KR200439298Y1 - microbe reactor - Google Patents

Abstract

The present invention is arranged in parallel to the inside of the main body while indenting the bottom of the main body in a conical or polygonal shape in order to improve the mixing power with the waste water inside the main body when forcedly ejecting the raw water containing the air flowing into the main body in the downward direction By placing the protrusions and the indents formed in each of the retention delay members to be perpendicular to each other, the residence time of the air is increased, and the adsorption member is placed inside the main body to promote the adsorption of microorganisms, thereby promoting the decomposition of organic matter and promoting the growth of the wastewater. Sludge relates to a microbial reaction stirrer which filters and removes by using desorption air.

Microbial reaction stirrer, retention delay member, adsorption part, media

Description

Microbe reactor

1 is a front view of a conventional microbial reaction stirrer.

Figure 2 is a plan view of a conventional microorganism reaction high stage.

Figure 3 is a side cross-sectional view of a conventional microbial reaction stirrer.

4 is a front view of the microbial reaction stirrer according to the present invention.

Figure 5 is a side cross-sectional view of a microbial reaction stirrer according to the present invention.

Figure 6 is a perspective view showing the installation of the stay delay member provided in the microbial reaction stirrer according to the present invention.

Figure 7 is a state diagram of the adsorption unit installed inside the microbial reaction stirrer according to the present invention.

* Description of the symbols for the main parts of the drawings *

1,100: main body 2,102: denitrification tank

4,104: activator 6,106: nitrification tank

12,112: raw water inlet pipe 16,116: air inlet pipe

108: inlet 110: outlet

130: blowout pipe 200: bottom depression

300: retention delay member 400: adsorption portion

410: frame 420: hanger bar

430: attachment member

The present invention relates to a microbial reaction stirrer, and more particularly conical or polygonal shape of the bottom of the main body in order to improve the mixing power with the waste water inside the main body when forced ejection of raw water containing air flowing into the main body in the downward direction In addition to the depression, the protrusions and the indentations formed in each of the staying delay members arranged in parallel to the inside of the body are disposed perpendicular to each other to increase the residence time of the air, and the adsorption member is placed inside the body to induce the adsorption of microorganisms. The present invention relates to a microbial reaction stirrer that promotes organic decomposition and purifies sludge from wastewater by inducing desorption using air for desorption.

Conventionally, only livestock wastewater is removed from the livestock wastewater, and the microbial treatment tank is transferred to the original wastewater for biological treatment, or after removing the contaminants from the livestock wastewater, centrifugation is performed again in a centrifuge to remove considerable amounts of organic matter and nitrogen. The pollution load was reduced and then treated in a microbial treatment tank.

The microbial treatment tank removes organic matter and nitrogen from livestock wastewater by using the metabolic activity of microorganisms. In general, the microbial treatment tank is operated by aerobic and anaerobic operation periods for a predetermined time period. Decomposition and nitrification proceeds, and during the anaerobic operation, denitrification and organic matter decomposition proceed, and the nitrogen component in the livestock wastewater becomes N ₂ gas, which is reduced and removed to the atmosphere, thereby decomposing a part of organic matter.

In the Utility Model Registration No. 0415478 registered by the applicant, a high rate microbial reaction stirrer for purifying wastewater and high concentration organic wastewater has been proposed.

1 to 3 is a view showing the microorganism reaction stirrer.

As shown in the drawing, the conventional microbial reaction stirrer is shaped into a main body 1 partitioned into a denitrification tank 2, an activation tank 4, and a nitrification tank 6.

The main body 1 includes a raw water inlet pipe 12.

At this time, each of the raw water inlet pipe 12 is provided with a raw water control valve 13 to regulate the flow control and flow amount of the raw water.

In addition, the main body 1 is provided with an internal conveying pipe 14 to convey raw water.

At this time, the inner conveying pipe 14 is provided with an inner conveying liquid control valve 15 to control the return of raw water.

In addition, the main body 1 is provided with an air inlet pipe 16 to inject air into the inside and to activate and purify the waste water inside the main body 1 with microorganisms.

In addition, the air inlet pipe 16 is provided with an air control valve 17 to control the flow state and flow amount of air.

In addition, the main body 1 is provided with a discharge pipe (19).

Then, the ejector 30 is provided at a portion where the raw water inlet pipe 12 and the air inlet pipe 16 are combined.

In addition, the main body 1 includes submersible air pumps 42, 44, and 46 inside the reaction tanks 2, 4, and 6, respectively, and submersible air pumps 42, 44, 46 and air inlet pipes. 16 is connected to the air inlet hoses 52, 54, 56.

And, the main body 1 is provided with a sludge discharge port 60 in the lower portion to discharge the sludge generated and sinking during the purification of the waste water to the outside.

On the other hand, the denitration reaction tank 2, the activation tank 4, and the nitrification reaction tank 6 are provided with the guide plate 100 in all or any one inside.

In addition, between the guide plate 100 and the inner wall of each of the reaction tanks 2, 4 and 6, the upper and lower layers communicate with each other to secure the flow path 102 to allow the wastewater treatment liquid to flow.

In particular, the flow paths 102 formed between the guide plates 100 and the inner walls of the reaction tanks 2, 4, and 6 are alternately provided in the up and down directions, thereby reducing the residence time of the waste water between the guide plates 100. Delayed to increase microbial activity.

On the other hand, the guide plate 100 is installed to be inclined symmetrically to each other in the longitudinal direction.

In addition, the main body 1 is provided with a circulation pipe 110 to circulate the wastewater treatment liquid of each of the denitration reaction tank 2, the activation tank 4 and the nitrification reaction tank 6.

However, the conventional wastewater and high concentration organic wastewater purification microorganism reaction stirrer sprays raw water mixed with air through the piping in the horizontal direction to the bottom surface of the main body, so that the air having a relatively low specific gravity rises simultaneously with the inside of the wastewater. There was a problem in that the mixing force with the lowering, thereby lowering the microbial activation.

In addition, the conventional microbial reaction stirrer has a problem that the microbial activation degree is reduced because the amount of air gathered in a limited corner portion of one guide plate is installed obliquely inside the body by forming the guide plate in a plate shape.

The present invention is devised to solve the above problems, the object of the present invention is to form a conical or polygonal cone shape of the bottom of the main body for ease of mixing with the waste water when forced ejection of raw water, including air in the vertical direction By forming the bottom depression of the side, and by placing the retardation member in parallel with the inside of the main body to sufficiently increase the residence time of the air and to provide the adsorption unit inside the main body to further increase the microbial activation by attaching sludge. A microbial reaction stirrer is provided.

The present invention for achieving the above object is to store the waste water therein, the denitrification tank, the activation tank, the nitrification tank is partitioned continuously connected to each other and each raw water containing the air is injected into the reaction tank to blow down In order to form an inlet and to discharge the purified wastewater treatment liquid, and to form a bottom depression having a bottom concave or conical in the shape of a conical or polygonal pyramid, and to increase the residence time of the air moving in the discharge pipe direction It is arranged in a plurality of layers and at the same time to be spaced apart at a certain interval on the same layer to the retention delay member connected to each inner surface of the reactor, and the discharge pipe and the retention delay member provided in the main body corresponding to the retention delay member It comprises an adsorption unit for attaching sludge contained in Placing the upper and the lower the residence delay member in a direction that is perpendicular to each other characterized in that it maximizes the residence time of the air.

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

4 is a front view of the microbial reaction stirrer according to the present invention, Figure 5 is a side cross-sectional view of the microbial reaction stirrer according to the present invention.

And, Figure 6 is a perspective view showing the installation of the retention delay member provided in the microbial reaction stirrer according to the present invention, Figure 7 is a state diagram of the adsorption unit installed in the microbial reaction stirrer according to the present invention.

4 and 5, the microbial reaction stirrer according to the present invention is divided into a denitrification tank 102, an activation tank 104, a nitrification reactor 106 to gradually purify the waste water stored therein. Appears as 100.

The main body 100 is arranged in the transverse direction in order to the denitration reaction tank 102, the activation tank 104, the nitrification reaction tank 106, and connects the respective reaction tanks (102, 104, 106) to the circulation pipe (107).

Here, the denitrification reactor 102 is a reaction tank for nitrifying the nitrate nitrogen which is nitrified in the stored waste water and returned inside.

In addition, the activation tank 104 is a reaction tank that decomposes organic matter and nitrates ammonia nitrogen in a waste water introduced after denitrification in a denitrification reaction 102 through a circulation pipe 107 for a predetermined time, and the nitrification reaction tank 106. Is a reaction tank that denitrates the remaining organic matter after nitrifying the ammonia nitrogen in the wastewater introduced after nitrifying in the activation tank 104 through the circulation pipe 107 for a predetermined time.

At this time, the activation tank 104 is preferably connected to two in series in order to sufficiently nitrify the ammonia nitrogen in the waste water.

Of course, the denitrification tank 102 and the nitrification tank 106 are also preferably connected in series.

At this time, the upper portion of the denitrification tank 102 and the lower portion of the activation tank 104 are connected to each other by the circulation pipe 107, likewise, the upper portion of the activation tank 104 and the lower portion of the nitrification reactor 106 are circulation pipe 107 is connected to each other.

In other words, the circulation pipe 107 sends the wastewater treatment liquid in a denitrification state for a predetermined time to the activating tank 104 in the denitrification tank 102, and in the wastewater introduced from the activating tank 104. After decomposing the organic material for a certain time and nitrifying the ammonia nitrogen, the remaining organic material is flowed into the nitrification tank 106 to activate microorganisms.

In addition, the main body 100 forms an inlet 108 at the lower circumference, and forms a discharge pipe 119 at the upper circumference.

For convenience, only the denitrification tank 102 is shown in FIG. 5 and will be mainly described.

On the other hand, the raw water inlet pipe 112 is inserted into the inlet 108 of the main body 100.

At this time, the main body 100 forms an inlet 108 around the denitrification tank 102 and inserts a raw water inlet pipe 112 into the inlet 108.

Since the main body 100 stores the waste water therein, it is natural to seal the gap generated by the inlet 108 and the raw water inlet pipe 112.

The raw water inlet pipe 112 is connected to the denitrification tank 102 to supply raw water.

At this time, the raw water inlet pipe 112 is provided with a raw water control valve 113 to adjust the flow control and flow rate of the raw water.

In particular, the raw water inlet pipe 112 is connected to each other by the air inlet pipe 116 at the same time.

Thus, each of the raw water inlet pipe 112 mixes the raw water and the air introduced through the air inlet pipe 116 to guide the inside of the main body 100.

In addition, the air inlet pipe 116 is extended to the desorption pipe 118 is inserted into the denitrification tank 102.

The desorption pipe 118 serves to induce desorbing sludge adsorbed to the adsorption unit 400 by directly ejecting external air to the adsorption unit 400 which will be described later when the air pump 140 operates.

Of course, the desorption pipe 118 is provided with an on-off valve 119 to open and close the desorption pipe 118 as necessary.

The air flowing into the body 100 serves to activate and purify the waste water inside the body 100 as microorganisms.

In addition, the air inlet pipe 116 is provided with an air control valve 117 to control the flow state and flow amount of air.

In addition, the raw water inlet pipe 112 is provided with an air pump 140, the air pump 140, the operation of the denitrification tank 102 through the supply of external air and raw water and the self-circulation of the internal fluid during operation. Each of the activating tank 104 and the nitrification tank 106 causes the flow of wastewater treatment liquid.

In this case, the wastewater treatment liquid refers to a liquid purified according to microorganism activation in a state in which wastewater, air and raw water are mixed.

On the other hand, the raw water inlet pipe 112 extending from the air pump 140 connected to the nitrification tank 106 and the raw water inlet pipe 112 extending from the air pump 140 connected to the denitrification reactor 102 is a supply pipe 122 ).

Here, since the microorganism-activated treated water flows through the raw water inlet pipe 112 extending from the air pump 140 connected to the nitrification reactor 106, the denitrification reaction tank is moved as the treated water is moved to the denitrification reactor 102. 102) Denitrification of the internally treated water is improved.

The supply pipe 122 is provided to supply the nitrified wastewater and air directly to the denitrification tank 102 when the denitrification reaction does not have to be performed.

In addition, the main body 100 is provided with a drain pipe 120 at the bottom.

At this time, at least three outlets 110 are formed in the main body 100 to discharge nitrogen in the gas state, denitrified nitrogen, and carbon dioxide generated by decomposition of organic matter, which are generated in each reaction tank 102, 104, and 106 and have a lower specific gravity than liquids. Is provided, the discharge pipe 119 is formed to discharge the purified wastewater treatment liquid, the drain pipe 120 is provided to discharge the sludge in the lower body 100 corresponding to the circumference of each reactor (102, 104, 106) do.

At this time, the discharge pipe 119 may be formed on the upper circumferential surface of each reaction tank (102, 104, 106), but is preferably formed only on the upper circumferential surface of the nitrification reactor 106 for finally purifying the waste water.

In particular, the discharge pipe 130 is formed extending in the lower direction at the end of the raw water inlet pipe 112 located inside the main body 100.

This improves the solubility of air and water by forcibly ejecting water and air introduced through the raw water inflow pipe 112 toward the bottom of the main body 100 using the air pump 140 and sludge accumulated on the bottom of the main body 100. This is to increase the mixing of air and air.

In addition, the ejection pipe 130 forms a tubular ejection guide member 160 having a lower end diameter at the end thereof.

The jet guide member 160 serves to further improve the ejection and agitation of the waste water and air and raw water by forcibly flowing the waste water from the upper side to the lower direction when the raw water including the air is ejected through the ejection pipe 130.

Here, the ejection guide member 160 is connected and fixed to the ejection pipe 130 by a plurality of ribs 162.

In particular, the jet guide member 160 has a cylindrical shape to reduce the diameter of the lower end portion to increase the output power.

In addition, an ejector 150 is provided at a connection portion of the raw water inlet pipe 112 and the air inlet pipe 116, which ejector 150 efficiently mixes raw water and air to maximize oxygen dissolution efficiency. Device.

On the other hand, the main body 100 forms a bottom depression 200 in which the bottom surface is concave in the shape of a cone or a polygonal pyramid.

The reason why the bottom recessed part 200 is formed is as air and water ejected to the center of the bottom of the bottom recessed part 200 through the ejection pipe 130 are evenly guided to the entire side of the bottom recessed part 200. This is to increase the microbial activity by supplying air all over the inside of the sludge.

In particular, the bottom recess 200 may be formed in a conical or polygonal shape over the entire body bottom surface, but is preferably formed for each bottom surface of each reactor (102, 104, 106).

At this time, the drain pipe 120 is preferably connected to the bottom of the bottom depression (200).

In addition, the reactor (102, 104, 106) of the main body 100 has a retardation member 300 in parallel with each other or in any one of the interior.

Of course, the retention delay member 300 is preferably provided in all the reaction tank (102, 104, 106).

In addition, the retention delay member 300 partitions the layer for the retention of the wastewater treatment liquid by arranging the plurality of layers in the longitudinal direction of each of the reaction tanks 102, 104, and 106.

In particular, the staying delay member 300 is provided to be connected to the both ends of the reaction tank 102 by welding or the like.

Thus, the stay retardation member 300 guides air and wastewater therebetween as it is arranged spaced apart from each other in the same layer.

Here, the retention delay member 300 increases the air residence time in the reaction tank 102 as the bottom delay recess 300 is formed in the shape of a hat shade formed with the concave portion 310.

In addition, as shown in Figure 6, the retention delay member 300 is arranged in a direction perpendicular to each other in the longitudinal direction can maximize the residence time of the air.

Thus, microbial activity is enhanced.

On the other hand, the main body 100 is provided with an adsorption unit 400 to filter the sludge contained in the wastewater treatment liquid therein.

The adsorption unit 400 is mounted on at least one of all the reaction tanks 102, 104, and 106, and is preferably formed in the main body 100 adjacent to the discharge pipe 119.

As illustrated in FIG. 7, the adsorption unit 400 includes a frame 410 having a hexahedron shape, a hanger bar 420 and the hooks disposed in the same direction on the upper and lower sides of the frame 410. It consists of an attachment member 430 for attaching the sludge to the bar 420.

At this time, the hook bar 420 forms a hook groove 422 along the axial direction to allow the attachment member 430 to be hooked.

The hanger 420 may be fixed to the frame 410 by welding or the like, or may be detachably mounted by bolting or the like.

Although not shown, the attachment member 430 is preferably made of a general media consisting of a loop that is a screen and a yarn provided around the loop to attach sludge.

Thus, the loop of the attachment member 430 is wound around the hook groove 422.

Although not shown, both ends of the attachment member 430 may be fixed to the hook groove 422 of the hook bar 420, respectively, or may be fixed by a band cable.

In particular, the frame 410 is provided with a fastening piece 510 having a fastening hole 512 at the upper edge, and the fastening piece 510 is fastened by a fastening member 520 inserted into the fastening hole 512. It is preferable that the main body 100 is detachably fastened.

The reason why the attachment member 430 attaches the sludge is to activate decomposing and purifying organic substances by reducing the detachment of microorganisms in the wastewater treatment liquid.

On the other hand, the main body 100 is preferably to support the frame 410 by forming a support jaw 440 on the inner surface.

In this case, the support jaw 440 preferably supports the lower side of the frame 410.

And, although not shown, in order for the attachment member 430 to be installed in the main body 100, it is preferable to form the upper surface of the main body 100 to be opened and closed.

As described above, the microbial reaction stirrer according to the present invention mutually increases the amount of infiltration of air into the sludge by the bottom surface concave in conical or polygonal shape when spraying raw water mixed with air in the vertical direction, which is the bottom surface direction of the main body. There is an effect of improving the stirring force.

In addition, the present invention has the effect of maximizing the residence time of the air in the waste water by arranging the independent staying delay members connecting both ends to the tank inner surface in the shape of a hat shade in the direction perpendicular to each other in the upper and lower layers.

In addition, the present invention has an effect that can improve the organic purification decomposition power by filtering the sludge contained in the waste water by having an adsorption unit inside the body.

Claims (3)

The waste water is stored inside, and the denitrification tank, the activation tank, and the nitrification tank are continuously connected to each other, and the raw water including air is injected into each of the reaction tanks to form a inlet to be discharged in a downward direction and to purify them. A main body having a discharge pipe for discharging the wastewater treatment liquid thus formed, the bottom recess having a bottom recessed in a conical or polygonal shape; A retention delay member connected to each inner side of the reaction tank so as to be arranged in a plurality of layers and spaced apart at a predetermined interval on the same layer to increase the residence time of the air moving in the discharge pipe direction; It is provided inside the main body corresponding to the discharge pipe and the retardation delay member comprises an adsorption unit for attaching the sludge contained in the wastewater treatment liquid, The retention delay member is a microbial reaction stirrer, characterized in that the upper and lower layers are arranged in a direction perpendicular to each other to maximize the residence time of the air. The method of claim 1, The adsorbing unit is formed in a hexahedral frame shape and supported by a support jaw protruding from the inner surface of the main body; Hanger bars arranged side by side in the same direction in the upper and lower sides of the frame, respectively recessed hanger grooves; Microbial reaction stirrer comprising an attachment member for alternately wound around the hook groove of the pair of hanger bar side by side in the vertical direction of the frame. The method of claim 2, The frame has a fastening piece having a fastening hole in the upper edge; The fastening piece is a microbial reaction stirrer, characterized in that the fastening member is detachably fastened by the fastening member inserted into the fastening hole.

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