JP5440822B1 - Recuperator operation method and exhaust gas treatment facility operation method - Google Patents

Abstract

The present invention provides a heat exchanger capable of efficiently discharging dust generated from exhaust gas with a decrease in temperature and an operation method thereof.
A heat exchanger according to the present invention includes a first element in which a flow path of exhaust gas discharged from a metal reduction treatment facility and containing volatile components extends from above to below, and is disposed downstream of the first element. The exhaust gas flow path extends from below to above, the second element is connected to the first element and the second element, and the dust collecting part is configured to collect the generated dust. An air flow path for flowing cooling air toward the first element.
[Selection] Figure 4

Description

The present invention relates to a recuperator used for heat recovery from exhaust gas discharged from a rotary hearth furnace and containing volatile components, and an operation method of an exhaust gas treatment facility provided with the recuperator .

  From a metal reduction treatment facility such as a rotary hearth furnace or a tunnel furnace, exhaust gas containing volatile components contained in the raw material is discharged. Examples of the volatile component include zinc, lead, and chlorine. The exhaust gas containing these volatile components is sent to an exhaust gas treatment facility. Exhaust gas treatment facilities are equipped with waste heat recovery devices (boilers, recuperators, etc.) for the purpose of heat recovery from high-temperature exhaust gas, and heat exchange between the high-temperature exhaust gas and refrigerant is carried out through these heat transfer surfaces. Is called.

  When the temperature of the exhaust gas containing volatile components decreases, the volatile components solidify and dust is generated, which adheres to the heat transfer surface of the heat exchanger. When the amount of dust attached increases, the heat recovery rate of the heat exchanger decreases, and when this further proceeds, the gas flow path is blocked, leading to operation stop. In order to prevent this, it is necessary to periodically stop and clean the exhaust gas treatment facility. However, when the exhaust gas treatment facility must be cleaned at a high frequency, the operating rate of the metal reduction treatment facility is significantly reduced.

  In order to maintain a high operation rate of the exhaust gas treatment facility and consequently a high operation rate of the metal reduction treatment facility, for example, as shown in Patent Document 1 below, a refrigerant (air or water) is disposed in the exhaust gas path upstream of the heat exchanger. ) Is known to supply. By reducing the temperature of the exhaust gas introduced into the heat exchanger, it is possible to prevent dust from firmly adhering to the heat transfer surface of the heat exchanger.

JP 2001-33173 A

  In the heat exchanger arranged at the rear stage of the metal reduction treatment facility, dust is generated from the exhaust gas as the temperature of the exhaust gas decreases as described above. Conventional heat exchangers may not be able to efficiently discharge when much dust is generated, and there is room for improvement in this regard.

The present invention has been made to solve the above problems, and an object of the present invention is to provide a recuperator capable of efficiently discharging dust generated from exhaust gas as the temperature drops and an operating method of an exhaust gas treatment facility including the same. To do.

A recuperator according to the present invention includes a first element in which a flow path of exhaust gas discharged from a rotary hearth furnace and containing a volatile component extends downward from above, a downstream of the first element, and the flow path of exhaust gas A second element extending upward from below, a dust collecting part for collecting dust generated while forming a connection part between the first element and the second element, and a dust discharge device provided in the dust collecting part, An air flow path for flowing cooling air from the last-stage element toward the front-most first element, and an opening for supplying cold air or pressurized water provided on the upstream side of the exhaust gas flow path are provided.

The recuperator is composed of a plurality of elements. Normally, a large amount of dust is generated in the foremost element (first element) into which the high-temperature exhaust gas is first introduced due to a decrease in the temperature of the exhaust gas, and the amount of dust generated decreases toward the subsequent element. For this reason, a flow path is provided in the first element so that the exhaust gas flows downward from above, so that a large amount of dust generated in the first element is easily collected in the dust collecting section. A flow path is provided in the element so that the exhaust gas flows from below to above, and a dust collecting portion is provided between these flow paths.

In a heat exchanger that uses air as a refrigerant, from the viewpoint of a high heat recovery rate, as described above, it is common to flow cooling air from the last-stage element toward the foremost first element. . In the present invention, in the case where it is necessary to rapidly cool the exhaust gas, the air flows from the first element toward the last element, that is, the exhaust gas flow and the parallel flow. Thus, the flow direction of air can be freely changed . By rapidly cooling the exhaust gas, volatile components contained in the exhaust gas are solidified at a stretch to become dust, and the dust can be prevented from being fused to the heat transfer surface. On the other hand, if the exhaust gas is not rapidly cooled, the liquefied volatile component is fused to the heat transfer surface and solidifies on the heat transfer surface. The solidified material fused on the heat transfer surface adheres firmly to the heat transfer surface and requires a lot of labor and time for the removal work.

The recuperator comprises a supply opening of the cold air or pressurized water is provided in the exhaust gas line upstream thereof. By providing such openings, prior to the exhaust gas is introduced into the recuperator can lower the temperature of the exhaust gas, the volatile component to the heat transfer surface of the recuperator can be prevented from fusing.

The recuperator may include a nozzle that injects air toward the heat transfer surface on the exhaust gas side. By continuously or intermittently injecting air from the nozzle, dust adhering to the heat transfer surface can be removed, thereby maintaining a high heat recovery rate.

The present invention provides a method for operating the recuperator . The operation method of the recuperator includes a step of flowing the exhaust gas from above to below the flow path of the exhaust gas in the first element, and a step of flowing cooling air from the last element toward the first element. . By flowing the exhaust gas in this way, dust generated in a large amount in the first element can be efficiently collected by the dust collecting part.

As described above, since the recuperator is freely configurable flow direction of the air, the method of operation, depending on the amount of dust generated from the exhaust gas, cooling air is directed to the elements of the last stage from the first element You may further provide the process of changing the flow direction of air so that it may flow. For example, the flow direction of the cooling air may be changed according to the zinc concentration of the raw material supplied to the rotary hearth furnace .

ADVANTAGE OF THE INVENTION According to this invention, the operating method of the recuperator which can discharge | emit efficiently the dust which generate | occur | produced from exhaust gas with the temperature fall, and an exhaust gas treatment facility provided with the same is provided.

It is a schematic block diagram which shows typically the waste gas processing equipment provided with the heat exchanger (recuperator) which concerns on embodiment of this invention. It is sectional drawing which shows typically the internal structure of a recuperator (heat exchanger). It is a graph which shows the quantity of the volatile matter which solidifies in each element of the 1-4th step | stage of a recuperator. It is a schematic diagram which shows the movement direction of the waste gas and dust in the 1st-stage element of a recuperator. (A) is a schematic diagram which shows the state which made exhaust gas and cooling air counter flow in a recuperator, (b) is a schematic diagram which shows the state which made exhaust gas and cooling air into parallel flow. It is a graph which shows the temperature of the waste gas and cooling air in a recuperator. It is a list | wrist which shows the example of the dust adhesion prevention measure which should be taken according to the zinc concentration of a raw material. It is a schematic block diagram which shows typically other embodiment of the waste gas processing equipment which concerns on this invention. It is a schematic block diagram which shows typically other embodiment of the waste gas processing equipment which concerns on this invention. It is a schematic block diagram which shows an example of the conventional waste gas processing equipment. It is a schematic diagram which shows the movement direction of the waste gas and dust in the 1st step | level element of the conventional recuperator.

  Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the drawings. In the description, the same reference numerals are used for the same elements or elements having the same function, and a duplicate description is omitted.

<Exhaust gas treatment equipment>
FIG. 1 is a schematic configuration diagram schematically showing an exhaust gas treatment facility provided with a heat exchanger (recuperator) according to an embodiment of the present invention. The exhaust gas treatment facility 50 shown in the figure is for recovering heat from the exhaust gas from the rotary hearth furnace (metal reduction treatment facility) 1 and separating and removing dust from the exhaust gas. Here, although the case where the exhaust gas from the rotary hearth furnace 1 is treated is illustrated, the exhaust gas treatment equipment 50 may be used for exhaust gas treatment from metal reduction treatment equipment other than the rotary hearth furnace 1.

  The rotary hearth furnace 1 is an apparatus for recovering metal by reducing metal oxide. The rotary hearth furnace 1 has an annular hearth, on which raw material pellets are spread, and the raw material pellets move in the high-temperature furnace by rotating the hearth in this state. The raw material pellet is a pellet of a mixture of a powder containing metal oxide and a carbon-based reducing agent. When the raw material pellets are heat-treated at a temperature of about 1200 to 1350 ° C. for about 5 to 20 minutes on the hearth, the reducing agent reduces the metal oxide to obtain a metal. High-temperature exhaust gas is generated by the combustion of the reducing agent and the combustion of fuel for heating the inside of the furnace. The temperature of the exhaust gas is about 900 to 1200 ° C. at the outlet of the rotary hearth furnace 1 (inlet of the duct 2). The exhaust gas contains components volatilized from the raw material pellets. Specific examples of the volatile component include volatile metals such as zinc, lead and alkali metals, and chlorine.

  The exhaust gas treatment facility 50 includes a boiler 3 connected to the duct 2 of the rotary hearth furnace 1, a recuperator (heat exchanger) 5, a spray cooling tower (cooler) 6, a baghouse 7, an induction fan 8, And a chimney 9. The pipeline L1 connected to the outlet of the boiler 3 branches off in the middle, one pipeline L1a is connected to the recuperator 5, and the other pipeline L1b is connected to the spray cooling tower 6. The pipe L2a connected to the outlet of the recuperator 5 and the pipe L2b connected to the outlet of the spray cooling tower 6 merge to form one pipe L2 and reach the baghouse 7. On-off valves (switching valves) V1-V4 are provided in the middle of the pipe lines L1a, L1b and the pipe lines L2a, L2b, and the exhaust gas flow paths can be switched by operating these valves. The exit of the baghouse 7 and the chimney 9 are connected by a pipe L3, and an induction fan 8 is provided in the middle of the pipe L3.

  In the exhaust gas treatment facility 50, the recuperator 5 and the spray cooling tower 6 are provided in parallel, and the on-off valves V1-V4 are disposed in the pipeline. Accordingly, it is possible to select whether the destination of the exhaust gas is the recuperator 5 or the spray cooling tower 6 according to the amount of dust generated from the exhaust gas, and the exhaust gas flows into both the recuperator 5 and the spray cooling tower 6. It can also be made. For this reason, even if the generation amount of dust greatly fluctuates with the fluctuation of the composition and amount of the raw material supplied to the rotary hearth furnace 1, the exhaust gas treatment can be appropriately performed. Each configuration will be described below.

  The boiler 3 is for generating water vapor using the heat of high-temperature exhaust gas. The boiler 3 is connected to the outlet of the duct 2.

  The recuperator 5 is for exchanging heat between exhaust gas and cooling air (refrigerant) via a heat transfer surface. The recuperator 5 collects the heat of the exhaust gas and coagulates volatile components from the exhaust gas whose temperature has decreased, and can separate and remove it as dust. The recuperator 5 in the present embodiment is composed of four elements E1-E4. FIG. 2 is a cross-sectional view schematically showing the internal structure of the first-stage element E1. As shown in the figure, a plurality of flat ducts 5a are provided in the element E1, and cooling air flows through these ducts 5a, and an outer surface (heat transfer surface) 5b of the duct 5a and an outer frame The exhaust gas flows through the flow path 5d defined by the inner surface 5c. Element E2-4 has the same configuration as element E1. Each element of the recuperator 5 may have a nozzle 5e that injects air toward the outer surface 5b of the pipe line 5a. By injecting air continuously or intermittently from the nozzle 5e, dust adhering to the outer surface 5b of the pipe line 5a can be removed, thereby maintaining a high heat recovery rate. In order to maintain a high heat recovery rate, a mechanism for mechanically scraping off dust adhering to the outer surface 5b of the pipe line 5a may be employed. A nozzle (not shown) similar to the nozzle 5e may be installed in the exhaust gas conduit in the boiler 3.

  The four elements E1 to E4 are arranged in series, the element (first element) E1 is provided on the most upstream side of the exhaust gas flow path, and the element E2 (second element) and the element E3 follow in the subsequent stage. The element E4 is provided on the most downstream side of the exhaust gas flow path. Note that the number of elements is not limited to four.

  In the element E1 into which the high temperature exhaust gas is introduced, a large amount of dust is generated due to the temperature decrease of the exhaust gas. In the subsequent elements E2-E4, the amount of dust generated is smaller than that of the element E1 (see FIG. 3). In the present embodiment, as shown in FIG. 4, the exhaust gas flows from above to below in the flow path 5d in the element E1, and the exhaust gas flows from below to above in the flow path 5d in the element E2. The white arrow G indicates the flow direction of exhaust gas, and the gray arrow D indicates the direction of dust movement. A dust collecting portion 5f is provided at a connection portion between the element E1 and the element E2, that is, a portion where the flow of the exhaust gas changes from below to above. With such a configuration, dust generated from the exhaust gas as the temperature decreases can be efficiently separated in the dust collecting portion 5f. A dust collecting portion 5f is also provided at a connection portion between the element E3 and the element E4. The dust collecting unit 5f is provided with a dust discharging device 5g. The dust discharge device 5g may be configured to include, for example, a screw conveyor disposed in the dust collecting unit 5f and a rotary valve that discharges the dust carried by the screw conveyor.

  From the viewpoint of generating a sufficient amount of dust in the element E1, the exhaust gas temperature at the outlet of the element E1 is preferably 500 to 400 ° C.

  The cooling air is introduced into the element E4 by the fan 10, sequentially passes through the elements E3, E2, and E1, and the air that has absorbed heat is discharged from the element E1. From the viewpoint of a high heat recovery rate, it is general to flow cooling air from the element E4 toward the element E1 (see FIG. 5A). In the present embodiment, for example, when it is necessary to rapidly cool the exhaust gas, the air flows in the flow path from the element E1 to the element E4, that is, in parallel with the flow of the exhaust gas. It is comprised so that the flow direction of air can be changed (FIG.5 (b)). Specifically, a plurality of valves may be provided in the cooling air pipe so that the cooling air can be switched between the inlet and the outlet of the recuperator 5.

  FIG. 6 is a graph showing the temperatures of exhaust gas and cooling air in the recuperator 5. A solid line indicates a case where the flow of cooling air is opposite to the exhaust gas, and a dashed line indicates a case where the flow of cooling air is parallel to the exhaust gas. As shown in FIG. 6, the amount of recovered heat is reduced by the parallel flow, but the temperature reduction of the exhaust gas in the element E1 (first stage) becomes remarkable. By rapidly cooling the exhaust gas, it is possible to suppress the volatile components contained in the exhaust gas from being solidified at a stretch and becoming dust, and fusing the dust to the outer surface 5b of the pipe line 5a. Thereby, the labor and time required for the cleaning operation of the recuperator 5 can be reduced.

  From the viewpoint of generating a sufficient amount of dust in the recuperator 5, the exhaust gas temperature at the outlet of the recuperator 5 (the outlet of the element E4) is preferably 300 ° C. or lower. An opening 5h for supplying cold air or pressurized water may be provided in the exhaust gas flow path (for example, the pipe line L1) on the upstream side of the recuperator 5 so that the temperature of the exhaust gas introduced into the recuperator 5 can be lowered in advance. By supplying cold air or pressurized water from the opening 5h, the temperature of the exhaust gas can be lowered before the exhaust gas is introduced into the recuperator 5, and the fusion of volatile components to the heat transfer surface of the recuperator 5 can be suppressed.

  In addition, FIG. 10 is a schematic block diagram which shows an example of the waste gas processing equipment provided with the conventional recuperator. The exhaust gas treatment facility 60 shown in the figure does not include the spray cooling tower 6, and the arrangement of the four elements of the recuperator 5 'is different from the exhaust gas treatment facility 50 according to the present embodiment. First, since the spray cooling tower 6 is not provided, the exhaust gas discharged from the boiler 3 must be always introduced into the recuperator 5 ′, and it is not possible to flexibly cope with fluctuations in the amount of dust generated. In the exhaust gas treatment facility 60, the elements E1 ′ and E2 ′ are arranged in the vertical direction and the elements E3 ′ and E4 ′ are arranged in the vertical direction from the viewpoint of reducing the site area. As shown in FIG. 11, the exhaust gas from the boiler 3 flows upward in the element E1 ′. On the other hand, the dust generated in the element E1 ′ tends to fall downward due to gravity. However, it is difficult for the dust to settle due to upward exhaust gas, and there is a possibility that the dust cannot be separated and removed sufficiently efficiently.

  The spray cooling tower 6 is provided in parallel with the recuperator 5, and is for rapidly cooling the exhaust gas as necessary. In the spray cooling tower 6, water is injected to the exhaust gas. Depending on the extent to which the exhaust gas temperature is lowered in the spray cooling tower 6, it is preferable to keep the amount of water injection to the minimum necessary so as not to cause troubles due to condensation and water-containing dust.

  The baghouse 7 contains a bag filter and is used for dust removal processing of exhaust gas introduced from the pipe L2. The exhaust gas temperature at the entrance of the baghouse 7 is preferably 120 to 190 ° C, more preferably 150 to 180 ° C. If the exhaust gas temperature is less than 120 ° C, acid corrosion is likely to occur in the bag house 7, while if it exceeds 190 ° C, the bag filter is likely to be burned out. The duct L2 is provided with an air supply duct 7a. By introducing air from the duct 7a into the duct L2, the exhaust gas temperature supplied to the baghouse 7 can be lowered. In addition, you may employ | adopt another dust collector instead of the baghouse 7, For example, a wet scrubber, an electric dust collector, etc. are mentioned.

  The exhaust gas from the baghouse 7 is introduced into the chimney 9 through the pipe L3, and is discharged from the tip of the chimney 9 to the atmosphere. Note that the air heated by the exhaust gas in the recuperator 5 is sent to the rotary hearth furnace 1, for example, and used as air for burning fuel.

<Exhaust gas treatment method>
Next, a method for treating exhaust gas with the exhaust gas treatment facility 50 will be described. In the exhaust gas treatment method according to the present embodiment, the flow of cooling air in the recuperator 5 according to the amount of dust generated from the exhaust gas, more specifically, according to the zinc concentration of the raw material supplied to the rotary hearth furnace 1. While changing the direction (FIG. 7 (4) air blowing direction change), it is selected whether to use one or both of the recuperator 5 and spray cooling tower 6 (FIG. 7 (5) spray cooling tower (combination / switching) ). FIG. 7 is a list of operation measures to be implemented at each stage when the zinc concentration of the raw material is divided into four stages. In addition, the following countermeasures may be implemented as appropriate regardless of the zinc concentration of the raw material, or may not be implemented.

  (1) Cold air blowing and (2) pressurized water blowing are measures implemented when the zinc concentration of the raw material is small (for example, more than 0.6 mass% and 1.5 mass% or less). By introducing cold air and / or pressurized water from the opening 5h, the exhaust gas temperature is lowered, dust in the exhaust gas is actively solidified, and volatile components are prevented from fusing to the equipment. In order to reduce the exhaust gas flow rate, pressurized water with a high temperature reduction effect per blowing rate is used preferentially until the exhaust gas moisture reaches a predetermined level (for example, 10%). It is preferable to reduce. When the pressurized water is introduced until the moisture content of the exhaust gas exceeds 10%, the bag house 7 is liable to be clogged with moisture or malfunction due to condensation.

  (3) The increase in the amount of cooling air is a measure implemented when the zinc concentration of the raw material is moderate (for example, more than 1.5 mass% and 4.0 mass% or less). By increasing the amount of cooling air in the recuperator 5, the outer surface temperature of the pipe line 5a is lowered, and dust is positively solidified on the outer surface 5b of the pipe line 5a to prevent the volatile components from fusing to the equipment. The pressure loss of the exhaust gas in the recuperator 5 may be monitored, and may be appropriately implemented when the value increases.

  (4) The air blowing direction change is a measure implemented when the zinc concentration of the raw material is medium (for example, more than 1.5 mass% and 4.0 mass% or less). By rapidly cooling the exhaust gas in the element E1 of the recuperator 5, it is possible to suppress volatile components contained in the exhaust gas from solidifying all at once to become dust and preventing the dust from fusing to the dust collecting part 5b of the pipe line 5a (FIG. 5). 6).

  (5) The spray cooling tower (combination / switching) is a measure implemented when the zinc concentration of the raw material is large (for example, more than 4.0% by mass). In order not to use the recuperator 5 where dust adhesion is intense or to reduce the amount of exhaust gas treated by the recuperator 5, all or part of the exhaust gas is introduced into the spray cooling tower 6, and the exhaust gas is cooled in the spray cooling tower 6.

  (6) As shown in FIG. 7, online air purge is a measure that can be performed at all times, and air from a nozzle (for example, the nozzle 5 e) toward the wall surface of a pipeline through which exhaust gas in the boiler 3 or the recuperator 5 flows. It is possible to blow off the adhered dust by spraying.

  (7) The recuperator bypass is a measure for continuing the operation even during cleaning of the recuperator 5 by temporarily introducing exhaust gas into the spray cooling tower 6 when cleaning the recuperator 5.

  (8) Offline soot blow is a measure for shortening boiler cleaning time. When the zinc concentration of the raw material is medium or higher, soot blow is performed in the boiler 3.

  The operating method of the recuperator 5 during normal operation and when the above (1) and (2) are performed is as follows. The exhaust gas flow path 5d in the element E1 is directed downward from above to emit exhaust gas. And a step of flowing cooling air from the element E4 toward the element E1 (see FIG. 5A). By flowing the exhaust gas in this way, dust generated in a large amount in the element E1 can be efficiently collected by the dust collecting part 5f.

  When the above (3) is performed, a step of changing the air flow direction is performed so that the cooling air flows from the element E1 toward the element E2.

  In the exhaust gas treatment method according to the present embodiment, one of the recuperator 5 and the spray cooling tower 6 can be used to perform the other cleaning operation while continuing the operation of the exhaust gas treatment facility 50. According to this embodiment, the period during which the operation must be stopped for maintenance and inspection can be minimized, and a high operating rate can be realized.

  According to this embodiment, even if an exhaust gas whose volatile component content may vary within a range of 0.1 to 10% by mass or more is an object to be treated, an exhaust gas is supplied to one or both of the recuperator 5 and the spray cooling tower 6. By switching the flow path so as to introduce the exhaust gas, the exhaust gas treatment can be performed flexibly. For example, the recuperator 5 can be used when the amount of dust is small, the spray cooling tower 6 can be used when the amount of dust is large, and the recuperator 5 and the spray cooling tower 6 can be used together when the amount of dust is further large. In addition, the trouble caused by condensation and water-containing dust can be minimized by carrying out only when cooling by the spray cooling tower 6 is necessary.

  According to this embodiment, the dust generated from the exhaust gas as the temperature decreases in the recuperator 5 can be efficiently separated. For this reason, it is possible to reduce the burden on the baghouse 7 subsequent to the recuperator 5.

  The preferred embodiment of the present invention has been described in detail above, but the present invention is not limited to the above embodiment. For example, in the said embodiment, although the transfer destination of the waste gas after passing the boiler 3 was illustrated to the recuperator 5 or the spray cooling tower 6, the mode from which the duct 2 was connected as shown in FIG. Branching in the middle, connecting one pipe line 2a to the boiler 3, connecting the other pipe line 2b to the spray cooling tower 6, and providing on-off valves Va and Vb in these pipe lines, respectively, The destination of the exhaust gas from 2 may be switched. For example, by closing the on-off valve Va and opening the on-off valve Vb, exhaust gas can be introduced into the spray cooling tower 6 and the boiler 3 and the recuperator 5 can be bypassed. This configuration is useful when it is expected that the dust adheres in the boiler 3 significantly, or when the operation is continued even when the operation is stopped due to the cleaning operation of the boiler 3. As shown in FIG. 9, the branched pipe line 2b may be communicated with the pipe line L1b. In this case, by operating a plurality of on-off valves including the on-off valves Va and Vb, it becomes possible to flexibly change the destination of the exhaust gas in accordance with the dust generation situation.

  Moreover, in the said embodiment, although the rotary hearth furnace 1 was illustrated as metal reduction processing equipment and the case where the waste gas from the rotary hearth furnace 1 was processed with the exhaust gas treatment equipment 50 was demonstrated, a tunnel furnace, a rotary kiln, or a shaft furnace The exhaust gas from the exhaust gas processing facility 50 may be processed.

  Furthermore, in the above-described embodiment, the case where the recuperator 5 that uses air as a refrigerant is employed as a particularly preferable example. However, instead of the recuperator 5, a heat exchanger capable of exchanging heat with exhaust gas is employed. May be. For example, a heat exchanger that uses a liquid such as water instead of air as a refrigerant may be used.

DESCRIPTION OF SYMBOLS 1 ... Rotary hearth furnace (metal reduction processing equipment), 3 ... Boiler, 5 ... Recuperator (heat exchanger), 5a ... Flat pipe line (air flow path), 5b ... Outer surface of flat pipe line (heat transfer surface) 5d ... exhaust gas flow path, 5e ... nozzle, 5f ... dust collecting part, 5h ... supply opening, 6 ... spray cooling tower (cooler), 50 ... exhaust gas treatment equipment, E1 ... element (first element), E2 ... Element (second element), E3 ... Element, E4 ... Element (last element), A ... Arrow indicating air flow, D ... Arrow indicating dust settling direction, G ... Arrow indicating exhaust gas flow , V1, V2, V3, V4, Va, Vb ... open / close valves (switching valves).

Claims (4)

A method of operating a recuperator used for heat recovery from exhaust gas discharged from a rotary hearth furnace and containing volatile components ,
The recuperator is
A first element in which the flow path of the exhaust gas extends downward from above;
A second element that is disposed downstream of the first element and in which an exhaust gas flow path extends upward from below;
A dust collecting part that collects the generated dust, while forming a connection part between the first element and the second element;
A dust discharge device provided in the dust collecting section;
An air flow path for flowing cooling air from the last-stage element to the first-stage first element;
An opening for supplying cold air or pressurized water provided upstream of the flow path of the exhaust gas;
The air flow direction can be changed so that air flows through the air flow path from the first element toward the last element.
The driving method is
Flowing the exhaust gas in the first element from above to flow downward, and flowing the exhaust gas in the second element from below to above,
Discharging the dust collected in the dust collecting part from the dust collecting part by the dust discharging device;
The following step A, step B and step C performed according to the zinc concentration of the raw material supplied to the rotary hearth furnace:
(Step A) a step of flowing cooling air through the air flow path from the last-stage element toward the first element when the zinc concentration of the raw material is less than 0.6% by mass;
(Step B) When the zinc concentration of the raw material is more than 0.6% by mass and not more than 1.5% by mass, cooling air is supplied to the air flow channel from the last element to the first element. A step of reducing the temperature of exhaust gas introduced into the recuperator by introducing cold air and / or pressurized water from the supply opening;
(Step C) When the zinc concentration of the raw material is more than 1.5% by mass and 4.0% by mass or less, the amount of the cooling air is more than when the zinc concentration of the raw material is less than 4.0% by mass. And changing the air blowing direction so that the cooling air flows from the first element toward the last element;
A recuperator operating method comprising: The recuperator operating method according to claim 1, wherein the recuperator has a mechanism for mechanically scraping dust adhering to the heat transfer surface on the exhaust gas side. The recuperator operating method according to claim 1 , wherein the recuperator includes a nozzle that injects air toward a heat transfer surface on an exhaust gas side . An exhaust gas treatment facility operating method in which exhaust gas discharged from a rotary hearth furnace and containing volatile components is introduced,
The exhaust gas treatment facility is
A recuperator used for heat recovery from the exhaust gas,
A cooler for cooling the exhaust gas by spraying water on the exhaust gas;
A switching valve for switching the exhaust gas flow path so that the exhaust gas is introduced into one or both of the recuperator and the cooler;
With
The recuperator is
A first element in which the flow path of the exhaust gas extends downward from above;
A second element that is disposed downstream of the first element and in which an exhaust gas flow path extends upward from below;
A dust collecting part that collects the generated dust, while forming a connection part between the first element and the second element;
A dust discharge device provided in the dust collecting section;
An air flow path for flowing cooling air from the last-stage element to the first-stage first element;
An opening for supplying cold air or pressurized water provided upstream of the flow path of the exhaust gas;
The air flow direction can be changed so that air flows through the air flow path from the first element toward the last element.
The driving method is
When the zinc concentration of the raw material is 4.0% by mass or less, the entire amount of the exhaust gas is introduced into the recuperator, and the recuperator operating method according to any one of claims 1 to 3 is performed.
When the zinc concentration of the raw material is more than 4.0% by mass, the following step D:
(Step D) A step of introducing all or part of the exhaust gas into the cooler by operating the switching valve, and cooling the exhaust gas in the cooler;
A method for operating an exhaust gas treatment facility.

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