JP2006167616A - Neutralizing apparatus - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To realize a neutralizing apparatus which is not affected by heat of boiler tail gas and can improve neutralization efficiency. <P>SOLUTION: The neutralizing apparatus 1 for neutralizing boiler draining liquid by the boiler tail gas is equipped with an ejector 10 which captures the boiler draining liquid, sucks the boiler tail gas and mixes the boiler tail gas with the boiler draining liquid. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to an apparatus for neutralizing alkaline boiler effluent with boiler exhaust gas.

  The boiler water inside the steam boiler can, which generates steam by heating the feed water, is decomposed by hydrogen carbonate ions and carbonate ions contained in the feed water to produce hydroxide ions. Concentration becomes increasingly alkaline. Further, if the operation of the steam boiler is continued, the can water is excessively concentrated to cause inconveniences such as carry-over. Therefore, a predetermined proportion of the can water is periodically added to the steam so as to maintain an appropriate can water concentration. It is necessary to discharge from the boiler. This operation is usually called concentration blow. Furthermore, after the steam boiler has been operated for a predetermined time, it is necessary to wash away all the can water in order to remove the so-called pot mud (sludge) that has settled at the bottom of the can body. This operation is usually called full blow.

  When discharging boiler drainage by concentration blow or full blow as described above, it is necessary to perform drainage treatment such as cooling and neutralization so as to conform to the drainage standards defined by the ordinance. As a method for neutralizing boiler wastewater, for example, there is a method in which acidic chemicals such as hydrochloric acid are added to boiler wastewater. However, in this method, handling of chemicals is dangerous. On the other hand, as a neutralization method without using chemicals, there is a method of mixing carbon dioxide gas into boiler waste water. In this method, since carbon dioxide gas is generally supplied from a cylinder, management such as confirmation and replacement of the remaining amount of the cylinder tends to be complicated.

Therefore, Patent Document 1 discloses a method for neutralizing carbon dioxide contained in boiler exhaust gas instead of supplying carbon dioxide from a cylinder.
JP 2001-293484 A

  Since the neutralization method according to Patent Document 1 supplies high-temperature boiler exhaust gas to the boiler drainage using a pump, there is a possibility that the members constituting the movable part of the pump are deteriorated by the heat of the boiler exhaust gas. Moreover, in the said patent document 1, although neutralization is accelerated | stimulated by bubbling boiler exhaust gas in boiler waste_water | drain, the further improvement of neutralization efficiency is desired rather than this method.

  The problem to be solved by the present invention is to realize a neutralization device that is not affected by the heat of boiler exhaust gas and that can improve the neutralization efficiency.

  The present invention has been made to solve the above problems, and the invention according to claim 1 is a neutralizing device for neutralizing boiler wastewater with boiler exhaust gas, and includes a means for sucking and mixing boiler exhaust gas into boiler wastewater. It is characterized by that.

  In the invention according to the first aspect, the boiler waste water and the boiler exhaust gas are mixed by the suction mixing means, whereby the boiler exhaust gas is efficiently brought into contact with the boiler waste water, and the boiler exhaust gas is dissolved in the boiler waste water.

  The invention described in claim 2 is characterized in that, in claim 1, a boiler drainage storage tank and a circulation path for circulating the boiler drainage in the storage tank are provided, and the suction mixing means is provided in the circulation path. Features.

  In such invention of Claim 2, the boiler waste_water | drain stored in the said storage tank circulates through the said circulation route, and boiler exhaust gas contacts repeatedly with respect to boiler waste_water | drain with the said suction mixing means, and melt | dissolves.

  The invention described in claim 3 is characterized in that, in claim 2, the suction mixing means injects boiler wastewater mixed with boiler exhaust gas into the storage tank.

  In such invention of Claim 3, the boiler exhaust gas which was not able to melt | dissolve in boiler waste_water | drain in the said suction mixing means blows out in the bubble form in the said storage tank, and melt | dissolves in boiler waste_water | drain.

  A fourth aspect of the present invention is characterized in that, in the first, second, or third aspect, a water pressure detecting means is provided on the upstream side of the inflow portion of the boiler drain to the suction mixing means.

  In the invention according to the fourth aspect, it is possible to detect the decrease by detecting the water pressure of the boiler waste water flowing into the suction and mixing means by the water pressure detecting means.

  According to the first aspect of the present invention, unlike the pump, the suction mixing means for mixing the boiler waste water and the boiler exhaust gas does not have a movable part, and therefore is not easily deteriorated by the heat of the boiler exhaust gas. For this reason, boiler exhaust gas can be stably supplied with respect to boiler waste_water | drain. Moreover, since the boiler waste water and the boiler exhaust gas are efficiently brought into contact with each other by the suction mixing means, and the boiler waste water is stirred by the turbulent flow effect generated by the suction mixing means, the neutralization can be efficiently performed.

  According to the second aspect of the present invention, the boiler waste water circulating through the circulation path is repeatedly brought into contact with the boiler exhaust gas in the suction and mixing means, so that the boiler exhaust gas can be efficiently dissolved in the boiler waste water. , Stable neutralization treatment can be performed.

  According to the third aspect of the present invention, even if the boiler exhaust gas sucked by the suction mixing means cannot be completely dissolved in the boiler drainage, the undissolved boiler exhaust gas can be dissolved in the storage tank. Thus, the neutralization efficiency can be improved.

  According to the invention described in claim 4, since it is possible to detect a decrease in the water pressure of the boiler wastewater flowing into the suction mixing means, the intake amount of the boiler exhaust gas sucked together with the intake of the boiler wastewater by the suction mixing means Can be detected. As a result, it is possible to prevent the processing capacity of the neutralizing device from being lowered. Further, when a pump is provided on the upstream side of the water pressure detecting means, a failure of the pump can be detected.

Hereinafter, the best mode for carrying out the neutralizing apparatus according to the present invention will be described.
The present invention is preferably implemented in a treatment apparatus for neutralizing alkaline boiler wastewater, so-called blow wastewater, with carbon dioxide contained in boiler exhaust gas. That is, the boiler wastewater from the steam boiler is efficiently neutralized with carbon dioxide contained in the boiler exhaust gas to lower the pH, and discharged as treated water that meets the wastewater standards.

  First, the first embodiment will be described. The neutralization apparatus in the first embodiment includes a drainage path through which boiler drainage from a steam boiler flows and an exhaust gas path for boiler exhaust gas used for neutralization. Furthermore, a boiler mixing means for taking in boiler wastewater supplied from the drainage path, sucking boiler exhaust gas supplied from the exhaust gas path, and mixing them is provided. The suction mixing unit is a unit that sucks gas using a negative pressure generated by a fluid flow and mixes and discharges liquid and gas. For example, an ejector or an aspirator can be used.

  The suction mixing means has a drainage supply port to which the drainage channel is connected and an exhaust gas suction port to which the exhaust gas channel is connected. From the exhaust gas suction port to the boiler drain taken in from the drainage supply port The sucked boiler exhaust gas is mixed.

  In such a neutralization apparatus of the first embodiment, boiler wastewater flowing through the drainage path is taken into the suction mixing means from the wastewater supply port. In the suction mixing means, the boiler exhaust gas sucked from the exhaust gas path is mixed with the boiler waste water. As a result, the boiler exhaust gas dissolves while efficiently contacting the boiler waste water.

  As described above, according to the neutralization device of the first embodiment, unlike the pump, the suction mixing unit does not have a movable part, and therefore is not easily deteriorated by the heat of the boiler exhaust gas. For this reason, boiler exhaust gas can be stably supplied with respect to boiler waste_water | drain. Moreover, since the said suction mixing means has the effect | action which makes a boiler wastewater and boiler exhaust gas contact efficiently, and also stirs by a turbulent flow effect, it can neutralize efficiently.

  Next, a second embodiment that is a modification of the first embodiment will be described. The neutralization apparatus in the second embodiment includes a storage tank that stores boiler wastewater from the steam boiler, and a circulation path that circulates boiler wastewater in the storage tank, and includes the suction mixing unit in the circulation path. ing. The circulation path is provided with a circulation pump, and the boiler drain in the storage tank is circulated through the circulation path by the circulation pump.

  Here, the suction mixing means injects boiler wastewater mixed with boiler exhaust gas into the storage tank.

  In such a neutralization apparatus of the second embodiment, the boiler wastewater stored in the storage tank circulates through the circulation path, and the boiler wastewater and the boiler exhaust gas are repeatedly contacted in the suction and mixing means. As a result, the boiler exhaust gas is dissolved in the boiler waste water. Further, the boiler exhaust gas that could not be dissolved in the boiler drainage in the suction mixing means is blown out into the storage tank in the form of bubbles, and is dissolved in the boiler drainage in the storage tank.

  As described above, according to the neutralization device of the second embodiment, the boiler wastewater circulating through the circulation path repeatedly contacts with the boiler exhaust gas in the suction mixing means, so that the boiler exhaust gas is efficiently dissolved in the boiler wastewater. And stable neutralization can be performed. Furthermore, when the boiler exhaust gas cannot be sufficiently dissolved by the suction mixing means, the undissolved boiler exhaust gas can be dissolved in the storage tank, so that the neutralization efficiency can be improved.

  Next, a third embodiment that is a modification of the first embodiment and the second embodiment will be described. The neutralizing device in the third embodiment is provided with a water pressure detecting means for detecting the water pressure of boiler drainage flowing through the circulation path in the circulation path. The water pressure detection means is, for example, a pressure switch or a pressure sensor, and is provided at a position upstream of the boiler wastewater inflow side to the suction mixing means and downstream of the circulation pump.

  In such a neutralization apparatus of the third embodiment, it is possible to detect the decrease by detecting the water pressure of the boiler drainage flowing through the circulation path and flowing into the suction mixing means by the water pressure detecting means. Is possible. Here, since the suction mixing means sucks the boiler exhaust gas as the boiler waste water is taken in, the intake air amount of the boiler exhaust gas decreases when the water pressure of the boiler waste water decreases. Therefore, if a decrease in the water pressure of the boiler wastewater flowing into the suction and mixing means is detected, it is possible to prevent the processing capacity of the neutralizing device from being lowered. Further, when a water pressure drop is detected by the water pressure detecting means, there are usually considered causes such as failure of the circulation pump and clogging of the circulation path, but it is possible to quickly cope with these problems.

Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a schematic explanatory view showing the configuration of a neutralization apparatus for carrying out the present invention.
In FIG. 1, a neutralizing apparatus 1 neutralizes alkaline blow drainage (hereinafter referred to as “boiler drain”) from a steam boiler 2 with carbon dioxide contained in boiler exhaust gas, and treats water that meets the drainage standards. As a discharge.

  The neutralization device 1 includes a drainage path 3 for supplying boiler drainage from the steam boiler 2, a boiler drainage storage tank 4, and an exhaust gas path 5 for supplying boiler exhaust gas used for neutralization.

  The steam boiler 2 includes an exhaust cylinder 6 that discards the exhaust gas that burns fuel to the outside. The exhaust cylinder 6 and the exhaust gas path 5 are connected to take out a part of the exhaust gas.

  The storage tank 4 is connected to both ends of a circulation path 7 for circulating the stored boiler drainage. The circulation path 7 is connected to the circulation pump 8, the water pressure detection means 9, and the ejector 10 in order from the upstream side. (An example of the suction mixing means) is provided.

  The ejector 10 has a drain supply port 11 to which the circulation path 7 is connected and an exhaust gas suction port 12 to which the exhaust gas path 5 is connected. The ejector 10 takes in boiler wastewater from the wastewater supply port 11 and sucks boiler exhaust gas from the exhaust gas suction port 12 to mix boiler wastewater and boiler exhaust gas. Boiler wastewater mixed with boiler exhaust gas is injected into the storage tank 4 from the discharge port 13 of the ejector 10.

  Here, the boiler exhaust gas is supplied to the ejector 10 or is stopped by opening and closing an exhaust gas supply valve 14 and an air valve 15 provided in the exhaust gas path 5 (details will be described later). explain).

  The drainage path 3 includes a cooling means 16. The cooling means 16 is a heat exchanger and includes a drain inlet 17 for supplying boiler drainage flowing through the drainage path 3 and a drain outlet 18 for discharging the cooled boiler drain. The cooling means 16 further includes a cooling water inlet 19 that supplies cooling water and a cooling water outlet 20 that discharges the heat-exchanged cooling water.

  The boiler waste water cooled by the cooling means 16 is temporarily stored in the storage tank 4, but if this cooling is insufficient and the water temperature is not determined by the drainage standard, the upstream side of the drain inlet 17 Returned to Specifically, when the boiler drainage in the storage tank 4 exceeds a predetermined temperature, the boiler drainage is returned to the upstream side of the drainage inlet 17 via the drainage return path 22 provided with the drainage return valve 21. It is.

  The storage tank 4 is provided with a temperature sensor 23 and a pH sensor 24 for detecting the water temperature and pH of the stored boiler drainage. Further, a treated water discharge path 25 for discharging neutralized boiler drainage, that is, treated water, is connected to the bottom of the storage tank 4, and a discharge valve 26 is connected to the treated water discharge path 25. Is provided. The discharge valve 26 is controlled by a control unit 27 so that it opens when the water quality detected by the temperature sensor 23 and the pH sensor 24 reaches a water temperature and pH that meet the drainage standard.

  Signals from the water pressure detecting means 9, the temperature sensor 23, and the pH sensor 24 are input to the control unit 27, respectively. Based on the input signals, the exhaust gas supply valve 14, the air valve 15, the drain return valve 21 and the discharge valve 26 are controlled to open and close.

  Next, the operation of the neutralizing device 1 will be described. Boiler drainage from the steam boiler 2 is stored in the storage tank 4 through the drainage path 3. In the drainage path 3, the boiler drainage is cooled by heat exchange in the cooling means 16. Specifically, the boiler drainage flowing through the drainage path 3 is introduced into the cooling means 16 from the drainage inlet 17 and cooled by being deprived of heat by the cooling water supplied from the cooling water inlet 19. Is done. The cooled boiler wastewater flows through the drainage path 3 from the drainage outlet 18 and is stored in the storage tank 4.

  When the temperature of the boiler wastewater stored in the storage tank 4 is detected by the temperature sensor 23 and is higher than the water temperature determined by the drainage standard, the drainage return valve 21 is opened by the control unit 27. Then, the boiler drainage in the storage tank 4 is returned to the upstream side of the drainage inlet 17 through the drainage return path 22 and is cooled again by the cooling means 16.

  On the other hand, the boiler wastewater stored in the storage tank 4 circulates in the circulation path 7 by driving the circulation pump 8. The boiler waste water circulating through the circulation path 7 is neutralized by the action of the ejector 10 by the boiler exhaust gas supplied from the exhaust gas path 5. Specifically, the ejector 10 takes in boiler wastewater from the wastewater supply port 11 and sucks boiler exhaust gas supplied from the exhaust gas passage 5 from the exhaust gas suction port 12 to mix boiler wastewater and boiler exhaust gas. To do. Thereby, boiler waste_water | drain and boiler waste gas are made to contact efficiently, and boiler waste_gas | exhaustion is dissolved in boiler waste_water | drain. And this boiler waste_water | drain is injected in the said storage tank 4 from the said discharge outlet 13. FIG. Here, the boiler exhaust gas that could not be dissolved in the boiler drainage in the ejector 10 is blown out into the storage tank 4 in the form of bubbles and is refined and dissolved in the boiler drainage.

  Supply of boiler exhaust gas to the ejector 10 and stop thereof are performed by controlling the opening and closing of the exhaust gas supply valve 14 and the air valve 15, respectively. Specifically, when supplying boiler exhaust gas to the ejector 10, the exhaust gas supply valve 14 is opened and the air valve 15 is closed. On the contrary, when the supply of boiler exhaust gas to the ejector 10 is stopped, the exhaust gas supply valve 14 is closed and the air valve 15 is opened to suck in the outside air. As described above, when outside air is sucked in when boiler exhaust gas is not supplied, vibration caused by pressure fluctuations generated in the ejector 10 is suppressed.

  Opening / closing control of the exhaust gas supply valve 14 and the air valve 15 is performed by the control unit 27 based on a signal from the pH sensor 24. For example, when the pH of boiler wastewater in the storage tank 4 exceeds a value determined by the wastewater standard, the control unit 27 opens the exhaust gas supply valve 14 and closes the air valve 15. On the other hand, when the pH of the boiler drainage in the storage tank 4 reaches a value determined by the drainage standard, the control unit 27 closes the exhaust gas supply valve 14 and opens the air valve 15.

  After the cooling and neutralization as described above, when the boiler drainage in the storage tank 4 reaches the water temperature and pH determined by the drainage standard, the control unit 27 opens the discharge valve 26, and the boiler Waste water is discharged out of the system through the treated water discharge path 25.

  By the way, the neutralizing device 1 is configured to detect the water pressure of the boiler wastewater flowing into the ejector 10 by the water pressure detecting means 9. For example, when the circulation pump 8 is broken or the circulation path 7 is clogged, the water pressure of the boiler drain to the ejector 10 decreases, and a sufficient negative pressure cannot be obtained at the exhaust gas suction port 12. For this reason, the amount of intake air of the boiler exhaust gas decreases, and the predetermined neutralization ability cannot be exhibited. Therefore, in this configuration, when the water pressure of the boiler waste water becomes a predetermined value or less, the control unit 27 issues an alarm or the like to notify the abnormality to the outside. As a result, maintenance of the circulation pump 8 and the circulation path 7 and the like can be quickly performed, and a decrease in the intake amount of boiler exhaust gas can be prevented in advance.

  The neutralizing device 1 described above includes a circulation path 7 for circulating the boiler drainage in the storage tank 4, and the ejector 10 is provided in the circulation path 7. However, the present invention is limited to this configuration. Is not to be done. For example, the ejector 10 may be provided in the drainage path 3. In this case, it is desirable to connect the drainage path 3 below the storage tank 4 and to inject the boiler wastewater mixed with boiler exhaust gas into the storage tank 4 from the discharge port 13.

It is a schematic explanatory drawing which shows the structure of one Example of the neutralization apparatus which concerns on this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Neutralizer 4 Reservoir 7 Circulation path 9 Water pressure detection means 10 Ejector

Claims (4)

In the neutralizer that neutralizes boiler wastewater with boiler exhaust gas,
A neutralizing apparatus comprising a suction mixing means for boiler exhaust gas into boiler wastewater. A storage tank for boiler drainage, and a circulation path for circulating boiler drainage in the storage tank,
The neutralization apparatus according to claim 1, wherein the suction and mixing unit is provided in the circulation path.   The neutralization apparatus according to claim 2, wherein the suction mixing unit injects boiler wastewater mixed with boiler exhaust gas into the storage tank.   The neutralization apparatus according to claim 1, 2, or 3, further comprising a water pressure detection means provided upstream of an inflow portion of boiler wastewater to the suction mixing means.

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