CN113185005B

CN113185005B - Method for on-line regeneration of activated carbon adsorption carrier by biological method

Info

Publication number: CN113185005B
Application number: CN202110587111.7A
Authority: CN
Inventors: 徐韡卿
Original assignee: Individual
Current assignee: Individual
Priority date: 2021-03-13
Filing date: 2021-05-27
Publication date: 2023-06-06
Anticipated expiration: 2041-05-27
Also published as: CN113185005A

Abstract

The invention relates to a method for regenerating active carbon on line by a biological method, which comprises the following steps: (1) In the filter tank, the composite functional microbial inoculum, the active carbon and the target raw water are mixed and cultivated, and domesticated to obtain the active carbon with stably attached composite functional bacterial colony suitable for the raw water environment; (2) And (3) introducing target raw water into the filter tank to degrade target pollutants to obtain the dischargeable water meeting the comprehensive sewage discharge standard or meeting the legal or legal requirements. According to the method, on the basis of retaining raw water and not filtering raw bacteria, the composite functional bacteria agent is put into the activated carbon filter tank, and a starting method of symbionts formed by compact and rich bacteria and secretion thereof is formed on the activated carbon adsorption carrier, so that the biological method on-line regeneration of the activated carbon is realized, the removal effect of target pollutants (organic matters, nitrogen and the like) is not reduced, the process is simplified, and the engineering operation and labor cost are greatly reduced.

Description

Method for on-line regeneration of activated carbon adsorption carrier by biological method

Technical Field

The invention belongs to the technical field of water treatment, and particularly relates to a method for regenerating an active carbon adsorption carrier on line by a biological method.

Background

The adsorption carrier is mainly used for adsorbing organic pollutants in the field of water treatment, and good adsorption carriers not only need very high adsorption capacity, but also have certain requirements on surface structures. Taking activated carbon as an example, the activated carbon has a rich void structure and a complex specific surface area, and has strong adsorption capacity and good chemical stability, so that the activated carbon is widely accepted as an application technology for various water quality treatments. However, the adsorption of the activated carbon to different water quality pollutants is stable, and once the adsorption saturation is achieved, the adsorption efficiency is reduced, even the activated carbon does not have adsorption capacity any more and needs to be replaced in time, so that the operation cost is high, and meanwhile, the treatment of the adsorption saturated activated carbon also becomes the burden of a user. Therefore, it is a common technical problem to apply to the field of water treatment, how to remove the adsorbate from the activated carbon saturated by adsorption to realize the regeneration of the activated carbon. The most commonly used heating regeneration method is to transfer the activated carbon saturated by adsorption, and the high-temperature degradation of the organic matters adsorbed in the activated carbon is carried out by setting the regeneration temperature to about 850 ℃, so that the method is widely applied to practical engineering. Although the method has a certain scale and universality, the method is complex in operation, consumes a great amount of energy consumption, operation and maintenance and labor cost, and is not suitable for practical engineering application. Therefore, how to realize the regeneration of the adsorption performance while the adsorption function of the activated carbon is exerted on site, so that the technical cost of treating the saturated activated carbon offline to regenerate the activated carbon is avoided, and the operation cost is saved.

At present, an ultrasonic regeneration method is mainly used as a remarkable technology in online treatment, an ultrasonic generating device is fixed in an activated carbon filter, an ultrasonic probe is extended into the activated carbon filter, and organic matters adsorbed on the surface of activated carbon are degraded by ultrasonic so as to realize in-situ regeneration. Although the technology can realize the regeneration of the activated carbon, the degradation activity of microorganisms can be influenced to a certain extent, and even fatal striking is caused to certain strains, so that certain degradation capacity is lost for the filter tank per se; the operating costs are also increased from the engineering application point of view. The biological regeneration is to decompose the organic matters adsorbed on the activated carbon by utilizing microorganisms so as to achieve the purpose of degrading pollutants and regenerating the activated carbon, and is also applied as a common water treatment technology. However, the feasibility of the technology in theory is difficult to put into complex engineering application, because different water systems are complex, and raw water contains different microorganism populations, the functional bacteria degrading the active carbon organic matters can be interfered, and even the functional bacteria are disabled. And the process or technology for maintaining the adsorption capacity of the activated carbon by decomposing the organic matters adsorbed on the activated carbon in a mode of directly adding functional bacteria is adopted, and the requirement on the organic matters in the water is less than 50mg/L, which severely limits the application of practical engineering. On the basis of the existing activated carbon filter, the degradability of the functional bacteria can be fully exerted only by the technical main body without depending on other technical means, and the interference of complex indigenous microorganisms in a raw water system on the degradation effect of exogenously added functional bacteria is not required to be considered, so that the adsorption and regeneration of the activated carbon are realized, and the method has a wide market prospect.

Disclosure of Invention

The invention aims to solve the defects in the prior art and provides a method for regenerating active carbon adsorption carriers on line by a biological method. The method realizes the technology of on-line regeneration of the activated carbon adsorption carrier by a biological method by putting the composite functional microbial inoculum into the activated carbon filter tank to form a biological film under the condition of retaining raw water and not removing original bacteria, simplifies the process and greatly reduces engineering operation and labor cost while ensuring that the removal effect of target pollutants (organic matters, nitrogen and the like) is not reduced.

Therefore, the invention provides a method for regenerating active carbon adsorption carriers on line by a biological method, which comprises the following steps:

step S1, in a filter tank, mixing and culturing a composite functional microbial inoculum, an activated carbon adsorption carrier and target raw water, and domesticating to obtain the activated carbon adsorption carrier with stably attached composite functional bacterial groups suitable for the raw water environment;

and S2, introducing target raw water into the filter tank to degrade target pollutants to obtain dischargeable water.

According to some embodiments of the invention, step S1 comprises:

step B, uniformly mixing the composite functional microbial inoculum, the nutrient solution and the target raw water to obtain a composite functional microbial inoculum-target raw water mixed solution;

Step C, adding the mixed solution of the composite functional microbial inoculum and the target raw water into a filter tank containing the activated carbon adsorption carrier, and adding the target raw water into the filter tank to enable the water level to rise until the activated carbon adsorption carrier is just immersed, so as to obtain a composite functional microbial inoculum-activated carbon adsorption carrier-target raw water mixture;

step D, after culturing the composite functional microbial inoculum-activated carbon adsorption carrier-target raw water mixture, evacuating the liquid in the filter tank;

step E, repeating the steps B-D to enable the compound functional bacteria group adapting to the raw water environment to be stably attached to the activated carbon adsorption carrier, so as to obtain the activated carbon adsorption carrier with the stably attached compound functional bacteria group adapting to the raw water environment;

in step E, steps B-D are repeated 2 or more times, preferably 2-3 times.

In some embodiments of the present invention, when the target pollutant in the target raw water is an organic matter and ammonia nitrogen, in the step B, uniformly mixing the composite functional microbial inoculum, the nutrient solution and the target raw water, and aerating to obtain a composite functional microbial inoculum-target raw water mixed solution; in the step D, air is introduced into the filter tank, and the mixture of the composite functional microbial inoculum, the activated carbon adsorption carrier and the target raw water is subjected to aerobic culture; preferably, the aerobic culture is carried out for 5 to 9 days.

In other embodiments of the present invention, when the target pollutant in the target raw water is an organic matter and total nitrogen, in the step D, standing, and performing anoxic cultivation on the composite functional microbial agent-activated carbon adsorption carrier-target raw water mixture; preferably, the anaerobic culture is performed for 3 to 5 days.

In the invention, the composite functional microbial inoculum comprises bacteria capable of degrading target pollutants in target raw water, it includes at least two of the genera of Eimeria (Thauera), rhodobacillus (Rhodobacillus), salmonella (Halomonas), sphingomonas (Sphingomonas), acinetobacter (Acinetobacter), agrimonia (Gemmobacter), brevibacterium (Brevibacterium), rhodococcus (Rhodococcus), micrococcus (Micrococcus), luo Saihe Microbacterium (Rhodanobacter), oligomonas (Stenotrophomonas), mycobacterium (Mycobacterium), pediococcus (Pediococcus), bacillus (Bacillus), achromobacter (Achromobacter), clostridium (Clostridium), microbacterium (Exiguobacterium), aeromonas (Aeromonas), pseudomonas (Pseudomonas) and Comamonas (Comamonas).

In the invention, the nutrient solution contains carbon, nitrogen and phosphorus elements; preferably, the nutrient solution contains glucose, urea and potassium dihydrogen phosphate; further preferably, the molar ratio of carbon, nitrogen and phosphorus in the nutrient solution is 100:5:1.

According to the invention, in the mixed solution of the composite functional microbial inoculum and the target raw water, the mass ratio of the composite functional microbial inoculum to the carbon source in the nutrient solution is (1-100) to 1, preferably (1-10) to 1; the total mass ratio of the water to the composite functional microbial inoculum and the nutrient solution is (1-1000) to 1, preferably (1-100) to 1.

In some embodiments of the present invention, in step C, the mixed solution of the composite functional microbial inoculum and the target raw water is uniformly distributed on the activated carbon adsorption carrier; preferably, the activated carbon adsorption carrier in the filter tank is a cleaned activated carbon adsorption carrier.

In the invention, the activated carbon adsorption carrier comprises activated carbon and/or activated coke.

In the present inventionIn some embodiments, the activated carbon is coal-derived granular activated carbon; preferably, the iodine value of the activated carbon is 600-1100, the intensity is more than 90 percent, and the specific surface area is 500-1200 m ² /g。

In other embodiments of the present invention, the activated coke has an iodine value of 400-800, an intensity of > 90% and a specific surface area of 400-800 m ² /g。

In some embodiments of the invention, in step D, the water temperature is maintained between 18 and 42 ℃, preferably between 28 and 35 ℃.

In the present invention, the COD of the target raw water is 40 to 3858mg/L, and in particular, the COD of the target raw water is 200 to 3858mg/L.

In some embodiments of the invention, the target raw water comprises one or more of regulating tank effluent, primary sedimentation tank effluent, secondary sedimentation tank effluent, high-density tank effluent, MBR membrane effluent, RO membrane concentrate and cooling tower circulating sewage for treating industrial wastewater; the industrial wastewater comprises one or more of textile dyeing and finishing wastewater, petrochemical wastewater, fine chemical wastewater, coal chemical wastewater, heat energy engineering wastewater, papermaking wastewater, medical wastewater, fermentation wastewater, food wastewater and municipal wastewater.

The beneficial effects of the invention are as follows:

the method for regenerating the active carbon adsorption carrier on line by the biological method can retain raw water, and on the basis of not filtering raw bacteria, the method for starting symbionts formed by compact and rich flora and secretion thereof is formed on the active carbon adsorption carrier by putting the composite functional microbial inoculum into an active carbon filter tank, so that the technology for regenerating the active carbon adsorption carrier on line by the biological method is realized, the removal effect of target pollutants (organic matters, nitrogen and the like) is not reduced, the process is simplified, and the engineering operation and labor cost are greatly reduced.

Drawings

The invention will be further elucidated with reference to the drawings.

FIG. 1 is a schematic diagram of a filter tank used in the study of the present invention.

Fig. 2 shows COD content variation during activated carbon adsorption saturation.

Figure 3 shows the COD content monitoring result of the inlet and outlet water of the No. I activated carbon filter.

FIG. 4 shows the COD content monitoring result (inflow COD 200-500 mg/L) of the inlet and outlet of the activated carbon filter No. II.

FIG. 5 shows the results of monitoring the COD content of the inlet and outlet of the No. II activated carbon filter (inflow COD 1996-2241 mg/L).

FIG. 6 shows the COD content monitoring result of the inlet and outlet of the activated carbon filter No. II (inflow COD 2655-3858 mg/L).

And 7, the COD content monitoring result of the inlet and outlet of the active coke filter tank II is shown.

FIG. 8 shows the results of monitoring the ammonia nitrogen content at the inlet and outlet of the activated carbon filter of the number II (13-29 mg/L of inlet ammonia nitrogen).

FIG. 9 shows the results of monitoring the ammonia nitrogen content of the inlet and outlet of the activated carbon filter of the II type (82-96 mg/L of inlet ammonia nitrogen).

FIG. 10 is a scanning electron microscope image of activated carbon before use.

FIG. 11 is a scanning electron microscope image of the activated carbon of the No. I filter.

FIG. 12 is a scanning electron microscope image of the activated carbon of the filter No. II.

Fig. 13 shows the trend of change in the adsorption of raw water COD, TN (total nitrogen) by activated carbon.

FIG. 14-1 shows the results of monitoring COD content of inlet and outlet water of the No. I filter.

FIG. 14-2 shows the result of monitoring TN content of inlet and outlet water of the No. I filter.

FIG. 15-1 shows the result of monitoring the COD content of inlet and outlet water of the No. II filter.

FIG. 15-2 shows the monitoring result of TN content of inlet water and outlet water of the No. II filter.

FIG. 16 shows the monitoring result of total nitrogen content of the inlet and outlet of the activated carbon filter No. II (total nitrogen in inlet water is 26-200 mg/L).

Preservation of bacterial species

The ceramic (Thauera sp.) is separated and identified by Xuqing and is preserved in China general microbiological culture Collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21641. The strain is named as a ceramic strain WQ2021001 (Thauera sp. Strain WQ 2021001) in the invention.

Xin Fangfang red bacillus (Rhodobacter Xinfangfangia), separated and identified by Xuqing, has been preserved in China general microbiological culture Collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21642. The strain is named as Xin Fangfang rhodobacter WQ2021002 strain (Rhodobacter Xinfangfangia strain WQ 2021002) in the invention.

Halomonas sp. Xuqing isolated and identified, which has been preserved in China general microbiological culture Collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21643. The strain is named as a Halomonas WQ2021003 strain (Halomonas sp.strain WQ 2021003) in the invention.

Sphingomonas sp. Xuqing, isolated and identified, has been preserved in China general microbiological culture Collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21644. The strain is named as Sphingomonas strain WQ2021004 (Sphingomonas sp. Strain WQ 2021004) in the invention.

Acinetobacter sp., separated and identified by Xuqing, and preserved in China general microbiological culture Collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21645. The strain was designated as Acinetobacter WQ2021005 strain (Acinetobacter sp. Strain WQ 2021005) in the present invention.

The germ bacillus (Gemmobacter sp.) is separated and identified by Xuqing and is preserved in China general microbiological culture Collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21646. The strain of the present invention was designated as the strain of Agrobacterium WQ2021006 (Gemmobacter sp.strain WQ 2021006).

Brevibacterium sp.) isolated and identified by Xuqing and deposited in China general microbiological culture Collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21647. The strain of the present invention was designated as Brevibacterium WQ2021007 strain (Brevibacterium sp.strain WQ 2021007).

Clostridium butyricum (Clostridium butyricum) separated and identified by Xuqing and is already in China general microbiological culture collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21648. The strain was designated as Clostridium butyricum WQ2021009 strain (Clostridium butyricum strain WQ 2021009) in the present invention.

Acetylmicrobacterium (Exiguobacterium acetylicum), separated and identified by Xuqing, has been in China general microbiological culture Collection center (CGMCC); address: the institute of microbiology, national academy of sciences, no. 3, north chen west way 1, region of korea, beijing city), date of preservation: 2021, 01 month 18, deposit number: CGMCC No.21649. The strain was named Acetobacter WQ2021010 strain (Exiguobacterium acetylicum strain WQ 2021010) in the present invention.

Detailed Description

In order that the invention may be readily understood, a detailed description of the invention will be provided below with reference to examples. Before the present invention is described in detail, it is to be understood that this invention is not limited to particular embodiments described. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting.

Unless defined otherwise, all terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention pertains. Although any methods and materials similar or equivalent to those described herein can also be used in the practice or testing of the present invention, the preferred methods and materials are now described.

I, terminology

The term "dischargeable water" as used herein refers to water that can be discharged or utilized in accordance with the integrated wastewater discharge standard or in accordance with laws or regulations.

The term "hydraulic retention time" as used herein refers to the average retention time (HRT) of the wastewater to be treated in the reactor, i.e. the average reaction time of the wastewater with microorganisms in the bioreactor.

The term "optionally" as used herein means that the ingredients are optionally added, either with or without addition.

The terms "about," "substantially," and "primarily" as used herein in connection with a range of an element, concentration, temperature, or other physical or chemical property or characteristic, cover a variation that may exist in the upper and/or lower limit of the range of the property or characteristic, including, for example, variations caused by rounding off, measurement methods, or other statistical variation. For example, as described herein, a numerical value associated with an amount, weight, etc., is defined as "about" being all values of each particular value plus or minus 1%. For example, the term "about 10%" should be interpreted as "9% to 11%".

II, embodiment

Aiming at the online regeneration problem of the activated carbon with saturated adsorption in the engineering application field, the activated carbon is always used as a pain point, the durability of the activated carbon cannot be improved in a delayed way, the operation and maintenance cost is improved, the external means are utilized for desorbing the organic matters of the activated carbon, certain influence is necessarily caused on the living environment of microorganisms, and even the sterilization result is generated, so that the degradation capability of the whole filter tank to water quality pollutants is greatly reduced. The optimal solution of online regeneration is to rely on the technology itself, so that the activated carbon with saturated adsorption can degrade the adsorbed organic matters through the microorganisms attached in the pores of the activated carbon without any additional technology, thereby improving the durability of the activated carbon and being capable of being used for a long time. In the process, any complicated technical operation is not needed, and the activated carbon is stably attached in the pores of the activated carbon by the addition mode of the functional microbial inoculum to form a symbiont formed by compact and rich flora and secretion thereof which adapt to the raw water environment, so that the activated carbon can be degraded and desorbed continuously by the functional microbial inoculum while adsorbing target pollutants (organic matters, nitrogen and the like), thereby keeping constant adsorption capacity. Meanwhile, in the operation process, the raw water flora and the added functional flora do not need to be considered to form a competition effect to sterilize the raw water flora, the functional flora and the living environment are not damaged, and the degradation performance of the functional strain can be kept in a good stable state. Therefore, considering the practical application value of engineering, the invention not only can keep the operation and maintenance cost reduced and is easy to operate, but also is completely suitable for the application background of the activated carbon adsorption carrier filter in most different water quality environments.

The invention relates to a method for regenerating active carbon adsorption carrier on line by biological method, which adopts a starting method of putting composite functional bacteria into an active carbon filter tank and forming symbiotes formed by compact and rich bacterial groups and secretion thereof on the active carbon adsorption carrier to realize the regeneration of the active carbon adsorption carrier on line by biological method, thereby improving the durability of the active carbon adsorption carrier, playing a good role in promoting the degradation of organic pollutants in effluent, simplifying the process and greatly reducing the engineering operation and labor cost while ensuring that the removal effect of target pollutants is not reduced.

The invention relates to a regenerated active carbon adsorption carrier, which is used for reproducing or recovering and even further improving the adsorption performance of the active carbon adsorption carrier.

The method specifically comprises the following steps:

and S2, directly introducing target raw water into the filter tank at full load to degrade target pollutants to obtain the dischargeable water.

The step S1 specifically includes:

step C, adding the mixed solution of the composite functional microbial inoculum and the target raw water into a filter tank containing the activated carbon adsorption carrier, uniformly distributing the mixed solution on the activated carbon adsorption carrier, adding the target raw water into the filter tank, and rising the water level until the activated carbon adsorption carrier is just immersed, so as to obtain a composite functional microbial inoculum-activated carbon adsorption carrier-target raw water mixture;

and E, repeating the steps B-D for more than 2 times, preferably 2-3 times, so that the compound functional flora adapting to the raw water environment is stably attached to the activated carbon adsorption carrier, and a symbiont formed by compact and rich flora and secretion thereof is formed, thus obtaining the activated carbon adsorption carrier with the stably attached compound functional flora adapting to the raw water environment.

The method of the invention is characterized in that:

the composite functional microbial agent is formed by combining bacteria of different microbial populations capable of degrading target pollutants in target raw water. The source of the bacteria constituting the composite functional microbial agent in the present invention is not particularly limited as long as it is a bacteria capable of degrading a target contaminant in a target raw water, and it can be obtained by screening or commercially available; preferably, the composite functional microbial agent comprises bacteria capable of degrading target pollutants in target raw water, it includes at least two species of bacteria of the genus Eimeria (Thermococcus), rhodobacter (Rhodobacillus), halomonas (Halomonas), sphingomonas (Sphingomonas), acinetobacter (Acinetobacter), agrimonia (Gemmobacter), brevibacterium (Brevibacterium), rhodococcus (Rhodococcus), micrococcus (Micrococcus), luo Saihe Microbacterium (Rhodanobacter), oligotrophic monas (Stenotrophomonas), mycobacterium (Mycobacterium), pediococcus (Pediococcus), bacillus (Bacillus), achromobacter (Achromobacter), clostridium (Clostridium), microbacterium (Exiguobacterium), pseudomonas (Pseudomonas) and Comamonas (Comamonas); among them, bacteria of the genus Eimeria (Thauera), the genus Rhodobacillus (Rhodobacillus), the genus Salmonella (Halomonas), the genus Sphingomonas (Sphingomonas), the genus Acinetobacter (Acinetobacter), the genus Agrimonia (Gemmobacter), the genus Brevibacterium (Brevibacterium), the genus Rhodococcus (Rhodococcus), the genus Micrococcus (Micrococcus), the genus Luo Saihe of Microbacterium (Rhodanobacter), the genus oligotrophic monas (Stenotrophomonas), the genus Mycobacterium (Mycobacterium), the genus Pediococcus (Pediococcus), the genus Bacillus (Bacillus), the genus Achromobacter (Achromobacter) can be used for aerobic culture; while Clostridium (Clostridium), microbacterium (Exiguobacterium), aeromonas (Aeromonas), pseudomonas (Pseudomonas) and Comamonas (Comamonas) can be used for the anoxic culture.

In the invention, the composite functional microbial inoculum is prepared in the form of seed liquid. The method for preparing the seed liquid in the present invention is not particularly limited, and can be prepared by a method conventional in the art.

The nutrient solution is a solution for providing rapid propagation and growth of microorganisms and mainly consists of three elements of carbon, nitrogen and phosphorus, wherein the nutrient solution comprises conventional glucose, urea and potassium dihydrogen phosphate, and the glucose, the urea and the potassium dihydrogen phosphate are added according to the proportion of C:N:P=100:5:1.

The active carbon adsorption carrier disclosed by the invention is a porous adsorption carrier with developed pore structure and stronger adsorptivity, and mainly comprises active carbon and/or active coke.

The activated carbon is granular activated carbon made of coal; preferably, the iodine value of the activated carbon is 600-1100, the intensity is more than 90 percent, and the specific surface area is 500-1200 m ² /g。

The active coke has an iodine value of 400-800, a strength of more than 90% and a specific surface area of 400-800 m ² /g。

The range of the target raw water is wider, the COD is 40-3858 mg/L, and particularly, the COD is 200-3858 mg/L, which is applicable to the invention; the target raw water comprises one or more of regulating tank effluent, primary sedimentation tank effluent, secondary sedimentation tank effluent, high-density tank effluent, MBR (membrane bioreactor) membrane effluent, RO membrane concentrate and cooling tower circulating sewage for treating industrial wastewater; the industrial wastewater comprises one or more of textile dyeing and finishing wastewater, petrochemical wastewater, fine chemical wastewater, coal chemical wastewater, heat energy engineering wastewater, papermaking wastewater, medical wastewater, fermentation wastewater, food wastewater and municipal wastewater.

In the mixed solution of the composite functional microbial inoculum and the target raw water, the mass ratio of the composite functional microbial inoculum to the carbon source in the nutrient solution is (1-100) to 1, preferably (1-10) to 1, and more preferably 1 to 1; the ratio of the total mass of the water to the total mass of the composite functional microbial inoculum and the nutrient solution is (1-1000) to 1, preferably (1-100) to 1, more preferably (1-10) to 1, and even more preferably 10 to 1.

In the step C, the composite functional microbial inoculum and the nutrient solution in the step B are mixed with the target raw water, then are uniformly added into the activated carbon filter tank, and are uniformly distributed on the activated carbon adsorption carrier in the filter tank. In the operation process, it is generally recommended to wash the activated carbon adsorption carrier in the filter tank in advance to wash away impurities such as floating carbon and ash, and keep the activated carbon adsorption carrier in a wet state, and the composite functional microbial agent-target raw water mixed solution is added into the filter tank containing the activated carbon adsorption carrier, so that better adhesion and growth of microorganisms are facilitated; and then the raw water is sent into a filter tank by a pump, and the water level is raised by the pump pressure until all the activated carbon adsorption carriers are immersed, so that the preparation for culture is made.

In the present invention, the mode of feeding the target raw water into the filter tank by the pump is not particularly limited, and a conventional pumping and water feeding mode can be adopted, for example, the target raw water can be fed into the filter tank from the bottom of the filter tank by the pump, or the target raw water can be fed into the filter tank from the upper part of the filter tank by the pump, and no special influence on the subsequent acclimatization of the composite functional microbial agent-activated carbon adsorption carrier-target raw water mixture by the pump is observed.

In the present invention, the "uniform adding" manner of "uniformly adding the composite functional microbial inoculum, nutrient solution and target raw water in the step B" after mixing them into the activated carbon filter tank and uniformly distributing them on the activated carbon adsorption carrier in the filter tank "is not particularly limited, as long as the composite functional microbial inoculum, nutrient solution and target raw water in the step B can be prepared and the mixed solution of them in the filter tank is" uniformly distributed "on the activated carbon adsorption carrier in the filter tank, for example, a uniform spraying manner may be adopted.

In the step D, the target pollutant in the target raw water determines whether the activated carbon filter is an aerobic filter or an anoxic filter, that is, the target pollutant in the target raw water determines whether the composite functional microbial agent-activated carbon adsorption carrier-target raw water mixture is subjected to aerobic culture or anoxic culture in the step D.

For example, when the target pollutants in the target raw water are organic matters and ammonia nitrogen, particularly when the ammonia nitrogen content in the target raw water is 5-100 mg/L, particularly when the ammonia nitrogen content is 13-96 mg/L, the activated carbon filter is an aerobic filter; in the step B, uniformly mixing the composite functional microbial inoculum, the nutrient solution and the target raw water, and aerating to obtain a composite functional microbial inoculum-target raw water mixed solution; and in the step D, air is conveyed to the bottom of the filter tank for stuffy aeration, and the target raw water containing the composite functional microbial inoculum and the activated carbon adsorption carrier is subjected to aerobic culture.

For another example, when the target pollutant in the target raw water is total nitrogen, particularly when the total nitrogen in the target raw water is in the range of 26-200 mg/L, the activated carbon filter is an anoxic filter; in the step D, the target raw water containing the composite functional microbial inoculum and the activated carbon adsorption carrier is subjected to anoxic culture without being subjected to stuffy aeration and standing.

And (3) performing stuffy aeration or static culture at the bottom of the filter tank by using an air pump, and evacuating liquid in the filter tank after the stuffy aeration lasting for 5-9 days or the static culture lasting for 3-5 days, so as to provide an adhesion living environment for the added strains. However, special care should be taken to maintain the water temperature between 18 and 42℃during aeration or still culture.

In the step E, in order to continuously increase the strain amount adapting to the raw water environment in a short time, the operations of the step B, the step C and the step D are repeated, and the steps are repeatedly circulated for 2 to 3 times to domesticate, so that the composite functional bacteria adapting to the raw water environment can be stably attached to the activated carbon adsorption carrier, and a symbiont formed by compact and rich bacterial groups and secretion thereof is formed, and at the moment, the target raw water can be directly introduced to degrade target pollutants.

The method is also characterized in that additional pretreatment of raw water, such as sterilization treatment of indigenous bacteria in the raw water, is not needed; in addition, the method of the invention can select aerobic or anaerobic conditions according to the target pollutants of raw water.

The activated carbon filter tank is a filter tank containing activated carbon adsorption carriers, is not particularly limited in the invention, and can be conventional or existing in the art as long as the activated carbon filter tank can realize on-line regeneration of the activated carbon adsorption carriers by a biological method and further degrade target pollutants.

The form of the liquid flow of the activated carbon filter is not particularly limited in the present invention, and either an up-flow type or a down-flow type may be adopted, for example, both up-flow type and down-flow type filters may be suitably used in the method of the present invention.

For example, in some examples, an activated carbon filter as shown in FIG. 1, which is the filter used in the research of the present invention, may be used, but is not limited to, and other types or configurations of activated carbon filters may be used.

The activated carbon filter tank shown in fig. 1 comprises a reaction column, a base and an aeration disc 8, wherein the reaction column and the base are sequentially arranged from top to bottom, and the aeration disc 8 is arranged between the reaction column and the base and connects the reaction column and the base; wherein the aeration disc 8 is an air distribution simulation device, and air holes are uniformly distributed on the surface of the aeration disc; the reaction column mainly comprises a column body 9 and an activated carbon adsorption carrier filled in the column body; the base mainly comprises a base matrix, and a water inlet port 5 and an air inlet 6 which are arranged on the base matrix, wherein one end of the water inlet port 5 is connected with a raw water pump 4, and the other end of the water inlet port is connected with the water inlet port 5 at the bottom of a column body 9 through a pipeline and is used for feeding target raw water into a reaction column (i.e. a filter tank); one end of the air inlet 6 is connected with an aeration pump 7, and the other end is connected with an aeration distributor in an aeration disc 8 for realizing aeration of the filter tank.

It will be appreciated by those skilled in the art that the aeration disc 8 serves to disperse and break up bubbles in practical engineering applications for gas distribution devices (including, but not limited to, perforated aeration pipes, gas distribution filter heads, gas distribution filter bricks, etc.) and graded gravel; the aeration disc 8 in the invention can be made of an air distribution device in practical engineering application, a resin plate or a plastic plate distributed with through air holes in laboratory experiments, and the like.

It should be noted that, the activated carbon filter tank shown in fig. 1 is mainly suitable for on-line regeneration of activated carbon adsorption carriers by an aerobic culture biological method, and for convenience of test and comparison, the test and research of on-line regeneration of activated carbon adsorption carriers by an anoxic culture biological method in the invention also adopts the activated carbon filter tank shown in fig. 1, and only in the anoxic culture process, the aeration device or the component is closed, and only stationary culture is needed.

In some specific embodiments of the present invention, the activated carbon filter shown in fig. 1 is used for on-line regeneration of activated carbon adsorption carriers by an aerobic culture biological method, which comprises:

1. in the filter tank, the composite functional microbial inoculum, the activated carbon adsorption carrier and the target raw water are mixed and cultivated, and domesticated to obtain the activated carbon adsorption carrier with stable attachment and the composite functional microbial community which is suitable for the raw water environment;

(1) Mixing the composite functional microbial inoculum and the nutrient solution, fully mixing the mixed solution with raw water in a water bucket 1, and aerating for 10-30 min to obtain a composite functional microbial inoculum-target raw water mixed solution;

(2) The mixed solution of the composite functional microbial inoculum and the target raw water is conveyed into the water inlet 5 through the pump 3, enters the column 9 through the water inlet at the bottom of the column 9, and can be continuously added into the target raw water cleaning bucket 1 and the cleaning water is also conveyed to the water inlet 5 if needed, meanwhile, raw water is injected from the raw water bucket 2, enters the column 9 through the water inlet 5 through the pump 4, and the liquid level in the column 9 reaches the surface of the activated carbon adsorption carrier in the completely immersed column 9. When the mixed solution fully wets the surface of the activated carbon adsorption carrier in the column 9, a composite functional microbial inoculum-activated carbon adsorption carrier-target raw water mixture is obtained;

(3) The reaction filter is an aerobic filter, and air is introduced into an aeration disc 8 for aeration through an air inlet 6 by using an aeration pump; the stuffy exposure is maintained for 5 to 9 days, and an environment for attaching survival is provided for the added strains.

After 5-9 days of stuffy exposure, the connecting pipe between the water inlet 5 and the raw water pump is disconnected, and the liquid in the filter tank is emptied from the water inlet 5.

(4) Repeating the operations of the steps (1) to (3), mixing functional bacterial liquid and nutrient solution, externally adding raw water, fully mixing, conveying the mixture to the surface of an activated carbon adsorption carrier, injecting the raw water into a reaction column, continuously evacuating the liquid until the time condition is reached, and recycling for 2-3 times for domestication.

Therefore, the externally-thrown composite functional microbial inoculum can be stably attached to the activated carbon adsorption carrier, and a compact and rich flora which is suitable for the raw water environment and a symbiont formed by secretion thereof are formed and embedded into rich pores of the activated carbon adsorption carrier. After a plurality of days, the activated carbon adsorption carrier with stably attached composite functional bacteria group adapting to the raw water environment is obtained.

2. Introducing target raw water into the filter tank to degrade target pollutants to obtain dischargeable water

Raw water is directly introduced from the raw water tank 2 to the reaction filter tank 9 to the liquid level which is level with the water outlet 10, the activated carbon filter tank also starts to put into production, pollutants in the raw water are degraded, and the degraded water can be discharged into the drainage tank 11 from the water outlet 10. In the whole degradation process, the activated carbon adsorption carrier degrades the adsorbed organic matters through the adsorption effect on the organic pollutants, and the microorganisms filled in the pores of the activated carbon adsorption carrier and the formed compact and rich flora and the symbiotic substance formed by the secretion of the compact and rich flora. The process realizes the process that the activated carbon adsorption carrier adsorbs the organic matters and is degraded by microorganisms to be desorbed, thereby further realizing the purpose of on-line regeneration of the activated carbon adsorption carrier, namely improving the durability of the activated carbon adsorption carrier.

When the activated carbon adsorption carrier is regenerated on line by an aerobic culture biological method, the composite functional microbial inoculum comprises at least two of bacteria of the genus terrestris (Thauera), rhodobacter (Rhodobacillus), halomonas (Halomonas), sphingomonas (Sphingomonas), acinetobacter (Acinetobacter), gemmobacter (Gemmobacter) and Brevibacterium (Brevibacterium). This is understood to mean that the complex functional bacterial agent is a dominant bacterial population consisting of two or more bacteria of the above-mentioned different genus.

The inventor researches and discovers that the composite functional microbial inoculum also optionally contains at least one of Rhodococcus (Rhodococcus), micrococcus (Micrococcus) and other bacteria in germ (Gemmobacter), and has better synergism on the online regenerated active carbon adsorption carrier for the aerobic culture of the composite functional microbial inoculum.

As used herein, "other bacteria in the genus Agrimonia (Gemmobacter)" refers to bacteria in the genus Agrimonia (Gemmobacter) other than the strain of Agrimonia WQ 2021006. It is understood that the bacteria of the genus Bacillus (Gemmobacter) constituting the composite functional microbial agent of the present invention are mainly the strain of Bacillus strain WQ2021006 having the preservation number of CGMCC No.21646, and in addition, the composite functional microbial agent may contain other bacteria of the genus Bacillus (Gemmobacter) which have a good synergistic effect on the composite functional microbial agent aerobic culture on-line regenerated activated carbon-based adsorbent carrier alone or together with at least one of the other bacteria of the genus Rhodococcus (Rhodococcus) and Micrococcus (Micrococcus).

For example, in some specific preferred embodiments of the present invention, the compound functional microbial inoculum mainly comprises a ceramic strain WQ2021001 (referred to as ceramic) with a collection number of CGMCC No.21641, a rhodobacter Xin Fangfang strain WQ2021002 (referred to as red bacillus Xin Fangfang) with a collection number of CGMCC No.21642, a halomonas strain WQ2021003 (referred to as halomonas) with a collection number of CGMCC No.21643, a sphingomonas strain WQ2021004 (referred to as sphingomonas) with a collection number of CGMCC No.21644, an Acinetobacter strain WQ2021005 (referred to as Acinetobacter) with a collection number of CGMCC No.21645, a germ strain WQ2021006 (referred to as germ) with a collection number of CGMCC No.21646, and a Brevibacterium strain WQ2021007 (referred to as Brevibacterium) with a collection number of CGMCC No. 21647; preferably, the composite functional microbial inoculum also comprises micrococcus flavus (Micrococcus flavus) with the preservation number of CGMCC1.5361, rhodococcus baileyi (Rhodococcus baikonurensis) with the preservation number of CGMCC1.10292 and budesoteria silt (Gemmobacter caeni) with the preservation number of CGMCC 1.7745.

In addition, it has been found that the composite functional microbial agent of the present invention optionally contains at least one of bacteria of the genus Luo Saihe (rhodobacter), the genus Stenotrophomonas (stenotomonas), the genus Mycobacterium (Mycobacterium), the genus Pediococcus (Pediococcus), the genus Bacillus (Bacillus) and the genus Achromobacter (Achromobacter), and has a synergistic effect on the on-line regeneration of an activated carbon-based adsorbent carrier for aerobic culture of the composite functional microbial agent.

For example, in some examples, the complex functional bacterial agent consists of the above-described Dow, xin Fangfang Red bacillus, salmonella, sphingomonas, acinetobacter, bacillus, brevibacterium, micrococcus flavus, bayer Luo Ergong coccus and Agrimonia, wherein, dow, xin Fangfang Red bacillus, salmonella, sphingomonas, acinetobacter, bacillus, brevibacterium, micrococcus flavus (L.) C the quantity ratio of the Barconpost Luo Ergong cocci to the silt buddleja is (1-2) to (0.5-1), the number ratio of the Barconcus baileyi Luo Ergong to the silt budding bacillus is (1-2) to (1-2) (1-2) 1-2 (0.5-1) 0.5-1 (0.5-1).

In other specific embodiments of the present invention, an activated carbon filter tank shown in fig. 1 is used for on-line regeneration of activated carbon type adsorption carriers by anoxic cultivation biological method, comprising:

(1) Mixing the composite functional microbial inoculum and the nutrient solution, and then fully and uniformly mixing the mixed solution with raw water in a water bucket 1 to obtain a composite functional microbial inoculum-target raw water mixed solution;

(3) Closing the aeration pump 7, closing the air inlet 6, wherein the reaction filter is an anoxic filter at the moment, and performing stationary culture; standing for 3-5 days to provide an environment for the added strains to adhere to living.

After 3-5 days of static culture, the connecting pipe between the water inlet 5 and the raw water pump is disconnected, and the liquid in the filter tank is emptied from the water inlet 5.

Therefore, the externally-thrown composite functional microbial inoculum can be stably attached to the surface of the activated carbon adsorption carrier, and a compact and rich flora which is suitable for the raw water environment and a symbiont formed by secretion thereof are formed and embedded into rich pores of the activated carbon adsorption carrier. After a plurality of days, the activated carbon adsorption carrier with stably attached composite functional bacteria group adapting to the raw water environment is obtained.

When the activated carbon adsorption carrier is regenerated on line by an anoxic cultivation biological method, the composite functional microbial inoculum comprises at least two of Clostridium (Clostridium) and bacillus pumilus (Exiguobacterium); this is understood to mean that the complex functional bacterial agent is a dominant bacterial population consisting of two or more bacteria of the above-mentioned different genus.

The inventor researches and discovers that when the composite functional microbial inoculum also contains at least one of Aeromonas (Aeromonas), pseudomonas (Pseudomonas) and Comamonas (Comamonas), the composite functional microbial inoculum has better synergism on the online regenerated active carbon adsorption carrier for the anoxic cultivation of the composite functional microbial inoculum.

In some preferred embodiments of the present invention, the composite functional microbial inoculum comprises clostridium butyricum WQ2021009 strain with a preservation number of CGMCC No.21648 and a micro-bacillus aceti WQ2021010 strain with a preservation number of CGMCC No. 21649; preferably, the composite functional microbial inoculum further comprises source aeromonas (Aeromonas aquariorum) with a preservation number of CGMCC No.1.9061, pseudomonas stutzeri (Pseudomonas stutzeri) with a preservation number of CGMCC1.15316 and comamonas aquatica (Comamonas aquatica) with a preservation number of CGMCC 1.8059.

For example, in some examples, the complex functional bacterial agent consists of clostridium butyricum, bacillus acetimus, aeromonas origin, pseudomonas stutzeri and comamonas aquatica, wherein the ratio of clostridium butyricum, bacillus acetimus, aeromonas origin, pseudomonas stutzeri and comamonas aquatica is (1-2) to (0.5-1), preferably (1-1.5) to (0.7-1), more preferably 1:1:0.7:0.7:0.7.

The method of the invention is that under the support of microorganism screening technology, the composite functional microbial inoculum is fully put into raw water to be degraded and fully mixed, then is poured into a filter tank filled with active carbon adsorption carriers for infiltration, stuffy exposure or standing and acclimation, and then is put into normal work, so that microorganisms are attached to the active carbon adsorption carriers and form symbionts formed by compact and rich bacterial groups and secretion thereof, target pollutants (organic matters, nitrogen and the like) adsorbed by the active carbon adsorption carriers are degraded for a long time, the adsorption efficiency of the active carbon adsorption carriers is ensured, and a more convenient solution is provided for online regeneration of the active carbon adsorption carriers by a biological method.

III, detection method

1. COD test experiment

The required instruments mainly comprise: digestion reactor (DRB 200, HACH), ultraviolet visible spectrophotometer (DR 3900, HACH).

The operation steps mainly comprise:

1. configuration analysis water sample

(1) Taking a COD prefabricated tube reagent bottle (the COD detection range is 30-1500 mg/L);

(2) Selecting a first sample as a blank, transferring 2ml of purified water into a prefabricated tube, screwing a cover and shaking uniformly. The method comprises the steps of carrying out a first treatment on the surface of the

(3) The second sample and a plurality of subsequent test samples are all moved to 2ml of the test sample into the prefabricated tube, and the cap is screwed down and then shaken uniformly. (note: after shaking, the preformed tube burns and scalds as normal.)

2. Digestion

(1) Starting up the DRB200 digestion device, and selecting a COD mode to heat up to 150 ℃;

(2) Opening a safety cover, sequentially putting the prefabricated pipe in the step 1 into the digestion hole, and covering the safety cover;

(3) After opening, carrying out digestion countdown for 120 min;

(4) And after the countdown is finished, the test tube can automatically enter a cooling state, when the temperature is reduced to 120 ℃, the safety cover is opened, and the prefabricated tube reagent is uniformly shaken and then sequentially placed into the test tube rack for standing and cooling to the room temperature.

3. Detection of

(1) Opening the hash DR3900, and starting according to options-all programs-435 program COD HR-;

(2) The first blank sample prefabricated tube is wiped clean and placed in the hole, a light shield is covered, and the first blank sample prefabricated tube is zeroed;

(3) The test samples were tested and recorded sequentially.

2. Ammonia nitrogen test experiment

The required instruments mainly comprise: ultraviolet visible spectrophotometers (DR 3900, HACH).

The operation steps mainly comprise:

1. configuration analysis water sample

(1) Taking a high-range ammonia nitrogen reagent tube (the detection range is 0.4-50 mg/L);

(2) The first sample was selected as blank, 0.1ml ammonia-free water was removed into the preformed tube, and a pack of Ammonia Salicylate reagent powder was added, followed by a pack of Ammonia Cyanurate reagent powder. The cover is covered tightly, and the reagent tube is shaken up and down to dissolve the powder;

(3) The second sample and several subsequent test samples were removed from the sample to be tested by 0.1ml into a preformed tube and then subjected to the same procedure as in (2).

2. Reaction

(1) The DR3900 instrument timer is started. The reaction was timed for 20min.

3. Detection of

(1) After the timing time is over, select NH ₃ -an N HR program;

(2) The blank-valued reagent tube was wiped clean and placed into a 16mm circular adapter. Pressing a Zero key to perform instrument zeroing;

(3) The rest sample tubes are put into an adapter to press a Read key to Read ammonia nitrogen content, and the result is in mg/LNH ₃ -N is a unit.

3. Total nitrogen test experiment

The required instruments mainly comprise: digestion reactor (DRB 200, HACH), uv-vis spectrophotometer (DR 3900, HACH).

The operation steps mainly comprise:

(1) Taking a high-range total nitrogen digestion reagent tube (the detection range is 2-150 mg/L), and adding a package of total nitrogen persulfate reagent powder package;

(2) Taking a reagent tube, adding 0.5ml of matched deionized water (or completely nitrogen-free water instead of the matched deionized water) as a blank, and respectively adding 0.5ml of sample into the rest reagent tubes;

(3) Covering the reagent tube with a cover, and shaking vigorously for at least 30s to mix uniformly;

(4) The DRB200 digestion vessel was opened and heated to 105 ℃. The reagent tube is inserted into the digestion device, covered with a cover, and heated for digestion for 30min. Immediately taking out from the digestion device after the digestion time is over, and putting the digestion device on a reagent tube cooling rack for cooling to room temperature;

(5) The lid of the reagent tube was opened, and a pack of TNA (total nitrogen A) reagent powder was added to each of the reagent tubes. The lid is covered and the reagent vessel 15s is shaken up and down. Starting an instrument timer, and performing timing reaction for 3min;

(6) After the timing time is over, the cover of the reagent tube is opened, and a TNB (total nitrogen B) reagent powder bag is respectively added into the reagent tube. The lid is covered and the reagent vessel 15s is shaken up and down. Starting an instrument timer, and performing timing reaction for 2min;

(7) After the timing time was completed, two TNC (total nitrogen C) reagent tubes were opened, and 2ml of the digestion solution was added to each TNC reagent tube. The lid was closed and the reagent tube was slowly inverted 10 times to mix well. Starting an instrument timer, and performing timing reaction for 5min;

(8) After the timing time has ended, DR3900 is opened and the TN HR program is selected. The blank-valued reagent tube was wiped clean and placed into a 16mm circular adapter. Pressing a Zero key to carry out instrument zeroing;

(9) The reagent tube containing the sample was wiped clean and placed in a 16mm circular adapter and the total nitrogen content was Read by pressing the "Read" key.

4. The method for detecting the biological membrane by SEM,

the required instruments mainly comprise: stereoscopic microscope (Leica, wild M5), critical point dryer (Leica, CPD 300), ion sputter (Leica, ACE 600), scanning electron microscope (Leica, S4800).

The operation steps mainly comprise:

1. reagent configuration

(1) 0.1mol/L phosphate buffer: 2.60g of NaH ₂ PO ₄ ·H ₂ O and 21.70g of NaHPO ₄ ·H ₂ O is dissolved in 500ml of sterile water, and the pH is adjusted to 7.2;

(2) 3% glutaraldehyde fixative: 50ml of 0.2mol/L phosphate buffer and 12ml of 25% glutaraldehyde are placed in a 100ml volumetric flask and mixed uniformly;

(3) 1% osmium acid: 25ml 4% OsO ₄ And 50ml of 0.2mol/L phosphate buffer are placed in a 100ml volumetric flask for constant volume.

2. Sample preparation method

(1) Washing the carrier sample with clear water;

(2) Fixing the sample for 3 hours by 3% glutaraldehyde;

(3) Rinsing with 0.1mol/L phosphate buffer solution for three times, each time for 5min;

(4) Fixing 1% osmium acid fixing solution for 1h;

(5) Rinsing with 0.1mol/L phosphate buffer solution for three times, each time for 5min;

(6) Gradient ethanol dehydration (30% → 50% → 70% → 90% → 100% ethanol 3 times, 10min each);

(7) Replacing with isoamyl acetate three times for 10min each time;

(8) Putting into a carbon dioxide critical point dryer for drying;

(9) And (5) mounting and metal spraying, and observing by an S-4800 field emission scanning electron microscope.

5. Plate counting method

The required instruments mainly comprise: vertical sterilization pot (HIRAYAMA, HRM 242), stirrer (IKA T25), incubator (conventional).

Sample preparation method

(1) Preparing a sterile LB solid culture medium plate and a sterile phosphate buffer solution for later use;

(2) Sampling 0.1-0.3 g of active carbon adsorption carrier from the reactor, and placing the carrier into a sterile centrifuge tube with 5 ml;

(3) Gently wash three times with 5ml sterile phosphate buffer, discard supernatant;

(4) Adding 5ml of sterile phosphate buffer again, and placing in a water bath ultrasonic kettle for ultrasonic treatment for 15min;

(5) 100 μl of the mixture was taken from 10 ^-1 Stepwise dilution to 10 ^-7 ；

(6) Taking 100 mu l of each gradient to prepare a flat plate coating;

(7) The plates were placed in a constant temperature incubator at 30℃for 72h to record colony counts.

Examples

The present invention will be specifically described below by way of specific examples. The experimental methods described below, unless otherwise specified, are all laboratory routine methods. The experimental materials described below, unless otherwise specified, are commercially available.

In the following examples, examples 1 to 6 are on-line regenerated activated carbon adsorption carriers by an aerobic culture biological method, and examples 1 to 3 all use activated carbon as an adsorption carrier; example 4 active coke is used as an adsorption carrier; wherein, the embodiment 1 adopts the effluent of a primary sedimentation tank in certain industrial printing and dyeing wastewater, and the COD is between 200 and 500 mg/L; example 2 adopts the effluent of the regulating tank in the wastewater of coal chemical industry, and the COD is between 1996 and 2241 mg/L; example 3 adopts the effluent of the regulating tank in the wastewater of coal chemical industry, and the COD is between 2655 and 3858 mg/L; example 4 adopts the effluent of a primary sedimentation tank of a certain printing and dyeing wastewater as the inlet water, and the COD range of the inlet water is 211 mg/L-283 mg/L; example 5 an oxidation ditch effluent of a sewage treatment plant with a certain open area is selected as the inlet water, and the ammonia nitrogen content is in the range of 13 mg/L-29 mg/L; example 6 a pharmaceutical wastewater was selected with an ammonia nitrogen content ranging from 82mg/L to 96mg/L.

The composite functional microbial inoculum is prepared in the form of seed liquid, and the seed liquid is prepared by a method conventional in the art.

When the active carbon adsorption carrier is regenerated on line by an aerobic culture biological method, the composite functional microbial inoculum consists of the following strains:

the storage number of the ceramic bacillus WQ2021001 strain is CGMCC No.21641;

Xin Fangfang rhodobacter WQ2021002 strain with preservation number of CGMCC No.21642;

the halomonas WQ2021003 strain has a preservation number of CGMCC No.21643;

sphingomonas WQ2021004 strain with a preservation number of CGMCC No.21644;

acinetobacter WQ2021005 strain with preservation number of CGMCC No.21645;

the preservation number of the germ bacillus WQ2021006 strain is CGMCC No.21646;

brevibacterium WQ2021007 strain with preservation number of CGMCC No.21647;

rhodococcus beidella (Rhodococcus baikonurensis) with the preservation number of CGMCC1.10292 (China general microbiological culture Collection center);

the collection number of the sludge germ bacillus (Gemmobacter caeni) is CGMCC1.7745 (China general microbiological culture Collection center);

micrococcus flavus (Micrococcus flavus) with a preservation number of CGMCC1.5361 (China general microbiological culture Collection center).

The composite functional microbial inoculum is prepared from seed liquid of ceramic-type bacteria, xin Fangfang red bacillus, halomonas, sphingomonas, acinetobacter, germ and short bacillus according to the volume ratio of ceramic-type bacteria, xin Fangfang red bacillus, halomonas, acinetobacter, germ, short bacillus, yellow micrococcus, rhodococcus bailii, germ of 1:1:1:1:1:1:0.7:0.7:0.7.

Examples 7-8 are on-line regenerated active carbon adsorption carriers by anoxic cultivation method, wherein active carbon is used as adsorption carrier, MBR produced water of a petrochemical plant is used as water inlet end water (raw water), and total nitrogen content of the water inlet is 26-200 mg/L.

When the activated carbon adsorption carrier is regenerated on line by the anoxic culture biological method, the composite functional microbial inoculum consists of the following strains:

clostridium butyricum WQ2021009 strain with a preservation number of CGMCC No.21648;

the preservation number of the strain of the Acetylmicrobacterium WQ2021010 is CGMCC No.21649;

the preservation number of the source aeromonas (Aeromonas aquariorum) is CGMCC NO.1.9061 (China general microbiological culture Collection center);

pseudomonas stutzeri (Pseudomonas stutzeri) with a preservation number of CGMCC1.15316 (China general microbiological culture Collection center);

comamonas aquatica (Comamonas aquatica) with a preservation number of CGMCC1.8059 (China Committee for culture Collection of microorganisms).

The composite functional bacterial agent is prepared from seed liquid of clostridium butyricum, acetominium bacillus, aeromonas, pseudomonas and comamonas according to the volume ratio of clostridium butyricum, acetominium bacillus, source aeromonas, pseudomonas stutzeri and comamonas aquatica = 1:1:0.7:0.7:0.7.

Example 1: on-line regenerated active carbon adsorption carrier by aerobic culture biological method

1. Test

(1) Two activated carbon filters with the same conditions are arranged, and the serial numbers are number I and number II respectively;

the structures of the two activated carbon filters are shown in the figure 1, the sizes of the reaction columns of the two filters are kept consistent, the same type of activated carbon is adopted, the particle sizes of the activated carbon and the number of the reaction columns are kept consistent, and the hydraulic retention time is 2 hours.

(2) Adding activated carbon saturated by adsorption into a No. I filter tank, and then adding a functional microbial inoculum to carry out aeration and degradation on raw water;

the adsorption performance of the activated carbon was tested by a beaker test. 5g/L of active carbon was selected and adsorption experiments were performed with three different COD concentrations of influent water. Sampling the effluent every 5min, measuring the COD value of the effluent, and judging whether the adsorptivity of the activated carbon is saturated or not according to the change of the COD value.

After the adsorption saturation is determined, adding activated carbon with the adsorption saturation into the No. I filter tank, adding a microbial inoculum according to the method, introducing raw water, aerating, adsorbing, sampling every 15min for COD detection, determining the adsorption saturation when the COD change is not obvious, evacuating liquid in the filter tank, immersing the activated carbon in a solution obtained by mixing functional bacterial liquid with target raw water, and carrying out aeration culture, and then, continuing to carry out raw water introduction test.

(3) According to the technical scheme of the invention, the composite functional bacterial liquid is added into the active carbon filter tank II;

the filter tank shown in figure 1 and the aerobic culture operation flow and steps are adopted, and after the composite functional bacterial liquid is added into the filter tank II, raw water is introduced for working.

(4) And (3) respectively taking produced water in the two activated carbon filters every day to detect COD, and after the experiment is terminated after 90 days of continuous operation, taking activated carbon particles in the reactor to detect the distribution condition of microorganisms on the activated carbon by means of scanning electron microscopy, strain counting and the like.

Through the reaction of the No. I and No. II filter tanks, water samples are collected and COD is measured every 24 hours continuously for 90 days, the reaction is stopped after 90 days, and the distribution of microorganisms on the activated carbon is detected by means of scanning electron microscopy, strain counting and the like by taking activated carbon particles in the two reactors.

2. Test results

In the step (2), the adsorption performance of the activated carbon is detected through a beaker experiment, and the analysis of the figure 2, which is generated by utilizing the COD value of the water sample test index, finds that the saturation time of the inflow water with low COD concentration is slow, the saturation time of the inflow water with high concentration is fast, when the COD value of the inflow water is 238.5mg/L, the adsorption time is about 70min, the outflow water COD is stable, and the other inflow water concentrations are all earlier than 70min. When the COD of the inflow water is 413.72mg/L, the adsorption time reaches 90min, and the COD content is slightly higher than that of the outflow water at 80min by 5.6%, so that the activated carbon has no adsorption performance after adsorption saturation, and even can desorb organic matters due to supersaturation. Similarly, the reason why the COD of the effluent is slightly higher than 70min at 80min can be deduced when the COD of the effluent is 635.3 mg/L. From this it can be inferred that the activated carbon has reached saturation.

In view of the fact that the COD concentration of the on-site effluent is between 200mg/L and 500mg/L, after activated carbon is adsorbed and saturated by the effluent with the COD concentration of 414mg/L, the effluent is added with bacterial liquid and then put into the site to monitor the COD value of the in-and-out water for 90 days, and the result is shown in figure 3. As can be seen from fig. 3, the activated carbon after saturated adsorption is further added with the composite functional microbial agent, so that the degradation effect on the organic matters of the raw water is not stable enough, because the microorganisms cannot be stably attached to the pores of the activated carbon, but are free in the outer surface of the activated carbon and the raw water environment, and the effective degradation work cannot be performed because of the lack of a stable implantation environment. Therefore, for realizing on-line regeneration of the activated carbon, the problem of adsorption saturation of the activated carbon in industrial application is solved, and the method is very important for the adding scheme of the composite functional microbial inoculum.

According to the method of the invention (i.e. the filter tank shown in fig. 1 and the aerobic culture operation flow and steps thereof), the same operation steps are carried out on site to monitor the COD value of the inlet and outlet water for 90 days, and the results also prove the above-mentioned points (see fig. 4), and the method has very remarkable effect of solving the adsorption saturation problem of the activated carbon on line by utilizing microbial degradation, has stable degradation efficiency and is not changed by the COD value of the inlet water, and fully demonstrates the effectiveness of the method for adding the composite functional microbial inoculum.

Fig. 10 is an electron microscope image of unused raw activated carbon, fig. 11 is an electron microscope image of saturated activated carbon added with a composite microbial inoculum, fig. 12 is an online activated carbon electron microscope image of degradation performed after adding the composite microbial inoculum, and the difference of the distribution of the surface microbial flora of the activated carbon can be clearly seen in the three images. FIG. 10 shows an uneven activated carbon surface with a reduced population of bacteria distributed in the uneven areas; FIG. 11 shows that a small amount of bacterial groups can be observed in comparison with FIG. 10, in which the activated carbon is saturated and the composite functional microbial inoculum is added; FIG. 12 shows that the activated carbon acclimatized by the addition of the composite microbial agent is provided with a large amount of abundant flora covering the pores of the activated carbon and forming symbiota formed by dense and abundant flora and secretion thereof; through visual comparison of an electron microscope, the method for adding the composite functional microbial inoculum provided by the invention can ensure that the composite microbial inoculum suitable for raw water environment is effectively attached to active carbon and degrades target pollutants without loss, so that the active carbon is regenerated on line.

Activated carbon in the No. I reactor and activated carbon in the No. II reactor are sampled respectively, bacterial count detection is carried out by using a plate counting method, and three samples are taken for counting respectively, and the results are shown in Table 1. The results of the three samples show that the number of bacteria on the activated carbon in the reactor I is much lower than the number of bacteria on the activated carbon in the reactor II by 2-3 orders of magnitude. The degradation effect of the saturated activated carbon on COD is not beneficial to the attached growth of microorganisms and the effect of removing COD is poor by combining with the degradation effect of the saturated activated carbon on COD in fig. 3 and 4, and the functional microbial agent adding mode can enable the microorganisms to be effectively attached to the activated carbon and effectively remove the COD.

Table 1 bacterial content on activated carbon in the No. I and No. II reactors

Activated carbon	I-type reactor	No. II reactor
			1	2.0×10 ⁵	2.7×10 ⁸
2	4.0×10 ⁵	2.1×10 ⁸
			3	2.4×10 ⁵	9.5×10 ⁷

Example 2: on-line regenerated active carbon adsorption carrier by aerobic culture biological method

To more specifically illustrate the effectiveness of the biological on-line regeneration adsorption carrier of the invention, a certain coal chemical field water sample is selected, the effluent of a regulating tank of the wastewater is used as the inlet water, and the wastewater is continuously operated on a No. II reactor of the embodiment 1, and the COD of the inlet water and the outlet water of the filter tank is monitored for 48 days, and the result is shown in figure 5. The COD of the inflow water ranges from 1996mg/L to 2241mg/L, and the COD of the outflow water fluctuates from 300mg/L to 600mg/L around the first 20 days, and the trend is stable after 20 days. Occasionally, the COD of the inflow water is too large, so that the degradation of strains is influenced, the fluctuation is caused, and the minimum COD of the outflow water can reach 102mg/L.

Example 3: on-line regenerated active carbon adsorption carrier by aerobic culture biological method

To more specifically explain the effectiveness of the biological on-line regeneration adsorption carrier, a certain coal chemical field water sample is continuously selected, the effluent of the wastewater regulating tank is used as the inlet water, the wastewater regulating tank continuously operates on the No. II reactor of the embodiment 2, and the COD of the inlet water and the outlet water of the filter tank is monitored for 27 days, and the result is shown in figure 6. The COD of the inflow water is 2655 mg/L-3858 mg/L, the fluctuation is larger, but in 27 days of monitoring, the COD of the outflow water is greatly reduced, and the COD of the outflow water is partially fluctuated, but in 15 days of monitoring, the COD of the outflow water gradually shows stable degradation trend.

Example 4: on-line regenerated active carbon adsorption carrier by aerobic culture biological method

In order to illustrate that the biological method on-line regeneration adsorption carrier is not limited to active carbon, and can also comprise other adsorption carriers with developed pore structures and large specific surface areas, in this embodiment, active coke is taken as an example, and parameter summary is made on the active coke adsorption carrier, as shown in the following table 2.

TABLE 2 basic parameters of adsorption Carrier active Coke

Name of the name

Surface of the body

Shape and shape

Diameter/mm

Void ratio

Specific surface area/(cm) ² /g)

Density/(g/cm) ³ )

Active coke

Roughness of

Columnar shape

1～1.5

40～50

500～600

0.5～0.8

And (3) selecting wastewater of a primary sedimentation tank of a certain printing and dyeing mill as a water inlet end, constructing a No. II filter tank, mixing, culturing and domesticating the composite functional microbial inoculum, active coke and target raw water, and then monitoring COD of water inlet and outlet of the filter tank for 40 days.

The other steps are the same as the active carbon, and only the active coke is used as a carrier to replace the active carbon.

After the operation method is completed, COD of the water entering and exiting the filter is monitored for 40 days, and the result is shown in FIG. 7. The COD change of the raw water is larger in the monitoring for 40 days, but the COD of the discharged water is more stable.

Example 5: on-line regenerated active carbon adsorption carrier by aerobic culture biological method

In order to illustrate that the biological method on-line regeneration adsorption carrier has remarkable effect of removing organic matters and obvious effect of removing ammonia nitrogen, a certain oxidation ditch effluent of a sewage treatment plant in a split area is selected as inflow water, a No. II filter is built, and after mixed culture and domestication of a composite functional microbial inoculum, active carbon and target raw water, the ammonia nitrogen of inflow water and outflow water of the filter are monitored for 273 days, and the result is shown in figure 8. The ammonia nitrogen content of the inlet water is 13 mg/L-29 mg/L, and the ammonia nitrogen content of the outlet water is stable and is lower than 1mg/L. This shows that the biological strains through aerobic culture are attached in the pores of the activated carbon and have very good degradation effect on ammonia nitrogen.

Example 6: on-line regenerated active carbon adsorption carrier by aerobic culture biological method

In order to more specifically explain that the biological on-line regeneration adsorption carrier has remarkable effect of removing organic matters and obvious effect of removing ammonia nitrogen, certain pharmaceutical wastewater is selected as water inlet, a No. II filter is built, and ammonia nitrogen in and out of the filter is monitored for 20 days after the composite functional microbial inoculum, the activated carbon and the target raw water are mixed, cultured and acclimatized, and the result is shown in figure 9. The ammonia nitrogen content of the inlet water is 82 mg/L-96 mg/L, and the ammonia nitrogen content of the outlet water is stable and is lower than 7mg/L. This shows that the biological strains through aerobic culture are attached in the pores of the activated carbon and have very good degradation effect on ammonia nitrogen.

Example 7:

the operation method of adding the functional microbial inoculum into the filter tank can realize the online regeneration of the activated carbon by adopting a control test and sampling detection.

1. Beaker experiment

A beaker test was set up to examine the adsorption performance of activated carbon. So as to provide the adsorption saturation data of the activated carbon for the filter tank conveniently. By selecting 5g/L of activated carbon, an adsorption experiment was performed with influent water having a COD concentration of 285.72mg/L, TN of 83.27 mg/L. Sampling the effluent every 5min, measuring the COD and TN values, and judging whether the adsorptivity of the activated carbon is saturated or not according to the change of the COD and TN. As shown in fig. 13.

From fig. 13, it can be seen that the COD of the raw water adsorbed by the activated carbon tends to decrease with time until it is stabilized for about 60min, and even after 80min, the COD tends to increase slightly. The reason for this is that after the adsorption is saturated, the activated carbon has no adsorption performance, and even the self organic matters are desorbed due to supersaturation, so that the activated carbon is verified to reach the saturated state. And the slow descending trend can be seen from the adsorption trend graph of TN, and the descending trend is parallel to stability until about 80 min. In the whole, the adsorption capacity of the activated carbon to the COD of the raw water reaches 34% and the adsorption capacity of the activated carbon to the TN reaches 62.8% in 60 min.

2. Comparison of the effects of the pilot plant

(1) In view of the fact that the COD concentration of the on-site raw water is between 200mg/L and 585mg/L, and the TN concentration is between 26 and 200 mg/L. Two activated carbon filters with the same conditions are arranged, and the number of the activated carbon filters is number I and number II respectively;

the structures of the two activated carbon filters are shown in figure 1, the sizes of the reaction columns of the two filters are kept consistent, the same type of activated carbon is adopted, the particle sizes of the activated carbon and the number of the reaction columns are kept consistent, and the hydraulic retention time is 2 hours.

(2) Adding activated carbon subjected to adsorption saturation in the beaker experiment into a No. I filter tank, introducing raw water, standing for adsorption, sampling every 15min for COD and TN detection, determining adsorption saturation when the variation of the COD and TN is not obvious, evacuating liquid in the filter tank, immersing the activated carbon in the solution mixed with the functional bacterial liquid and the target raw water for standing culture according to the method, and continuing the raw water introduction experiment.

(3) According to the technical scheme of the invention, the active carbon which is not expanded and adsorbed is added into the No. II filter, and the filter and the anoxic culture operation flow are shown in the figure 1, and after the composite functional bacterial liquid is added into the No. II filter, raw water is introduced for working.

(4) Through the reaction of the No. I and No. II filters, water samples are collected and tested for COD and TN every 24 hours continuously for 90 days, and the reaction is stopped after 90 days, as shown in FIG. 14-1 and FIG. 14-2, the COD and TN of the No. I filter are monitored in real time, and the COD and TN of the No. II filter are monitored in real time in FIG. 15-1 and FIG. 15-2.

From the comparison of FIGS. 14-1 and 15-1, the real-time monitoring of the COD of the incoming water was varied but fluctuated between 200 and 500 mg/L. The saturated activated carbon is effective in degrading the inlet water after being added with the composite functional bacterial liquid, but the phenomenon has fluctuation to a certain extent in the whole, so that the phenomenon can be presumed that the microbial attachment to the saturated activated carbon has fewer bacteria, more bacteria are free on the outer surface of the activated carbon or the whole interior of the filter tank, and the place for domesticating and culturing to form the biological film is not single and not firm, so that the degree of degradation has fluctuation. In the view of FIG. 15-1, the degradation operation performed after the activated carbon without adsorption and the functional bacteria liquid are mixed is superior to the activated carbon added after saturation in effect, the COD value of the discharged water basically floats between 100mg/L, and the floating range is small in the whole view. Therefore, it was also verified that the above-mentioned hypothesis that the place where the microorganism adheres to and grows to form the symbiota formed by dense and abundant flora and secretion thereof is single and stable, and the effect on degradation of water is remarkable. In the same way, from the comparison of 14-2 and 15-2, the unsaturated activated carbon is subjected to the addition of the functional microbial inoculum and implantation domestication on the gaps and the surfaces of the unsaturated activated carbon, so that a symbiont formed by compact and rich flora and secretion thereof can be formed on the activated carbon adsorption carrier, the unsaturated activated carbon has a remarkable effect on degrading nitrogenous organic matters, and the unsaturated activated carbon has a degradation amplitude with small fluctuation.

Example 8: on-line regenerated active carbon adsorption carrier by anoxic culture biological method

In order to demonstrate that the on-line regeneration adsorption carrier of the anoxic cultivation method has obvious total nitrogen removal, MBR produced water in a petrochemical plant is adopted as water inlet (raw water), the total nitrogen content range is 26-200 mg/L, a No. II filter tank is built, and after the composite functional microbial inoculum, the activated carbon and the target raw water are mixed, cultivated and acclimatized, the total nitrogen of water inlet and outlet of the filter tank is monitored for 90 days.

After the operation method is completed, the total nitrogen in the water inlet and outlet of the filter is monitored for 90 days, and the result is shown in fig. 16. The total nitrogen content of the inlet water is 26-200 mg/L, the total nitrogen removal effect in the whole outlet water is remarkable, and the removal rate is stabilized at 75% -90%. The total nitrogen of the water outlet has smaller fluctuation on the 28 th day, is influenced by the sudden increase of the total nitrogen content of the water inlet, but can not influence the integral normal operation of the filter tank, and after the system is subjected to transient adaptation, even if the total nitrogen content of the water inlet is continuously increased, the total nitrogen content of the water outlet is basically stable. Therefore, biological strains cultured by anoxic culture are attached to the pores of the activated carbon to have good degradation effect on total nitrogen, and the running condition of the integral filter tank has no strict adaptation requirement on a water inlet end, which is sufficient to prove that the technology has good applicability to industrial sites.

The invention demonstrates the effectiveness of the method for realizing online regeneration of the activated carbon through the experiment. In order to more specifically illustrate the value of the invention for engineering application, the invention adopts actual industrial wastewater for verification.

It should be noted that the above-described embodiments are only for explaining the present invention and do not constitute any limitation of the present invention. The invention has been described with reference to exemplary embodiments, but it is understood that the words which have been used are words of description and illustration, rather than words of limitation. Modifications may be made to the invention as defined in the appended claims, and the invention may be modified without departing from the scope and spirit of the invention. Although the invention is described herein with reference to particular means, materials and embodiments, the invention is not intended to be limited to the particulars disclosed herein, as the invention extends to all other means and applications which perform the same function.

Claims

1. A method for regenerating an active carbon adsorption carrier on line by a biological method, which comprises the following steps:

Step S2, introducing target raw water into the filter tank to degrade target pollutants to obtain dischargeable water;

the step S1 comprises the following steps:

in the step E, repeating the steps B-D2-3 times;

when the target pollutants in the target raw water are organic matters and ammonia nitrogen, uniformly mixing the composite functional microbial inoculum and the nutrient solution with the target raw water in the step B, and aerating to obtain a composite functional microbial inoculum-target raw water mixed solution; in the step D, air is introduced into the filter tank, and the mixture of the composite functional microbial inoculum, the activated carbon adsorption carrier and the target raw water is subjected to aerobic culture; the aerobic culture time is 5-9 days;

The composite functional microbial inoculum consists of at least two of a ceramic bacillus WQ2021001 strain with the preservation number of CGMCC No.21641, a rhodobacter Xin Fangfang WQ2021002 strain with the preservation number of CGMCC No.21642, a halomonas WQ2021003 strain with the preservation number of CGMCC No.21643, a sphingomonas WQ2021004 strain with the preservation number of CGMCC No.21644, an Acinetobacter WQ2021005 strain with the preservation number of CGMCC No.21645, a germ bacillus WQ2021006 strain with the preservation number of CGMCC No.21646, a Brevibacterium WQ2021007 strain with the preservation number of CGMCC No.21647, a yellow micrococcus with the preservation number of CGMCC1.5361, a rhodococcus beingde with the preservation number of CGMCC1.10292 and a sludge germ with the preservation number of CGMCC 1.7745;

the COD of the target raw water is 200-3858 mg/L, and the ammonia nitrogen content is 13-96 mg/L.

2. The method of claim 1, wherein the nutrient solution comprises glucose, urea, and potassium dihydrogen phosphate; the mol ratio of carbon, nitrogen and phosphorus in the nutrient solution is 100:5:1; in the mixed solution of the composite functional microbial inoculum and the target raw water, the mass ratio of the composite functional microbial inoculum to the carbon source in the nutrient solution is (1-10) to 1; the total mass ratio of the target raw water to the composite functional microbial inoculum to the nutrient solution is (1-100) to 1.

3. The method according to claim 1, wherein in step C, the mixed solution of the complex functional microbial inoculum and the target raw water is uniformly distributed on the activated carbon type adsorption carrier.

4. The method of claim 1, wherein the activated carbon-based adsorption support comprises activated carbon and/or activated coke.

5. The method of claim 4, wherein the activated carbon is a coal-based granular activated carbon; the iodine value of the activated carbon is 600-1100, the strength is more than 90%, and the specific surface area is 500-1200 m ² /g。

6. The method according to claim 4, wherein the activated coke has an iodine value of 400-800, an intensity of > 90% and a specific surface area of 400-800 m ² /g。

7. The method according to claim 1, wherein in step D, the water temperature is maintained between 18 and 42 ℃.

8. The method of any one of claims 1-7, wherein the target raw water comprises one or more of a conditioning tank effluent, a primary settling tank effluent, a secondary settling tank effluent, a dense tank effluent, an MBR membrane effluent, an RO membrane concentrate, and cooling tower cycle blowdown water for treating industrial wastewater; the industrial wastewater comprises one or more of textile dyeing and finishing wastewater, petrochemical wastewater, fine chemical wastewater, coal chemical wastewater, heat energy engineering wastewater, papermaking wastewater, medical wastewater, fermentation wastewater, food wastewater and municipal wastewater.