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WO2018150510A1 - Procédé d'inhibition de scorification et système de production d'énergie au charbon - Google Patents

Procédé d'inhibition de scorification et système de production d'énergie au charbon Download PDF

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Publication number
WO2018150510A1
WO2018150510A1 PCT/JP2017/005691 JP2017005691W WO2018150510A1 WO 2018150510 A1 WO2018150510 A1 WO 2018150510A1 JP 2017005691 W JP2017005691 W JP 2017005691W WO 2018150510 A1 WO2018150510 A1 WO 2018150510A1
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Prior art keywords
slagging
coal
inhibitor
pulverized coal
combustion
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Application number
PCT/JP2017/005691
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English (en)
Japanese (ja)
Inventor
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 JP2017549351A priority Critical patent/JP6304459B1/ja
Priority to PCT/JP2017/005691 priority patent/WO2018150510A1/fr
Publication of WO2018150510A1 publication Critical patent/WO2018150510A1/fr

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J7/00—Arrangement of devices for supplying chemicals to fire

Definitions

  • the present invention relates to a slugging suppression method and a coal-fired power generation system.
  • ash melting point When an elution inhibitor made of a calcium-containing material is introduced into a combustion boiler, the melting temperature of coal ash (hereinafter also referred to as “ash melting point”) is lowered, so that slagging is likely to occur in the combustion boiler.
  • an object of the present invention is to provide a slagging suppression method and a coal thermal power generation system that can suppress the occurrence of slagging in a combustion boiler while suppressing the elution of trace elements from coal ash.
  • a pulverized coal machine that pulverizes coal to produce pulverized coal, and a combustion boiler that combusts the pulverized coal produced by the pulverized coal machine with primary air and secondary air supplied to the subsequent stage of the primary air;
  • a slagging suppression method in a coal-fired power generation system comprising: a slagging inhibitor for suppressing slagging in the combustion boiler, wherein a slagging inhibitor is disposed at 825 ° C. after coal combustion in the combustion boiler from 825 ° C.
  • Slagging suppression method for supplying to the region up to the melting point temperature.
  • a pulverized coal machine that pulverizes coal to produce pulverized coal, and a combustion boiler that combusts the pulverized coal produced by the pulverized coal machine with primary air and secondary air that is supplied after the primary air;
  • the slagging inhibitor that suppresses slagging in the combustion boiler is applied to a region from 825 ° C. to the coal ash melting point temperature after the combustion location of the pulverized coal in the combustion boiler.
  • a coal-fired power generation system including a slagging inhibitor supply unit for supplying.
  • the slagging inhibitor supply unit supplies the slagging inhibitor to a flow path for mixing a part of exhaust gas generated by combustion of pulverized coal with secondary air.
  • the slagging inhibitor supply unit supplies the slagging inhibitor to a flow path for mixing a part of exhaust gas generated by combustion of pulverized coal with secondary air.
  • the slagging inhibitor supply unit is downstream of a gas recirculation ventilator provided in a flow path for mixing part of the exhaust gas generated by the combustion of pulverized coal with secondary air.
  • the coal-fired power generation system according to any one of (8) to (14), which is supplied to the side.
  • the generation of slagging in the combustion boiler can be suppressed while suppressing the elution of trace elements from the coal ash.
  • FIG. 1 is a schematic configuration diagram showing a pulverized coal combustion facility 1 in a coal thermal power generation system.
  • the coal-fired power generation system includes a pulverized coal combustion facility 1 shown in FIG. 1, a steam turbine (not shown), a generator, and the like.
  • a pulverized coal combustion section 16 described later, heat generated during the combustion of the pulverized coal is converted into steam. When the steam turbine is rotated by this steam, power is generated by the generator.
  • nitrogen oxide (NOx), soot, sulfur oxide (SOx), etc. generated during the combustion of the pulverized coal are removed by a denitration device 181, a dust collector 182 and a desulfurization device (not shown) in the subsequent stage. Discharged from the chimney.
  • NOx nitrogen oxide
  • SOx sulfur oxide
  • the pulverized coal combustion facility 1 includes a coal supply unit 12, a pulverized coal generation unit 14, a pulverized coal combustion unit (combustion boiler) 16, a coal ash treatment unit 18, and a slagging inhibitor supply unit. 20.
  • the coal supply unit 12 supplies coal to the pulverized coal generation unit 14.
  • the pulverized coal generation unit 14 converts the coal supplied from the coal supply unit 12 to pulverized coal.
  • the pulverized coal combustion unit 16 burns pulverized coal.
  • the coal ash processing unit 18 processes coal ash generated by the combustion of pulverized coal.
  • the slagging inhibitor supply unit 20 supplies the slagging inhibitor to the pulverized coal combustion unit 16.
  • the coal supply unit 12 includes a coal bunker 121 and a coal feeder 122.
  • the coal bunker 121 stores coal to be supplied to the coal feeder 122.
  • the coal feeder 122 continuously supplies the coal supplied from the coal bunker 121 to a pulverized coal machine 141 (described later).
  • the coal feeder 122 includes a device (not shown) that adjusts the amount of coal supplied.
  • the coal feeder 122 can adjust the amount of coal supplied to the pulverized coal machine 141.
  • the coal supply unit 12 includes a coal gate (not shown) at the boundary between the coal bunker 121 and the coal feeder 122. The coal gate prevents air from the coal feeder 122 from flowing into the coal bunker 121.
  • the pulverized coal generation unit 14 includes a pulverized coal machine (mill) 141 and an air supply unit 142 that supplies air to the pulverized coal machine 141.
  • the pulverized coal machine 141 pulverizes the coal supplied from the coal feeder 122 through the coal supply pipe to a fine particle size to produce pulverized coal.
  • the pulverized coal machine 141 mixes the pulverized coal with the air supplied from the air supply unit 142. Since the pulverized coal is preheated and dried by mixing with air, it easily burns in the furnace 161 (described later).
  • the pulverized coal is supplied to the pulverized coal combustion unit 16 by blowing air.
  • the types of the pulverized coal machine 141 include a roller mill, a tube mill, a ball mill, a beater mill, an impeller mill, and the like, but are not limited to these and may be any mill used in pulverized coal combustion.
  • Pulverized coal combustion unit 16 includes a furnace 161, a heater 162 (heat exchange unit), and an air supply unit 163.
  • the furnace 161 combusts the pulverized coal supplied from the pulverized coal machine 141 together with the air and exhaust gas supplied from the air supply unit 163.
  • the heater 162 heat exchange unit
  • the air supply unit 163 supplies combustion air (primary air and secondary air) to the furnace 161.
  • coal ash (coal combustion residue) is generated. Due to the generation of coal ash, the phenomenon called slagging and fouling described above occurs.
  • Slagging is a phenomenon in which molten ash particles adhere to and accumulate near the burner, boiler suspension pipe, furnace wall, water-cooled wall pipe, and the like, causing problems such as closing of the gas flow path.
  • fouling is a phenomenon in which the sulfuric acid compound that has become vapor adheres to the surface of the heat transfer tube, and an adhesion layer of combustion ash is formed thereon, which causes problems such as corrosion of the heat transfer tube. Slagging and fouling are likely to occur when the ash melting point is lowered.
  • the pulverized coal combustion unit 16 supplies the air necessary for complete combustion of the pulverized coal in two places, ie, a burner 61 and an air supply port 62 provided in the upper part of the burner. It is composed of a stage combustion method.
  • the burner 61 is supplied with pulverized coal together with primary air and exhaust gas. Secondary air is supplied to the air supply port 62 together with the exhaust gas.
  • the exhaust gas supplied to the burner 61 and the air supply port 62 is obtained by recirculating part of the exhaust gas discharged from the pulverized coal combustion unit 16.
  • the pulverized coal combustion unit 16 when the air (oxygen) supplied to the burner 61 is large, the combustion temperature becomes high, and a large amount of nitrogen oxide (NOx) is generated together with coal ash. Therefore, by adjusting the distribution amount of the primary air and the exhaust gas supplied to the burner 61 and burning the pulverized coal in a state where oxygen is insufficient, the generation of nitrogen oxides can be suppressed. Further, by adjusting the distribution amount of the secondary air and exhaust gas supplied to the air supply port 62 and increasing oxygen, the combustion reaction can be further promoted between the air supply port 62 and the furnace outlet.
  • the air (oxygen) supplied to the burner 61 when the air (oxygen) supplied to the burner 61 is large, the combustion temperature becomes high, and a large amount of nitrogen oxide (NOx) is generated together with coal ash. Therefore, by adjusting the distribution amount of the primary air and the exhaust gas supplied to the burner 61 and burning the pulverized coal in a state where oxygen is insufficient, the generation of nitrogen oxides can be suppress
  • coal ash is generated. Further, together with coal ash, exhaust gases such as sulfur oxide (SOx) such as sulfur dioxide (SO 2 ) and sulfur trioxide (SO 3 ) and nitrogen oxide (NOx) are generated. These coal ash and exhaust gas are discharged to the coal ash treatment unit 18.
  • SOx sulfur oxide
  • SO 2 sulfur dioxide
  • SO 3 sulfur trioxide
  • NOx nitrogen oxide
  • the coal ash treatment unit 18 includes a denitration device 181, a dust collector 182, and a coal ash collection silo 183.
  • the denitration device 181 removes nitrogen oxides in the exhaust gas discharged from the pulverized coal combustion unit 16.
  • ammonia gas is injected as a reducing agent into a relatively high temperature (300 to 400 ° C.) exhaust gas, and nitrogen oxides in the exhaust gas are decomposed into harmless nitrogen and water vapor by the action of the denitration catalyst.
  • a so-called dry ammonia catalytic reduction method is preferably used.
  • the dust collector 182 collects coal ash (dust) in the exhaust gas with an electrode.
  • the dust collectors 182 are preferably provided in a plurality of stages.
  • Coal ash collected by the dust collector 182 is temporarily stored in the coal ash recovery silo 183.
  • the exhaust gas from which the coal ash has been removed is discharged from the chimney after the sulfur oxide is removed by a desulfurization apparatus (not shown).
  • the coal ash collection silo 183 temporarily stores the coal ash collected by the dust collector 182.
  • the slagging inhibitor supply unit 20 supplies the slagging inhibitor to the pulverized coal combustion unit 16.
  • the slagging inhibitor supply unit 20 supplies the slagging inhibitor to the region of the furnace 161 from 825 ° C. to the coal ash melting point temperature.
  • the “coal ash melting point temperature” is generally a temperature between 1220 ° C. and 1600 ° C., although it varies depending on the coal type of coal.
  • the region where the slagging inhibitor is normally supplied is the narrowest region depending on the coal type of coal, the region from 825 ° C to 1220 ° C of the furnace 161, and the widest region of 825 ° C of the furnace 161. To 1600 ° C. The position where the slagging inhibitor is supplied will be described later.
  • the slagging inhibitor is an alkaline earth metal compound, for example, a calcium-containing material such as calcium carbonate (CaCO 3 ). In this embodiment, an example in which limestone is used as a slagging inhibitor will be described.
  • the slagging inhibitor is preferably granular or powdery.
  • the average particle size of the slagging inhibitor is preferably 10 ⁇ m to 100 ⁇ m, and more preferably 10 ⁇ m to 70 ⁇ m.
  • the slagging suppression method according to the present invention includes a pulverized coal machine that pulverizes coal to produce pulverized coal, and secondary air that supplies the pulverized coal produced by the pulverized coal machine to primary air and a subsequent stage of the primary air. And a slagging suppression method in a coal-fired power generation system provided with a combustion boiler, wherein a slagging inhibitor for suppressing slagging in the combustion boiler is a region from 825 ° C. to a coal ash melting point temperature in the combustion boiler. It is characterized by supplying to.
  • the slugging suppression method according to the present invention will be described using the pulverized coal combustion facility 1 described above.
  • the slagging suppression method includes a coal supply step S10 for supplying coal, a pulverized coal generation step S20 for pulverizing the supplied coal to generate pulverized coal, and a pulverized coal combustion step S30 for burning the pulverized coal. And a coal ash treatment step S40 for treating coal ash generated by the combustion of pulverized coal, and a slagging inhibitor supply step S50 for supplying a slagging inhibitor.
  • each process from coal supply process S10 to coal ash treatment process S40 is performed in coal supply part 12, pulverized coal generation part 14, pulverized coal combustion part 16, and coal ash treatment part 18 of pulverized coal combustion facility 1, respectively. Is called.
  • slagging inhibitor supply process S50 is performed by pulverized coal combustion process S30 mentioned above.
  • ⁇ Coal supply process S10> First, in the coal supply step S ⁇ b> 10, the coal stored in the coal bunker 121 is supplied to the pulverized coal machine 141 by the coal feeder 122.
  • the coal supplied to the pulverized coal machine 141 is specifically bituminous coal, subbituminous coal, lignite, etc., but is not limited to these coals, and may be any coal that can perform pulverized coal combustion. .
  • pulverized coal production process S20> the coal supplied from the coal feeder 122 is pulverized by the pulverized coal machine 141 to produce pulverized coal.
  • the produced pulverized coal is supplied to the furnace 161.
  • the average particle size of the pulverized coal may be in the particle size range generally used in pulverized coal combustion, and is generally a pulverization degree of 74 ⁇ m or less and 80 wt% or more.
  • the pulverized coal generated by the pulverized coal machine 141 is burned by the furnace 161.
  • the pulverized coal burns in the vicinity of a burner zone 161a (described later) in the furnace 161, and the furnace temperature at this time reaches 1300 ° C to 1500 ° C.
  • the coal ash produced by the combustion rises along the direction of the arrow and is sent to the denitration device 181 (coal ash treatment unit 18) together with the exhaust gas.
  • the furnace temperature in the vicinity of the upper part of the burner zone 161a is from 825 ° C. to the coal ash melting temperature.
  • a slagging inhibitor supply step S50 which is a step of supplying a slagging inhibitor, which is a feature of the present invention, is performed in a pulverized coal combustion step S30 as shown in FIG. 1 (S51 in FIG. 1).
  • a pulverized coal combustion step S30 as shown in FIG. 1 (S51 in FIG. 1).
  • the supply of the slagging inhibitor performed in the pulverized coal combustion step S30 will be described.
  • FIG. 2 is a diagram showing a configuration of the furnace 161 and its surroundings in the pulverized coal combustion facility 1.
  • a burner 61 is provided below the furnace 161.
  • the burner 61 is supplied with pulverized coal 200 supplied from the pulverized coal machine 141 (see FIG. 1), primary air 201 supplied from the air supply unit 163, and recirculated exhaust gas 203.
  • the pulverized coal 200 burns in the furnace 161 mainly in the burner zone 161a.
  • An air supply port 62 is provided in the upper part of the burner 61.
  • the air supply port 62 is supplied with the secondary air 202 supplied from the air supply machine 163 and the recirculated exhaust gas 203.
  • the combustion reaction of the pulverized coal that has not been burned in the vicinity of the burner zone 161a is promoted, and the pulverized coal can be completely burned.
  • the exhaust gas 203 (combustion gas) generated by the combustion of pulverized coal is discharged together with the coal ash from the furnace outlet 161b to the subsequent denitration device 181 (the coal ash treatment unit 18).
  • heat exchange units such as a superheater, a reheater, and a economizer are provided near the upper portion of the burner 61 and the furnace outlet 161b.
  • the pulverized coal combustion unit 16 recirculates a part of the exhaust gas 203 and supplies it to the burner 61 and the air supply port 62 as a gas recirculation ventilator 63, a dust collector 64,
  • the exhaust gas passage 100 is provided.
  • the gas recirculation ventilator 63 is a blower fan that takes in a part of the exhaust gas 203 discharged from the furnace outlet 161 b and sends it to the burner 61 and the air supply port 62.
  • the dust collector 64 is a device that collects coal ash (dust) contained in the exhaust gas 203. As the dust collector 64, for example, a mechanical dust collector can be used.
  • the exhaust gas passage 100 is an air duct that guides part of the exhaust gas 203 discharged from the furnace outlet 161 b to the burner 61 and the air supply port 62.
  • the exhaust gas passage 100 includes a first exhaust gas passage 110, a second exhaust gas passage 120, and a third exhaust gas passage 130.
  • the first exhaust gas passage 110 is a passage for taking out the exhaust gas 203 from the furnace outlet 161b side.
  • a gas recirculation ventilator 63 and a dust collector 64 are connected to the first exhaust gas passage 110.
  • the upstream end of the first exhaust gas passage 110 is connected to the furnace outlet 161b side.
  • the downstream end of the first exhaust gas passage 110 is connected to the exhaust gas inlet side of the dust collector 64.
  • the second exhaust gas passage 120 is a passage that guides the exhaust gas 203 to the burner 61.
  • the upstream end of the second exhaust gas passage 120 is connected to the exhaust gas outlet side of the dust collector 64.
  • the downstream end portion of the second exhaust gas passage 120 is connected to an exhaust gas introduction portion (not shown) of the burner 61.
  • the third exhaust gas passage 130 is a passage that guides the exhaust gas 203 to the air supply port 62.
  • the upstream end of the third exhaust gas passage 130 is connected to the exhaust gas outlet side of the dust collector 64 together with the upstream end of the second exhaust gas passage 120 described above.
  • the downstream end of the third exhaust gas passage 130 is connected to an exhaust gas introduction part (not shown) of the air supply port 62.
  • a slagging inhibitor passage 140 is connected to the third exhaust gas passage 130.
  • the slagging inhibitor passage 140 is a passage for supplying the slagging inhibitor 204 from the slagging inhibitor supply unit 20 to the third exhaust gas passage 130.
  • the slagging inhibitor 204 is intermittently supplied between the dust collector 64 and the air supply port 62 at a predetermined time interval.
  • the exhaust gas passage 100 including the third exhaust gas passage 130 functions as a flow channel for mixing a part of the exhaust gas 203 with the secondary air 202.
  • a blower fan that pushes the exhaust gas 203 downstream may be provided in the middle of the second exhaust gas passage 120 and the third exhaust gas passage 130.
  • a part of the exhaust gas 203 taken out from the furnace outlet 161 b side is guided to the dust collector 64 through the gas recirculation ventilator 63 by the first exhaust gas passage 110.
  • the exhaust gas 203 branches into the second exhaust gas passage 120 and the third exhaust gas passage 130 on the exhaust gas outlet side of the dust collector 64 and is guided to the burner 61 and the air supply port 62, respectively.
  • the exhaust gas 203 guided to the burner 61 is supplied from the burner 61 to the furnace 161 together with the pulverized coal 200 and the primary air 201.
  • the exhaust gas 203 guided to the air supply port 62 is supplied to the furnace 161 from the air supply port 62 together with the secondary air 202 and the slagging inhibitor 204.
  • the mechanism in which slagging is suppressed by introducing the slagging inhibitor 204 from the air supply port 62 into the furnace 161 in the region from 825 ° C. to the coal ash melting point temperature is as follows. Conceivable.
  • the slagging inhibitor 204 When calcium carbonate (CaCO 3 ), which is the slagging inhibitor 204, is supplied to the furnace 161 together with the secondary air 202, the slagging inhibitor 204 is introduced into the vicinity of the upper portion of the burner zone 161a from the air supply port 62. Since the furnace temperature in the vicinity is from 825 ° C. to the coal ash melting point temperature, CaCO 3 is decomposed into CaO and CO 2 . Although the decomposed CaO has a low melting point as a compound, the decomposed CaO has a melting point of about 2570 ° C., and therefore reacts with coal ash in the vicinity of the upper part of the burner zone 161a where the temperature is lower than that of the burner zone 161a. It becomes difficult. As described above, when the slagging inhibitor 204 is supplied from the air supply port 62 to the vicinity of the upper portion of the burner zone 161a, a large amount of CaO is present alone, so that the ash melting point is estimated to increase
  • the slagging inhibitor 204 intermittently at predetermined time intervals, the slagging generated in the vicinity of the burner, the boiler suspension pipe, the furnace wall, the water-cooled wall pipe, etc., as shown in FIG. A sandwich structure of a low melting point compound such as Fe, Ca, Si, Al, and Mg and a mass of CaO is obtained. As a result, slagging is easily peeled off at the interface between the low melting point compound and the CaO lump, thereby preventing the slagging from becoming enormous.
  • a low melting point compound such as Fe, Ca, Si, Al, and Mg and a mass of CaO
  • the ash melting point of the ash produced by separately adding in the vicinity was measured.
  • the amount of calcium carbonate added separately at around 950 ° C. was added so as to be the same amount (CaO: 3.1%) in terms of calcium in ash when “A charcoal and B charcoal” were burned. .
  • the measurement results are shown in Table 1.
  • the ash melting point of the ash produced by exclusively burning “A charcoal” was 1311 to 1364 ° C.
  • the ash melting point of the ash produced by burning only “B charcoal” was 1234 to 1301 ° C.
  • the ash melting point of the ash produced by burning “A coal + B coal” was 1235 to 1301 ° C., which was lower than the ash melting point of the ash produced by burning only “A coal”.
  • the ash melting point of the ash produced by burning “A charcoal” and adding calcium carbonate separately at around 950 ° C. is higher than the ash melting point of the ash produced by burning only “A charcoal”, It was 1323 to 1387 ° C.
  • the mechanism is considered as follows.
  • the decomposed CaO reacts with selenium oxide, arsenic trioxide, boron oxide, and the like, which are trace elements contained in coal ash, and is insoluble insoluble compounds such as calcium selenite, calcium arsenate, and calcium borate, respectively. Is generated. That is, trace elements are chemically captured by CaO to produce a hardly soluble insoluble compound.
  • the slagging inhibitor 204 into the furnace 161 in the region from 825 ° C. to the coal ash melting point, which is after the pulverized coal combustion location, the behavior of the trace elements contained in the coal ash is controlled, Elution of more trace elements can be suppressed.
  • the slagging inhibitor 204 is supplied to a region from 825 ° C. to the coal ash melting point temperature in the furnace 161, after the combustion location of the pulverized coal. Therefore, generation
  • the pulverized coal combustion facility 1 of the present embodiment can sufficiently suppress the elution of trace elements even for a coal type having a high content of trace elements, which has been difficult in the past, and therefore greatly increases the applicable coal types. be able to. Thereby, for example, the fuel cost cost can be reduced by using an inexpensive coal type having a high trace element content.
  • the present invention is not limited to this and may be supplied continuously.
  • the present invention is not limited to this and may be supplied continuously.
  • CaO islands are generated in places during the slagging mainly composed of a low melting point compound.
  • slagging since there is a boundary surface between CaO in a spherical shape with a small particle size and the low melting point compound, slagging has a structure that tends to collapse into a granular shape, thus preventing enlargement of slagging. It becomes possible.
  • the slagging inhibitor is supplied to the third exhaust gas passage 130 , but the present invention is not limited to this. If the slagging inhibitor can be supplied to the region from 825 ° C. to the coal ash melting point temperature in the furnace 161 after the pulverized coal combustion location, the position for supplying the slagging inhibitor can be appropriately selected.
  • the slagging inhibitor may be supplied from between the gas recirculation ventilator 63 and the dust collector 64 (the first exhaust gas passage 110).
  • the present invention is not limited to this. Moreover, you may supply a slagging inhibitor to the furnace 161 with a vapor

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Abstract

La présente invention concerne un procédé d'inhibition de scorification et un système de production d'énergie au charbon, pouvant inhiber la production de scorification à l'intérieur d'une chaudière à combustion et inhibant en même temps l'élution d'éléments trace en provenance des cendres de charbon. Ledit procédé d'inhibition de scorification, pour un système de production d'énergie au charbon muni d'un pulvérisateur de charbon (141) destiné à pulvériser du charbon afin de produire du charbon pulvérisé, et d'une chaudière à combustion (16) destinée à utiliser de l'air primaire et de l'air secondaire, alimenté à un étage ultérieur par rapport à l'air primaire, pour brûler le charbon pulvérisé produit par le pulvérisateur de charbon (141), consiste à alimenter un inhibiteur de scorification destiné à inhiber la scorification dans la chaudière de combustion (16) au niveau d'une région à une température comprise entre 825 °C et le point de fusion du charbon à l'intérieur de la chaudière à combustion (16), et au niveau d'un étage ultérieur par rapport à l'emplacement de combustion du charbon pulvérisé.
PCT/JP2017/005691 2017-02-16 2017-02-16 Procédé d'inhibition de scorification et système de production d'énergie au charbon WO2018150510A1 (fr)

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JP2017549351A JP6304459B1 (ja) 2017-02-16 2017-02-16 スラッギング抑制方法及び石炭火力発電システム
PCT/JP2017/005691 WO2018150510A1 (fr) 2017-02-16 2017-02-16 Procédé d'inhibition de scorification et système de production d'énergie au charbon

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113108297A (zh) * 2021-05-24 2021-07-13 西安热工研究院有限公司 一种对冲燃烧锅炉防渣剂的添加系统和方法

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114263926B (zh) * 2022-01-26 2024-04-02 西安热工研究院有限公司 一种防控高碱煤锅炉结渣沾污的系统和方法

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58182004A (ja) * 1982-04-20 1983-10-24 Ishikawajima Harima Heavy Ind Co Ltd 微粉炭の低窒素酸化物燃焼法
JPS6348392A (ja) * 1986-08-15 1988-03-01 Toa Netsuken Kk 石炭の排ガスダストのクリンカ−アツシユ抑制方法
US4960577A (en) * 1988-02-04 1990-10-02 Acurex Corporation Enhanced sorbent injection combined with natural gas reburning for a sox control for coal fired boilers
US5220875A (en) * 1992-04-15 1993-06-22 American Oxycarb Corporation Method of reducing sulfur dioxide content in flue gases
JP2005307117A (ja) * 2004-04-26 2005-11-04 Taiho Ind Co Ltd スラッギング防止用燃料添加剤及び燃料の燃焼方法
JP2008170110A (ja) * 2007-01-12 2008-07-24 Chugoku Electric Power Co Inc:The 有害微量元素溶出抑制剤添加量算出方法及びこれを用いた有害微量元素溶出抑制方法
US7430969B2 (en) * 2003-05-28 2008-10-07 Omni Materials, Inc. Method for reducing the amount of a sulfur dioxide in a flue gas resulting from the combustion of a fossil fuel
JP2012189295A (ja) * 2011-03-14 2012-10-04 Kurita Water Ind Ltd クリンカー防止剤
JP2014507620A (ja) * 2011-01-14 2014-03-27 エンバイロンメンタル・エナジー・サービシーズ・インコーポレイテッド 瀝青炭を用いて炉を運転するための方法およびそれによるスラグ生成を低減するための方法
JP2016020799A (ja) * 2014-06-18 2016-02-04 ナルコジャパン合同会社 クリンカをコントロールする方法

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10118450A (ja) * 1996-10-15 1998-05-12 Nippon Steel Corp 石炭焚きストーカ炉の脱硫方法

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58182004A (ja) * 1982-04-20 1983-10-24 Ishikawajima Harima Heavy Ind Co Ltd 微粉炭の低窒素酸化物燃焼法
JPS6348392A (ja) * 1986-08-15 1988-03-01 Toa Netsuken Kk 石炭の排ガスダストのクリンカ−アツシユ抑制方法
US4960577A (en) * 1988-02-04 1990-10-02 Acurex Corporation Enhanced sorbent injection combined with natural gas reburning for a sox control for coal fired boilers
US5220875A (en) * 1992-04-15 1993-06-22 American Oxycarb Corporation Method of reducing sulfur dioxide content in flue gases
US7430969B2 (en) * 2003-05-28 2008-10-07 Omni Materials, Inc. Method for reducing the amount of a sulfur dioxide in a flue gas resulting from the combustion of a fossil fuel
JP2005307117A (ja) * 2004-04-26 2005-11-04 Taiho Ind Co Ltd スラッギング防止用燃料添加剤及び燃料の燃焼方法
JP2008170110A (ja) * 2007-01-12 2008-07-24 Chugoku Electric Power Co Inc:The 有害微量元素溶出抑制剤添加量算出方法及びこれを用いた有害微量元素溶出抑制方法
JP2014507620A (ja) * 2011-01-14 2014-03-27 エンバイロンメンタル・エナジー・サービシーズ・インコーポレイテッド 瀝青炭を用いて炉を運転するための方法およびそれによるスラグ生成を低減するための方法
JP2012189295A (ja) * 2011-03-14 2012-10-04 Kurita Water Ind Ltd クリンカー防止剤
JP2016020799A (ja) * 2014-06-18 2016-02-04 ナルコジャパン合同会社 クリンカをコントロールする方法

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113108297A (zh) * 2021-05-24 2021-07-13 西安热工研究院有限公司 一种对冲燃烧锅炉防渣剂的添加系统和方法

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