KR101124508B1 - Apparatus and method of waste water treatment with membranes - Google Patents

Abstract

The present invention forms a microbial culture condition of the desired dominant species in the biological reaction tank by performing the separation and sterilization process of organic matter and solids using a rotary plate-type membrane module or an immersion membrane module prior to the biological reaction treatment and accordingly wastewater treatment capacity The present invention relates to a membrane wastewater treatment apparatus and method for improving the separation efficiency.
Membrane wastewater treatment apparatus according to an embodiment of the present invention for realizing this, the solid-liquid separator for filtering the contaminants contained in the wastewater; Rotating plate-type separator module including a separator disk filter provided inside the filter and a rotating means for rotating the separator disk filter to separate organics and solids contained in the raw wastewater passing through the solid-liquid separator and at the same time to disinfect bacteria. ; An anaerobic treatment tank or an aerobic treatment tank for removing nutrients contained in the sterile wastewater treated by the rotary plate-type separator module, or a biological reaction tank having a combination of an anaerobic treatment tank and an aerobic treatment tank; and the biological reaction tank Includes; process group that stores the processed water processed in.

Description

Separator Wastewater Treatment System and Method {APPARATUS AND METHOD OF WASTE WATER TREATMENT WITH MEMBRANES}

The present invention relates to a membrane wastewater treatment apparatus and method, and more particularly, in the biological reactor by performing the separation and sterilization process of organic matter and solids using a rotary plate-type membrane module or an immersion membrane module prior to the biological reaction treatment. The present invention relates to a membrane wastewater treatment apparatus and method for forming microbial culture conditions of a desired dominant species and thus improving wastewater treatment ability.

In general, livestock and manure wastewater, along with other industrial wastewater and pollutants, are the cause of serious environmental pollution that contaminates groundwater, rivers and oceans, which are sources of drinking water for humans and animals and plants.

Such livestock and manure wastewater treatment methods include physicochemical treatment and biological treatment.

While the physicochemical treatment method is expensive and has the disadvantage of reprocessing the product after treatment, the biological treatment method removes a large amount of organic components in the form of carbon dioxide and methane gas to remove organic matter in the wastewater, thereby increasing the amount of product after treatment. There is an advantage that can be reduced.

Biological treatment method mainly uses microorganisms to decompose and separate contaminants in wastewater, and is mainly used for the treatment of wastewater containing organic matter and sludge produced therefrom, and relatively low cost and various processes are developed and widely used. have. Microorganisms used in the biological treatment is composed of algae, bacteria, fungi, protozoa, and the like, decomposes and removes organic contaminants and multiplies with nutrients to purify wastewater.

Conventionally, wastewater treatment facilities are mostly operated by adding unit processes to activated sludge processes.

However, activated sludge processes can remove most suspended solids and organics, but only 10-20% of nutrients such as nitrogen and phosphorus are treated. In water bodies such as rivers, coastal seas and lakes, eutrophication occurs when nutrients such as nitrogen and phosphorus increase.

The eutrophication activates the production of nutrient-containing organisms, thereby changing the ecosystem of nature, causing red tide in the seas, and causing abnormal growth such as algae in lakes. This process proceeds smoothly in the natural world, but when large quantities of livestock wastewater, domestic sewage, and factory wastewater flow in, nutrients increase excessively, and odor and water pollution caused by decay are promoted due to the mass propagation of algae. It loses its value as a water resource.

Therefore, the purpose of wastewater treatment for the protection of water resources is to focus on the removal of nitrogen and phosphorus, and it is urgent to develop a process that meets the regulatory concentration that will be further strengthened.

The reactions required to treat nitrogen compounds are an aerobic nitrification process that oxidizes nitrogen compounds and an anoxic denitrification process that degass the oxidized nitrogen compound into a gaseous nitrogen gas to degas it. The method requires phosphorus release, which releases phosphorus in the microorganisms in the anaerobic state, and an aerobic state, ingesting excessive phosphorus.

Conventionally, as a treatment process for the removal of nutrients contained in such wastewater, a relatively large contaminant is removed by using a solid-liquid separator such as a vibration screen, a centrifuge or a drum screen, and a belt using a flocculant to remove fine solids. Pretreatment process with press, decanter, etc., biological reaction to remove organic matter such as nutrients by using anaerobic or aerobic microorganism, and raw waste water after biological reaction can be precipitated and recycled as liquid fertilizer or fertilizer or using membrane A post-treatment step is performed to discharge the purified water in the purified state.

However, in the conventional wastewater treatment method, the treatment cost is increased by administering a chemical such as a flocculant to filter out small foreign substances contained in the wastewater in the pretreatment process and another environmental pollution caused by the administration of the chemical. There was a problem that, even when the separator is used without administering a flocculant, manure sludge is fixed on the surface of the separator and periodic washing of the membrane is required.

In addition, in the biological reaction tank, the nutrients can be removed by microorganisms only by adjusting the occupancy rate so that the desired microorganisms among the anaerobic or aerobic microorganisms to be proliferated in each zone are controlled.

However, the conventional wastewater treatment apparatus has a problem in that the equilibrium of microbial culture conditions of the desired dominant species is broken as other bacteria are not removed from the outside in the wastewater introduced into the biological reactor.

In addition, there is a problem in that a separate sterilizing agent must be added to the biological reaction tank to remove the bacteria introduced from the outside, and the volume of the biological reaction tank is unnecessarily large in order to secure a space for cultivating the dominant species microorganism according to the external bacteria inflow. There was also an uneconomic problem.

The present invention has been made in order to solve the above problems, it is possible to form the microbial culture conditions of the desired dominant species in the biological reactor by performing the separation and sterilization of organic matter and solids contained in the wastewater prior to entering the biological reactor. It is an object of the present invention to provide a membrane wastewater treatment apparatus and method.

Separation membrane wastewater treatment apparatus according to an embodiment of the present invention for realizing the object as described above, the solid-liquid separator for filtering the contaminants contained in the wastewater; Rotating plate-type membrane module including a separator disk filter provided inside the filter and a rotating means for rotating the membrane disk filter to separate organics and solids contained in the raw wastewater passing through the solid-liquid separator and to disinfect bacteria. ; An anaerobic treatment tank or an aerobic treatment tank for removing nutrients contained in the raw wastewater sterilized by the rotary plate-type separator module, or a biological reaction tank having a combination of an anaerobic treatment tank and an aerobic treatment tank; and the biological reaction tank Includes; process group that stores the processed water processed in.

Here, the separation membrane disc filter may be configured such that a plurality of the separation membrane disc filters are respectively spaced apart from each other by a predetermined interval, and adjacent separation membrane disc filters of the adjacent hollow shafts are installed so as not to overlap or overlap each other.

In addition, the rotary plate-type membrane module, the filter washing line for supplying the washing water to the washing water storage unit, and comprises a plurality of nozzles connected to the filter washing line to spray the washing water to each of the separation membrane disk filter to wash Can be.

Separation membrane wastewater treatment apparatus according to another embodiment of the present invention, the solid-liquid separator for filtering the contaminants contained in the wastewater; In order to separate organics and solids contained in the raw wastewater passing through the solid-liquid separator and to disinfect bacteria, the submerged membrane provided in the tank and the submerged membrane are compressed to prevent the blockage of the submerged membrane. An immersion type membrane module including an air diffuser for supplying air; An anaerobic treatment tank or an aerobic treatment tank for removing nutrients contained in the original wastewater sterilized through the immersion membrane module, or a biological reaction tank having a combination of an anaerobic treatment tank and an aerobic treatment tank; and the biological reaction tank Includes; process group that stores the processed water processed in.

The submerged membrane module may include an air supply pipe for supplying compressed air to an air diffuser, and a plurality of nozzles connected to the air supply pipe for injecting compressed air to each of the submerged membranes. Can be.

Separation membrane wastewater treatment method according to an embodiment of the present invention comprises the steps of filtering the contaminants contained in the raw wastewater collected in the raw wastewater storage tank by the solid-liquid separator; Separation and sterilization of organic matter and solids while passing through the rotating plate-type membrane module having a membrane disk filter for rotating the waste water filtered out the contaminants; and Anaerobic treatment of biological wastewater And nutrients are removed through the bath and the aerobic treatment tank selectively or in combination.

In addition, the treated water passing through the biological reaction tank is filtered while passing through the rotary plate-type membrane module or immersion membrane module again; may be configured to further include.

Separation membrane wastewater treatment method according to another embodiment of the present invention comprises the steps of filtering the contaminants contained in the raw wastewater collected in the raw wastewater storage tank by the solid-liquid separator; Separation and sterilization of the organic matter and solids while passing through the immersion membrane module having the immersion membrane and the diffuser; and the wastewater passed through the immersion membrane module and anaerobic of the biological reactor It comprises a step of removing nutrients through the treatment tank and aerobic treatment tank selectively or in combination.

In addition, the treated water passing through the biological reaction tank is filtered while passing through the immersion membrane module or the rotary plate-type membrane module again; may be configured to further include.

According to the membrane wastewater treatment apparatus and method according to the present invention, the biodegradable solids contained in the wastewater by performing the separation and sterilization process of organic matter and solids using a rotary membrane-type membrane module or an immersion membrane module prior to the biological reaction treatment And through the effective removal of the color and odor contained in the organic suspended solids and the causes of eutrophication nitrogen, phosphorus, wastewater has the advantage of improving the purification capacity of the wastewater and improve the quality of the effluent.

In addition, according to the present invention, since it is possible to treat wastewater without using a separate flocculant or sterilizing agent, it is possible to reduce the process cost and to prevent the occurrence of contaminants in the process.

In addition, according to the present invention, by preventing the external bacteria from entering the biological reactor in advance, not only can the volume of the biological reactor be miniaturized, but also the environment in which the microorganisms can be smoothly grown by the water spray phase method in the biological reactor. It can work.

1 is a block diagram of a membrane wastewater treatment apparatus according to the present invention,
Figure 2 is a cross-sectional view showing the configuration of a rotary plate-type membrane module of the membrane wastewater treatment apparatus according to the present invention,
3 is a partial detailed cross-sectional configuration of the filter in FIG.
4 is a cross-sectional configuration diagram of the separator disc filter of FIG. 3;
Figure 5 is a cross-sectional view showing the configuration of the immersion membrane module of the membrane wastewater treatment apparatus according to the present invention,
6 is a flow chart of the membrane wastewater treatment method according to the present invention.

Hereinafter, the configuration and operation of the preferred embodiment of the present invention will be described in detail with reference to the accompanying drawings.

1 is a configuration diagram of a membrane wastewater treatment apparatus according to the present invention, Figure 2 is a cross-sectional view showing the configuration of a rotating plate-shaped membrane module of the membrane wastewater treatment apparatus according to the present invention, Figure 3 is a partial detailed cross-sectional configuration of the filter in Figure 2 4 is a cross-sectional view of the membrane filter of the membrane of Figure 3, Figure 5 is a cross-sectional view showing the configuration of the immersion membrane module of the membrane wastewater treatment apparatus according to the present invention.

Membrane wastewater treatment apparatus according to the present invention, the raw wastewater storage tank 10 to collect the raw wastewater, and solid-liquid separator 20 for removing a relatively large contaminants contained in the wastewater using a vibration screen, a centrifuge or a drum screen, etc. ), A first treatment water tank 30 in which the raw waste water passing through the solid-liquid separator 20 is stored, a strainer 40 for filtering again the contaminants not filtered out of the solid-liquid separator 20, and the strainer. It comprises a rotary plate-type membrane module 50 or immersion membrane module 55 for separating the organic matter and solids contained in the raw wastewater passed through the (40) and at the same time to disinfect bacteria contained in the raw wastewater.

And a second treatment tank 60 in which raw waste water sterilized by the rotary plate-type membrane module 50 or an immersion membrane module 55 is collected, and included in the original waste water collected in the second treatment tank 60. In the biological reaction tank (70) having an anaerobic treatment tank (71) and an aerobic treatment tank (72) for removing nutrients such as nitrogen and phosphorus, and the raw wastewater passing through the biological reaction tank (70) Strainer 41 for filtering the contained contaminants, the treated water passing through the strainer 41 is stored and the sediment is processed into a liquid ratio, and the process tank 80 to discharge the supernatant and the process tank And a rotary plate-like membrane module 51 or an immersion type membrane module 56 for selectively filtering the supernatant discharged from 80 again.

The membrane wastewater treatment apparatus of the present invention having the above configuration includes organic matter and solids contained in the wastewater through the rotary plate-type membrane module 50 or the immersion membrane module 55 at the stage before the raw wastewater is introduced into the biological reactor 70. By separating and treating the bacteria contained in the original wastewater at the same time by the sterilization process characterized in that the biological reaction tank 70 is characterized in that configured to form the culture conditions of the anaerobic or aerobic microorganisms of the desired dominant species.

2 to 4, the rotary plate-type separator module 50 receives the wastewater of the first treatment water tank 30 through the supply pipe 110 and the pump 120 to filter and extracts the filtered water, using a motor ( Filter 200 for filtering using a plurality of membrane disk filter 210 rotated by the 220, and compressed air supply unit for supplying compressed air to the filter 200 to discharge the waste water inside the filter 200 ( 300 and a washing water storage unit 400 for storing the washing water for washing the inside of the filter 200.

Referring to the operation of the rotary plate-like membrane module 50 of the above configuration, first, the waste water stored in the first treatment tank 30 through the valve (V1), supply pipe 110 and the pump 120, the filter 200 Is supplied.

In the filter 200, the hollow shaft 230 is rotated by the motor 220, and the separator disc filters 210 having a central portion inserted into the hollow shaft 230 rotate.

Due to the rotation of the separator disc filter 210, it is possible to prevent debris from accumulating on the surface of the separator disc filter 210. Accordingly, it is possible to install the filter 200 at the stage before the biological reactor 70.

The separation membrane disc filter 210 includes a support 211 coupled to the side of the hollow shaft 230, a flow path film 213 coupled to provide a space between the support 211, and the flow path film 213. It is configured to include a filter 212 is located on the upper portion, the supply port through which the filtered water can be introduced into the hollow shaft 230 to communicate with the space provided between the support 211 and the flow path film 213 231 is provided.

In this configuration, the wastewater supplied is filtered by the filter 212 so that foreign matter in the wastewater remains on the upper portion of the filter 212, and only water passes through the filter 212 and passes through the flow path membrane 213. The flow path membrane 213 and the support 211 is introduced into the space, the introduced filtered water is stored in the second treatment tank 60 through the inside of the hollow shaft 230 through the supply port 231. The foreign matter separated from the filtered water is discharged to the outside through the drain line 240.

In this case, in order to increase the efficiency of the filtration, the compressed air supply unit 300 may supply the compressed air to the inside of the filter 200 to further promote separation of foreign matter and water by increasing the pressure. In addition, by connecting the pump 221 to the end of the hollow shaft 230, by driving the pump 221 to reduce the pressure inside the hollow shaft 230 to further improve the filtration efficiency in the filter 212 Can be.

When the waste water and the washing water are discharged, the compressed air supplied by the compressed air supply unit 300 prevents the filter 212 from being damaged by the internal pressure reduction of the hollow shaft 230, and facilitates the discharge of the filtered water. Play a role.

As the filtration process is repeated, sludge may adhere to the surface of the filter 212, and clogging of the filter 212 may be prevented by the rotation of the separation disk filter 210.

In addition, the separation membrane disk filter 210 is coupled to a plurality of the plurality of hollow shafts 230 at predetermined intervals, respectively, and the separation membrane disk filters 210 of the adjacent hollow shaft 230 are respectively installed without overlapping or overlapping each other. Can be installed.

Accordingly, turbulence is formed when the separator disc filter 210 is rotated, thereby further reducing the sludge adhered to the surface of the separator disc filter 210.

In addition, branched from the supply pipe 110 further includes a filter washing line 410 and a nozzle 411 for supplying and spraying the washing water of the washing water storage unit 400 to the separator disk filter 210 side of the filter 200. It is desirable to. In this case, it is possible to prevent the sludge from sticking to the surface of the separator disc filter 210.

Referring to the process of washing the sludge from the separation membrane disk filter 210, in the state in which the valve (V1) is closed, the valve (V2) is opened, the washing water in the washing water storage unit 400, the pump 120 and the supply pipe ( 110 is supplied through the plurality of nozzles 411 coupled to the filter washing line 410 through the open valve (V4), the valve V3 is closed in the closed state (V3). It is sprayed on the surface of each separator disk filter 210.

Alternatively, the washing water may be introduced into the filter 200 through the valve V3, or the washing water may be introduced into the filter 200 in a state in which both the valve V3 and the valve V4 are open.

At this time, the washing water is sprayed at an appropriate pressure by the diameter of the nozzle 411 and the pressure of the pump 120 to remove the sludge.

Then, when each separator disk filter 210 is rotated using the motor 220, the separator disk filter is fixed even when the nozzles 411 coupled to the filter washing line 410 are fixed by the rotation of the separator disk filter 210. It is possible to wash the entirety of 210.

The nozzle 411 is preferably provided with discharge ports on both sides so as to simultaneously wash the upper and lower surfaces of the adjacent membrane disk filter 210.

Here, the separator disk filter 210 constituting the rotating plate-shaped separator module 50 has a micrometer size of several micrometers in order to filter out microorganisms contained in the raw wastewater in addition to filtering organic matter and solids contained in the raw wastewater. In consideration of the above, it is preferable that the resolution of the filter 212 is configured to have a range of 0.0001 μm to 1 μm.

Even if the gap of the filter 212 is configured to be small, the rotary plate-type membrane module 50 includes a self-cleaning function as described above, thereby preventing clogging of the membrane disk filter 210 due to sludge of organic matter, solid matter and bacteria. It becomes possible.

In the separator wastewater treatment apparatus according to the present invention, an immersion type membrane module 55 may be employed as a configuration to replace the above-described rotating plate-type separator module 50.

Referring to Figure 5, the immersion membrane module 55 is a water tank 552 for receiving and storing the waste water of the first treatment water tank 30 through the supply pipe 110a and the pump 120a, and the water tank 552. And an immersion type separation membrane 550 for disintegrating organic materials and solids contained in the raw wastewater and disinfecting bacteria at the same time, and to prevent the immersion type separation membrane 550 from being blocked by foreign substances. It includes a diffuser device 555 for supplying compressed air to the immersion separator 550. The diffuser 555 is connected to the air supply unit 500 through an air supply pipe 551.

A discharge pipe 222 is connected to the second treatment water tank 60 at an upper portion of the immersion membrane 550, and a suction pump 223 is provided on the discharge pipe 222.

The immersion type separator 550 has a plurality of separators having a resolution in the range of 0.0001 μm to 1 μm at regular intervals.

When the suction pressure is generated by the operation of the suction pump 223, the wastewater outside the immersion separation membrane 550 accommodated in the water tank 552 is sucked into the immersion separation membrane 550, and the organic matter contained in the waste water and Solids and bacteria are filtered out in the immersion separator 550, and the filtered treated water is collected from the upper part of the immersion separator 550 and is transferred to the second treatment tank 60 along the discharge pipe 222.

As the filtration process is repeated, foreign substances including organic matter, solid matter, and bacteria may be fixed to the surface of the immersion separator 550. In order to prevent such clogging, an air diffuser is provided below the immersion separator 550. 555 is provided to remove the foreign matter stuck to the surface of the immersion type separation membrane 550 by supplying compressed air upward.

Here, the diffuser device 555 is composed of a plurality of nozzles 556 in order to effectively remove the foreign matter stuck to the surface of the immersion separator 550, compressed air is injected to both surfaces of the immersion separator 550. Can be configured in a manner.

And when foreign matter is accumulated in the tank 552 or more a predetermined amount may be configured to be discharged to the outside through the drain line (240a) provided in the lower portion of the tank (552).

Reference numerals V6, V7, and V8 denote valves provided on the supply pipe 110a, the air supply pipe 551, and the drain line 240a.

As described above, the raw waste water filtered and sterilized by the rotary plate-type membrane module 50 or the immersion membrane module 55 is introduced into the second treatment tank 60 and then transferred to the biological reaction tank 70.

The biological reaction tank 70 is composed of a plurality of anaerobic treatment tank 71 and aerobic treatment tank 72, the raw wastewater introduced into the biological reaction tank 70 is a plurality of anaerobic treatment tank 71 and aerobic treatment The nutrients contained in the raw waste water are removed while passing through the tank 72 selectively or in combination.

In the biological reactor (70) can be used for the trickling phase method to propagate microorganisms.

The trickling method is to pile up filter materials such as gravel, crushed stone, wood, and other intermediate layers having pores formed on the surface thereof, and to allow the anaerobic or aerobic microorganisms to proliferate inside the pores. .

The microorganisms decompose and treat organic matter in the raw wastewater while adsorbing and parasitic inside the pores.

Since the foreign matter is filtered from the rotary plate-type membrane module 50 or the immersion membrane module 55 before the raw waste water is introduced into the biological reaction tank 70, it is possible to prevent the problem of clogging of the air gap by the foreign matter. Will be.

In the anaerobic treatment tank 71 of the biological reaction tank 70, nitrogen is discharged by substantial denitrification by anaerobic microorganisms, and in the aerobic treatment tank 72, the intake process of phosphorus released while the nitrification process is promoted by the aerobic microorganisms proceeds. At the same time, residual organic matter is removed by the microorganism.

In this case, in the anaerobic treatment tank 71 and the aerobic treatment tank 72, the anaerobic microorganism and the aerobic microorganism should be dominant. If external bacteria are introduced into the biological reactor 70, these predominant conditions cannot be created.

In the case of the present invention, since the sterilization treatment is performed in the rotary plate-type membrane module 50 or the immersion membrane module 55, it is easy to make a predominant condition of each microorganism in the biological reaction tank 70.

In addition, the biological reaction tank 70 may be configured to perform a process of removing organic matter, nitrogen, phosphorus, and chromaticity remaining in the original wastewater by aeration of air.

6 is a flow chart of the membrane wastewater treatment method according to the present invention.

Separation membrane wastewater treatment method using the wastewater treatment apparatus, the raw wastewater is collected in the raw wastewater storage tank (10) (S 101), after passing through the solid-liquid separator (20) and caught the contaminants, the first treatment water tank (30) (S 102), the raw wastewater of the first treatment tank 30 is a rotary plate-like separator module 50 or 0.0001 ㎛ ~ 1 having a rotating separator disk filter 210 having a resolution of 0.0001 ㎛ ~ 1 ㎛ After the separation and sterilization of the organic matter and the solid through the immersion membrane module 55 having the immersion membrane 550 having a separation ability of μm is introduced into the second treatment tank 60 (S 103).

The raw wastewater of the second treatment tank (60) is selectively or in combination with the anaerobic treatment tank (71) and the aerobic treatment tank (72) of the biological reaction tank (70) depending on the wastewater concentration. 80) (S 104).

In the process tank 80, the sediment of the raw wastewater treated in the biological reaction tank 70 is processed into a liquid ratio, and the supernatant is subjected to a discharge process (S 105). In addition, the treated water optionally passing through the process tank 80 is discharged after passing through the rotary plate-type membrane module 51 or the submerged membrane module 56 to improve the quality of the discharged water (S 106). .

According to the wastewater treatment apparatus and method according to the present invention as described above, unlike the wastewater treatment method according to the prior art, organic matter and solids contained in the raw wastewater through the rotary plate-type membrane module 50 or the immersion membrane module 55 In addition, by sterile microorganisms by filtering the micro-sized bacteria can be cultivated smoothly the desired microorganism in the biological reaction tank (70).

Therefore, the solid wastes and organic suspended solids contained in the raw waste water and nutrients such as nitrogen and phosphorus, which are the causes of eutrophication, are removed, and color and odor are removed through the aeration of air to discharge the purified water. It is possible to improve the purification treatment capacity and improve the quality of effluent water.

It will be apparent to those skilled in the art that the present invention is not limited to the above embodiments and can be practiced in various ways without departing from the technical scope of the present invention. will be.

10: wastewater storage tank 20: solid-liquid separator
30: first treatment tank 40,41: strainer
50,51: rotating membrane module 55,56: immersion membrane module
60: second treatment tank 70: biological reaction tank
71: anaerobic treatment tank 72: aerobic treatment tank
80: process tank 110,110a: supply pipe
120,120a: Pump 200: Strainer
210: separator disk filter 220: motor
230: hollow shaft 240,240a: drain line
300: compressed air supply unit 400: wash water storage unit
410: filter washing line 411,556: nozzle
500: air supply 550: dipping membrane
551: air supply pipe 552: water tank
555: diffuser

Claims (9)

Solid-liquid separator to filter out contaminants contained in wastewater;
Rotating plate-type membrane module including a separator disk filter provided inside the filter and a rotating means for rotating the membrane disk filter to separate organics and solids contained in the raw wastewater passing through the solid-liquid separator and to disinfect bacteria. ;
An anaerobic treatment tank or an aerobic treatment tank for removing nutrients contained in the raw wastewater sterilized by the rotary plate-type separator module, or a biological reaction tank having a combination of an anaerobic treatment tank and an aerobic treatment tank; and
A process tank for storing the treated water treated in the biological reaction tank;
Separator wastewater treatment apparatus comprising a. The method of claim 1,
The separation membrane disc filter is a plurality of separation membrane disc filters are respectively coupled to a predetermined interval spaced apart, the separation membrane disc filter of the adjacent hollow shaft is installed so as not to overlap each other or overlap each other. The method according to claim 1 or 2,
The rotating plate separator module,
And a plurality of nozzles connected to the filter washing line to supply the washing water to the filter, and a plurality of nozzles connected to the filter washing line to spray and wash the washing water onto each of the membrane disc filters. Solid-liquid separator to filter out contaminants contained in wastewater;
In order to separate organics and solids contained in the raw wastewater passing through the solid-liquid separator and to disinfect bacteria, the submerged membrane provided in the tank and the submerged membrane are compressed to prevent the blockage of the submerged membrane. An immersion type membrane module including an air diffuser for supplying air;
An anaerobic treatment tank or an aerobic treatment tank for removing nutrients contained in the sterile wastewater treated by the immersion membrane module, or a biological reaction tank having a combination of an anaerobic treatment tank and an aerobic treatment tank; and
A process tank for storing the treated water treated in the biological reaction tank;
Separator wastewater treatment apparatus comprising a. The method of claim 4, wherein
The immersion membrane module,
Separation membrane wastewater treatment apparatus comprising an air supply pipe for supplying the compressed air to the air dispersing device and a plurality of nozzles connected to the air supply pipe for injecting compressed air to each of the immersion type separation membrane. Filtering contaminants contained in the raw wastewater collected in the raw wastewater storage tank by a solid-liquid separator;
Separation and sterilization of organic matter and solids while passing through the rotating plate-type separator module having a separator disk filter for rotating the waste water filtered out the contaminants; And
Removing nutrients through the anaerobic treatment tank and the aerobic treatment tank of the biological reaction tank through the rotary plate-type membrane module selectively or in combination;
Membrane wastewater treatment method comprising a. The method of claim 6,
And filtering the treated water passing through the biological reaction tank again through the rotating plate-type membrane module or the submerged membrane module. Filtering contaminants contained in the raw wastewater collected in the raw wastewater storage tank by a solid-liquid separator;
Separating and disinfecting the organic matter and the solids while passing through the immersion separator module having the immersion separator and the diffuser;
Removing the nutrients through the anaerobic treatment tank and the aerobic treatment tank of the biological reaction tank through the immersion membrane module through the immersion membrane module;
Membrane wastewater treatment method comprising a. The method of claim 8,
Separation of the treated water passing through the biological reaction tank and the filtration treatment while passing through the immersion membrane module or rotary plate-type membrane module again; Separation membrane wastewater treatment method further comprising.

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