JPS58224208A - Uniform dispersion type pulverized coal firing equipment - Google Patents
Uniform dispersion type pulverized coal firing equipmentInfo
- Publication number
- JPS58224208A JPS58224208A JP10469982A JP10469982A JPS58224208A JP S58224208 A JPS58224208 A JP S58224208A JP 10469982 A JP10469982 A JP 10469982A JP 10469982 A JP10469982 A JP 10469982A JP S58224208 A JPS58224208 A JP S58224208A
- Authority
- JP
- Japan
- Prior art keywords
- pulverized coal
- vane
- venturi
- airflow
- elbow
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D1/00—Burners for combustion of pulverulent fuel
- F23D1/02—Vortex burners, e.g. for cyclone-type combustion apparatus
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は微粉炭等、石炭を微細な粒子−に粉砕したも
のを燃焼させる装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for burning coal pulverized into fine particles, such as pulverized coal.
最近の燃料事情の変化に伴い石炭の燃料的価値が見直さ
れ、火力発電所用大型ボイラを始めとする事業所用大型
ボイラにおいても重油との混焼、もしくは石炭専焼のボ
イラが相当数使用されている。この場合石炭の燃焼の効
率化、制御性の向上等の観点から石炭を所定の粒径に粉
砕した後、これをバーナ部に気流輸送する方法が採用さ
れている。粉砕した石炭の粒径は種々のものがあるが、
通常は200メツシュ通過率か70〜80%程度の微粉
炭が使用されることが多い(以下微粉炭で説明する)。With recent changes in the fuel situation, the value of coal as a fuel has been reconsidered, and a considerable number of large boilers for business use, including large boilers for thermal power plants, are now using co-firing with heavy oil or only burning coal. In this case, from the viewpoint of improving the efficiency and controllability of coal combustion, a method is adopted in which the coal is pulverized to a predetermined particle size and then air-flow conveyed to the burner section. There are various particle sizes of crushed coal, but
Usually, pulverized coal with a 200 mesh passing rate or about 70 to 80% is often used (hereinafter, pulverized coal will be explained).
炉内に供給された微粉炭は炉内の熱により急激に加熱さ
れ短時間で燃焼するためストーカ焚き等に比較して格段
に制御性が向上する。Since the pulverized coal supplied into the furnace is rapidly heated by the heat inside the furnace and combusted in a short time, controllability is significantly improved compared to stoker firing, etc.
微粉炭は通常理論空気量の20〜50%の空気と共にバ
ーナから吹き出し燃焼し、バーナ周囲から供給される二
次空気により燃焼する。この場合気流輸送用の管路から
バーナに至る際に、流路が約90変更されるが、この流
路の変更により気流輸送される粉砕炭は慣性によって分
級され、バーナから不均一に噴似されて燃焼が不安定と
なったり制御が困難となったりする虞れがある。Pulverized coal is normally blown out from a burner and combusted with air in an amount of 20 to 50% of the theoretical air amount, and is combusted by secondary air supplied from around the burner. In this case, the flow path is changed approximately 90 times from the pneumatic transport pipe to the burner, but as a result of this change in flow path, the pulverized coal transported by air flow is classified by inertia, and is unevenly sprayed from the burner. There is a risk that combustion may become unstable or difficult to control.
このため発明者等は先にバーナ筒を構成する筒状体内に
旋回用ベーンを配置して気流に旋回力を与えて流路の変
更による微粉炭の分級効果を減殺するよう構成した。ま
たこの場合気流の旋回力により気流中の微粉炭は筒状体
の壁面側に遠心分離される傾向を生じるため、旋回ベー
ンの下流側にさらにベンチュリーを配置して気流の通過
面積を減少させ、粒子の均一な分布を図るようにしたも
のを提供している。このベンチュリーを配置したものは
粒子の均一な拡散に4 は一定の効果
を発揮することが確認されたが、今だ十分ではなく、全
体的には微粉炭を流路の・中心側に集中させる傾向を生
している。For this reason, the inventors first disposed swirling vanes in the cylindrical body constituting the burner cylinder to apply swirling force to the airflow, thereby reducing the effect of classifying the pulverized coal by changing the flow path. In addition, in this case, the pulverized coal in the airflow tends to be centrifuged toward the wall surface of the cylindrical body due to the swirling force of the airflow, so a venturi is further placed downstream of the swirling vane to reduce the area through which the airflow passes. We offer products designed to ensure uniform distribution of particles. It has been confirmed that this Venturi arrangement has a certain effect on the uniform diffusion of particles, but it is still not sufficient, and overall the pulverized coal is concentrated in the center of the flow path. It's creating a trend.
この発明の目的は上述した問題点に鑑み、微粉炭の分散
をより良好にして燃焼効率をさらに向上させた微粉炭燃
焼装置を提供することにある。SUMMARY OF THE INVENTION In view of the above-mentioned problems, an object of the present invention is to provide a pulverized coal combustion device in which pulverized coal is better dispersed and combustion efficiency is further improved.
要するにこの発明は、バーナ筒を構成する筒状体内にベ
ンチュリーを配置し、さらにベンチュリ設置部下流側に
角度調節可能なベーンを取り付はベンチュリーにおいて
筒状体中心側に集中する傾向を生じる微粉炭を再分散さ
せ、かつ要すればこのベーンを耐摩耗性の高いセラミッ
クスとする口とを特徴とするものである。In short, this invention arranges a venturi inside a cylindrical body constituting a burner cylinder, and furthermore, attaches an angle-adjustable vane to the downstream side of the venturi installation part. and, if necessary, the vane is made of highly wear-resistant ceramic.
以下この発明の実施例を図面により説明する。Embodiments of the present invention will be described below with reference to the drawings.
第1図において、1はバーナ筒を形成する筒状体であり
、2は同筒状体内に形成したベンチュリーである。3は
ベンチュリー出口部近傍に配置した微粉炭再拡散ベーン
であり、ベーン回動軸3aの端部にはベベルギヤ4を取
り付け、レバー5の操作によりベーン3の取り付は角度
が変更し得るよう構成しである。この場合、図示しない
リンク機構により複数枚のベーンは同時に作動する。な
お図示のベーンはベンチュリー内に配置したが、もとよ
りベンチュリ下流側の筒状体内に配置してもよい。また
このベーン3自体は微粉炭が激しく擦過してゆくため摩
耗が激しいので、耐摩耗性の高いセラミックスに ′よ
り形成するのが好ましい。次に符号1oは筒状体1とほ
ぼ同一軸心線上に配置した案内筒であり、前記ベーン3
はこの案内筒によりその一端が支持されることにな−る
。8は筒状体lと接続するエルボ、9はエルボ8内に配
置した支持筒であり、このうち支持筒9は前記案内筒1
oを支持している。11は案内筒10内に配置した重油
バーナであり、主として微粉炭点火用に使用する。In FIG. 1, 1 is a cylindrical body forming a burner cylinder, and 2 is a venturi formed within the cylindrical body. Reference numeral 3 denotes a pulverized coal re-diffusion vane placed near the outlet of the venturi, and a bevel gear 4 is attached to the end of the vane rotating shaft 3a, so that the angle at which the vane 3 is attached can be changed by operating a lever 5. It is. In this case, the plurality of vanes operate simultaneously by a link mechanism (not shown). Although the illustrated vanes are arranged inside the venturi, they may of course be arranged inside the cylindrical body on the downstream side of the venturi. Further, since the vane 3 itself is subject to severe wear due to the intense rubbing of the pulverized coal, it is preferable that the vane 3 be formed of highly wear-resistant ceramic. Next, reference numeral 1o denotes a guide cylinder disposed approximately on the same axis as the cylindrical body 1, and the vane 3
will be supported at one end by this guide tube. 8 is an elbow connected to the cylindrical body l; 9 is a support tube disposed inside the elbow 8; of these, the support tube 9 is connected to the guide tube 1;
I support o. Reference numeral 11 denotes a heavy oil burner disposed within the guide cylinder 10, which is mainly used for igniting pulverized coal.
12は支持筒9を支持する支持板としての作用も果す微
粉炭粒子混合用ベーンであり、エルボ下部から流入する
微粉炭含有気体に旋回力を与える。13はエルボ人口部
に設けた別の微粉炭混合用ベーンであり、かっ14はこ
のエルボ8に接続する微粉炭供給管である。Reference numeral 12 denotes a pulverized coal particle mixing vane that also functions as a support plate for supporting the support cylinder 9, and provides a swirling force to the pulverized coal-containing gas flowing from the lower part of the elbow. Reference numeral 13 indicates another pulverized coal mixing vane provided at the elbow portion, and numeral 14 indicates a pulverized coal supply pipe connected to this elbow 8.
ス供給用の通路であり、噴射口15aから噴射してバー
ナ火炎を2次空気からシールする。16はこの不活性ガ
ス用の通路に対して不活性ガスGを供給する管路である
。次に17は2次空気通路であり、不活性ガス通路の周
囲に形成しである。This is a passageway for supplying air, and the air is injected from the injection port 15a to seal the burner flame from secondary air. Reference numeral 16 denotes a pipe line for supplying inert gas G to this inert gas passage. Next, 17 is a secondary air passage, which is formed around the inert gas passage.
18は同2次空気通路入口に形成した流量調節板であり
、レバー19およびこれに接続するリンク20により開
度を調節して2次空気流量を調節する。21は二次空気
通路出口部に配置した空気旋回用ベーンであり、レバー
23.ベベルギヤ24を介してベーン回動用シャフト2
2を回動し、旋回用ベーン21の角度を調節して空気の
旋回力を調節する。なおこの場合各旋回ベーンは図示し
ないリンク機構によりレバー23の作動により同時に角
度変更を行なう。25は2次空気通路17のさらに外周
部に形成した3次空気通路であり、26は3次空気通路
入口に設けた流量調節板、27は同調節板回動用レバー
、28は3次空気通路出口部に配置した3次空気旋回用
のベーンであり、−29.ベベルギヤ30.ベーン回動
用シャフトにより角度調節を行ない、3次空気の旋回力
を調節する。Reference numeral 18 denotes a flow rate adjusting plate formed at the entrance of the secondary air passage, and its opening degree is adjusted by a lever 19 and a link 20 connected thereto to adjust the secondary air flow rate. Reference numeral 21 denotes an air swirling vane arranged at the outlet of the secondary air passage, and lever 23. Vane rotation shaft 2 via bevel gear 24
2 and adjust the angle of the swirling vane 21 to adjust the swirling force of the air. In this case, the angles of each of the rotating vanes are simultaneously changed by operating the lever 23 using a link mechanism (not shown). 25 is a tertiary air passage formed on the outer periphery of the secondary air passage 17, 26 is a flow rate adjustment plate provided at the entrance of the tertiary air passage, 27 is a lever for rotating the adjustment plate, and 28 is a tertiary air passage. A vane for swirling tertiary air placed at the outlet, -29. Bevel gear 30. The angle is adjusted using the vane rotating shaft to adjust the turning force of the tertiary air.
以上の装置において、微粉炭供給管14を上昇した微粉
炭含有気体はエルボ8.の人口において微粉炭混合用ベ
ーン13により旋回力を与えられてエルボ内に流入し、
その流路を約90°変更する。口の流路変更の場合、微
粉炭は慣性により流れの外側へと分級される傾向にある
が、ベーン13により旋回流が形成己れるので、分級は
抑制される傾向にある。流路変更を終った気流はさらに
別のベーン12により旋回力が与えられる。In the above apparatus, the pulverized coal-containing gas that has ascended through the pulverized coal supply pipe 14 is transferred to the elbow 8. The pulverized coal flows into the elbow after being given a swirling force by the pulverized coal mixing vane 13 at a population of
The flow path is changed by about 90°. In the case of changing the flow path at the mouth, the pulverized coal tends to be classified to the outside of the flow due to inertia, but since a swirling flow is formed by the vanes 13, the classification tends to be suppressed. A swirling force is applied to the airflow after changing the flow path by another vane 12.
これにより気流中の微粉炭は筒状体1の内周壁側に遠心
分離される傾向を生じる。第2図はこの微粉炭の分散状
態を示し、微粉炭Cは筒状体1の内壁面に近づくほど濃
度は高くなり、気流の進行方向に直交する面(第2図に
示す面)では分布が不均一となるが、筒状体内壁円周方
向4 においては均一に分散し、内壁
面の一部に高濃度域や低濃度域が形成されることはない
。この状態において気流はベンチュリに流入する。この
ベンチュリ2において気流の通過面積は減少し、気流進
行方向に直交する面においても微粉炭は均一に分布する
。しかしベンチュリ出口において、気流自体はA工の如
く拡散するが、微粉炭、特に粒子の径が大きいものを中
心に、Ap如く慣性により直進する傾向を生じ、ベンチ
ュリ出口では逆に微粉炭が案内筒10側に多く分布する
ようになる。このため、ベーン3により気流に再度旋回
力を与えて最終的に微粉炭を均一に分散させ、炉内に噴
射燃焼させる。なお、レバー5により、気流速度に対応
させてベーン3の角度を調節することにより微粉炭の分
散は常持良好に行なうことができる。As a result, the pulverized coal in the airflow tends to be centrifuged toward the inner circumferential wall of the cylindrical body 1. Figure 2 shows the state of dispersion of this pulverized coal. The concentration of pulverized coal C increases as it approaches the inner wall surface of the cylindrical body 1, and its distribution is However, it is uniformly dispersed in the circumferential direction 4 of the inner wall of the cylindrical body, and no high concentration area or low concentration area is formed in a part of the inner wall surface. In this state, airflow flows into the venturi. In this venturi 2, the area through which the airflow passes is reduced, and the pulverized coal is evenly distributed even on a plane perpendicular to the direction of airflow movement. However, at the outlet of the venturi, the airflow itself diffuses as shown in A, but the pulverized coal, especially those with large particle diameters, tends to travel straight due to inertia, as shown in Ap. It will be mostly distributed on the 10 side. For this reason, the vanes 3 apply swirling force to the airflow again to finally disperse the pulverized coal uniformly and inject it into the furnace for combustion. By adjusting the angle of the vane 3 using the lever 5 in accordance with the airflow velocity, the pulverized coal can be constantly dispersed.
この発明を実施することにより微粉炭の噴射速度の如何
に係りなく常時微粉炭を均一に分散しながら噴射するの
で常時安定した微粉炭燃焼を行なうことができる。By carrying out this invention, pulverized coal is always injected while being uniformly dispersed regardless of the injection speed of the pulverized coal, so that stable pulverized coal combustion can be performed at all times.
第1図はこの発明の実施例を示す微粉炭燃焼装置の断面
図、第2図は第1図のA−A線による断面図である。
l・・・・・・筒状体
2・・・・・・ベンチュリ
3・・・・・・微粉炭再拡散用ベー、ン3a・・・・・
・ベーン回動軸
4・・・・・・ベベルギヤ
5 ・・・・・・ し ノく−
8・・・・・・エルボ
10・・・・・・案内筒
13・・・・・・微粉炭拡散用ベーンFIG. 1 is a sectional view of a pulverized coal combustion apparatus showing an embodiment of the present invention, and FIG. 2 is a sectional view taken along line A--A in FIG. 1. l...Cylindrical body 2...Venturi 3...Pulverized coal re-diffusion vane 3a...
・Vane rotation shaft 4...Bevel gear 5...Shinoku-8...Elbow 10...Guide cylinder 13...Pulverized coal Diffusion vane
Claims (1)
炭を筒状体から噴射し燃焼するものにおいて、エルボ内
には微粉炭拡散用のベーンを形成し、かつベーン形成部
下流側の筒状体内部にはベンチュリを形成し、さらにベ
ンチュリ形成部下流側には取り付は角度調節可能に気流
再拡散用ベーンを配置したことを特徴とする均一拡散型
微粉炭燃焼装置。 2、 気流再拡散用ベーンの角度調節を、ベーンに取す
イ」りたベーン回動軸、およびベベルギヤを介してベー
ン回動軸に接続するレバーとから構成したことを特徴と
する特許請求の範囲第1項記載の均一拡散型微粉炭燃焼
装置。 3、 気流再拡散用ベーンをセラミックスにより形成し
たことを特徴とする特許請求の範囲第1項または第2項
記載の均一拡散型微粉炭燃焼装置。[Claims] 1. In a device in which the flow direction of pulverized coal is changed by an elbow and the pulverized coal is injected from a cylindrical body for combustion, a vane for dispersing the pulverized coal is formed in the elbow, and a vane for dispersing the pulverized coal is formed in the elbow. Uniform diffusion type pulverized coal combustion characterized by a venturi being formed inside the cylindrical body on the downstream side of the forming part, and a vane for airflow re-diffusion whose attachment angle is adjustable on the downstream side of the venturi forming part. Device. 2. The angle adjustment of the airflow re-diffusion vane is made up of a vane rotating shaft attached to the vane and a lever connected to the vane rotating shaft via a bevel gear. A uniform diffusion type pulverized coal combustion device according to scope 1. 3. A uniform diffusion type pulverized coal combustion device according to claim 1 or 2, wherein the airflow re-diffusion vane is made of ceramics.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10469982A JPS58224208A (en) | 1982-06-19 | 1982-06-19 | Uniform dispersion type pulverized coal firing equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10469982A JPS58224208A (en) | 1982-06-19 | 1982-06-19 | Uniform dispersion type pulverized coal firing equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58224208A true JPS58224208A (en) | 1983-12-26 |
JPH0262770B2 JPH0262770B2 (en) | 1990-12-26 |
Family
ID=14387723
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10469982A Granted JPS58224208A (en) | 1982-06-19 | 1982-06-19 | Uniform dispersion type pulverized coal firing equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58224208A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0926112A (en) * | 1995-07-14 | 1997-01-28 | Kawasaki Heavy Ind Ltd | Pulverized coal burner |
WO2017002675A1 (en) * | 2015-06-30 | 2017-01-05 | 三菱日立パワーシステムズ株式会社 | Solid fuel burner |
WO2019220597A1 (en) * | 2018-05-17 | 2019-11-21 | 三菱日立パワーシステムズ株式会社 | Support-sleeve protective member and solid fuel burner provided with same |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5236609A (en) * | 1975-09-16 | 1977-03-22 | Takeda Chem Ind Ltd | Process for preparation of alcohol and carbon monoxide |
JPS54159741A (en) * | 1978-06-07 | 1979-12-17 | Mitsubishi Heavy Ind Ltd | Powdery fuel burner |
-
1982
- 1982-06-19 JP JP10469982A patent/JPS58224208A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5236609A (en) * | 1975-09-16 | 1977-03-22 | Takeda Chem Ind Ltd | Process for preparation of alcohol and carbon monoxide |
JPS54159741A (en) * | 1978-06-07 | 1979-12-17 | Mitsubishi Heavy Ind Ltd | Powdery fuel burner |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0926112A (en) * | 1995-07-14 | 1997-01-28 | Kawasaki Heavy Ind Ltd | Pulverized coal burner |
WO2017002675A1 (en) * | 2015-06-30 | 2017-01-05 | 三菱日立パワーシステムズ株式会社 | Solid fuel burner |
JP2017015305A (en) * | 2015-06-30 | 2017-01-19 | 三菱日立パワーシステムズ株式会社 | Solid fuel burner |
US10731850B2 (en) | 2015-06-30 | 2020-08-04 | Mitsubishi Hitachi Power Systems, Ltd. | Solid fuel burner |
WO2019220597A1 (en) * | 2018-05-17 | 2019-11-21 | 三菱日立パワーシステムズ株式会社 | Support-sleeve protective member and solid fuel burner provided with same |
TWI715981B (en) * | 2018-05-17 | 2021-01-11 | 日商三菱動力股份有限公司 | Support sleeve protection member and solid fuel burner provided with the same |
AU2018423543B2 (en) * | 2018-05-17 | 2022-03-17 | Mitsubishi Power, Ltd. | Support-sleeve protective member and solid fuel burner provided with same |
Also Published As
Publication number | Publication date |
---|---|
JPH0262770B2 (en) | 1990-12-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3880570A (en) | Method and apparatus for reducing nitric in combustion furnaces | |
KR101633958B1 (en) | Method of using a suspension smelting furnace, a suspension smelting furnace, and a concentrate burner | |
CN1137340C (en) | Pulverized coal burner and method of using same | |
US3302596A (en) | Combustion device | |
US4428727A (en) | Burner for solid fuels | |
US4457241A (en) | Method of burning pulverized coal | |
US4479442A (en) | Venturi burner nozzle for pulverized coal | |
CZ291734B6 (en) | Combustion burner and combustion apparatus comprising such combustion burner | |
US3649211A (en) | Air augmented duct burner | |
CZ293962B6 (en) | Pulverized coal combustion burner | |
CN1032274C (en) | Burner of rotary kiln and combustion method thereof | |
GB1576345A (en) | Burner for powdered fuel | |
CZ130296A3 (en) | Process and apparatus for burning powder fuel | |
IE890701L (en) | Improvements in burners | |
JPS59131817A (en) | Assembly of burner register | |
US4902221A (en) | Burner assembly for coal fired furnaces | |
US4397295A (en) | Burner for burning pulverized fuel | |
JPS58224207A (en) | Pulverized coal firing equipment | |
US7810441B2 (en) | Coal burner assembly | |
JPS58224208A (en) | Uniform dispersion type pulverized coal firing equipment | |
US4201539A (en) | Flame forming burner | |
JPS6122105A (en) | Current distribution type burner assembly with absorber injector | |
JPS58193006A (en) | Burner for ground coke | |
CN106030210B (en) | Pulse burner and operation method for buring solid fuel | |
BG65334B1 (en) | Burner and method for the combustion of particulate fuel |