WO2012115014A1

WO2012115014A1 - Pneumatic transport facility for chlorine bypass dust, and cement kiln exhaust gas treatment system equipped with the facility

Info

Publication number: WO2012115014A1
Application number: PCT/JP2012/053866
Authority: WO
Inventors: 朝明西岡; 靖雄柳原; 和之伊藤; 俊一長崎; 一平中島; 渡辺　晴夫; 小林　稔
Original assignee: 電気化学工業株式会社; デンカエンジニアリング株式会社
Priority date: 2011-02-22
Filing date: 2012-02-17
Publication date: 2012-08-30
Also published as: CN103261114A; JP2012171839A; JP4746158B1

Abstract

Provided is a transport facility for chlorine bypass dust, in which the occurrence of a blockage in a pipe can be reduced during the transport of the chlorine bypass dust. A pneumatic transport facility for dust collected from a cement kiln exhaust gas, comprising: a first dust collection tank which is equipped with an inlet port and a discharge port for a cement kiln exhaust gas, a dust collector for collecting dust from the cement kiln exhaust gas, and a discharge port for the collected dust; a pressurized tank which is equipped with an inlet port for the dust from the first dust collection tank, an inlet port for air and an discharge port for pneumatic transport of the dust and which enables the pneumatic transport of the dust by means of compressed air; an air supply source which supplies dried and compressed air having an atmospheric dew point of -35˚C or lower to the pressurized tank; and a second dust collection tank which is equipped with an inlet port for dust that is pneumatically transported from the pressurized tank through a second pipe, a dust collector for collecting dust, and a discharge port for air.

Description

Chlorine bypass dust pneumatic transportation equipment and cement kiln exhaust gas treatment system equipped with the equipment

The present invention relates to an air transportation facility for chlorine bypass dust. The present invention also relates to a cement kiln exhaust gas treatment system equipped with the chlorine bypass dust pneumatic transportation facility according to the present invention.

The exhaust gas from the cement kiln equipment contains volatile components such as alkali chlorides and alkali sulfates. These volatile components are gradually concentrated while circulating between the preheater and the kiln in the cement kiln facility, and are taken into the clinker to adversely affect the quality of the cement and adhere to the inner wall of the preheater as a coating. In order to block the inner wall surface of the preheater or the like, a part of the exhaust gas is extracted from the volatile component concentration region near the bottom of the cement kiln kiln (Japanese Patent Laid-Open Nos. 9-175847 and 11- No. 35355, JP 2001-335348 A, Japanese Patent No. 4435273, etc.). The volatile component in the extracted exhaust gas solidified by cooling is called chlorine bypass dust.

Chlorine bypass dust can be processed with a finishing mill together with cement clinker, etc., but there is a certain distance from the cement kiln to the finishing mill, and it is necessary to transport the chlorine bypass dust to there. As a conventional method for transporting chlorine bypass dust, there is a method in which chlorine bypass dust is extracted from a storage tank near a cement kiln and transported to a storage tank near a finishing mill by a truck (Japanese Patent Laid-Open No. 2000-354838). However, since chlorine bypass dust is deliquescent, there is a problem that when the wall surface temperature of these storage tanks is lowered, piping is clogged due to deliquescence, making it difficult to extract chlorine bypass dust from the storage tank. Japanese Patent No. 3318714 describes the possibility of transporting the chlorine bypass dust out of the cement kiln system and then transporting it to the cement finishing mill by pneumatic transport. However, chlorine bypass dust is highly deliquescent. The pipes are clogged during pneumatic transportation, and there has been no success so far.

In order to prevent these blockages, a method has been proposed in which water is added to chlorine bypass dust to form a slurry, and this slurry is mixed in a cement manufacturing mill together with at least one of clinker, gypsum, and a mixed material (Japanese Patent Application Laid-Open (JP-A)). 2000-354838). According to the literature, by applying in combination with an apparatus having a coarse powder separation step of dust in the bypass gas, it is possible to make the slurry generation amount at most 1% with respect to the cement production amount. It is described that this amount is equal to or less than the amount of water sprayed in the mill at the time of clinker grinding and does not affect the quality of cement.

Japanese Patent Laid-Open No. 9-175847 JP-A-11-35355 JP 2001-335348 A Japanese Patent No. 4435273 JP 2000-354838 A Japanese Patent No. 3318714

However, the method of slurrying chlorine bypass dust described in Japanese Patent Application Laid-Open No. 2000-354838 is likely to cause corrosion and blockage of the watering nozzle in the mill. As a result, it becomes difficult to control the amount of water sprayed from the nozzle, and the mill outlet temperature is likely to fluctuate due to fluctuations in the water sprinkling amount.

The present invention has been made in view of the above circumstances, and eliminates the need for truck transportation to the finish mill of chlorine bypass dust, while reducing piping blockage in the process of transporting chlorine bypass dust by a method different from slurrying. It is an object of the present invention to provide a chlorine bypass dust transport facility that can be used. Moreover, this invention makes it a subject to provide the processing system of the cement kiln exhaust gas provided with the transport equipment of the said chlorine bypass dust.

The present inventor has intensively studied to solve the above problems, and found that it is effective to pneumatically transport dehumidified dry air having a predetermined dew point without discharging chlorine bypass dust out of the system. Based on this, the following invention was created.

In one aspect of the present invention,
A first dust collecting tank having a cement kiln exhaust gas inlet and outlet, a dust collector for collecting dust from the cement kiln exhaust gas, and a collected dust outlet;
A pressurized tank having a dust inlet from the first dust collection tank, an air inlet, and a dust air outlet, and for pneumatically transporting the dust by compressed air; provided that the first dust The dust outlet in the collection tank is above the dust inlet in the pressurized tank, and both are communicated by a first pipe.
An air supply source for supplying dry compressed air having an atmospheric dew point of −35 ° C. or lower to the pressurized tank;
A dust inlet that is pneumatically transported from the pressurized tank through the second pipe, a dust collector for collecting the dust, and a second dust collection tank having an air outlet;
Is a pneumatic transportation facility for dust collected from cement kiln exhaust gas.

In one embodiment of the pneumatic transportation equipment according to the present invention, the exhaust gas flowing into the cement kiln exhaust gas of the first dust collection tank has an atmospheric dew point of 10 to 40 ° C. and a temperature of 50 to 150 ° C. Previously dehumidified and cooled.

In another embodiment of the pneumatic transportation facility according to the present invention, the air supply source includes an adsorption air dryer or a heatless air dryer.

In still another embodiment of the pneumatic transportation facility according to the present invention, the gas temperature in the pressurized tank is 0 to 40 ° C.

The pneumatic transportation equipment according to the present invention is still another embodiment,
Pressure switch to monitor the pressure in the pressurized tank,
A level switch for monitoring the amount of dust in the pressurized tank; and
When the level switch detects that the amount of dust in the pressurized tank has reached a predetermined level, the supply of dust from the first dust collection tank to the pressurized tank is stopped, and the pressurized tank is dried. When the pressure switch detects that the pressure has been increased by air and increased to a predetermined pressure, it starts air transportation of dust to the second dust collection tank, and then the pressure switch indicates that the pressure has decreased to the predetermined pressure. When detected, the apparatus further includes a control mechanism that stops pneumatic transportation of dust and restarts supply of dust from the first dust collection tank to the pressurized tank.

In still another embodiment of the pneumatic transportation facility according to the present invention, the supply of dust from the first dust collection tank to the pressurized tank is stopped, and then the pressurization from the first dust collection tank is performed. The time until the supply of dust to the tank is restarted is within 10 minutes.

In still another embodiment of the pneumatic transportation facility according to the present invention, dust is passing through the first pipe from the dust outlet in the first dust collecting tank to the dust inlet in the pressurized tank. The dry air flows in the first pipe from the pressurized tank toward the first dust collecting tank at a flow rate that does not flow backward.

In still another embodiment of the pneumatic transportation facility according to the present invention, the pressure in the pressurized tank during pneumatic transportation of dust is 0.1 to 0.5 MPaG.

In still another embodiment of the pneumatic transportation facility according to the present invention, the dust in the pressurized tank flows into the pressurized tank during pneumatic transportation of the dust from the pressurized tank to the second dust collecting tank. Being fluidized by dry air.

In still another embodiment of the pneumatic transportation facility according to the present invention, two or more pressurized tanks are installed in parallel, and at least one of the remaining pressurized tanks during pneumatic transportation is at least one of the pressurized tanks. Dust is put into one pressurized tank from the first dust collection tank.

In still another embodiment of the pneumatic transportation facility according to the present invention, a primary storage tank is installed in series before the pressurized tank, and the first dust collection is performed during the pneumatic transportation of the latter pressurized tank. Dust is thrown from the tank into the primary storage tank.

In another aspect of the present invention,
A cement kiln exhaust gas treatment system comprising the pneumatic transportation equipment and the extraction facility for cement kiln exhaust gas according to the present invention described above,
The extraction facility for cement kiln exhaust gas includes an extraction pipe for extracting a part of the cement kiln exhaust gas, a blower for supplying air for dehumidification and cooling into the extraction pipe, and a collector connected to the outlet of the extraction pipe. A dust cyclone, an air cooler connected to the outlet of the cyclone, a blower for supplying air for dehumidification and cooling into the air cooler, and an induction fan,
The outlet of the first dust collection tank is connected to the induction fan,
The second dust collection tank has an outlet for the collected dust, which is in communication with a mill or cement clinker tank for cement production;
This is a cement kiln exhaust gas treatment system.

In one embodiment of the cement kiln exhaust gas treatment system according to the present invention, the air outlet of the second dust collection tank is connected to the induction fan.

In another embodiment of the cement kiln exhaust gas treatment system according to the present invention, the gas flow rate at the outlet of the extraction pipe is set to 10 m / s or more.

According to the pneumatic transportation equipment and the cement kiln exhaust gas treatment system according to the present invention, the chlorine bypass dust is deliquescent during storage or transportation, so that dust adheres to and clogs the container and piping. This makes it possible to pneumatically transport chlorine bypass dust that is practical.

1 is a cement kiln exhaust gas treatment system according to an embodiment of the present invention. In the pneumatic transportation equipment of chlorine bypass dust concerning the present invention, it is a mimetic diagram showing an example at the time of installing a pressurized tank in parallel. It is a schematic diagram which shows an example at the time of installing a primary storage tank in the front | former stage of a pressurized tank in the pneumatic transport equipment of the chlorine bypass dust which concerns on this invention.

<1. Air transportation equipment>
Referring to FIG. 1, the chlorine bypass dust pneumatic transportation facility according to the present invention is, in one embodiment,
A first dust collection tank 100 having a cement kiln exhaust gas inlet 101 and outlet 102, a dust collector 103 for collecting dust from the cement kiln exhaust gas, and a collected dust outlet 104;
A pressurized tank 200 having a dust inlet 201 from the first dust collection tank 100, an air inlet 202, and a dust air transport outlet 203 for pneumatically transporting the dust by compressed air; The dust outlet 104 in the first dust collection tank 100 is above the dust inlet 201 in the pressurized tank 200, and both are communicated by the first pipe 105.
An air supply source 300 for supplying dry compressed air having an atmospheric pressure dew point of −35 ° C. or lower to the pressurized tank 200;
A dust inlet 401 that is pneumatically transported from the pressurized tank 200 through the second pipe 204, a dust collector 402 for collecting dust, and a second dust collection tank 400 having an air outlet 403;
It has.

Deliquession is a phenomenon in which when a solid is exposed to the atmosphere, it absorbs water vapor in the atmosphere and dissolves it to create an aqueous solution. The chlorine bypass dust generated by cooling the exhaust gas extracted in the cement manufacturing process generally has potassium chloride (hereinafter referred to as KCl) as a main component. Although there is a report that pure KCl does not have deliquescence, the chlorine bypass dust shows very high deliquescence because it contains other components such as CaO and SiO _{2 in} addition to potassium chloride. Table 1 shows the storage time dependence of the moisture content of chlorine bypass dust and Portland cement under conditions of room temperature and humidity of 100%. It can be understood how high the deliquescence of chlorine bypass dust is. it can.

The cement kiln exhaust gas flows into the first dust collection tank 100 through the inlet 101. The inflowing cement kiln exhaust gas contains chlorine bypass dust, which is collected by the dust collector 103. Although there is no restriction | limiting in particular as a kind of dust collector, For example, a bag filter, a cyclone, and an electric dust collector are suitable. The exhaust gas after the chlorine bypass dust is collected is discharged from the outlet 102.

Cement kiln exhaust gas is generally a high-temperature and high-humidity gas having a temperature of about 900 to 1100 ° C. and an atmospheric dew point of 55 ° C. or higher, typically about 60 to 70 ° C. When the cement kiln exhaust gas flows into the first dust collection tank 100 in such a high temperature and high humidity state, the dust collector 103 exceeds the durability limit and malfunctions. In the first pipe 105, the chlorine bypass dust to which moisture adheres is deliquescent and is likely to be clogged. On the other hand, if the cement kiln exhaust gas is cooled by dehumidified air in order to perform dehumidification strongly, the equipment cost jumps and is not realistic.

Therefore, the cement kiln exhaust gas flowing into the inlet 101 is preferably dehumidified in advance so that the atmospheric dew point is 10 to 40 ° C., and more preferably dehumidified to 20 to 30 ° C. . Further, the cement kiln exhaust gas flowing into the inlet 101 is preferably cooled in advance so that the temperature becomes 50 to 150 ° C., and more preferably precooled so that the temperature becomes 60 to 100 ° C. . Further, the relative humidity is preferably less than 100%, more preferably 50% or less, and even more preferably 20% or less. If it is this range, outside air can be utilized as cooling air, and it is practical also from the viewpoint of durability of the dust collector 103 and suppression of deliquescence in the first dust collection tank 100 and the first pipe 105. Lowering the exhaust gas temperature after cooling improves the durability of the bag filter, and it is possible to use an inexpensive product with a low heat-resistant temperature for the bag filter. In order to maintain the desired temperature and prevent deliquescent of the dust, the temperature is kept by any known means such as covering the periphery of the first dust collection tank 100 with a heat insulating material or installing a heater around it. Or you may heat.

The exhaust gas discharged from the cement kiln exhaust gas outlet 102 can be directed to the induction fan 108 through the exhaust pipe 106, for example. After exiting the induction fan 108, it can be exhausted from the chimney after passing through a dryer, a stabilizer, an electric dust collector or the like as necessary. As the induction fan 108, it is convenient and economical to use a kiln IDF that attracts most of the exhaust gas from the cement kiln. The kiln IDF is also used in the embodiment according to FIG. A bag filter exhaust fan 107 is preferably installed upstream of the induction fan 108 to collect dust that could not be collected by the dust collector 103, and is also installed in the present embodiment of FIG.

On the other hand, the dust collected in the first dust collection tank 100 goes from the outlet 104 to the lower pressurized tank 200 through the first pipe 105. As shown in FIG. 1, the outlet 104 is preferably provided at the bottom of the first dust collection tank 100 so that the dust collected in the first dust collection tank 100 can be extracted by gravity. The one dust collection tank 100 is preferably formed in a tapered shape or a cone shape that is recessed toward the bottom from the viewpoint of facilitating extraction of dust. Further, by arranging the dust outlet 104 in the first dust collection tank 100 above the dust inlet 201 in the pressurized tank 200, the dust discharged from the outlet 104 passes through the first pipe 105 by gravity. Thus, it can fall naturally into the pressurized tank 200. The first pipe 105 communicating the dust inlet 201 and the dust outlet 104 preferably extends in the vertical direction, but may be slightly inclined as long as the dust is smoothly transported.

Although not employed in the embodiment according to FIG. 1, dust is passing through the first pipe 105 from the dust outlet 104 in the first dust collection tank 100 to the dust inlet 201 in the pressurized tank 200. The dry air described later may flow through the first pipe 105 from the pressurized tank 200 toward the first dust collecting tank 100 at a flow rate that does not cause the dust to flow backward. As a result, the deliquescence of dust in the first pipe 105 can be suppressed. From the viewpoint of preventing dust deliquescence, the first pipe 105 may be kept warm or heated. The first pipe 105 can be provided with a valve for controlling the flow of dust. For example, a dust input valve 501 can be provided at or near the dust outlet 104, and a dust input valve 502 can be provided at or near the dust inlet 201.

The pressurized tank 200 stores the dust from the first dust collection tank 100. When a predetermined amount of dust accumulates, it is sealed and pressurized to the pressure necessary for pneumatic transport of the dust, and then the transport valve 504 installed at the dust air transport outlet 203 is opened to collect the dust in the second dust collection. Air transport to tank 400. During transportation, compressed air is introduced from the air inlet 202 into the second dust collection tank 400 through the second pipe 204.

This compressed air is supplied from the air supply source 300 to the pressurized tank 200 through the air pipe 303. The air supply source 300 is generally provided with an air compressor 301 using outside air, but is not limited thereto. An air supply valve 503 for controlling the supply of compressed air can be installed in the air pipe 303 between the air supply source 300 and the pressurized tank 200. From the viewpoint of preventing dust deliquescence, air should have as low a dew point as possible. Specifically, it is desirable to use dry air having an atmospheric dew point of −35 ° C. or lower. As a result, even if the gas temperature in the pressurized tank 200 is not particularly heated (for example, 0 to 40 ° C., typically 10 to 30 ° C.), liquefaction of dust is suppressed to a practical level. be able to. The atmospheric pressure dew point of the compressed air is more preferably −40 ° C. or less, still more preferably −50 ° C. or less, most preferably −60 ° C. or less. The temperature can be 80 ° C to -35 ° C. Such dry air can be obtained by using an air supply source 300 having an air dryer 302 such as an adsorption air dryer or a heatless air dryer.

As for the compressed air pressure condition, if the transport pressure is too low, the dust cannot be transported to the destination, but if the transport pressure is too high, the relative humidity increases and the liquefaction of the dust easily occurs. It is preferable that the pressure inside the pressurized tank 200 is adjusted to be 0.1 to 0.5 MPaG.

During the pneumatic transportation of dust from the pressurized tank 200 to the second dust collection tank 400, it is preferable that the dust in the pressurized tank 200 is in a fluid state due to the dry air flowing into the pressurized tank 200. Thereby, it is possible to suppress the dust in the pressurized tank 200 from adhering to the inner wall of the pressurized tank 200, and it is possible to reduce the dust remaining in the pressurized tank 200 after pneumatic transportation. For this purpose, for example, as shown in FIG. 1, an air inlet 202 can be provided at the bottom of the pressurized tank 200. The dust stored in the pressurized tank 200 is fluidized by the compressed air introduced into the pressurized tank 200.

It is also possible to keep warm or warm by any known means such as covering the periphery of the pressurized tank 200 with a heat insulating material or installing a heater around it. Although not employed in the embodiment according to FIG. 1, relatively high-temperature compressed air can be supplied by providing the air supply source 300 with a heater. As a result, the relative humidity of the gas in the pressurized tank 200 and the second pipe 204 can be lowered, which is useful for preventing dust deliquescence.

Dust is introduced into the second dust collection tank 400 from the inlet 401 by pneumatic transportation. The second dust collection tank 400 has a dust collector 402 for collecting dust and an air outlet 403. Although there is no restriction | limiting in particular as a kind of dust collector, For example, a bag filter is suitable. The air after the dust is collected is discharged from the outlet 403. The air discharged from the outlet 403 may be released to the atmosphere as it is, or may be discharged by providing a dedicated exhaust system. Further, as shown in FIG. 1, an exhaust pipe 404 may be connected to the outlet 403, and this may be joined to the exhaust pipe 106 of the first dust collection tank 100. This is economical because the exhaust system is integrated.

Since the above-described dry air is fed into the second dust collection tank 400, there is almost no moisture brought into the second dust collection tank 400. Therefore, chlorine bypass dust can be stored for a long time while suppressing deliquescence. For example, it can be stored for one week or longer, and preferably can be stored for one month or longer. After the storage period, the dust can be smoothly discharged from the second dust collection tank 400. The discharged dust can be put into a nearby cement manufacturing mill (finishing mill) or a cement clinker tank through a valve such as a rotary valve.

The pneumatic transport facility for chlorine bypass dust according to the present invention can include a pressure switch 601 for monitoring the pressure in the pressurized tank 200 and a level switch 602 for monitoring the amount of dust in the pressurized tank 200. A control mechanism for controlling pneumatic transport can be provided. For example, the control mechanism can operate the pneumatic transportation facility in the following procedure. When the level switch 602 detects that the amount of dust in the pressurized tank 200 has reached a predetermined amount, the supply of dust from the first dust collection tank 100 to the pressurized tank 200 is stopped, and the pressure is increased. The tank 200 is pressurized with dry air, and when it is detected by the pressure switch 601 that the pressure has risen to a predetermined pressure, the air transportation of dust to the second dust collecting tank 400 is started, and then the pressure is lowered to the predetermined pressure. When this is detected by the pressure switch 601, the pneumatic transportation of dust is stopped, and the supply of dust from the first dust collection tank 100 to the pressurized tank 200 is resumed.

A more detailed operation procedure of the pneumatic transportation facility in the embodiment according to FIG. 1 will be described. When the input valve 501, the input valve 502, the air supply valve 503, and the transport valve 504 are closed, first, the input valve 502 and the input valve 501 are opened in order, so that the inside of the first dust collection tank 100. Is started to enter the pressurized tank 200. When the level switch 602 detects that the amount of dust in the pressurized tank 200 has reached a predetermined amount, the charging source valve 501 and the charging valve 502 are closed in order, so that the addition from the first dust collection tank 100 is performed. The supply of dust to the pressure tank 200 is stopped. Next, the air supply valve 503 is opened, and the inside of the pressurized tank 200 is pressurized with dry air. When the pressure switch 601 detects that the pressure has risen to a predetermined pressure, the transport valve 504 is opened and the pneumatic transport of dust to the second dust collection tank 400 is started. The pressure in the pressurized tank 200 decreases rapidly when there is no dust to be transported. Therefore, when the pressure switch 601 detects that the pressure has dropped to a predetermined pressure, the air supply valve and the transport valve are closed in order to stop the air transport of dust. Thereafter, when the input valve 502 and the input source valve 501 are sequentially opened, the input of the dust in the first dust collection tank 100 into the pressurized tank 200 is started again, and the above-described operation is repeated.

While dust is pneumatically transported from the pressurized tank 200 to the second dust collection tank 400, the supply of dust from the first dust collection tank 100 to the pressurized tank 200 is stopped. The dust is accumulated in one dust collecting tank 100. However, since the humidity in the first dust collection tank 100 is relatively high, from the viewpoint of suppressing dust deliquescence, the dust should stay in the first dust collection tank 100 for a long time. Is not preferred. Therefore, after the supply of dust from the first dust collection tank 100 to the pressurized tank 200 is stopped, the supply of dust from the first dust collection tank 100 to the pressurized tank 200 is restarted. The shorter time is desirable, for example, preferably within 10 minutes, and more preferably within 5 minutes. However, if this time is too short, the frequency of opening and closing of the valve increases, which adversely affects the life of the valve. Therefore, it is preferably 1 minute or longer, and typically 2 to 4 minutes.

As another method, as shown in FIG. 2, two pressurized tanks 200 are installed in parallel, and dust can be put into the other pressurized tank while one pressurized tank is pneumatically transported. If necessary, two or more pressurized tanks 200 may be installed in parallel. In that case, while a certain pressurized tank is pneumatically transported, dust is thrown into the remaining pressurized tank from the first dust collection tank. Alternatively, as shown in FIG. 3, a primary storage tank 205 is installed in series in the front stage of the pressurized tank, and dust is thrown into the primary storage tank 205 in the previous stage while the subsequent pressurized tank 200 is transported by air. When transportation is completed, dust can be put into the pressurized tank from the primary storage tank. By doing in this way, dust can be continuously discharged from the first dust collection tank 100. Dry air similar to that sent to the pressurized tank 200 can be sent to the primary storage tank 205 to keep the inside dry.

<2. Cement kiln exhaust gas treatment system>
The above-described chlorine bypass dust pneumatic transportation facility according to the present invention can be combined with a cement kiln exhaust gas extraction facility to constitute a cement kiln exhaust gas treatment system. As a result, a series of steps from recovering chlorine bypass dust from the exhaust gas extracted from the cement kiln and treating it with the finishing mill can be continuously performed by the piping system. The cement kiln exhaust gas treatment system according to the present invention eliminates the need for truck transportation to the finishing mill of chlorine bypass dust, reduces pipe blockage in the transportation process of chlorine bypass dust, and corrodes the water spray nozzle in the finishing mill. In addition, it is possible to reduce the clogging and blockage, and it is possible to pneumatically transport chlorine bypass dust that is practical.

Referring to FIG. 1, a cement kiln exhaust gas treatment system according to the present invention includes, in one embodiment, the above-described chlorine bypass dust pneumatic transportation facility and cement kiln exhaust gas extraction facility according to the present invention, and cement kiln exhaust gas. The extraction equipment is connected to an extraction pipe 702 for extracting a part of the cement kiln exhaust gas, a blower 703 for supplying air for dehumidification and cooling into the extraction pipe 702, and an outlet of the extraction pipe 702. A dust collecting cyclone 704, an air cooler 705 connected to the outlet of the cyclone 704, a blower 706 for supplying air for dehumidification and cooling into the air cooler 705, and an induction fan 108. The inlet 101 of the first dust collection tank 100 is in communication with the air cooler 705 and the exhaust pipe 710, and The outlet 102 of the waste collection tank 100 is connected to the induction fan 108 by the exhaust pipe 106, and the second dust collection tank 400 has an outlet 405 of the collected dust, which is used for cement production. To a mill or cement clinker tank.

The extraction pipe 702 extracts a part of the exhaust gas containing volatile components discharged from the rotary kiln. The exhaust gas is a hot and humid gas as described above. In addition to the kiln kiln 701, the bleed pipe 702 is generally provided in the middle of a rising duct or a calcining furnace that extends right above the kiln kiln 701. In FIG. 1, air is extracted from the rising duct. A blower 703 is connected to the extraction pipe 702 by a duct, from which air for dehumidification and cooling is pushed into the extraction pipe 702 so as to flow in the direction of the cyclone 704. The introduced air cools and dehumidifies the exhaust gas while mixing with the extracted exhaust gas. As described above, outside air is sufficient as the air used here, but for the reason of securing the cooling rate, the gas flow rate at the outlet of the extraction pipe 702 is preferably 10 m / s or more, for example, 10 to 30 m / s. It can be.

The mixed gas of the exhaust gas and the cooling air that has exited the extraction pipe 702 is introduced into the dust collecting cyclone 704 through the exhaust pipe 709, and coarse particles are separated. Thereafter, the mixed gas is mixed with the cooling air pushed by the blower 706 in the air cooler 705 and further cooled. Thereafter, the mixed gas is introduced into the first dust collection tank 100 through the exhaust pipe 710, and the chlorine bypass dust is recovered in the first dust collection tank 100 from the exhaust gas. The amount of air for dehumidification and cooling supplied from the blower 703 and the blower 706 is adjusted so that the temperature and humidity of the cement kiln exhaust gas flowing into the first dust collection tank 100 are within the above-described ranges. That's fine. The operation of the pneumatic transport facility for chlorine bypass dust after the chlorine bypass dust is introduced into the first dust collection tank 100 is as described above.

Hereinafter, the present invention will be described using examples, but the present invention is not limited to these examples.

Example 1
The cement kiln exhaust gas treatment system in the embodiment of FIG. 1 was operated for one week under the following operating conditions.

<Operating conditions>
(1) Cement kiln exhaust gas at the inlet of the extraction pipe 702:
-Temperature: 900-1100 ° C
-Atmospheric pressure dew point: 60-69 ° C
-Air volume: 150 [m ³ N / min]
(2) Air for cooling and dehumidification:
-Outside air (temperature: 2-16 ° C, atmospheric dew point: -5-11 ° C)
-Air volume sent from the blower to the extraction pipe 702: 250 [m ³ N / min]
-Air flow rate sent from the blower to the cooler 705: 320 [m ³ N / min]
(3) Gas flow velocity at the outlet of the extraction pipe 702: 15 m / s
(4) Cement kiln exhaust gas flowing into the inlet 101:
-Gas temperature: 58-82 ° C
-Atmospheric pressure dew point: 30-39 ° C
(5) Dust collector 103 of the first dust collection tank 100: Bag filter (6) Presence / absence of heat insulation of the first dust collection tank 100: Existence (heat insulation material + electric heater)
(7) Presence / absence of heat insulation of the first pipe 105: Existence (heat insulation material)
(8) Gas temperature in the pressurized tank 200: 12 to 38 ° C
(9) Pressure in the pressurized tank during pneumatic transportation: 0.15 MPaG
(10) Transportation air supply source:
Air compressor Adsorption air dryer (SHD3045 made by CKD)
(11) Atmospheric pressure dew point of transport air: -40 to -56 ° C
(12) Presence / absence of heat retention of the pressurized tank 200: Existence (heat insulation material)
(13) Dust collector 402 of second dust collection tank 400: bag filter (14) After the supply of dust from the first dust collection tank 100 to the pressurized tank 200 is stopped, the first dust collection Time until dust supply from the collection tank 100 to the pressurized tank 200 is restarted: about 2 minutes (15) Pressure switch height (PISH) setting value: 0.15 MPaG
(16) Pressure switch low (PIS L) set value: 0.06 MPaG
(17) Level switch height (LS H) set value: 0.1 m ³
(18) Pneumatic transport distance: 150m

The dew points of the cement kiln exhaust gas at the inlet of the extraction pipe 702 and the cement kiln exhaust gas flowing into the inlet 101 were calculated based on JIS Z 8808-1995 by measuring the moisture content in the exhaust gas using a moisture absorption pipe.
The dew point of air for cooling and dehumidification and the dew point of air for transportation were measured by a capacitance type temperature and humidity sensor.

In addition, when the chemical analysis of the chlorine bypass dust obtained by sampling a part of the exhaust gas in the extraction pipe 702 and cooling it, the results shown in Table 2 were obtained.

As a result of operating the cement kiln exhaust gas treatment system under the above operating conditions, almost no dust was observed on any of the first pipe 105, the pressurized tank 200, and the second pipe 204.

(Example 2)
The cement kiln exhaust gas treatment system in the embodiment shown in FIG. 1 was operated for one week in the same manner as in Example 1 except that the operating conditions were changed as follows.
<Operating conditions>
(1) Air for cooling and dehumidification:
-Outside air (temperature: 2-16 ° C, atmospheric dew point: -5-11 ° C)
-Air volume sent from the blower to the extraction pipe 702: 100 [m ³ N / min]
-Air flow rate sent from the blower to the cooler 705: 100 [m ³ N / min]
(2) Gas flow velocity at the outlet of the extraction pipe 702: 6 m / s
(3) Cement kiln exhaust gas flowing into the inlet 101:
-Gas temperature: 230-270 ° C
-Atmospheric pressure dew point: 43-52 ° C
(4) Gas temperature in the pressurized tank 200: 65 to 98 ° C

As a result of operating the cement kiln exhaust gas treatment system under the above operating conditions, almost no dust was observed on any of the first pipe 105, the pressurized tank 200, and the second pipe 204. However, since the temperature of the cement kiln exhaust gas flowing into the first dust collection tank is too high, it is considered that the life of the bag filter is affected. Specifically, it will affect the deterioration life of the resin of the bag filter filter cloth due to high temperature, and continuous operation for six months will be impossible.

(Comparative Example 1)
The cement kiln exhaust gas treatment system was operated for one week under the same conditions as in Example 1 except that the compressed air was not dried with an air dryer. The atmospheric pressure dew point of the transportation air was −5 to 5 ° C. As a result, in all of the first pipe 105, the pressurized tank 200, and the second pipe 204, a larger amount of dust adheres and grows than in the first embodiment, which causes clogging in the pipe, and continuous operation is performed during the test. It became impossible.

DESCRIPTION OF SYMBOLS 100 First dust collection tank 101 Cement kiln exhaust gas inlet 102 Cement kiln exhaust gas outlet 103 Dust collector 104 Dust outlet 105 First pipe 106 Exhaust pipe
107 Bag filter exhaust fan 108 Induction fan 200 Pressurized tank 201 Dust inlet 202 from the first dust collection tank 202 Air inlet 203 Dust air transport outlet 204 Second piping 205 Primary storage tank 300 Air supply source 301 Air Compressor 302 Air Dryer 303 Air Pipe 400 Second Dust Collection Tank 401 Air Dust Inlet 402 Dust Collector 403 Air Outlet 404 Exhaust Pipe 405 Dust Outlet 501 Input Source Valve 502 Input Valve 503 Air Supply Valve 504 Transport valve 601 Pressure switch
602 Level switch 701 Kiln kiln bottom 702 Extraction pipe 703 Blower 704 Dust collection cyclone 705 Air cooler 706 Blower 709 Exhaust pipe 710 Exhaust pipe

Claims

A first dust collecting tank having a cement kiln exhaust gas inlet and outlet, a dust collector for collecting dust from the cement kiln exhaust gas, and a collected dust outlet;
A pressurized tank having a dust inlet from the first dust collection tank, an air inlet, and a dust air outlet, and for pneumatically transporting the dust by compressed air; provided that the first dust The dust outlet in the collection tank is above the dust inlet in the pressurized tank, and both are communicated by a first pipe.
An air supply source for supplying dry compressed air having an atmospheric dew point of −35 ° C. or lower to the pressurized tank;
A dust inlet that is pneumatically transported from the pressurized tank through the second pipe, a dust collector for collecting the dust, and a second dust collection tank having an air outlet;
Air transport equipment for dust collected from exhaust gas from a cement kiln.
The exhaust gas flowing into the cement kiln exhaust gas inlet of the first dust collection tank is dehumidified and cooled in advance so that the atmospheric dew point is 10 to 40 ° C and the temperature is 50 to 150 ° C. Air transport equipment.
The air transportation equipment according to claim 1 or 2, wherein the air supply source has an adsorption air dryer or a heatless air dryer.
The pneumatic transportation equipment according to any one of claims 1 to 3, wherein the gas temperature in the pressurized tank is 0 to 40 ° C.
Pressure switch to monitor the pressure in the pressurized tank,
A level switch for monitoring the amount of dust in the pressurized tank; and
When the level switch detects that the amount of dust in the pressurized tank has reached a predetermined level, the supply of dust from the first dust collection tank to the pressurized tank is stopped, and the pressurized tank is dried. When the pressure switch detects that the pressure has been increased by air and increased to a predetermined pressure, it starts air transportation of dust to the second dust collection tank, and then the pressure switch indicates that the pressure has decreased to the predetermined pressure. 5. A control mechanism according to claim 1, further comprising a control mechanism that stops pneumatic transportation of dust when detected and restarts supply of dust from the first dust collection tank to the pressurized tank. Pneumatic transport equipment as described.
Within 10 minutes from when the supply of dust from the first dust collection tank to the pressurized tank is stopped until the supply of dust from the first dust collection tank to the pressurized tank is resumed The pneumatic transportation equipment according to claim 5.
While dust passes through the first pipe from the dust outlet in the first dust collection tank to the dust inlet in the pressurized tank, the first dust collection from the pressurized tank at a flow rate that does not cause the dust to flow back. The pneumatic transportation equipment according to any one of claims 1 to 6, wherein the dry air flows in the first pipe toward the tank.
The pneumatic transportation equipment according to any one of claims 1 to 7, wherein the pressure in the pressurized tank during the pneumatic transportation of dust is 0.1 to 0.5 MPaG.
The dust in the pressurized tank is in a fluidized state by the dry air flowing into the pressurized tank during the pneumatic transportation of the dust from the pressurized tank to the second dust collecting tank. Pneumatic transportation equipment according to item.
Two or more pressurized tanks are installed in parallel, and when at least one pressurized tank is pneumatically transported, at least one of the remaining pressurized tanks receives dust from the first dust collection tank. The pneumatic transportation equipment according to any one of claims 1 to 4, which is input.
The primary storage tank is installed in series in front of the pressurized tank, and dust is thrown into the primary storage tank from the first dust collection tank while the latter pressurized tank is pneumatically transported. The pneumatic transport facility according to any one of the above.
A cement kiln exhaust gas treatment system comprising the pneumatic transportation facility according to any one of claims 1 to 11 and a cement kiln exhaust gas extraction facility,
The extraction facility for cement kiln exhaust gas includes an extraction pipe for extracting a part of the cement kiln exhaust gas, a blower for supplying air for dehumidification and cooling into the extraction pipe, and a collector connected to the outlet of the extraction pipe. A dust cyclone, an air cooler connected to the outlet of the cyclone, a blower for supplying air for dehumidification and cooling into the air cooler, and an induction fan,
The outlet of the first dust collection tank is connected to the induction fan,
The second dust collection tank has an outlet for the collected dust, which is in communication with a mill or cement clinker tank for cement production;
Cement kiln exhaust gas treatment system.
The cement kiln exhaust gas treatment system according to claim 12, wherein an air outlet of the second dust collection tank is connected to the induction fan.
The cement kiln exhaust gas treatment system according to claim 12 or 13, wherein the gas flow rate at the outlet of the extraction pipe is 10 m / s or more.