WO2019106796A1 - Powdered coal supply device and toxic trace element elution suppression method - Google Patents

Powdered coal supply device and toxic trace element elution suppression method Download PDF

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Publication number
WO2019106796A1
WO2019106796A1 PCT/JP2017/043122 JP2017043122W WO2019106796A1 WO 2019106796 A1 WO2019106796 A1 WO 2019106796A1 JP 2017043122 W JP2017043122 W JP 2017043122W WO 2019106796 A1 WO2019106796 A1 WO 2019106796A1
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Prior art keywords
coal
elution
pulverized
feeder
pulverized coal
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PCT/JP2017/043122
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French (fr)
Japanese (ja)
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英嗣 清永
健治 引野
啓一郎 盛田
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中国電力株式会社
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Priority to JP2018513561A priority Critical patent/JP6744401B2/en
Priority to PCT/JP2017/043122 priority patent/WO2019106796A1/en
Publication of WO2019106796A1 publication Critical patent/WO2019106796A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K1/00Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L7/00Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam

Definitions

  • the present invention relates to a pulverized coal feeding device and a harmful trace element elution suppression method.
  • it is a pulverized coal feeding apparatus and a harmful trace element elution suppression method for use in a coal thermal power plant using pulverized coal as a fuel for a boiler, wherein the elution inhibitor is a fine powder that suppresses the elution of harmful trace elements from combustion residue of coal.
  • the present invention relates to the structure of a pulverized coal feeding device and a method for suppressing harmful trace element elution, which can be reliably added to charcoal at a constant rate.
  • pulverized coal is used as fuel for a boiler.
  • the coal stored in the coal storage plant is discharged, and coal is transported to the pulverized coal feeding device by a coal transport mechanism such as a conveyor.
  • the pulverized coal supply apparatus includes a coal pulverizer (mill) that pulverizes massive coal into fine particles to form pulverized coal.
  • Pulverized coal produced by the coal pulverizer is sent to a boiler and burned in the boiler.
  • the combustion heats the water to generate steam.
  • oil may be supplied to the boiler.
  • the steam generated in the boiler is supplied to a steam turbine, a generator is driven by the steam turbine, and power can be supplied by the generator.
  • the steam that has passed through the steam turbine is condensed by the condenser and condensed to the boiler together with the makeup water.
  • the pulverized coal supply apparatus described above includes a coal bunker storing coal, a coal feeder, and a coal pulverizer.
  • a coal bunker storing coal
  • coal feeder a coal feeder
  • coal pulverizer a coal pulverizer
  • the coal feeder has a transfer conveyor inside, and coal supplied from the coal feeding pipe is horizontally transferred by the transfer conveyor. Then, coal is discharged from the transfer conveyor to the coal discharge port formed at the end of the transfer conveyor. Furthermore, coal is introduced into the coal pulverizer through a second coal feed pipe formed in connection with the coal discharge port.
  • the call gate valve for opening and closing the first coal feeding pipe is disposed immediately above the feeder. The call gate valve can be opened and closed manually.
  • coal ash to be a residue after combustion contains trace amounts of harmful trace elements such as boron, fluorine, selenium, arsenic and hexavalent chromium.
  • harmful trace elements such as boron, fluorine, selenium, arsenic and hexavalent chromium.
  • an elution inhibitor for coal addition consisting of calcium carbonate (CaCO 3 ) to coal
  • CaO calcium oxide
  • alkali Discloses a method for suppressing the elution of harmful trace elements that contributes to the suppression of elution of harmful trace elements (see, for example, Patent Document 2).
  • the harmful trace element elution suppression method according to Patent Document 2 can be easily applied to the improvement of existing equipment because addition of the elution inhibitor is added at the stage of coal during combustion or before combustion instead of coal ash after combustion. And. Moreover, the harmful trace element elution suppression method by patent document 2 will not be specifically limited if the timing of addition is addition in the state of coal, Any of a coal feeder, a coal pulverizer, and a boiler may be sufficient, And
  • Patent Document 2 discloses the timing of the addition of the harmful trace element elution inhibitor, the place where the harmful trace element elution inhibitor is injected is not specified.
  • Pulverized coal supply apparatus and harmful trace element elution suppression method for use in a coal thermal power plant using pulverized coal as fuel for a boiler, wherein mixing ratio of coal and elution control agent of harmful trace element falls within a certain ratio
  • the present invention has been made in view of such problems, and it is a pulverized coal supply device and a harmful trace element elution suppression method used for a coal-fired power generation facility using pulverized coal as a fuel for a boiler It is an object of the present invention to provide a pulverized coal feeding apparatus and a harmful trace element elution suppression method, in which the mixing ratio of a trace element elution inhibitor can be contained in a constant ratio.
  • the present inventors comprise a pulverized coal feeding apparatus comprising a conveyer for conveying coal, and a coal pulverizer disposed below the downstream end of the conveyer and crushing coal to form pulverized coal.
  • Dispense elution inhibitor that suppresses elution of harmful trace elements from above the conveyer conveyor or coal pulverizer to make the mixing ratio of coal and elution inhibitor of harmful trace elements constant by dropping it into the coal pulverizer
  • the inventors have invented the following new pulverized coal feeding apparatus and harmful trace element elution suppression method as follows.
  • a pulverized coal supply apparatus includes: a coal bunker storing coal; a coal feeder including therein a conveyer for conveying coal supplied from the coal bunker from one end to the other end; And a pulverized coal feeder including a coal pulverizer for pulverizing coal input from the other end of the feeder to produce pulverized coal, wherein the feeder is configured to discharge coal. And a box-shaped frame with the coal discharge opening at the bottom of the other end, and an elution inhibitor that can suppress the elution of harmful trace elements from the combustion residue of coal toward the coal discharge opening of the frame. And an elution inhibitor addition device.
  • the elution inhibitor addition device includes a hopper storing the elution inhibitor, and a screw feeder for feeding the elution inhibitor supplied from the hopper toward the coal discharge port of the frame. Is preferred.
  • the coal feeder includes a first motor for driving the conveyer, and the anti-elution agent addition device includes a second motor for driving the screw feeder, and corresponds to the rotational speed of the first motor.
  • the rotational speed of the second motor is adjusted.
  • the said elution inhibiting agent contains 1 or more types selected from the group which consists of a limestone, a limestone, and quick lime.
  • the elution inhibitor is preferably in the form of granules or powder.
  • the harmful trace element elution suppression method according to the present invention is the harmful trace element elution suppression method in a coal-fired thermal power plant equipped with a pulverized coal feed device, wherein the pulverized coal feed device comprises a conveyor for conveying coal; A coal pulverizer disposed below the downstream end of the conveyer and crushing coal to form pulverized coal; harmful trace elements from above the conveyer or the coal pulverizer The elution inhibitor which suppresses the elution of is dropped to the said coal pulverizer.
  • the rotational speed of the second motor for driving the screw feeder that feeds the elution inhibitor toward the coal pulverizer is adjusted in accordance with the rotational speed of the first motor for driving the transport conveyor. Is preferred.
  • the pulverized coal feeding device is disposed at the end of the conveyer, and the elution inhibitor addition device is disposed above the coal discharge port from which coal is discharged, and the elution of harmful trace elements in the elution inhibitor addition device
  • the mixing ratio of coal and the elution inhibitor of harmful trace element can be made constant by storing the inhibitor and supplying the elution inhibitor of harmful trace element from the elution inhibitor addition device toward the coal discharge port.
  • the harmful trace element elution suppression method is a harmful trace element elution suppression method in a coal-fired power plant equipped with a pulverized coal feeding device, wherein the pulverized coal feed device comprises a conveyer for conveying coal, and a downstream of the conveyer. And a coal pulverizer, which is disposed below the end of the side to pulverize coal to produce pulverized coal, and which prevents elution of harmful trace elements from above the conveyer conveyor or the coal pulverizer.
  • the agent By dropping the agent into a coal pulverizer, the mixing ratio of coal and the elution inhibitor of harmful trace elements can be made constant.
  • FIG. 1 is a schematic view showing a configuration of an example of a coal-fired power plant using a pulverized coal supply apparatus according to an embodiment of the present invention.
  • FIG. 2 is a front view showing the configuration of a pulverized coal supply device according to an embodiment of the present invention.
  • a coal-fired power plant 100 includes a pulverized coal supply device 10 and a boiler 20.
  • the coal-fired power plant 100 further includes a steam turbine 30 and a condenser 40.
  • the pulverized coal supply device 10 includes a coal bunker 11 and a coal feeder 12.
  • the pulverized coal feeding device 10 further includes an elution inhibitor adding device 13 and a coal pulverizer 14.
  • coal C is conveyed to a coal bunker 11 by a conveyor 15 with a dustproof cover from a coal storage station (not shown). Then, massive coal C is temporarily stored in the coal bunker 11. Coal C stored in the coal bunker 11 is supplied to the coal feeder 12.
  • the coal feeder 12 internally includes a transport conveyor 12 c.
  • the transport conveyor 12 c can transport the coal C supplied from the coal bunker 11 from one end to the other end.
  • the coal pulverizer 14 can pulverize the coal C fed from the other end of the coal feeder 12 to produce pulverized coal.
  • the boiler 20 internally includes a combustion chamber 2 r fueled by pulverized coal produced by the coal pulverizer 14.
  • oil is sent to the combustion chamber 2 r via an oil feed pipe (not shown).
  • pulverized coal can be burned.
  • combustion air is sent to the combustion chamber 2r by a ventilator.
  • two-stage combustion is performed. By this combustion, the water supplied from the feed pump 41 is heated to become superheated steam, and the superheated steam is sent from the boiler 20 to the steam turbine 30.
  • the steam turbine 30 internally includes a turbine (impeller). If the superheated steam is fed into the turbine from its axial direction, the turbine can be rotated. The rotating shaft of the turbine is connected to the rotor of the generator 31. When superheated steam is fed into the steam turbine 30, power can be supplied by the rotor of the generator 31 rotating.
  • a turbine impeller
  • the superheated steam that has consumed kinetic energy in the steam turbine 30 is returned to water by being cooled and condensed in the condenser 40. In other words, it is recovered.
  • the condensed water is circulated to the boiler 20 by the feed water pump 41 together with the makeup water.
  • the coal thermal power generation facility 100 heats water with the boiler 20 using pulverized coal as fuel to generate superheated steam, and sends the superheated steam to the steam turbine 30. Power can be supplied by the generator 31.
  • the coal bunker 11 is composed of an inverted conical main body 11 b whose top surface is opened and a coal feeding pipe 11 p extending from the bottom of the main body 11 b.
  • the coal feed pipe 11 p is connected to one end of the coal feeder 12. Bulk coal C stored in the main body 11 b can be dumped into the inside of the coal feeder 12 through the coal feeding pipe 11 p.
  • a call gate valve 11c is disposed in the middle of the coal feeding pipe 11p.
  • the call gate valve 11c is internally provided with a valve body capable of opening and closing the pipe line of the coal feeding pipe 11p.
  • the call gate valve 11 c connects the third motor 11 m.
  • the call gate valve 11c is internally provided with a conversion mechanism (not shown) for converting the rotational movement of the third motor 11m into the forward and backward movement of the valve body.
  • a conversion mechanism (not shown) for converting the rotational movement of the third motor 11m into the forward and backward movement of the valve body.
  • the coal feeder 12 includes a box-like frame 12 f and a conveyer 12 c.
  • the frame 12 f opens the coal outlet 12 s from which the coal C is discharged at the bottom of the other end.
  • the coal discharge port 12s is an inlet opening of a coal feeding pipe 14p connecting the frame 12f and the coal pulverizer 14.
  • the coal C discharged to the coal injection port 12s is fed to the coal pulverizer 14 and pulverized coal C is pulverized by the coal pulverizer 14, whereby pulverized coal can be produced.
  • the conveyer 12c is composed of a pair of rollers 121 and 122 and an endless belt 12v.
  • the pair of rollers 121 and 122 are spaced apart from each other.
  • the endless belt 12v winds a pair of rollers 121 and 122.
  • the roller 121 is a driving wheel
  • the roller 122 is a driven wheel.
  • the drive side roller 121 couples the first motor 12 m.
  • the first motor 12m When the first motor 12m is rotated in one direction, the upper side of the endless belt 12v can travel from one end to the other end, and the coal C supplied from the coal bunker 11 is conveyed toward the coal discharge port 12s it can.
  • the 1st motor 12m can adjust the input quantity per unit time of the coal C introduce
  • the anti-elution agent addition device 13 includes an inverted conical hopper 13 h having an open top and a screw feeder 13 f.
  • the hopper 13h stores the elution inhibitor Ea.
  • the elution inhibitor Ea can suppress the elution of harmful trace elements from the combustion residue of coal.
  • a gate valve 13v is provided between the hopper 13h and the screw feeder 13f.
  • the gate valve 13v can open and close a pipeline from the hopper 13h to the screw feeder 13f.
  • the pipeline from the hopper 13 h to the screw feeder 13 f can be opened and closed.
  • the screw feeder 13 f can send out the elution inhibitor Ea supplied from the hopper 13 h toward the coal discharge port 12 s of the frame 12 f.
  • the screw feeder 13f connects the second motor 13m.
  • the spiral screw 13s can be rotated to send out the elution inhibitor Ea in the axial direction.
  • the rotation of the second motor 13m corresponds to the rotational speed of the first motor 12m, that is, corresponding to the input amount of coal C input to the coal pulverizer 14 per unit time.
  • the amount of the elution inhibitor Ea can be adjusted at an appropriate rate.
  • the pulverized coal feeding device 10 is formed at the end of the conveyer 12c, and places a hopper 13h with a screw feeder 13f above the coal discharge opening 12s from which coal is discharged, Disposal agent Ea of harmful trace elements is stored in hopper 13h, and screw feeder 13f is driven to feed elution stop agent Ea of harmful trace elements from hopper 13h to coal injection port 12s, thereby causing harmful effects to coal and harmful substances.
  • the mixing ratio of the elution inhibitor Ea of trace element can be made constant.
  • the coal feeder 12 includes a first motor 12 m that drives the transfer conveyor 12 c. Further, the elution inhibitor adding device 13 is provided with a second motor 13m that drives the screw feeder 13f.
  • the rotational speed of the second motor 13m corresponding to the rotational speed of the first motor 12m, that is, corresponding to the input amount of coal C input to the coal pulverizer 14 per unit time.
  • the amount of elution inhibitor Ea can be adjusted at an appropriate rate.
  • the elution inhibitor Ea contains one or more selected from the group consisting of limestone, limestone and quicklime.
  • the elution inhibitor Ea is preferably in the form of granules or powder.
  • the average particle size of the elution inhibitor Ea preferably does not exceed 200 ⁇ m.
  • the pulverized coal and the elution inhibitor Ea can be mixed and delivered to the boiler 20.
  • the coal pulverizer 14 be internally provided with a classifier utilizing centrifugal force, so-called dry cyclone. After classifying the pulverized coal and the elution inhibitor Ea pulverized by the coal pulverizer 14 into predetermined particle sizes, it is possible to deliver the pulverized coal and the elution inhibitor Ea to the boiler 20.
  • the means for supplying elution inhibitor Ea to coal feeder 12 is not limited to screw feeder 13f.
  • the type of feeder or conveyor serving as the supplying means is not limited as long as the transportation means is suitable for powder transportation.
  • the elution inhibitor Ea may be dropped onto the conveyer 12c, and the elution inhibitor Ea for suppressing elution of harmful trace elements from above the coal pulverizer 14 is pulverized by a coal pulverizer. By dropping it to 14, the addition amount of the elution inhibitor Ea can be adjusted at an appropriate ratio with respect to the coal.
  • the pulverized coal supply apparatus adds the elution inhibitor to the feed speed of the first motor for driving the conveyer by separately providing the means for injecting coal and the elution inhibitor into the feeder. You can adjust the amount.
  • the harmful trace element elution suppression method according to the present invention can separately supply the coal and the elution inhibitor upstream of the coal pulverizer without mixing the coal and the elution inhibitor on the conveyor for conveying the coal to the coal bunker. Therefore, the amount of elution inhibitor added to coal can be adjusted.
  • the pulverized coal supply device can be expected to have the following effects. (1) By mixing with pulverized coal and feeding the elution inhibitor of the proper composition to the boiler and burning it at a high temperature, it is possible to accelerate the uptake of harmful trace elements into the coal ash. (2) Since the elution inhibitor mixed with pulverized coal is fed into the boiler and burned at a high temperature, harmful trace elements flowing from the exhaust gas into the desulfurization apparatus can be suppressed.

Abstract

The present invention provides a powdered coal supply device with which the ratio between coal and an elution prevention agent for toxic trace elements can be uniform. This powdered carbon supply device 10 is provided with: a coal bunker 11 in which coal is stored; a coal feeder 12 that has therein a transportation conveyor 12c that transports the coal supplied from the coal bunker 11; and a coal pulverizer 14 that pulverizes the coal charged from the coal feeder 12 and generates powdered coal. The coal feeder 12 is provided with a box-like frame 12f and an elution suppression agent adding device 13. The frame 12f has a coal dropping port 12s from which the coal is discharged and which is open at a lower part of another end part. The elution suppression agent adding device 13 can drop, toward the coal dropping port 12s in the frame 12s, an elution suppression agent Ea for suppressing the elution of toxic trace elements from combustion residue of the coal.

Description

微粉炭供給装置及び有害微量元素溶出抑制方法Pulverized coal supply device and harmful trace element elution suppression method
 本発明は、微粉炭供給装置及び有害微量元素溶出抑制方法に関する。特に、微粉炭をボイラの燃料とする石炭火力発電設備に用いられる微粉炭供給装置及び有害微量元素溶出抑制方法であって、石炭の燃焼残滓から有害微量元素の溶出を抑制する溶出防止剤を微粉炭に一定の割合で確実に添加できる、微粉炭供給装置の構造及び有害微量元素溶出抑制方法に関する。 TECHNICAL FIELD The present invention relates to a pulverized coal feeding device and a harmful trace element elution suppression method. In particular, it is a pulverized coal feeding apparatus and a harmful trace element elution suppression method for use in a coal thermal power plant using pulverized coal as a fuel for a boiler, wherein the elution inhibitor is a fine powder that suppresses the elution of harmful trace elements from combustion residue of coal. The present invention relates to the structure of a pulverized coal feeding device and a method for suppressing harmful trace element elution, which can be reliably added to charcoal at a constant rate.
 例えば、石炭火力発電所では、ボイラの燃料として微粉炭を用いている。この石炭火力発電所では、貯炭場に蓄えた石炭を払出し、コンベアなどの石炭搬送機構によって、石炭を微粉炭供給装置に搬送している。この微粉炭供給装置は、塊状の石炭を微細になるまで粉砕して微粉炭を生成する石炭微粉砕機(ミル)を含んでいる。 For example, in a coal-fired power plant, pulverized coal is used as fuel for a boiler. In this coal thermal power plant, the coal stored in the coal storage plant is discharged, and coal is transported to the pulverized coal feeding device by a coal transport mechanism such as a conveyor. The pulverized coal supply apparatus includes a coal pulverizer (mill) that pulverizes massive coal into fine particles to form pulverized coal.
 石炭微粉砕機で生成された微粉炭は、ボイラに送られ、ボイラで燃焼される。この燃焼によって水を加熱して蒸気を発生させる。なお、ボイラの内部の点火にあっては、石油がボイラに供給されることもある。 Pulverized coal produced by the coal pulverizer is sent to a boiler and burned in the boiler. The combustion heats the water to generate steam. In the case of ignition inside the boiler, oil may be supplied to the boiler.
 ボイラで発生した蒸気は、蒸気タービンに供給され、蒸気タービンによって発電機が駆動され、発電機によって電力を供給できる。なお、蒸気タービンを通過した蒸気は、復水器で復水され、補給水と共にボイラに復水されている。 The steam generated in the boiler is supplied to a steam turbine, a generator is driven by the steam turbine, and power can be supplied by the generator. The steam that has passed through the steam turbine is condensed by the condenser and condensed to the boiler together with the makeup water.
 上述した微粉炭供給装置は、石炭を貯留した石炭バンカー、給炭機、及び、石炭微粉砕機を備えている。石炭バンカーには、貯炭場から石炭搬送機構によって搬送された石炭が一時的に保管されている。そして、石炭バンカーから第1給炭管を介して、給炭機に石炭が供給される。 The pulverized coal supply apparatus described above includes a coal bunker storing coal, a coal feeder, and a coal pulverizer. In the coal bunker, coal transported from the coal storage station by the coal transport mechanism is temporarily stored. Then, coal is supplied from the coal bunker to the coal feeder via the first coal feeding pipe.
 給炭機は、搬送コンベアを内部に備え、給炭管から供給された石炭が搬送コンベアにより水平方向に移送される。そして、搬送コンベアから、搬送コンベアの端部に形成した石炭投下口に石炭が排出される。更に、石炭投下口に連接して形成した第2給炭管を介して、石炭が石炭微粉砕機に投入される。上述した微粉炭供給装置は、第1給炭管を開閉するためのコールゲート弁を給炭機の直上に配設している。このコールゲート弁は、手動で開閉できる。 The coal feeder has a transfer conveyor inside, and coal supplied from the coal feeding pipe is horizontally transferred by the transfer conveyor. Then, coal is discharged from the transfer conveyor to the coal discharge port formed at the end of the transfer conveyor. Furthermore, coal is introduced into the coal pulverizer through a second coal feed pipe formed in connection with the coal discharge port. In the pulverized coal feeding device described above, the call gate valve for opening and closing the first coal feeding pipe is disposed immediately above the feeder. The call gate valve can be opened and closed manually.
 ところで、コールゲート弁を閉方向に手動で駆動して第1給炭管を閉じると、コールゲート弁以降の給炭管と搬送コンベアとの間に石炭が溜まったままの状態となる。これにより、第1給炭管に石炭詰まりが生じることがある。そして、石炭微粉砕機を長期間停止した後、運転を再開した際においても、石炭微粉砕機に石炭を安定して供給できる微粉炭供給装置が開示されている(例えば、特許文献1参照)。 By the way, when the call gate valve is manually driven in the closing direction to close the first coal feeding pipe, coal is still accumulated between the coal feeding pipe after the call gate valve and the transport conveyor. This may cause coal clogging in the first coal feed pipe. And after stopping a coal pulverizer for a long period of time, when resuming operation, the pulverized coal supply device which can stably supply coal to a coal pulverizer is disclosed (for example, refer to patent documents 1). .
 一方、微粉炭をボイラの燃料とする石炭火力発電では、燃焼後の残渣となる石炭灰には、ホウ素、フッ素、セレン、ヒ素、六価クロムなどの有害微量元素を微量ながら含んでいる。このため、石炭灰に含まれている有害微量元素の溶出濃度を法定の規制値以下に低減するための技術が検討されている。 On the other hand, in coal-fired power generation using pulverized coal as a fuel for boilers, coal ash to be a residue after combustion contains trace amounts of harmful trace elements such as boron, fluorine, selenium, arsenic and hexavalent chromium. For this reason, techniques for reducing the elution concentration of harmful trace elements contained in coal ash to less than legally regulated values have been studied.
 例えば、炭酸カルシウム(CaCO)からなる石炭添加用溶出防止剤を石炭に添加することで、酸化カルシウム(CaO)の作用により、多くの有害微量元素が灰石炭灰へ移行、併せてアルカリの作用により有害微量元素の溶出抑制に寄与する、有害微量元素溶出抑制方法が開示されている(例えば、特許文献2参照)。 For example, by adding an elution inhibitor for coal addition consisting of calcium carbonate (CaCO 3 ) to coal, many harmful trace elements are transferred to ash coal ash by the action of calcium oxide (CaO), and additionally the action of alkali Discloses a method for suppressing the elution of harmful trace elements that contributes to the suppression of elution of harmful trace elements (see, for example, Patent Document 2).
特開2012-26724号公報Unexamined-Japanese-Patent No. 2012-26724 特開2008-275181号公報JP 2008-275181 A
 特許文献2による有害微量元素溶出抑制方法は、溶出防止剤の添加を燃焼後の石炭灰ではなく、燃焼中又は燃焼前の石炭の段階で添加するので、既存の設備の改良で簡単に適用できる、としている。又、特許文献2による有害微量元素溶出抑制方法は、添加のタイミングが石炭の状態での添加であれば特に限定されず、給炭機、石炭微粉砕機、ボイラのいずれであってもよい、としている。 The harmful trace element elution suppression method according to Patent Document 2 can be easily applied to the improvement of existing equipment because addition of the elution inhibitor is added at the stage of coal during combustion or before combustion instead of coal ash after combustion. And. Moreover, the harmful trace element elution suppression method by patent document 2 will not be specifically limited if the timing of addition is addition in the state of coal, Any of a coal feeder, a coal pulverizer, and a boiler may be sufficient, And
 しかし、特許文献2による有害微量元素溶出抑制方法は、有害微量元素の溶出防止剤の添加のタイミングを開示しているが、有害微量元素の溶出防止剤の投入場所は明示していない。 However, although the harmful trace element elution suppression method according to Patent Document 2 discloses the timing of the addition of the harmful trace element elution inhibitor, the place where the harmful trace element elution inhibitor is injected is not specified.
 例えば、石炭を石炭バンカーに搬送するコンベア上で、粒状の炭酸カルシウム(CaCO3)を混合すると、塊状の石炭よりもはるかに粒径の細かい炭酸カルシウムが石炭バンカーの底部に先に落下し、石炭と炭酸カルシウムの混合比にバラツキが生じる結果になる。そして、石炭と炭酸カルシウムの混合比が一定の数値範囲に収まらないことから、有害微量元素をうまく抑制できない心配があった。石炭バンカーの後工程で、石炭に対して、有害微量元素の溶出防止剤を適正な割合で添加することが困難になる心配がある。 For example, when granular calcium carbonate (CaCO 3) is mixed on a conveyor that transports coal to a coal bunker, calcium carbonate having a much smaller particle size than the bulk coal falls first at the bottom of the coal bunker, and This results in variations in the mixing ratio of calcium carbonate. And, since the mixing ratio of coal and calcium carbonate does not fall within a certain numerical range, there is a concern that harmful trace elements can not be suppressed well. There is a concern that it will be difficult to add an elution inhibitor of harmful trace elements at an appropriate ratio to the coal in the post process of the coal bunker.
 微粉炭をボイラの燃料とする石炭火力発電設備に用いられる微粉炭供給装置及び有害微量元素溶出抑制方法であって、石炭と有害微量元素の溶出防止剤の混合比が一定の割合に収まることが可能な微粉炭供給装置及び有害微量元素溶出抑制方法が求められている。そして、以上のことが本発明の課題といってよい。 Pulverized coal supply apparatus and harmful trace element elution suppression method for use in a coal thermal power plant using pulverized coal as fuel for a boiler, wherein mixing ratio of coal and elution control agent of harmful trace element falls within a certain ratio There is a need for possible pulverized coal supply devices and methods for controlling the release of harmful trace elements. And, the above can be said to be the problem of the present invention.
 本発明は、このような課題に鑑みてなされたものであり、微粉炭をボイラの燃料とする石炭火力発電設備に用いられる微粉炭供給装置及び有害微量元素溶出抑制方法であって、石炭と有害微量元素の溶出防止剤の混合比が一定の割合に収まることが可能な微粉炭供給装置及び有害微量元素溶出抑制方法を提供することを目的とする。 The present invention has been made in view of such problems, and it is a pulverized coal supply device and a harmful trace element elution suppression method used for a coal-fired power generation facility using pulverized coal as a fuel for a boiler It is an object of the present invention to provide a pulverized coal feeding apparatus and a harmful trace element elution suppression method, in which the mixing ratio of a trace element elution inhibitor can be contained in a constant ratio.
 本発明者らは、微粉炭供給装置を石炭を搬送する搬送コンベアと、搬送コンベアの下流側の端部の下方に配置され、石炭を粉砕して微粉炭を生成する石炭微粉砕機で構成し、搬送コンベア、又は石炭微粉砕機の上方から、有害微量元素の溶出を抑制する溶出防止剤を石炭微粉砕機に投下することで、石炭と有害微量元素の溶出防止剤の混合比を一定にできると考え、これに基づいて、以下のような新たな微粉炭供給装置及び有害微量元素溶出抑制方法を発明するに至った。 The present inventors comprise a pulverized coal feeding apparatus comprising a conveyer for conveying coal, and a coal pulverizer disposed below the downstream end of the conveyer and crushing coal to form pulverized coal. , Dispense elution inhibitor that suppresses elution of harmful trace elements from above the conveyer conveyor or coal pulverizer to make the mixing ratio of coal and elution inhibitor of harmful trace elements constant by dropping it into the coal pulverizer Based on this idea, the inventors have invented the following new pulverized coal feeding apparatus and harmful trace element elution suppression method as follows.
 (1)本発明による微粉炭供給装置は、石炭を貯留した石炭バンカー、前記石炭バンカーから供給された石炭を一方の端部から他方の端部に搬送する搬送コンベアを内部に有する給炭機、及び、前記給炭機の他方の端部から投入された石炭を粉砕して微粉炭を生成する石炭微粉砕機を備えた微粉炭供給装置であって、前記給炭機は、石炭が排出される石炭投下口を他方の端部の下部に開口した箱状のフレームと、前記フレームの石炭投下口に向かって、石炭の燃焼残渣から有害微量元素の溶出を抑制する溶出防止剤を投下自在な溶出防止剤添加装置と、を備えている。 (1) A pulverized coal supply apparatus according to the present invention includes: a coal bunker storing coal; a coal feeder including therein a conveyer for conveying coal supplied from the coal bunker from one end to the other end; And a pulverized coal feeder including a coal pulverizer for pulverizing coal input from the other end of the feeder to produce pulverized coal, wherein the feeder is configured to discharge coal. And a box-shaped frame with the coal discharge opening at the bottom of the other end, and an elution inhibitor that can suppress the elution of harmful trace elements from the combustion residue of coal toward the coal discharge opening of the frame. And an elution inhibitor addition device.
 (2)前記溶出防止剤添加装置は、前記溶出防止剤を貯留したホッパーと、前記ホッパーから供給された前記溶出防止剤を前記フレームの石炭投下口に向かって送り出すスクリューフィーダと、を備えていることが好ましい。 (2) The elution inhibitor addition device includes a hopper storing the elution inhibitor, and a screw feeder for feeding the elution inhibitor supplied from the hopper toward the coal discharge port of the frame. Is preferred.
 (3)前記給炭機は、前記搬送コンベアを駆動する第1モータを備え、前記溶出防止剤添加装置は、前記スクリューフィーダを駆動する第2モータを備え、前記第1モータの回転速度に対応して、前記第2モータの回転速度を調整していることが好ましい。 (3) The coal feeder includes a first motor for driving the conveyer, and the anti-elution agent addition device includes a second motor for driving the screw feeder, and corresponds to the rotational speed of the first motor. Preferably, the rotational speed of the second motor is adjusted.
 (4)前記溶出防止剤は、石灰石、消灰石、生石灰からなる群より選択される1種以上を含んでいることが好ましい。 (4) It is preferable that the said elution inhibiting agent contains 1 or more types selected from the group which consists of a limestone, a limestone, and quick lime.
 (5)前記溶出防止剤は、粒状体又は粉末状体からなることが好ましい。 (5) The elution inhibitor is preferably in the form of granules or powder.
 (6)本発明による有害微量元素溶出抑制方法は、微粉炭供給装置を備える石炭火力発電設備における有害微量元素溶出抑制方法であって、前記微粉炭供給装置は、石炭を搬送する搬送コンベアと、前記搬送コンベアの下流側の端部の下方に配置され、石炭を粉砕して微粉炭を生成する石炭微粉砕機と、を備え、前記搬送コンベア又は前記石炭微粉砕機の上方から、有害微量元素の溶出を抑制する溶出防止剤を前記石炭微粉砕機に投下する。 (6) The harmful trace element elution suppression method according to the present invention is the harmful trace element elution suppression method in a coal-fired thermal power plant equipped with a pulverized coal feed device, wherein the pulverized coal feed device comprises a conveyor for conveying coal; A coal pulverizer disposed below the downstream end of the conveyer and crushing coal to form pulverized coal; harmful trace elements from above the conveyer or the coal pulverizer The elution inhibitor which suppresses the elution of is dropped to the said coal pulverizer.
 (7)前記搬送コンベアを駆動する第1モータの回転速度に対応して、前記溶出防止剤を前記石炭微粉砕機に向かって送り出すスクリューフィーダを駆動する第2モータの回転速度を調整していることが好ましい。 (7) The rotational speed of the second motor for driving the screw feeder that feeds the elution inhibitor toward the coal pulverizer is adjusted in accordance with the rotational speed of the first motor for driving the transport conveyor. Is preferred.
 本発明による微粉炭供給装置は、搬送コンベアの端部に形成し、石炭が排出される石炭投下口の上方に、溶出防止剤添加装置を配置し、溶出防止剤添加装置に有害微量元素の溶出防止剤を貯留し、溶出防止剤添加装置から石炭投下口に向けて、有害微量元素の溶出防止剤を供給することで、石炭と有害微量元素の溶出防止剤の混合比を一定にできる。 The pulverized coal feeding device according to the present invention is disposed at the end of the conveyer, and the elution inhibitor addition device is disposed above the coal discharge port from which coal is discharged, and the elution of harmful trace elements in the elution inhibitor addition device The mixing ratio of coal and the elution inhibitor of harmful trace element can be made constant by storing the inhibitor and supplying the elution inhibitor of harmful trace element from the elution inhibitor addition device toward the coal discharge port.
 本発明による有害微量元素溶出抑制方法は、微粉炭供給装置を備える石炭火力発電設備における有害微量元素溶出抑制方法であって、微粉炭供給装置は、石炭を搬送する搬送コンベアと、搬送コンベアの下流側の端部の下方に配置され、石炭を粉砕して微粉炭を生成する石炭微粉砕機と、を備え、搬送コンベア又は石炭微粉砕機の上方から、有害微量元素の溶出を抑制する溶出防止剤を石炭微粉砕機に投下することで、石炭と有害微量元素の溶出防止剤の混合比を一定にできる。 The harmful trace element elution suppression method according to the present invention is a harmful trace element elution suppression method in a coal-fired power plant equipped with a pulverized coal feeding device, wherein the pulverized coal feed device comprises a conveyer for conveying coal, and a downstream of the conveyer. And a coal pulverizer, which is disposed below the end of the side to pulverize coal to produce pulverized coal, and which prevents elution of harmful trace elements from above the conveyer conveyor or the coal pulverizer. By dropping the agent into a coal pulverizer, the mixing ratio of coal and the elution inhibitor of harmful trace elements can be made constant.
本発明の一実施形態による微粉炭供給装置を用いた石炭火力発電設備の一例による構成を示す概略図である。It is the schematic which shows the structure by an example of the coal-fired-power-generation installation using the pulverized coal supply apparatus by one Embodiment of this invention. 本発明の一実施形態による微粉炭供給装置の構成を示す正面図である。It is a front view which shows the structure of the pulverized coal supply apparatus by one Embodiment of this invention.
 以下、図面を参照して本発明を実施するための形態を説明する。
 (石炭火力発電所の構成)
 最初に、本発明の一実施形態による微粉炭供給装置を用いた石炭火力発電設備の一例による構成を説明する。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
(Composition of coal-fired power plant)
First, a configuration according to an example of a coal-fired power plant using a pulverized coal supply device according to an embodiment of the present invention will be described.
 図1は、本発明の一実施形態による微粉炭供給装置を用いた石炭火力発電設備の一例による構成を示す概略図である。図2は、本発明の一実施形態による微粉炭供給装置の構成を示す正面図である。 FIG. 1 is a schematic view showing a configuration of an example of a coal-fired power plant using a pulverized coal supply apparatus according to an embodiment of the present invention. FIG. 2 is a front view showing the configuration of a pulverized coal supply device according to an embodiment of the present invention.
 図1を参照すると、本発明の一例による石炭火力発電設備100は、微粉炭供給装置10とボイラ20を備えている。又、石炭火力発電設備100は、蒸気タービン30と復水器40を備えている。 Referring to FIG. 1, a coal-fired power plant 100 according to an example of the present invention includes a pulverized coal supply device 10 and a boiler 20. The coal-fired power plant 100 further includes a steam turbine 30 and a condenser 40.
 図1又は図2を参照すると、微粉炭供給装置10は、石炭バンカー11と給炭機12を備えている。又、微粉炭供給装置10は、溶出防止剤添加装置13と石炭微粉砕機14を備えている。 Referring to FIG. 1 or 2, the pulverized coal supply device 10 includes a coal bunker 11 and a coal feeder 12. The pulverized coal feeding device 10 further includes an elution inhibitor adding device 13 and a coal pulverizer 14.
 図1又は図2を参照すると、石炭バンカー11には、図示しない貯炭場から防塵カバー付きのコンベア15によって塊状の石炭Cが搬送される。そして、石炭バンカー11には、塊状の石炭Cが一時的に貯留されている。石炭バンカー11に貯留された石炭Cは、給炭機12に供給される。 Referring to FIG. 1 or 2, bulk coal C is conveyed to a coal bunker 11 by a conveyor 15 with a dustproof cover from a coal storage station (not shown). Then, massive coal C is temporarily stored in the coal bunker 11. Coal C stored in the coal bunker 11 is supplied to the coal feeder 12.
 図2を参照すると、給炭機12は、搬送コンベア12cを内部に備えている。搬送コンベア12cは、石炭バンカー11から供給された石炭Cを一方の端部から他方の端部に搬送できる。石炭微粉砕機14は、給炭機12の他方の端部から投入された石炭Cを粉砕して微粉炭を生成できる。 Referring to FIG. 2, the coal feeder 12 internally includes a transport conveyor 12 c. The transport conveyor 12 c can transport the coal C supplied from the coal bunker 11 from one end to the other end. The coal pulverizer 14 can pulverize the coal C fed from the other end of the coal feeder 12 to produce pulverized coal.
 図1を参照すると、ボイラ20は、石炭微粉砕機14で生成した微粉炭を燃料とする燃焼室2rを内部に有している。図1に示した例では、燃焼室2rには、送油管(図示せず)を介して石油が送られている。そして、燃焼室2rでは、石油を燃焼すると共に、微粉炭を燃焼できる。又、燃焼室2rには、通風機によって燃焼用空気が送られている。このように、ボイラ20の燃焼室2rでは、二段燃焼が実施されている。この燃焼によって、給水ポンプ41から給水された水が加熱され過熱蒸気となって、この過熱蒸気がボイラ20から蒸気タービン30に送られる。 Referring to FIG. 1, the boiler 20 internally includes a combustion chamber 2 r fueled by pulverized coal produced by the coal pulverizer 14. In the example shown in FIG. 1, oil is sent to the combustion chamber 2 r via an oil feed pipe (not shown). And in the combustion chamber 2r, while burning oil, pulverized coal can be burned. Further, combustion air is sent to the combustion chamber 2r by a ventilator. Thus, in the combustion chamber 2r of the boiler 20, two-stage combustion is performed. By this combustion, the water supplied from the feed pump 41 is heated to become superheated steam, and the superheated steam is sent from the boiler 20 to the steam turbine 30.
 図1を参照すると、蒸気タービン30は、タービン(羽根車)を内部に備えている。タービンにその軸方向から過熱蒸気を送り込むと、タービンを回転できる。タービンの回転軸は、発電機31のロータに連結している。蒸気タービン30に過熱蒸気を送り込むと、発電機31のロータが回転することで、電力を供給できる。 Referring to FIG. 1, the steam turbine 30 internally includes a turbine (impeller). If the superheated steam is fed into the turbine from its axial direction, the turbine can be rotated. The rotating shaft of the turbine is connected to the rotor of the generator 31. When superheated steam is fed into the steam turbine 30, power can be supplied by the rotor of the generator 31 rotating.
 図1を参照すると、蒸気タービン30で運動エネルギーを消費した過熱蒸気は、復水器40で冷却して凝縮することで水に戻される。つまり、復水される。この復水は、補給水と共に、給水ポンプ41によってボイラ20へと循環される。 Referring to FIG. 1, the superheated steam that has consumed kinetic energy in the steam turbine 30 is returned to water by being cooled and condensed in the condenser 40. In other words, it is recovered. The condensed water is circulated to the boiler 20 by the feed water pump 41 together with the makeup water.
 このように、図1又は図2を参照すると、石炭火力発電設備100は、微粉炭を燃料としたボイラ20で水を加熱して過熱蒸気を発生し、過熱蒸気を蒸気タービン30に送り込むことで、発電機31で電力を供給できる。 Thus, referring to FIG. 1 or FIG. 2, the coal thermal power generation facility 100 heats water with the boiler 20 using pulverized coal as fuel to generate superheated steam, and sends the superheated steam to the steam turbine 30. Power can be supplied by the generator 31.
 [微粉炭供給装置の構成]
 次に、本発明の一実施形態による微粉炭供給装置10の構成を説明する。
[Composition of pulverized coal supply device]
Next, the configuration of the pulverized coal supply device 10 according to the embodiment of the present invention will be described.
 (石炭バンカー構成)
 最初に、実施形態による石炭バンカー11の構成を説明する。図2を参照すると、石炭バンカー11は、上面を開口した逆円錐形の本体11bと本体11bの底部から延びる給炭管11pで構成している。給炭管11pは、給炭機12の一方の端部に接続している。本体11bに貯留された塊状の石炭Cは、給炭管11pを介して、給炭機12の内部に投下できる。
(Coal bunker composition)
First, the configuration of the coal bunker 11 according to the embodiment will be described. Referring to FIG. 2, the coal bunker 11 is composed of an inverted conical main body 11 b whose top surface is opened and a coal feeding pipe 11 p extending from the bottom of the main body 11 b. The coal feed pipe 11 p is connected to one end of the coal feeder 12. Bulk coal C stored in the main body 11 b can be dumped into the inside of the coal feeder 12 through the coal feeding pipe 11 p.
 図2を参照すると、給炭管11pの途上には、コールゲート弁11cを配置している。コールゲート弁11cは、給炭管11pの管路を開閉できる弁体を内部に備えている。コールゲート弁11cは、第3モータ11mを連結している。 Referring to FIG. 2, a call gate valve 11c is disposed in the middle of the coal feeding pipe 11p. The call gate valve 11c is internally provided with a valve body capable of opening and closing the pipe line of the coal feeding pipe 11p. The call gate valve 11 c connects the third motor 11 m.
 図2を参照すると、コールゲート弁11cは、第3モータ11mの回転運動を弁体の進退運動に変換する変換機構(図示せず)を内部に備えている。第3モータ11mの出力軸を一方の方向に回転すると、給炭管11pの管路を開くことができる。第3モータ11mの出力軸を他方の方向に回転すると、給炭管11pの管路を閉じることができる。 Referring to FIG. 2, the call gate valve 11c is internally provided with a conversion mechanism (not shown) for converting the rotational movement of the third motor 11m into the forward and backward movement of the valve body. When the output shaft of the third motor 11m is rotated in one direction, the pipeline of the coal feeding pipe 11p can be opened. When the output shaft of the third motor 11m is rotated in the other direction, the pipeline of the coal feeding pipe 11p can be closed.
 図2を参照して、微粉炭供給装置10は、給炭管11pの管路を閉じた後、予め定めた第1の時間が経過すると、給炭機12を停止して、その後、更に第2の時間が経過すると石炭微粉砕機14を停止するように制御しているので、コールゲート弁11c以降の給炭通路中の石炭Cが給炭機12に供給されてしまい、コールゲート弁11c以降の給炭通路に石炭Cが滞留することがない。そのため、石炭微粉砕機14を長期間停止したとしても、給炭通路に石炭詰まりが生じることを防止できる。 Referring to FIG. 2, after the pulverized coal feeding device 10 closes the pipe line of the coal feeding pipe 11 p, when the first predetermined time elapses, the coal feeding machine 12 is stopped, and then, Since the coal pulverizer 14 is controlled to stop when the time of 2 elapses, the coal C in the coal feeding passage after the call gate valve 11 c is supplied to the coal feeder 12, and the coal gate valve 11 c Coal C does not stay in the subsequent coal feeding passage. Therefore, even if the coal pulverizer 14 is stopped for a long time, it is possible to prevent coal clogging in the coal feeding passage.
 (給炭機の構成)
 次に、実施形態による給炭機12の構成を説明する。図2を参照すると、給炭機12は、箱状のフレーム12fと搬送コンベア12cを備えている。フレーム12fは、石炭Cが排出される石炭投下口12sを他方の端部の下部に開口している。
(Configuration of the coal feeder)
Next, the configuration of the coal feeder 12 according to the embodiment will be described. Referring to FIG. 2, the coal feeder 12 includes a box-like frame 12 f and a conveyer 12 c. The frame 12 f opens the coal outlet 12 s from which the coal C is discharged at the bottom of the other end.
 図2を参照すると、実体として、石炭投下口12sは、フレーム12fと石炭微粉砕機14を接続する給炭管14pの入口開口である。石炭投下口12sに排出された石炭Cが石炭微粉砕機14に投入され、石炭微粉砕機14で塊状の石炭Cが粉砕されることで、微粉炭を生成できる。 Referring to FIG. 2, as a substance, the coal discharge port 12s is an inlet opening of a coal feeding pipe 14p connecting the frame 12f and the coal pulverizer 14. The coal C discharged to the coal injection port 12s is fed to the coal pulverizer 14 and pulverized coal C is pulverized by the coal pulverizer 14, whereby pulverized coal can be produced.
 図2を参照すると、搬送コンベア12cは、一組のローラ121・122と無端ベルト12vで構成している。一組のローラ121・122は、互いに離間して配置されている。無端ベルト12vは、一組のローラ121・122を巻き掛けしている。図2で示した例では、ローラ121を駆動輪とし、ローラ122を従動輪としている。 Referring to FIG. 2, the conveyer 12c is composed of a pair of rollers 121 and 122 and an endless belt 12v. The pair of rollers 121 and 122 are spaced apart from each other. The endless belt 12v winds a pair of rollers 121 and 122. In the example shown in FIG. 2, the roller 121 is a driving wheel, and the roller 122 is a driven wheel.
 図2を参照すると、駆動側のローラ121は、第1モータ12mを連結している。第1モータ12mを一方の方向に回転すると、無端ベルト12vの上側を一方の端部から他方の端部に向かって走行でき、石炭バンカー11から供給した石炭Cを石炭投下口12sに向かって搬送できる。又、第1モータ12mは、その回転速度を制御することで、石炭微粉砕機14に投入される石炭Cの単位時間当たりの投入量を調整できる。 Referring to FIG. 2, the drive side roller 121 couples the first motor 12 m. When the first motor 12m is rotated in one direction, the upper side of the endless belt 12v can travel from one end to the other end, and the coal C supplied from the coal bunker 11 is conveyed toward the coal discharge port 12s it can. Moreover, the 1st motor 12m can adjust the input quantity per unit time of the coal C introduce | transduced into the coal pulverizer 14 by controlling the rotational speed.
 (溶出防止剤添加装置の構成)
 次に、実施形態による溶出防止剤添加装置13の構成を説明する。図2を参照すると、溶出防止剤添加装置13は、上面を開口した逆円錐形のホッパー13hとスクリューフィーダ13fを備えている。ホッパー13hは、溶出防止剤Eaを貯留している。溶出防止剤Eaは、石炭の燃焼残渣から有害微量元素の溶出を抑制できる。
(Configuration of elution inhibitor addition device)
Next, the configuration of the elution inhibitor adding apparatus 13 according to the embodiment will be described. Referring to FIG. 2, the anti-elution agent addition device 13 includes an inverted conical hopper 13 h having an open top and a screw feeder 13 f. The hopper 13h stores the elution inhibitor Ea. The elution inhibitor Ea can suppress the elution of harmful trace elements from the combustion residue of coal.
 図2を参照すると、ホッパー13hとスクリューフィーダ13fの間には、ゲート弁13vを設けている。ゲート弁13vは、ホッパー13hからスクリューフィーダ13fに至る管路を開閉できる。ハンドルを操作することで、ホッパー13hからスクリューフィーダ13fに至る管路を開閉できる。 Referring to FIG. 2, a gate valve 13v is provided between the hopper 13h and the screw feeder 13f. The gate valve 13v can open and close a pipeline from the hopper 13h to the screw feeder 13f. By operating the handle, the pipeline from the hopper 13 h to the screw feeder 13 f can be opened and closed.
 図2を参照すると、スクリューフィーダ13fは、ホッパー13hから供給された溶出防止剤Eaをフレーム12fの石炭投下口12sに向かって送り出すことができる。スクリューフィーダ13fは、第2モータ13mを連結している。 Referring to FIG. 2, the screw feeder 13 f can send out the elution inhibitor Ea supplied from the hopper 13 h toward the coal discharge port 12 s of the frame 12 f. The screw feeder 13f connects the second motor 13m.
 図2を参照して、第2モータ13mを回転すると、螺旋状のスクリュー13sを回転させて、溶出防止剤Eaを軸方向に送り出すことができる、又、第2モータ13mは、その回転速度を制御することで、石炭投下口12sを介して、石炭微粉砕機14に投入される溶出防止剤Eaの単位時間当たりの投入量を調整できる。 With reference to FIG. 2, when the second motor 13m is rotated, the spiral screw 13s can be rotated to send out the elution inhibitor Ea in the axial direction. By controlling, it is possible to adjust the input amount per unit time of the elution inhibitor Ea input to the coal pulverizer 14 through the coal discharge port 12s.
 図2を参照して、第1モータ12mの回転速度に対応して、すなわち、石炭微粉砕機14に投入される石炭Cの単位時間当たりの投入量に対応して、第2モータ13mの回転速度を調整することで、溶出防止剤Eaの添加量を適正な割合で調整できる。 Referring to FIG. 2, the rotation of the second motor 13m corresponds to the rotational speed of the first motor 12m, that is, corresponding to the input amount of coal C input to the coal pulverizer 14 per unit time. By adjusting the speed, the amount of the elution inhibitor Ea can be adjusted at an appropriate rate.
 [微粉炭供給装置の作用]
 次に、実施形態による微粉炭供給装置10の作用及び効果を説明する。
[Operation of pulverized coal supply device]
Next, the operation and effects of the pulverized coal supply device 10 according to the embodiment will be described.
 図1又は図2を参照すると、微粉炭供給装置10は、搬送コンベア12cの端部に形成し、石炭が排出される石炭投下口12sの上方に、スクリューフィーダ13f付きのホッパー13hを配置し、ホッパー13hに有害微量元素の溶出防止剤Eaを貯留し、スクリューフィーダ13fを駆動してホッパー13hから石炭投下口12sに向けて、有害微量元素の溶出防止剤Eaを供給することで、石炭と有害微量元素の溶出防止剤Eaの混合比を一定にできる。 Referring to FIG. 1 or 2, the pulverized coal feeding device 10 is formed at the end of the conveyer 12c, and places a hopper 13h with a screw feeder 13f above the coal discharge opening 12s from which coal is discharged, Disposal agent Ea of harmful trace elements is stored in hopper 13h, and screw feeder 13f is driven to feed elution stop agent Ea of harmful trace elements from hopper 13h to coal injection port 12s, thereby causing harmful effects to coal and harmful substances. The mixing ratio of the elution inhibitor Ea of trace element can be made constant.
 図2を参照すると、給炭機12は、搬送コンベア12cを駆動する第1モータ12mを備えている。又、溶出防止剤添加装置13は、スクリューフィーダ13fを駆動する第2モータ13mを備えている。第1モータ12mの回転速度に対応して、すなわち、石炭微粉砕機14に投入される石炭Cの単位時間当たりの投入量に対応して、第2モータ13mの回転速度を調整することで、溶出防止剤Eaの添加量を適正な割合で調整できる。 Referring to FIG. 2, the coal feeder 12 includes a first motor 12 m that drives the transfer conveyor 12 c. Further, the elution inhibitor adding device 13 is provided with a second motor 13m that drives the screw feeder 13f. By adjusting the rotational speed of the second motor 13m, corresponding to the rotational speed of the first motor 12m, that is, corresponding to the input amount of coal C input to the coal pulverizer 14 per unit time, The amount of elution inhibitor Ea can be adjusted at an appropriate rate.
 図2を参照して、溶出防止剤Eaは、石灰石、消灰石、生石灰からなる群より選択される1種以上を含んでいる。溶出防止剤Eaは、粒状体又は粉末状体からなることが好ましい。溶出防止剤Eaの平均粒径は、200μmを超えないことが好ましい。微粉炭と溶出防止剤Eaを混合してボイラ20に送出することが可能になる。 Referring to FIG. 2, the elution inhibitor Ea contains one or more selected from the group consisting of limestone, limestone and quicklime. The elution inhibitor Ea is preferably in the form of granules or powder. The average particle size of the elution inhibitor Ea preferably does not exceed 200 μm. The pulverized coal and the elution inhibitor Ea can be mixed and delivered to the boiler 20.
 図1又は図2を参照して、石炭微粉砕機14は、遠心力を利用した分級装置、いわゆる、乾式サイクロンを内部に備えることが好ましい。石炭微粉砕機14で粉砕した微粉炭及び溶出防止剤Eaを所定の粒径に分級した後に、これらの微粉炭及び溶出防止剤Eaをボイラ20に送出することが可能になる。 With reference to FIG. 1 or 2, it is preferable that the coal pulverizer 14 be internally provided with a classifier utilizing centrifugal force, so-called dry cyclone. After classifying the pulverized coal and the elution inhibitor Ea pulverized by the coal pulverizer 14 into predetermined particle sizes, it is possible to deliver the pulverized coal and the elution inhibitor Ea to the boiler 20.
 図2を参照して、溶出防止剤Eaを給炭機12に供給する手段は、スクリューフィーダ13fに限定されない。紛体輸送に適した輸送手段であれば、供給手段となるフィーダ又はコンベアの種類は、限定されない。 Referring to FIG. 2, the means for supplying elution inhibitor Ea to coal feeder 12 is not limited to screw feeder 13f. The type of feeder or conveyor serving as the supplying means is not limited as long as the transportation means is suitable for powder transportation.
 図2を参照して、溶出防止剤Eaは、搬送コンベア12c上に投下してもよく、石炭微粉砕機14の上方から、有害微量元素の溶出を抑制する溶出防止剤Eaを石炭微粉砕機14に投下することで、石炭に対して溶出防止剤Eaの添加量を適正な割合で調整できる。 Referring to FIG. 2, the elution inhibitor Ea may be dropped onto the conveyer 12c, and the elution inhibitor Ea for suppressing elution of harmful trace elements from above the coal pulverizer 14 is pulverized by a coal pulverizer. By dropping it to 14, the addition amount of the elution inhibitor Ea can be adjusted at an appropriate ratio with respect to the coal.
 本発明による微粉炭供給装置は、給炭機への石炭と溶出防止剤の注入手段を別々に設けることで、搬送コンベアを駆動する第1モータの回転速度に対応して、溶出防止剤の添加量を調整できる。 The pulverized coal supply apparatus according to the present invention adds the elution inhibitor to the feed speed of the first motor for driving the conveyer by separately providing the means for injecting coal and the elution inhibitor into the feeder. You can adjust the amount.
 本発明による有害微量元素溶出抑制方法は、石炭を石炭バンカーに搬送するコンベア上で石炭と溶出防止剤を混合することなく、石炭微粉砕機の上流側で石炭と溶出防止剤を別々に供給できるので、石炭に対する溶出防止剤の添加量を調整できる。 The harmful trace element elution suppression method according to the present invention can separately supply the coal and the elution inhibitor upstream of the coal pulverizer without mixing the coal and the elution inhibitor on the conveyor for conveying the coal to the coal bunker. Therefore, the amount of elution inhibitor added to coal can be adjusted.
 本発明による微粉炭供給装置は、次のような効果が期待できる。
 (1)微粉炭と混合して適正配合の溶出防止剤をボイラに送り込んで、高温で燃焼するので、石炭灰へ有害微量元素の取り込みを促進できる。
 (2)微粉炭と混合して適正配合の溶出防止剤をボイラに送り込んで、高温で燃焼するので、排ガスから脱硫装置に流入する有害微量元素を抑制できる。
The pulverized coal supply device according to the present invention can be expected to have the following effects.
(1) By mixing with pulverized coal and feeding the elution inhibitor of the proper composition to the boiler and burning it at a high temperature, it is possible to accelerate the uptake of harmful trace elements into the coal ash.
(2) Since the elution inhibitor mixed with pulverized coal is fed into the boiler and burned at a high temperature, harmful trace elements flowing from the exhaust gas into the desulfurization apparatus can be suppressed.
 10 微粉炭供給装置
 11 石炭バンカー
 12 給炭機
 12c 搬送コンベア
 12f フレーム
 12s 石炭投下口
 13 溶出防止剤添加装置
 14 石炭微粉砕機
 C 石炭
 Ea 溶出防止剤
DESCRIPTION OF SYMBOLS 10 pulverized coal supply apparatus 11 coal bunker 12 coal feeding machine 12c conveyer 12f flame | frame 12s coal pouring opening 13 elution inhibiting agent addition apparatus 14 coal pulverizer C coal Ea elution inhibiting agent

Claims (7)

  1.  石炭を貯留した石炭バンカー、前記石炭バンカーから供給された石炭を一方の端部から他方の端部に搬送する搬送コンベアを内部に有する給炭機、及び、前記給炭機の他方の端部から投入された石炭を粉砕して微粉炭を生成する石炭微粉砕機を備えた微粉炭供給装置であって、
     前記給炭機は、
     石炭が排出される石炭投下口を他方の端部の下部に開口した箱状のフレームと、
     前記フレームの石炭投下口に向かって、石炭の燃焼残渣から有害微量元素の溶出を抑制する溶出防止剤を投下自在な溶出防止剤添加装置と、を備えている、微粉炭供給装置。
    From the other end of the coal bunker which stored the coal bunker which stored coal, the conveyance conveyer which conveys the coal supplied from the coal bunker from one end to the other end, and the other side of the coal feeder A pulverized coal feeding apparatus comprising a coal pulverizer for pulverizing input coal to form pulverized coal,
    The coal feeder is
    A box-like frame that opens at the lower end of the other end of the coal outlet from which the coal is discharged;
    A pulverized coal feeding apparatus, comprising: an elution inhibitor addition device capable of pouring an elution inhibitor that suppresses elution of harmful trace elements from combustion residue of coal toward a coal injection port of the frame.
  2.  前記溶出防止剤添加装置は、
     前記溶出防止剤を貯留したホッパーと、
     前記ホッパーから供給された前記溶出防止剤を前記フレームの石炭投下口に向かって送り出すスクリューフィーダと、を備えている、請求項1記載の微粉炭供給装置。
    The elution inhibitor addition device is
    A hopper storing the elution inhibitor,
    The pulverized coal feeder according to claim 1, further comprising: a screw feeder for feeding out the elution inhibitor supplied from the hopper toward a coal discharge port of the frame.
  3.  前記給炭機は、前記搬送コンベアを駆動する第1モータを備え、
     前記溶出防止剤添加装置は、前記スクリューフィーダを駆動する第2モータを備え、
     前記第1モータの回転速度に対応して、前記第2モータの回転速度を調整している、請求項2記載の微粉炭供給装置。
    The coal feeder comprises a first motor for driving the transport conveyor,
    The elution inhibitor addition device comprises a second motor for driving the screw feeder,
    The pulverized coal feeding device according to claim 2, wherein the rotational speed of the second motor is adjusted according to the rotational speed of the first motor.
  4.  前記溶出防止剤は、石灰石、消灰石、生石灰からなる群より選択される1種以上を含んでいる、請求項1から3のいずれかに記載の微粉炭供給装置。 The pulverized coal supply device according to any one of claims 1 to 3, wherein the elution inhibitor contains one or more selected from the group consisting of limestone, limestone and quicklime.
  5.  前記溶出防止剤は、粒状体又は粉末状体からなる、請求項4記載の微粉炭供給装置。 The pulverized coal feeding device according to claim 4, wherein the elution inhibitor is in the form of particles or powder.
  6.  微粉炭供給装置を備える石炭火力発電設備における有害微量元素溶出抑制方法であって、
     前記微粉炭供給装置は、
     石炭を搬送する搬送コンベアと、
     前記搬送コンベアの下流側の端部の下方に配置され、石炭を粉砕して微粉炭を生成する石炭微粉砕機と、を備え、
     前記搬送コンベア又は前記石炭微粉砕機の上方から、有害微量元素の溶出を抑制する溶出防止剤を前記石炭微粉砕機に投下する、有害微量元素溶出抑制方法。
    A method for suppressing harmful trace element elution in a coal-fired thermal power plant equipped with a pulverized coal supply device, comprising:
    The pulverized coal supply device
    A conveyer that conveys coal;
    And a coal pulverizer, which is disposed below the downstream end of the transport conveyor and crushes coal to produce pulverized coal.
    The harmful trace element elution suppression method which drops the elution inhibiting agent which suppresses elution of harmful trace element from the upper part of the said conveyance conveyor or the said coal pulverizer to the said coal pulverizer.
  7.  前記搬送コンベアを駆動する第1モータの回転速度に対応して、前記溶出防止剤を前記石炭微粉砕機に向かって送り出すスクリューフィーダを駆動する第2モータの回転速度を調整している、請求項6記載の有害微量元素溶出抑制方法。 The rotational speed of a second motor for driving a screw feeder that feeds the elution inhibitor toward the coal pulverizer is adjusted in accordance with the rotational speed of a first motor for driving the transport conveyor. The harmful | toxic trace element elution suppression method of 6 statement.
PCT/JP2017/043122 2017-11-30 2017-11-30 Powdered coal supply device and toxic trace element elution suppression method WO2019106796A1 (en)

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