JPH10160370A - Heat exchanger and method of operation - Google Patents

Abstract

PROBLEM TO BE SOLVED: To obtain clean high temperature gas without containing dust by heat recovering from high temperature exhaust gas containing the dust. SOLUTION: A first fluidized bed heat exchanger 45 constituting fluidized beds 44a and 44b, a second fluidized bed heat exchanger 49 constituting fluidized beds 48a and 48b, high temperature exhaust gas containing the dust is fed to the first fluidized bed heat exchanger 45, the clean gas without containing dust as the air is fed to the second fluidized bed heat exchanger 49. Heating medium is supplied through a fourth air tight exhaust means 51 from the fluidized bed 48b that is at the under step of the second fluidized bed heat exchanger 49 to the fluidized bed 44a that is at the upper step of the first fluidized bed heat exchanger 45 by a transferring means 87. Heating medium forming the fluidized bed 44b that is at the under step of the first fluidized bed heat exchanger 45 is conducted to the fluidized bed 48a that is at the upper step of the second fluidized bed heat exchanger 49 by chutes 83 and 84 being intervened with a third air tight exhausting means 50. The clean gas without containing the dust is heated by the exhaust gas containing the dust through indirect heat exchange circulating heating medium.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION The present invention relates to a fluid medium, such as silica, limestone and iron powder, which is used as a heat medium and which is supplied with high-temperature exhaust gas containing dust from a firing furnace or the like. Circulation between the bed heat exchanger and the other fluidized bed heat exchanger to which a low-temperature gas to be heated, such as normal-temperature air, is supplied, and the sensible heat of the high-temperature exhaust gas containing the dust is converted to the low-temperature gas to be heated. And a method for operating the same.

[0002]

2. Description of the Related Art FIG. 16 is a simplified cross-sectional view showing a typical prior art heat exchange device 1. This prior art is disclosed, for example, in Japanese Patent Application Laid-Open No. 54-139160. The heat exchange device 1 includes a first fluidized bed heat exchanger 4 that uses high-temperature exhaust gas as a fluidizing gas, and a second fluidized bed heat exchanger 5 that uses a low-temperature heated gas as a fluidizing gas.
A heat medium is circulated between the fluidized bed heat exchangers 4 and 5 of these two towers to recover heat from the high temperature exhaust gas and heat the low temperature gas to be heated. The high-temperature exhaust gas contains dust discharged from a firing furnace such as a rotary kiln, for example, about 100%.
The exhaust gas is 0 ° C., and the low-temperature gas to be heated is air at normal temperature.

Each of the fluidized bed heat exchangers 4 and 5 is provided with a plurality of dispersion plates 6a to 6d; 6e to 6h, respectively. There is a gap between which the heat medium can pass, and
A plurality of partition walls 7 are provided for each of a to 6d; Each of the dispersion plates 6a to 6d;
At each end of 6e to 6h, the overflow pipe 9 is alternately changed in position.
a to 9d; 9e to 9h, and these overflow pipes 9a
9d; 9e to 9h, the respective dispersion plates 6a to 6d;
The heat medium on e to 6h can move from the upper stage to the lower stage.

An exhaust gas discharge port 10 and a heat medium supply port 11 are provided above the first fluidized bed heat exchanger 4, and an exhaust gas supply port 12 and a heat medium discharge port 13 are provided below it. A heated gas discharge port 14 and a heat medium supply port 15 are provided at an upper portion of the second fluidized bed heat exchanger 5, and a heated gas supply port 16 and a heat medium discharge port 17 are provided at a lower portion thereof. Can be The heat medium discharged from the heat medium outlet 13 of the first fluidized bed heat exchanger 4 is supplied by the first heat medium transport passage 18
It is supplied to the heat medium supply port 15 of the second fluidized bed heat exchanger 5,
The heat medium discharged from the heat medium outlet 17 of the second fluidized bed heat exchanger 5 is supplied to the heat medium supply port 11 of the first fluidized bed heat exchanger 4 by the second heat medium transport passage 19. The first and second heat medium transport paths 18 and 19 are realized by a bucket conveyor, an air transport pipe, or the like.

The heat medium supplied from the heat medium discharge port 17 of the second fluidized bed heat exchanger 5 to the heat medium supply port 11 of the first fluidized bed heat exchanger 4 by the second heat medium transport pipe 19 Fluidized by the high-temperature exhaust gas supplied from the port 12, and as indicated by arrows A1 to A9, the heat medium supply port 1
1. Dispersion plate 6a, overflow pipe 9a, dispersion plate 6b, overflow pipe 9
b, the heat is accumulated through the dispersion plate 6c, the overflow pipe 9c, the dispersion plate 6d, and the overflow pipe 9d, and guided to the heat medium outlet 13. Further, the exhaust gas from which the sensible heat has been recovered from the lowermost dispersion plate 6d through the uppermost dispersion plate 6a is discharged from the exhaust gas discharge port 10.

As described above, the high-temperature medium supplied from the heat medium discharge port 13 of the first fluidized bed heat exchanger 4 to the heat medium supply port 15 of the second fluidized bed heat exchanger 5 by the first heat medium transport path 18 Is fluidized by the low-temperature heated gas supplied from the heated gas supply port 16, and as shown by arrows B1 to B9, the heat medium supply port 15, the dispersion plate 6e, the overflow pipe 9e The sensible heat is recovered through the dispersion plate 6f, the overflow pipe 9f, the dispersion plate 6g, the overflow pipe 9g, the dispersion plate 6h, and the overflow pipe 9h, and is guided to the heat medium discharge port 17, and the second heat The medium is again supplied to the heat medium supply port 11 of the first fluidized bed heat exchanger 4 by the medium transport path 19.

In this way, the heat medium recovers sensible heat from the high temperature exhaust gas in the first fluidized bed heat exchanger 4 while repeating a series of circulation, and is guided to the second fluidized bed heat exchanger 5 to Is heated. In the second fluidized bed heat exchanger 5, the heated gas that has been heated by passing through the lowermost dispersion plate 6 h to the uppermost dispersion plate 6 e is discharged from the heated gas discharge port 14.

[0008]

In such prior art, there is no means for controlling the flow rate of the heat medium passing through the overflow pipes 9a to 9h. Each overflow pipe 9a ~
For example, the overflow pipe 9a provided at the uppermost stage of the first fluidized bed heat exchanger 4 among 9h will be described. As shown in an enlarged view in FIG. Is formed, and the overflow layer 9 is formed.
a of the heat medium from the upper opening 22 and the overflow pipe 9a
It is necessary to balance the outflow of the heat medium from the lower opening 23. However, in practice, the outflow is larger than the inflow because the inflow amount and the outflow amount vary in quantity and time. In some cases, the total weight of the heat medium forming the stagnation layer 21 in the overflow pipe 9a becomes smaller than the total weight of the heat medium forming the stagnation layer 21 having an appropriate height in a balanced state. As a result, the pressure loss in the overflow pipe 9a is reduced, and a so-called short path occurs in which the exhaust gas rises at high speed in the overflow pipe 9a.

When the gas is short-passed by the overflow pipe 9a as described above, the heat medium cannot flow into the overflow pipe 9a from the upper opening portion 22, and the dispersion plate 6 of the upper fluidized bed can be prevented.
a, the gas superficial velocity on the dispersion plate 6a decreases, the stability of the fluidized bed decreases, the temperature and the flow rate of the gas to be heated become unstable, and the fluidization stops. Problem arises. Further, since the exhaust gas supplied from the exhaust gas supply port 12 into the first fluidized bed heat exchanger 4 contains dust, the dust is transferred to the second fluidized bed heat exchanger by the first heat medium transport passage 18 together with the heat medium. Therefore, there is a problem that the dust is mixed into the high-temperature heated gas discharged from the heated gas discharge port 14 of the second fluidized bed heat exchanger 5.

[0010] Accordingly, an object of the present invention is to provide a heat exchange apparatus capable of recovering heat from an exhaust gas containing dust to obtain a clean, high-temperature gas free of dust and having a stable temperature and flow rate. It is to provide a driving method.

[0011]

According to the present invention, the heat medium on the dispersion plate is fluidized by the first gas,
A first fluidized bed heat exchanger for forming a multi-stage fluidized bed connected via a hermetic discharge means for the heat medium, and a hermetic discharge means for the heat medium by fluidizing the heat medium on the dispersion plate with the second gas And a second fluidized bed heat exchanger forming a plurality of fluidized beds connected via a fluidized bed heat exchanger, wherein the lowermost fluidized bed of the first fluidized bed heat exchanger and the uppermost fluidized bed of the second fluidized bed heat exchanger Of the second fluidized bed heat exchanger and the uppermost fluidized bed of the first fluidized bed heat exchanger are hermetically sealed with the heat medium. A circulation path of the heat medium is formed by being connected via the discharge means, and the flow rate of any one heat medium of the airtight discharge means is set to a predetermined value,
A pressure loss detecting means for detecting the pressure loss of the fluidized bed of the heat medium discharged by all the remaining airtight discharge means, respectively, and the detected pressure loss becomes a predetermined value in response to an output of the pressure loss detecting means. And a means for controlling the flow rate of the hermetic discharge means for discharging the heat medium from the fluidized bed having the detected pressure loss. According to the present invention, the first fluidized bed heat exchanger comprises a first fluidized bed heat exchanger.
The heat medium on the dispersion plate is fluidized by the gas to form a fluidized bed having a plurality of stages. can do. The second fluidized bed heat exchanger is
The heat medium on the dispersion plate is fluidized by the gas to form a plurality of fluidized beds, each fluidized bed is connected via an airtight discharge means, and the heat medium can move from the upper stage to the lower stage between the fluidized layers. it can. The lowermost fluidized bed of the first fluidized-bed heat exchanger and the uppermost fluidized bed of the second fluidized-bed heat exchanger are connected by an airtight discharge means, and the second fluidized-bed heat exchanger is connected to the lowermost fluidized bed. The lowermost fluidized bed and the uppermost fluidized bed of the first fluidized bed heat exchanger are connected by an airtight discharge means. First
The heat medium forming the lowermost fluidized bed in the fluidized bed heat exchanger is guided to the uppermost fluidized bed of the second fluidized bed heat exchanger via the airtight discharge means, and the second fluidized bed heat exchanger The heat medium forming the uppermost fluidized bed is guided to the lowermost fluidized bed via the airtight discharge means. Further, the heat medium forming the lowermost fluidized bed of the second fluidized-bed heat exchanger is guided to the uppermost fluidized bed of the first fluidized-bed heat exchanger via the hermetic discharge means, and the first fluidized-bed heat exchanger is heated. The heat medium forming the fluidized bed at the uppermost stage of the exchanger is guided to the lowermost fluidized bed via the hermetic discharge means, thus circulating the heat medium between the first and second fluidized bed heat exchangers. A path is formed. In any one of the plurality of hermetic discharge means, the flow rate of the heat medium is set to a predetermined value. Further, the pressure loss of the fluidized bed of the heat medium discharged by all the remaining airtight discharge means is detected by the pressure loss detection means. Here, the pressure loss of the fluidized bed may be either a pressure loss caused by the fluidized bed alone or a pressure loss caused by a dispersion plate in which the fluidized bed is formed. In all of the remaining airtight discharge means, the flow rate of the heat medium is controlled by the flow rate control means. Such control increases or decreases the flow rate of the heat medium discharged from each hermetic discharge means based on the output of the pressure loss detection means so that the detected pressure loss becomes a predetermined value. Thus, control is performed so that the pressure loss due to each fluidized bed is maintained at the predetermined value. The first gas is a high-temperature exhaust gas containing dust discharged from, for example, a firing furnace, and the second gas may be room-temperature air. Such a second gas is a gas to be heated and is a gas to be heated by recovering heat from the first gas. Therefore, in the first fluidized bed heat exchanger, the sensible heat is recovered from the first gas to the heat medium, and the heat medium moves from the uppermost fluidized bed to the lowermost fluidized bed and is transferred to the second fluidized bed heat exchanger. The heat medium of the uppermost fluidized bed is guided to the lowermost fluidized bed. In the second fluidized bed heat exchanger, the sensible heat of the heat medium is recovered by each fluidized bed by the second gas, and the second gas is heated. Since the hermetic discharge means is interposed between the first and second fluidized bed heat exchangers, the first gas containing dust from the first fluidized bed heat exchanger is guided to the second fluidized bed heat exchanger. Is prevented,
Dust does not mix with the second gas in the second fluidized bed heat exchanger. In this way, heat can be recovered from the exhaust gas containing dust to obtain a clean high-temperature gas. Moreover, the pressure loss of each fluidized bed is detected by the pressure loss detecting means, respectively, and the flow rate control means is configured to control the flow rate of each airtight discharge means based on the detected pressure loss. Can be kept constant, and the temperature and flow rate of the second gas heated by the heat medium recovered from the first gas can be stabilized.

According to a second aspect of the present invention, in addition to the configuration of the first aspect of the present invention, in the middle of the heat medium circulation path,
A heat medium supply source having a heat medium storage portion, an on-off valve for supplying / cutting off the heat medium from the storage portion, and a side provided in parallel with the heat medium supply source and another on-off valve interposed therebetween And the road is interposed. According to the present invention,
A heat medium supply source and a bypass are interposed in the middle of the heat medium circulation path. The heat medium supply source includes a storage unit that stores a fixed amount of the heat medium, and an on-off valve that supplies or shuts off the heat medium from the storage unit to the circulation path. Another opening / closing valve is interposed also in the bypass, and when supplying the heat medium from a state where no heat medium exists in the first and second fluidized bed heat exchangers, for example, at the start of operation. Opening the on-off valve of the heat medium supply source to supply the heat medium from the reservoir, and supply the heat medium until the pressure loss due to each fluidized bed of the first and second fluidized bed heat exchangers reaches a predetermined value. be able to. When the heat medium is replenished due to the consumption of the heat medium during operation, the on-off valve of the heat medium supply source is opened, and the heat medium can be gradually replenished from the storage unit. In this way, when the pressure loss of each fluidized bed reaches a predetermined value and continuous operation is performed, the heat medium is supplied into the circulation path from the side path, and the heat medium in the circulation path decreases during operation. In this case, the heat medium can be supplied without dissipating or leaking the first gas from the heat medium supply source, so that the heat medium can be efficiently supplied by selectively using the heat medium supply source and the bypass depending on the supply amount. Or replenish. Also, when the operation is stopped, close the on-off valve on the bypass,
By closing the on-off valve below the storage unit so as to store the heat medium in the storage unit, the heat medium in each fluidized bed can be discharged and stored in the storage unit.

According to a third aspect of the present invention, in addition to the configuration of the first or second aspect, one of the first and second gases is a dust-containing gas, and the first gas using this dust-containing gas is used.
Of the heat medium discharged from the lowermost fluidized bed of one of the fluidized bed heat exchangers to the first or second fluidized bed heat exchanger via an airtight discharge means A compressed gas supply means for discharging compressed gas so that the flow velocity in the flow path exceeds the superficial velocity ub of the lowermost fluidized bed near the upper end of the flow path. It is characterized by. According to the present invention, airtightness is performed from the lowest fluidized bed of one of the first and second fluidized bed heat exchangers using dust-containing gas to the other of the first and second fluidized bed heat exchangers. A compressed gas supply unit is provided near the upper end of the flow path of the heat medium discharged through the discharge unit.
The compressed gas supply means may be configured such that the flow velocity of the flow path exceeds a superficial velocity ub of the lowermost fluidized bed of one of the first and second fluidized bed heat exchangers from which the heat medium is discharged. The compressed gas is discharged so that dust is prevented from being transported together with the heat medium from the one fluidized bed heat exchanger to the other fluidized bed heat exchanger via the flow path. When a dust-containing gas is used as one of the first and second gases, for example, air is used as the other of the first and second gases. First, when a dust-containing gas is used as the first gas, the heat medium is fluidized by the dust-containing gas and heated by the dust-containing gas on the dispersion plate in the first fluidized bed heat exchanger. The heat medium thus heated is guided to the second fluidized bed heat exchanger via the airtight discharge means as described above. The second fluidized bed heat exchanger is supplied with air as a second gas, and the heat medium is fluidized by the air on the dispersion plate in the second fluidized bed heat exchanger, so that the sensible heat of the heat medium is reduced. Can be recovered by air. As described above, when the dust-containing gas is supplied to the first fluidized-bed heat exchanger as the first gas and the air is supplied to the second fluidized-bed heat exchanger as the second gas, the heat medium is the first and the second. By circulating between the two fluidized bed heat exchangers, sensible heat can be recovered from the dust-containing gas, and air as the second gas can be heated. Therefore, since the second gas does not directly contact the first gas and is heated by the heat medium, the second gas discharged from the second fluidized bed heat exchanger does not contain dust, and clean high-temperature gas is removed. Obtainable. Also, when using clean air as the first gas and using a dust-containing gas as the second gas, the heat medium is circulated between the first and second fluidized bed heat exchangers, and the second fluidized bed heat exchanger is used. The sensible heat is recovered from the dust-containing gas as the second gas, and the heated heat medium is guided to the first fluidized bed heat exchanger,
Heat is obtained by exchanging heat with the clean air that is a gas, so that a clean gas at a high temperature that does not contain dust can be obtained.

According to a fourth aspect of the present invention, in the configuration of the third aspect of the invention, the discharge speed of the compressed gas by the compressed gas supply means is such that the flow velocity of the heat medium in the flow path is the superficial velocity ub of the fluidized bed. Is selected to be 1.2 to 3.0 times. According to the present invention, the discharge speed of the compressed gas is selected to be 1.2 to 3.0 times the superficial velocity ub. If the discharge speed of such a compressed gas is 1.2 times or less of the superficial velocity ub, dust cannot be completely removed, and the temperature of the dust-containing gas in a clean gas heated through a heat medium is reduced. Dust gets mixed in. Also, the discharge speed of the compressed gas is 3.
If it is 0 times or more, the compressed gas is short-passed, and it is difficult to stably discharge the heat medium. for that reason,
The discharge speed of the compressed gas is selected to be 1.2 to 3.0 times the superficial velocity ub, so that dust can be reliably prevented from being mixed into clean air.

According to a fifth aspect of the present invention, in the first aspect, the first and second fluidized bed heat exchangers each have a plurality of fluidized beds, The layer is characterized in that the layer is formed to be smaller as the temperature of the first and second gases becomes lower due to heat exchange with the heating medium, so that the cross-sectional area is equal to or greater than the minimum fluidization rate umf. According to the present invention, each of the fluidized beds of the first and second fluidized bed heat exchangers has the first and second gases having a minimum fluidization rate um.
The first gas and the second gas are formed to be smaller as the temperature of the first gas and the second gas becomes lower. With such a configuration, the heat medium can be reliably fluidized on each of the dispersion plates of the first and second fluidized bed heat exchangers, and can sufficiently exchange heat with the first and second gases. The cross-sectional area of the lower temperature fluidized bed of the first and second gases is smaller than the cross-sectional area of the higher temperature fluidized bed of the first and second gases, which allows the apparatus to be downsized. In addition, the first and second
It is possible to form a stable fluidized bed without largely changing the gas supply amount according to the temperatures of the first and second gases, and to perform sufficient heat exchange.

According to a sixth aspect of the present invention, in the configuration of the fifth aspect, the temperature of the first gas is higher than the temperature of the second gas, and the first and second fluidized bed heat exchangers are provided. Has a plurality of stages of fluidized beds, wherein the cross-sectional area of the fluidized bed of the first fluidized bed heat exchanger is formed such that the upper stage is formed smaller than the lower stage, and the cross-sectional area of the fluidized bed of the second fluidized bed heat exchanger is , The lower stage is formed smaller than the upper stage. According to the present invention, since the cross-sectional area of the upper fluidized bed of the first fluidized-bed heat exchanger is selected to be smaller than the cross-sectional area of the lower fluidized bed, the gas temperature decreases due to heat exchange in the lower fluidized bed. Even in the upper fluidized bed, a stable fluidized bed can be formed at an appropriate superficial velocity. The first gas supplied to such a first fluidized bed heat exchanger is, for example, a high-temperature exhaust gas containing dust discharged from a firing furnace, and such a high-temperature first gas firstly flows through a lower fluidized bed. Forming and heating the heating medium,
The heat medium supplied to the lower fluidized bed exchanges heat in the upper fluidized bed with the first gas whose temperature has been reduced by the heat exchange in the lower fluidized bed. Therefore, the preheated heat medium that forms the upper fluidized bed is supplied to the lower fluidized bed, and the heat medium in the lower stage further rises in temperature due to heat exchange with the high-temperature first gas, and the high-temperature heat medium is removed. The second fluidized bed heat exchanger is guided to the upper fluidized bed. In this second fluidized bed heat exchanger, the cross-sectional area of the upper fluidized bed is larger than the cross-sectional area of the lower fluidized bed, and therefore, it is possible to select an appropriate superficial velocity corresponding to the temperature of the fluidized bed. A stable fluidized bed can be formed. The second gas supplied to the second fluidized-bed heat exchanger is, for example, normal-temperature air. The second gas having such a low temperature exchanges heat in the lower fluidized bed, and the preheated second gas is the second gas. 1 The fluidized bed heat exchanger exchanges heat with the high-temperature heat medium guided from the lower fluidized bed at the lower stage to raise the temperature. Therefore, it is possible to obtain a second gas that does not contain high-temperature dust that has been heat-exchanged in the upper fluidized bed.

According to a seventh aspect of the present invention, in addition to any one of the first to sixth aspects, the sensible heat of the first gas is reduced by the second gas.
A heat exchange device for recovering with a gas, a first gas temperature detecting means for detecting a temperature of the first gas after heat exchange from a first fluidized bed heat exchanger, and a response to an output of the first gas temperature detecting means. And another control means for increasing the flow rate of the heat medium by the one hermetic discharge means as the temperature of the first gas detected increases so as to become a preset temperature. Features. According to the present invention,
A first gas temperature detector for detecting a temperature of the first gas from the first fluidized bed heat exchanger; and a hermetic discharge means as the temperature of the first gas detected by the first gas temperature detector increases. And control means for largely controlling the flow rate of the heat medium by any one of the above. When the flow rate of the heat medium by one airtight discharge means is increased by such a control means, the pressure loss of the fluidized bed to which the heat medium discharged by this airtight discharge means is supplied increases. In response to the output of the pressure loss detecting means, the flow rate of the hermetic discharge means is controlled so as to increase to a predetermined pressure loss in response to the output of the pressure loss detecting means. When the pressure loss of each fluidized bed increases in this way, the flow rate of the airtight discharge means is sequentially set to be large, and the circulation amount of the heat medium increases. Therefore, when the temperature of the first gas introduced into the first fluidized-bed heat exchanger increases, the circulation amount of the heat medium is increased to increase the heat recovery of the first fluidized-bed heat exchanger to increase the first gas The temperature after the heat exchange can be controlled to a predetermined value. In this way, the heat medium of a constant temperature is guided to the upper fluidized bed of the second fluidized bed heat exchanger,
The first gas introduced into the first fluidized bed heat exchanger without greatly changing the temperature of the second gas from the second fluidized bed heat exchanger
It is possible to cope with a change in gas temperature.

According to an eighth aspect of the present invention, there is provided a heat exchange apparatus for recovering the sensible heat of the first gas by the second gas, in addition to the constitution of the first aspect. Second
A second gas temperature detecting means for detecting the temperature of the second gas after heat exchange from the fluidized bed heat exchanger; and detecting the temperature of the second gas in response to an output of the second gas temperature detecting means so as to reach a preset temperature. As the temperature of the second gas decreases, the flow rate of the heat medium by the one hermetic discharge means is controlled to be larger.
And two control means. According to the present invention, the temperature of the second gas from the second fluidized-bed heat exchanger is detected by the second gas temperature detecting means, and as the temperature of the second gas decreases, the control means performs the operation by one airtight discharge means. Control is performed to increase the flow rate of the heat medium. Accordingly, the amount of heat recovered in the first fluidized bed heat exchanger increases, and the sensible heat of the heat medium increases, so that the amount of heat recovered in the second fluidized bed heat exchanger also increases. The temperature of the second gas can be increased.

According to a ninth aspect of the present invention, in addition to the configuration of the eighth aspect, the present invention further includes a second gas flow rate detecting means for detecting a flow rate of the second gas, and the other control means comprises: In response to the output of the second gas temperature detecting means, as the flow rate detected by the second gas flow detecting means increases, the flow rate of the heat medium by the one hermetic discharge means increases to a preset temperature. It is characterized in that it is set large. According to the present invention, the flow rate of the second gas from the second fluidized bed heat exchanger is detected by the second gas flow rate detection means, and as the flow rate detected by the second gas flow rate detection means increases, one As the airtight discharge means, for example, the flow rate of the heat medium by the airtight discharge means for guiding the heat medium from the upper fluidized bed to the lower fluidized bed of the first fluidized bed heat exchanger, or from the upper fluidized bed of the second fluidized bed heat exchanger The flow rate of the heat medium by the airtight discharge means leading to the lower fluidized bed is set such that the temperature detected by the second gas temperature detection means becomes a predetermined value. In this way, the flow rate of the second gas discharged from the second fluidized bed heat exchanger is also monitored, and when the flow rate of the second gas increases, control is performed so that the temperature of the second gas does not decrease. be able to.

The present invention described in claim 10 provides the present invention according to claims 1 to 9
Any one of the first gas and the second gas is a dust-containing gas, and any one of the first and second fluidized beds in which the dust-containing gas is used. The uppermost fluidized bed of the heat exchanger is provided with dust collecting means for collecting and guiding dust from the one or the other gas from the uppermost stage of one of the other fluidized bed heat exchangers. I do. According to the present invention, one of the first and second gases is a dust-containing gas, and for convenience of explanation, the first gas is a dust-containing gas, and the second gas is a clean non-dust-containing gas such as air. Suppose that The first gas that is the dust-containing gas is supplied to the first fluidized bed heat exchanger, and the sensible heat is recovered by the heat medium. The high-temperature heat medium that has recovered the sensible heat is guided to the upper fluidized bed of the second fluidized-bed heat exchanger, and the heat medium is successively guided to the lower fluidized bed so that the dust-free second gas and heat are transferred. Exchange and the second gas is heated. The second gas discharged from the uppermost stage of the second fluidized bed heat exchanger is guided to, for example, a subsequent heat demanding facility after the dust contained in the second gas is collected by the dust collecting means. Such a second
The reason that the gas contains dust is that when the first gas passes through each fluidized bed in the first fluidized bed heat exchanger, dust in the first gas adheres to the heat medium of each fluidized bed, or the heat medium Is supplied to the first fluidized-bed heat exchanger together with the second fluidized-bed heat exchanger even if the amount is small compared to the dust contained in the first gas after heat recovery discharged from the first fluidized-bed heat exchanger. This is because dust enters the second gas discharged from the vessel, and the heat medium containing such dust is circulated between the first and second fluidized bed heat exchangers. Such a dust collecting means is not limited to the case where the first gas contains the dust and the second gas does not contain the dust, but the case where the second gas contains the dust and the first gas does not contain the dust. Similarly, the first gas containing no dust is provided to collect dust in the first gas after heat exchange discharged from the first fluidized bed heat exchanger in which the first medium and the heat medium come into contact with each other. In this manner, dust introduced by the heat medium used for heat exchange with the dust-containing gas can be removed, and a clean high-temperature gas can be obtained.

According to the eleventh aspect of the present invention, the heat medium on the dispersion plate is fluidized by the first gas to form a fluidized bed of a plurality of stages connected via the heat medium airtight discharge means.
A fluidized-bed heat exchanger, and a second fluidized-bed heat exchanger that fluidizes the heat medium on the distribution plate with the second gas to form a multi-stage fluidized bed that is connected through hermetic discharge means of the heat medium. Wherein the lowermost fluidized bed of the first fluidized bed heat exchanger and the uppermost fluidized bed of the second fluidized bed heat exchanger are connected by a hermetic discharge means for the heat medium, and the second fluidized bed heat exchanger The fluidized bed at the bottom of the vessel and the fluidized bed at the top of the first fluidized bed heat exchanger are connected via hermetic discharge means of the heat medium to form a circulation path for the heat medium, and the pressure of each fluidized bed is increased. Pressure loss detection means for detecting the loss, respectively, in response to the output of the pressure loss detection means,
Control means for controlling the flow rate of the airtight discharge means for discharging the heat medium from the fluidized bed in which the detected pressure loss occurs, so that the detected pressure loss becomes a predetermined value, In a state where the heat medium is not present on the dispersion plate by an amount that is less than a predetermined value of the loss or the heat medium is not present on the dispersion plate, the heat medium is supplied in the middle of the circulation path, and all the fluidized beds are discharged. When each pressure loss reaches the predetermined value, the supply of the heat medium is stopped, and then only one of all hermetic discharge means is controlled without detecting the pressure loss, and the flow rate is reduced. A method for operating a heat exchange device, wherein the method is set to a predetermined value and all remaining hermetic discharge means are controlled by detecting the pressure loss. According to the present invention, a state in which the heat medium is present on each of the first and second fluidized bed heat exchangers in an amount that causes less than a predetermined value of the pressure loss or the heat medium is not present on the first and second fluidized bed heat exchangers Then, the heat medium is supplied from the middle of the circulation path by the control means, and when the pressure loss of all the fluidized beds reaches a predetermined value, the supply of the heat medium is stopped, and
Only one hermetic discharge means is controlled until the flow rate reaches a predetermined value, and all remaining hermetic discharge means are controlled by the detected value of the pressure loss of each fluidized bed. By setting the flow rate of the one hermetic discharge means based on the temperature of the first or second gas after heat exchange discharged from the first or second fluidized bed heat exchanger, the first and second gases are It can be around the desired temperature. With the circulation amount of the heat medium set in advance in this way, the first and second gas discharged from the first and second fluidized bed heat exchangers based on the detected value of the pressure loss of each fluidized bed. Temperature control can be performed.
Therefore, at the start of operation, a heat medium is supplied onto each of the dispersion plates of the first and second fluidized bed heat exchangers to form a fluidized bed,
After all the fluidized beds have been formed, the pressure loss of each fluidized bed can be kept constant, and the temperatures of the first and second gases can be controlled by the flow rate of the heat medium, so that the operation can be performed smoothly and smoothly from the start of operation. The temperatures of the first and second gases are stabilized in a short time, heat is recovered from one of the first and second gases containing dust, and one of the first and second gases is heated to clean the other. Hot gas can be obtained.

[0022]

FIG. 1 is a system diagram showing a heat exchanger 41 according to an embodiment of the present invention. Heat exchange device 41
Is a first fluidized bed that fluidizes the heat medium on the dispersion plates 42a and 42b with the first gas to form a plurality of fluidized beds 44a and 44b connected via the first airtight discharge means 43 for the heat medium. The heat exchanger 45 and the heat medium on the dispersion plates 46a and 46b are fluidized by the second gas, and the plurality of fluidized beds 48a and 48a connected through the second airtight discharge means 47 for the heat medium.
The second fluidized bed heat exchanger 49 forming the second fluidized bed heat exchanger 49 is connected to the lowermost fluidized bed 44b of the first fluidized bed heat exchanger 45 and the uppermost fluidized bed 48a of the second fluidized bed heat exchanger 49. A third airtight discharge means 50 for guiding the heat medium from the lowermost fluidized bed 44b of the first fluidized bed heat exchanger 45 to the uppermost fluidized bed 48a of the second fluidized bed heat exchanger 49; Table 49
Of the lowermost fluidized bed 48b and the first fluidized bed heat exchanger 45
The fourth fluidized bed 44a of the first fluidized bed heat exchanger 45 is connected to the fourth fluidized bed 44a of the first fluidized bed heat exchanger 45. And a hermetic discharge means 51.

The heat exchange device 41 further comprises first to fourth
First to fourth pressure loss detections for detecting the pressure losses ΔP1, ΔP2, ΔP3, ΔP4 of the fluidized beds 44a, 48a, 44b, 48b of the heat medium discharged by the airtight discharge means 43, 47, 50, 51, respectively. Means 52-55, and responding to the outputs of the first to third pressure loss detecting means 52-54,
The detected pressure loss ΔP1 to ΔP3 is a predetermined value ΔP
Fluidized beds 44a, 48a, 44b having the detected pressure losses ΔP1 to ΔP3 so as to be 1a to ΔP3a.
First to third airtight discharge means 43 for discharging the heat medium from
First to third control means 56 to control the flow rates of 47 and 50
58, first to fourth airtight discharge means 43, 47, 50, 5
And a flow rate setting means 60 for setting the flow rate of the heat medium discharged by the fourth airtight discharge means 51, which is any one of the airtight discharge means, to a predetermined value.

The first fluidized-bed heat exchanger 45 closes a straight cylindrical portion 63, an inverted truncated cone portion 64 connected to a lower end portion of the cylindrical portion 63, and an upper end opening of the cylindrical portion 63. A furnace body 66 having an upper lid portion 65 and a truncated cone portion 64 are formed,
A gas supply unit 67 to which the first gas is supplied. The furnace body 66 and the gas supply unit 67 are made of castable refractories.

The space in the furnace 66 is formed by the two dispersion plates 4
The upper heat exchange chamber 68, the lower heat exchange chamber 69, and the wind box 70 are partitioned by 2a and 42b. The gas supply part 67 has a first gas of, for example, about 1000 ° C. from a firing furnace.
Exhaust gas containing dust, that is, dust-containing gas is supplied,
The first gas supplied to the gas supply unit 67 is guided to the wind box 70 in the truncated cone 64. Each of the dispersion plates 42a and 42b has
A plurality of through holes 71a and 71b are respectively formed, and the first gas led into the wind box 70 from the gas supply unit 67 passes through the through holes 71b of the lower dispersion plate 42b and the lower heat exchange chamber 69.
Into the upper heat exchange chamber 68 through the through holes 71a of the upper dispersion plate 42a. In this manner, the heat medium is fluidized by the high-temperature first gas ejected through the through holes 71a, 71b of each of the dispersion plates 42a, 42b, so that the fluidized beds 44a, 44b can be respectively formed. The heat medium preferably does not deteriorate or wear due to heat. For example, silica sand, limestone, iron powder or the like having a particle size of 1 to 5 mm is used.

The second fluidized bed heat exchanger 49 closes a straight cylindrical portion 73, an inverted truncated cone portion 74 connected to a lower end portion of the cylindrical portion 73, and an upper end opening of the cylindrical portion 73. A furnace body 76 having an upper lid portion 75, and a truncated cone portion 74,
For example, it has a gas supply unit 77 to which a second gas that is air at room temperature is supplied.

The space inside the furnace body 76 accommodates the two dispersion plates 4
The upper heat exchange chamber 78, the lower heat exchange chamber 79, and the wind box 80 are partitioned by 6a and 46b. The gas supply unit 7
7, the second gas is guided into the wind box 80 of the truncated cone portion 74, passes through the through hole 81b of the lower dispersion plate 46b, and is ejected into the lower heat exchange chamber 79. Then, the heat is blown out into the upper heat exchange chamber 78 through the through holes 81a of the upper dispersion plate 46a, and the heat medium on each of the dispersion plates 46a and 46b is fluidized to form the fluidized beds 48a and 48b, respectively. .

The heat medium forming the upper fluidized bed 44a of the first fluidized bed heat exchanger 45 is guided to the lower fluidized bed 44b via the chute 106, the first airtight discharge means 43 and the chute 107. In the second fluidized bed heat exchanger 49, the upper dispersion plate 4 forming the upper fluidized bed 48a
The heat medium on the lower dispersion plate 4a passes through the chute 109, the second hermetic discharge means 47 and the chute 110.
6b.

The lower dispersion plate 4 of the first fluidized bed heat exchanger 45
The heat medium that forms the fluidized bed 44b on 2b
3. The third hermetic discharge means 50 and the chute 84 feed the fluidized bed 48a formed on the upper dispersion plate 46a of the second fluidized bed heat exchanger 49 from above the interface. Dispersion plate 4 in lower stage of second fluidized bed heat exchanger 49
The heat medium that forms the fluidized bed 48b on the
5. The fluidized bed 44a in the upper stage of the first fluidized bed heat exchanger 45 is located above the interface through the fourth hermetic discharge means 51, the chute 86, the transport means 87, the heat medium supply source 90, and the chute 88. It is thrown in from. A heat medium supply source 90 that supplies a heat medium via a heat medium input chute 89 is provided at the upper end of the transport means 87, and the heat medium can be supplied to the chute 88.

FIG. 2 is a front view showing a specific configuration of the heat medium supply source 90. The heat medium supply source 90 is provided with a supply pipe 92 having a heat medium supply port 91 into which a heat medium is supplied from the transport means 87 and a heat medium supplied through the supply pipe 92. A transfer unit 93 which is realized by, for example, a screw conveyor for transferring from one end to the other end, and a storage unit for storing a fixed amount of the heat medium supplied from the supply pipe 92 to one end of the transfer unit 93. A certain storage hopper 94, a bypass chute 95 for guiding the heat medium from the other end of the transfer means 93 to the heat medium input chute 89, and a heat medium input chute 89 interposed between the heat transfer medium and the heat medium input chute 89, A first opening / closing valve which is opened to allow the passage of the heat medium through the heat medium input chute 89 when a small amount of the heat medium is supplied, and shuts off the heat medium input chute 89 when the heat medium is not supplied. When a continuous operation is performed by forming a circulation path of the heat medium between the first and second fluidized bed heat exchangers 45 and 49 interposed between the valve closing valve 96 and the bypass chute 95, the transfer means 93 continuously operates. In order to supply the heat medium to the first fluidized bed heat exchanger 45, a second on-off valve 97 that allows or shuts off the passage of the heat medium through the bypass chute 95, the one end of the transfer means 93,
Interposed in a chute 99 connecting the storage hopper 94,
When the heat medium is supplied by the transfer means 93 and the bypass chute 95, the chute 99 is shut off to cut off the passage of the heat medium to the storage hopper 94, and when the operation is stopped, the heat medium in the heat exchanger is stored. Has a third on-off valve 98 that opens the chute 99 and guides the heat medium from the supply pipe 92 to the storage hopper 94 via the chute 99.

The storage hopper 94 is connected to a cylindrical portion 101 having a straight cylindrical shape, a lower end portion of the cylindrical portion 101, an inverted truncated conical portion 102, and an upper end portion of the cylindrical portion 101. And a heat medium stored in the storage hopper 94. The heat medium stored in the storage hopper 94 is opened by the first opening / closing valve 96 by a desired amount. It is configured such that it can be supplied to the vessel 45 or can be gradually replenished when the heat medium is consumed.

The operation of the heat medium supply source 90 is summarized in Table 1 below.

[0033]

[Table 1]

In another embodiment of the present invention, the transfer means 93 uses a hollow chute inclined so that the other end is lower than the one end where the storage hopper 94 is provided, instead of the screw conveyor. You may do so.

FIG. 3 is an enlarged sectional view showing the vicinity of the lower dispersion plate 42b of the first fluidized bed heat exchanger 45. As described above, the dispersion plate 4 having the plurality of through-holes 71b is provided on the cylindrical portion 63 that constitutes a part of the furnace body 66 of the first fluidized-bed heat exchanger 45.
2b are provided. Each through hole 7 of such a dispersion plate 42b
1b passing from bottom to top and ejecting,
A fluidized bed 44b having a predetermined height is formed on the dispersion plate 42b.

As shown in FIG. 1, a heating medium inlet 112a is formed in the furnace wall of the cylindrical portion 63, and opens toward the free boat portion above the interface 111 of the upper fluidized bed 44a. The chute 88 is connected to the heat medium inlet 112a, and the heat medium transported upward from below by the transport means 87 is again transferred from the heat medium inlet 112a to the upper fluidized bed 44a via the chute 88. At the start of the operation or at the start of the operation, a heat medium is supplied from the heat medium supply chute 89 of the heat medium supply source 90 via the chute 88. Thus, the heat medium inlet 112a
Is provided above the interface 111 of the fluidized bed 44a.
Because the heat medium can be smoothly injected into the fluidized bed 44a,
In addition, this is because the adhesion blockage of the heat medium inlet 112a can be prevented.

As shown in FIG. 3, the furnace wall of the cylindrical portion 63 is provided with a heat medium discharge port 113 which opens below the interface 111 of the lower fluidized bed 44b and faces the fluidized bed 44b. The heating medium outlet 113 is provided with the chute 8.
3 and the third airtight discharge means 50 and the chute 8
The heat medium forming the fluidized bed 44b is airtightly sealed through the second
The fluidized bed heat exchanger 49 can be guided on the upper fluidized bed 48a. From the first fluidized bed heat exchanger 45, the second
When transferring the heat medium to the fluidized bed heat exchanger 49, the first
Since the first gas containing dust is supplied to the fluidized bed heat exchanger 45, the dust may be led to the second fluidized bed heat exchanger 49 together with the heat medium. Therefore, a clean gas containing no dust is supplied from the compressed gas supply unit 114 to the chute 83. This compressed gas is, for example, clean air, and the superficial velocity u in the chute 83 is
₀ is selected to be about 1.2 to 3 times the superficial velocity ub on the dispersion plate 42b. This prevents dust from flowing into the chute 83 and allows only the heat medium to pass through. The compressed gas from the compressed gas supply unit 114 is supplied to a compressed gas supply unit 115 formed on the chute 83.
Is injected into the chute 83 from the supply port 116, and the compressed gas is discharged toward the fluidized bed 44b on the dispersion plate 42b. Thus, the chute 83 is supplied from the supply port 116 of the compressed gas supply unit 115 by the compressed gas supply unit 114.
The compressed gas supplied to the fluidized bed 44b is guided to the fluidized bed 44b by a third airtight discharge means 50 interposed between the chute 83 and another chute 84, whereby the gas from the chute 83 to the chute 84 is This is because the passage is blocked.

FIG. 4 is an enlarged sectional view showing a specific structure of the first hermetic discharge means 43. The first airtight discharge means 43
The chute 10 guides the heat medium forming the upper fluidized bed 44a of the first fluidized bed heat exchanger 45 to the lower fluidized bed 44b.
6 and 107, a rotary valve 123 provided with a rotor 122 rotatably driven in the direction of arrow A within the casing 121, and rotatably driving the rotor 122 in the direction of arrow A at a predetermined rotation speed. This is realized by a rotary feeder having a motor 124.

The casing 121 includes an upper fluidized bed 44a.
An inflow portion 127 having a flange 126 flanged to the flange 125 of the side chute 106 with a bolt, a nut, or the like, and the rotor 122 connected to the inflow portion 127 so as to be rotatable in the arrow A direction. A rotor housing portion 129 having a right cylindrical rotor housing space 128 coaxial with the horizontal rotation axis, and a heat medium guided by the rotor 122 and connected to the rotor housing portion 129, the lower chute 107 on the side of the fluidized bed 44b on the lower side. An outflow portion 132 having a flange 131 which is flanged by a bolt and a nut of the flange 130 is provided.

The rotor 122 has a rotating shaft 133 which is driven to rotate in the direction of arrow A by the motor 124, and a plurality of blades 134 radially provided on the rotating shaft 133 at equal intervals in the circumferential direction. Each of the blades 134 of the rotor 122 has such a small spacing that the outermost end face 135 farthest from the rotation axis can rotate without biting the heat medium with the inner peripheral face 136 of the rotor housing 129. This allows only the heat medium to be guided from the chute 106 on the upper fluidized bed 44a side to the chute 107 on the lower fluidized bed 44b side, thereby blocking the passage of gas.

The rotor 122 includes an upper fluidized bed 44a.
Of the heat medium and gas introduced into the inflow portion 127 from the chute 106 on the side, only the raw material is stored in the storage space 137 between the adjacent blades 134 in the circumferential direction.
The rotation of 22 causes the storage space 137 to move outflow section 132
When facing the internal space, the heat medium in the storage space 137 falls into the outflow portion 132, and thus only the heat medium can be discharged to the downstream side without passing gas. Rotor 12
2, the inner peripheral surface 136 of the rotor housing portion 129 is rotated.
In order to prevent the heat medium from being caught between the blades 134 and the blades 134, the downstream wall 138 in the arrow A direction, which is the downstream side in the rotation direction of the rotor 122 of the inflow portion 127, Are integrally formed with a biting prevention piece 139 projecting in the opposite direction. Such a biting prevention piece 139 is provided as a so-called baffle plate, and can prevent biting of a heat medium having a large particle diameter.

The second to fourth airtight discharge means 47, 50,
51 also has the same configuration as the above-mentioned first hermetic discharge means 43, and description thereof will be omitted to avoid duplication.

FIG. 5 is an enlarged sectional view showing a first hermetic discharge means 43a according to another embodiment of the present invention. The first hermetic discharge means 43a of the present embodiment includes a first fluidized bed heat exchanger 4
5, an L valve 141 that blocks the passage of gas by a material seal using a heat medium supplied from the upper fluidized bed 44a via the chute 106 and guides only the heat medium to the chute 107 on the lower fluidized bed 44b side; Valve 14
And pushing means 142 for pushing the heat medium deposited in the heating medium. The L valve 141 is a substantially L-shaped bent cylindrical body, and includes a rising portion 143 that rises upward, and a horizontal portion 144 that is bent and connected to the lower end portion of the rising portion 143 at a substantially right angle and extends horizontally. The rising portion 14 of the horizontal portion 144
3 has a falling part 145 which is bent substantially at a right angle and extends downward from the other end opposite to the one end in the longitudinal direction in which the three parts 3 are continuous. A flange 146 is formed at an upper end of the rising portion 143, and the flange 146 is flange-joined to a flange 125 formed at a lower end of the chute 106 by bolts and nuts. A flange 147 is formed at the lower end of the falling part 145, and the flange 147 is formed.
7 is a flange 13 formed at the upper end of the chute 107
1 and is flanged by bolts and nuts. Such an L valve 141 has a fireproof structure, for example, and is airtightly connected between the chutes 106 and 107.

From the upper chute 106 to the L valve 141
Heat medium supplied into the rising portion 143 of the horizontal portion 14
4, a repose surface 149 having a repose angle φ _r is formed and deposited upward from a corner 148 facing the space in the falling portion 145. Thus, the horizontal portion 1 in the L valve 141
The material is sealed by the heat medium deposited from the top 44 to the rising portion 143, and the passage of gas from the upper chute 106 to the lower chute 107 is prevented.

In order to discharge only the heat medium in such a state, a nozzle member 150 for injecting gas toward the repose surface 149 of the heat medium is provided on the inner wall surface 143a of the rising portion 143.
Are provided substantially parallel to the horizontal portion 144. The gas supplied to the nozzle member 150 is, for example, the nozzle member 15
This is air at room temperature from a blower 151 provided independently for zero, and the flow control valve 200 interposed between the nozzle member 150 and the blower 151 is opened and closed to easily adjust the gas ejection amount. It is configured to be able to.
Further, as shown by a virtual line 205, a configuration may be adopted in which compressed air is intermittently injected by opening and closing the electromagnetic valve 206 instead of the blower 151. The extruding means 142 includes the nozzle member 150 and the blower 151. As described later, the setting of the injection amount of the gas injected from the nozzle member 150 is performed in the upper fluidized bed 4.
It is determined based on the pressure loss according to 4a. The second of the remainder
The fourth to fourth hermetic discharge means 47, 50, 51 may also be configured in the same manner as the first hermetic discharge means 43a.

FIG. 6 is an enlarged sectional view showing a first hermetic discharge means 43b according to still another embodiment of the present invention. The first airtight discharge means 43b of the present embodiment is provided with a pressing rod 152 instead of the nozzle member 150 described above. The pressing rod 152 is made of a heat resistant metal or a molded refractory in the shape of a right column, and is driven by a driving cylinder 153 in an axial direction parallel to the horizontal portion 144. Means 154 are constituted. The drive cylinder 153 is a double acting high pressure cylinder for example, a heat medium deposited to form a resting surface 149 forming a repose angle phi _r in the L valve 141, the push rod 15
2 is the stroke S from the inner wall surface 143a of the rising portion 143.
By protruding by R, the heating medium in the horizontal portion 144 is pressed, whereby the resting surface 149 is broken, and the heating medium is pushed to the falling portion 145 side beyond the corner portion 148,
It falls into the lower chute 107. The stroke SR and the operation cycle of the drive cylinder 153 are determined based on the pressure loss caused by the upper fluidized bed 44a, similarly to the pushing means 142 shown in FIG. When the pushing means 154 using such a pressing rod 152 is adopted, the pushing means 154 is moved by the pushing rod 152 compared to when the pushing means 142 using the nozzle member 150 shown in FIG. Since it is only necessary to extrude the heat medium deposited in the valve 141, the lower fluidized bed 4
There is no problem that the temperature of the heat medium guided to 4b decreases. However, there is a problem that an air pressure source for supplying an operating pressure to the drive cylinder 153 is separately required, and the configuration becomes large. The remaining second to fourth hermetic discharge means 47, 50, 51 may also be configured similarly to the first hermetic discharge means 43b.

FIG. 7 shows first to fourth airtight discharge means 43 and 4.
Control device 161 for controlling operations of 7, 50 and 51
FIG. 2 is a block diagram showing an electrical configuration of the embodiment. Control device 161
Are the pressure loss set values ΔP1a, ΔP2a, ΔP3a,
Setting means 1 for setting ΔP4a and temperature set value T1a
62 and first to fourth pressure loss detecting means 52 for detecting pressure loss due to each of the fluidized beds 44a, 48a, 44b, 48b.
55, a temperature detector 163 for detecting the temperature T1 of the gas discharged from the second fluidized-bed heat exchanger 45, and a control means 16 realized by a central processing unit (CPU).
4 and the first signal in response to the control signal from the control means 164.
To the fourth airtight discharge means 43, 47, 50, and 51, respectively.

Since the set values of the compression and the flow rate can be inputted by the same key input means, the flow rate setting means 60 may be included in the setting means 162 or may be individual.

The control means 164 has the pressure loss set values ΔP1a to ΔP4a set by the setting means 162.
And the pressure loss detection values ΔP1 to ΔP4 from the first to fourth pressure loss detection means 52 to 55, and the pressure loss detection values ΔP1 to ΔP4 are compared with the pressure loss set values ΔP1a to ΔP4a.
If it is less than, a control signal is output so as to decelerate or stop the corresponding driving means 168 to 171, and each of the pressure loss detection values ΔP1 to ΔP4 becomes a corresponding one of the pressure loss set values ΔP1a to ΔP4.
If a is exceeded, a control signal is output to increase or activate each of the driving means 168 to 171. The setting means 16
For example, when the temperature set value T1a is set in place of the pressure loss set value ΔP4a by the control unit 164, the control means 164 sets the temperature set value T1a and the temperature T1 detected by the temperature detector 163.
If the detected temperature value T1 is less than the set temperature value T1a, a deceleration signal or a stop signal is output to the driving means 171. If the detected temperature value T1 exceeds the set temperature value T1a, an acceleration signal or a speed-up signal is output. The driving signal is output to the driving unit 171. The driving unit 171 is connected to the control unit 16 as described above.
4 compares the temperature detection value T1 from the temperature detector 163 with the temperature set value T1a by the setting means 162, and responds to the output speed increase signal, drive start signal, deceleration signal, and stop signal, respectively. Motor 1 of airtight discharge means 51
The rotation speed of 67 is controlled. Such a temperature detector 16
Which one of the temperature detection value T1 and the first to fourth pressure loss detection means 52 to 55 is to be adopted may be switched by the setting means 162, and the temperature detector 163 and the first to fourth pressure loss detection means 52 to 55 may be switched. Fourth pressure loss detecting means 5
A comparison judgment is made by adopting all the detection values of 2 to 55,
The operation buttons of the fourth hermetic discharge means 43, 47, 50, and 51 are programmed, and control signals from the control means 164 are transmitted according to the program.
To the first to fourth airtight discharge means 43, 4
7, 50 and 51 may be controlled.

FIG. 8 is a flowchart for explaining the operation of the heat exchange device 41. The operation is started in step a1, and the heat medium is supplied to the chute 88 by the heat medium supply source 90 in step a2. When the heat medium is charged, as described with reference to FIG. 2 described above, the third opening / closing valve 98 provided above the storage hopper 94 is closed and the first opening / closing valve 98 is interposed in the heat medium charging chute 89. On-off valve 9
6 is opened to supply the heat medium from the storage hopper. When the second on-off valve 97 is open, the fluidized beds 44a, 44b, 48
When a predetermined amount of the heat medium stays in the order a and b and the fourth airtight discharge means 51 starts discharging, the first on-off valve 96 is closed to stop the supply of the heat medium, and the fourth airtight discharge means 5 is closed.
The heat medium discharged from the first fluidized bed heat exchanger 45 is transferred from a chute 88 via a transfer means 93, a bypass chute 95 and a heat medium input chute 89 via a transport means 87.
Continuously on the upper dispersion plate 42a. At this time, the first to fourth pressure loss detection means 52 to 55 have started the detection operation, and the first to fourth airtight discharge means 43, 47, 5 have been started.
0,51 have also begun the ejection operation.

In this state, the heat medium supply source 90
Continues the supply operation of the heat medium, and in step a3, the control means 164 determines each pressure loss detection value ΔP1 based on the pressure loss detection values ΔP1 to ΔP4 from the first to fourth pressure loss detection means 52 to 55. To ΔP4 become the pressure loss set values ΔP1a to ΔP4a respectively set by the setting means 162, so that the first to fourth airtight discharge means 43, 47, 50,.
The amount of supply of the heat medium by 51 is controlled.

The start-up of the heat exchange device 41 at the start of the operation as described above is performed before the heat medium supply source 90 supplies the heat medium to the first fluidized bed heat exchanger 45 from the gas supply unit 67. High temperature exhaust gas including dust is supplied,
In addition, room temperature air is supplied to the second fluidized bed heat exchanger 49 as a gas to be heated at a constant flow rate from the gas supply unit 77 by a blower.

The heat medium supply source 9 is
The heat medium supplied from the first fluidized bed heat exchanger 45 includes an upper fluidized bed 44a, a lower fluidized bed 44b, a second fluidized bed heat exchanger 49, an upper fluidized bed 48a, and a lower fluidized bed 48b. Are circulated in this order, and the second fluidized-bed heat exchanger 49
The temperature of the gas to be treated discharged from is gradually increased. In this way, the pressure loss detection values ΔP1 to ΔP4 obtained by the pressure loss detection means 52 to 55 become the pressure set values ΔP1a to ΔP
4a, the first to fourth airtight discharge means 43, 4
7, 50 and 51 control the discharge amount.

In step a4, the pressure loss detection values ΔP1 to ΔP4 obtained by the first to fourth pressure loss detection means 52 to 55
Is determined to have reached the pressure loss set values ΔP1a to ΔP4a. These pressure loss set values ΔP1a to ΔP1
4a is set to, for example, 300 mmAq, and if it has reached, it proceeds to the next step a5, and if not, it returns to step a3. At step a5, the flow rate setting means 60 sets the flow rate of the fourth hermetic discharge means 51. The first and third hermetic discharge means 4 other than the fourth hermetic discharge means 51 discharge air at such a set flow rate.
Any one of 3, 47, and 50 may be selected to perform the discharge operation at a set flow rate instead of the fourth airtight discharge means 51.

After the normal operation is continued in this manner, when the operation is completed in step a6, the discharging operation by the first to fourth hermetic discharging means 43, 47, 50, 51 by the control means 164 is released, and The operation of detecting the pressure loss by the first to fourth pressure loss detecting means 52 to 55 is released, and all the operations are completed.

In step a5, the flow rate of the fourth hermetic discharge means 51 is set by the flow rate setting means 60. However, as another embodiment of the present invention, the discharge rate of the first fluidized bed heat exchanger 45 is reduced. Temperature detector 1 in pipe
63, and a temperature T detected by the temperature detector 163.
1 is higher, the fourth hermetic discharge means 51
By increasing the flow rate Q4 of the heat medium supplied from the lower fluidized bed 48b of the fluidized bed heat exchanger 49 to the upper fluidized bed 44a of the first fluidized bed heat exchanger 45, the detected temperature T1 is set to the set value T1a. May be controlled so that Note that FIG.
The relationship between the temperature T1 of the discharge pipe of the first fluidized bed heat exchanger 45 and the flow rate Q4 of the heat medium discharged by the fourth hermetic discharge means 51 is shown.

As another embodiment of the present invention, the second embodiment
The temperature detector 20 is provided in the exhaust pipe of the fluidized bed heat exchanger 49 to detect the temperature T2 of the gas discharged from the second fluidized bed heat exchanger 49, and as the temperature T2 increases, the second temperature T2 increases.
The detected temperature T2 may be controlled to be the set value T2a by decreasing the flow rate Q3 of the heat medium guided from the upper fluidized bed 48a to the lower fluidized bed 48b of the fluidized bed heat exchanger 49. FIG. 10 shows the second fluidized bed heat exchanger 49.
The relationship between the temperature T2 of the discharge pipe and the flow rate Q3 of the heat medium discharged by the second hermetic discharge means 47 is shown.

FIG. 11 is a system diagram showing a heat exchanger 41a according to still another embodiment of the present invention. In the above embodiment, the first to fourth pressure loss detecting means 52 to 55 are:
The space of the free boat portion above each interface between the fluidized beds 44a, 44b, 48a, 48b and the dispersion plates 42a, 4
Each of the fluidized beds 44a, 44b, 48a, 48b is based on a pressure difference between the space 2b, 46a, 46b and the space below.
And the pressure loss due to each of the dispersion plates 42a, 42b, 46a, 46b is detected as a pressure loss due to the fluidized bed. However, as still another embodiment of the present invention,
The pressure difference between the portion near the upper surface of each of the dispersion plates 42a, 42b, 46a, 46b and the space above the interface between the fluidized beds 44a, 44b, 48a, 48b is measured, and the fluidized bed 44 is measured.
a, 44b, 48a, and 48b may be configured to detect pressure loss. In this way, the first to fourth hermetic discharge means 43 and 4 are based on the pressure loss caused by the fluidized bed alone.
Since the flow rate is controlled by 7, 50, and 51, the influence of clogging of the through holes 71a, 71b, 81a, and 81b formed in each of the dispersion plates 42a, 42b, 46a, and 46b is not included, and the fluidized bed is accurately formed. Of the fluidized beds 44a, 44b, 48a, and 48b, thereby controlling the AC contact time between the gas and the heat medium, thereby controlling the temperature to a predetermined temperature. .

FIG. 12 is a system diagram showing a heat exchanger 41b according to still another embodiment of the present invention. The transport means 87 in each of the above embodiments is realized by a bucket conveyor, but in still another embodiment of the present invention, the air transport pipe 175 and the air transport pipe 175
A blower 176 for supplying air from the lower end of the second fluidized bed; an ejector 177 interposed in the air transport pipe 175 for sucking the heat medium from the lower fluidized bed 48b of the second fluidized bed heat exchanger 49 by negative pressure; A transport means 180 is provided which is constituted by a collecting cyclone 178 to which the upper end of the collecting cyclone 175 is connected, and an airtight discharging means 179 interposed in a chute 88 into which the heat medium collected by the collecting cyclone 178 is guided. . The hermetic discharge means 179 may perform a discharge operation at a predetermined constant flow rate, or may perform a discharge operation at a flow rate equal to the discharge amount of the fourth hermetic discharge means 51.

According to the transport means 180, a negative pressure is generated in the ejector 177 by the pressurized air supplied from the blower 176 into the air transport pipe 175, and the negative pressure causes the second fluidized bed heat exchange. Fluidized bed 48 in the lower part of the vessel 49
The heat medium discharged from b into the chute 86 by the chute 85 and the fourth airtight discharge means 51 is guided to the collection cyclone 178 in a short time, and the air supplied into the air transport pipe 175 by the blower 176 is exhausted to the outside. Only the heat medium collected by the collection cyclone 178 is transferred from the chute 88 to the upper dispersion plate 42 of the first fluidized bed heat exchanger 45.
a. Since the heat medium is transported in the air transport pipe 175 in a short time in this manner, the amount of heat radiation can be reduced, and the heat recovery efficiency can be improved.

FIG. 13 is a system diagram showing a heat exchanger 41c according to still another embodiment of the present invention. Note that the same reference numerals are given to portions corresponding to the above-described embodiment. In the present embodiment, an exhaust pipe 183 for guiding exhaust gas is provided above the second fluidized bed heat exchanger 49, and a collecting cyclone 184 is connected to the upper end of the exhaust pipe 183. The collected heat medium is a chute 1
It is supplied by 85 to the transport means 87 described above. Therefore, the chute 185 is provided with an airtight discharge means 186. With such a configuration, the second fluidized bed heat exchanger 49
The fine and granular heat medium contained in the gas discharged from the gas is collected by the collection cyclone 184, supplied to the transport means 87 again, and returned to the first fluidized bed heat exchanger 49. As a result, the consumption of the heating medium can be reduced, and the leakage of the heating medium to the succeeding heated gas consuming equipment can be eliminated or reduced. Further, instead of the transporting means 87, a transporting means 180 shown in FIG. 12 may be used, whereby the heat recovery efficiency can be improved.

FIG. 14 is a system diagram showing a heat exchanger 41d according to still another embodiment of the present invention. Note that the same reference numerals are given to portions corresponding to the above-described embodiment. The heat exchange device 41d of the present embodiment is different from the first fluidized bed heat exchanger 45d in that the cylindrical portion 63 forming the upper fluidized bed 44a
The hollow tower cross-sectional area of a is formed smaller than the hollow tower cross-sectional area of the cylindrical section 63b forming the lower fluidized bed 44b, and in the second fluidized bed heat exchanger 49d, the cylindrical section forming the lower fluidized bed 48b is formed. The hollow tower cross-sectional area of 73b is formed smaller than the hollow tower cross-sectional area of the cylindrical portion 73a forming the upper fluidized bed 48a. Thus, in the first fluidized bed heat exchanger 45d,
Since the upper fluidized bed 44a is configured to have a smaller sectional area than the lower fluidized bed 44b, each fluidized bed 44a,
An appropriate superficial velocity corresponding to the temperature of 44b can be selected, a stable fluidized bed is formed, the flow rate of the heat medium is stabilized, and the temperatures of the first and second fluidized bed heat exchangers 45d, 49d are stabilized. Can be done. In the second fluidized bed heat exchanger 49d, the upper fluidized bed 48a has a larger cross-sectional area than the lower fluidized bed 48b, so that the appropriate superficial velocity corresponding to the temperature of each fluidized bed 48a, 48b is obtained. The first and second fluidized bed heat exchangers 45d, 49 form a stable fluidized bed and stabilize the flow rate of the heat medium.
The temperature of d can be stabilized. With the above configuration, a stable and high heat recovery efficiency can be achieved.

FIG. 15 is a graph showing the relationship between the number of stages of the fluidized bed and the outlet gas temperature in an experiment conducted by the present inventor. The horizontal axis indicates the number of stages of the fluidized bed, and the vertical axis indicates the outlet gas temperature of each heat exchanger. The first fluid supplied to the first fluidized bed heat exchanger 45
The gas was 5000 Nm ³ / hour x 1000 which burned heavy oil.
Exhaust gas containing dust at a temperature of 2 ° C.
The second gas supplied to No. 9 is 5000 Nm ³ / hour × 20
° C air, and the heat medium used was silica sand. The first and second fluidized bed heat exchangers have the same structure, and while increasing the number of fluidized beds, the flow rate of the heat medium is changed by 6000 kg / h for the solid line, 7500 kg / h for the dashed line, and 9000 kg / h for the broken line. The temperature T _GO of the first gas discharged from the first fluidized bed heat exchanger and the temperature T _AO of the second gas discharged from the second fluidized bed heat exchanger 49 were measured for each number of stages of the fluidized bed. As is clear from the figure, as the number of stages of the fluidized bed increases and the flow rate of the heat medium increases, the temperature of the second gas to be heated increases, and the temperature of the first gas decreases. Was confirmed. As described above, by changing the number of stages of the fluidized bed from one to four, the temperature T _AO of the second gas can be increased by about 300 ° and the temperature T _GO of the first gas can be reduced by about 300 °. When the flow rate of the heat medium was increased, the temperature T _GO of the first gas was decreased, but the temperature T _AO of the second gas was increased, and it was confirmed that the heat recovery efficiency was improved.

As another embodiment of the present invention, in the above-described embodiment, each of the furnace bodies 66 and 76 and the storage hopper 94 may be square.

[0065]

According to the first aspect of the present invention, in the first fluidized bed heat exchanger, sensible heat is recovered from the first gas to the heat medium, and the heat medium is transferred from the uppermost fluidized bed to the heat medium. It moves to the lower fluidized bed and is guided to the uppermost fluidized bed of the second fluidized bed heat exchanger, and the heat medium of this uppermost fluidized bed is guided to the lowermost fluidized bed. In the second fluidized bed heat exchanger, the sensible heat of the heat medium is recovered by the second gas by each fluidized bed,
The second gas is heated. Since the hermetic discharge means is interposed between the first and second fluidized bed heat exchangers, the first gas containing dust from the first fluidized bed heat exchanger is guided to the second fluidized bed heat exchanger. This prevents dust from entering the second gas in the second fluidized bed heat exchanger. In this way, heat can be recovered from the exhaust gas containing dust to obtain a clean high-temperature gas. Moreover, the pressure loss of each fluidized bed is detected by the pressure loss detecting means, respectively, and the flow rate control means is configured to control the flow rate of each airtight discharge means based on the detected pressure loss. Can be kept constant, and the temperature and flow rate of the second gas heated by the heat medium recovered from the first gas can be stabilized.

According to the second aspect of the present invention, when the heat medium is continuously supplied, the heat medium is supplied into the circulation path from the side path, and the heat medium in the circulation path is supplied during operation. When the amount of the heat medium becomes low, the heat medium can be supplied without dissipating or leaking the first gas from the heat medium supply source. Can be supplied or replenished.

According to the third aspect of the present invention, since the second gas is not directly in contact with the first gas but is heated by the heat medium, the second gas discharged from the second fluidized bed heat exchanger Contains no dust and can obtain clean high-temperature gas. Also, when using clean air as the first gas and using a dust-containing gas as the second gas, the heat medium is circulated between the first and second fluidized bed heat exchangers, and the second fluidized bed heat exchanger is used. The sensible heat is recovered from the dust-containing gas as the second gas, and the heated heat medium is guided to the first fluidized bed heat exchanger. A clean gas can be obtained at a high temperature that does not contain the gas.

According to the fourth aspect of the present invention, the flow velocity of the compressed gas ejected to the heat medium discharge pipe in the discharge pipe is 1.2 to 3.0 times the superficial velocity ub of the fluidized bed. Because it is chosen,
It is possible to reliably prevent dust from being mixed into clean air.

According to the fifth aspect of the present invention, the heat medium is reliably fluidized on each of the dispersion plates of the first and second fluidized bed heat exchangers so that the first and second gases are sufficiently mixed with each other. Heat exchange, eliminating the need to determine the cross-sectional area of the remaining fluidized bed based on the superficial velocity of the first and second gases in the high temperature fluidized bed of the first and second gases, thereby miniaturizing the apparatus. Accordingly, the heat exchange can be sufficiently performed without changing the supply amounts of the first and second gases largely according to the temperatures of the first and second gases.

According to the present invention, the cross-sectional area of the upper fluidized bed of the first fluidized-bed heat exchanger is selected to be smaller than the cross-sectional area of the lower fluidized bed. Since a corresponding appropriate superficial velocity can be obtained, a stable fluidized bed can be formed. Accordingly, the flow rate of the heat medium is stabilized, and the temperatures of the first and second gases can be stabilized. The first gas supplied to such a first fluidized bed heat exchanger is, for example, a high-temperature exhaust gas containing dust discharged from a firing furnace, and such a high-temperature first gas firstly flows through a lower fluidized bed. The formed heating medium is heated, and the heating medium supplied to the lower fluidized bed exchanges heat in the upper fluidized bed with the first gas whose temperature has been reduced by the heat exchange in the lower fluidized bed. Therefore, the pre-heated heat medium forming the upper fluidized bed is supplied to the lower fluidized bed, and the heat medium in the lower step further rises in temperature due to heat exchange with the high-temperature first gas. Has a higher temperature than the upper fluidized bed, and the high-temperature heat medium is guided to the upper fluidized bed of the second fluidized-bed heat exchanger.

In the second fluidized bed heat exchanger, the sectional area of the upper fluidized bed is larger than the sectional area of the lower fluidized bed, so that an appropriate superficial velocity corresponding to the temperature of each fluidized bed can be obtained. Therefore, a stable fluidized bed can be formed. Accordingly, the flow rate of the heat medium is stabilized, and the temperatures of the first and second gases can be stabilized. The second gas supplied to the second fluidized-bed heat exchanger is, for example, normal-temperature air. The second gas having such a low temperature exchanges heat in the lower fluidized bed, and the preheated second gas is the second gas. 1 The fluidized bed heat exchanger exchanges heat with the high-temperature heat medium guided from the lower fluidized bed at the lower stage to raise the temperature.
Therefore, the temperature of the upper fluidized bed is higher than the temperature of the lower fluidized bed, and thus the second gas that does not contain high-temperature dust that has been heat-exchanged in the fluidized bed can be obtained.

According to the present invention, since the flow rate of the heat medium discharged by one airtight discharge means is increased by the control means, the fluidized bed to which the heat medium discharged by this airtight discharge means is supplied is provided. The pressure loss is increased, and the pressure loss is detected by the pressure loss detecting means, and the control means provided corresponding to the fluidized bed responds to the output of the pressure loss detecting means so that the pressure loss becomes a set value of the pressure loss. Control is performed so that the flow rate of the airtight discharge means is increased.
In this way, the flow rate of the airtight discharge means is sequentially set to be large so that the pressure loss of each fluidized bed becomes constant, and the circulation amount of the heat medium increases.

Accordingly, the first flow rate from the first flow bed heat exchanger
When the temperature of the gas increases, the circulation amount of the heat medium is increased to increase the heat recovery amount in the first fluidized bed heat exchanger and the heat medium is transferred to the upper fluidized bed of the second fluidized bed heat exchanger. As a result, it is possible to eliminate the temperature change of the first gas discharged from the first fluidized bed heat exchanger without greatly changing the temperature of the second gas from the second fluidized bed heat exchanger.

According to the present invention, the temperature of the second gas from the second fluidized-bed heat exchanger is detected by the second gas temperature detecting means, and the control is performed as the temperature of the second gas decreases. The means controls the flow rate of the heat medium by one airtight discharge means to be large. Therefore, the amount of heat recovery in the first fluidized bed heat exchanger is increased, whereby the temperature of the second gas from the second fluidized bed heat exchanger can be increased.

According to the present invention, the flow rate of the second gas discharged from the second fluidized bed heat exchanger is also monitored, and if the flow rate of the second gas increases and the gas temperature decreases, ,
The amount of heat recovery in the first fluidized bed heat exchanger is increased by controlling the flow rate of the heat medium by one airtight discharge means to be large. Thus, when the flow rate of the second gas increases, control can be performed so that the temperature of the second gas does not decrease.

According to the tenth aspect of the present invention, the dust collecting means is not limited to the case where the first gas contains dust and the second gas does not contain dust, but the second gas contains dust. , First
Similarly, when the gas does not contain dust, the dust in the first gas after the heat exchange discharged from the first fluidized bed heat exchanger in which the first gas not containing the dust and the heat medium are in AC contact with each other is removed. Since the dust can be collected, dust introduced by the heat medium used for heat exchange with the dust-containing gas can be removed, and a clean high-temperature gas can be obtained.

According to the eleventh aspect of the present invention, the temperature of the first and second gases can be controlled by the flow rate of the circulating heat medium while the pressure loss of each fluidized bed is controlled to be constant. The temperature of the first and second gases is stabilized smoothly and in a short time from the start of the operation, and heat is recovered from one of the first and second gases containing dust, and any one of the first and second gases is recovered. The other can be heated to obtain a clean hot gas.

[Brief description of the drawings]

FIG. 1 is a system diagram showing a heat exchange device 41 according to an embodiment of the present invention.

FIG. 2 is a front view showing a specific configuration of a heat medium supply source 90.

FIG. 3 is a lower dispersion plate 42b of the first fluidized bed heat exchanger 45.
It is an expanded sectional view of a vicinity.

FIG. 4 is an enlarged sectional view showing a specific configuration of the first hermetic discharge means 43.

FIG. 5 shows a first airtight discharge means 4 according to another embodiment of the present invention.
It is an expanded sectional view showing 3a.

FIG. 6 is an enlarged sectional view showing a first hermetic discharge unit 43b according to still another embodiment of the present invention.

FIG. 7 shows first to fourth hermetic discharge means 43, 47, 50, and 5;
FIG. 3 is a block diagram showing an electrical configuration of a control device 161 for controlling the operation of the first control device.

FIG. 8 is a flowchart for explaining the operation of the heat exchange device 41.

FIG. 9 shows the temperature of the gas discharged from the first fluidized bed heat exchanger 45 and the fourth hermetic discharge means 51 according to another embodiment of the present invention.
6 is a graph showing a relationship with a flow rate.

FIG. 10 shows the relationship between the temperature of the gas discharged from the second fluidized bed heat exchanger 49 and the flow rate of the heat medium from the upper fluidized bed 48a to the lower fluidized bed 48b according to still another embodiment of the present invention. FIG.

FIG. 11 is a system diagram showing a heat exchange device 41a according to still another embodiment of the present invention.

FIG. 12 is a system diagram showing a heat exchange device 41b according to still another embodiment of the present invention.

FIG. 13 is a system diagram showing a heat exchange device 41c according to still another embodiment of the present invention.

FIG. 14 is a system diagram showing a heat exchange device 41d according to still another embodiment of the present invention.

FIG. 15 is a graph showing a relationship between the number of stages of a fluidized bed and an outlet gas temperature according to an experiment performed by the present inventor.

FIG. 16 is a simplified sectional view showing a typical prior art heat exchanger 1;

FIG. 17 is an enlarged cross-sectional view of the vicinity of the top overflow pipe 9a of the first fluidized-bed heat exchanger 4 shown in FIG.

[Explanation of symbols]

 41, 41a to 41d Heat exchangers 42a, 42b; 46a, 46b Dispersion plates 43, 43a, 43b First airtight discharge means 44a, 44b; 48a, 48b Fluidized beds 45, 45d First fluidized bed heat exchangers 47 Second airtightness Discharge means 49, 49d Second fluidized bed heat exchanger 50 Third airtight discharge means 51 Fourth airtight discharge means 52 First pressure loss detection means 53 Second pressure loss detection means 54 Third pressure loss detection means 55 Fourth pressure loss Detection means 56 First control means 57 Second control means 58 Third control means 59 Fourth control means 60 Setting means 87, 180 Transportation means 90 Heat medium supply source

Claims (11)

[Claims] 1. A first fluidized bed heat exchanger for fluidizing a heat medium on a dispersion plate by a first gas to form a plurality of fluidized beds connected through hermetic discharge means of the heat medium, A second fluidized bed heat exchanger that fluidizes the heat medium on the plate with the second gas to form a fluidized bed of a plurality of stages connected via hermetic discharge means of the heat medium. The lowermost fluidized bed of the second fluidized bed heat exchanger is connected to the lowermost fluidized bed of the second fluidized bed heat exchanger by the hermetic discharge means of the heat medium. , The uppermost fluidized bed of the first fluidized bed heat exchanger is connected via a heat medium airtight discharge means to form a circulation path of the heat medium, and the flow rate of any one of the heat medium of the airtight discharge means Is set to a predetermined value, and the pressure of the fluidized bed of the heat medium discharged by all remaining airtight discharge means Pressure loss detecting means for detecting the respective losses, in response to the output of the pressure loss detecting means, so that the heat medium from the fluidized bed having the detected pressure loss so that the detected pressure loss becomes a predetermined value. Means for controlling the flow rate of the hermetic discharge means for discharging. 2. A heat medium supply source having a heat medium storage section, an on-off valve for supplying / cutting off the heat medium from the storage section, and a heat medium supply source in the middle of the heat medium circulation path. 2. The heat exchange device according to claim 1, wherein a side passage provided in parallel with another opening / closing valve is interposed. 3. One of the first and second gases is a dust-containing gas, and the lowermost fluidized bed of one of the first and second fluidized-bed heat exchangers using the dust-containing gas. The flow path of the heat medium discharged through the airtight discharge means to the other one of the first and second fluidized bed heat exchangers has a flow velocity in the flow path near the upper end of the flow path. 2. A compressed gas supply means for discharging compressed gas so as to have a speed exceeding the superficial tower speed ub of the lowermost fluidized bed is provided.
Or the heat exchange device according to 2. 4. The discharge speed of the compressed gas by the compressed gas supply means is such that the flow velocity of the heat medium in the flow path is the superficial velocity ub of the fluidized bed.
4. The heat exchange device according to claim 3, wherein the heat exchange device is selected to be 1.2 to 3.0 times. 5. The first and second fluidized bed heat exchangers each have a plurality of stages of fluidized beds, and each fluidized bed has a first and a second fluidized bed so that the cross-sectional area thereof is equal to or greater than the minimum fluidization speed umf. The heat exchange device according to any one of claims 1 to 4, wherein the second gas is formed to be smaller as the temperature of the second gas becomes lower by heat exchange with the heat medium. 6. The temperature of the first gas is a value exceeding the temperature of the second gas, the first and second fluidized bed heat exchangers each have a plurality of stages of fluidized beds, The cross-sectional area of the fluidized bed of the exchanger is formed such that the upper stage is smaller than the lower stage, and the cross-sectional area of the fluidized bed of the second fluidized bed heat exchanger is formed smaller than the upper stage. 5. The heat exchange device according to 5. 7. A heat exchange device for recovering sensible heat of a first gas by a second gas, wherein the first gas temperature detects the temperature of the first gas after heat exchange from a first fluidized bed heat exchanger. Detecting means, in response to the output of the first gas temperature detecting means, the flow rate of the heat medium by the one hermetic discharge means as the detected temperature of the first gas increases so as to become a preset temperature. The heat exchange device according to any one of claims 1 to 6, further comprising another control means for largely controlling the temperature. 8. A heat exchange device for recovering sensible heat of a first gas by a second gas, wherein a second gas temperature for detecting a temperature of the second gas after heat exchange from a second fluidized bed heat exchanger. Detecting means, in response to the output of the second gas temperature detecting means, the flow rate of the heat medium by the one hermetic discharge means as the detected temperature of the second gas decreases so as to become a preset temperature. The heat exchange device according to any one of claims 1 to 6, further comprising another control means for largely controlling the temperature. 9. The apparatus further comprises a second gas flow rate detecting means for detecting a flow rate of the second gas, wherein the another control means responds to an output of the second gas temperature detecting means to attain a preset temperature. 9. The heat exchange device according to claim 8, wherein the flow rate of the heat medium by the one hermetic discharge unit is set to increase as the flow rate detected by the second gas flow rate detection unit increases. 10. The method according to claim 1, wherein one of the first gas and the second gas is a dust-containing gas, and the uppermost one of the first and second fluidized-bed heat exchangers using the dust-containing gas. The bed is provided with dust collecting means for collecting and guiding dust from the other one of the gases from the uppermost stage of the other one of the fluidized bed heat exchangers. A heat exchange device according to any one of the above. 11. A first fluidized bed heat exchanger that fluidizes the heat medium on the dispersion plate with the first gas to form a plurality of fluidized beds connected through hermetic discharge means for the heat medium; A second fluidized bed heat exchanger for fluidizing the heat medium on the plate by the second gas to form a multi-stage fluidized bed connected through hermetic discharge means of the heat medium, The lowermost fluidized bed of the second fluidized bed heat exchanger is connected to the lowermost fluidized bed of the second fluidized bed heat exchanger by the hermetic discharge means of the heat medium. , The uppermost fluidized bed of the first fluidized bed heat exchanger is connected via a hermetic discharge means for the heated medium to form a circulation path for the heated medium, and pressure loss detection for detecting the pressure loss of each fluidized bed. Means, and the detected pressure loss becomes a predetermined value in response to the output of the pressure loss detecting means. Control means for controlling the flow rate of the hermetic discharge means for discharging the heat medium from the fluidized bed in which the detected pressure loss has occurred, and the heat medium is dispersed by an amount less than an amount that generates a predetermined value of the pressure loss. In the state where the heat medium is present on the plate or the heat medium is not present on the dispersion plate, the heat medium is supplied in the middle of the circulation path, and each pressure loss of all the fluidized beds has reached the predetermined value. When the supply of the heat medium is stopped, the flow rate is set to a predetermined value without controlling one of all the hermetic discharge means by detecting the pressure loss, and all of the remaining The method for operating a heat exchange device, wherein the airtight discharge means is controlled by detecting the pressure loss.