JP5472848B2 - Combustion chamber temperature control device in waste melting furnace equipment - Google Patents
Combustion chamber temperature control device in waste melting furnace equipment Download PDFInfo
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- JP5472848B2 JP5472848B2 JP2009168000A JP2009168000A JP5472848B2 JP 5472848 B2 JP5472848 B2 JP 5472848B2 JP 2009168000 A JP2009168000 A JP 2009168000A JP 2009168000 A JP2009168000 A JP 2009168000A JP 5472848 B2 JP5472848 B2 JP 5472848B2
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- 238000002485 combustion reaction Methods 0.000 title claims description 44
- 230000008018 melting Effects 0.000 title claims description 35
- 238000002844 melting Methods 0.000 title claims description 35
- 239000002699 waste material Substances 0.000 title claims description 31
- 239000007789 gas Substances 0.000 claims description 23
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- 239000000567 combustion gas Substances 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims 1
- 238000010790 dilution Methods 0.000 description 6
- 239000012895 dilution Substances 0.000 description 6
- 239000000428 dust Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
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- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Description
本発明は、廃棄物を溶融処理する廃棄物溶融炉から発生する可燃ガス及び可燃残渣を燃焼させる燃焼室の温度を、廃棄物溶融炉に羽口から送風する送風量を調節して制御する、廃棄物溶融炉設備における燃焼室の温度制御に関する。 The present invention controls the temperature of the combustion chamber for burning the combustible gas and the combustible residue generated from the waste melting furnace for melting the waste by adjusting the amount of air blown from the tuyere to the waste melting furnace, The present invention relates to temperature control of a combustion chamber in a waste melting furnace facility.
一般廃棄物、産業廃棄物、シュレッダーダスト等の廃棄物をシャフト炉式廃棄物溶融炉で溶融処理する際に発生する可燃ガス及び可燃残渣(チャー)を含有する排ガスは、溶融炉の後段に設置されている燃焼室に導入して燃焼させ、排出される高温の燃焼排ガスはボイラーで熱回収が行われる(特許文献1、2参照)。 Exhaust gas containing combustible gas and combustible residue (char) generated when melting waste such as general waste, industrial waste, and shredder dust in a shaft furnace type waste melting furnace is installed at the latter stage of the melting furnace. The high-temperature combustion exhaust gas that is introduced into the combustion chamber and burned and discharged is recovered by a boiler (see Patent Documents 1 and 2).
廃棄物溶融炉に投入される廃棄物のごみ質は一定でなく変動するため、廃棄物溶融炉から排出される排ガス中の可燃ガスの成分やチャーの量などが変動する。例えば、自動車シュレッダーダスト(ASR)等のプラスチック含有廃棄物のような粒径が小さくかつプラスチック類が多く急速熱分解が起こりやすい廃棄物が廃棄物溶融炉に投入されて処理される場合、熱分解後の可燃ガス及びチャーが飛散して燃焼室に導入されて急激に燃焼室の温度が上昇する。燃焼室の温度が急上昇すると、後続のボイラーの蒸気量が急激に変動するために望ましくない。 Since the waste quality of the waste introduced into the waste melting furnace is not constant and fluctuates, the combustible gas components and the amount of char in the exhaust gas discharged from the waste melting furnace fluctuate. For example, when waste containing a small particle size, such as waste containing plastic such as automobile shredder dust (ASR), and containing a large amount of plastics, which is susceptible to rapid thermal decomposition, is put into a waste melting furnace and processed. Later combustible gas and char are scattered and introduced into the combustion chamber, and the temperature of the combustion chamber rises rapidly. A sudden rise in the temperature of the combustion chamber is undesirable because the amount of steam in subsequent boilers fluctuates rapidly.
従来、燃焼室の温度の急上昇時には燃焼室へ吹き込む希釈空気量を増調整して対応していた。しかしながら、可燃ガスやチャーを燃焼させるためのメインバーナの燃焼空気量の制御性限界もあって温度上昇を抑えることができない場合があった。さらに、最悪の場合には燃焼室内にてクリンカが生成して操業継続できなくなる事象も見られた。 Conventionally, when the temperature of the combustion chamber suddenly rises, the amount of diluted air blown into the combustion chamber is increased and dealt with. However, there is a case where the temperature rise cannot be suppressed due to the controllability limit of the combustion air amount of the main burner for burning the combustible gas or char. Furthermore, in the worst case, clinker was generated in the combustion chamber and the operation could not be continued.
そこで、本発明は、廃棄物溶融炉での熱分解後の可燃ガス及びチャーの飛散量を抑制することにより燃焼室の温度の急上昇を防止し、最適な燃焼室の温度維持管理を可能にする、廃棄物溶融炉設備における燃焼室温度制御装置を提供するものである。 Therefore, the present invention prevents the sudden increase in the temperature of the combustion chamber by suppressing the amount of scattered combustible gas and char after pyrolysis in the waste melting furnace, and enables optimal combustion chamber temperature maintenance management. , there is provided a combustion room temperature-controlling device that put the waste melting furnace facilities.
本発明の燃焼室温度制御装置は、炉上部から廃棄物を投入し、炉下部に配設した複数段の羽口から酸素源を供給して、炉底部の排出孔から反応熱によって溶融した廃棄物中の灰分及び非燃焼物を排出する廃棄物溶融炉で発生する可燃ガス及び可燃残渣を燃焼する燃焼室温度制御装置において、前記羽口のうち上段及び中段羽口を前記廃棄物溶融炉の外周に間隔をおいて設置するとともに、上下方向において重ならないように該廃棄物溶融炉の円周方向にずらして配置し、前記可燃ガス及び可燃残渣を燃焼するバーナを燃焼室に配置し、該バーナから排出される燃焼ガスの温度を測定する温度計を燃焼ガスが排出されるレベルに配置し、さらに前記上段羽口および/または中段羽口から送風される酸素源の送風量を調節する流量調節弁を前記上段羽口及び中段羽口の酸素源供給管にそれぞれ設置するとともに、前記上段羽口及び中段羽口のそれぞれについて個別の流量調節弁の調節量を設定し、この設定値を前記温度計で測定した温度に応じて調整する空気供給制御装置を設けたことを特徴とする。 Combustion chamber temperature control device of the present invention, disposal by introducing waste from the furnace top, and supplies the oxygen source from the tuyere of a plurality of stages which is disposed in the lower part of the furnace and melted by the heat of reaction from the discharging hole of the furnace bottom portion In a combustion chamber temperature control apparatus for combusting combustible gas and combustible residue generated in a waste melting furnace that discharges ash and non-combustibles in waste, the upper and middle tuyere of the tuyere are disposed in the waste melting furnace. Installed at intervals on the outer periphery, and arranged to be shifted in the circumferential direction of the waste melting furnace so as not to overlap in the vertical direction, and a burner for burning the combustible gas and combustible residue is disposed in the combustion chamber, A flowmeter that adjusts the flow rate of the oxygen source blown from the upper tuyeres and / or the middle tuyeres, with a thermometer that measures the temperature of the combustion gas exhausted from the burner disposed at a level at which the combustion gases are exhausted Adjust the control valve to the upper Each we established the oxygen source supply pipe of the tuyere and middle tuyere sets an adjustment amount of the individual flow control valves for each of said upper tuyeres and middle tuyere were measured this setting by the thermometer An air supply control device that adjusts according to temperature is provided .
本発明では、燃焼室温度が急上昇した際には、その温度上昇幅に応じて廃棄物溶融炉の上段送風羽口、中段送風羽口及び下段送風羽口の空気量が各羽口レベル個別に設定された制御量で調整されることで、燃焼室温度急上昇が抑制され適正範囲内の温度に維持管理することが可能となる。 In the present invention, when the combustion chamber temperature suddenly rises, the amount of air in the upper blower tuyeres, the middle blower tuyeres and the lower blower tuyeres of the waste melting furnace is individually determined according to the temperature rise width. By adjusting with the set control amount, a rapid increase in the temperature of the combustion chamber is suppressed, and it becomes possible to maintain and manage the temperature within an appropriate range.
従来技術では、廃棄物溶融炉から発生する熱分解後の可燃ガス及びチャーの発生量は制御しておらず、燃焼室の燃焼空気量による燃焼室温度制御しかできないため、燃焼空気量の制御性限界もあって急激な温度上昇を抑えることが難しかったが、本発明により、廃棄物溶融炉側での自動送風制御により炉内での熱分解量を調整することが可能となり、燃焼空気量による温度制御に加えて可燃ガス及びチャー発生量の制御も可能になったことで、燃焼室温度の急上昇を大幅に抑制することが可能となった。 The conventional technology does not control the generation amount of combustible gas and char after pyrolysis generated from the waste melting furnace, and can only control the combustion chamber temperature by the combustion air amount in the combustion chamber. Although there was a limit, it was difficult to suppress a rapid temperature rise, but according to the present invention, it is possible to adjust the amount of thermal decomposition in the furnace by automatic blowing control on the waste melting furnace side, and it depends on the amount of combustion air In addition to temperature control, it became possible to control the amount of combustible gas and char generation, so that it was possible to greatly suppress the rapid increase in the combustion chamber temperature.
また、本発明では、溶融炉の安定溶融状況を維持できる送風量バランスを保ちながら送風流量調節も可能となる。 Further, according to the present invention, it is possible to adjust the flow rate of the air flow while maintaining the air flow rate balance that can maintain the stable melting state of the melting furnace.
本発明の実施例を図面により説明する。 Embodiments of the present invention will be described with reference to the drawings.
図1において、シャフト炉式廃棄物溶融炉1の後段に燃焼室2が配置されている。溶融炉1から排出される可燃ガス及びチャーを含有する排ガスは、溶融炉1と燃焼室2に接続された排ガスダクト5から燃焼室2のメインバーナに導入され、燃焼室2内に噴出し火炎を形成する。メインバーナには、例えば、前記特許文献に記載されているバーナに排ガスダクト5から可燃ガス及びチャーが供給される。
In FIG. 1, a
燃焼室2には希釈空気を導入する希釈空気導入口3が接続され、導入する希釈空気量は希釈空気調整弁4で調整される。燃焼室2には、メインバーナ温度計6が配置されている。メインバーナ温度計6には放射温度計が使用され、メインバーナと同レベルに配置されて温度計の対面側の雰囲気温度を計測する。
A dilution air introduction port 3 for introducing dilution air is connected to the
溶融炉1には、酸素源が送風される上部羽口と下段羽口9が設けられている。酸素源として、上部羽口には空気、下段羽口9には酸素富化空気が送風される。上部羽口は、本実施例では、上段羽口7、中段羽口8で構成されている。上部羽口と下段羽口9には、それぞれ溶融炉1の外周に間隔をおいて複数個の羽口が配置される。上部羽口は図2(a)に示す上段羽口7と図2(b)に示す中段羽口8が上下方向において重ならないように溶融炉1の円周方向にずらして配置することにより、吹き込む空気量が炉内で偏らないで均一に流れるようにしている。
The melting furnace 1 is provided with an upper tuyere and a lower tuyere 9 through which an oxygen source is blown. As an oxygen source, air is blown to the upper tuyere and oxygen-enriched air is blown to the lower tuyere 9. The upper tuyere is composed of an
上段羽口7、中段羽口8及び下段羽口9には、送風機13の酸素源供給配管18から分岐した上段羽口用ヘッダ14、中段羽口用ヘッダ15及び下段羽口用ヘッダ16にそれぞれ接続されている上段羽口空気供給管19、中段羽口空気供給管20及び下段羽口空気供給管21から空気が供給される。各空気供給管19,20,21には、それぞれ流量調整弁10,11,12設けられている。メインバーナ温度計6の温度信号は、空気供給制御装置17に入力されて、各流量調整弁10,11,12へ流量調節制御信号が出力される。
The
空気供給制御装置17には、燃焼室2の燃焼温度に対して、上段羽口7、中段羽口8、下段羽口9のそれぞれについて個別の流量調節弁の調節量が設定されており、メインバーナ温度計で計測された温度の変動量に対して流量調節弁の調節量の設定値を流量調節弁へ制御信号として出力する。
In the air
図3のグラフに示すように、溶融炉からの可燃ガスやチャー飛散が多くなって燃焼室2のメインバーナ温度が上昇した際に、メインバーナ温度計6で計測した温度信号が温度制御装置17に入力されると、温度制御装置17では上段羽口送風空気量22の流量調整弁10の調整量の制御信号が出力されて減調整されることで燃焼室のバーナ燃焼ガス温度24が抑えられる。本実施例では、上段羽口のみを流量調整を行いバーナ温度の調整を行った。
As shown in the graph of FIG. 3, when combustible gas and char scattering from the melting furnace increase and the main burner temperature in the
図4のグラフに示すように、溶融炉からの可燃ガスやチャー飛散が多くなって燃焼室2のメインバーナ温度が上昇した際に、メインバーナ温度計6で計測した温度信号が温度制御装置17に入力されると、温度制御装置17では上段羽口送風空気量22、中段羽口送風空気量23のそれぞれの設定に応じて各流量調整弁10,11の調整量の制御信号が出力されて減調整されることで、燃焼室2のバーナ燃焼ガス温度24の上昇を抑制することもできる。本実施例では、上段羽口7を50%の範囲内、中段羽口30%の範囲内で調整している。
As shown in the graph of FIG. 4, when the combustible gas and char scattering from the melting furnace increase and the main burner temperature in the
1:溶融炉 2:燃焼室
3:希釈空気導入口 4:希釈空気調整弁
5:排ガスダクト 6:メインバーナ温度計
7:上段羽口 8:中段羽口
9:下段羽口 10:上段羽口用流量調節弁
11:中段羽口用流量調節弁 12:下段羽口用流量調節弁
13:送風機 14:上段羽口用ヘッダ
15:中段羽口用ヘッダ 16:下段羽口用ヘッダ
17:空気供給制御装置 18:酸素源供給配管
19:上段羽口空気供給管 20:中段羽口空気供給管
21:下段羽口空気供給管 22:上段羽口送風空気量
23:中段羽口送風空気量 24:メインバーナ温度
1: Melting furnace 2: Combustion chamber 3: Dilution air introduction port 4: Dilution air adjustment valve 5: Exhaust gas duct 6: Main burner thermometer 7: Upper tuyere 8: Middle tuyere 9: Lower tuyere 10: Upper tuyere Flow control valve 11: Flow control valve for middle tuyere 12: Flow control valve for lower tuyere 13: Blower 14: Header for upper tuyere 15: Header for middle tuyere 16: Header for lower tuyere 17: Air supply Control device 18: oxygen source supply pipe 19: upper stage tuyere air supply pipe 20: middle stage tuyere air supply pipe 21: lower stage tuyere air supply pipe 22: upper stage tuyere air supply 23: middle stage tuyere air supply 24: Main burner temperature
Claims (1)
前記羽口のうち上段及び中段羽口を前記廃棄物溶融炉の外周に間隔をおいて設置するとともに、上下方向において重ならないように該廃棄物溶融炉の円周方向にずらして配置し、
前記可燃ガス及び可燃残渣を燃焼するバーナを燃焼室に配置し、該バーナから排出される燃焼ガスの温度を測定する温度計を燃焼ガスが排出されるレベルに配置し、さらに前記上段羽口および/または中段羽口から送風される酸素源の送風量を調節する流量調節弁を前記上段羽口及び中段羽口の酸素源供給管にそれぞれ設置するとともに、前記上段羽口及び中段羽口のそれぞれについて個別の流量調節弁の調節量を設定し、この設定値を前記温度計で測定した温度に応じて調整する空気供給制御装置を設けたことを特徴とする燃焼室温度制御装置。 Waste is introduced from the upper part of the furnace, oxygen sources are supplied from a plurality of tuyeres arranged at the lower part of the furnace, and ash and non-combustible substances in the waste melted by reaction heat are discharged from the discharge hole at the bottom of the furnace. In a combustion chamber temperature control device for burning combustible gas and combustible residue generated in a waste melting furnace,
Among the tuyere, the upper and middle tuyere are installed at an interval on the outer periphery of the waste melting furnace, and are shifted in the circumferential direction of the waste melting furnace so as not to overlap in the vertical direction,
Wherein the burner for burning a combustible gas and combustible residue located in the combustion chamber, a thermometer for measuring the temperature of the combustion gas discharged from the burner is arranged at the level of the combustion gas is discharged, further the upper tuyeres and A flow control valve for adjusting the amount of oxygen source blown from the middle tuyere is installed in each of the upper tuyere and middle tuyere oxygen source supply pipes, and each of the upper tuyere and middle tuyere A combustion chamber temperature control device comprising an air supply control device for setting an adjustment amount of an individual flow rate control valve and adjusting a set value according to a temperature measured by the thermometer .
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