KR101460958B1 - Appatus for wastewater of used coal ash of coal thermo power plant - Google Patents

Abstract

The present invention relates to a wastewater treatment apparatus for a thermal power plant company, comprising: a filtration tank for separating and discharging sludge by receiving sludge supplied with waste water containing fly ash; filtering the suspended matters contained in the sludge- And an acidity adjusting tank for neutralizing the waste water in a state in which the floating matters are removed from the filtering tank, wherein the filtration tank, the filtering tank and the acidity adjusting tank are connected so that the waste water treatment tank can flow over the tank in order.
Unlike the prior art, unlike the prior art, emergency landfill treatment water treatment facility is installed in order to secure stable operation of the company headquarters and increase sanitary conditions by increasing landfill capacity in the company's premises. As the operation is required, wastewater containing coal ash used as a fuel for the thermal power plant can be passed through functional filtration tank, GFF (Gravity Flow Fiber Filter) and pH adjustment tank, and SS and pH can be treated within legal limits.

Description

[0001] APPARATUS FOR WASTEWATER OF USED COAL ASH OF COAL THERMO POWER PLANT [0002]

The present invention relates to a wastewater treatment apparatus for a thermal power plant company, and more particularly, to an apparatus for treating wastewater discharged from a thermal power plant, more specifically, , The wastewater containing coal ash that has been used as fuel for the thermal power plant is passed through the functional filtration tank, the Gravity Flow Fiber Filter (GFF) and the pH adjustment tank, The present invention relates to a wastewater treatment apparatus of a thermal power plant company capable of treating pH within a legal standard value.

The basic principle of the company's wastewater treatment is that it is filtered after chemical treatment and the pH is neutralized and finally discharged.

However, due to the large amount of water, there are economic problems in chemical treatment and problems of subsequent treatment such as sludge disposal cost.

The secondary problem may not occur much if only the suspended matter can be sufficiently treated by utilizing the characteristics of the company wastewater without chemical treatment. Thus, various methods such as floating pump type treatment, centrifugal separation treatment, and general filter treatment are used.

The background art of the present invention is disclosed in Korean Patent No. 10-0462506 (04.12.09).

Conventional coal fly ash processing equipment for coal-fired power plants basically involves a problem of requiring a large processing space due to the enlargement of landfills and a problem of seawater.

Therefore, there is a need to improve this.

Disclosure of the Invention The present invention has been made in order to solve the above problems, and it is an object of the present invention to provide a GFF (GFF) filtration tank, And to provide a wastewater treatment apparatus.

In order to reduce the flow rate when the filtration tank is introduced into the functional filtration tank, a plurality of partition walls are formed, and through the perforated plate and the partition wall, And an object thereof is to provide a processing apparatus.

The apparatus for treating wastewater of a thermal power plant according to the present invention is characterized by comprising: a filtration tank for separating and discharging sludge by being supplied with waste water containing fly ash; a filter for filtering the suspended matters contained in the waste water in a state in which the sludge is removed from the filtration tank Wherein the filtration tank, the filtering tank, and the acidity adjusting tank are connected in such a manner that the waste water is swept in the order of the waste water treatment tank .

The filtration tank is provided with a first filtration tank for primarily inducing sedimentation of the sludge from the initially introduced filtration treatment water and discharging the sludge from the first filtration treatment tank and a second filtration treatment device for separating and discharging the sludge as much as possible, 2 filtration tank.

The filtration tank is provided with a first water tank having a first inlet at the lower side of the circumferential surface for receiving the treated water and having a first outlet at one side for discharging the precipitated sludge, A plurality of first partition walls for reducing the flow rate of the sludge by reducing the flow velocity of the sludge, and a first partition wall provided at the bottom of the first water tank for preventing the aggregation of sludge by aerating the sludge, .

Wherein the first partition wall is divided into a call barrier wall spaced apart from an inner wall of the first water tank and erected in the first water tank and corresponding to both sides thereof, And flat plate-shaped flat walls spaced apart from each other to correspond to both side edges of the arc partition wall.

Preferably, the arc partition wall and the flat partition wall penetrate the first moving hole so that the settled sludge can be moved toward the first outlet.

The first aeration unit may include a first aeration tank provided in the first tank and open to the upper side and provided with a first opening hole at the lower side of the circumference, a second aeration tank provided in the first aeration tank, And a first perforation nozzle fixed to the upper side of the first aeration tank and passing through the perforation hole and filtering the sludge and suspended solids flowing through the first perforation hole and rising.

The filtration tank includes a second water tank for receiving the treated water, a second partition for changing the flow direction of the supplied treated water to reduce the flow velocity, and a second partition wall provided in the second water tank, And a second width-wise portion for preventing agglomeration.

The filtration tank may include an inlet tank for receiving the sludge separated from the filtration tank and temporarily storing the sludge so as to precipitate the residual sludge, and a plurality of GFF filters for filtering suspended solids from the filtration water flowing in the inflow tank A filter tank, a reverse osmosis water tank for storing reverse osmosis water for backwashing the reverse osmosis treated water that is flooded with the floating matters removed from the filter tank, and a discharge tank for temporarily storing and discharging the ozonized water .

Preferably, the filter tank is provided with a pail to divide the installation space of the GFF filter and allow the filtered treatment water to flow over the filter tank.

Wherein the acidity adjusting tank comprises an adjusting tank for storing the treating water flowing over from the filtering tank for neutralizing the strongly corrosive solution to the treating water and for interrupting the discharge of the neutralized treating water, And an adjusting partition which is arranged alternately in the direction from the inflow side to the discharge side of the water to reduce the flow velocity.

According to the present invention, the wastewater treatment apparatus of a thermal power plant company can increase the removal efficiency of suspended substances only by using a functional filtration tank and a GFF (Gravity Flow Fiber Filter) filtration tank without the disadvantages of chemical treatment and a large space.

It is possible to increase the removal efficiency of suspended solids with only the functional filtration tank and the GFF filtration tank without the disadvantages of the chemical treatment and the wide space.

In addition, the present invention can reduce the load of the GFF by minimizing the flow rate when flowing into the functional filtration tank by passing through a plurality of partition walls and a piercing plate and a partition wall capable of floating fine particulate matter.

1 is a plan view of a wastewater treatment plant of a thermal power plant company according to an embodiment of the present invention.
2 to 14 are sectional views of a wastewater treatment apparatus of a thermal power plant company according to an embodiment of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, an embodiment of an apparatus for treating wastewater from a thermal power plant according to the present invention will be described with reference to the accompanying drawings. In this process, the thicknesses of the lines and the sizes of the components shown in the drawings may be exaggerated for clarity and convenience of explanation. In addition, the terms described below are defined in consideration of the functions of the present invention, which may vary depending on the intention or custom of the user, the operator. Therefore, definitions of these terms should be made based on the contents throughout this specification.

FIG. 1 is a plan view of a wastewater treatment apparatus according to an embodiment of the present invention, and FIGS. 2 to 14 are cross-sectional views of a wastewater treatment apparatus for a thermal power plant according to an embodiment of the present invention.

Referring to FIGS. 1 to 14, a thermal power plant company wastewater treatment apparatus according to an embodiment of the present invention includes a filtration tank 100, a filtering tank 400, and an acidity adjusting tank 500.

In addition, the filtration tank 100, the filtering tank 400, and the acidity adjusting tank 500 of the thermal power plant company wastewater treatment apparatus according to an embodiment of the present invention are connected so that the waste water treatment water flows through the waste water treatment apparatus in order. This is to reduce the size of the company's wastewater treatment plant.

Particularly, the filtration tank 100 serves to separate and discharge the sludge by receiving the filtration water containing fly ash, and the filtration tank 400 is provided in the filtration tank 100 to remove the sludge from the sludge- And the acidity adjusting tank 500 functions to neutralize the waste water in the state where the floating matters are removed from the filtering tank 400 and discharge the treated water.

At this time, although only one filtration tank 100 may be provided, it is preferable that a plurality of filtration tanks 100 are provided in order to improve the degree of sedimentation of the sludge and filter sludge as much as possible.

For convenience, the filtration tank 100 is shown as being provided with two adjacently connected.

That is, the filtration tank 100 includes a first filtration tank 200 and a second filtration tank 300.

The first filtration tank 200 first induces sedimentation of the sludge from the initially introduced sludge treatment water and discharges the sludge from the first sludge treatment tank 200 to the second filtration tank 300, Thereby separating and discharging the sludge as much as possible.

The first filtration tank 200 includes a first water tank 210, a first partition 220 and a first partition 230.

The first water tank 210 forms an outer shape of the first filtration tank 200, and has a first inlet 212 at a lower side of the circumferential surface to receive the water to be treated. The first water tank 210 forms a first outlet 214 on one side for discharging the settled sludge.

Of course, the first inlet 212 and the first outlet 214 are not limited to the number and the position formed in the first water tank 210. Of course, it is preferable that the first inlet 212 and the first outlet 214 are automatically opened and closed by a valve.

At this time, the treatment water flows into the first water tank 210 at a high speed through a first inlet 212 by a pump (not shown). In this case, the flow of the treatment water is fast and the sludge is not easily settled.

Accordingly, the first water tank 210 is provided with the first partition 220.

The first partition wall 220 is provided in the first water tank 210 to reduce the flow rate of the forcible water to be forced into the first tank tank 210 to improve the sedimentation speed of the sludge. The first partition wall 220 may be provided in the first water tank 210, but it is preferable that a plurality of the first partition walls 220 are provided to minimize the flow rate of the rotary treatment water.

That is, the first partition 220 includes a call partition 222 having a flat trajectory and a flat partition 224 having a flat plate shape.

The call partition wall 222 is installed on the bottom of the first water tank 210 so that the treatment water flowing at a high speed into the first inlet 212 hits the first time. The arc partition wall 222 is spaced apart from the inner wall of the first water tank 210 to which both sides of the water barrier tank 222 correspond, so that the treatment water that has lost a predetermined kinetic energy flows. Particularly, the arc partition wall 222 collides with the circulating water flowing back toward the first inlet 212 and flows into the first inlet 212, and is formed in a planar arc shape to further reduce energy.

In addition, the flat partition wall 224 is provided on the rear side of the call partition wall 222 with respect to the inflow direction of the treatment water for once more reducing the flow rate of the treatment water. At this time, the flat partition wall 224 is formed in a flat plate shape.

The flat partition wall 224 is provided in the first water tank 210 so as to be spaced apart from the rear side of the arc partition 222 by a predetermined distance. The flat partition wall 224 is spaced apart from each other so as to partially overlap with both side edges of the arc partition wall 222. That is, the arc partition wall 222 and the flat partition wall 224 are staggered to minimize the clearance of the treated water.

Of course, the call partition wall 222 and the flat partition wall 224 can be deformed into various shapes.

In addition, the sludge settled on the bottom of the first filtration tank 200 can not flow to the first discharge port 214 due to the arc partition wall 222 and the flat partition wall 224. Thus, the arc partition wall 222 and the flat partition wall 224 pass through the first movement hole 226 so that the settled sludge can be moved toward the first discharge port 214. [ At this time, the size and shape of the first moving hole 226 are not limited.

Meanwhile, the first aeration part 230 is provided in the first water tank 210 so as to augment the decanted processing water passing through the first partition 220. Thus, the first aeration portion 230 aids the treatment water to prevent sludge from clumping.

The first aeration part 230 includes a first aeration tank 232, a first aeration nozzle 234, and a first perforated plate 236.

The first aeration tank 232 is provided inside the first water tank 210 and opens upward. The first aeration tank 232 penetrates through the first opening 233 below the circumferential surface. At this time, the first aeration tank 232 can be deformed into various shapes.

The first aeration nozzle 234 is provided inside the first aeration tank 232. At this time, the first aeration nozzle 234 is provided on the bottom surface of the first tank 210 or the bottom surface of the first aeration tank 232, and injects the supplied air into the processing water. The shape and the number of the first aeration nozzles 234 are not limited.

The first perforated plate 236 is fixed on the upper side of the first aeration tank 232. At this time, the first pier plate 236 is bound to the first aeration tank 232 by various binding methods.

In addition, the first perforated plate 236 penetrates the perforation hole to reduce the spraying force due to the flow of air and the treatment water and the impact of air.

The first pier plate 236 passes the air and the pouring water through the perforation holes, but the sludge and suspended solids flowing into the interior through the first open hole 233 formed in the first aeration tank 232, It gets caught. Accordingly, the sludge and suspended solids contained in the pumped water are attached to the first pier plate 236 to be predetermined.

Accordingly, the first perforated plate 236 must be cleaned periodically or intermittently. Of course, the first perforated plate 236 can be cleaned by various methods such as washing water injection.

On the other hand, the second filtration tank 300 is disposed adjacent to the first filtration tank 200, and the sludge and suspended solids are partially received in the first filtration tank 200.

Accordingly, the flow channel 110 is recessed at the connection portion between the first filtration tank 200 and the second filtration tank 300.

Particularly, the second filtration tank 300 includes a second water tank 310, a second partition 320, and a second partition 330.

The second water tank (310) is connected to the first water tank (210) and is integrally formed. Thus, the flow grooves 110 are formed at the same corners of the first water tank 210 and the second water tank 310.

Thus, the sludge and suspended solids, which are primarily filtered in the first tank 210, are supplied to the second tank 310 through the sluice grooves 110.

Of course, the second water tank 310 can be deformed into various shapes.

In addition, the second water tank 310 has a second outlet 312 for discharging sludge that is secondarily filtered. It is preferable that the second outlet 312 is provided so as to be opened and closed.

The second partition 320 is installed in the second water tank 310 so as to slow the flow rate by changing the flow direction of the supplied water.

The second partition 320 may be provided in the second water tank 310 so that the overflowing water may flow through the first water tank 110. For convenience, one second barrier rib 320 is shown. Of course, the second bank 320 can be modified into various shapes.

The second vent pipe 330 is provided at the bottom of the second water tank 310 to prevent the sludge from being clumped by aeration of the treated water decelerated by the second partition 320.

In particular, the second aeration portion 330 includes a second aeration tank 332, a second aeration nozzle 334, and a second perforated plate 336.

The second aeration tank 332 is provided inside the second water tank 310 and opens upward. In addition, the second aeration tank 332 passes through the second opening hole 333 below the circumferential surface. At this time, the second aeration tank 332 can be deformed into various shapes.

The second aeration nozzle 334 is provided inside the second aeration tank 332. At this time, the second aeration nozzle 334 is disposed on the bottom surface of the second tank tank 310 or the bottom surface of the second aeration tank 332, and injects the supplied air into the processing water. The shape and the number of the second aeration nozzles 334 are not limited.

The second perforated plate 336 is fixed on the upper side of the second aeration tank 332. At this time, the second pier plate 336 is bound to the second aeration tank 332 by various binding methods.

In addition, the second perforated plate 336 penetrates the perforation hole to reduce the spraying force due to the flow of the air and the treatment water and the impact of the air.

The sludge and suspended solids flowing into the second pore plate 336 through the second opening hole 333 formed in the second aeration tank 332 pass through the pore hole 333, It gets caught. Accordingly, the sludge and suspended matters contained in the treated water are attached to the second perforated plate 336 to be filtered as much as possible.

Accordingly, the second perforated plate 336 must be cleaned periodically or intermittently. Of course, the second perforated plate 336 can be cleaned by various methods such as washing water injection.

The filtering tank 400 serves to filter the floating matters suspended in the treated water in a state where the sludge is removed while passing through the first filtration tank 200 and the second filtration tank 300. At this time, the filtering tank 400 includes a plurality of GFF filters (Gravity Flow Fiber Filter) 422 to improve the degree of filtering of floating matters. In particular, as the sludge is passed through the GFF filter 422 with the sludge being separated and discharged as much as possible, the load of the GFF filter 422 is reduced.

The filtering tank 400 includes an inlet tank 410, a filter tank 420, a reverse osmosis tank 430, and a discharge tank 440.

The inflow tank 410 serves to temporarily sink the residual sludge by temporarily storing the treated water separated from the sludge while passing through the first filtration tank 200 and the second filtration tank 300.

As the second filtration tank 300 is formed with the rim grooves 110 in the rim, the rinse water flows into the inflow tank 410 through the rim grooves 110. Of course, the inflow tank 410 can be deformed into various shapes.

In addition, the filter tank 420 is supplied with the circulating water flowing in the inflow tank 410, and has a plurality of GFF filters 422 for filtering suspended matters from the circulating water.

In addition, the reverse oily water tank 430 serves to store reverse osmosis water in order to back up the water to be treated overflowed in the state in which the floating matters are removed from the GFF filter 422 in the filter tank 420. Reverse sea water can be applied in various ways such as purified water.

In addition, the discharge tank 440 temporarily stores the circulating water that is overflowed in a backwashed state, and sinks the foreign substances contained therein, and discharges the purified white water.

Here, 'discharge' means that the rotary process water flows over the upper side of the discharge tank 440 and flows to the acidity adjustment tank 500.

At this time, the second water tank 310, the inflow tank 410, the filter tank 420, the reverse osmosis water tank 430, and the discharge tank 440 are connected in order to flow the waste water.

In addition, the filter tank 420 is provided with a flow-through jaw 424 for partitioning the installation space of the GFF filter 422 and for overflowing the filtered treatment water. As a result, the rotary treatment water is purified to the maximum extent.

On the other hand, the acidity adjusting tank 500 serves to neutralize the waste water in the state where the floating matters are removed from the filtering tank 400.

The acidity adjusting tank 500 includes an adjusting tank 510 and an adjusting partition 520.

The adjustment tank 510 stores the pumped water to be flowed from the discharge tank 440 of the filtering tank 400 so as to neutralize the pumped water with the strong acid solution, and controls the discharge of the neutralized pumped water . The adjustment tank 510 has a discharge port 512 so as to be openable and closable, and controls the discharge of the purified and neutralized treated water.

The adjusting partition 520 is disposed in the adjusting tank 510 in a staggered direction from the inflow side to the inflow side of the rotary treatment water to reduce the flow velocity. This is to reduce the flow rate of the treatment water to be mixed with the strong acid solution to be neutralized.

Of course, the adjustment partition 520 can be formed in various shapes and arranged.

While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it will be understood by those of ordinary skill in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims. I will understand. Accordingly, the true scope of the present invention should be determined by the following claims.

100: Filtration tank 200,300: First and second filtration tank
210, 310: first and second tank tanks 220, 320:
230, 330: first and second width bases 400:
410: inlet tank 420: filter tank
422: GFF filter 430: reverse osmosis tank
440: discharge tank 500: acidity adjusting tank
510: adjusting tank 520: adjusting partition

Claims (10)

A filtration tank for collecting and discharging the sludge by receiving the filtration water containing fly ash;
A filtration tank for filtering the suspended matters contained in the treated water in a state where the sludge is removed from the filtration tank; And
And an acidity adjusting tank for neutralizing the waste water in a state where the floating matters are removed from the filtering tank,
Wherein the filtration tank, the filtering tank,
Wherein the filtering tank comprises: an inflow tank for sinking the residual sludge by temporarily storing the sludge separated from the filtration tank; And
And a filter tank having a plurality of GFF filters for filtering suspended solids from the waste water flowing in the inflow tank.
The filtration apparatus according to claim 1,
A first filtration tank for primarily inducing sedimentation of the sludge from the first treated water to be treated; And
And a second filtration tank for separating and discharging the sludge as much as possible by inducing sedimentation of the sludge from the filtration water flowing over from the first filtration tank.
The filtration apparatus according to claim 1 or 2,
A first water tank having a first inlet at a lower side of the circumferential surface to receive the treated water and having a first outlet at one side for discharging the settled sludge;
A plurality of first diaphragms provided in the first water tank for reducing the flow rate of forcedly flowing water to improve the settling velocity of the sludge; And
And a first aeration unit provided in the first tank to prevent sludge from being clumped by aeration of the treated water.
The plasma display panel of claim 3,
A barrier rib formed on the first water tank and spaced apart from an inner wall of the first water tank corresponding to the first water tank, And
And a flat plate-like flat partition wall spaced apart from each other so as to correspond to both side edges of the arc partition wall to reduce the flow velocity of the rotary treatment water once more.
5. The method of claim 4,
Wherein the arc partition wall and the flat partition wall penetrate the first transfer hole so that the settled sludge can be moved in the direction of the first discharge port.
The air conditioner according to claim 3,
A first aeration tank which is provided in the first water tank and opens to the upper side and has a first opening hole at the lower side of the circumference;
A first aeration nozzle provided in the first aeration tank for spraying air into the treatment water; And
And a first perforated plate fixed to the upper surface of the first aeration tank and passing through the perforated hole and filtering the sludge and floating matters flowing through the first open hole to ascend. Device.
The filtration apparatus according to claim 1 or 2,
A second water tank for receiving the treated water;
A second diaphragm for changing a flow direction of supplied circulating water to decelerate the flow velocity; And
And a second aeration unit provided in the second tank to prevent sludge from being bunched by aeration of the treated water.
The filtering apparatus according to claim 1,
A backwash water tank for storing backwash water to backwash the treated water flowing over the filter tank in a state that the floating matter is removed from the filter tank; And
Further comprising a discharge tank for temporarily storing and discharging the waste water treated in a backwash process state.
The method according to claim 1,
Wherein the filter tank is provided with a paddle to divide the installation space of the GFF filter and to flow the filtered treatment water overflow.
9. The process according to claim 1 or 8,
A regulating tank for storing the pumped water flowing from the filtering tank so as to neutralize the strongly pumped liquid into the pumped water and controlling the discharge of the neutralized pumped water; And
And an adjusting partition wall disposed in the adjustment tank so as to be offset from each other in the direction from the inflow side to the outflow side of the rotary treatment water to reduce the flow velocity.

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