coal chemical industry high ammonia nitrogen wastewater by the SBR process pool according to claim 2, characterized in that the aeration amount in the SBR pool refers to the change through the inlet valve opening in the SBR pool and the frequency conversion frequency of the fan The size of the aeration in the tank, the continuous aeration is used to control the aeration mode, the aeration is 70m 3 /min-80m 3 /min.
  10. 如权利要求2所述的一种强化SBR工艺池处理煤化工高氨氮废水的方法,其特征在于,所述SBR池内污泥浓度为3500-5500mg/L;优选的冬季污泥浓度为5000-5500mg/L,夏季污泥浓度为3500-4000mg/L;The method for enhancing the treatment of coal chemical industry high ammonia nitrogen wastewater by the SBR process tank according to claim 2, characterized in that the sludge concentration in the SBR tank is 3500-5500mg/L; the preferred winter sludge concentration is 5000-5500mg /L, the summer sludge concentration is 3500-4000mg/L;
    优选的,所述SBR池的水力停留时间为6-8h,水力停留时间根据进水负荷变化调整,进水负荷稳定,停留时间为6小时,进水增加波动,在线溶氧值未达到2mg/L,依据溶氧值延长停留时间,直至出水合格;Preferably, the hydraulic retention time of the SBR pool is 6-8h, the hydraulic retention time is adjusted according to the change of the inlet water load, the inlet water load is stable, the residence time is 6 hours, the inlet water increases and fluctuates, and the online dissolved oxygen value does not reach 2mg/ L, extend the residence time according to the dissolved oxygen value until the effluent is qualified;
    优选的,通过蓄水池回流出水调整调节池的氨氮浓度。Preferably, the ammonia nitrogen concentration of the adjustment tank is adjusted through the backflow water from the storage tank.
PCT/CN2019/000245 2018-12-25 2019-12-12 Method for treating high ammonia-nitrogen wastewater of the coal chemical industry with reinforced sbr process pool WO2020133553A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020217007768A KR20210036407A (en) 2018-12-25 2019-12-12 Reinforcement method to treat high ammonia nitrogen wastewater from coal chemical industry in SBR process pool

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201811585754.2A CN109574213B (en) 2018-12-25 2018-12-25 Method for treating high ammonia nitrogen wastewater in coal chemical industry by using enhanced SBR process tank
CN201811585754.2 2018-12-25

Publications (1)

Publication Number Publication Date
WO2020133553A1 true WO2020133553A1 (en) 2020-07-02

Family

ID=65931554

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2019/000245 WO2020133553A1 (en) 2018-12-25 2019-12-12 Method for treating high ammonia-nitrogen wastewater of the coal chemical industry with reinforced sbr process pool

Country Status (3)

Country Link
KR (1) KR20210036407A (en)
CN (1) CN109574213B (en)
WO (1) WO2020133553A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109574213B (en) * 2018-12-25 2021-12-28 兖矿国宏化工有限责任公司 Method for treating high ammonia nitrogen wastewater in coal chemical industry by using enhanced SBR process tank
CN111423059A (en) * 2020-04-07 2020-07-17 水艺控股集团股份有限公司 Improved SBR sewage treatment device and method
CN111533370B (en) * 2020-04-29 2021-08-10 华南理工大学 Optimal arrangement method for biochemical treatment structures of sequencing batch sewage treatment process

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103382051A (en) * 2013-07-06 2013-11-06 北京工业大学 Apparatus and method used for enhancing low-temperature bio-nitrification effects
CN104609659A (en) * 2015-01-14 2015-05-13 合肥工业大学 Method for enhancing denitrification efficiency of coal-chemical engineering wastewater treated with SBR technology
CN206940526U (en) * 2017-04-10 2018-01-30 安徽汇泽通环境技术有限公司 A kind of modified form SBR sewage disposal systems
CN107879468A (en) * 2017-10-30 2018-04-06 中铁第四勘察设计院集团有限公司 A kind of photovoltaic multistage SBR parallel connections waste water mixed processing technique
CN109574213A (en) * 2018-12-25 2019-04-05 兖矿国宏化工有限责任公司 A method of strengthening SBR process pool and handles coal chemical industry high ammonia-nitrogen wastewater
US10399876B2 (en) * 2017-06-09 2019-09-03 inCTRL Solutions Inc. Ammonia-based aeration control with SRT Control

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101503267B (en) * 2009-03-13 2010-12-01 哈尔滨工业大学 Coal chemical industry wastewater treating method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103382051A (en) * 2013-07-06 2013-11-06 北京工业大学 Apparatus and method used for enhancing low-temperature bio-nitrification effects
CN104609659A (en) * 2015-01-14 2015-05-13 合肥工业大学 Method for enhancing denitrification efficiency of coal-chemical engineering wastewater treated with SBR technology
CN206940526U (en) * 2017-04-10 2018-01-30 安徽汇泽通环境技术有限公司 A kind of modified form SBR sewage disposal systems
US10399876B2 (en) * 2017-06-09 2019-09-03 inCTRL Solutions Inc. Ammonia-based aeration control with SRT Control
CN107879468A (en) * 2017-10-30 2018-04-06 中铁第四勘察设计院集团有限公司 A kind of photovoltaic multistage SBR parallel connections waste water mixed processing technique
CN109574213A (en) * 2018-12-25 2019-04-05 兖矿国宏化工有限责任公司 A method of strengthening SBR process pool and handles coal chemical industry high ammonia-nitrogen wastewater

Also Published As

Publication number Publication date
CN109574213A (en) 2019-04-05
KR20210036407A (en) 2021-04-02
CN109574213B (en) 2021-12-28

Similar Documents

Publication Publication Date Title
WO2022121321A1 (en) Method for enhancing nitrogen and phosphorus removal by combining multi-stage ao short-range denitrification coupling anammox process with sludge hydrolytic acidification
CN110002594B (en) Device and method for realizing shortcut nitrification-anaerobic ammonia oxidation based on hydroxylamine side inhibition
CN102633359B (en) Method for treating total nitrogen of nitrogen-containing chemical wastewater
AU731280B2 (en) Process, using ammonia rich water for the selection and enrichment of nitrifying micro-organisms for nitrification of wastewater
CN100534928C (en) Short-path deep biological denitrogenation method for city garbage percolate
WO2020133553A1 (en) Method for treating high ammonia-nitrogen wastewater of the coal chemical industry with reinforced sbr process pool
US20210317025A1 (en) Device and method for sulphur cycle-based advanced denitrification of waste water coupling autotrophic denitrification and heterotrophic denitrification
CN108046518B (en) Enhanced nitrogen and phosphorus removal device and method for low-carbon source sewage
CN102603128A (en) Method for advanced treatment and recycling of landfill leachate
CN101781056B (en) Treatment method of waste papermaking water
CN110759604B (en) Two-stage SBR (sequencing batch reactor) series efficient biological denitrification method for low-carbon-source sewage
CN110642478A (en) Coupled treatment system and method for coking phenol-cyanogen wastewater by biochemical method and physicochemical method
CN104478177B (en) A kind of processing method of leather-making waste water
CN104609659B (en) A kind of method strengthening SBR PROCESS FOR TREATMENT coal chemical industrial waste water denitrification efficiency
CN111675426A (en) Polyurethane sewage treatment system and method applying composite microbial inoculum
CN107986443B (en) Whole-course autotrophic nitrogen removal method suitable for sewage with large COD/N fluctuation
CN111867983B (en) High solids dissolved air flotation system and method
CN201220931Y (en) Apparatus for realizing sludge shortcut nitrification by using FA and FNA control
CN114620830A (en) Municipal sewage treatment system and method
CN114133095A (en) Biological enhanced treatment device and process for high-salinity oily wastewater
CN111847641A (en) Short-cut nitrification anaerobic ammonia oxidation reaction device and method for realizing sequential batch/continuous flow
CN111620440A (en) Method and equipment for treating low-carbon-nitrogen-ratio domestic sewage by using improved CASS-MBR process
CN212334747U (en) Short-cut nitrification anaerobic ammonia oxidation reaction device for realizing sequence batch/continuous flow
CN217173393U (en) Integrated sewage treatment device
CN109607784B (en) Method for electromagnetic wave loading backflow sludge regulation and control system microbial community structure

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 19905691

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 20217007768

Country of ref document: KR

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 19905691

Country of ref document: EP

Kind code of ref document: A1