WO2011079827A1 - Extreme halophilic bacteria, composite halophilic bacterium microbial agent and uses thereof - Google Patents

Extreme halophilic bacteria, composite halophilic bacterium microbial agent and uses thereof Download PDF

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WO2011079827A1
WO2011079827A1 PCT/CN2011/000145 CN2011000145W WO2011079827A1 WO 2011079827 A1 WO2011079827 A1 WO 2011079827A1 CN 2011000145 W CN2011000145 W CN 2011000145W WO 2011079827 A1 WO2011079827 A1 WO 2011079827A1
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halophilic
extreme
composite
cgmcc
salt
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PCT/CN2011/000145
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李捍东
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中国环境科学研究院
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    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
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    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • C12N1/205Bacterial isolates
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    • C12P39/00Processes involving microorganisms of different genera in the same process, simultaneously
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    • 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
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    • C12R2001/00Microorganisms ; Processes using microorganisms
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    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • C12R2001/07Bacillus
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    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • C12R2001/38Pseudomonas

Definitions

  • the present invention relates to the field of microorganisms, and in particular to extreme halophilic bacteria, complex halophilic bacteria agents and applications.
  • high-salt wastewater such as printing and dyeing, papermaking, chemicals, pesticides, oil production, seafood processing, etc.
  • wastewater will usually contain high concentrations of organic pollutants, direct discharge will The environment causes serious pollution.
  • high-salt organic wastewater is not suitable for conventional biological treatment due to the toxic effects of salt on common microorganisms.
  • Extreme halophilic bacteria to select and isolate extreme halophilic bacteria for selection and combination culture; and to use extreme halophilic bacteria for the start-up and debugging of high-salt organic wastewater biological treatment system.
  • a further object of the present invention is to provide a composite halophilic fungus comprising the above extreme halophile.
  • Another object of the present invention is to provide a method of treating high salt production wastewater.
  • Another object of the invention is to provide the use of the above extreme halophiles.
  • the extreme halophilic bacteria according to the present invention may be Salmonella iHalomonas sp), and its storage number is CGMCC No. 3081.
  • the extreme halophilic bacteria according to the present invention may be Pseudomonas sp., and its storage number is: CGMCC No. 3082.
  • the extreme halophilic bacteria according to the present invention may be Bacillus sp. 1 ⁇ 23ci77 ⁇ sp), and its storage number is CGMCC No. 3083.
  • the composite halophilic bacteria agent according to the present invention includes any two or three of the above extreme halophilic bacteria CGMCC No. 3081, CGMCC No. 3082, and CGMCC No. 3083.
  • the composite halophilic bacteria agent according to the present invention comprises the above three extreme halophilic bacteria, wherein the halophilic bacteria CGMCC No. 3081: CGMCC No. 3082: CGMCC No. 3083 is 3:3:1.
  • the method for preparing the above composite halophilic bacteria agent according to the present invention comprises the following steps:
  • CGMCC No. 3081, CGMCC No. 3082, CGMCC No. 3083 are cultured in a composite microbial culture medium at 25_35 ° C for 7 days - 10 days;
  • the above cultured compound extreme halophilic agent is expanded and cultured in an expansion medium to obtain a compound halophilic bacteria agent, wherein, in the steps 1) and 2), the medium formula used is: Yeast extract 10 g / L, protein halophilic 15g / L, MgS0 4 ⁇ 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7. 0.
  • the present invention also provides a method of treating high-salt production wastewater, the method comprising the step of adding the above-mentioned composite halophilic bacteria to a production wastewater treatment system, characterized in that the COD concentration of the production wastewater is 3000 rag/ L -3500 mg / L, cultured step by step according to the system's 1/10-1/20 volume ratio, and finally the treatment system is completely completed.
  • the invention also provides the use of the above extreme halophilic salt in the treatment of high salt production wastewater.
  • the process for treating the cyanuric chloride production wastewater using the combination of the three extreme halophilic bacteria of the present invention is mainly divided into two stages:
  • the extreme halophilic composite fungicide is expanded and cultured according to the needs of the site; then the extreme halophilic composite fungicide is added to the wastewater treatment system for treating cyanuric chloride, and the extreme halophilic composite fungicide is periodically added.
  • the three extreme halophilic composite microbial agents were able to grow well in the treatment system and form a biofilm, completing the start-up phase.
  • the acclimation phase is entered, namely: gradually reducing the dosage of the extreme halophilic composite microbial agents, and gradually increasing the amount of cyanuric cyanide production wastewater until the dosage of the extreme halophilic composite fungicide is 0, the amount of cyanuric acid production wastewater increased to 100%;
  • T0C total organic carbon
  • T0C total organic carbon
  • T0C total organic carbon
  • the composite extreme halophilic bacteria agent combined with the three extreme halophilic bacteria of the present invention can effectively treat the high-salt cyanuric chloride production wastewater, and the principle is as follows:
  • the three extreme halophilic bacteria can be high High salt and organic matter in the wastewater of cyanuric chloride production as a nutrient. The more nutrients, the better the growth of extreme halophilic bacteria.
  • the successful application of the aerobic pre-suspended biofilm solves the problem that the anaerobic reaction starts slowly and is difficult to be synchronized with the aerobic reaction, and the rapid start of the anaerobic reaction is realized;
  • the muddy water is difficult to separate, and maintains the microbial concentration in the device, increasing the volumetric load.
  • the invention obtains three strains of extreme halophilic bacteria with salinity resistance of 15-25%, and the compound extreme halophilic bacteria agent after combination of three extreme halophilic bacteria can effectively treat high-salt cyanuric chloride production wastewater.
  • the method of the present invention is more in line with the national policy of "circular economy” and “energy saving and emission reduction", which can save a large amount of operating costs for enterprises and realize resource recycling treatment.
  • Fig. 1 is a flow chart showing the process of treating the high-salt cyanuric chloride production wastewater by the three extreme halophilic bacteria combinations of the present invention.
  • Figure 2 is a fatty acid profile of Halomonas CGMCC No. 3081.
  • Figure 3 is a fatty acid profile of Bacillus sp. G3 ⁇ 4ci7 i/s) CGMCC No. 3083.
  • Figure 4 shows the fatty acid profile of Pseudomonas (Malomonas CGMCC No. 3082. Extremely halophilic bacteria:
  • the collected sludge is in a liquid enrichment medium containing 16wt%-26wtl of salt) Enrichment culture in medium 25-35 3 for 3-10 days;
  • the components of the liquid enriched medium and the contents of the components are as follows: peptone 15 g / L, MgS0 4 ⁇ 7H 2 0 20 g / L, KCL 2 g / L, NaCL 150 - 250 g / L, pH 7. 0 ;
  • the components of the separation medium and the content of each component are the same as the components of the purified separation culture medium and the components, and are: casein hydrolysate 5 g/L, yeast extract 10 g/L, peptone 15g / L, MgS0 4 ⁇ 7H 2 0 20 g / L, KCL 2 g / L,, NaCL 150-250 g / L, pH 7. 0;
  • MIDI Sherlock Mi s identification system software can control Agi lent's 6850, 6890 and 7890 GCs, through the short chain obtained by gas chromatography A map of the type and content of fatty acids is compared to quickly and accurately identify microbial species.
  • Figure 2 is a fatty acid profile of Halomos sinensis CGMCC No. 3081, which has a salt tolerance of 15%-25%.
  • the method of identification is the same as the method for identifying nas nas iHal nas; Figure 3 For the fatty acid profile of Bacillusus Us77/s) CGMCC No. 3083, the Bacillus sp. has a salt tolerance of 15% to 25%.
  • the identification method is the same as the method for identifying M. monosyllium IMomonas;
  • Figure 4 shows the fatty acid profile of Pseudomonas alomo s CGMCC No. 3082, the salt tolerance of the Pseudomonas ⁇ Halomonas) is 15% - 25% .
  • the effect of removing the total organic carbon (T0C) is 80. 01%;
  • the total halophilic bacteria CGMCC No. 3082 had a total organic carbon (T0C) removal effect of 69.71%;
  • the extreme halophilic bacteria CGMCC No. 30823 had a total organic carbon (T0C) removal effect of 74.66%; 86%;
  • composition of the composite agent medium and the content of each component are: yeast extract 10 g / L, protein halophilic 15 g / L, MgS0 4 ⁇ 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g/L , P H 7. 0.
  • the above compound extreme halophilic agent is expanded and cultured in a compound halophilic agent expansion medium at 25-30 ° C for 7-10 days to obtain a compound halophilic agent;
  • composition of the composite agent and the content of each component are: yeast extract 10 g / L, peptone 15 g / L, MgS0 4 - 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g /L, pH 7. 0.
  • Example 3 Using the three extreme halophilic bacteria combinations of the present invention to treat the simulated production of cyanuric chloride production wastewater of "Degusai Sanzheng (Yingkou) Fine Chemical Co., Ltd.”
  • the above three extreme halophilic bacteria of the present invention are cultured in a composite bacterial culture medium at 25 ° C for 10 days to obtain a composite halophilic agent;
  • composition of the composite microbial culture medium is: yeast extract 10 g/L, protein halophilic 15 g/L, MgS0 4 ⁇ 7H 2 0 20 g/L, KCL 2 g/L, NaCL 180 g/L, pH 7. 0 ;
  • the above-mentioned compound extreme halophilic agent is expanded and cultured in a composite microbial expansion medium at 25 ° C for 10 days to obtain a compound halophilic agent after expanding the culture;
  • the composite agent expansion medium components are: yeast extract 10 g / L, peptone 15 g / L, MgS0 4 ⁇ 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7 . 0;
  • the three extreme halophilic bacteria combinations of the present invention are used for treating high-salt cyanuric chloride production wastewater containing "salt of 18 wt% to 20 wt%" of "Hebei Lingang Chemical Co., Ltd.”; the process is basically the same as that of the embodiment 1.
  • the above three extreme halophilic bacteria of the present invention are cultured for 3 days in 3CTC in a composite bacterial culture medium to obtain a composite halophilic agent;
  • composition of the composite microbial culture medium is: yeast extract 10 g/L, protein halophilic 15 g/L, MgS0 4 ⁇ 7H 2 0 20 g/L, KCL 2 g/L, NaCL 180 g/L, pH 7. 0 ;
  • the above-mentioned compound extreme halophilic agent is expanded and cultured in a composite microbial expansion medium for 3 days, and a compound halophilic agent is obtained after expanding the culture;
  • the composite agent expansion medium components are: yeast extract 10 g / L, peptone 15 g / L, MgS0 4 ⁇ 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7 . 0; 2. Add the above compound bacteria to the treatment system of high-salt cyanuric chloride production wastewater, and add the extreme halophilic agent according to the volume of the biological treatment system of 1Z10-1/20.
  • T0C content can reach below 10mg/L
  • ammonia nitrogen content is below 4mg/L
  • cyanide content reaches below 0. 054mg/L
  • basic high-salt cyanuric chloride production wastewater reaches enterprise back With requirements.
  • the above three extreme halophilic bacteria of the present invention are cultured in a composite bacterial culture medium at 35 ° C for 7 days to obtain a composite halophilic agent;
  • composition of the composite bacteria medium is: yeast extract 10 g / L, protein halophilic 15 g / L, MgS0 4 ⁇ 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7. 0 ;
  • the above-mentioned compound extreme halophilic agent is cultured in a combined microbial expansion medium for 35 days, and expanded for 7 days to obtain a composite halophilic agent after expanding the culture;
  • the composite agent expansion medium components are: yeast extract 10 g / L, peptone 15 g / L, MgS0 4 - 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7 . 0;

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Abstract

Three extreme halophilic bacteria strains and composite halophilic bacterium microbial agent containing the three extreme halophilic bacteria strains and uses thereof are provided. The extreme halophilic bacteria strains obtained in the present invention are halomonas sp. CGMCC No.3081, pseudomonas sp. CGMCC No.3082 and bacillus sp. CGMCC No.3083.The composite halophilic bacterium microbial agent containing the extreme halophilic bacteria strains above are also provided. Three extreme halophilic bacteria strains which have tolerance of salinity of 15-25% are isolated. The composite halophilic bacterium microbial agent obtained by combining the three extreme halophilic bacteria strains can treat the wastewater produced in the production process of high-salt cyanuric chloride effectively.

Description

极端嗜盐菌、 及复合嗜盐菌菌剂和应用  Extreme halophilic bacteria, and complex halophilic bacteria agents and applications
技术领域 Technical field
本发明涉及微生物领域, 具体地涉及极端嗜盐菌、复合嗜盐菌菌 剂和应用。  The present invention relates to the field of microorganisms, and in particular to extreme halophilic bacteria, complex halophilic bacteria agents and applications.
背景技术 Background technique
随着我国工业化进程的加快, 诸多生产领域会产生高含盐废水, 如印染、 造纸、 化工、 农药、 采油、 海产品加工等, 此类废水通常会 含有高浓度有机污染物, 直接排放会对环境造成严重污染。而且, 高 含盐有机废水因盐分对普通微生物的毒害作用而不适于常规生物处 理。 这主要是因为: (一) 盐浓度过高时, 水体的渗透压高, 易使微 生物细胞脱水,引起细胞原生质分离;(二)在含盐浓度高的情况下, 盐析作用会使脱氢酶活性降低; 〔三) 高氯离子浓度对细菌有毒害作 用; (四) 由于水的密度增加, 活性污泥容易上浮流失, 难于达到泥 水分离。  With the acceleration of China's industrialization process, many production areas will produce high-salt wastewater, such as printing and dyeing, papermaking, chemicals, pesticides, oil production, seafood processing, etc., such wastewater will usually contain high concentrations of organic pollutants, direct discharge will The environment causes serious pollution. Moreover, high-salt organic wastewater is not suitable for conventional biological treatment due to the toxic effects of salt on common microorganisms. This is mainly because: (1) When the salt concentration is too high, the osmotic pressure of the water body is high, which tends to dehydrate the microbial cells and cause the separation of the cell protoplasts; (2) in the case of a high salt concentration, the salting out will dehydrogenate The enzyme activity is reduced; 〔3) The high chloride ion concentration is toxic to bacteria; (4) Due to the increase of water density, the activated sludge is easy to float and it is difficult to achieve muddy water separation.
国内现存的高盐废水处理方法有多效蒸发、 反渗透、 电渗析等, 然而这些方法普遍存在着能耗高、经济效益差、存在二次污染的缺点, 这与国家积极倡导的 "节能减排" 、 "循环经济"原则相违背, 如 何实现高盐有机废水的资源化治理成为当今水污染防治的一个难点。  The existing high-salt wastewater treatment methods in China have multi-effect evaporation, reverse osmosis, electrodialysis, etc. However, these methods generally have the disadvantages of high energy consumption, poor economic efficiency and secondary pollution, which is related to the “energy saving reduction” actively advocated by the state. The principle of "recycling economy" and "circular economy" are contrary to each other. How to realize the resource management of high-salt organic wastewater has become a difficult point in the prevention and control of water pollution.
近年来, 国内对于高含盐有机废水的生物处理大多局限于实验室 小试、并且多集中于活性污泥的盐度驯化。 当高盐废水的盐度高于 5% 时, 处理效果开始恶化。 嗜盐菌是一类极端微生物, 盐分是其生长、 繁殖的必要条件,直接利用其处理高含盐有机废水逐渐受到人们的关 注, 然而现阶段, 嗜盐菌的现场实验研究以至高盐废水净化回用工程 案例, 尚未见报道。  In recent years, domestic biological treatment of high-salt organic wastewater has been limited to laboratory tests and concentrated on the salinity of activated sludge. When the salinity of the high-salt wastewater is higher than 5%, the treatment effect begins to deteriorate. Halophilic bacteria are a kind of extreme microorganisms. Salt is a necessary condition for their growth and reproduction. The direct treatment of high-salt organic wastewater has attracted people's attention. However, at this stage, the field experiment of halophilic bacteria and purification of high-salt wastewater Reusing engineering cases, no reports have been reported.
何健,李顺鹏,崔中利等在 "含盐工业废水生化处理耐盐污泥驯 化及其机制" (中国环境科学,2002, 22 (6) : 546〜550 )中: 该研究所 用的微生物是普通的微生物, 不是嗜盐菌。将普通的微生物用于高盐 废水是有难度的, 微生物不能直接用于高盐废水处理, 废水的盐度只 能让普通微生物不断适应,但这种适应是很有限度一般含盐可到到 5%。 胡训杰,杨玉楠,刘红等在 "嗜盐菌强化生物活性炭处理不同盐 度采油废水的 He Jian, Li Shunpeng, Cui Zhongli et al. "In the domestication of salt-tolerant industrial wastewater with salt-tolerant sludge and its mechanism" (Chinese Journal of Environmental Science, 2002, 22 (6): 546~550): The microorganisms used in this study are common. Microbes, not halophiles. It is difficult to use ordinary microorganisms for high-salt wastewater. Microorganisms cannot be directly used for high-salt wastewater treatment. The salinity of wastewater can only be adapted to ordinary microorganisms, but this adaptation is very limited. 5%. Hu Xunjie, Yang Yunan, Liu Hong et al. In the treatment of different salinity production wastewater by halophilic bacteria-enhanced biological activated carbon
研究" (环境科学,2007, 28 (10) : 2213〜2217 ) 中: 本实验采用生物 活性炭处理方法,通过投加嗜盐菌 (但没有公开是那种嗜盐菌) 进行 生物强化,研究生物膜 (嗜盐菌被固定在活性炭上形成的生物膜) 对 于不同水质、 不同盐浓度采油废水的适应性及处理效果,以期为胜利 油田不同地区含盐量不同的采油废水的处理提供可靠的参考;该嗜盐 菌只能耐受 2 %〜6 %盐浓度, 所处理的废水含盐浓度最高达到 3. 3%。 Research" (Environmental Science, 2007, 28 (10): 2213~2217): This experiment uses biological activated carbon treatment method, by adding halophilic bacteria (but not disclosed as the kind of halophilic bacteria) for bio-enhancement, research organisms Membrane (biofilm formed by halophilic bacteria immobilized on activated carbon) The adaptability and treatment effect of different water quality and different salt concentration of oil production wastewater, in order to provide a reliable reference for the treatment of oil production wastewater with different salt content in different areas of Shengli Oilfield 3%。 The sulphate sulphate sulphate sulphate.
解庆林,李艳红,朱义年等在 "高盐度污水生物处理技术研究" (环境工程 2004, 22 (2) : 15〜16 ) 中, 针对废水盐度高和可生化性较 好的特点, 首先分别从城市污水处理厂取活性污泥和消化污泥, 进行 驯化, 然后进行废水生物化学处理实验; 在室内实验的基础上, 再将 实验装置搬运至污水站进行现场试验, 首先利用 UASB 厌氧反应器和 SBR 好氧反应器分别处理废水, 再采用 MSB厌氧反应器与 SBR好氧 反应器联合生化进行废水处理; 其提到工艺流程, 对嗜盐菌的描述不 多, 从其处理的油污水来看, 嗜盐菌的嗜盐度大约在 1%〜3%。  Xie Qinglin, Li Yanhong, Zhu Yinian, etc. In the "Study on Biological Treatment Technology of High Salinity Wastewater" (Environmental Engineering 2004, 22 (2): 15~16), the characteristics of high salinity and good biodegradability of wastewater are firstly The municipal sewage treatment plant takes activated sludge and digested sludge for domestication, and then carries out biochemical treatment of wastewater. On the basis of laboratory experiments, the experimental device is transported to the sewage station for on-site testing, first using the UASB anaerobic reactor. The wastewater is treated separately with the SBR aerobic reactor, and the wastewater is treated with the MSB anaerobic reactor and the SBR aerobic reactor. The process flow refers to the description of the halophilic bacteria. In view, the halophilicity of halophilic bacteria is about 1% to 3%.
王钱福在 "嗜盐菌的分离及其多相分类学研究" (兰州大学生命 科学学院, 2007 ) 中主要讲述了嗜盐菌的富集培养和分离, 从青岛和 甘肃河西走廊地区的高盐环境采集到样品,进行嗜盐微生物的分离和 多相分类研究, 该嗜盐微生物耐盐度仅达到 20%, 但并没有应用到废 水的处理。  Wang Qianfu's "Separation of halophilic bacteria and its multi-phase taxonomy" (Lanzhou University School of Life Sciences, 2007) mainly describes the enrichment and isolation of halophilic bacteria, from the high in the Hexi Corridor area of Qingdao and Gansu. Samples were collected from the salt environment for separation of halophilic microorganisms and multi-phase classification studies. The salinity of the halophilic microorganisms was only 20%, but it was not applied to wastewater treatment.
因此, 现有技术存在: 现有普通微生物或耐盐菌的其耐盐度仅在 6%以下; 和  Therefore, the prior art exists: existing general microorganisms or salt-tolerant bacteria have a salt tolerance of only 6% or less;
未进行其应用研究, 如工业废水处理的研究等缺陷。 No application research, such as research on industrial wastewater treatment, has been carried out.
处理高含盐有机废水的关键在于: 首先要筛选分离出能耐受高含 盐有机废水  The key to the treatment of high-salt organic wastewater is: First, we must screen and isolate organic wastewater that can withstand high salinity.
的极端嗜盐菌; 要将所筛选分离出极端嗜盐菌进行选优、 组合培养; 并将极端嗜盐菌用于高含盐有机废水生物处理系统的启动、 调试等。 Extreme halophilic bacteria; to select and isolate extreme halophilic bacteria for selection and combination culture; and to use extreme halophilic bacteria for the start-up and debugging of high-salt organic wastewater biological treatment system.
至今还没有一种即高效又经济实用的处理高盐有机废水中的治 理方法。  To date, there has not been an efficient and economical treatment method for treating high-salt organic wastewater.
发明内容 本发明的发明人为了解决上述高盐废水处理中存在的缺陷提出 并完成了本发明。 Summary of the invention The inventors of the present invention have proposed and completed the present invention in order to solve the defects existing in the above-described high-salt wastewater treatment.
因此本发明的目的是筛选极端嗜盐菌。  It is therefore an object of the invention to screen for extreme halophiles.
本发明的再一目的是提供包含上述极端嗜盐菌的复合嗜盐菌菌 剂。  A further object of the present invention is to provide a composite halophilic fungus comprising the above extreme halophile.
本发明的再一目的是提供制备上述复合嗜盐菌菌剂的方法。  It is still another object of the present invention to provide a method of preparing the above-described complex halophilic bacteria agent.
本发明的另一目的是提供处理高盐生产废水的方法。  Another object of the present invention is to provide a method of treating high salt production wastewater.
本发明的另一目的是提供上述极端嗜盐菌的应用。  Another object of the invention is to provide the use of the above extreme halophiles.
根据本发明的极端嗜盐菌, 可以为盐单胞菌 iHalomonas sp) , 其保藏编号为: CGMCC No. 3081。  The extreme halophilic bacteria according to the present invention may be Salmonella iHalomonas sp), and its storage number is CGMCC No. 3081.
根据本发明的极端嗜盐菌, 可以为假单胞菌 sp) , 其保藏编号为: CGMCC No. 3082。  The extreme halophilic bacteria according to the present invention may be Pseudomonas sp., and its storage number is: CGMCC No. 3082.
根据本发明的极端嗜盐菌, 可以为芽孢杆菌 ½3ci77^ sp) , 其 保藏编号为: CGMCC No. 3083。  The extreme halophilic bacteria according to the present invention may be Bacillus sp. 1⁄23ci77^ sp), and its storage number is CGMCC No. 3083.
根据本发明的复合嗜盐菌菌剂包括上述极端嗜盐菌 CGMCC No. 3081、 CGMCC No. 3082、 CGMCC No. 3083中任意两种或三种。  The composite halophilic bacteria agent according to the present invention includes any two or three of the above extreme halophilic bacteria CGMCC No. 3081, CGMCC No. 3082, and CGMCC No. 3083.
优选, 根据本发明的复合嗜盐菌菌剂包括上述三种极端嗜盐菌, 其中, 所述嗜盐菌 CGMCC No. 3081: CGMCC No. 3082: CGMCC No. 3083 为 3 : 3: 1。  Preferably, the composite halophilic bacteria agent according to the present invention comprises the above three extreme halophilic bacteria, wherein the halophilic bacteria CGMCC No. 3081: CGMCC No. 3082: CGMCC No. 3083 is 3:3:1.
根据本发明的制备上述复合嗜盐菌菌剂的方法包括以下步骤: The method for preparing the above composite halophilic bacteria agent according to the present invention comprises the following steps:
1 )将上述嗜盐菌 CGMCC No. 3081、 CGMCC No. 3082、 CGMCC No. 3083 中的一种或多种在复合菌剂培养基中、 在 25_35°C培养 7天 -10天;1) one or more of the above-mentioned halophilic bacteria CGMCC No. 3081, CGMCC No. 3082, CGMCC No. 3083 are cultured in a composite microbial culture medium at 25_35 ° C for 7 days - 10 days;
2 ) 将上述培养的复合极端嗜盐菌剂在扩大培养基中进行扩大培 养, 得复合嗜盐菌菌剂, 其中, 在所述步骤 1 )和 2 ) 中, 所使用的培 养基配方为:酵母浸膏 10 g/L,蛋白嗜盐 15g/L, MgS04 · 7H20 20 g/L , KCL 2 g/L , NaCL 180 g/L , pH 7. 0。 2) The above cultured compound extreme halophilic agent is expanded and cultured in an expansion medium to obtain a compound halophilic bacteria agent, wherein, in the steps 1) and 2), the medium formula used is: Yeast extract 10 g / L, protein halophilic 15g / L, MgS0 4 · 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7. 0.
本发明还提供了一种处理高盐生产废水的方法,所述方法包括向 生产废水处理系统中投加上述复合嗜盐菌菌剂的步骤, 其特征在于, 生产废水的 COD浓度为 3000 rag/L -3500 mg/L, 按系统的 1/10-1/20 容积比逐级进行培养, 最终达到处理系统完全完成培养。  The present invention also provides a method of treating high-salt production wastewater, the method comprising the step of adding the above-mentioned composite halophilic bacteria to a production wastewater treatment system, characterized in that the COD concentration of the production wastewater is 3000 rag/ L -3500 mg / L, cultured step by step according to the system's 1/10-1/20 volume ratio, and finally the treatment system is completely completed.
本发明还提供了上述极端嗜盐在处理高盐生产废水中的应用。 如图 1所示, 使用本发明的三株极端嗜盐菌的组合处理三聚氯氰 生产废水的工艺流程主要以下分两个阶段: The invention also provides the use of the above extreme halophilic salt in the treatment of high salt production wastewater. As shown in Fig. 1, the process for treating the cyanuric chloride production wastewater using the combination of the three extreme halophilic bacteria of the present invention is mainly divided into two stages:
(一) 启动阶段  (1) Start-up phase
1、 复合极端嗜盐菌剂的制备  1. Preparation of compound extreme halophilic agent
将上述三株极端嗜盐菌进行组合, 制备极端嗜盐菌复合菌剂; Combining the above three extreme halophilic bacteria to prepare an extreme halophilic composite fungus;
2、 极端嗜盐菌复合菌剂的现场应用 2. Field application of extreme halophilic composite microbial agents
将极端嗜盐菌复合菌剂按现场所需要进行扩大培养; 然后再将极 端嗜盐菌复合菌剂投加于处理三聚氯氰生产废水处理系统中,定期加 入极端嗜盐菌复合菌剂,使三种极端嗜盐菌复合菌剂在处理系统能良 好生长并形成生物膜, 完成了启动阶段。  The extreme halophilic composite fungicide is expanded and cultured according to the needs of the site; then the extreme halophilic composite fungicide is added to the wastewater treatment system for treating cyanuric chloride, and the extreme halophilic composite fungicide is periodically added. The three extreme halophilic composite microbial agents were able to grow well in the treatment system and form a biofilm, completing the start-up phase.
(二) 驯化阶段  (ii) Domestication stage
启动阶段完成后, 进入驯化阶段, 即: 逐渐减少极端嗜盐菌复合 菌剂的投加量, 并逐渐增加三聚氯氰生产废水的量, 直到极端嗜盐菌 复合菌剂的投加量为 0, 三聚氯氰生产废水的量增加到 100%;  After the start-up phase is completed, the acclimation phase is entered, namely: gradually reducing the dosage of the extreme halophilic composite microbial agents, and gradually increasing the amount of cyanuric cyanide production wastewater until the dosage of the extreme halophilic composite fungicide is 0, the amount of cyanuric acid production wastewater increased to 100%;
启动及驯化完成后, 就进入整个生物系统与设备调试、 运行, 最 终使得高盐三聚氯氰废水的出水达到净化回用标准。  After the start-up and domestication are completed, the whole biological system and equipment are commissioned and operated, and the effluent of the high-salt cyanuric chloride wastewater is finally purified.
根据本发明的极端嗜盐菌 CGMCC No. 3081 , 该盐单胞菌在处理高 盐三聚氯氰生产废水中去除总有机碳 (T0C ) 效果为 80. 01%;  01%; The effect of the removal of total organic carbon (T0C) in the high-salt cyanide production wastewater is 80. 01%;
根据本发明的极端嗜盐菌 CGMCC No. 3082 , 该假单胞菌在处理高 盐三聚氯氰生产废水中去除总有机碳 (T0C ) 效果为 69. 71%;  The effect of removing total organic carbon (T0C) in the treatment of high-salt cyanuric chloride production wastewater is 69.71%, according to the extreme halophilic bacteria CGMCC No. 3082 of the present invention;
根据本发明的极端嗜盐菌 CGMCC No. 30823 , 该芽孢杆菌在处理高 盐三聚氯氰生产废水中去除总有机碳 (T0C ) 效果为 74. 66%;  The effect of removing total organic carbon (T0C) in the treatment of high-salt cyanuric chloride production wastewater is 74.66%, according to the extreme halophilic bacteria CGMCC No. 30823 of the present invention;
上述三株极端嗜盐菌组合后, 在处理高盐三聚氯氰生产废水中去 除 T0C效果为 94. 86%。  After the combination of the above three extreme halophilic bacteria, the effect of removing T0C in the high-salt cyanide production wastewater was 94.86%.
本发明的三株极端嗜盐菌组合后的复合极端嗜盐菌菌剂之所以 能将高盐三聚氯氰生产废水进行有效的处理, 其原理为: 该三株极端 嗜盐菌可将高盐三聚氯氰生产废水中的高盐和有机物作为营养物,营 养物越多极端嗜盐菌生长越好, 当废水中营养物质越来越少、并少到 无法利用的量的时候, 该极端嗜盐菌就处于生长缓慢、不生长甚至休 眠状态; 即使得高盐三聚氯氰生产废水达到合格出水标准;一旦再有 新的高盐三聚氯氰生产废水进入处理系统时,该三株极端嗜盐菌又会 处于快速生长的状态。 因此, 根据本发明的方法, 好氧预挂生物膜的 成功运用解决了厌氧反应启动慢、 难于与好氧反应同步进行的难题, 实现了厌氧反应的快速启动;同时解决了高盐废水泥水难于分离的难 题, 并维持了装置内的微生物浓度, 增加了容积负荷。 The composite extreme halophilic bacteria agent combined with the three extreme halophilic bacteria of the present invention can effectively treat the high-salt cyanuric chloride production wastewater, and the principle is as follows: The three extreme halophilic bacteria can be high High salt and organic matter in the wastewater of cyanuric chloride production as a nutrient. The more nutrients, the better the growth of extreme halophilic bacteria. When the amount of nutrients in the wastewater is less and less, and the amount is not available, Extremely halophilic bacteria are in a state of slow growth, no growth or even dormancy; that is, the high-salt cyanuric chloride production wastewater meets the qualified water discharge standard; once new high-salt cyanuric chloride production wastewater enters the treatment system, the third Extreme halophilic bacteria In a state of rapid growth. Therefore, according to the method of the present invention, the successful application of the aerobic pre-suspended biofilm solves the problem that the anaerobic reaction starts slowly and is difficult to be synchronized with the aerobic reaction, and the rapid start of the anaerobic reaction is realized; The muddy water is difficult to separate, and maintains the microbial concentration in the device, increasing the volumetric load.
本发明分离得到了耐盐度在 15-25%的 3株极端嗜盐菌菌株, 三株极 端嗜盐菌组合后的复合极端嗜盐菌菌剂能将高盐三聚氯氰生产废水 进行有效的处理, 与其他处理技术相比, 本发明的方法更符合 "循环 经济" 、 "节能减排" 的国家政策, 能为企业节约大量的运行成本, 实现废水的资源化处理。 附图说明 The invention obtains three strains of extreme halophilic bacteria with salinity resistance of 15-25%, and the compound extreme halophilic bacteria agent after combination of three extreme halophilic bacteria can effectively treat high-salt cyanuric chloride production wastewater. Compared with other processing technologies, the method of the present invention is more in line with the national policy of "circular economy" and "energy saving and emission reduction", which can save a large amount of operating costs for enterprises and realize resource recycling treatment. DRAWINGS
图 1为本发明的三株极端嗜盐菌组合用于处理高盐三聚氯氰生产 废水工艺流程图。  Fig. 1 is a flow chart showing the process of treating the high-salt cyanuric chloride production wastewater by the three extreme halophilic bacteria combinations of the present invention.
图 2为盐单胞菌 Halomonas CGMCC No. 3081的脂肪酸图谱。 图 3为芽孢杆菌 G¾ci7 i/s) CGMCC No. 3083的脂肪酸图谱。  Figure 2 is a fatty acid profile of Halomonas CGMCC No. 3081. Figure 3 is a fatty acid profile of Bacillus sp. G3⁄4ci7 i/s) CGMCC No. 3083.
图 4所示为假单胞菌 (Malomonas CGMCC No. 3082的脂肪酸图谱。 极端嗜盐菌:  Figure 4 shows the fatty acid profile of Pseudomonas (Malomonas CGMCC No. 3082. Extremely halophilic bacteria:
( 1 ) 盐单胞菌 ( alomor s sp) , 保藏编号为 CGMCC No. 3081 , 保藏日期: 2009年 6月 1日;  (1) Alomor s sp, deposited under the symbol CGMCC No. 3081, date of deposit: June 1, 2009;
( 2 ) 假单胞菌
Figure imgf000007_0001
sp) , 保藏编号 CGMCC No. 3082 , 保藏日期: 2009年 6月 1日;
( 2 ) Pseudomonas
Figure imgf000007_0001
Sp), deposit number CGMCC No. 3082, date of deposit: June 1, 2009;
( 3 ) 所示为芽孢杆菌 dc/ ^), 保藏编号 CGMCC No. 3083, 保 藏日期: 2009年 6月 1日, 保藏于中国微生物菌种保藏管理委员会普通 微生物中心,地址:北京市朝阳区大屯路,中国科学院微生物研究所, 100101。 具体实fe^:  (3) shown as Bacillus dc/^), deposit number CGMCC No. 3083, date of deposit: June 1, 2009, deposited at the General Microbiology Center of the China Microbial Culture Collection Management Committee, Address: Chaoyang District, Beijing Kushiro, Institute of Microbiology, Chinese Academy of Sciences, 100101. Specific real fe^:
实施例 1觸极端嗜盐菌  Example 1 Extreme Extreme Halophilic Bacteria
1、 极端嗜盐菌菌株的分离  1. Separation of extreme halophilic strains
1. 1 ) 原位多点法采集盐化工企业的污泥池及污水排污口处的污 泥样泥;  1. 1) In-situ multi-point method for collecting sludge from the sludge tank of the salt chemical industry and sewage sludge at the sewage discharge port;
1. 2 )将所采集的污泥样泥在含盐 16wt%-26wtl)的液体富集培养基 中 25-35 Ό进行富集培养 3-10天; 1. 2) The collected sludge is in a liquid enrichment medium containing 16wt%-26wtl of salt) Enrichment culture in medium 25-35 3 for 3-10 days;
1. 3 )再将经富集培养后的污泥样泥在分离培养基中、 25-35 Ό下 进行分离培养, 得到分离单菌株; 再将分离得到的单菌株在纯化分离 培养基中进行 2-6次纯化分离培养, 从而选出耐盐度在 15-25%的 23株 极端嗜盐菌菌株;所使用的纯化分离培养基与上述分离培养基的组分 及各组分含量相同;  1. 3) The sludge-like mud after enrichment and cultivation is separated and cultured in a separation medium at 25-35 Torr to obtain a single strain; the isolated single strain is then subjected to purification and separation medium. 2-6 purification and isolation cultures were selected to select 23 strains of extreme halophilic bacteria with a salt tolerance of 15-25%; the purified separation medium used was the same as the components and components of the above separation medium;
所述液体富集培养基组分及各组分含量如下: 蛋白胨 15g/L, MgS04 · 7H20 20 g/L, KCL 2 g/L, NaCL 150—250 g/L, pH 7. 0; The components of the liquid enriched medium and the contents of the components are as follows: peptone 15 g / L, MgS0 4 · 7H 2 0 20 g / L, KCL 2 g / L, NaCL 150 - 250 g / L, pH 7. 0 ;
所述分离培养基组分及各组分含量与所述纯化分离培养培养基 组分及各组分含量相同, 均为: 酪素水解物 5 g/L, 酵母浸膏 10 g/L, 蛋白胨 15g/L, MgS04 · 7H20 20 g/L , KCL 2 g/L,, NaCL 150-250 g/L , pH 7. 0; The components of the separation medium and the content of each component are the same as the components of the purified separation culture medium and the components, and are: casein hydrolysate 5 g/L, yeast extract 10 g/L, peptone 15g / L, MgS0 4 · 7H 2 0 20 g / L, KCL 2 g / L,, NaCL 150-250 g / L, pH 7. 0;
2、 分离筛选极端嗜盐菌  2. Separation and screening of extreme halophiles
将分离得到的耐盐度在 15-25%的 23株极端嗜盐菌菌株进行逐株 筛选:  The isolated strains of 23 extreme halophilic strains with a salt tolerance of 15-25% were screened one by one:
将每一株极端嗜盐菌菌株在含盐 18wt%-20 \^%的高盐三聚氯氰 废水中进行处理效果试验:  The treatment effect of each strain of extreme halophilic bacteria in high-salt cyanuric chloride wastewater containing 18wt%-20% of salt:
2. 1 )选出去除 T0C效果为 80. 01%的一株菌株, 进行测定, 定为盐 单胞菌 Halomonas sp) (保藏于中国微生物菌种保藏管理委员会普 通微生物中心, 保藏编号为 CGMCC No. 3081 );  2. 1) Select a strain with a T0C removal effect of 80. 01% and measure it as Halomonas sp) (preserved by the General Microbiology Center of the China Microbial Culture Collection Management Committee, with the accession number CGMCC No 3081 );
其鉴定技术为: 采用微生物生理生化反应与 MIDI Sherlock Mi s 相结合进行鉴定; MIDI Sherlock Mi s鉴定系统软件可以操控 Agi lent 公司的 6850、 6890和 7890型气相色谱,通过对气相色谱获得的短链脂 肪酸的种类和含量的图谱进行比对,从而快速准确地对微生物种类进 行鉴定。  Its identification technology is: Identification of microbial physiological and biochemical reactions combined with MIDI Sherlock Mi s; MIDI Sherlock Mi s identification system software can control Agi lent's 6850, 6890 and 7890 GCs, through the short chain obtained by gas chromatography A map of the type and content of fatty acids is compared to quickly and accurately identify microbial species.
图 2为盐单胞菌 Halomo s CGMCC No. 3081的脂肪酸图谱, 该盐 单胞菌 Halomoms 的耐盐度为 15%-25%。  Figure 2 is a fatty acid profile of Halomos sinensis CGMCC No. 3081, which has a salt tolerance of 15%-25%.
2. 2 )选出去除 T0C效果为 74. 66%的一株菌株菌株, 进行测定, 定 为芽孢杆菌 (^ci ^ sp) (保藏于中国微生物菌种保藏管理委员会 普通微生物中心, 保藏编号 CGMCC No. 3083);  2. 2) Select a strain of strain that has a T0C removal effect of 74.66%, and determine it as Bacillus (^ci ^ sp) (deposited in the General Microbiology Center of the China Microbial Culture Collection Management Committee, deposit number CGMCC No. 3083);
其鉴定方法与鉴定盐单胞菌 iHal面 nas 的方法相同; 图 3所示 为芽孢杆菌 Us«7A/s) CGMCC No. 3083的脂肪酸图谱, 该芽孢杆菌 (Bacillus sp)的耐盐度为 15%- 25%。 The method of identification is the same as the method for identifying nas nas iHal nas; Figure 3 For the fatty acid profile of Bacillusus Us77/s) CGMCC No. 3083, the Bacillus sp. has a salt tolerance of 15% to 25%.
2. 3 )选出去除 T0C效果为 69. 71%的一株菌株菌株, 进行测定定为 假单胞菌 ( ¾ew i¾^a3s sp) (保藏于中国微生物菌种保藏管理委员 会普通微生物中心, 保藏编号 CGMCC No. 3082);  2. 3) Select a strain of strain that has a T0C removal effect of 69.71%, and determine it as Pseudomonas (3⁄4ew i3⁄4^a3s sp) (deposited in the General Microbiology Center of the China Microbial Culture Collection Management Committee, No. CGMCC No. 3082);
其鉴定方法与鉴定盐单胞菌 IMomonas 的方法相同; 图 4所示 为假单胞菌 alomo s CGMCC No. 3082的脂肪酸图谱, 该假单胞菌 { Halomonas) 的耐盐度为 15%_25%。  The identification method is the same as the method for identifying M. monosyllium IMomonas; Figure 4 shows the fatty acid profile of Pseudomonas alomo s CGMCC No. 3082, the salt tolerance of the Pseudomonas { Halomonas) is 15% - 25% .
通过将上述三株极端嗜盐菌分别、以及组合后处理高盐三聚氯氰 废水的试验, 得出极端嗜盐菌 CGMCC No. 3081 , 去除总有机碳 (T0C ) 效果为 80. 01%; 极端嗜盐菌 CGMCC No. 3082去除总有机碳 (T0C) 效果 为 69. 71%; 极端嗜盐菌 CGMCC No. 30823去除总有机碳 (T0C ) 效果为 74. 66%; 上述三株极端嗜盐菌组合后处理高盐三聚氯氰废水的去除 T0C效果为 94. 86%;  01%; The effect of removing the total organic carbon (T0C) is 80. 01%; The total halophilic bacteria CGMCC No. 3082 had a total organic carbon (T0C) removal effect of 69.71%; the extreme halophilic bacteria CGMCC No. 30823 had a total organic carbon (T0C) removal effect of 74.66%; 86%; After removing the T0C effect of the high-salt cyanuric chloride wastewater after the combination of the bacteria was 94.86%;
实施例 2制备复合嗜盐菌剂 Example 2 Preparation of Compound Halophilic Agent
1 ) 将上述三株极端嗜盐菌在复合菌剂培养基中 25-35Ό培养 7天 - 10天,其中,所述菌株 CGMCC No. 3081: CGMCC No. 3082: CGMCC No. 3083 为 3 : 3 : 1, 得复合极端嗜盐菌剂;  1) The above three extreme halophilic bacteria are cultured in a compound culture medium at 25-35 7 for 7 days to 10 days, wherein the strain CGMCC No. 3081: CGMCC No. 3082: CGMCC No. 3083 is 3:3 : 1, a compound extreme halophilic agent;
所述复合菌剂培养基组分及各组分含量为: 酵母浸膏 10 g/L, 蛋 白嗜盐 15g/L, MgS04 · 7H20 20 g/L , KCL 2 g/L, NaCL 180 g/L , PH 7. 0。 The composition of the composite agent medium and the content of each component are: yeast extract 10 g / L, protein halophilic 15 g / L, MgS0 4 · 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g/L , P H 7. 0.
2 ) 将上述复合极端嗜盐菌剂进行扩大培养  2) Expanding the above-mentioned compound extreme halophilic agent
将上述复合极端嗜盐菌剂在复合嗜盐菌剂扩大培养基中 25-30 °C, 进行扩大培养 7-10天, 得复合嗜盐菌剂;  The above compound extreme halophilic agent is expanded and cultured in a compound halophilic agent expansion medium at 25-30 ° C for 7-10 days to obtain a compound halophilic agent;
所述复合菌剂扩大培养基组分及各组分含量为: 酵母浸膏 10 g/L, 蛋白胨 15g/L, MgS04 - 7H20 20 g/L, KCL 2 g/L, NaCL 180 g/L, pH 7. 0。 实施例 3使用本发明的三株极端嗜盐菌组合处理 "德固赛三征 (营口)精细化工有限公司"的三聚氯氰生产废水的模拟实验 The composition of the composite agent and the content of each component are: yeast extract 10 g / L, peptone 15 g / L, MgS0 4 - 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g /L, pH 7. 0. Example 3 Using the three extreme halophilic bacteria combinations of the present invention to treat the simulated production of cyanuric chloride production wastewater of "Degusai Sanzheng (Yingkou) Fine Chemical Co., Ltd."
使用本发明的三株极端嗜盐菌组合用于处理 "德固赛三征(营口 ) 精细化工有限" 的含盐 18wt%的高盐三聚氯氰生产废水: 1、 首先制备复合试验菌剂: The use of the three extreme halophilic bacteria combinations of the present invention is used to treat 18% by weight of high-salt cyanuric chloride production wastewater containing "Degussa Sanzheng (Yingkou) Fine Chemicals Co., Ltd.": 1. First prepare a composite test agent:
将本发明的上述三株极端嗜盐菌在复合菌剂培养基中 25 °C培养 10天, 得复合嗜盐菌剂;  The above three extreme halophilic bacteria of the present invention are cultured in a composite bacterial culture medium at 25 ° C for 10 days to obtain a composite halophilic agent;
所述复合菌剂培养基组分为:酵母浸膏 10 g/L,蛋白嗜盐 15g/L, MgS04 · 7H20 20 g/L, KCL 2 g/L, NaCL 180 g/L, pH 7. 0 ; The composition of the composite microbial culture medium is: yeast extract 10 g/L, protein halophilic 15 g/L, MgS0 4 · 7H 2 0 20 g/L, KCL 2 g/L, NaCL 180 g/L, pH 7. 0 ;
将上述复合嗜盐菌剂进行扩大培养:  The above composite halophilic agent is expanded and cultured:
将上述复合极端嗜盐菌剂在复合菌剂扩大培养基中、 25°C进行扩 大培养 10天, 得扩大培养后复合嗜盐菌剂;  The above-mentioned compound extreme halophilic agent is expanded and cultured in a composite microbial expansion medium at 25 ° C for 10 days to obtain a compound halophilic agent after expanding the culture;
所述复合菌剂扩大培养基组分为: 酵母浸膏 10 g/L , 蛋白胨 15g/L, MgS04 · 7H20 20 g/L , KCL 2 g/L, NaCL 180 g/L, pH 7. 0; The composite agent expansion medium components are: yeast extract 10 g / L, peptone 15 g / L, MgS0 4 · 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7 . 0;
2、 向高盐三聚氯氰生产废水的处理系统投加上述复合菌剂, 按 生物处理系统体积的 1/10投加极端嗜盐菌剂。 将该公司的含盐 18wt% 的高盐三聚氯氰生产废水进行预处理(所述预处理为本领域的公知技 术) 后, 进入所述处理系统, 经厌氧处理和好氧处理处理后, T0C含 量可达到 10mg/L以下、 氨氮含量达到 4mg/L以下, 氰化物含量达到 0. 054mg/L以下, 基本达到该企业废水回用标准。  2. Add the above compound bacteria to the treatment system of high-salt cyanuric chloride production wastewater, and add an extreme halophilic agent according to 1/10 of the volume of the biological treatment system. After pretreating the company's salt-containing 18 wt% high-salt cyanuric chloride production wastewater (the pretreatment is a well-known technique in the art), it enters the treatment system and is subjected to anaerobic treatment and aerobic treatment. The T0C content can reach below 10mg/L, the ammonia nitrogen content is below 4mg/L, and the cyanide content is below 0. 054mg/L, which basically meets the wastewater reuse standard of the enterprise.
实施例 4使用本发明的三株极端嗜盐菌组合处理 "河北临港化工 有限公司"的三聚氯氰生产废水的模拟实验  Example 4 Simulation experiment of the wastewater of cyanuric chloride production of "Hebei Lingang Chemical Co., Ltd." using the three extreme halophilic bacteria combinations of the present invention
使用本发明的三株极端嗜盐菌组合用于处理 "河北临港化工有 限公司"含盐 18wt%-20wt%的高盐三聚氯氰生产废水; 其工艺与实施 例 1工艺流程基本相同。  The three extreme halophilic bacteria combinations of the present invention are used for treating high-salt cyanuric chloride production wastewater containing "salt of 18 wt% to 20 wt%" of "Hebei Lingang Chemical Co., Ltd."; the process is basically the same as that of the embodiment 1.
1、 首先制备复合试验菌剂:  1. First prepare a composite test agent:
将本发明的上述三株极端嗜盐菌在复合菌剂培养基中 3CTC培养 80天, 得复合嗜盐菌剂;  The above three extreme halophilic bacteria of the present invention are cultured for 3 days in 3CTC in a composite bacterial culture medium to obtain a composite halophilic agent;
所述复合菌剂培养基组分为:酵母浸膏 10 g/L,蛋白嗜盐 15g/L, MgS04 · 7H20 20 g/L , KCL 2 g/L, NaCL 180 g/L , pH 7. 0 ; The composition of the composite microbial culture medium is: yeast extract 10 g/L, protein halophilic 15 g/L, MgS0 4 · 7H 2 0 20 g/L, KCL 2 g/L, NaCL 180 g/L, pH 7. 0 ;
将上述复合嗜盐菌剂进行扩大培养:  The above composite halophilic agent is expanded and cultured:
将上述复合极端嗜盐菌剂在复合菌剂扩大培养基中 3CTC,进行扩 大培养 8天, 得扩大培养后复合嗜盐菌剂;  The above-mentioned compound extreme halophilic agent is expanded and cultured in a composite microbial expansion medium for 3 days, and a compound halophilic agent is obtained after expanding the culture;
所述复合菌剂扩大培养基组分为: 酵母浸膏 10 g/L , 蛋白胨 15g/L, MgS04 · 7H20 20 g/L , KCL 2 g/L, NaCL 180 g/L, pH 7. 0; 2、 向高盐三聚氯氰生产废水的处理系统投加上述复合菌剂, 按 生物处理系统体积的 1Z10-1/20投加极端嗜盐菌剂。 将该公司含盐 18wt%-20wt%的高盐三聚氯氰生产废水进行预处理后, 进入本实施例 的高盐三聚氯氰生产废水的生物处理系统,在这个系统中有厌氧和好 氧处理, 经生物系统处理后, T0C含量可达到 10mg/L以下, 氨氮含量 达到 4mg/L以下, 氰化物含量达到 0. 054mg/L以下, 基本高盐三聚氯氰 生产废水达到企业回用要求。 The composite agent expansion medium components are: yeast extract 10 g / L, peptone 15 g / L, MgS0 4 · 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7 . 0; 2. Add the above compound bacteria to the treatment system of high-salt cyanuric chloride production wastewater, and add the extreme halophilic agent according to the volume of the biological treatment system of 1Z10-1/20. After pretreating the company's salt-containing 18wt%-20wt% high-salt cyanuric chloride production wastewater, it enters the biological treatment system of the high-salt cyanuric chloride production wastewater of the present embodiment, in which anaerobic and anaerobic Aerobic treatment, after treatment by biological system, T0C content can reach below 10mg/L, ammonia nitrogen content is below 4mg/L, cyanide content reaches below 0. 054mg/L, basic high-salt cyanuric chloride production wastewater reaches enterprise back With requirements.
实施例 5使用本发明的三株极端嗜盐菌组合处理 "德固赛三征 (重庆)精细化工有限公司"的三聚氯氰生产废水的模拟实验  Example 5 Simulation experiment of the wastewater of cyanuric chloride production of "Degussa Sanzheng (Chongqing) Fine Chemical Co., Ltd." using the three extreme halophilic bacteria combinations of the present invention
使用本发明的三株极端嗜盐菌组合用于处理 "德固赛三征(重庆) 精细化工有限公司"含盐 13wt%-15wt%的高盐三聚氯氰生产废水, 流 程与上述两个实例基本相同。  The use of the three extreme halophilic bacteria combinations of the present invention for treating "Degussa Sanzheng (Chongqing) Fine Chemical Co., Ltd." salt-containing 13wt%-15wt% high-salt cyanuric chloride production wastewater, the process and the above two The examples are basically the same.
1、 首先制备复合试验菌剂:  1. First prepare a composite test agent:
将本发明的上述三株极端嗜盐菌在复合菌剂培养基中 35°C培养 7 天, 得复合嗜盐菌剂;  The above three extreme halophilic bacteria of the present invention are cultured in a composite bacterial culture medium at 35 ° C for 7 days to obtain a composite halophilic agent;
所述复合菌剂培养基组分为:酵母浸膏 10 g/L ,蛋白嗜盐 15g/L, MgS04 · 7H20 20 g/L, KCL 2 g/L, NaCL 180 g/L , pH 7. 0 ; The composition of the composite bacteria medium is: yeast extract 10 g / L, protein halophilic 15 g / L, MgS0 4 · 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7. 0 ;
将上述复合嗜盐菌剂进行扩大培养:  The above composite halophilic agent is expanded and cultured:
将上述复合极端嗜盐菌剂在复合菌剂扩大培养基中 35Ό,进行扩 大培养 7天, 得扩大培养后复合嗜盐菌剂;  The above-mentioned compound extreme halophilic agent is cultured in a combined microbial expansion medium for 35 days, and expanded for 7 days to obtain a composite halophilic agent after expanding the culture;
所述复合菌剂扩大培养基组分为: 酵母浸膏 10 g/L , 蛋白胨 15g/L, MgS04 - 7H20 20 g/L , KCL 2 g/L, NaCL 180 g/L, pH 7. 0; The composite agent expansion medium components are: yeast extract 10 g / L, peptone 15 g / L, MgS0 4 - 7H 2 0 20 g / L, KCL 2 g / L, NaCL 180 g / L, pH 7 . 0;
2、 向高盐三聚氯氰生产废水的处理系统投加上述复合菌剂, 按 生物处理系统体积的 1/20 投加极端嗜盐菌剂。 将该公司含盐 18wt%_2(¼t%的高盐三聚氯氰生产废水进行预处理后, 进入本实施例 的高盐三聚氯氰生产废水的生物处理系统,在这个系统中有厌氧和好 氧处理, 经生物系统处理后, T0C含量可达到 30-40mg /L以下, 氨 氮含量达到 10mg /L以下, 氰化物含量达到 0. 05mg/L以下, 达到高 盐三聚氯氰生产废水达到企业回用要求。  2. Add the above-mentioned composite microbial agent to the treatment system of high-salt cyanuric chloride production wastewater, and add an extreme halophilic agent according to 1/20 of the volume of the biological treatment system. After pretreating the company's salt-containing 18wt%_2 (1⁄4t% high-salt cyanuric chloride production wastewater), it enters the biological treatment system of the high-salt cyanuric chloride production wastewater of this embodiment, and there is anaerobic in this system. And aerobic treatment, after treatment by biological system, T0C content can reach below 30-40mg / L, ammonia nitrogen content below 10mg / L, cyanide content of less than 0. 05mg / L, to achieve high-salt cyanuric chloride production wastewater Meet the enterprise recycling requirements.

Claims

权利要求 Rights request
1、 一种极端嗜盐菌, 其特征在于, 所述嗜盐菌为盐单胞菌, 其 保藏编号为: CGMCC No. 3081 ο  An extreme halophilic bacterium, characterized in that the halophilic bacterium is a salt bacterium, and the preservation number is: CGMCC No. 3081 ο
2、 一种极端嗜盐菌, 其特征在于, 所述嗜盐菌为假单胞菌, 其 保藏编号为: CGMCC No. 3082。  2. An extreme halophilic bacterium, wherein the halophilic bacterium is Pseudomonas, and the storage number is CGMCC No. 3082.
3、 一种极端嗜盐菌, 其特征在于, 所述嗜盐菌为芽孢杆菌, 其 保藏编号为: CGMCC No. 3083。  3. An extreme halophilic bacterium, wherein the halophilic bacterium is Bacillus, and the storage number is CGMCC No. 3083.
4、 一种复合嗜盐菌菌剂, 其特征在于, 所述复合嗜盐菌菌剂包 括权利要求 1、 2或 3所述的极端嗜盐菌中任意两种或三种。  A complex halophilic bacterial agent, characterized in that the composite halophilic bacterial agent comprises any two or three of the extreme halophilic bacteria according to claim 1, 2 or 3.
5、 根据权利要求 4所述的复合嗜盐菌菌剂, 其特征在于, 所述复 合嗜盐菌菌剂包括权利要求 1、 2和 3所述的极端嗜盐菌, 其中, 所述 菌株 CGMCC No. 3081: CGMCC No. 3082: CGMCC No. 3083为 3: 3: 1。  The composite halophilic bacteria agent according to claim 4, wherein the complex halophilic bacteria agent comprises the extreme halophilic bacteria according to claims 1, 2 and 3, wherein the strain CGMCC No. 3081: CGMCC No. 3082: CGMCC No. 3083 is 3: 3: 1.
6、一种制备权利要求 4所述的复合嗜盐菌菌剂的方法, 其特征在 于, 所述方法包括以下步骤:  A method of producing a composite halophilic bacterial agent according to claim 4, wherein the method comprises the steps of:
1 )将权利要求 1、 2、 3所述的嗜盐菌中的一种或多种在复合菌剂 培养基中、 在 25-35 Ό培养 7天 -10天;  1) cultivating one or more of the halophilic bacteria according to claim 1, 2, 3 in a composite microbial culture medium at 25-35 7 for 7 days to 10 days;
2 ) 将上述培养的复合极端嗜盐菌剂在扩大培养基中进行扩大培 养, 得复合嗜盐菌菌剂。  2) The above-mentioned cultured compound extreme halophilic agent is expanded and cultured in an expanded medium to obtain a compound halophilic bacteria agent.
7、根据权利要求 6所述的方法,其特征在于,在所述步骤 1 )和 2 ) 中, 所使用的培养基配方为: 酵母浸膏 10 g/L, 蛋白嗜盐 15g/L, MgS04 · 7H20 20 g/L , KCL 2 g/L, NaCL 180 g/L , pH 7. 0。 The method according to claim 6, characterized in that in the steps 1) and 2), the medium used is: yeast extract 10 g/L, protein halophilic 15 g/L, MgS0 4 · 7H 2 0 20 g/L , KCL 2 g/L, NaCL 180 g/L, pH 7. 0.
8、 一种处理高盐生产废水的方法, 其特征在于, 所述方法包括 向生产废水处理系统中投加权利要求 4 所述的复合嗜盐菌菌剂的步 骤, 其中,生产废水的 C0D浓度为 3000 mg/L -3500 rag/L , 按系统的 1/10-1/20容积比添加。  A method for treating high-salt production wastewater, characterized in that the method comprises the step of adding the complex halophilic bacterial agent according to claim 4 to a production wastewater treatment system, wherein the COD concentration of the production wastewater It is 3000 mg/L -3500 rag/L and is added in a 1/10-1/20 volume ratio of the system.
9、权利要求 1、 2或 3所述的极端嗜盐在处理高盐生产废水中的 应用。  9. The use of extreme halophilicity as claimed in claim 1, 2 or 3 for the treatment of high salt production wastewater.
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