JP5020656B2 - Coke oven combustion method and combustion apparatus - Google Patents

Coke oven combustion method and combustion apparatus Download PDF

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JP5020656B2
JP5020656B2 JP2007035334A JP2007035334A JP5020656B2 JP 5020656 B2 JP5020656 B2 JP 5020656B2 JP 2007035334 A JP2007035334 A JP 2007035334A JP 2007035334 A JP2007035334 A JP 2007035334A JP 5020656 B2 JP5020656 B2 JP 5020656B2
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combustion
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air
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JP2008195902A (en
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三千雄 田端
正彦 横溝
喜一 堂山
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Nippon Steel Corp
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本発明は、コークス炉において空気の流量を調節するコークス炉の燃焼方法および燃焼装置に関する。   The present invention relates to a combustion method and combustion apparatus for a coke oven that adjusts the flow rate of air in the coke oven.

一般にコークス炉は、炉幅方向(炉団方向)に交互に複数列配列した炭化室と燃焼室との対で一つの炉を形成し、通常は50から100個の炉が集まって1つの炉団を構成している。そして、各燃焼室は、炉壁(レンガ壁)を介して炭化室と隣接し、炉長方向に20から30個の小燃焼室に仕切られており、各小燃焼室の底部は蓄熱室に通じている(特許文献1、図1)。   In general, a coke oven forms one furnace by a pair of carbonization chambers and combustion chambers arranged in a plurality of rows alternately in the furnace width direction (furnace group direction), and usually 50 to 100 furnaces gather to form one furnace. A group is formed. Each combustion chamber is adjacent to the carbonization chamber via a furnace wall (brick wall) and is partitioned into 20 to 30 small combustion chambers in the furnace length direction, and the bottom of each small combustion chamber is a heat storage chamber. (Patent Document 1, FIG. 1).

各小燃焼室には、予熱用蓄熱室で予熱された燃料ガスと空気が供給され、これらの燃焼によって炉壁を通じて両側の炭化室が加熱されて石炭の乾留が行われる。そして、各小燃焼室で生成した排ガスは熱回収用蓄熱室に引き落とされて熱回収され、さらに炉底部に設けられている水平炎道(ソールフリュー)に排出された排ガスは炉の前後方に分配されて煙突から大気に排出される。この予熱用蓄熱室と熱回収用蓄熱室は例えば20分あるいは30分といった制御周期で交互に切り替えられる。なお、予熱用蓄熱室を「立ち側」、熱回収用蓄熱室を「引き側」と称す。   Each small combustion chamber is supplied with fuel gas and air preheated in the heat storage chamber for preheating, and by these combustion, the carbonization chambers on both sides are heated through the furnace wall, and dry distillation of coal is performed. The exhaust gas generated in each small combustion chamber is pulled down to the heat recovery heat storage chamber and recovered, and the exhaust gas discharged to the horizontal flame path (sole flue) provided at the bottom of the furnace is located at the front and rear of the furnace. It is distributed and discharged from the chimney to the atmosphere. The heat storage chamber for preheating and the heat storage chamber for heat recovery are alternately switched at a control cycle of, for example, 20 minutes or 30 minutes. The preheating heat storage chamber is referred to as the “standing side”, and the heat recovery heat storage chamber is referred to as the “pulling side”.

また、燃焼室の高さ方向における燃焼温度を均一にし、局部的な高温燃焼を無くして燃焼排ガス中のNOxを低減させるコークス炉の操業方法として、燃焼用空気の一部を底部から、残りを高さ方向の一箇所または複数箇所から供給する多段型燃焼方式が提案されている(特許文献2)。   In addition, as a method of operating a coke oven in which the combustion temperature in the height direction of the combustion chamber is made uniform, local high-temperature combustion is eliminated, and NOx in the combustion exhaust gas is reduced, part of the combustion air is removed from the bottom. There has been proposed a multistage combustion system that supplies from one place or a plurality of places in the height direction (Patent Document 2).

図2は、上述した多段型燃焼方式を採用したコークス炉の燃焼装置を示し、(a)(b)は同一の小燃焼室21-1・・・・・21-nを立ち側と引き側に分離して示したもので、小燃焼室21は、天井壁面との間に隙間を有する仕切壁22により第1燃焼室部23と、第2燃焼室部24とに仕切られ、図2(a)は第1燃焼室部23を立ち側燃焼室部とした場合、図2(b)は第1燃焼室部23を引き側燃焼室部とした場合を示す。また、第1燃焼室部23と第2燃焼室部24にはそれぞれ底部空気供給系25と多段空気供給系26により燃焼用の空気を底部と高さ方向の複数箇所より供給可能となっており、第1燃焼室部23を立ち側とした場合には引き側となる第2燃焼室部24側における底部空気供給系と多段空気供給系とが排ガス排出系として用いられる。   FIG. 2 shows a combustion apparatus for a coke oven that employs the above-described multistage combustion method. (A) and (b) show the same small combustion chamber 21-1. 2, the small combustion chamber 21 is partitioned into a first combustion chamber portion 23 and a second combustion chamber portion 24 by a partition wall 22 having a gap between the small combustion chamber 21 and the ceiling wall surface. FIG. 2A shows a case where the first combustion chamber portion 23 is a standing combustion chamber portion, and FIG. 2B shows a case where the first combustion chamber portion 23 is a pulling combustion chamber portion. In addition, combustion air can be supplied to the first combustion chamber portion 23 and the second combustion chamber portion 24 from a plurality of locations in the bottom and height directions by a bottom air supply system 25 and a multistage air supply system 26, respectively. When the first combustion chamber portion 23 is the standing side, the bottom air supply system and the multistage air supply system on the second combustion chamber portion 24 side that is the pulling side are used as the exhaust gas discharge system.

第1燃焼室部23の下方に第1蓄熱室27が対応して配置され、第2燃焼室部24の下方に第2蓄熱室(不図示)が対応してそれぞれ配置され、第1蓄熱室27には炉底(底部)側第1ソールフリュー28からソールフリュー―蓄熱室連絡孔30を介して空気が供給され、前記第2蓄熱室には不図示の炉底(底部)側第2ソールフリューから同様にソールフリュー―蓄熱室連絡孔を介して空気が供給される。そして、第1蓄熱室27は第1燃焼室部23用の底部空気供給系25と多段空気供給系26と接続され、高温の空気が第1燃焼室部23内へ供給される。なお、第1燃焼室部23及び第2燃焼室部24に対して燃料ガスが供給可能となっており、第1燃焼室部23を立ち側とした場合に燃料ガスを第1燃焼室部23内に供給し、燃焼用の空気と混合することにより燃焼し、上昇して炉壁を加熱する。 A first heat storage chamber 27 is disposed below the first combustion chamber 23 and a second heat storage chamber (not shown) is disposed below the second combustion chamber 24 to correspond to the first heat storage chamber. 27 is supplied with air from the furnace bottom (bottom) side first sole flue 28 through the sole flue-heat storage chamber communication hole 30, and the second heat storage chamber has a furnace bottom (bottom) side second sole ( not shown ) . Similarly, air is supplied from the flue through the sole flue-heat storage chamber communication hole. The first heat storage chamber 27 is connected to the bottom air supply system 25 and the multistage air supply system 26 for the first combustion chamber section 23, and high-temperature air is supplied into the first combustion chamber section 23. In addition, fuel gas can be supplied to the first combustion chamber portion 23 and the second combustion chamber portion 24, and the fuel gas is supplied to the first combustion chamber portion 23 when the first combustion chamber portion 23 is set to the standing side. It is supplied to the inside and burned by mixing with combustion air, and then rises to heat the furnace wall.

そして、燃焼排ガスは仕切壁22を矢印で示すように迂回し引き側となる第2燃焼室部24を経て、底部空気排出系及び多段空気排出系から引き側となる第2蓄熱室を通過し、引き側となる炉底側第2ソールフリューに排出される。   The combustion exhaust gas passes through the second heat storage chamber on the pulling side from the bottom air discharge system and the multistage air discharge system through the second combustion chamber portion 24 on the pulling side, bypassing the partition wall 22 as indicated by an arrow. Then, it is discharged to the furnace bottom side second sole flue that becomes the pulling side.

炉底側第1ソールフリュー28は煙道(不図示)と第1変更弁29を介して接続され、同様に炉底側第2ソールフリューも煙道(不図示)を介して第2変更弁(不図示)に接続されていて、これらの煙道が煙突に接続されている。   The furnace bottom side first sole flue 28 is connected to a flue (not shown) via a first change valve 29. Similarly, the furnace bottom side second sole flue 28 is also connected to a second change valve via a flue (not shown). (Not shown) and these flues are connected to the chimney.

第1燃焼室部23が立ち側に使用されている場合に、第1変更弁29は閉状態に維持され、燃焼用の空気を第1蓄熱室27に供給させ、第2燃焼室部24が引き側に使用されている場合に、前記第2変更弁は開状態に維持され、前記第2蓄熱室を通過した排ガスを煙突から大気に排出させる。 When the first combustion chamber 23 is used on the standing side, the first change valve 29 is maintained in a closed state, and combustion air is supplied to the first heat storage chamber 27, so that the second combustion chamber 24 is When used on the pulling side, the second change valve is maintained in an open state, and exhaust gas that has passed through the second heat storage chamber is discharged from the chimney to the atmosphere.

また、図2(b)に示すように、第1燃焼室部23を引き側として使用した場合には、第1変更弁29は開状態となる。   As shown in FIG. 2B, when the first combustion chamber 23 is used as the pulling side, the first change valve 29 is opened.

一方、特許文献2には、底部から供給する燃焼用空気量を全供給空気量の50%以上として操業するのが望ましいとしているが、底部空気吹出孔及び多段の空気吹出孔から供給される燃焼用空気量の比率を所要割合に調整する方法として、図3(a)(b)に示すように、燃焼室の底部空気吹出孔31、多段の空気吹出孔33にスライドブリック32、34を設け、スライドブリック32、34をスライドさせて空気吹出孔31、33の開口面積を調整する方法が提案されており、具体的には図3(c)に示すように、作業者が燃焼室の炉頂からスライドブリック開度調整棒34をスライドブリック32、33まで挿入し、スライドブリック開度調整棒34を操作してスライドブリックをスライドさせることが提案されている。
特開平11−035944号公報 特開2000−351975号公報
On the other hand, in Patent Document 2, it is desirable to operate with the combustion air amount supplied from the bottom part being 50% or more of the total supply air amount, but the combustion supplied from the bottom air outlet hole and the multistage air outlet hole As a method of adjusting the ratio of the working air amount to a required ratio, as shown in FIGS. 3A and 3B, slide bricks 32 and 34 are provided in the bottom air blowing hole 31 and the multistage air blowing holes 33 of the combustion chamber. A method of adjusting the opening area of the air blowing holes 31 and 33 by sliding the slide bricks 32 and 34 has been proposed. Specifically, as shown in FIG. It has been proposed to insert the slide brick opening adjustment rod 34 from the top to the slide bricks 32 and 33 and to operate the slide brick opening adjustment rod 34 to slide the slide brick.
JP 11-035944 A JP 2000-351975 A

ところで、底部空気吹出孔及び多段の空気吹出孔から供給される燃焼用空気量の比率を所要割合に調整するために、燃焼室の底部空気吹出孔31,多段の空気吹出孔33に対するスライドブリック32,34をスライドさせる方法は、以下に示すように作業性が悪い等といった問題が指摘され、調整作業は現実的に困難であった。
1 約1000℃の燃焼室の炉頂で作業者がスライドブリック開度調整棒34を操作するが、この作業は遠隔で行われ、しかも高温の燃焼室内に挿入されたスライドブリック開度調整棒34は柔らかくなるため、微調整ができない。
2 調整作業が高温環境下であり、重筋作業となる。
3 燃焼室内温度が高温のため、スライドブリックと壁とが焼きつき、開度調整作業が難しく、無理に調整すると煉瓦の損傷を招くおそれもある。
By the way, in order to adjust the ratio of the amount of combustion air supplied from the bottom air blowing holes and the multistage air blowing holes to a required ratio, the slide brick 32 with respect to the bottom air blowing holes 31 and the multistage air blowing holes 33 of the combustion chamber. , 34 have been pointed out as having problems such as poor workability as described below, and adjustment work was actually difficult.
1 The operator operates the slide brick opening adjustment rod 34 at the top of the combustion chamber at about 1000 ° C. This operation is performed remotely, and the slide brick opening adjustment rod 34 inserted into the high temperature combustion chamber. Because it becomes soft, fine adjustment is not possible.
2 The adjustment work is in a high temperature environment and is a heavy work.
3 Because the temperature in the combustion chamber is high, the slide brick and the wall are seized, making it difficult to adjust the opening, and there is a risk of brick damage if adjusted forcibly.

本発明は、このような従来の問題を解決し、重筋作業を要することなく底部空気吹出孔及び多段の空気吹出孔から供給される燃焼用空気量の比率を所要割合に確実に調整することができるコークス炉の燃焼方法及び燃焼装置を提供することを目的とする。   The present invention solves such a conventional problem and reliably adjusts the ratio of the amount of combustion air supplied from the bottom air blowing holes and the multistage air blowing holes to a required ratio without requiring heavy work. It is an object of the present invention to provide a combustion method and combustion apparatus for a coke oven that can perform the above.

本発明は、上記技術的課題を解決するものであり、その発明の要旨とするところは以下の通りである。
(1)底部及び高さ方向の異なる多段位置にそれぞれ空気吹出孔を備えた二つの燃焼室部を交互に立ち側と引き側に切り替えて燃焼を行うコークス炉の燃焼方法において、立ち側の燃焼室部には底部と高さ方向の異なる多段位置の空気吹出孔にそれぞれ別々の蓄熱室から流量比率を調整した燃焼用空気を供給し、引き側の燃焼室部からは、底部の空気吹出孔から底部側蓄熱室を経て底部側ソールフリューを介して燃焼排ガスを排出すると共に、多段位置の空気吹出孔から多段側蓄熱室を経て多段側ソールフリューを介して燃焼排ガスを排出し、前記底部側蓄熱室と前記多段側蓄熱室に引き落とされる排ガスの流量比率を、底部空気吹出孔用の蓄熱室と多段の空気吹出孔用の蓄熱室に供給される燃焼用空気の流量比率に合わせたことを特徴とするコークス炉の燃焼方法。
(2)底部及び高さ方向の異なる多段位置にそれぞれ空気吹出孔を備えた二つの燃焼室部を交互に立ち側と引き側に切り替えて燃焼を行うコークス炉の燃焼室と、前記各燃焼室部の底部側空気吹出孔に通じる底部側蓄熱室、及び多段側空気吹出孔に通じる多段側蓄熱室と、前記一方の燃焼室部用の底部側蓄熱室及び多段側蓄熱室に別々に通じる底部側第1ソールフリュー、及び多段側第1ソールフリューと、前記他方の燃焼室部用の底部側蓄熱室及び多段側蓄熱室に別々に通じる底部側第2ソールフリュー、及び多段側第2ソールフリューと、前記底部側第1ソールフリュー、多段側第1ソールフリュー、底部側第2ソールフリュー、及び多段側第2ソールフリューの排出側に夫々設けた排出ガス流量調整手段と、を有し、立ち側の燃焼室部用の底部側蓄熱室及び多段側蓄熱室に供給する燃焼用空気の流量比率に合わせて、引き側の排出ガス流量調整手段を調整したことを特徴とするコークス炉の燃焼装置。
The present invention solves the above technical problem, and the gist of the invention is as follows.
(1) In the combustion method of a coke oven in which combustion is performed by alternately switching the two combustion chamber portions each having the air blowing holes at the bottom portion and the multistage positions in the height direction between the standing side and the pulling side, Combustion air having a flow rate adjusted from separate heat storage chambers is supplied to the air blowing holes at different stages in the height direction from the bottom to the chamber, and the bottom air blowing holes are supplied from the combustion chamber on the pull side. The exhaust gas is discharged from the bottom side heat storage chamber through the bottom side sole flue, and the flue gas is discharged from the air blowing holes at the multistage position through the multistage side heat storage chamber and the multistage side sole flue. The flow rate ratio of the exhaust gas drawn down to the heat storage chamber and the multistage side heat storage chamber is adjusted to the flow rate ratio of the combustion air supplied to the heat storage chamber for the bottom air outlet and the heat storage chamber for the multistage air outlet. Features Combustion method of the coke oven.
(2) A combustion chamber of a coke oven that performs combustion by alternately switching two combustion chamber portions each having air blowing holes at the bottom portion and multi-stage positions in different height directions to a standing side and a pulling side, and each of the combustion chambers bottom side regenerators communicating on the bottom side air outlet hole parts, and a multi-stage-side air and the multi-stage-side heat storage chamber communicating with the outlet hole, leading separately to the bottom side regenerator and multistage side regenerator for the one combustion chamber bottom Side first sole flue, multi-stage side first sole flue, bottom- side second sole flue and multi-stage side second sole flue that separately communicate with the other combustion chamber portion bottom- side heat storage chamber and multi-stage side heat storage chamber And exhaust gas flow rate adjusting means provided on the discharge side of the bottom side first sole flue, the multistage side first sole flue, the bottom side second sole flue, and the multistage side second sole flue, respectively, Side combustion chamber The bottom side regenerator and in accordance with the flow ratio of the combustion air supplied to the multi-stage side regenerator, coke oven of the combustion apparatus, characterized in that to adjust the exhaust gas flow rate adjusting means pulling side.

本発明によれば、燃焼室の底部と多段位置から吹出燃焼用空気量を、低NOxを達成するために必要な流量割合に熱効率を低下させることなく容易に調整することが可能となった。 According to the present invention, it is possible to easily adjust the amount of air for combustion from the bottom of the combustion chamber and the multistage position to the flow rate ratio required to achieve low NOx without reducing the thermal efficiency.

以下本発明を図面に示す実施形態に基づいて説明する。   Hereinafter, the present invention will be described based on embodiments shown in the drawings.

図1は本発明を適用したコークス炉の燃焼装置の一実施形態を示す概略図で、(a)(b)は図2に示す従来例と同様に、同一の小燃焼室21-1・・・・・21-nを立ち側と引き側に分離して示したもので、小燃焼室21を仕切壁22により第1燃焼室部23と第2燃焼室部24とに仕切り、第1燃焼室部23と第2燃焼室部24にはそれぞれ底部空気吹出孔及び多段の空気吹出孔を設けた構成も図2に示す従来例と同様である。なお、図1(a)は第1燃焼室を立ち側燃焼室部とした場合、図(b)は第2燃焼室部24を引き側燃焼室部とした場合を示す。 FIG. 1 is a schematic view showing an embodiment of a combustion apparatus for a coke oven to which the present invention is applied. (A) and (b) are the same small combustion chambers 21-1... As in the conventional example shown in FIG. ... 21-n is shown separated into a standing side and a pulling side, and the small combustion chamber 21 is partitioned into a first combustion chamber portion 23 and a second combustion chamber portion 24 by a partition wall 22, and the first combustion is performed. The configuration in which the chamber portion 23 and the second combustion chamber portion 24 are respectively provided with a bottom air blowing hole and a multistage air blowing hole is the same as the conventional example shown in FIG. Incidentally, FIG. 1 (a) when the trailing-side combustion chamber portion of the first combustion chamber part 2 3, FIG. 1 (b) shows the case of a pull-side combustion chamber portion of the second combustion chamber 24.

本実施形態は、第1燃焼室部23において、底部空気吹出孔用の炉底側第1蓄熱室1と、多段の空気吹出孔用の多段側第1蓄熱室2とを別々に設け、同様に第2燃焼室部24において、底部空気吹出孔用の炉底側第2蓄熱室3と、多段の空気吹出孔用の多段側第2蓄熱室4とを別々に設けている。   In the first embodiment, the first combustion chamber portion 23 is provided separately with the furnace bottom side first heat storage chamber 1 for the bottom air blowing holes and the multistage side first heat storage chamber 2 for the multistage air blowing holes. In addition, in the second combustion chamber section 24, a furnace bottom side second heat storage chamber 3 for the bottom air outlet hole and a multistage second heat storage chamber 4 for the multistage air outlet holes are separately provided.

また、第1燃焼室部23用に2つのソールフリュー5、6を設け、炉底(底部)側第1ソールフリュー5はソールフリュー―蓄熱室連絡孔30を介して炉底(底部)側第1蓄熱室1に接続され、多段側第1ソールフリュー6はソールフリュー―蓄熱室連絡孔30を介して多段側第1蓄熱室2に接続されている。 In addition, two sole flues 5 and 6 are provided for the first combustion chamber portion 23, and the furnace bottom (bottom) side first sole flue 5 is connected to the furnace bottom (bottom) side first through the sole flue-heat storage chamber communication hole 30. The first heat storage chamber 1 is connected, and the first multi-stage sole sole 6 is connected to the first multi-stage heat storage chamber 2 via a sole-heat storage chamber communication hole 30.

同様に、第2燃焼室部24用に2つのソールフリュー7、8を設け、炉底(底部)側第2ソールフリュー7はソールフリュー―蓄熱室連絡孔30を介して炉底(底部)側第2蓄熱室3に接続され、多段側第2ソールフリュー8はソールフリュー―蓄熱室連絡孔30を介して多段側第2蓄熱室4に接続されている。 Similarly, two sole flues 7 and 8 are provided for the second combustion chamber portion 24, and the second sole flue 7 on the furnace bottom (bottom) side is disposed on the furnace bottom (bottom) side via the sole flue-heat storage chamber communication hole 30. Connected to the second heat storage chamber 3, the multistage-side second sole flue 8 is connected to the multistage-side second heat storage chamber 4 via the sole flue-heat storage chamber communication hole 30.

炉底側第1ソールフリュー5及び多段側第1ソールフリュー6の排出端部は合流して第1変更弁9に接続され、炉底側第2ソールフリュー7及び多段側第2ソールフリュー8の排出端部は合流して第2変更弁10に接続され、さらに煙道を経て煙突につながっている。   The discharge end portions of the furnace bottom side first sole flue 5 and the multistage side first sole flue 6 merge and are connected to the first change valve 9, and the furnace bottom side second sole flue 7 and the multistage side second sole flue 8 The discharge ends join together and are connected to the second change valve 10 and further connected to the chimney via the flue.

また、炉底側第1ソールフリュー5及び多段側第1ソールフリュー6の排出端部にはそれぞれ第1変更弁入口ダンパー11が設けられ、炉底側第2ソールフリュー7及び多段側第2ソールフリュー8の排出端部にはそれぞれ第2変更弁入口ダンパー12が設けられ、排ガスの流量を調整可能としている。   Further, first change valve inlet dampers 11 are provided at the discharge end portions of the furnace bottom side first sole flue 5 and the multistage side first sole flue 6 respectively, and the furnace bottom side second sole flue 7 and the multistage side second sole are provided. A second change valve inlet damper 12 is provided at the discharge end portion of the flue 8 so that the flow rate of the exhaust gas can be adjusted.

さらに、炉底側第1蓄熱室1には第1燃焼室部23用の底部空気供給系25を接続し、多段側第1蓄熱室2には第1燃焼室部23用の多段空気供給系26を接続し、炉底側第2蓄熱室3には第2燃焼室部24用の底部空気供給系25を接続し、多段側第2蓄熱室4には第2燃焼室部24用の多段空気供給系26を接続している。   Further, a bottom air supply system 25 for the first combustion chamber portion 23 is connected to the furnace bottom side first heat storage chamber 1, and a multistage air supply system for the first combustion chamber portion 23 is connected to the multistage first heat storage chamber 2. 26, a bottom air supply system 25 for the second combustion chamber 24 is connected to the furnace bottom side second heat storage chamber 3, and a multistage for the second combustion chamber portion 24 is connected to the multistage second heat storage chamber 4. An air supply system 26 is connected.

本実施形態において、炉底側第1ソールフリュー5及び多段側第1ソールフリュー6内をそれぞれ流れる燃焼用空気は、不図示の流量調整コック等で構成される元弁の弁開度を調整することにより、第1燃焼室部23内に供給される燃焼用空気量を別々に調整して低NOxを達成するために必要な流量割合で底部空気吹出孔及び多段の空気吹出孔から供給することができる。   In the present embodiment, the combustion air flowing through the furnace bottom side first sole flue 5 and the multistage side first sole flue 6 adjusts the valve opening degree of the main valve composed of a flow adjustment cock (not shown). Thus, the amount of combustion air supplied into the first combustion chamber portion 23 is separately adjusted and supplied from the bottom air outlet hole and the multistage air outlet holes at a flow rate ratio required to achieve low NOx. Can do.

第1燃焼室部23を立ち側とした場合、燃焼用空気は炉底側第1蓄熱室1と多段側第1蓄熱室2を通過して高温に加熱されて任意の流量割合で底部空気供給系25と多段空気供給系26を経て第1燃焼室23内に供給される。この場合、各第2変更弁入口ダンパー12は、炉底側第2ソールフリュー7と多段側第2ソールフリュー8を流れる排ガスの流量割合が上述の燃焼用空気の流量割合に一致するように弁開度をそれぞれ調整している。これは、第2燃焼室部24を立ち側とした場合に引き側となる第1燃焼室部23に通じる炉底側第1ソールフリュー5と多段側第1ソールフリュー6にそれぞれ取り付けた第1変更弁入口ダンパー11についても適用される。   When the first combustion chamber portion 23 is set to the standing side, the combustion air passes through the furnace bottom-side first heat storage chamber 1 and the multistage-side first heat storage chamber 2 and is heated to a high temperature to supply bottom air at an arbitrary flow rate. The gas is supplied into the first combustion chamber 23 through the system 25 and the multistage air supply system 26. In this case, each of the second change valve inlet dampers 12 is controlled so that the flow rate ratio of the exhaust gas flowing through the furnace bottom side second sole flue 7 and the multistage second sole flue 8 matches the flow rate ratio of the combustion air described above. Each opening is adjusted. This is the first attached to the furnace bottom side first sole flue 5 and the multistage side first sole flue 6 leading to the first combustion chamber portion 23 which is the pulling side when the second combustion chamber portion 24 is the standing side. This also applies to the change valve inlet damper 11.

本実施形態において、第1燃焼室部23と第2燃焼室部24とに対して一定時間毎に燃焼の切り替えが行われ、燃料ガスと空気、及び燃焼排ガスは立ち側と引き側とが入れ替わる。図1において、切り替え前における引き側の蓄熱室1、2は燃焼排ガスが保有する顕熱を蓄え、切り替え後に立ち側の炉底側及び多段側の燃焼用空気をそれぞれ予熱する。このときに、立ち側の炉底側第1蓄熱室1と多段側第1蓄熱室2に流入する空気流量の割合と、引き側であったときの炉底側第1蓄熱室1と多段側第1蓄熱室2に流入する排ガスの流量割合をバランスさせないと、熱交換率が低下する。   In the present embodiment, combustion is switched for the first combustion chamber portion 23 and the second combustion chamber portion 24 at regular intervals, and fuel gas and air and combustion exhaust gas are switched between the standing side and the pulling side. . In FIG. 1, the heat storage chambers 1 and 2 on the pulling side before switching store sensible heat held in the combustion exhaust gas, and preheat the combustion air on the standing furnace bottom side and the multistage side after switching, respectively. At this time, the ratio of the air flow rate flowing into the standing-side furnace bottom side first heat storage chamber 1 and the multi-stage side first heat storage chamber 2, and the furnace bottom side first heat storage chamber 1 and the multi-stage side at the pulling side If the flow rate ratio of the exhaust gas flowing into the first heat storage chamber 2 is not balanced, the heat exchange rate decreases.

すなわち、仮に立ち側の炉底蓄熱室に6割の燃焼用空気が入り、多段側蓄熱室に4割りが入ったとし、燃焼室で燃焼後、燃焼排ガスが引き側の炉底、多段それぞれの蓄熱室に引き落とされた場合、炉底側蓄熱室抜熱過多となり、多段側は抜熱不足となる。この場合、消費熱量の悪化および燃焼用空気の予熱不足から燃焼が不安定となるおそれが発生する。 That is, assuming that 60% of combustion air enters the standing furnace bottom side heat storage chamber and 40% enters the multi-stage side heat storage chamber, and after combustion in the combustion chamber, the combustion exhaust gas flows into the pull-down side furnace bottom and multi-stage respectively. When the heat storage chamber is pulled down, the furnace bottom side heat storage chamber has excessive heat removal, and the multistage side has insufficient heat extraction. In this case, there is a possibility that the combustion becomes unstable due to the deterioration of the heat consumption and the insufficient preheating of the combustion air.

しかし、本実施形態では、立ち側の炉底側蓄熱室及び多段側蓄熱室に入る燃焼用の空気量の割合と、そのときの引き側の炉底側蓄熱室及び多段側蓄熱室に引き落とされる燃焼排ガスの流量割合をバランスさせているので、高い熱交換率を維持することができる。   However, in this embodiment, the ratio of the amount of combustion air entering the standing-side furnace bottom-side heat storage chamber and the multistage-side heat storage chamber, and the pull-down side furnace bottom-side heat storage chamber and the multistage-side heat storage chamber are pulled down. Since the flow rate ratio of the combustion exhaust gas is balanced, a high heat exchange rate can be maintained.

本発明の一実施形態を示すコークス炉の燃焼装置を示す概略図で、(a)は立ち側、(b)は引き側を示す。It is the schematic which shows the combustion apparatus of the coke oven which shows one Embodiment of this invention, (a) shows the standing side, (b) shows the pulling side. 従来のコークス炉の燃焼装置を示す概略図で、(a)は立ち側、(b)は引き側を示す。It is the schematic which shows the combustion apparatus of the conventional coke oven, (a) shows the standing side, (b) shows the pulling side. 従来の底部空気吹出孔及び多段の空気吹出孔から供給される燃焼空気量の比率を調整する方法を示す図。The figure which shows the method of adjusting the ratio of the amount of combustion air supplied from the conventional bottom part air blowing hole and a multistage air blowing hole.

符号の説明Explanation of symbols

1 炉底(底部)側第1蓄熱
2 多段側第1蓄熱
3 炉底(底部)側第2蓄熱
4 多段側第2蓄熱
5 炉底(底部)側第1ソールフリュー
6 多段側第1ソールフリュー
7 炉底(底部)側第2ソールフリュー
8 多段側第2ソールフリュー
9 第1変更弁
10 第2変更弁
11 第1変更弁入口ダンパー
12 第2変更弁入口ダンパー
21 燃焼室
22 仕切壁
23 第1燃焼室部
24 第2燃焼室部
25 炉底(底部)空気供給系
26 多段空気供給系
27 第1蓄熱室
28 炉底(底部)側第1ソールフリュー
29 変更弁
30 ソールフリュー―蓄熱室連絡孔
DESCRIPTION OF SYMBOLS 1 Furnace bottom (bottom part) side 1st thermal storage chamber 2 Multistage side 1st thermal storage chamber 3 Furnace bottom (bottom part) side 2nd thermal storage chamber 4 Multistage side 2nd thermal storage chamber 5 Furnace bottom (bottom part) side 1st sole flue 6 Multistage side First sole flue 7 Furnace bottom (bottom) side second sole flue 8 Multi-stage second sole flue 9 First change valve 10 Second change valve 11 First change valve inlet damper 12 Second change valve inlet damper 21 Combustion chamber 22 partition wall 23 first combustion chamber 24 and the second combustion chamber portion 25 hearth (bottom) air supply system 26 the multi-stage air supply system 27 first regenerator 28 hearth (bottom) side first sole flues 29 reversing valve 30 Sole Flue-Heat Storage Room Communication Hole

Claims (2)

底部及び高さ方向の異なる多段位置にそれぞれ空気吹出孔を備えた二つの燃焼室部を交互に立ち側と引き側に切り替えて燃焼を行うコークス炉の燃焼方法において、
立ち側の燃焼室部には底部と高さ方向の異なる多段位置の空気吹出孔にそれぞれ別々の蓄熱室から流量比率を調整した燃焼用空気を供給し、引き側の燃焼室部からは、底部の空気吹出孔から底部側蓄熱室を経て底部側ソールフリューを介して燃焼排ガスを排出すると共に、多段位置の空気吹出孔から多段側蓄熱室を経て多段側ソールフリューを介して燃焼排ガスを排出し、前記底部側蓄熱室と前記多段側蓄熱室に引き落とされる排ガスの流量比率を、底部空気吹出孔用の蓄熱室と多段の空気吹出孔用の蓄熱室に供給される燃焼用空気の流量比率に合わせたことを特徴とするコークス炉の燃焼方法。
In the combustion method of the coke oven, in which combustion is performed by alternately switching the two combustion chamber portions each having the air blowing holes at the bottom portion and the multistage position in the height direction to the standing side and the pulling side,
Combustion air adjusted in flow rate ratio is supplied from separate heat storage chambers to the air blowing holes at different stages in the height direction from the bottom to the combustion chamber on the standing side, and from the combustion chamber on the pulling side to the bottom Exhaust flue gas is discharged from the air outlet hole through the bottom side heat storage chamber and through the bottom side sole flue, and the flue gas is discharged from the air outlet hole at the multistage position through the multistage side heat storage chamber and through the multistage side sole flue. The flow rate ratio of the exhaust gas drawn down to the bottom side heat storage chamber and the multistage side heat storage chamber is changed to the flow rate ratio of combustion air supplied to the heat storage chamber for the bottom air outlet hole and the heat storage chamber for the multistage air outlet hole. A coke oven combustion method characterized by being combined.
底部及び高さ方向の異なる多段位置にそれぞれ空気吹出孔を備えた二つの燃焼室部を交互に立ち側と引き側に切り替えて燃焼を行うコークス炉の燃焼室と、前記各燃焼室部の底部側空気吹出孔に通じる底部側蓄熱室、及び多段側空気吹出孔に通じる多段側蓄熱室と、前記一方の燃焼室部用の底部側蓄熱室及び多段側蓄熱室に別々に通じる底部側第1ソールフリュー、及び多段側第1ソールフリューと、前記他方の燃焼室部用の底部側蓄熱室及び多段側蓄熱室に別々に通じる底部側第2ソールフリュー、及び多段側第2ソールフリューと、前記底部側第1ソールフリュー、多段側第1ソールフリュー、底部側第2ソールフリュー、及び多段側第2ソールフリューの排出側に夫々設けた排出ガス流量調整手段と、を有し、立ち側の燃焼室部用の底部側蓄熱室及び多段側蓄熱室に供給する燃焼用空気の流量比率に合わせて、引き側の排出ガス流量調整手段を調整したことを特徴とするコークス炉の燃焼装置。 A combustion chamber of a coke oven that performs combustion by alternately switching two combustion chamber portions each having air blowing holes at different positions in the bottom portion and in the height direction to a standing side and a pulling side, and a bottom portion of each combustion chamber portion bottom side regenerators leading to the side air discharge holes, and a multi-stage-side air and the multi-stage-side heat storage chamber communicating with the outlet hole, the bottom side first leading separately to the bottom side regenerator and multistage side regenerator for the one combustion chamber portion sole flues, and the multi-stage-side first sole flues and leads separately to the bottom side regenerator and multistage side regenerator for the other combustion chamber bottom side second sole flues, and a multi-stage-side second sole flues, the Combustion on the standing side, comprising a bottom side first sole flue, a multistage side first sole flue, a bottom side second sole flue, and an exhaust gas flow rate adjusting means provided on the discharge side of the multistage side second sole flue, respectively. bottom for the chamber part In accordance with the flow ratio of the combustion air supplied to the side regenerator and multi-side regenerator, combustion apparatus of the coke oven, characterized in that to adjust the exhaust gas flow rate adjusting means pulling side.
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