JPH085014A - Powder combustion burner - Google Patents

Powder combustion burner

Info

Publication number
JPH085014A
JPH085014A JP13600394A JP13600394A JPH085014A JP H085014 A JPH085014 A JP H085014A JP 13600394 A JP13600394 A JP 13600394A JP 13600394 A JP13600394 A JP 13600394A JP H085014 A JPH085014 A JP H085014A
Authority
JP
Japan
Prior art keywords
powder
heavy oil
secondary air
granular material
combustion burner
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.)
Pending
Application number
JP13600394A
Other languages
Japanese (ja)
Inventor
Katsuhide Murata
勝英 村田
Norio Tezuka
則雄 手塚
Yoichi Takahashi
洋一 高橋
Masaaki Nonaka
正昭 野中
Yoshihiro Kodama
嘉弘 児玉
Masamunenori Shirakawa
真宗規 白川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP13600394A priority Critical patent/JPH085014A/en
Publication of JPH085014A publication Critical patent/JPH085014A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 【目的】 廃プラスチック粉粒体等の低融点粉粒体であ
っても、バーナ先端部を閉塞することなく、安定燃焼す
ることができる粉体燃焼バーナを提供する。 【構成】 粉粒体を気相搬送し、火炉11内に噴出して
燃焼する粉体燃焼バーナであって、液体燃料cを噴霧す
る重油噴出管2と、重油噴出管2の外周に一次空気aの
流通路を形成する一次空気供給管3と、一次空気供給管
3の外周に二次空気bの流通路5を形成する二次空気供
給管4とを有する重油燃焼バーナの二次空気流路内に、
粉粒体を気相搬送して火炉11内に噴出する複数の粉粒
体噴出管6を設ける。
(57) [Abstract] [Purpose] To provide a powder combustion burner capable of stable combustion without blocking the tip of the burner even with powder particles having a low melting point such as waste plastic particles. [Composition] A powder combustion burner which carries powder particles in a gas phase and ejects and burns them into a furnace 11. A heavy oil jet pipe 2 for spraying a liquid fuel c, and primary air around the heavy oil jet pipe 2 are provided. A secondary air flow of a heavy oil combustion burner having a primary air supply pipe 3 forming a flow passage of a and a secondary air supply pipe 4 forming a flow passage 5 of secondary air b on the outer periphery of the primary air supply pipe 3. In the street,
A plurality of powdery or granular material ejection pipes 6 for carrying the powdery or granular material in a vapor phase and ejecting it into the furnace 11 are provided.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、粉体燃焼バーナに係
り、特に廃プラスチックを粉砕したプラスチック粉粒体
に代表される低融点粉粒体を燃焼する粉体燃焼バーナに
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a powder combustion burner, and more particularly to a powder combustion burner for combusting low melting point powder particles represented by plastic powder particles obtained by crushing waste plastic.

【0002】[0002]

【従来の技術】近年、産業の発達および多様化等に伴っ
て産業廃棄物または一般廃棄物として廃棄される廃プラ
スチックの量は年々増加の一途をたどっている。このよ
うな廃プラスチックの処理方法として、例えばマテリア
ル・リサイクル、サーマル・リサイクル、単純焼却、埋
め立て等があげられるが、単純焼却や埋め立ては、単に
その処理を目的とするものであり、廃プラスチックを有
効利用したことにはならない。一方、マテリアル・リサ
イクルできれば、最も好ましいが、多種多様のプラスチ
ックが混合した廃プラスチックを再生して製品化するた
めには多くの障害があり、しかもコストアップにつなが
るので、実用化は困難である。
2. Description of the Related Art In recent years, the amount of waste plastic discarded as industrial waste or general waste has been increasing year by year with the development and diversification of industry. Examples of methods for treating such waste plastics include material recycling, thermal recycling, simple incineration, and landfill, but simple incineration and landfill are merely for the purpose of treating the waste plastics. It has not been used. On the other hand, it is most preferable if the material can be recycled, but it is difficult to put it into practical use because there are many obstacles to recycling waste plastics mixed with various kinds of plastics to commercialize the waste plastics, and moreover, the cost is increased.

【0003】そこで、最も現実かつ有効な処理方法とし
て、廃プラスチックを燃料として燃焼し、その熱量を回
収するサーマル・リサイクル方法が種々提案されてい
る。プラスチックは元来、石油を主原料とする、石炭以
上の燃焼特性を有するものであり、たとえ廃プラスチッ
クであっても燃料という観点からみると高い商品価値を
有する。廃プラスチックのサーマル・リサイクル法の一
つとして、例えば廃プラスチックを粉砕して微粉砕粒と
し、これを気相搬送してバーナで燃焼し、ボイラで熱回
収する方法がある。
Therefore, as the most practical and effective treatment method, various thermal recycling methods have been proposed in which waste plastic is burned as fuel and the amount of heat thereof is recovered. Originally, plastics, which are mainly made of petroleum, have combustion characteristics superior to those of coal, and even waste plastics have high commercial value from the viewpoint of fuel. One of the thermal recycling methods for waste plastics is, for example, a method in which waste plastics are crushed into finely crushed particles, which are conveyed in a gas phase, burned in a burner, and recovered in a boiler.

【0004】ところで、廃プラスチックの粉粒体は、例
えば200〜300℃で溶融する低融点物質であり、こ
のような低融点の粉粒体を従来の重油バーナまたはスラ
リバーナを用いて燃焼しようとすると、火炎やバーナタ
イルからの輻射熱等によって前記粉粒体が融点以上に加
熱されて溶融し、バーナ先端部を閉塞したり、大きい塊
または薄片状の溶融物となってバーナ先端部から落下す
る間に、または火炉内を浮遊する間に表面積不足のため
に不完全燃焼するという問題が生じる。
By the way, the waste plastic powder and granules are low-melting substances that melt at, for example, 200 to 300 ° C., and if such low-melting powder granules are to be burned using a conventional heavy oil burner or slurry burner. While the powder or granules are heated to a temperature higher than the melting point and melted by flames or radiant heat from burner tiles, the burner tip is blocked, or a large lump or flaky melt is dropped from the burner tip. However, the problem of incomplete combustion occurs due to insufficient surface area while floating in the furnace.

【0005】このため、低融点粉粒体を安定燃焼するた
めの粉体燃焼バーナの開発が望まれている。
Therefore, there is a demand for the development of a powder combustion burner for stably burning low melting point powder particles.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、上記
要請に鑑み、例えば廃プラスチック粉粒体等の低融点の
粉粒体であってもバーナ先端部を閉塞することなく、長
期間安定燃焼することができる粉体燃焼バーナを提供す
ることにある。
SUMMARY OF THE INVENTION In view of the above demands, an object of the present invention is to stabilize a long-term powder particle without blocking the burner tip even if the powder particle has a low melting point, such as waste plastic powder. It is to provide a powder combustion burner capable of burning.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
本発明者は、既設の重油炊ボイラ装置を利用して粉粒体
を燃焼することが最も望ましいと考え、鋭意研究した結
果、重油バーナの二次空気流路内に、粉粒体を気相搬送
して火炉内に噴出する粉体ノズルを設けることにより、
前記二次空気による冷却効果を利用して粉粒体を溶融さ
せることなく搬送して火炉内に噴出できることを見出
し、本発明に到達した。
In order to achieve the above object, the inventor of the present invention thought that it is most desirable to combust powders using an existing heavy oil cooking boiler device, and as a result of earnest research, a heavy oil burner was found. In the secondary air flow path of, by providing a powder nozzle that carries the powder particles in a gas phase and ejects them into the furnace,
The present invention has been accomplished by finding that powder particles can be transported and jetted into a furnace without melting by utilizing the cooling effect of the secondary air.

【0008】すなわち、本願で特許請求される発明は、
以下のとおりである。 (1)粉粒体を気相搬送し、火炉内に噴出して燃焼する
粉体燃焼バーナであって、液体燃料を噴霧する重油噴出
管と、該重油噴出管の外周に一次空気流路を形成する一
次空気供給管と、該一次空気供給管の外周に二次空気流
路を形成する二次空気供給管とを有する重油燃焼バーナ
の前記二次空気流路内に、粉粒体を気相搬送して火炉内
に噴出する複数の粉粒体噴出管を等間隔に設けたことを
特徴とする粉体燃焼バーナ。
That is, the invention claimed in this application is as follows:
It is as follows. (1) A powder combustion burner that conveys powdery particles in a gas phase and injects and burns them into a furnace, wherein a heavy oil ejection pipe for spraying liquid fuel and a primary air flow passage are provided around the outer periphery of the heavy oil ejection pipe. In the secondary air flow passage of a heavy oil combustion burner having a primary air supply pipe to be formed and a secondary air supply pipe forming a secondary air flow passage on the outer periphery of the primary air supply pipe, the powdery particles are vaporized. A powder combustion burner, characterized in that a plurality of powder and granular material ejection pipes for carrying phases and ejecting them into a furnace are provided at equal intervals.

【0009】[0009]

【作用】重油バーナの二次空気流路内に、粉粒体を気相
搬送して火炉内に噴出する複数の粉粒体噴出管を配置し
たことにより、火炎やバーナタイルからの強い輻射熱に
よって溶融され易い、例えば廃プラスチックを粉砕した
低融点粉粒体であっても、前記二次空気流路を流通する
二次空気によって溶融温度以下に冷却しつつ搬送して火
炉内に噴射することができるので、粉粒体噴出管内にお
ける噴出前の粉粒体の溶融が防止される。従って粉粒体
が溶融することによる噴出管の閉塞、塊状化による不完
全燃焼等のトラブルを防止して前記粉粒体を長期間安定
に燃焼することができる。
[Function] By arranging a plurality of powdery particles ejecting pipes that carry the powdery particles in the vapor phase and eject them into the furnace in the secondary air flow path of the heavy oil burner, strong radiation heat from the flame or burner tile It is easy to melt, for example, even if it is a low melting point granular material crushed from waste plastic, it can be conveyed while being cooled to a melting temperature or lower by the secondary air flowing through the secondary air channel and injected into the furnace. Therefore, it is possible to prevent the powder or granular material from being melted in the powder or granular material ejection pipe before being ejected. Therefore, it is possible to prevent trouble such as blockage of the ejection pipe due to melting of the powder and granules and incomplete combustion due to agglomeration, and the powder and granules can be stably burned for a long period of time.

【0010】本発明において、粉粒体噴出管の噴出口は
重油噴出管の噴出口よりもわずかに内側、すなわち上流
側に開口することが好ましい。これによって粉粒体先端
部の輻射熱による加熱を防止して噴出される前の粉粒体
の溶融を有効に防止することができる。本発明におい
て、粉粒体噴出管の噴出口の内周面にセラミックをコー
ティングしたり、前記噴出口の形状を断面円弧状にする
ことが好ましい。これによって噴出口における粉粒体の
閉塞防止効果が向上する。また、粉粒体噴出管を二重管
にして水等の冷却流体で冷却することもできる。粉粒体
噴出管の数は特に限定されないが、6本または8本等の
偶数であることが好ましく、二次空気流路の全円周に等
間隔に配置することが好ましい。
In the present invention, it is preferable that the ejection port of the powder and granular material ejection pipe is opened slightly inward of the ejection port of the heavy oil ejection pipe, that is, upstream. As a result, it is possible to prevent the tip portion of the powder or granules from being heated by the radiant heat and effectively prevent the powder or granules from being melted before being ejected. In the present invention, it is preferable that the inner peripheral surface of the ejection port of the powder or granular material ejection pipe is coated with ceramic, or the ejection port has an arc-shaped cross section. As a result, the effect of preventing blockage of the powder or granules at the ejection port is improved. Further, it is also possible to make the powder and granular material ejection pipe into a double pipe and cool it with a cooling fluid such as water. Although the number of the powder and granular material ejection pipes is not particularly limited, it is preferably an even number such as 6 or 8, and it is preferable to dispose the powder and granular material ejection pipes at equal intervals on the entire circumference of the secondary air flow path.

【0011】[0011]

【実施例】次に本発明を実施例によってさらに詳細に説
明する。図1は、本発明である粉体燃焼バーナの一実施
例を示す縦断面図、図2は、図1のA方向視図である。
図において、この粉体燃焼バーナは、重油噴出口1を有
する重油噴出管2と、該重油噴出管2の外周に一次空気
aの流路を形成する一次空気供給管3と、該一次空気供
給管3の先端部に設けられたスワラー8と、前記一次空
気供給管3の外周に二次空気bの流路を形成する二次空
気供給管4と、該二次空気供給管4で形成される二次空
気流路5内に、円周方向に等間隔に配置された8本の粉
粒体噴出管6と、該粉粒体噴出管6の先端部の粉粒体噴
出口7とから主として構成されている。9は着火バー
ナ、10はのぞき窓、11は火炉、14はバーナタイル
である。
EXAMPLES Next, the present invention will be described in more detail by way of examples. FIG. 1 is a longitudinal sectional view showing an embodiment of the powder combustion burner according to the present invention, and FIG. 2 is a view as seen from the direction A in FIG.
In the figure, this powder combustion burner includes a heavy oil ejection pipe 2 having a heavy oil ejection port 1, a primary air supply pipe 3 forming a flow path of primary air a on the outer periphery of the heavy oil ejection pipe 2, and the primary air supply. The swirler 8 provided at the tip of the pipe 3, the secondary air supply pipe 4 forming a flow path of the secondary air b on the outer circumference of the primary air supply pipe 3, and the secondary air supply pipe 4 In the secondary air flow path 5, the eight powdery or granular material ejection pipes 6 arranged at equal intervals in the circumferential direction and the powdery or granular material ejection port 7 at the tip of the powdery or granular material ejection pipe 6 are provided. It is mainly composed. Reference numeral 9 is an ignition burner, 10 is a sight glass, 11 is a furnace, and 14 is a burner tile.

【0012】このような構成において、一次空気供給管
3および二次空気供給管4にそれぞれ所定量の一次空気
aおよび二次空気bが供給され、この状態で、所定量の
液体燃料c、例えばC重油が重油噴出管2を経て噴出口
1から火炉11内に噴射され、前記一次空気a、および
スワラー8で旋回流を形成する二次空気bと混合し、着
火バーナ9によって着火されて燃焼する。このようにし
て着火された液体燃料cの燃焼が安定した後、例えばポ
リエチレン、ポリプロピレン、ポリスチレン等の廃プラ
スチックを、例えば1000μm以下に粉砕した廃プラ
スチック粉粒体と空気とを混合した気−固混合物dが、
粉粒体噴出管6を経て、二次空気流路5を流通する二次
空気bで溶融温度以下、例えば200〜300℃以下に
冷却されながら流通し、粉粒体噴出口7から火炉11内
に噴射されて燃焼する。
In such a configuration, the primary air supply pipe 3 and the secondary air supply pipe 4 are respectively supplied with a predetermined amount of primary air a and secondary air b, and in this state, a predetermined amount of liquid fuel c, for example, C heavy oil is injected from the jet port 1 into the furnace 11 through the heavy oil jet pipe 2, mixed with the primary air a and the secondary air b forming a swirling flow in the swirler 8, and ignited by the ignition burner 9 and burned. To do. After the combustion of the liquid fuel c ignited in this way becomes stable, a waste-plastic mixture obtained by pulverizing waste plastics such as polyethylene, polypropylene, polystyrene, etc., for example, to a size of 1000 μm or less and air and a solid-air mixture are mixed. d is
The secondary air b flowing through the secondary air flow path 5 through the powder and granular material ejection pipe 6 flows while being cooled to a melting temperature or lower, for example, 200 to 300 ° C. or lower, and flows from the powder or granular material ejection port 7 into the furnace 11. It is injected and burned.

【0013】本実施例によれば、重油バーナを改良して
粉粒体を燃焼するようにしたことにより、既設のボイラ
装置を有効に利用して、例えば廃プラスチック等の低融
点粉粒体を燃焼することができるので、特別の設備投資
を必要とすることなく、廃プラスチックの粉体燃料化技
術に対応することができる。本実施例によれば、重油バ
ーナの二次空気流路5内に、複数の粉粒体噴出管6を設
けたことにより、廃プラスチック粉粒体と空気とを混合
した気−固混合物dを前記廃プラスチック粉粒体の融点
以下の温度に保ちつつ搬送して噴出口7から火炉11に
噴出することができるので、廃プラスチックの溶融によ
る粉粒体噴出管6および粉粒体噴出口7の閉塞を防止し
て前記廃プラスチック粉粒体を安定燃焼することができ
る。
According to the present embodiment, the heavy oil burner is improved so that the granular material is burned, so that the existing boiler device can be effectively used to remove the granular material having a low melting point such as waste plastic. Since it can be combusted, it is possible to deal with the technology for converting waste plastic into powder fuel without requiring any special capital investment. According to the present embodiment, by providing the plurality of powder and granular material ejection pipes 6 in the secondary air flow path 5 of the heavy oil burner, the gas-solid mixture d in which the waste plastic powder and granular material is mixed with the air is produced. Since the waste plastic powder can be conveyed while being kept at a temperature equal to or lower than the melting point of the waste plastic and ejected from the ejection port 7 to the furnace 11, the powder ejection pipe 6 and the powder ejection port 7 of the waste plastic are melted. It is possible to prevent clogging and stably burn the waste plastic particles.

【0014】本実施例において、粉粒体の燃焼が安定し
た後は、液体燃料cの供給量を所定量だけ減少させるこ
とが好ましい。
In the present embodiment, it is preferable to reduce the supply amount of the liquid fuel c by a predetermined amount after the combustion of the powdery or granular material is stabilized.

【0015】[0015]

【発明の効果】本発明によれば、重油バーナの二次空気
流路内に複数の粉粒体噴出管を配置したことにより、低
融点の粉粒体であっても、溶融することなく気相搬送し
て火炉内に噴射することができるので、粉粒体噴出管お
よび噴出口の閉塞を防止して粉粒体を安定に完全燃焼す
ることができる。
EFFECTS OF THE INVENTION According to the present invention, by arranging a plurality of powder and granular material ejection pipes in the secondary air flow path of a heavy oil burner, even a powder and granular material having a low melting point can be vaporized without melting. Since the particles can be phase-conveyed and injected into the furnace, it is possible to prevent the powder and granular material ejection pipe and the ejection port from being blocked, and to stably and completely combust the powder and granular material.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例である粉体燃焼バーナの縦断
面図。
FIG. 1 is a vertical sectional view of a powder combustion burner which is an embodiment of the present invention.

【図2】図1のA方向視図。FIG. 2 is a view from the direction A in FIG.

【符号の説明】[Explanation of symbols]

1:重油噴出口、2:重油噴出管、3:一次空気供給
管、4:二次空気供給管、5:二次空気流路、6:粉粒
体噴出管、7:粉粒体噴出口、8:スワラー、9:着火
バーナ、10:のぞき窓、11:火炉。
1: Heavy oil ejection port, 2: Heavy oil ejection pipe, 3: Primary air supply pipe, 4: Secondary air supply pipe, 5: Secondary air flow path, 6: Powder particle ejection pipe, 7: Particle ejection port , 8: swirler, 9: ignition burner, 10: sight glass, 11: furnace.

フロントページの続き (72)発明者 野中 正昭 岡山県玉野市玉3丁目1番1号 三井造船 株式会社玉野事業所内 (72)発明者 児玉 嘉弘 岡山県玉野市玉3丁目1番1号 三井造船 株式会社玉野事業所内 (72)発明者 白川 真宗規 岡山県玉野市玉3丁目1番1号 三井造船 株式会社玉野事業所内Front Page Continuation (72) Inventor Masaaki Nonaka 3-1-1 Tam, Tamano-shi, Okayama Mitsui Engineering & Ships Co., Ltd. Tamano Works Co., Ltd. (72) Inventor Yoshihiro Kodama 3-1-1 Tamama-shi, Tamano-shi, Okayama Company Tamano Works (72) Inventor Masanori Shirakawa 3-1-1 Tam, Tamano City, Okayama Prefecture Mitsui Engineering & Shipbuilding Co., Ltd. Tamano Works

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 粉粒体を気相搬送し、火炉内に噴出して
燃焼する粉体燃焼バーナであって、液体燃料を噴霧する
重油噴出管と、該重油噴出管の外周に一次空気流路を形
成する一次空気供給管と、該一次空気供給管の外周に二
次空気流路を形成する二次空気供給管とを有する重油燃
焼バーナの前記二次空気流路内に、粉粒体を気相搬送し
て火炉内に噴出する複数の粉粒体噴出管を等間隔に設け
たことを特徴とする粉体燃焼バーナ。
1. A powder combustion burner which carries powder particles in a gas phase and jets and burns them into a furnace, wherein a heavy oil jet pipe for spraying liquid fuel and a primary air flow around the outer periphery of the heavy oil jet pipe. In the secondary air flow passage of a heavy oil combustion burner having a primary air supply pipe forming a passage, and a secondary air supply pipe forming a secondary air passage on the outer periphery of the primary air supply pipe, a granular material A powder combustion burner, characterized in that a plurality of powder and granular material ejection pipes for carrying the material in a gas phase and ejecting it into a furnace are provided at equal intervals.
JP13600394A 1994-06-17 1994-06-17 Powder combustion burner Pending JPH085014A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13600394A JPH085014A (en) 1994-06-17 1994-06-17 Powder combustion burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13600394A JPH085014A (en) 1994-06-17 1994-06-17 Powder combustion burner

Publications (1)

Publication Number Publication Date
JPH085014A true JPH085014A (en) 1996-01-12

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP13600394A Pending JPH085014A (en) 1994-06-17 1994-06-17 Powder combustion burner

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Country Link
JP (1) JPH085014A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110500591A (en) * 2019-08-09 2019-11-26 南京绿帝环保能源科技有限公司 The fuel type coloured glaze state processing unit and its processing method of dangerous waste material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110500591A (en) * 2019-08-09 2019-11-26 南京绿帝环保能源科技有限公司 The fuel type coloured glaze state processing unit and its processing method of dangerous waste material

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