KR100451816B1 - Microbial media and wastewater treatment apparatus - Google Patents

Abstract

The present invention relates to a bio-contact small scale wastewater treatment apparatus, for example, in which a carrier using a modified wood chip is installed in an anaerobic tank, a first and a second aeration tank, respectively.

An anaerobic tank in which the introduced waste water is removed, denitrified and solid-liquid separated by organic anaerobic and anaerobic and aerobic microorganisms; An anaerobic tank for promoting organic matter removal and denitrification by anaerobic microorganisms attached to or suspended from the carrier; First and second aeration tanks, which are aerated by a vigorous vent installed in the lower part of the carrier to remove fine and dissolved organic matter remaining in the waste water and accelerate nitrification; By returning the sludge accumulated in the lower part of the sedimentation tank to the storage tank through the sludge conveying member, the sludge residence time is kept long and the nitrated nitrogen is returned, so that the effective denitrification is carried out in the anoxic tank and the phosphorus-removing microorganisms in which phosphorus is excessively ingested in the aeration tank It precipitates in the sedimentation tank and effectively removes the phosphorus, characterized in that consisting of a discharge tank to discharge only the fine water to precipitate after removing the fine particles suspended.

Description

Carrier and wastewater treatment device using same {MICROBIAL MEDIA AND WASTEWATER TREATMENT APPARATUS}

The present invention relates to a bio-contact small scale wastewater treatment apparatus, for example, in which a carrier using a modified wood chip is installed in an anaerobic tank, a first and a second aeration tank, respectively.

In population centers of large cities, large-scale sewage treatment plants or large-scale sewage treatment plants are installed, and residential sewage is collectively processed by linking the conduits in the districts. Unlike the general pollutants, the domestic sewage not only directly affects water pollution, Small sources are scattered throughout the country. In particular, in urban or rural areas where sewer supply is insufficient, most of the living sewage is discharged to the natural water system and the damage of the water ecosystem is accelerated as it flows beyond the midnight capacity of the lake or river. As nutrients such as nitrogen and phosphorus are continuously introduced into the water, eutrophication is frequently occurring, and the value of use as a source of living water is greatly impaired.

Chemical and biological methods are used to remove organic matter and nutrients in domestic sewage or waste water. However, the characteristics of untreated sewage, the type of sewage treatment method, and the degree of nutrient removal required should be considered. The removal of organic matter or nutrients through the chemical method ensures high efficiency, while biological methods with relatively low sludge generation are preferred due to economic burden due to drug purchase costs and large amounts of sludge.

The main process of the biological method is aerobic process by mixing sewage and microorganisms to induce the metabolism of microorganisms to remove organic matter and nutrients. Small-scale sewage treatment equipment uses activated sludge or long-term aeration techniques that use suspended growth microorganisms at first, which is difficult to cope with sludge swelling phenomenon and large load fluctuations and large surplus sludge occurs during operation. There is a problem such as.

For this reason, the carrier which can process microorganisms to a support body is used a lot of methods using the high concentration microorganism attached to a carrier by the method of adding a floating growth method. In the biofilm process using a carrier, microorganisms adhere to the carrier to form a biofilm, which is different from the microorganisms in a dispersed state, and the physiological mechanisms of the species are different, resulting in increased resistance, increased growth rate, increased metabolic activity, and resistance to toxic effects. do.

The microenvironment formed on the solid surface has a different pH, ionic strength and organic matter concentration than the whole environment. Therefore, when microbial community is different, microorganisms with slow growth rate are preserved in the system by attachment and maintain high concentration. The concentration of organic matter is increased due to the adhesion of solid surface and the hydrolyzate is not leaked to provide a good environment for microbial growth, thereby increasing microbial activity. In addition, resistance to toxic substances is increased by the age of microorganisms, food chains, and encapsulation of bacteria, and the amount of sludge generated to the outside is small and the degradability of hardly decomposable substances is also strong.

And, since the biofilm is formed, unlike the activated sludge method, there is no sludge floating phenomenon due to the sludge swelling phenomenon, so the operation management is easy and the microbial concentration per unit volume can be maintained high due to the operating characteristics. In order to increase the treatment efficiency of the biofilm process, it is important to apply the carrier to the actual process, while operating in the optimum operating conditions suitable for the carrier while maintaining the appropriate amount of adherent microorganisms. In addition, since it is necessary to keep the microorganisms used for wastewater treatment in an aeration tank at an appropriate level, an appropriate microorganism attachment carrier is necessary for the growth or adhesion growth of the microorganisms.

There are many kinds of carriers such as activated carbon fibers, powdered activated carbon, polyvinyl alcohol and porous plastics, waste yagurt bottles, polymer resin fiber yarns, porous ceramics or glass carriers, and diatomaceous earth. As the microbial carrier, it is necessary to use a carrier suitable for the characteristics of the influent wastewater, such as the concentration of organic matter in the wastewater, the concentration of nitrogen and phosphorus, the presence of toxic substances, and the acidity of the wastewater.

In order to increase the treatment efficiency of the biofilm process, the biofilm surface area per unit surface area of the carrier should be increased.Because the biofilm is formed / grown by attaching microorganisms to the carrier surface, it is possible to form biofilm quickly in engineering terms and maintain high concentration of microorganisms. It is important to find out the conditions of the carrier. In addition, the small scale sewage treatment apparatus is a sewage treatment apparatus using a carrier, a new high performance carrier is required.

The present invention has been invented in view of the above circumstances, and can be recycled as a carrier by modifying various kinds of materials, and using the characteristics of the carrier improves the efficiency of wastewater treatment, and the process is simple and operation is easy. The purpose of the present invention is to provide a carrier and a wastewater treatment device using the bioreactor installed in a real sewage treatment plant to evaluate the reliability through the characteristics and treatment efficiency of the reactor by removing biological organic matter and nutrients using the real sewage. There is this.

1 is a plan view showing a carrier and a wastewater treatment apparatus using the same according to an embodiment of the present invention,

2 to 4 are cross-sectional views of each of parts A-A, B-B, and C-C shown in FIG. 1;

5 is a plan view showing a carrier and a wastewater treatment apparatus using the same according to another embodiment of the present invention;

6 to 8 are respective cross-sectional views of A-A, B-B, and C-C portions shown in FIG. 5.

♠ Explanation of symbols on the main parts of the drawing ♠

1: Storage tank 2: Anaerobic tank

3: anaerobic tank 4: first aeration tank

5: second aeration tank 6: settling tank

7: discharge tank 8: blower

9: sludge conveying member 10: carrier

11: siphon 12: tube

According to the present invention for achieving the above object, the carriers respectively installed in the anaerobic tank, the first and the second aeration tank are amorphous, tetrahedral, elliptical, and circular, having a porosity of 30 to 80%, and a size of 2 to 20 Cm. Made of wood or modified wood chips, porous plastic, waste yogurt bottle, polymer resin fiber yarn, foamed resin such as polyurethane, crushed stone such as basalt or granite, powdered contact material such as granular activated carbon or sawdust. It features.

In addition, the wastewater treatment apparatus of the present invention, the storage tank for classifying the solid and liquid by mixing and storing the introduced wastewater and the external transport sludge returned from the settling tank; An anaerobic tank in which wastewater flowed into the middle siphon of this storage tank removes organic matter, denitrates, and solid-liquid separation by aerobic, anaerobic, and aerobic microorganisms; An anaerobic tank in which the inflow water flowing into the middle and lower siphons of the anoxic tank passes through the carrier from the top to the bottom, and promotes organic matter removal and denitrification by anaerobic microorganisms attached to or suspended from the carrier; Inflow water from the bottom of the carrier of the anaerobic tank by the siphon passes through the carrier from the top to the bottom of the first aeration tank, and the inflow into the second aeration tank through the outlet of the lower portion passes from the bottom of the carrier to the bottom of the carrier. First and second aeration tanks that are aerated by the tuyeres installed in the tank to remove fine and dissolved organic matter remaining in the waste water and accelerate nitrification; Inflow water from the upper part of the second aeration tank moves through the pipe into the settling tank, and the sludge settles down gradually, and only the clear treated water of the upper layer flows out, and the sludge accumulated in the settling tank bottom through the sludge conveying member is returned to the storage tank. A sedimentation tank which maintains the sludge residence time and conveys nitrified nitrogen so that effective denitrification is achieved in the anoxic tank, and at the same time, precipitated phosphorus-removing microorganisms in excess of phosphorus in the aeration tank are precipitated in the sedimentation tank to effectively remove phosphorus; The treated water introduced from the upper portion of the sedimentation tank is characterized in that it consists of a discharge tank that removes the fine particles suspended during the stay in the discharge tank and then discharges only the clear upper water.

Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.

1 is a plan view showing a carrier and a wastewater treatment apparatus using the same according to an embodiment of the present invention, Figures 2 to 4 shows the A-A, B-B, C-C shown in Figure 1 Each section is a cross section.

First, the carrier 10 is a modified wood chip, which is installed in the anaerobic tank 3, the first and the second aeration tanks 4 and 5, which will be described later. The shape of the carrier 10 is amorphous, tetrahedral, elliptical and circular. -80%, 2-20 Cm in size, wood or modified wood chips, porous plastics, waste yogurt bottles, high-molecular resin fibers, foamed resins such as polyurethane, crushed stone such as basalt or granite, granular activated carbon or sawdust It is made by filling a powdery contact medium such as.

On the front of the anaerobic tank 3, a storage tank 1 and an anaerobic tank 2 are provided, and these tanks 1-3 are provided with siphons 11 on one side thereof, respectively. On the rear surface of the second aeration tank 5, a settling tank 6 and a discharge tank 7 are installed in parallel as shown in FIG. The air is sent by the blower 8 to the bottom of the said 1st and 2nd aeration tanks 4 and 5, the settling tank 6, and the discharge tank 7, respectively. In addition, the settling tank 6 is connected to the storage tank 1 through the sludge conveying member 9 while the second aeration tank 5 is connected through the pipe 12, the second aeration tank 5 and the first The aeration tank 4 is connected through the outlet 13 of the lower portion.

Small-scale wastewater treatment apparatus of the present invention is the storage tank 1 and the anaerobic tank 2, the anaerobic tank 3 of the carrier 10, the first and second aeration tank 4, the external waste water sequentially through the inlet shown in FIG. 5) and discharged through the parallel settling tank 6 and the discharge tank 7 to the outlet. As shown in FIG. 2, sludge in the settling tank 6 is sent to the storage tank 1 through the sludge conveying member 9.

In the present invention constituted as described above, the size of each tank (1-7) is based on the central anaerobic tank (3), the storage tank (1): anaerobic tank (2): anaerobic tank (3): first aeration tank by volume ratio (4): second aeration tank (5): sedimentation tank (6) + discharge tank (7) are each made of a ratio of 0.3-0.7: 1.5-2: 1.0: 2-3: 1-2: 0.3-0.7, The height is 1.5-2.4 and is divided into a discharge tank of 0.7-1.1 and a settling tank of 0.8-1.3. In addition, the shape and water level of each tank 1-7, the intake water position of the inflow water, the outlet position of the outlet, the filling position of the carrier 10, the position of the blower 8, and the like are shown in Figs.

The storage tank 1 is for classifying solids and liquids by mixing and storing the introduced wastewater and the external conveying sludge returned from the settling tank 6. The wastewater flowing into the intermediate siphon 11 of the storage tank 1 is removed from organic matter, denitrified, and solid-liquid separation by aerobic anaerobic, anaerobic, and aerobic microorganisms during a certain period of time in the anaerobic tank 2. In this oxygen-free tank 2, nitrogen removal (denitrification) is carried out by effectively converting the nitrogenous nitrogen returned from the precipitation tank 6 into the nitrogen gas by the denitrification microorganism as the electron acceptor. Organics can be used as an energy source for denitrification, leading to effective organic removal.

The inflow water flowing into the middle and lower siphons 11 of the anoxic tank 2 passes through the carrier 10 in the middle from above the anaerobic tank 3 and is purified. The filling rate of the carrier 10 is 0-50% (volume ratio), and the porosity is about 30-80% although it depends on the type and material of the carrier 10.

In the anaerobic tank 3, organic matter removal and denitrification are promoted by anaerobic microorganisms attached to or suspended from the carrier 10, which releases phosphorus out of the microorganisms in the process of ingesting organic matter by the phosphorus removing microorganism. More than half of the organic matter is removed by the microorganism in the course of passing through the anaerobic tank 2 and the anaerobic tank 3, and the organic matter is further promoted by the microorganisms coated on the carrier 10. In addition, by placing the anoxic tank (2) in front of the anaerobic tank (3) it can prevent the phosphate release of the phosphorus-removing microorganism due to the nitrate nitrogen coming from the sludge conveying process.

The inflow water introduced by the siphon 11 from the lower portion of the central carrier 10 of the anaerobic tank 3 passes through the carrier 10 from the top of the first aeration tank 4 to the bottom of the first aeration tank 4. Influent water entering the second aeration tank (5) through the outlet (13) passes under the carrier (10) up. In the first and second aeration tanks 4 and 5, the aeration holes 8 'provided at the lower portion of the carrier 10 are aerated to remove even fine organic and dissolved organic matter remaining in the waste water and accelerate nitrification. Accordingly, the carrier 10 is filled in the first and second aeration tanks 4 and 5 at a volume ratio of 50 to 80%.

In the first and second aeration tanks 4 and 5, the remaining dissolved organic matter is almost removed, and this process is further facilitated by the microbial layer coated on the carrier 10. In addition, the microorganisms are strongly adsorbed in the processing of the filled carrier 10 to form a membrane to prevent the desorption of the microorganisms and to maintain strong environmental conditions against rapid external environmental changes, such as inflow of acid, alkaline wastewater. In these aeration tanks, nitrification occurs in which ammonia nitrogen is converted to nitrate nitrogens such as nitrite nitrogen and nitrate nitrogen, and higher nitrification occurs through the second aeration tank 5.

Therefore, the phosphorus removal microorganisms that have passed through the anaerobic tank 3 to the aeration tanks 4 and 5 can effectively remove phosphorus by ingesting up to five times more phosphorus due to a sudden environmental change from the anaerobic state to the aerobic state.

The inflow water introduced from the upper portion of the second aeration tank 5 moves into the sedimentation tank 6 through the pipe 12, and the sludge settles down gradually, and only the clear treated water of the upper layer flows out into the discharge tank 7. This sludge tank 6 carries sludge accumulated in the lower part of the sedimentation tank 6 through the sludge conveying member 9 to the storage tank 1, thereby maintaining the sludge residence time long, and conveying the nitrified nitrogen to the anoxic tank 2 ) To ensure effective denitrification. At the same time, the phosphorus removal microorganisms in which phosphorus is excessively ingested in the aeration tanks 4 and 5 may be precipitated and removed in the precipitation tank 6 to effectively remove phosphorus.

The treated water introduced from the upper portion of the sedimentation tank 6 precipitates and removes the fine particles suspended during the residence in the discharge vessel 7, and then flows only the clear upper water.

FIG. 5 is a plan view showing a carrier and a wastewater treatment apparatus using the same according to another embodiment of the present invention, and FIGS. 6 to 8 show parts A-A, B-B, and C-C shown in FIG. Each section is a cross section.

The carrier and the wastewater treatment apparatus using the same shown in FIG. 5 are divided into three parts according to the circumstances of the installation place, unlike the carrier and the wastewater treatment apparatus using the same shown in FIG. Oxygen-free tank (2) and anaerobic tank (3), the middle part consists of the first aeration tank (4) and the second aeration tank (5) in parallel, and the parallel settling tank (6) and discharge tank (7). Since the action and effect are the same, detailed description thereof is omitted.

As described above, according to the present invention, the storage tank, the anaerobic tank, the anaerobic tank, the first and the second aeration tank, the settling tank and the discharge tank can be divided into various forms depending on the circumstances of the installation place, and the carrier is the anaerobic tank, the first and the It is possible to provide a small-scale wastewater treatment apparatus each installed in the second aeration tank.

Claims (8)

delete delete A storage tank for mixing and storing the introduced waste water and the external conveying sludge returned from the settling tank to classify the solid and the liquid; An anaerobic tank in which wastewater flowed into the middle siphon of this storage tank removes organic matter, denitrates, and solid-liquid separation by aerobic, anaerobic, and aerobic microorganisms; An anaerobic tank in which the inflow water flowing into the middle and lower siphons of the anoxic tank passes through the carrier from the top to the bottom, and promotes organic matter removal and denitrification by anaerobic microorganisms attached to or suspended from the carrier; Inflow water from the bottom of the carrier of the anaerobic tank by the siphon passes through the carrier from the top to the bottom of the first aeration tank, and the inflow into the second aeration tank passes through the bottom of the carrier from the bottom of the carrier to the bottom of the carrier. First and second aeration tanks that are aerated by the tuyeres installed in the tank to remove fine and dissolved organic matter remaining in the waste water and accelerate nitrification; Inflow water from the upper part of the second aeration tank moves through the pipe into the settling tank, and the sludge settles down gradually, and only the clear treated water of the upper layer flows out, and the sludge accumulated in the settling tank bottom through the sludge conveying member is returned to the storage tank. A sedimentation tank which maintains the sludge residence time and conveys nitrified nitrogen so that effective denitrification is achieved in the anoxic tank, and at the same time, precipitated phosphorus-removing microorganisms in excess of phosphorus in the aeration tank are precipitated in the sedimentation tank to effectively remove phosphorus; The treatment water introduced from the upper portion of the sedimentation tank is a sewage treatment system characterized in that the discharge tank to remove the fine water suspended in the sedimentation while remaining in the discharge tank, and only outflow the clear upper water. The method of claim 3, wherein When the size of each tank is based on the central anaerobic tank, the storage tank: anoxic tank: anaerobic tank: first aeration tank: second aeration tank: sedimentation tank and discharge tank are 0.3 -0.7: 1.5-2: 1: 1.0: 2-3: 1 -2: wastewater treatment device, characterized in that the ratio of 0.3-0.7 The method of claim 3, wherein The storage tank, the anaerobic tank, the anaerobic tank, the first and second aeration tanks are sequentially installed, the sewage treatment apparatus characterized in that the sedimentation tank and the discharge tank is installed in parallel to the second aeration tank. The method of claim 3, wherein A waste water treatment apparatus, wherein parallel storage tanks, anoxic tanks, and anaerobic tanks are provided, and first and second aeration tanks are installed in parallel, and sedimentation tanks and discharge tanks are installed in parallel, respectively. The method of claim 3, Carriers installed in the anaerobic tank, the first and the second aeration tank are amorphous, tetrahedral, elliptical, and circular, having a porosity of 30 to 80%, a size of 2 to 20 cm, and a material of wood or modified wood, porous plastic, or lung. A wastewater treatment apparatus characterized by filling powder contact materials such as yoghurt empty bottles, polymer resin fiber yarn, foamed resin such as polyurethane, crushed stone such as basalt or granite, granular activated carbon or sawdust. The method of claim 3, A ratio of the carriers filled in the anaerobic tank, the first and the second aeration tank is composed of 0 to 50%, 50 to 80% and 50 to 80% by volume ratio, respectively.