JP2007253052A - Equipment and method for water cleaning - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide equipment for water cleaning, in which a return water to be returned from a Mn removal tank to a water arriving well is neutralized effectively, so that the amount of an oxidizer to be used in the water arriving well can be reduced. <P>SOLUTION: The equipment for water cleaning is provided with: the water arriving well 4 in which raw water for water cleaning is received; a precipitation basin 6 for precipitating suspended matter contained in the raw water and removing the precipitated suspended matter; a water treatment facility 8 for treating the supernatant water from the precipitation basin as required; a concentration tank 10 for concentrating sludge in the supernatant water separated in the precipitation basin 6; a dehydrator 14 for dehydrating the concentrated sludge separated in the concentration tank 10; the Mn removal tank 12 for removing a manganese component contained in the supernatant water in the concentration tank 10; and a return line 19 for returning the return water from the Mn removal tank 12 to the water arriving well 4. A neutralization tank 20 is arranged on the return line 19. Waste combustion gas from a gas engine or a gas turbine or the carbonated water produced by utilizing the waste combustion gas is supplied to the neutralization tank 20, so that the return water is neutralized by the supplied waste combustion gas or carbonated water in the neutralization tank 20. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a water purification treatment facility and a treatment method for treating purified water as required.

  Water treatment equipment that treats raw water from the settling basin as required, as well as a landing well that takes raw water for water purification, a sedimentation basin that precipitates and removes suspensions contained in the raw water, And a concentration tank for concentrating the water sludge separated in the sedimentation basin and a dehydrator for dewatering the concentrated sludge separated in the concentration tank, and returning the supernatant water from the concentration tank to the landing well What was made is known (for example, refer patent document 1). In addition, since manganese components are included in the return water returned from the concentration tank to the receiving well, a Mn removal tank is provided between the concentration tank and the receiving well, and is included in the returned water in this Mn removal tank. There is also known one that removes the manganese component. There is also known one in which the dewatered separation water from the dehydrator is returned to the concentration tank. The removal of the manganese component in this water purification treatment facility is carried out by adding an alkali agent to the Mn removal tank and removing it in the form of manganese hydroxide in an alkaline atmosphere. After removing the manganese component in this way, the return water is returned to the landing well. Will be returned.

JP 11-347595 A

  However, the above-described water purification equipment has the following problems to be solved. The return water from which the manganese component has been removed in the Mn removal tank exhibits alkalinity, and this alkaline return water is returned to the landing well. In addition, the raw water taken into the landing well often exhibits weak alkalinity (about pH 7-8) due to assimilation of aquatic plants and the like, and the alkalinity tends to be somewhat stronger in summer. On the other hand, it is desirable to adjust the pH to be weakly acidic in the landing well in order to efficiently remove suspended matter in the raw water and to suppress the generation of bromic acid during ozone treatment in the water treatment facility. .

  For this reason, conventionally, an acid agent such as sulfuric acid is administered to the landing well to adjust the pH, but in such pH adjustment, the raw water and the return water are adjusted at the landing well. Since both are performed, there is a problem that the amount of the acid agent used in the landing well increases and the cost of the water purification treatment increases.

  An object of the present invention is to provide a water purification treatment facility and a treatment method capable of effectively neutralizing the return water returned from the Mn removal tank to the landing and reducing the amount of the acid agent in the landing well. That is.

The water purification treatment facility according to claim 1 of the present invention requires a landing well that takes in raw water for water purification, a sedimentation basin that precipitates and removes suspensions contained in the raw water, and water from the sedimentation basin. A water treatment facility for water treatment on the street, a concentration tank for concentrating the water sludge separated in the sedimentation basin, a dehydrator for dewatering the concentrated sludge separated in the concentration tank, and a supernatant of the concentration tank A water purification treatment facility comprising a Mn removal tank for removing manganese components contained in water, and a return line for returning return water from the Mn removal tank to the landing well,
The return line is provided with a neutralization tank, and combustion exhaust gas from a gas engine or a gas turbine is supplied to the neutralization tank. In this neutralization tank, return water from the Mn removal tank is contained by the combustion exhaust gas. It is characterized by being summed.

Moreover, the water purification treatment facility according to claim 2 of the present invention includes a landing well that takes in raw water for water purification, a sedimentation basin that precipitates and removes suspensions contained in the raw water, and water from the sedimentation basin. Water treatment equipment for water treatment as required, a concentration tank for concentrating water sludge separated in the settling basin, a dehydrator for dewatering the concentrated sludge separated in the concentration tank, and the concentration tank A water purification treatment facility comprising a Mn removal tank that removes the manganese component contained in the supernatant water, and a return line that returns the return water from the Mn removal tank to the landing well,
The return line is provided with a neutralization tank, and carbonated water obtained from combustion exhaust gas from a gas engine or gas turbine is supplied to the neutralization tank. In this neutralization tank, the return water from the Mn removal tank Is neutralized with the carbonated water.

  Further, in the water purification treatment facility according to claim 3 of the present invention, the carbonated water condenses the combustion exhaust gas from the gas engine or the gas turbine to obtain carbonated water, or the combustion exhaust gas. It is produced | generated using the melt | dissolution apparatus for melt | dissolving and obtaining carbonated water.

  Further, in the water purification treatment facility according to claim 4 of the present invention, the combustion exhaust gas from the gas engine or the gas turbine is supplied to the landing well, and the raw water is subjected to pH adjustment treatment by the combustion exhaust gas in the landing well. It is characterized by being.

  Moreover, in the water purification treatment facility according to claim 5 of the present invention, the carbonated water obtained from the combustion exhaust gas from the gas engine or the gas turbine is supplied to the landing well, and the raw water is supplied to the landing well. A pH adjustment treatment is performed with the carbonated water.

Moreover, the water purification treatment facility according to claim 6 of the present invention includes a landing well that takes in raw water for water purification, a sedimentation basin that precipitates and removes suspensions contained in the raw water, and water from the sedimentation basin. A water treatment facility equipped with a water treatment facility for treating water as required,
Carbonated water obtained from combustion exhaust gas from a gas engine or a gas turbine is supplied to the landing well, and raw water is subjected to pH adjustment treatment with the carbonated water in the landing well.

Further, in the water purification method according to claim 7 of the present invention, the raw water for water purification is taken in the landing well, the suspension contained in the taken raw water is settled and removed in the sedimentation basin, and the sedimentation basin In addition to water treatment as required by the water treatment facility, the water sludge separated in the sedimentation basin is concentrated in the concentration tank, and is contained in the supernatant water supernatant in the concentration tank. A water purification method for removing the manganese component in the Mn removal tank and returning the returned water from the Mn removal tank to the landing well,
A neutralization tank is provided between the Mn removal tank and the landing well, combustion exhaust gas from a gas engine or gas turbine or carbonated water obtained from the combustion exhaust gas is supplied to the neutralization tank, and the neutralization tank Then, the return water from the Mn removal tank is neutralized with the combustion exhaust gas or the carbonated water.

  According to the water purification treatment facility of the first aspect of the present invention, the neutralization tank is provided in the return line from the Mn removal tank, and the combustion exhaust gas from the gas engine or the gas turbine is supplied to the neutralization tank. In recent years, a cogeneration system is often installed in a water purification plant because it consumes a large amount of electric power, and the combustion exhaust gas of the gas engine or gas turbine of this cogeneration system is effectively used to remove it from the Mn removal tank. The return water can be neutralized and returned to the landing well. By neutralizing the return water in the neutralization tank in this way, the contact efficiency of the combustion exhaust gas becomes higher than when treating in the landing well, and this return water can be efficiently neutralized. Further, by performing the neutralization treatment in the neutralization tank in this manner, the amount of the acid agent used for the pH adjustment treatment in the landing well can be reduced, thereby reducing the cost of the water purification treatment. be able to. In addition, after returning the dehydration separation water from a dehydrator to a concentration tank, you may make it return to a landing well after removing a manganese component together in this Mn removal tank.

  Moreover, according to the water purification treatment facility according to claim 2 of the present invention, carbonated water obtained from combustion exhaust gas from the gas engine or gas turbine is supplied to the neutralization tank provided in the return line from the Mn removal tank. Is done. Thus, by neutralizing the return water using carbonated water in the neutralization tank, the return water can be efficiently neutralized, and more efficiently by using it as carbonated water in particular. Neutralization treatment can be performed.

  Moreover, according to the water-purifying treatment facility described in claim 3 of the present invention, the carbonated water can be obtained by condensing the combustion exhaust gas with the condenser or dissolving it with the dissolving device. For example, since a large amount of water is handled at a water purification plant, water in the combustion exhaust gas is condensed by heat exchange with this water, and carbon dioxide is absorbed into the condensed water to obtain carbonated water. Combustion exhaust gas is introduced into a melting device, and carbon dioxide in the combustion exhaust gas can be dissolved in water to obtain carbonated water.

  Further, according to the water purification treatment facility according to claim 4 of the present invention, since the combustion exhaust gas from the gas engine or gas turbine is also supplied to the landing well, the combustion exhaust gas of the gas engine or gas turbine is effectively used. Then, pH treatment of the raw water of the landing well can be performed.

  Further, according to the water purification treatment facility according to claim 5 or 6 of the present invention, carbonated water obtained from the combustion exhaust gas from the gas engine or gas turbine is also supplied to the landing well. It becomes easy to contact, acts effectively, and can perform an efficient pH treatment.

  Moreover, according to the water purification method of claim 7 of the present invention, the neutralization tank provided in the return line from the Mn removal tank has the combustion exhaust gas from the gas engine or gas turbine or the carbon dioxide obtained from this combustion exhaust gas. Since water is supplied, the return water from the Mn removal tank can be neutralized and returned to the landing well by effectively using the combustion exhaust gas of the gas engine or gas turbine of this cogeneration system.

  Hereinafter, with reference to an accompanying drawing, an embodiment of a water treatment facility according to the present invention is described. First, with reference to FIG. 1, the water purification equipment of 1st Embodiment is demonstrated. FIG. 1 is a block diagram schematically showing the water purification treatment facility of the first embodiment.

  In FIG. 1, this water purification treatment facility 2 includes a landing well 4, a sedimentation basin 6, a water treatment facility 8, a concentration tank 10, and a Mn removal tank 12. Raw water led from rivers and the like is taken into the landing well 4. The raw water taken into the landing well 4 is guided to the settling basin 6 through the raw water supply line 5, and suspended matter and the like in the raw water are precipitated and removed in the settling basin 6. In order to enhance the precipitation effect in the settling basin 6, a flocculant is added to the raw water flowing from the landing well 4 to the settling basin 6, and the suspension in the raw water is flocculated by the flocculant. In order to enhance the coagulation effect by the coagulant and to prevent the generation of bromic acid during the ozone treatment in the water treatment facility 8, combustion exhaust gas as an acid agent is supplied to the landing well 4 as will be described later, and the combustion exhaust gas Is used to adjust the pH of the raw water to, for example, about pH 6.5 to 6.9.

  The clean water separated in the settling basin 4 is guided to the water treatment facility 8 through the clean water supply line 7. Although not shown, the water treatment facility 8 includes an ozone treatment device, an activated carbon treatment device, a post-treatment device, a chlorine disinfection device, and the like. The ozone treatment device performs ozone treatment on the treated water to convert the hardly decomposable organic matter in the raw water into the easily degradable organic matter, and the activated carbon treatment device removes the organic matter contained in the treated water. The post-treatment device removes trace substances and microorganisms leaking from the activated carbon treatment device, and the chlorine disinfection device sterilizes the treated water by adding liquid chlorine or sodium hypochlorite. The water treated in this way by the water treatment facility 8 is supplied as purified water to a home, factory, etc. through a purified water supply line 9 (for example, a water pipe).

  On the other hand, the water sludge separated in the settling tank 4 is fed to the concentration tank 10 through the water sludge feed line 11. In the concentration tank 10, the water sludge is concentrated by, for example, gravity, and the concentrated sludge concentrated in the concentration tank 10 and drawn from the bottom is fed to the dehydrator 114 through the concentrated sludge feed line 11. The supernatant water from 10 is fed to the Mn removal tank 12 through the supernatant water feed line 13.

  In the dewatering device 14, the concentrated sludge is dehydrated, and the dewatered sludge dehydrated by this dewatering treatment is fed to the dryer 16 through the dewatered sludge feed line 15, and dehydrated and separated by the dewatering device 14. The dehydrated separated water is returned to the concentration tank 10 through the separated water supply line 17. In the dryer 16, the dewatered sludge is dried and the dried sludge is taken out as a solid matter. In this drying process, heat generated in the gas turbine 18 of the cogeneration system installed in the water purification plant is used, and the dehydrated sludge can be reduced by effectively using the heat of the gas turbine 18. In addition, the electric power generated in the cogeneration system is used as electric power for various facilities in the water purification plant.

  The supernatant water from the concentration tank 10 is supplied to the Mn removal tank 12, and the manganese component is removed in the Mn removal tank 12. For example, caustic soda solution as an alkaline agent is charged into the Mn removal tank 12 and removed in the form of manganese hydroxide in an alkaline atmosphere. Since the alkaline agent is used, the return water from the Mn removal tank 12 exhibits alkalinity. The return water from which the manganese component has been removed is returned from the Mn removal tank 12 to the landing well 4 through the return line 19 and mixed with the raw water from the river or the like in the landing well 4, and the mixed raw water is as described above. Purified.

  In this water purification treatment facility 2, it is important to provide a neutralization tank 20 in the return line 19 and neutralize the return water in the neutralization tank 20. In this embodiment, the return water fed from the concentration tank 10 through the return line 19 flows into the neutralization tank 20, and the combustion exhaust gas from the gas turbine 18 of the cogeneration system enters the neutralization tank 20 as the first exhaust gas. It is supplied through the feeding line 21. With this configuration, in the neutralization tank 20, the combustion exhaust gas from the gas turbine 18 acts on the return water in the neutralization tank 20. The combustion exhaust gas contains a large amount of carbon dioxide, which is an acidic component. When this carbon dioxide dissolves in the return water, the combustion exhaust gas exhibits acidity. Therefore, the combustion exhaust gas from the gas turbine 18 is used to enter the neutralization tank 20. Thus, the neutralization treatment of the return water can be performed, and the use of the drug can be suppressed or the use thereof can be eliminated. The neutralized return water is returned to the landing well 4 through the return line 19, and by neutralizing and returning in this way, there is no need to perform pH adjustment processing on the return water in the landing well 4. The pH adjustment process of the landing well 4 may be performed on the raw water taken, and thereby the pH adjustment on the raw water can be performed efficiently. The neutralization treatment with the combustion exhaust gas is efficiently performed with a relatively simple configuration by, for example, bubbling the combustion exhaust gas supplied through the first exhaust gas supply line 21 into the return water in the neutralization tank 20. Sum processing can be performed.

  In this embodiment, the combustion exhaust gas from the gas turbine 18 is also supplied to the landing well 4 through the second exhaust gas supply line 23, and the combustion exhaust gas from the gas turbine 18 acts on the raw water in the landing well 4. The raw water is weakly alkaline (pH 7-8) due to the assimilation of aquatic plants, etc., but by supplying combustion exhaust gas that dissolves in the raw water and exhibits acidity, the pH of the raw water can be adjusted. It is possible to suppress or eliminate the use of a large amount of medicine required for the adjustment process. The pH adjustment process by the landing well 4 is also efficiently performed with a relatively simple configuration by bubbling the combustion exhaust gas supplied through the second exhaust gas supply line 23 into the raw water in the landing well 4, for example. Sum processing can be performed.

  In this embodiment, in addition to the power and heat generated by the cogeneration system, the combustion exhaust gas generated by the gas turbine 18 is also used as the acid agent, so that the entire system can be operated efficiently, and this combustion exhaust gas is also used. The neutralization process of the return water from the Mn removal tank 12 and the pH adjustment of the raw water of the landing well 4 can be performed using In addition, in order to supply combustion exhaust gas from the gas turbine 18 to the first and second combustion exhaust gas supply lines 21 and 23 as required, a supply blower (not shown) is provided as necessary.

  In the water purification treatment facility 2 described above, the combustion exhaust gas from the gas turbine 18 is used for the neutralization process of the return water and the pH adjustment process of the raw water. However, the pH adjustment process of the raw water is used only for the neutralization process of the return water. May use an acidic drug similar to the conventional one, such as sulfuric acid.

  Then, with reference to FIG.2 and FIG.3, the water purification treatment equipment of 2nd Embodiment is demonstrated. FIG. 2 is a block diagram schematically showing the water purification treatment facility of the second embodiment, and FIG. 3 is a diagram simply showing the condensing device of the water purification treatment facility of FIG. 2 and 3, substantially the same members as those in the first embodiment described above are denoted by the same reference numerals, and description thereof is omitted.

  In FIG. 2, in the water purification treatment facility 2 </ b> A of the second embodiment, carbonated water is generated using the combustion exhaust gas from the gas turbine 18, and this carbonated water is supplied to the neutralization tank 20 and the landing well 4. The More specifically, a condensing device 30 is provided in the flue gas exhaust line 31 of the water purification treatment facility 2A. The condensing device 30 condenses moisture in the flue gas into water, and absorbs carbon dioxide in the condensed water. To produce carbonated water. The carbonated water generated in this manner is fed to the neutralization tank 20 through the first carbonated water feed line 32 and fed to the landing well 4 through the second carbonated water feed line 34.

  In the neutralization tank 20, carbonated water introduced through the first carbonated water supply line 32 acts on the return water from the Mn removal tank 12, and the return water is neutralized by this carbonated water, and the neutralization treatment. The returned water is returned to the landing well 4 through the return line 19. Further, in the landing well 4, carbonated water introduced through the second carbonated water supply line 34 acts on the taken raw water (including return water), and the raw water is subjected to pH adjustment treatment by this carbonated water, and pH The above-described water purification treatment is performed on the adjusted raw water. By using it as carbonated water in this way, the contact efficiency with return water and raw water is increased, handling such as transportation is facilitated, and the efficiency of neutralization treatment and pH adjustment treatment can be enhanced.

  The condensing device 30 can be configured as shown in FIG. 3, for example. In FIG. 3, the condensing device 30 includes a heat exchanger 36, and the combustion exhaust gas from the gas turbine 18 is led to the heat exchanger 36 through the combustion exhaust gas discharge line 31, and is discharged to the atmosphere through the heat exchanger 36. . A recovery line 38 is connected to a portion of the combustion exhaust gas discharge line 31 downstream of the heat exchanger 36, and a recovery tank 40 is provided in the recovery line 38. A carbonated water delivery line 42 is connected to the recovery tank 40, and first and second carbonated water feed lines 32, 34 are connected to the carbonated water feed line 42, and A delivery pump 41 is provided. Further, a part of the purified water treated by the water treatment facility 8 is led to the heat exchanger 36 through the purified water feed line 44, and is fed to the home, factory, etc. through the heat exchanger 36 (water treatment facility). The remainder of the purified water from 8 is fed directly without passing through the heat exchanger 36.

  In such a condensing device 30, the combustion exhaust gas from the gas turbine 18 flows through the combustion exhaust gas discharge line 31, and part of the purified water from the water treatment facility 8 flows through the purified water feed line 44, and in the heat exchanger 36. Heat exchange is performed between the combustion exhaust gas and the purified water. Since the purified water treated at the water purification plant is kept at a relatively low temperature of 20 ° C. or lower throughout the year, the combustion exhaust gas is cooled by this purified water, and the moisture in the combustion exhaust gas is condensed into water, thus condensing. Carbon dioxide in the combustion exhaust gas is absorbed by the condensed water thus produced, and carbonated water is generated using the combustion exhaust gas.

  The generated carbonated water is collected in the collection tank 40 through the collection line 38. Then, the carbonated water collected in this way is sent out from the collection tank 40 by the delivery pump 41 and fed to the neutralization tank 20 through the first carbonated water feed line 32, and the second carbonated water feed line 34. To the landing well 4 through.

  In order to efficiently dissolve carbon dioxide in the condensate, the absorption refrigerator is driven using steam or hot water obtained from a cogeneration system as a heat source, and gas is generated using cold water generated by the absorption refrigerator. The combustion exhaust gas from the turbine may be cooled to obtain carbonated water.

  In order to obtain carbonated water, the melting device 50 shown in FIG. 4 may be used instead of the condensing device 30 shown in FIG. In FIG. 4, the dissolution apparatus 50 shown in the figure includes a dissolution tank 54 into which a part of purified water subjected to water treatment as required by the water treatment facility 8 flows through the purified water supply line 52. Instead of purified water, raw water taken from, for example, a river may be supplied to the dissolution tank 54 through a raw water supply line (not shown).

  Combustion exhaust gas from the gas turbine 18 is fed to the dissolution tank 54 through the combustion exhaust gas discharge line 31 and is bubbled into the water from the tip of the combustion exhaust gas discharge line 31 immersed in the water in the dissolution tank 54. By bubbling in this manner, carbonated water can be obtained efficiently. The produced carbonated water is collected in the collection tank 40 through the collection line 38, and the collected carbonated water is sent out from the collection tank 40 by the delivery pump 41 and sent to the neutralization tank 20 through the first carbonated water feed line 32. And supplied to the landing well 4 through the second carbonated water supply line 34. Accordingly, even when such a dissolving device 50 is used, carbonated water can be supplied to the neutralization tank 20 to perform the neutralization treatment of the return water, as in the case of using the condensing device 30, and the landing well 4 can be supplied with carbonated water to adjust the pH of the raw water.

  In order to efficiently dissolve carbon dioxide, an absorption refrigerator is driven using water vapor or hot water obtained from a cogeneration system as a heat source, and the flue gas from a gas turbine is added to the cold water obtained by this absorption refrigerator. May be dissolved.

  In the above-described water purification treatment facility 2A, carbonated water obtained using the combustion exhaust gas from the gas turbine 18 is used for the neutralization treatment of the return water and the pH adjustment treatment of the raw water, but only the neutralization treatment of the return water. For the pH adjustment treatment of raw water, an acidic chemical similar to the conventional one, such as sulfuric acid, may be used, or this carbonated water may be used only for pH treatment of raw water.

Example In order to confirm the neutralization treatment and pH adjustment treatment with combustion exhaust gas, the following experiment was conducted. A 16 liter dissolution tank (aeration tank) was prepared for the experiment, and 12 liters of return water (pH 11) (water after removing the manganese component in the Mn removal tank) was added to this aeration tank and cogeneration was performed. Combustion exhaust gas from the system gas turbine was bubbled into the return water of the aeration tank to neutralize the return water. In order to neutralize the return water, the return water is neutralized to about pH 6.8 by supplying combustion exhaust gas with a gas-liquid ratio of about 2 to 5 (m ³ -exhaust gas / m ³ -raw water). I was able to.

In addition, 12 liters of raw water (pH 7.5) (raw water of the landing well) is introduced into the aeration tank described above, and the combustion exhaust gas from the gas turbine of the cogeneration system is bubbled into the raw water of the aeration tank. The pH was adjusted. In order to adjust the pH of the raw water, the raw water is adjusted to pH 6.8 or less by supplying combustion exhaust gas with a gas-liquid ratio of about 0.25 to 0.4 (m ³ -exhaust gas / m ³ -raw water). did it.

  As mentioned above, although embodiment of the water-purifying treatment equipment and the processing method according to this invention was described, this invention is not limited to this embodiment, A various deformation | transformation thru | or correction | amendment are possible without deviating from the scope of the present invention. is there.

  For example, in the above-described embodiment, the gas turbine 18 is used as a drive source of the thermoelectric generator of the cogeneration system. However, a gas engine may be used as the drive source, and in this case, the gas engine 18 is discharged from the gas engine. Combustion exhaust gas is used. It is desirable to use natural gas (for example, city gas) as the fuel for the gas turbine or gas engine. By burning natural gas, the influence of the impurities contained in the combustion exhaust gas on the physical properties of tap water is affected. Can be reduced.

The block diagram which shows simply the water purification treatment equipment of 1st Embodiment. The block diagram which shows simply the water purification treatment equipment of 2nd Embodiment. FIG. 3 is a diagram simply illustrating the condensing device of the water purification treatment facility of FIG. 2. The figure which shows a melt | dissolution apparatus simply.

Explanation of symbols

2,2A Water purification treatment facility 4 Landing well 6 Sedimentation basin 8 Water treatment facility 10 Concentration tank 12 Mn removal tank 18 Gas turbine 19 Return line 20 Neutralization tank 21, 23 Combustion exhaust gas supply line 30 Condenser 32, 34 Carbonated water supply Supply line 50 Dissolving device

Claims (7)

A landing well that takes in raw water for water purification, a sedimentation basin that precipitates and removes suspensions contained in the raw water, a water treatment facility that treats the water from the sedimentation basin as required, and the sedimentation basin. A concentration tank for concentrating the separated water sludge, a dehydrator for dewatering the concentrated sludge separated in the concentration tank, a Mn removal tank for removing manganese components contained in the supernatant water of the concentration tank, , A water purification treatment facility comprising a return line for returning the return water from the Mn removal tank to the landing well,
The return line is provided with a neutralization tank, and combustion exhaust gas from a gas engine or a gas turbine is supplied to the neutralization tank. In this neutralization tank, return water from the Mn removal tank is contained by the combustion exhaust gas. Clean water treatment facility characterized by being treated in Japanese. A landing well that takes in raw water for water purification, a sedimentation basin that precipitates and removes suspensions contained in the raw water, a water treatment facility that treats the water from the sedimentation basin as required, and the sedimentation basin. A concentration tank for concentrating the separated water sludge, a dehydrator for dewatering the concentrated sludge separated in the concentration tank, a Mn removal tank for removing manganese components contained in the supernatant water of the concentration tank, , A water purification treatment facility comprising a return line for returning the return water from the Mn removal tank to the landing well,
The return line is provided with a neutralization tank, and carbonated water obtained from combustion exhaust gas from a gas engine or gas turbine is supplied to the neutralization tank. In this neutralization tank, the return water from the Mn removal tank Is purified by the carbonated water.   The carbonated water is generated using a condensing device for condensing the combustion exhaust gas from the gas engine or the gas turbine to obtain carbonated water, or a dissolving device for dissolving the combustion exhaust gas to obtain carbonated water. The water purification equipment according to claim 2, wherein   The water purification treatment facility according to claim 1, wherein the combustion exhaust gas from the gas engine or the gas turbine is supplied to the landing well, and raw water is subjected to pH adjustment treatment by the combustion exhaust gas in the landing well. .   The carbonated water obtained from the combustion exhaust gas from the gas engine or the gas turbine is supplied to the landing well, and the raw water is subjected to pH adjustment treatment by the carbonated water in the landing well. The water treatment facility according to 2 or 3. Purified water equipped with a landing well that takes in raw water for water purification, a sedimentation basin that precipitates and removes suspensions contained in the raw water, and a water treatment facility that treats the water from the sedimentation basin as required A processing facility,
Carbonated water obtained from combustion exhaust gas from a gas engine or a gas turbine is supplied to the landing well, and the raw water is subjected to pH adjustment treatment with the carbonated water in the landing well. The raw water for clean water is taken in the landing well, the suspension contained in the taken raw water is settled and removed in the sedimentation basin, and the water from the sedimentation basin is treated with water treatment equipment as required. In addition, the water sludge separated in the sedimentation basin is concentrated in a concentration tank, the manganese component contained in the supernatant water supernatant in the concentration tank is removed in the Mn removal tank, from the Mn removal tank A water purification method for returning the returned water to the receiving well,
A neutralization tank is provided between the Mn removal tank and the landing well, combustion exhaust gas from a gas engine or gas turbine or carbonated water obtained from the combustion exhaust gas is supplied to the neutralization tank, and the neutralization tank The water purification process is characterized by neutralizing the return water from the Mn removal tank with the combustion exhaust gas or the carbonated water.

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