JP2005083724A - Corrosion prevention method and apparatus of melting furnace secondary combustion chamber dust extractor - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To prevent the occurrence of the high-temperature and low-temperature corrosion of a dust extractor. <P>SOLUTION: Ash melting facilities are composed so that the complete combustion treatment of a melting exhaust gas 16 can be made by providing a melting furnace secondary combustion chamber 18 equipped with a two-stage damper type dust extractor 22 on the downstream side of a burner type ash melting furnace I. A cooling air blowing nozzle 31 is connected to the lower end of the melting furnace secondary combustion chamber 18. A suction collection line 29 for sucking and collecting incineration residue 2 leaked from an ash storage tank pusher 3 in the burner type ash melting furnace I is connected to the cooling air blowing nozzle 31. Collected air 30 by sucking and collecting the incineration residue 2 leaked from the ash storage tank pusher 3 is blown into the melting furnace secondary combustion chamber 18 by the cooling air blowing nozzle 31, and the temperature near the inlet of the dust extractor 22 is reduced to about 400°C for suppressing high-temperature corrosion. Temperature at the inlet side is set to about 400°C, thus preventing temperature from decreasing to 150°C or less even at the outlet side of the dust extractor 22 and preventing low-temperature corrosion from occurring. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

The present invention relates to a method and an apparatus for preventing corrosion of a melting furnace secondary combustion chamber dust discharger used to prevent corrosion of a dust discharger for discharging dust from a melting furnace secondary combustion chamber provided downstream of an ash melting furnace. It is about.

In recent years, incineration treatment methods that incinerate waste in an incinerator include municipal waste and other general waste, and industrial waste such as sewage sludge, building waste, shredder dust, and various sludges. Incineration residue consisting of incineration ash and dust (including fly ash) generated by this incineration process is made into slag by melting at high temperature so that volume reduction and detoxification can be achieved. It is becoming.

As an ash melting furnace used for melting the above incineration residue, unburned residue remains in the incineration residue discharged from the incinerator, and combustion heat generated by burning the unburned residue is used as a melting heat source. Self-combustion type internal melting furnaces that can be made have been developed, and examples of the types include burner type melting furnaces, rotary surface melting furnaces, coke bed type ash melting furnaces, DC electric resistance type ash melting furnaces, etc. There is.

As an example of an ash melting facility equipped with such an ash melting furnace, FIG. 3 shows an outline of an ash melting facility using a burner type melting furnace, which has the following configuration. That is, the burner type melting furnace I pushes the incineration residue 2 supplied from a supply unit (not shown) such as a conveyor into the ash storage tank 1 into the upper end of the ash storage tank 1 extending in the vertical direction in order to store the incineration residue. An ash storage tank pusher 3 for supply is connected via an ash storage tank seal damper 4. The ash storage tank 1
A combustion chamber 5 having a large number of aeration nozzles 7 in the bottom hearth 6 is continuously provided on one side of the lower end portion of the steel plate so as to have a downward slope toward the downstream side. Further, a melting furnace supply pusher 8 for pushing out the incineration residue 2 in the ash storage tank 1 to the hearth 6 of the combustion chamber 5 is provided on the other side of the lower end of the ash storage tank 1, and the ash storage tank pusher 3 The incineration residue 2 pushed and fed into the storage tank 1 is pushed out onto the hearth 6 by the melting furnace supply pusher 8, and the unburned residue in the incineration residue 2 is diffused into the aeration nozzle 7.
The incineration residue 2 is melted by the combustion heat by the high-temperature air supplied through the surface of the combustion chamber 5, thereby forming the surface melting portion 2 b near the outlet 5 a portion of the combustion chamber 5.

Furthermore, it forms in the shape of a sideways cylinder, the inlet 10 is provided in one side of the bottom part side, the slag outlet 11 is provided in the other side of the bottom part, and the bottom part between the inlet 10 and the slag outlet 11 is provided. Bathtub 9a
The outlet 5a of the combustion chamber 5 is connected in a tangential direction to the inlet 10 of the melting furnace main body 9 so as to form an integral structure, and a sump is formed from the surface melting portion 2b near the outlet 5a portion of the combustion chamber 5. 9
The molten slag 2a flows to a. On the other hand, in the upper position of the melting furnace body 9 on the slag outlet 11 side, the auxiliary combustion burner 12 for controlling the temperature of the entire furnace using kerosene or the like as fuel can be injected in the horizontal direction so that the combustion gas can be injected from the tangential direction. It is installed in. Therefore, the combustion gas injected from the tangential direction into the melting furnace main body 9 by the auxiliary burner 12 and the combustion gas sent from the combustion chamber 5 into the melting furnace main body 9 are swirled to make a swirl flow (vortex flow). 13), the molten slag 2a flowing into the hot water reservoir 9a is heated by the swirling flow 13 to promote melting of the unmelted portion.

Furthermore, a plurality of oxygen burners 14 are installed downward at a required portion of the melting furnace main body 9, and a combustion oil fuel such as kerosene is burned using oxygen in the oxygen burners 14 to generate a high-temperature jet. By heating the range from the surface melting part 2b to the sump 9a by this high-temperature jet, it is possible to further increase the speed of melting unmelted ash, iron pieces, clinker, etc. It can be realized.

Thereafter, the molten slag 2a overflows from the hot water reservoir 9a and is discharged through the discharge chute 15 from the slag outlet 11 and recovered as slag (for example, see Non-Patent Document 1).

On the other hand, the molten exhaust gas 16 generated in the melting furnace main body 9 contains some unburned gas.
Therefore, a secondary combustion chamber 18 having a tower shape extending in the vertical direction is provided. The secondary combustion chamber 18 is provided with an exhaust gas inlet 19 at the lower side wall, a gas outlet 20 at the top, and a secondary air supply nozzle 21 at a required position on the side wall. A secondary air supply unit (not shown) is connected via a secondary air line 25. Further, the lower end portion of the secondary combustion chamber 18 is provided with a dust discharger 22 of a two-stage damper type at the lower end thereof as a hopper 18a. An exhaust gas outlet 17 provided on one end wall (not shown in the figure) of the melting furnace main body 9 in the burner type ash melting furnace I is connected to the exhaust gas inlet 19 via an exhaust gas line 23, so that the melting furnace The molten exhaust gas 16 discharged from the main body 9 is guided into the secondary combustion chamber 18 through the exhaust gas line 23,
The unburned gas in the molten exhaust gas 16 is completely burned by the secondary combustion air 24 blown from the secondary air supply unit (not shown) through the secondary air line 25 and the secondary air supply nozzle 21. The exhaust gas 16a after being subjected to the combustion treatment is discharged from the gas outlet 20.

The dust 26 generated when the unburned gas in the molten exhaust gas 16 is burned in the secondary combustion chamber 18 is dropped in the secondary combustion chamber 18 and is dropped at the lower end of the secondary combustion chamber 18. By alternately opening and closing the upper damper 22a and the lower damper 22b of the dust discharger 22 provided, the dust exhauster 22 is discharged to the outside in a state where the atmosphere inside and outside the secondary combustion chamber 18 is shut off.

In addition, in the said ash storage tank pusher 3, incineration residue 2 may inject and leak a little with the operation | movement. Therefore, a suction hood 27 is provided so as to cover the outside of the ash storage tank pusher 3, and the suction hood 27 and the secondary air line 25 are connected to the suction recovery line provided with an ash fusion seal blower 28 in the middle. The recovered air 30 that is connected through the suction ash 27 and sucked and recovered by the suction hood 27 from the incineration residue 2 leaking from the ash storage tank pusher 3 is supplied from the secondary air supply nozzle 21 via the suction recovery line 29 and the secondary air line 25. Secondary combustion air 24 to the secondary combustion chamber 18
By blowing together, it can be used as a part of the air for secondary combustion of the molten exhaust gas 16.

By the way, the ash sump that collects the combustion ash generated in the marine boiler can be cooled by circulating cooling water as a cooling jacket structure having a cooling passage, and the ash sump has an inert gas. It has been conventionally known that an inert gas can be supplied to the combustion ash accumulated in the ash pool by connecting a supply pipe (see, for example, Patent Document 1).

Japanese Utility Model Publication No. 62-192025 Inoue, Narusawa, Nakano, Kishi, “Development of Self-Combustion Internal Melting Furnace”, Proceedings of the 12th JSME Conference, JSCE, October 31, 2001, p. 816-818

However, the dust discharger 22 provided at the lower end of the secondary combustion chamber 18 in the conventional ash melting facility is concerned about the problem of corrosion due to molten salt due to the use environment at high temperatures.

That is, the internal atmosphere of the dust discharger 22 is 700 to 800 ° C. in the upper damper 22a on the inlet side due to the influence of the internal temperature of the secondary combustion chamber 18 that causes the molten exhaust gas 16 to be completely burned. Even if the temperature drops by about 200 ° C. by passing through the upper damper 22a, the lower damper 22b also has a temperature of 500 to 70.
The atmosphere is as high as 0 ° C. On the other hand, in the molten exhaust gas 16 to be treated in the secondary combustion chamber 18, there may be salts such as alkali salts such as K, Ca, Na, sulfates, etc. derived from the incinerated waste. In a so-called high temperature corrosion temperature range of 330 ° C. or higher, the metal surface of the dust discharger 22 reacts at a high temperature to generate iron chloride or alkaline iron sulfate, thereby promoting the corrosion reaction. Therefore, when the internal atmospheric temperature of the dust discharger 22 is in the high temperature corrosion temperature range as described above, there is a problem that the inside of the dust discharger 22 is easily corroded.

In addition, the inert gas described in the said patent document 1 is that the unburned part contained in the high-temperature combustion ash collected from the boiler in the ash storage starts secondary combustion in the ash storage, and the combustion heat In order to extinguish the secondary combustion by blowing when the temperature in the ash pool rises due to,
It is not intended to control the temperature of the combustion ash that is not in secondary combustion. Therefore, from what was described in the above-mentioned Patent Document 1, as in the corrosion prevention method and apparatus of the melting furnace secondary combustion chamber dust discharger of the present invention, in order to prevent low temperature corrosion in addition to high temperature corrosion,
There is no suggestion of controlling the ambient temperature.

Therefore, the present invention provides a dust discharger for a melting furnace secondary combustion chamber, which can prevent the occurrence of high temperature corrosion and further prevent the occurrence of low temperature corrosion. An object of the present invention is to provide a corrosion prevention method and apparatus for an ejector.

In order to solve the above problems, the present invention blows cooling air from the outside near the inlet of the dust discharger provided at the lower end of the melting furnace secondary combustion chamber, Corrosion prevention method for the melting furnace secondary combustion chamber dust discharger that lowers the temperature to the required temperature that can suppress high temperature corrosion, and in the vicinity of the dust discharger inlet provided at the lower end of the melting furnace secondary combustion chamber,
A corrosion prevention device for a melting furnace secondary combustion chamber dust discharger having a configuration in which a cooling air blowing nozzle for blowing cooling air is provided.

Also, as the cooling air blown in the vicinity of the inlet of the dust discharger, a method and apparatus are used in which the recovered air obtained by sucking and collecting the incineration residue leaking from the ash storage tank pusher on the upstream side of the ash melting furnace is used.

Furthermore, the temperature of the atmosphere on the inlet side of the dust ejector is set to about 400, which is a relatively low rate of high temperature corrosion.
Set to ℃.

Furthermore, a flow rate adjusting valve is provided upstream of the cooling air blowing nozzle, and a temperature detector is provided in the vicinity of the dust discharger inlet, inside the dust discharger, and / or at the outlet side end of the dust discharger. The flow rate adjusting valve is adjusted based on the temperature detected by the temperature detector so that the amount of air blown from the cooling air blowing nozzle can be adjusted.

According to the present invention, the following excellent effects are exhibited.
(1) It is required that the temperature of the atmosphere on the inlet side of the dust discharger can be controlled to suppress high-temperature corrosion by blowing cooling air from the outside near the inlet of the dust discharger provided at the lower end of the melting furnace secondary combustion chamber. Corrosion prevention method for melting furnace secondary combustion chamber dust discharger lowered to temperature, and cooling air blowing nozzle for blowing cooling air in the vicinity of the inlet of the dust discharger provided at the lower end of the melting furnace secondary combustion chamber Therefore, the internal temperature of the lower end of the melting furnace secondary combustion chamber near the inlet of the dust discharger is lowered, thereby reducing the dust. Since the temperature of the dust and air entering the discharger can be lowered and the internal temperature of the dust discharger can be lowered, the rate at which high temperature corrosion occurs in the dust discharger can be suppressed.
(2) As a cooling air blown in the vicinity of the inlet of the dust discharger, cooling is achieved by using a method and an apparatus in which the recovered air obtained by sucking and collecting the incineration residue leaking from the ash storage tank pusher upstream of the ash melting furnace is used. It is possible to effectively use the recovered air obtained by sucking and collecting the incineration residue leaking from the ash storage tank pusher as the working air, and further, it is necessary to provide a new blower for blowing the cooling air into the lower end of the melting furnace secondary combustion chamber. Can be eliminated.
(3) By setting the temperature of the inlet side atmosphere of the dust discharger to about 400 ° C.,
The internal temperature of the upper damper of the dust discharger can be set to about 400 ° C. where the rate of high-temperature corrosion is relatively low, and further, the temperature is lowered by about 200 ° C. when the material passing through the upper damper reaches the lower damper. However, the internal temperature of the lower damper can be maintained at a temperature higher than 150 ° C. Therefore, the occurrence of high temperature corrosion of the dust discharger can be suppressed, and the possibility of low temperature corrosion occurring on the outlet side of the dust discharger can be prevented.
(4) A flow rate adjustment valve is provided on the upstream side of the cooling air blowing nozzle, and in the vicinity of the inlet of the dust discharger,
A temperature detector is provided in at least one of the inside of the dust discharger and the outlet side end of the dust discharger, and the cooling air is adjusted by adjusting the flow rate adjusting valve based on the temperature detected by the temperature detector. By adopting a configuration that allows the amount of air blown from the blow nozzle to be adjusted, the internal temperature of the dust discharger is automatically maintained within a temperature range that prevents high temperature corrosion and prevents low temperature corrosion. It becomes possible to control.

  The best mode for carrying out the present invention will be described below with reference to the drawings.

FIG. 1 shows an embodiment of a corrosion prevention method and apparatus for a dust discharger of a melting furnace secondary combustion chamber of the present invention. In the same configuration as that shown in FIG. In the vicinity of the inlet of the dust discharger 22, a cooling air blowing nozzle 31 is provided at a position near the inlet of the dust discharger 22, and cooling air to be described later is blown from the outside through the blowing nozzle 31. The ambient temperature can be lowered to the required temperature.

Specifically, a suction collection line 29 for sucking and collecting the incineration residue 2 by having the cooling air blowing nozzle 31 and the suction hood 27 provided outside the ash storage tank pusher 3 and having an ash fusion seal blower 28 in the middle. The incineration residue 2 leaking from the ash storage tank pusher 3 is connected with the suction hood 2
The recovered air 30 sucked and recovered in 7 can be blown into the vicinity of the inlet of the dust discharger 22 from the cooling air blowing nozzle 31 as the cooling air.

The temperature near the inlet of the dust discharger 22 at the lower end of the melting furnace secondary combustion chamber 18 which is lowered by blowing the recovered air 30 from the cooling air blowing nozzle 31 is set to about 400 ° C. This is an upper damper 22 that is opened and closed as the inlet of the dust discharger 22.
The temperature inside a is set to about 400 ° C. at which the high-temperature corrosion rate is relatively low, so that the occurrence of high-temperature corrosion can be suppressed, and the dust 26 and the atmosphere that have passed through the upper damper 22a and then transferred to the lower damper 22b Even if the temperature drops by about 200 ° C., the temperature inside the lower damper 22b can be maintained at a temperature higher than 150 ° C., and thereby the lower damper 22b
This prevents the internal temperature of the gas from decreasing to 150 ° C. or lower, which is the acid dew point, to prevent condensation of acid gas and to prevent the occurrence of low-temperature corrosion on the outlet side of the dust discharger 22. .

Other configurations are the same as those shown in FIG. 3, and the same components are denoted by the same reference numerals.

Thus, according to the corrosion prevention method and apparatus for the secondary combustion chamber dust discharger of the present invention having the above-described configuration, the internal temperature of the dust discharger 22 provided at the lower end of the melting furnace secondary combustion chamber 18 is Since the temperature of the side is maintained at about 400 ° C. or less, the salt contained in the molten exhaust gas 16 is prevented from reacting with the metal surface of the dust discharger 22, and the dust discharger 22 is The rate of high temperature corrosion can be reduced. Moreover, in the dust discharger 22, the inlet side temperature is set to about 400 ° C. to prevent the ambient temperature from becoming 150 ° C. or lower even on the outlet side. Can be prevented.

Further, as the cooling air for cooling the vicinity of the inlet of the dust discharger 22, the recovery air 30 that suctions and collects the incineration residue 2 leaking from the ash storage tank pusher 3 can be used, and the suction recovery that distributes the recovery air 30. Since the ash melt seal blower 28 is provided in the line 29, it is not necessary to newly provide a blower for blowing cooling air into the lower end portion of the melting furnace secondary combustion chamber 18.

The recovered air 3 blown near the inlet of the dust discharger 22 of the melting furnace secondary combustion chamber 18.
0 includes the incineration residue 2 leaked from the ash storage tank pusher 3.
Since 2 is not always open, the recovered air 30 after being used for cooling the inlet side of the dust discharger 22 is mostly in the melting furnace secondary combustion chamber 18 as in the prior art. Is used as secondary combustion air for completely burning the molten exhaust gas 16.

Next, FIG. 2 shows another embodiment of the present invention. In the same configuration as shown in FIG. 1, the temperature near the inlet of the dust discharger 22 is arranged at the lower end of the melting furnace secondary combustion chamber 18. And a cooling air blowing nozzle 3 in the suction recovery line 29 are provided.
1 is provided with a flow rate adjustment valve 33 at an upstream position, and a controller 34 for giving a command to the flow rate adjustment valve 33 based on a temperature detection signal input from the temperature detector 32. It is.

The controller 34 is configured so that the temperature detected by the temperature detector 32 is about 400 ° C.
The opening of the flow rate adjusting valve 33 is controlled to adjust the flow rate of the recovered air 30 that is blown from the cooling air blowing nozzle 31 to the vicinity of the inlet of the dust discharger 22. That is, when the temperature detected by the temperature detector 32 is higher than 400 ° C., the opening amount of the flow rate adjusting valve 33 is increased to increase the amount of the recovered air 30 to be blown in, while the temperature detected by the temperature detector 32 is increased. Is lower than 400 ° C., the recovered air 30 to be blown in with the opening of the flow rate adjusting valve 33 being reduced.
It suffices to reduce the amount of.

The recovered air 30 flowing through the suction recovery line 29 is changed to the cooling air blowing nozzle 31.
If the flow rate is limited when the air is blown into the vicinity of the inlet of the dust discharger 22 as cooling air, surplus is generated in the recovered air 30. In this case, in order to be able to supply this surplus to the melting furnace secondary combustion chamber 18 as air for secondary combustion of the molten exhaust gas 16, the upstream side of the flow rate adjustment valve 33 in the suction recovery line 29. A branch pipe 35 may be provided at a position, and the branch pipe 35 may be connected to a midway position of the secondary air line 25. Other configurations are the same as those shown in FIG. 1, and the same components are denoted by the same reference numerals.

According to this embodiment, even if the internal temperature of the melting furnace secondary combustion chamber 18 changes, it is possible to automatically control the temperature in the vicinity of the inlet of the dust discharger 22 to be maintained at about 400 ° C. Become.

In addition, this invention is not limited only to the said embodiment, The cooling air blowing nozzle 3
If the temperature near the inlet of the dust discharger 22 can be lowered to about 400 ° C. by blowing into the lower end of the melting furnace secondary combustion chamber 18, the cooling air supplied to 1 is simply a low temperature taken from the outside. Or low-temperature air other than the recovered air 30, such as low-temperature air circulated by a blower other than the ash fusion seal blower 28 provided in the ash melting facility. As an ash melting furnace, if it is of a type having a melting furnace secondary combustion chamber 18, self-combustion type internal melting such as a rotary surface melting furnace, a coke bed type ash melting furnace, a DC electric resistance type ash melting furnace, etc. The present invention can also be applied to a dust discharger 22 in a secondary combustion chamber 18 of a melting furnace of an ash melting furnace of a type other than the burner type melting furnace I, such as a furnace or an ash melting furnace other than the self-combustion type. As the temperature at which the vicinity of the inlet of the dust discharger 22 should be lowered, if the temperature on the outlet side of the dust discharger 22 does not become 150 ° C. or lower, it passes through the upper and lower dampers 22a and 22b of the dust discharger 22. Depending on the temperature drop rate of the dust 26, 400 ° C. may be slightly changed. The temperature detector 32 in the embodiment of FIG. 2 is configured so that the temperature drop rate of the dust 26 due to passing through the dust discharger 22 is clear, and the inside of the dust discharger 22 or the outlet of the dust discharger 22. It may be possible to detect by estimating the inlet side temperature of the dust discharger 22 provided on the side, and temperature detectors are provided on both the inlet side and the outlet side of the dust discharger 22 so that the inlet side The amount of air blown from the cooling air nozzle 31 is adjusted based on the detected temperature of each temperature detector so that the temperature of the air does not rise to the high temperature corrosion zone and the temperature on the outlet side does not fall to the low temperature corrosion zone. Of course, various modifications can be made without departing from the scope of the present invention.

It is a schematic diagram showing one embodiment of a corrosion prevention method and apparatus for a melting furnace secondary combustion chamber dust discharger of the present invention. It is a schematic diagram which shows the other form of implementation of this invention. It is a schematic diagram which shows the conventionally used ash melting equipment.

Explanation of symbols

I Burner melting furnace (ash melting furnace)
2 Incineration residue 3 Ash storage tank pusher 18 Melting furnace secondary combustion chamber 22 Dust discharger 29 Suction recovery line 30 Recovery air (cooling air)
31 Cooling air blowing nozzle 32 Temperature detector 33 Flow control valve

Claims (6)

Cooling air is blown from the outside near the inlet of the dust discharger provided at the lower end of the melting furnace secondary combustion chamber, and the temperature of the atmosphere on the inlet side of the dust discharger is lowered to the required temperature that can suppress high-temperature corrosion. A method for preventing corrosion of a dust discharger in a secondary combustion chamber of a melting furnace. 2. The melting furnace secondary combustion chamber dust according to claim 1, wherein the recovered air obtained by sucking and collecting incineration residue leaking from the ash storage tank pusher on the upstream side of the ash melting furnace is used as the cooling air blown near the inlet of the dust discharger. Corrosion prevention method for ejector. The method for preventing corrosion of a melting furnace secondary combustion chamber dust discharger according to claim 1 or 2, wherein the temperature of the atmosphere on the inlet side of the dust discharger is about 400 ° C. Dust discharge of the melting furnace secondary combustion chamber characterized by having a configuration in which a cooling air blowing nozzle for blowing cooling air is provided in the vicinity of the inlet of the dust discharger provided at the lower end of the melting furnace secondary combustion chamber Machine corrosion prevention device. 5. The melting furnace secondary combustion chamber dust according to claim 4, wherein a downstream end of a suction recovery line for sucking and collecting incineration residue leaking from an ash storage tank pusher upstream of the ash melting furnace is connected to the cooling air blowing nozzle. Corrosion prevention device for discharge machine. A flow rate adjusting valve is provided on the upstream side of the cooling air blowing nozzle, and a temperature detector is provided in at least one of the vicinity of the inlet of the dust discharger, the inside of the dust discharger, and the end on the outlet side of the dust discharger. 6. The melting furnace secondary combustion chamber dust discharge according to claim 4, wherein the amount of air blown from the cooling air blowing nozzle can be adjusted by adjusting the flow rate adjusting valve based on the temperature detected by the detector. Machine corrosion prevention device.

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