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CN108996672A - A kind of membrane pollution of membrane bioreactor and sludge yield control method - Google Patents

A kind of membrane pollution of membrane bioreactor and sludge yield control method Download PDF

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CN108996672A
CN108996672A CN201810807412.4A CN201810807412A CN108996672A CN 108996672 A CN108996672 A CN 108996672A CN 201810807412 A CN201810807412 A CN 201810807412A CN 108996672 A CN108996672 A CN 108996672A
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membrane
sludge
membrane bioreactor
control method
sludge yield
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余冉
陈舟凯
展漫军
张涛
崔婷婷
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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
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1268Membrane bioreactor systems
    • 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
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • 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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  • Biodiversity & Conservation Biology (AREA)
  • Hydrology & Water Resources (AREA)
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  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Activated Sludge Processes (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The present invention relates to a kind of membrane bioreactor (MBR) control membrane fouling and sludge yield control method, include the following steps: 1) to prepare multi-functional composite bacteria agent with the one or more of Bdellovibrio class bacterium, yellow myxococcus, saccharomycete, bacillus, actinomyces;2) by multi-functional composite bacteria agent directly or after situ activation according to water, water quality, system temperature, stream plus investment aerobic membrane bioreactor.By adding a kind of multi-functional composite bacteria agent with the characteristics such as microorganism predation and extracellular hydrolase secretion capacity be strong into MBR reactor, cleavable microorganism wall simultaneously destroys sludge structure, inhibit biofilm formation on membrane reactor, reduce the content of extracellular polymeric (EPS) and dissolved phenols (SMP) in mud mixed liquid, promote muddy water synchronous degradation, effectively slow down the fouling membrane and control system sludge yield of MBR, achieve the effect that sludge concentration in stable reactor, mitigate sewage and Treatment of Sludge pressure, and on water quality treatment without influence.

Description

一种膜生物反应器膜污染与污泥产率控制方法Membrane bioreactor membrane fouling and sludge yield control method

技术领域technical field

本发明涉及一种控制方法,特别涉及一种膜生物反应器膜污染与污泥产率控制方法,属于生物技术处理污泥的技术领域。The invention relates to a control method, in particular to a method for controlling membrane pollution and sludge yield of a membrane bioreactor, and belongs to the technical field of sludge treatment by biotechnology.

背景技术Background technique

近年来,膜生物反应器(MBR)作为一项富有创新性和前景的废水处理工艺,日益受到人们的关注。它将膜的物理分离和活性污泥的生物降解结合起来,以膜分离装置取代传统活性污泥反应器中的二沉池,从而实现高效的固液分离。与传统的废水生物处理工艺相比具有许多优点,包括:出水水质好,占地面积小等。然而,MBR 运行过程中产生的膜污染问题需耗费大量的费用,极大程度地制约了它的推广。In recent years, membrane bioreactor (MBR), as an innovative and promising wastewater treatment process, has attracted increasing attention. It combines the physical separation of membranes with the biodegradation of activated sludge, and replaces the secondary settling tank in traditional activated sludge reactors with membrane separation devices to achieve efficient solid-liquid separation. Compared with the traditional wastewater biological treatment process, it has many advantages, including: good effluent quality, small footprint, etc. However, the membrane fouling problem generated during the operation of MBR will cost a lot of money, which greatly restricts its promotion.

膜污染是指在膜过滤过程中水中的溶质大分子、微小颗粒和胶体粒子等物质在膜表面形成滤饼层,这些污染物的积累会增加过滤阻力,从而增加整个系统运行能耗。膜污染形成的原因复杂,有研究发现,溶解性难降解小分子有机物析出并与污泥混合液悬浮固体(MLSS)结合在膜表面会形成凝胶层,引起膜污染,造成膜堵塞,同时认为胞外聚合物(EPS)和溶解性微生物产物(SMP)的是引起膜污染最关键的物质。Membrane fouling refers to the solute macromolecules, tiny particles and colloidal particles in water forming a filter cake layer on the membrane surface during the membrane filtration process. The accumulation of these pollutants will increase the filtration resistance, thereby increasing the energy consumption of the entire system. The causes of membrane fouling are complex. Some studies have found that the precipitation of soluble and refractory small molecule organic matter and the combination of sludge mixed liquid suspended solids (MLSS) on the membrane surface will form a gel layer, causing membrane fouling and membrane clogging. At the same time, it is believed that Extracellular polymeric substances (EPS) and soluble microbial products (SMP) are the most critical substances that cause membrane fouling.

同时,目前我国污水生化处理过程中产生的剩余污泥量巨大,中国城镇污水处理厂每年产生的含水率为80 %的污泥超过了3000万吨,且污泥处理成本高昂,约占污水处理厂运行费用的 25-40 %,为污水处理厂运行带来了不小的负担,同时实际应用中污泥处置不当所造成的污染问题较为严重。因此,需要加快污泥处理处置方式的转变,只有从源头最大程度地控制与减少污泥产生量,才是满足生态环境保护与可持续发展要求的最佳方向。At the same time, at present, the amount of excess sludge produced in the biochemical treatment of sewage in my country is huge. The sludge with a water content of 80% produced by China's urban sewage treatment plants exceeds 30 million tons every year, and the cost of sludge treatment is high, accounting for about 10% of sewage treatment. 25-40% of the plant's operating cost, which brings a lot of burden to the operation of the sewage treatment plant. At the same time, the pollution problem caused by improper sludge disposal in practical applications is relatively serious. Therefore, it is necessary to accelerate the transformation of sludge treatment and disposal methods. Only by controlling and reducing the amount of sludge generated from the source to the greatest extent is the best direction to meet the requirements of ecological environment protection and sustainable development.

发明内容Contents of the invention

本发明正是针对现有技术中存在的技术问题,提供一种膜生物反应器膜污染与污泥产率控制方法,所要解决的技术问题为提供一种膜生物反应器膜污染缓解与污泥产率控制生物技术,综合运用微生物裂解、EPS和SMP降解、抑制生物膜形成结构等原理,实现泥水同步降解,减少凝胶层形成,缓解膜污染并控制系统污泥产率,达到稳定反应器内污泥浓度的效果,减少污水和污泥处理成本,无二次污染及卫生安全问题。The present invention aims at the technical problems existing in the prior art and provides a membrane bioreactor membrane fouling and sludge yield control method. The technical problem to be solved is to provide a membrane bioreactor membrane fouling mitigation and sludge yield control method. Yield control biotechnology, comprehensively using the principles of microbial lysis, EPS and SMP degradation, and inhibition of biofilm formation structure, etc., to achieve synchronous degradation of mud and water, reduce gel layer formation, alleviate membrane fouling and control system sludge yield, to achieve stable reactors The effect of internal sludge concentration reduces the cost of sewage and sludge treatment, and there is no secondary pollution and health and safety issues.

为了实现上述目的,本发明的技术方案如下:一种膜生物反应器膜污染与污泥产率控制方法,所述方法包括具体如下:1)以蛭弧菌类生物、黄色黏球菌、酵母菌、芽孢杆菌、放线菌的一种或几种制备多功能复合菌剂;In order to achieve the above object, the technical scheme of the present invention is as follows: a membrane bioreactor membrane fouling and sludge yield control method, the method comprises as follows: One or more of Bacillus, Bacillus, and Actinomycetes to prepare multifunctional composite bacterial agents;

2)将多功能复合菌剂直接或现场活化后流加投入膜生物反应器。2) Feed the multifunctional composite microbial agent into the membrane bioreactor after direct or on-site activation.

作为本发明的一种改进,所述步骤1)中多功能复合菌剂中微生物浓度范围在106—1013pfu/mL。As an improvement of the present invention, the concentration range of microorganisms in the multifunctional composite bacterial agent in the step 1) is 10 6 -10 13 pfu/mL.

作为本发明的一种改进,所述步骤2)中的多功能复合菌剂投加量为膜生物反应器内处理水量的0.05~0.5‰。As an improvement of the present invention, the dosage of the multifunctional composite bacterial agent in the step 2) is 0.05-0.5‰ of the treated water in the membrane bioreactor.

作为本发明的一种改进,所述步骤2)中的多功能复合菌剂投加频率为2-10d。As an improvement of the present invention, the dosing frequency of the multifunctional composite bacterial agent in the step 2) is 2-10d.

作为本发明的一种改进,所述步骤2)中的膜生物反应器为好氧-膜反应器,投加点设置在膜生物反应器的进水口附近。As an improvement of the present invention, the membrane bioreactor in step 2) is an aerobic-membrane reactor, and the dosing point is set near the water inlet of the membrane bioreactor.

作为本发明的一种改进,所述的膜生物反应器,初始污泥质量浓度需控制在5~22g/L ,优选为6~18 g/L,噬菌微生物可通过粘附捕食(Epibiotic predation)、侵入捕食(Endobiotic predation)、狼群捕食(Wolfpack group)等作用杀死并降解细菌,如蛭弧菌类生物(Bdellovibrio-and-like organisms)和黄色黏球菌Myxococcus xanthus等。如蛭弧菌是以捕食宿主菌为生的小型寄生性革兰氏阴性好氧细菌,在自然界中广泛存在,其可裂解大多数革兰氏阴性菌和少部分革兰氏阳性菌,但不会侵染真核细胞,对动物与人体无致病性,《饲料药物添加剂允许使用品种目录》中已将蛭弧菌列入饲料药物添加剂允许使用的微生物有益菌类中。黄色粘球菌可以捕食各类原核生物,包括蓝细菌、各类革兰氏阳性菌株和大肠杆菌、根瘤菌等各类革兰氏阴性菌。膜生物反应器内的高污泥浓度条件(5~22 g/L)和曝气高溶解氧环境(1-2mg/L)保证了该类细菌与宿主细菌的充分接触并适宜其生长。MBR反应器内的蛭弧菌与黄色黏球菌等通过捕食宿主细胞以达到增殖生长的同时,有效减缓反应器内污泥浓度随着污水处理时间的延长而不断增加的趋势,从而可控制系统污泥产率,大大减少后续剩余污泥的处理处置需求和费用,降低污水处理系统运行与处理成本。同时MBR投资和运行成本较高,MBR的膜组件造价高,并在反应器运行过程中容易出现膜污染,其主要原因是由于污水生物处理过程中一些溶解性难降解有机物——主要是来源于污泥细胞胞外多聚物(EPS)和和溶解性微生物产物(SMP)中的蛋白质、多糖和腐殖酸等,这些解性难降解有机物析出并与污泥混合液悬浮固体(MLSS)结合富集到膜表面形成凝胶层与生物膜,故需要定期清洗。而多功能复合菌剂中的蛭弧菌与黄色黏球菌等可通过分泌胞外蛋白酶、聚糖酶等水解污泥中的蛋白质、糖类、核酸和脂肪酸类物质,并协同其噬菌作用降低污泥产率、将反应器内污泥浓度稳定维持在最佳控制工况范围内的同时,降解膜表面凝胶层生成的前驱物与组成物质,有效防止微生物的附着与凝胶层的形成、避免膜污染产生,延长膜使用寿命,保证MBR运行的稳定性与长期性,降低其运行费用。As an improvement of the present invention, in the membrane bioreactor, the initial sludge mass concentration needs to be controlled at 5-22 g/L, preferably 6-18 g/L, and phage microorganisms can prey by adhesion (Epibiotic predation ), invasive predation ( Endobiotic predation), wolf pack predation (Wolfpack group), etc. kill and degrade bacteria, such as Bdellovibrio -and-like organisms and Myxococcus xanthus . For example, Bdellovibrio is a small parasitic Gram-negative aerobic bacterium that preys on host bacteria, and it exists widely in nature. It can lyse most Gram-negative bacteria and a small number of Gram-positive bacteria, but not It can infect eukaryotic cells and is non-pathogenic to animals and humans. Bdellovibrio has been included in the list of microorganisms and beneficial bacteria allowed to be used in feed drug additives in the "Catalogue of Allowed Species of Feed Drug Additives". Myxococcus xanthus can prey on various prokaryotes, including cyanobacteria, various Gram-positive strains, and various Gram-negative bacteria such as Escherichia coli and Rhizobium. The conditions of high sludge concentration (5-22 g/L) and aeration and high dissolved oxygen environment (1-2mg/L) in the membrane bioreactor ensure the full contact between this type of bacteria and the host bacteria and are suitable for their growth. The Bdellovibrio and Myxococcus xanthus in the MBR reactor can proliferate and grow by preying on the host cells, and at the same time effectively slow down the increasing trend of the sludge concentration in the reactor with the extension of the sewage treatment time, so that the system sewage can be controlled. Sludge yield, greatly reducing the need and cost of subsequent treatment and disposal of excess sludge, and reducing the operation and treatment costs of the sewage treatment system. At the same time, the investment and operation costs of MBR are high, the cost of MBR membrane modules is high, and membrane fouling is prone to occur during the operation of the reactor. Proteins, polysaccharides and humic acids in sludge cell extracellular polymers (EPS) and soluble microbial products (SMP), these degradable refractory organics are precipitated and combined with sludge mixed liquid suspended solids (MLSS) It is enriched to the surface of the membrane to form a gel layer and biofilm, so it needs to be cleaned regularly. Bdellovibrio and Myxococcus xanthus in the multifunctional composite bacterial agent can hydrolyze proteins, sugars, nucleic acids and fatty acids in sludge by secreting extracellular proteases, polycanases, etc., and cooperate with their phagocytosis to reduce Sludge yield, while maintaining the sludge concentration in the reactor stably within the range of optimal control conditions, degrade the precursors and components generated by the gel layer on the surface of the membrane, effectively preventing the adhesion of microorganisms and the formation of the gel layer , Avoid membrane fouling, prolong the service life of the membrane, ensure the stability and long-term operation of MBR, and reduce its operating costs.

本发明专利主要运用微生物裂解、EPS和SMP降解、污泥絮体结构破坏等原理相藕合,经济高效达到缓解膜污染并控制系统污泥产率的效果。通过投加噬菌微生物(蛭弧菌类生物和黄色黏球菌等)促进了污泥中部分微生物的裂解与泥水同步降解,抑制了污泥产率,可保证反应器内污泥浓度长期稳定在设计最佳浓度范围内,同时减缓膜上微生物的附着和抑制凝胶层形成,有效控制膜污染。同时本发明提出的多功能复合菌剂通过复配其他菌种,主要包括酵母菌、芽孢杆菌、放线菌,其可作为高效蛋白酶、聚糖酶产生菌可强化EPS和SMP水解,协同提高噬菌微生物生物捕食作用,加速污泥絮体裂解,强化EPS和SMP降解,能够大大提升减缓膜污染的效果,延长多功能复合菌剂作用时间。各组分之间相互协同作用,共同提高膜污染和污泥浓度控制效果。与现有技术相比,多功能复合菌剂具有经济普适、操作简单、作用持久等优势,显著减少污泥排放量和排放频次,减轻污泥处理处置压力,无二次污染及卫生安全问题,从源头减少污泥排放量并有效减缓膜污染,具有多重经济和环保效益。The patent of the invention mainly uses the principles of microbial cracking, EPS and SMP degradation, and sludge floc structure destruction to achieve the effects of alleviating membrane fouling and controlling the sludge yield of the system in an economical and efficient manner. By adding bacteriophage microorganisms (Bdellovibrio organisms and Myxococcus xanthus, etc.), the cracking of some microorganisms in the sludge and the simultaneous degradation of sludge and water are promoted, the sludge production rate is inhibited, and the sludge concentration in the reactor can be kept stable for a long time. Design the optimum concentration range, slow down the adhesion of microorganisms on the membrane and inhibit the formation of gel layer at the same time, effectively control membrane fouling. At the same time, the multifunctional composite bacterial agent proposed by the present invention can be used as high-efficiency protease and polycanase producing bacteria to strengthen the hydrolysis of EPS and SMP by compounding other strains, mainly including yeast, bacillus, and actinomycetes, and synergistically improve the The biological predation of bacteria and microorganisms can accelerate the cracking of sludge flocs and strengthen the degradation of EPS and SMP, which can greatly improve the effect of slowing down membrane fouling and prolong the action time of multifunctional composite bacteria agents. The components work synergistically to jointly improve the control effect of membrane fouling and sludge concentration. Compared with the existing technology, the multi-functional composite bacterial agent has the advantages of economy and universality, simple operation and long-lasting effect, which can significantly reduce sludge discharge and discharge frequency, reduce the pressure of sludge treatment and disposal, and have no secondary pollution and health and safety problems , reduce sludge discharge from the source and effectively slow down membrane fouling, which has multiple economic and environmental benefits.

相对于现有技术,本发明的优点如下:1)发明通过投加多功能复合菌剂强化了内源微生物的自身裂解,促进了泥水同步降解,有效控制系统污泥产率,以保证在较长时间内不外排污泥的情况下控制反应器内污泥浓度稳定在设计浓度范围内从而长期正常运行;2)该方案抑制生物膜形成,减少污泥混合液中EPS和 SMP的含量,有效减缓膜污染,延长膜使用寿命,降低MBR膜工艺运行费用;3)该方案无需投加酶制剂、化学解偶联剂、氧化剂等化学制剂,操作简单且无环境生态与卫生安全问题;4)该方案显著减少污泥排放量和排放频次,减轻污泥处理处置压力,降低污泥处理处置成本;5)该工艺出水水质稳定良好。Compared with the prior art, the advantages of the present invention are as follows: 1) The invention strengthens the self-lysis of endogenous microorganisms by adding multifunctional composite bacterial agents, promotes the synchronous degradation of mud and water, and effectively controls the sludge production rate of the system to ensure Control the sludge concentration in the reactor to be stable within the design concentration range for a long time without discharging the sludge, so as to operate normally for a long time; 2) This scheme inhibits the formation of biofilm and reduces the content of EPS and SMP in the sludge mixture, Effectively slow down membrane fouling, prolong the service life of the membrane, and reduce the operating cost of the MBR membrane process; 3) This scheme does not need to add chemical preparations such as enzyme preparations, chemical uncoupling agents, and oxidants, and is easy to operate and has no environmental, ecological, and health issues; 4 ) This scheme significantly reduces the amount and frequency of sludge discharge, reduces the pressure on sludge treatment and disposal, and reduces the cost of sludge treatment and disposal; 5) The effluent quality of the process is stable and good.

附图说明Description of drawings

图1为实施例1空白组和实验组膜污染状态示意图;Fig. 1 is the schematic diagram of embodiment 1 blank group and experimental group membrane fouling state;

图2为实施例1中系统日污泥排放量状态示意图。Fig. 2 is a schematic diagram of the state of the daily sludge discharge of the system in Example 1.

图3为实施例2运行60天内实验组和对照组污泥增长状态示意图;Fig. 3 is the schematic diagram of the sludge growth state of the experimental group and the control group within 60 days of the embodiment 2 operation;

图4为实施例2连续运行中2组实验的出水达标情况示意图;Fig. 4 is the schematic diagram of the effluent up-to-standard situation of 2 groups of experiments in the continuous operation of embodiment 2;

具体实施方式Detailed ways

为了加强对本发明的理解和认识,下面结合附图和具体实施方式对本发明做出进一步的说明和介绍。In order to enhance the understanding and recognition of the present invention, the present invention will be further described and introduced below in conjunction with the drawings and specific embodiments.

实施例1:一种膜生物反应器膜污染与污泥产率控制方法,所述方法包括具体如下:1)以蛭弧菌类生物、黄色黏球菌、斯托普蛭弧菌、斯塔尔蛭弧菌、酵母菌、芽孢杆菌、放线菌的一种或几种制备多功能复合菌剂;Embodiment 1: a kind of membrane bioreactor membrane fouling and sludge yield control method, described method comprises as follows specifically: 1) with Bdellovibrio class organism, xanthococcus, Stoop Bdellovibrio, Starr One or more of Bdellovibrio, yeast, bacillus, and actinomycetes to prepare multifunctional composite bacterial agents;

2)将多功能复合菌剂直接或现场活化后流加投入膜生物反应器。2) Feed the multifunctional composite microbial agent into the membrane bioreactor after direct or on-site activation.

所述步骤1)中多功能复合菌剂中微生物浓度范围在106—1013pfu/mL。The concentration range of microorganisms in the multifunctional composite bacterial agent in the step 1) is 10 6 -10 13 pfu/mL.

所述步骤2)中的多功能复合菌剂投加量为膜生物反应器内处理水量的0.05~0.5‰。The dosage of the multifunctional composite bacterial agent in the step 2) is 0.05-0.5‰ of the treated water in the membrane bioreactor.

所述步骤2)中的多功能复合菌剂投加频率为2-10d。The dosing frequency of the multifunctional composite bacterial agent in the step 2) is 2-10 days.

所述步骤2)中的膜生物反应器为好氧-膜反应器,投加点设置在膜生物反应器的入口处。The membrane bioreactor in step 2) is an aerobic-membrane reactor, and the dosing point is set at the entrance of the membrane bioreactor.

所述的膜生物反应器,初始污泥质量浓度需控制在5~22 g/L ,优选为6~18 g/L6~10 g/L 。In the membrane bioreactor, the initial sludge mass concentration needs to be controlled at 5-22 g/L, preferably 6-18 g/L6-10 g/L.

所述步骤2)中的多功能复合菌剂投加于膜生物反应器中,系统最终噬菌微生物数量达到103 pfu/mL以上。The multifunctional composite bacterial agent in the step 2) is added to the membrane bioreactor, and the final number of phage microorganisms in the system reaches more than 10 3 pfu/mL.

应用实施例1Application Example 1

通过在实验室模拟MBR工艺,验证本方法对缓解膜污染和污泥产率控制效果。By simulating the MBR process in the laboratory, the effect of this method on mitigating membrane fouling and controlling sludge yield was verified.

MBR工艺模拟装置主要由进水箱;蠕动泵,2个平行的膜生物反应器装置(包括膜组件);曝气系统(空气泵、空气流量计和曝气管)组成。The MBR process simulation device is mainly composed of water inlet tank; peristaltic pump, two parallel membrane bioreactor devices (including membrane modules); aeration system (air pump, air flow meter and aeration tube).

接种污泥取自江苏省某污水处理厂浓缩池。试验用水采用人工配水模拟生活污水,水质参数为COD 300~400 mg/L,NH4 +-N 30~40 mg/L,pH值为6.5~8.0。膜组件为聚偏氟乙烯(PVDF) 中空纤维膜板膜,膜平均孔径为 0.1μm。水力停留时间为10h,曝气强度为0.6m3/h。室温条件下运行。经过20~30 天培养后,反应器内的污泥浓度和性质基本稳定。试验中污泥的 MLSS 浓度均保持在 8g/L左右。The inoculum sludge was taken from the thickening tank of a sewage treatment plant in Jiangsu Province. The test water is artificially distributed to simulate domestic sewage. The water quality parameters are COD 300-400 mg/L, NH 4 + -N 30-40 mg/L, and pH 6.5-8.0. The membrane module is a polyvinylidene fluoride (PVDF) hollow fiber membrane with an average pore size of 0.1 μm. The hydraulic retention time is 10h, and the aeration intensity is 0.6m 3 /h. Run at room temperature. After 20-30 days of cultivation, the sludge concentration and properties in the reactor are basically stable. The MLSS concentration of the sludge in the test was kept around 8g/L.

运行稳定后,设置实验室与空白组。实验组每隔4个周期投加一次多功能复合菌剂,投加比为进水的0.1‰After the operation is stable, set up the laboratory and the blank group. The experimental group was dosed with a multifunctional compound bacterial agent every 4 cycles, and the dosing ratio was 0.1‰ of the influent

其配比如下:Its ratio is as follows:

蛭弧菌类生物,80%;Bdellovibrio organisms, 80%;

芽孢杆菌,10%;Bacillus, 10%;

放线菌,10%。Actinomycetes, 10%.

其中,蛭弧菌类生物活菌数为8×1010 pfu/mL。Among them, the number of live bacteria of Bdellovibrio was 8×10 10 pfu/mL.

膜污染情况可以用过膜压差(TMP)来表示。根据膜组件设计的要求,在恒流抽吸条件下,管道吸引压力需保持在5~50kPa的范围内才能延长膜的使用寿命,当TMP超过50kPa就需要对膜组件进行清洗。在恒流抽吸作用下运行MBR,随着膜污染的加剧,TMP会不断升高。Membrane fouling can be represented by transmembrane pressure (TMP). According to the design requirements of the membrane module, under the condition of constant flow suction, the suction pressure of the pipeline must be kept in the range of 5-50kPa to prolong the service life of the membrane. When the TMP exceeds 50kPa, the membrane module needs to be cleaned. When running the MBR under the action of constant pumping, the TMP will continue to rise as the membrane fouling increases.

膜反应器中反映的过膜压差(TMP)值能直观地表现膜污染现状,过膜压差值越高表示膜片的过滤性越差,膜通量越低。The transmembrane pressure difference (TMP) value reflected in the membrane reactor can intuitively express the status of membrane fouling. The higher the transmembrane pressure difference value, the worse the filterability of the membrane and the lower the membrane flux.

从图1中可以看出,空白对照组在12天后膜污染严重,TMP达到50kPa;而实验组在接种多功能复合菌剂后,在31天后发生膜污染,可见多功能复合菌剂使膜的可持续过滤性大大增强,膜使用周期延长了近2倍,。As can be seen from Figure 1, the membrane fouling of the blank control group was serious after 12 days, and the TMP reached 50kPa; and the membrane fouling occurred after 31 days after the experimental group was inoculated with the multifunctional composite bacterial agent. The sustainable filtration performance is greatly enhanced, and the membrane service life is extended by nearly 2 times.

污泥产率控制效果一般可通过日污泥排放量来反映污泥增长情况,用污泥产率变化来表征。系统运行过程中两组系统的日污泥排放情况如图4所示,污泥产率如表1所示。The control effect of sludge yield can generally reflect the growth of sludge through the daily sludge discharge, and it can be characterized by the change of sludge yield. The daily sludge discharge of the two groups of systems during the operation of the system is shown in Figure 4, and the sludge yield is shown in Table 1.

系统日污泥排放量如图2所示,在运行的30 d中,实验组系统始终保持着较低的日污泥排放量,并始终低于空白组。说明实验组可以维持较低的日污泥增长量,即可有效控制系统的污泥浓度。如表1所示,两组系统的污泥产率分别为0.311和0.162 kg MLSS/kg COD,证实通过投加多功能复合菌剂可以有效控制污泥产率。前面专利写作都没提污泥排放量,只说明维持污泥浓度,这里却作为一个指标,是不是前面要做相应调整,改为降低了污泥产率和剩余污泥排放量。The daily sludge discharge of the system is shown in Figure 2. During the 30 days of operation, the system of the experimental group has always maintained a low daily sludge discharge, which is always lower than that of the blank group. It shows that the experimental group can maintain a low daily sludge growth, which can effectively control the sludge concentration of the system. As shown in Table 1, the sludge yields of the two groups of systems were 0.311 and 0.162 kg MLSS/kg COD, respectively, confirming that the sludge yield can be effectively controlled by adding multifunctional composite bacterial agents. The previous patent writing did not mention the amount of sludge discharge, but only explained the maintenance of sludge concentration, but here it is used as an indicator, whether to make corresponding adjustments to reduce the sludge production rate and residual sludge discharge.

表1Table 1

应用实施例2:Application Example 2:

在某城镇污水处理厂好氧-膜生物反应器投加多功能复合菌剂进行试验。污水厂处理水量为1万m3/d,有2组平行的膜-生物反应器工艺,两组工艺中的污泥浓度初始浓度控制在7000-8000mg/L,其中一组作为对照,一组作为实验组,在实验组的膜生物反应器(好氧池)内投加蛭弧菌类生物、黄色黏球菌、芽孢杆菌、放线菌混合多功能复合菌剂。The experiment was carried out by adding multifunctional compound bacterial agent to the aerobic-membrane bioreactor of a certain urban sewage treatment plant. The water treatment capacity of the sewage plant is 10,000 m 3 /d. There are 2 groups of parallel membrane-bioreactor processes. As the experimental group, in the membrane bioreactor (aerobic pool) of the experimental group, a mixed multifunctional compound bacterial agent of Bdellovibrio, Myxococcus xanthus, Bacillus and Actinomycetes was added.

其中,多功能复合菌剂配比如下:Among them, the ratio of multifunctional compound bacterial agent is as follows:

蛭弧菌类生物,65%;Bdellovibrio-like organisms, 65%;

黄色黏球菌,15%;Myxococcus xanthus, 15%;

芽孢杆菌,12%;Bacillus, 12%;

放线菌,8%。Actinomycetes, 8%.

其中,蛭弧菌类生物和黄色粘球菌的活菌数为(6~9)×1011 pfu/mL。Among them, the number of viable bacteria of Bdellovibrio and Myxococcus xanthus was (6~9)×10 11 pfu/mL.

先将多功能复合菌剂加5倍自来水曝气活化4 h,用蠕动泵流加到膜生物反应器的进水口,流加量为处理水量的0.1‰,投加频率为3天一次。First add multi-functional compound bacterial agent to 5 times of tap water to aerate and activate for 4 h, then feed it to the water inlet of the membrane bioreactor with a peristaltic pump.

连续运行2个月,每隔5d检测实验组和对照组的出水水质、污泥浓度变化,期间不排泥。同时每隔10d测定膜污染情况,其中膜污染情况主要通过测序过膜压力(TMP)的增长趋势来表征。After continuous operation for 2 months, the effluent quality and sludge concentration of the experimental group and the control group were detected every 5 days, and no sludge was discharged during the period. At the same time, the membrane fouling was measured every 10 days, and the membrane fouling was mainly characterized by the growth trend of the sequencing transmembrane pressure (TMP).

由表2的结果可知,本发明中多功能复合菌剂的添加,能够大大减缓MBR膜污染,延长膜使用寿命。From the results in Table 2, it can be known that the addition of the multifunctional composite bacterial agent in the present invention can greatly slow down the fouling of the MBR membrane and prolong the service life of the membrane.

由图3可知,连续运行10d后,实验组污泥性状明显改善,污泥产生量开始减少,在运行后期基本保持在9000~1000mg/L,而对照组污泥浓度呈持续增长趋势,最终达到14000~15000mg/L,这说明投加多功能复合菌剂可显著降低生化处理系统中污泥的增长速率,减少污泥产量,即可以有效控制系统中污泥产率,降低剩余污泥的排放量,减轻污水处理厂剩余污泥处理处置压力。It can be seen from Figure 3 that after 10 days of continuous operation, the sludge properties of the experimental group were significantly improved, and the amount of sludge production began to decrease, and remained at 9000-1000 mg/L in the late stage of operation, while the sludge concentration of the control group showed a continuous increase trend, and finally reached 14000~15000mg/L, which shows that the addition of multifunctional compound bacterial agents can significantly reduce the growth rate of sludge in the biochemical treatment system and reduce the sludge production, which can effectively control the sludge production rate in the system and reduce the discharge of excess sludge reduce the pressure on the treatment and disposal of excess sludge in sewage treatment plants.

由图4可知,在连续运行过程中,2组实验的出水COD,NH4 +-N,TN,TP均能达到一级A标准。利用多功能复合菌剂进行膜污染和污泥产率控制过程中,系统对COD、总氮和总磷的去除效果不会受到影响,出水水质良好,可作为回用中水。It can be seen from Figure 4 that during continuous operation, the effluent COD, NH 4 + -N, TN, and TP of the two groups of experiments can all reach the first-class A standard. In the process of controlling membrane fouling and sludge yield by using multifunctional compound bacteria agent, the removal effect of the system on COD, total nitrogen and total phosphorus will not be affected, and the quality of the effluent is good, which can be used as reclaimed water.

表2Table 2

需要说明的是上述实施例,并没有用来限定本发明的保护范围,在上述基础上所作出的等同替换或者替代均属于本发明权利要求的保护范围。It should be noted that the above-mentioned embodiments are not used to limit the protection scope of the present invention, and equivalent replacements or substitutions made on the above-mentioned basis all belong to the protection scope of the claims of the present invention.

Claims (9)

1. a kind of membrane pollution of membrane bioreactor and sludge yield control method, which is characterized in that the method includes specifically such as Under: 1) with Bdellovibrio class biology, yellow myxococcus, saccharomycete, bacillus, actinomyces one or more prepare it is multi-functional multiple Combined bacteria agent;2) by multi-functional composite bacteria agent, directly or after situ activation stream adds investment membrane bioreactor.
2. membrane pollution of membrane bioreactor according to claim 1 is alleviated and sludge yield control method, it is characterised in that: In the step 1) in multi-functional composite bacteria agent microorganism concn range 106—1013pfu/mL。
3. membrane pollution of membrane bioreactor according to claim 1 is alleviated and sludge yield control method, it is characterised in that: Multi-functional composite bacteria agent dosage in the step 2 is 0.05 ~ 0.5 ‰ of processing water in membrane bioreactor.
4. membrane pollution of membrane bioreactor according to claim 1 is alleviated and sludge yield control method, it is characterised in that: It is 2-10d that multi-functional composite bacteria agent in the step 2, which adds frequency,.
5. membrane pollution of membrane bioreactor according to claim 1 is alleviated and sludge yield control method, it is characterised in that: Membrane bioreactor in the step 2 is aerobic-membrane reactor, and the water inlet that membrane bioreactor is arranged in toss area is attached Closely.
6. membrane pollution of membrane bioreactor according to claim 1 is alleviated and sludge yield control method, it is characterised in that: The membrane bioreactor, initial sludge quality concentration need to be controlled in 5 ~ 22 g/L.
7. membrane pollution of membrane bioreactor according to claim 1 is alleviated and sludge yield control method, it is characterised in that: In the step 1) in multi-functional composite bacteria agent the toatl proportion of Bdellovibrio class biology and yellow myxococcus 70% or more.
8. membrane pollution of membrane bioreactor according to claim 1 is alleviated and sludge yield control method, it is characterised in that: Multi-functional composite bacteria agent dosage in the step 2 is 0.15 ~ 0.35 ‰ of processing water in membrane bioreactor.
9. membrane pollution of membrane bioreactor according to claim 1 is alleviated and sludge yield control method, it is characterised in that: The membrane bioreactor, initial sludge quality concentration need to be controlled in 6 ~ 18 g/L.
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CN111410391A (en) * 2019-12-07 2020-07-14 余冉 Method for reducing abundance of multiple antibiotic resistance genes in excess sludge and limiting horizontal transfer thereof using microbial lysis reaction
CN111422979A (en) * 2020-01-13 2020-07-17 福建农林大学 A method for alleviating membrane fouling of anaerobic membrane bioreactor

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Application publication date: 20181214