CN114455697A - A method for controlling fouling of MBR membranes based on microbial quorum sensing quenching - Google Patents
A method for controlling fouling of MBR membranes based on microbial quorum sensing quenching Download PDFInfo
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- 239000012528 membrane Substances 0.000 title claims abstract description 38
- 230000018612 quorum sensing Effects 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title claims abstract description 16
- 230000000813 microbial effect Effects 0.000 title claims abstract description 15
- 238000010791 quenching Methods 0.000 title claims abstract description 14
- 230000000171 quenching effect Effects 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 24
- 241000894006 Bacteria Species 0.000 claims abstract description 19
- 239000010802 sludge Substances 0.000 claims abstract description 19
- 238000009285 membrane fouling Methods 0.000 claims abstract description 9
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 8
- 239000003656 tris buffered saline Substances 0.000 claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000009835 boiling Methods 0.000 claims abstract description 3
- 239000000243 solution Substances 0.000 claims description 33
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- 239000010865 sewage Substances 0.000 claims description 15
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical class OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 claims description 13
- 239000007983 Tris buffer Substances 0.000 claims description 11
- LOKCTEFSRHRXRJ-UHFFFAOYSA-I dipotassium trisodium dihydrogen phosphate hydrogen phosphate dichloride Chemical compound P(=O)(O)(O)[O-].[K+].P(=O)(O)([O-])[O-].[Na+].[Na+].[Cl-].[K+].[Cl-].[Na+] LOKCTEFSRHRXRJ-UHFFFAOYSA-I 0.000 claims description 10
- 239000002953 phosphate buffered saline Substances 0.000 claims description 10
- 238000004140 cleaning Methods 0.000 claims description 9
- 239000011780 sodium chloride Substances 0.000 claims description 8
- 150000003839 salts Chemical class 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 7
- 230000001580 bacterial effect Effects 0.000 claims description 6
- 239000012153 distilled water Substances 0.000 claims description 6
- 238000002474 experimental method Methods 0.000 claims description 6
- 230000002572 peristaltic effect Effects 0.000 claims description 6
- 239000011734 sodium Substances 0.000 claims description 6
- 239000011550 stock solution Substances 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 239000012510 hollow fiber Substances 0.000 claims description 5
- 238000001556 precipitation Methods 0.000 claims description 5
- 230000015556 catabolic process Effects 0.000 claims description 4
- 238000006731 degradation reaction Methods 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 4
- 230000001954 sterilising effect Effects 0.000 claims description 4
- 238000004659 sterilization and disinfection Methods 0.000 claims description 4
- 239000005708 Sodium hypochlorite Substances 0.000 claims description 3
- 238000011109 contamination Methods 0.000 claims description 3
- 238000013480 data collection Methods 0.000 claims description 3
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 claims description 3
- 230000003203 everyday effect Effects 0.000 claims description 3
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- 231100000719 pollutant Toxicity 0.000 claims description 3
- 238000005070 sampling Methods 0.000 claims description 3
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims description 3
- 239000006228 supernatant Substances 0.000 claims description 3
- 239000008399 tap water Substances 0.000 claims description 3
- 235000020679 tap water Nutrition 0.000 claims description 3
- 238000012546 transfer Methods 0.000 claims description 3
- 238000002835 absorbance Methods 0.000 claims description 2
- 239000000337 buffer salt Substances 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 239000013618 particulate matter Substances 0.000 claims description 2
- -1 polytetrafluoroethylene Polymers 0.000 claims description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 2
- 239000012266 salt solution Substances 0.000 claims description 2
- 238000011954 pollution control method Methods 0.000 claims 2
- 150000004676 glycans Chemical class 0.000 abstract description 3
- 229920001282 polysaccharide Polymers 0.000 abstract description 3
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- 238000012258 culturing Methods 0.000 abstract 1
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- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 2
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- 238000005202 decontamination Methods 0.000 description 1
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/006—Regulation methods for biological treatment
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
本发明公开了一种基于微生物群体感应猝灭的MBR膜污染控制方法,包括以下步骤:S1:使用MBR反应器进行反应,S2:将活性污泥以1%v/v接种至20mL以GCL为单以一碳源的M9培养基中,在30℃下150rpm摇床中培养5‑7天后,S3:将GCL富集菌或活性污泥用50mmol/L pH=7.0的TRIS缓冲盐溶液清洗,将100uL纯水加入等体积的400nmol/L的AHL中以作为空白对照,将活性污泥煮沸10min后,调节OD600=1.0,将混合液在30℃、120rpm的摇床中培养,定时取出一份混合液置于99℃水浴中10min以灭活细菌,此时即可完成对MBR膜的污染控制本发明所述的一种基于微生物群体感应猝灭的MBR膜污染控制方法,通过再经过反应后,使得其膜表面生物膜中粘附的细胞及分分泌的多糖类物质减少,证明随着污泥停留时间的增长,MBR中的生物污染更轻。The invention discloses a method for controlling MBR membrane fouling based on microbial quorum sensing quenching. In the M9 medium with only one carbon source, after culturing in a 150rpm shaker for 5-7 days at 30°C, S3: wash the GCL enriched bacteria or activated sludge with 50mmol/L pH=7.0 TRIS buffered saline solution, Add 100uL of pure water to an equal volume of 400nmol/L AHL as a blank control. After boiling the activated sludge for 10min, adjust OD600=1.0, incubate the mixture in a shaker at 30°C and 120rpm, and take out a portion regularly. The mixed solution is placed in a 99° C. water bath for 10 minutes to inactivate the bacteria, at which point the pollution control of the MBR membrane can be completed. , which reduced the adhered cells and secreted polysaccharides in the biofilm on the membrane surface, which proved that with the increase of sludge residence time, the biological pollution in MBR was lighter.
Description
技术领域technical field
本发明涉及MBR膜的污染控制领域,特别涉及一种基于微生物群体感应猝灭的MBR膜污染控制方法。The invention relates to the field of pollution control of MBR membranes, in particular to a method for controlling pollution of MBR membranes based on microbial quorum sensing quenching.
背景技术Background technique
膜生物反应器的工艺从成熟到推广应用已经历痕迹,但膜污染问题却一直难以解决,并阻碍着该技术的发展,在微生物研究领域,微生物群体感应的概念几乎与膜生物反应器工艺于同一时间被提出,并同时经历了快速的发展,微生物群体感应即细菌通过分泌信号分子,并检测其浓度来感知菌群密度,进而触发一系列群体行为,此前,群体感应的研究主要集中在微生物领域,近年来一些关于水处理工艺中群体感应的报道也相继出现,并有研究通过抑制MBR中的微生物群体感应取得了良好的膜污染控制效果,这为膜污染控制提供了一条新思路,但关于膜生物反应器中的群体感应及其猝灭的研究尚处于探索阶段,膜生物反应器的运行参数,如污泥停留时间,对反应器中群体感应的影响尚未被深入探讨,已报道的群体感应猝灭措施过于复杂且其稳定性也有待加强,此外基于群体感应猝灭的膜污染控制措施对MBR除污染效能的影响也尚未被仔细考察过。The process of membrane bioreactor has experienced traces from maturity to popularization, but the problem of membrane fouling has been difficult to solve and hinders the development of this technology. In the field of microbial research, the concept of microbial quorum sensing is almost the same as that of membrane bioreactor technology. It was proposed at the same time and experienced rapid development at the same time. Microbial quorum sensing means that bacteria sense the density of bacteria by secreting signal molecules and detecting their concentration, which in turn triggers a series of group behaviors. Previously, research on quorum sensing mainly focused on microorganisms. In recent years, some reports on quorum sensing in water treatment processes have appeared one after another, and some studies have achieved good membrane fouling control effects by inhibiting microbial quorum sensing in MBR, which provides a new idea for membrane fouling control. The research on quorum sensing and its quenching in membrane bioreactors is still in the exploratory stage. Quorum sensing quenching measures are too complicated and their stability needs to be strengthened. In addition, the effect of membrane fouling control measures based on quorum sensing quenching on the decontamination efficiency of MBR has not been carefully investigated.
发明内容SUMMARY OF THE INVENTION
本发明的主要目的在于提供一种基于微生物群体感应猝灭的MBR膜污染控制方法,可以有效解决背景技术中的问题。The main purpose of the present invention is to provide a method for controlling the fouling of MBR membranes based on microbial quorum sensing quenching, which can effectively solve the problems in the background art.
为实现上述目的,本发明采取的技术方案为:To achieve the above object, the technical scheme adopted in the present invention is:
一种基于微生物群体感应猝灭的MBR膜污染控制方法,包括以下操作步骤:A method for controlling fouling of MBR membranes based on microbial quorum sensing quenching, comprising the following operation steps:
S1:准备材料:中空纤维膜、生活污水、活性污泥、M9培养基、Tris缓冲盐溶液、磷酸缓冲盐溶液;S1: Preparation materials: hollow fiber membrane, domestic sewage, activated sludge, M9 medium, Tris buffered saline solution, phosphate buffered saline solution;
S2:使用MBR反应器进行反应:在进行使用时,需保证温度约为20-26℃,每天将经过1mm筛网过滤后的生活污水加入到高位水箱中,高位水箱中的原水进入各恒水位水箱中再分配到反应器中,再由蠕动泵抽吸出水,将压力变送器连接在膜组件与抽吸蠕动泵之间,精确测量、采集各MBR中的跨膜压差数据,由单片机收集、处理压力变送器信号并传送至电脑记录数据,数据采集频率为1分钟/次,MBR中膜组件完全污染后,跨膜压差>70kPa时,将其取出,先用自来水将膜表面的污染物冲洗下来,再用含有0.01molL的NaOH及200ppm的次氯酸钠的化学清洗液浸泡1-2h,经化学清洗后可重复使用;S2: Use MBR reactor for reaction: When using, it is necessary to ensure that the temperature is about 20-26 °C, and the domestic sewage filtered by 1mm screen is added to the high-level water tank every day, and the raw water in the high-level water tank enters each constant water level The water tank is redistributed to the reactor, and then the peristaltic pump sucks the water, and the pressure transmitter is connected between the membrane module and the suction peristaltic pump, and the transmembrane pressure difference data in each MBR is accurately measured and collected. Collect and process the pressure transmitter signal and transmit it to the computer to record the data. The data collection frequency is 1 minute/time. After the membrane module in the MBR is completely polluted, when the transmembrane pressure difference is >70kPa, take it out, and first use tap water to clean the membrane surface. The pollutants are washed down, and then soaked in a chemical cleaning solution containing 0.01molL of NaOH and 200ppm of sodium hypochlorite for 1-2h, and can be reused after chemical cleaning;
S3:将活性污泥以1%v/v接种至20mL以GCL为单以一碳源的M9培养基中,在30℃下150rpm摇床中培养5-7天后,待菌液变浑浊,将其转接至新的以GCL为单一碳源的M9培养基中,培养基为20mL,继续培养,经过三次转接培养之后,富集完成,将所得细菌保存于4℃冰箱中;S3: Inoculate activated sludge at 1% v/v into 20 mL of M9 medium with GCL as a single carbon source, and culture it in a shaker at 150 rpm at 30°C for 5-7 days. It was transferred to a new M9 medium with GCL as a single carbon source, the medium was 20 mL, and the cultivation was continued. After three transfer cultivations, the enrichment was completed, and the obtained bacteria were stored in a 4°C refrigerator;
S4:将GCL富集菌或活性污泥用50mmol/L pH=7.0的Tris缓冲盐溶液清洗,离心机清洗的机的规格为7000rpm,10min,4℃离心,弃去上清液,再加入TRIS缓冲盐清洗两次,再用TRIS缓冲盐将菌液的浓度调至600nm处吸光度为1.0,用TRIS缓冲盐将1g/L的AHL储备液稀释至400nmol/L,向1.5mL离心管中加入100uL以上菌液及等体积的400nmol/L的AHL溶液,重复配制几份以供后续降解实验中连续取样,将100uL纯水加入等体积的400nmol/L的AHL中以作为空白对照,将活性污泥煮沸10min后,调节OD600=1.0,将混合液在30℃、120rpm的摇床中培养,定时取出一份混合液置于99℃水浴中10min,以灭活细菌,用0.45um的滤膜将细菌滤去后将样品保存于4℃中,此时即可完成对MBR膜的污染控制。S4: Wash the GCL-enriched bacteria or activated sludge with 50mmol/L Tris buffered saline solution with pH=7.0. The specifications of the centrifuge cleaning machine are 7000rpm, 10min, centrifuge at 4°C, discard the supernatant, and then add TRIS Wash with buffer salt twice, then adjust the concentration of bacterial solution to absorbance at 600nm to 1.0 with TRIS buffer salt, dilute 1g/L AHL stock solution to 400nmol/L with TRIS buffer salt, and add 100uL to a 1.5mL centrifuge tube The above bacterial liquid and an equal volume of 400nmol/L AHL solution were prepared in several copies for continuous sampling in subsequent degradation experiments, and 100uL of pure water was added to an equal volume of 400nmol/L AHL as a blank control. After boiling for 10min, adjust OD600=1.0, incubate the mixture in a shaker at 30°C and 120rpm, and periodically take out a portion of the mixture and place it in a 99°C water bath for 10min to inactivate bacteria. Use a 0.45um filter to remove bacteria. After filtration, the samples were stored at 4°C, and the contamination control of the MBR membrane could be completed at this time.
优选的,所述实验中采用的中空纤维膜其材质为聚偏四氟乙烯,孔径为0.01um,膜丝外径为1.85mm,单根膜丝长度为60cm,所述生活污水取水后两天之内应用完,使用前,先用1mm的筛子将污水中的颗粒物过滤掉,再向水中加入255mg/L的NaHCO3,以调节碱度。Preferably, the hollow fiber membrane used in the experiment is made of polytetrafluoroethylene, the pore size is 0.01um, the outer diameter of the membrane filament is 1.85mm, and the length of a single membrane filament is 60cm. After the application is finished, before use, filter out the particulate matter in the sewage with a 1mm sieve, and then add 255mg/L NaHCO 3 to the water to adjust the alkalinity.
优选的,所述M9培养基配置时先配制5×M9盐,将92.39g的Na2HPO4-12H2O、15g的KH2PO4、2.5g的NaC1及5.0g的NH4Cl,溶解于800mL的蒸馏水中,充分溶解后定容至1000mL,用预先配制好的NaOH溶液将其pH调节至7.4,121℃20min灭菌后,于常温下保存,取约700mL的灭菌水,加入200mL配制好并灭菌的5×M9盐,加入2mL已灭菌的1molL的MgSO4溶液,加入2mLGCL,加入100uL已灭菌的1mol/LCaCl2,若加入CaCl2时溶液仍是热的会出现沉淀,这时剧烈摇晃直至沉淀溶解即可,用已灭菌的蒸馏水定容至1000mL,常温下保存,以待使用。Preferably, when the M9 medium is prepared, 5×M9 salt is prepared first, and 92.39g of Na 2 HPO 4 -12H 2 O, 15g of KH 2 PO 4 , 2.5g of NaCl and 5.0g of NH 4 Cl are dissolved Dissolve it in 800mL of distilled water, fully dissolve it to 1000mL, adjust its pH to 7.4 with a pre-prepared NaOH solution, sterilize it at 121°C for 20min, and store it at room temperature. Take about 700mL of sterilized water and add 200mL Prepared and sterilized 5×M9 salt, add 2mL of sterilized 1molL MgSO 4 solution, add 2mL GCL, add 100uL of sterilized 1mol/LCaCl 2 , if the solution is still hot when CaCl 2 is added, precipitation will occur , then shake vigorously until the precipitate dissolves, dilute to 1000mL with sterilized distilled water, and store at room temperature until use.
优选的,所述Tris缓冲盐溶液配置时将6.05g三羟甲基氨基甲烷及8.76gNaCl溶于800mL去离子水中,用1molL的HC1溶液将其pH调至7.0,定溶于1L,121℃20min灭菌后,常温下保存,以备使用。Preferably, when the Tris buffered salt solution is prepared, 6.05g of Tris and 8.76g of NaCl are dissolved in 800mL of deionized water, adjusted to pH 7.0 with 1molL of HCl solution, and dissolved in 1L at 121°C for 20min After sterilization, store at room temperature for use.
优选的,所述磷酸缓冲盐溶液配置时首先配置10x的磷酸缓冲盐溶液储备液,将80g的NaC1、2g的KCl、35.8g的Na2HPO4-12H2O、2.4g的KH2PO4溶于800mL水中,充分溶解后定容于1000mL,调节pH至7.4,常温下保存。Preferably, when the phosphate buffered saline solution is configured, 10x phosphate buffered saline solution stock solution is first prepared, and 80 g of NaCl, 2 g of KCl, 35.8 g of Na 2 HPO 4 -12H 2 O, 2.4 g of KH 2 PO 4 Dissolve in 800mL of water, fully dissolve and dilute to 1000mL, adjust pH to 7.4, and store at room temperature.
与现有技术相比,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
本发明中,通过加入的NaHCO3,能调节生活污水中的碱度,因为生活污水中氨氮浓度较高,避免在MBR中的消化作用会过度消耗碱度,使得反应器中的pH降低,再经过反应后,使得其膜表面生物膜中粘附的细胞及分分泌的多糖类物质减少,证明着随着污泥停留时间的增长,MBR中的生物污染更轻,再遇到污泥中群体感应菌分泌出的长链信号分子更容易被群体感应粗灭菌降解,则反应器中长链的浓度会更高,直至被完全降解,此方法下污泥对信号分子的降解性能更好且反应器中信号分子的浓度也相应更低。In the present invention, by adding NaHCO 3 , the alkalinity in the domestic sewage can be adjusted, because the ammonia nitrogen concentration in the domestic sewage is relatively high, it is avoided that the digestion in the MBR will consume the alkalinity excessively, so that the pH in the reactor is reduced, and then the After the reaction, the cells adhering to the biofilm on the membrane surface and the secreted polysaccharides are reduced, which proves that with the increase of the sludge residence time, the biological pollution in the MBR is lighter, and then encounters the sludge in the sludge. The long-chain signal molecules secreted by quorum-sensing bacteria are more likely to be degraded by quorum-sensing rough sterilization, and the concentration of long-chain chains in the reactor will be higher until they are completely degraded. Under this method, sludge has better degradation performance of signal molecules And the concentration of signal molecules in the reactor is correspondingly lower.
具体实施方式Detailed ways
下面将结合本发明的实施例,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
本发明涉及一种基于微生物群体感应猝灭的MBR膜污染控制方法,包括以下步骤:The present invention relates to a kind of MBR membrane fouling control method based on microbial quorum sensing quenching, comprising the following steps:
S1:准备材料:中央纤维膜、生活污水、活性污泥、M9培养基、Tris缓冲盐溶液、磷酸缓冲盐溶液,实验中采用的中空纤维膜其材质为聚偏四氟乙烯,孔径为0.01um,膜丝外径为1.85mm,单根膜丝长度为60cm,生活污水取水后两天之内应用完,使用前,先用1mm的筛子将污水中的颗粒物过滤掉,再向水中加入255mg/L的NaHCO3,以调节碱度,M9培养基配置时先配制5×M9盐,将92.39g的Na2HPO4-12H2O、15g的KH2PO4、2.5g的NaC1及5.0g的NH4Cl,溶解于800mL的蒸馏水中,充分溶解后定容至1000mL,用预先配制好的NaOH溶液将其pH调节至7.4,121℃20min灭菌后,于常温下保存,取约700mL的灭菌水,加入200mL配制好并灭菌的5xM9盐,加入2mL已灭菌的1molL的MgSO4溶液,加入2mLGCL,加入100uL已灭菌的1mol/LCaCl2,若加入CaCl2时溶液仍是热的会出现沉淀,这时剧烈摇晃直至沉淀溶解即可,用已灭菌的蒸馏水定容至1000mL,常温下保存,以待使用,TRIS缓冲盐溶液配置时将6.05g三羟甲基氨基甲烷及8.76gNaCl溶于800mL去离子水中,用1molL的HC1溶液将其pH调至7.0,定溶于1L,121℃20min灭菌后,常温下保存,以备使用,磷酸缓冲盐溶液配置时首先配置10x的磷酸缓冲盐溶液储备液,将80g的NaC1、2g的KCI、35.8g的Na2HPO4-12H2O、2.4g的KH2PO4溶于800mL水中,充分溶解后定容于1000mL,调节pH至7.4,常温下保存。S1: Preparation materials: central fiber membrane, domestic sewage, activated sludge, M9 medium, Tris buffered saline solution, phosphate buffered saline solution, the hollow fiber membrane used in the experiment is made of polyvinylidene fluoride with a pore size of 0.01um , the outer diameter of the membrane wire is 1.85mm, and the length of a single membrane wire is 60cm. It should be used within two days after the domestic sewage is taken. Before use, use a 1mm sieve to filter out the particles in the sewage, and then add 255mg/ L of NaHCO 3 to adjust the alkalinity, first prepare 5×M9 salt when M9 medium is prepared, mix 92.39g of Na 2 HPO 4 -12H 2 O, 15g of KH 2 PO 4 , 2.5g of NaCl and 5.0g of NH 4 Cl, dissolved in 800 mL of distilled water, fully dissolved and then adjusted to 1000 mL, adjusted to pH 7.4 with a pre-prepared NaOH solution, sterilized at 121 °C for 20 min, and stored at room temperature, take about 700 mL of sterilized Bacteria water, add 200mL prepared and sterilized 5xM9 salt, add 2mL sterilized 1molL MgSO 4 solution, add 2mL GCL, add 100uL sterilized 1mol/LCaCl 2 , if CaCl 2 is added, the solution is still hot Precipitation will appear, then shake vigorously until the precipitation dissolves, dilute to 1000mL with sterilized distilled water, and store it at room temperature until use. When preparing the TRIS buffered saline solution, mix 6.05g of tris-hydroxymethylaminomethane and 8.76g of tris. Dissolve gNaCl in 800 mL of deionized water, adjust its pH to 7.0 with 1 molL of HCl solution, dissolve in 1 L, sterilize at 121 °C for 20 min, and store it at room temperature for use. When configuring phosphate buffered saline solution, first configure 10x Phosphate buffered saline solution stock solution, dissolve 80g of NaCl, 2g of KCI, 35.8g of Na 2 HPO 4 -12H 2 O, and 2.4g of KH 2 PO 4 in 800 mL of water, fully dissolve and set the volume to 1000 mL, and adjust the pH To 7.4, store at room temperature.
S2:使用MBR反应器进行反应:在进行使用时,需保证温度约为20-26度,每天将经过1mm筛网过滤后的生活污水加入到高位水箱中,高位水箱中的原水进入各恒水位水箱中再分配到反应器中,再由蠕动泵抽吸出水,将压力变送器连接在膜组件与抽吸蠕动泵之间,精确测量、采集各MBR中的跨膜压差数据,由单片机收集、处理压力变送器信号并传送至电脑记录数据,数据采集频率为1分钟/次,MBR中膜组件完全污染后,跨膜压差>70kPa时,将其取出,先用自来水将膜表面的污染物冲洗下来,再用含有0.01molL的NaOH及200ppm的次氯酸钠的化学清洗液浸泡1-2h,经化学清洗后可重复使用。S2: Use MBR reactor for reaction: When using, it is necessary to ensure that the temperature is about 20-26 degrees, and the domestic sewage filtered by 1mm screen is added to the high-level water tank every day, and the raw water in the high-level water tank enters each constant water level The water tank is redistributed to the reactor, and then the peristaltic pump sucks the water, and the pressure transmitter is connected between the membrane module and the suction peristaltic pump, and the transmembrane pressure difference data in each MBR is accurately measured and collected. Collect and process the pressure transmitter signal and transmit it to the computer to record the data. The data collection frequency is 1 minute/time. After the membrane module in the MBR is completely polluted, when the transmembrane pressure difference is >70kPa, take it out, and first use tap water to clean the membrane surface. The pollutants are washed down, and then soaked in a chemical cleaning solution containing 0.01molL of NaOH and 200ppm of sodium hypochlorite for 1-2h, and can be reused after chemical cleaning.
S3:将活性污泥以1%v/v接种至20mL以GCL为单以一碳源的M9培养基中,在30℃下150rpm摇床中培养5-7天后,待菌液变浑浊,将其转接至新的以GCL为单一碳源的M9培养基中,培养基为20mL,继续培养,经过三次转接培养之后,富集完成,将所得细菌保存于4℃冰箱中。S3: Inoculate activated sludge at 1% v/v into 20 mL of M9 medium with GCL as a single carbon source, and culture it in a shaker at 150 rpm at 30°C for 5-7 days. It was transferred to a new M9 medium with GCL as a single carbon source, the medium was 20 mL, and the cultivation was continued. After three transfer cultivations, the enrichment was completed, and the obtained bacteria were stored in a 4°C refrigerator.
S4:将GCL富集菌或活性污泥用50mmol/LpH=7.0的TRIS缓冲盐溶液清洗,离心机清洗的机的规格为7000rpm,10min,4℃离心,弃去上清液,再加入Tris缓冲盐清洗两次,再用Tris缓冲盐将菌液的浓度调至600nm处吸光度为1.0,用TRIS缓冲盐将1g/L的AHL储备液稀释至400nmolL,向1.5mL离心管中加入100uL以上菌液及等体积的400nmol/L的AHL溶液,重复配制几份以供后续降解实验中连续取样,将100uL纯水加入等体积的400nmol/L的AHL中以作为空白对照,将活性污泥煮沸10min后,调节OD600=1.0,将混合液在30℃、120rpm的摇床中培养,定时取出一份混合液置于99℃水浴中10min,以灭活细菌,用0.45um的滤膜将细菌滤去后将样品保存于4℃中,此时即可完成对MBR膜的污染控制。S4: Wash the GCL enriched bacteria or activated sludge with 50mmol/L pH=7.0 TRIS buffered saline solution, the specifications of the centrifuge cleaning machine are 7000rpm, 10min, centrifuge at 4°C, discard the supernatant, and then add Tris buffer Wash twice with salt, then adjust the concentration of the bacterial solution to 1.0 at 600nm with Tris buffer, dilute 1g/L AHL stock solution to 400nmolL with TRIS buffer, and add more than 100uL of bacterial solution to a 1.5mL centrifuge tube and an equal volume of 400nmol/L AHL solution, repeat the preparation of several copies for continuous sampling in subsequent degradation experiments, add 100uL of pure water to an equal volume of 400nmol/L AHL as a blank control, and boil the activated sludge for 10min. , adjust OD600=1.0, cultivate the mixture in a shaker at 30°C and 120rpm, take out a portion of the mixture regularly and place it in a 99°C water bath for 10 minutes to inactivate bacteria, and filter out the bacteria with a 0.45um filter. The samples were stored at 4°C, at which point the contamination control of the MBR membrane was completed.
本发明通过加入的NaHCO3,能调节生活污水中的碱度,因为生活污水中氨氮浓度较高,避免在MBR中的消化作用会过度消耗碱度,使得反应器中的pH降低,再经过反应后,使得其膜表面生物膜中粘附的细胞及分分泌的多糖类物质减少,证明着随着污泥停留时间的增长,MBR中的生物污染更轻,再遇到污泥中群体感应菌分泌出的长链信号分子更容易被群体感应粗灭菌降解,则反应器中长链的浓度会更高,直至被完全降解,此方法下污泥对信号分子的降解性能更好且反应器中信号分子的浓度也相应更低。The present invention can adjust the alkalinity in the domestic sewage by adding NaHCO 3 , because the ammonia nitrogen concentration in the domestic sewage is relatively high, it is avoided that the digestion in the MBR will consume the alkalinity excessively, so that the pH in the reactor is lowered, and then the reaction is carried out. After that, the cells adhered to the biofilm on the membrane surface and the secreted polysaccharide substances were reduced, which proved that with the increase of the sludge residence time, the biological pollution in the MBR was lighter, and then encountered the quorum sensing in the sludge. The long-chain signal molecules secreted by bacteria are more likely to be degraded by quorum sensing rough sterilization, and the concentration of long chains in the reactor will be higher until they are completely degraded. The concentration of signal molecules in the device is correspondingly lower.
尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, and substitutions can be made in these embodiments without departing from the principle and spirit of the invention and modifications, the scope of the invention is defined by the appended claims and their equivalents.
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