JPS59228964A - Fluid diffuser - Google Patents

Fluid diffuser

Info

Publication number
JPS59228964A
JPS59228964A JP10176383A JP10176383A JPS59228964A JP S59228964 A JPS59228964 A JP S59228964A JP 10176383 A JP10176383 A JP 10176383A JP 10176383 A JP10176383 A JP 10176383A JP S59228964 A JPS59228964 A JP S59228964A
Authority
JP
Japan
Prior art keywords
flow
fluid
nozzle
dispersion
fluid distributor
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
Application number
JP10176383A
Other languages
Japanese (ja)
Other versions
JPS6341625B2 (en
Inventor
Toshiharu Kumazawa
俊治 熊沢
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.)
Mitsubishi Precision Co Ltd
Original Assignee
Mitsubishi Precision 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 Mitsubishi Precision Co Ltd filed Critical Mitsubishi Precision Co Ltd
Priority to JP10176383A priority Critical patent/JPS59228964A/en
Publication of JPS59228964A publication Critical patent/JPS59228964A/en
Publication of JPS6341625B2 publication Critical patent/JPS6341625B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To stabilize the spraying condition of fuel into a combustion furnace and to prevent sticking and accumulation of carbon by forming the guiding surface of a fluid diffuser into a specific shape. CONSTITUTION:The gaseous mixture composed of gas and liquid ejected from a nozzle 1 collides and reflects against and on a circular collision surface 4 and collides against the succeedingly ejected flow between an ejecting hole 1a and circular collision surface 4, thereby forming diffusing flow S1. The flow S1 is diffused stably at a wide angle alpha by the guiding effect of a divergent diffusing and guiding surface 5. The flow S1 burns in a furnace F and a part of the high temp. gas flows backward in the form of circulating flow S2 along the spherical surface of a projecting end 6 and sticks on the spherical surface, thereby removing unburned particles which are intruded into the flow S1. The intruded flow S2 is the high temp. gas contg. a flame and therefore the ignition and flame stabilization of the flow S1 are continuously and stably accomplished.

Description

【発明の詳細な説明】 技術分野 本発明は、ノズルから噴出する流体を衝突させて薄膜広
角に分散させる流体分散器に関し、特に気液混合燃料流
体を分散流に形成する流体分散器に関する。
TECHNICAL FIELD The present invention relates to a fluid distributor that causes fluid ejected from a nozzle to collide and disperse in a thin film over a wide angle, and more particularly to a fluid distributor that forms a gas-liquid mixed fuel fluid into a dispersed flow.

従来技術 ノズルの噴孔から噴出する流体をそのノズル噴孔の下流
側に設けた流体分散器に衝突反射させ。
Prior Art Fluid ejected from the nozzle hole of a nozzle collides with and is reflected by a fluid distributor provided downstream of the nozzle hole.

ノズル噴孔からの後続の噴出流体と衝突させて外部へ薄
膜広角開傘状に分散させる方法および構造は、特許第1
008187号および特許第941825号として公知
である。この従来の流体分散器は分散流を下流に向けて
案内する案内面が無く、故に分散流が流体分散器を離れ
た瞬間に1分散流内側の流体粒子が流体力学的に発生す
る分散器外周の負圧に巻き込まれて分散器に付着し、従
って流体が気液混合燃料流体の場合にあっては、周囲の
燃焼熱によって乾燥したカーボン粒子となって付着堆積
し、それが保炎、安定燃焼をさまたげる結果を招くこと
になる。
The method and structure for colliding with the subsequent ejected fluid from the nozzle nozzle hole and dispersing it to the outside in a thin film wide-angle umbrella shape are disclosed in Patent No. 1.
No. 008187 and patent no. 941825. This conventional fluid disperser does not have a guide surface that guides the dispersed flow downstream, so the moment the dispersed flow leaves the fluid disperser, fluid particles inside one dispersed flow are hydrodynamically generated around the outer circumference of the disperser. If the fluid is a gas-liquid mixed fuel fluid, the surrounding combustion heat will cause it to become dried carbon particles that will adhere to the disperser and become flame-holding and stable. This will result in hindering combustion.

発明の目的 依って本発明の目的は、上記従来の流体分散器を改善し
て特に気液混合燃料の噴霧分散用に適し。
OBJECTS OF THE INVENTION Accordingly, it is an object of the present invention to improve the above-mentioned conventional fluid dispersion device so as to be particularly suitable for spray dispersion of gas-liquid mixed fuel.

燃焼炉中への燃料噴霧分散形状の安定化と、燃料中に含
まれるカーボンの流体分散器外周への付着堆積を防止す
ることができる流体分散器を提供することにある。
It is an object of the present invention to provide a fluid distributor that can stabilize the shape of fuel spray dispersion into a combustion furnace and prevent carbon contained in the fuel from adhering to the outer periphery of the fluid distributor.

発明の構成1作用効果 本発明によれば、流体噴出ノズルの下流側に設けた流体
分散器において、前記流体噴出ノズルから噴出する流体
が衝突する円形衝突面を前記ノズルの噴孔と略同心に設
け、かつ前記円形衝突面の外周から下流に向けて略錐形
に拡開する傾面として形成されると共に該傾面の成す角
度を予め選定した分散角度に定めた分散案内面を設け、
また前記分散案内面の下流側に連設されかつ下流方向に
向けて突出させた略球形の突出面として形成され前記分
散流の一部逆流循環流を密着流動させる循環案内面を設
けたことを特徴とする流体分散器が提供される。
Structure 1 of the Invention Effects According to the present invention, in the fluid distributor provided on the downstream side of a fluid ejection nozzle, a circular collision surface on which fluid ejected from the fluid ejection nozzle collides is approximately concentric with the nozzle hole of the nozzle. a dispersion guide surface formed as a substantially conical inclined surface expanding downstream from the outer periphery of the circular collision surface, and with the angle formed by the inclined surface set to a preselected dispersion angle;
Further, a circulation guide surface is provided which is connected to the downstream side of the dispersion guide surface and is formed as a substantially spherical protruding surface that protrudes toward the downstream direction, and allows a part of the dispersion flow to closely flow the reverse circulation flow. A fluid distributor is provided.

上記のように構成した本発明の流体分散器を有する流体
噴出ノズルを燃焼炉中に設置し、気液混合燃料の噴霧分
散に用いれば、燃焼炉中への燃料噴霧分散形状の安定化
を達成し、かつ分散流によって流体分散器の周囲および
下流側に流体力学的に生ずる負圧領域への一部燃料分散
流の逆流循環流を上記流体分散器の周囲に沿って剥離す
ることなく案内流動させ、流体分散器外周に付着した異
物を取除き、上記燃料分散流中へ再び巻き込み。
If a fluid ejection nozzle having the fluid distributor of the present invention configured as described above is installed in a combustion furnace and used for spray dispersion of gas-liquid mixed fuel, stabilization of the shape of fuel spray dispersion in the combustion furnace can be achieved. In addition, the reverse circulation flow of a part of the fuel dispersed flow to the negative pressure region hydrodynamically generated around and downstream of the fluid distributor due to the dispersed flow is guided without separation along the periphery of the fluid distributor. Remove foreign matter attached to the outer periphery of the fluid disperser and re-involve it into the fuel dispersed flow.

合流させるから燃料に含まれるカーボンの流体分散器外
周への付着を防止することができ、究極的に良好な燃焼
作用を維持できるのである。以下。
By merging them together, it is possible to prevent the carbon contained in the fuel from adhering to the outer periphery of the fluid distributor, and ultimately to maintain a good combustion effect. below.

本発明を添付図面に示す実施例に基いて更に詳細に説明
する。
The present invention will be explained in more detail based on embodiments shown in the accompanying drawings.

さて、第1図において、1は流体、っまシ空気または蒸
気と燃料粒子との気液混合流体Fを噴出する噴孔1aを
有したノズルであり、その中心軸線に沿って1本発明に
よる流体分散器2を支持する支持棒3が装入され、内奥
部で適宜の保持具。
Now, in FIG. 1, reference numeral 1 denotes a nozzle having a nozzle hole 1a for ejecting a fluid, pure air, or a gas-liquid mixed fluid F of steam and fuel particles. A support rod 3 supporting the fluid distributor 2 is inserted, and a suitable holder is inserted deep inside.

例えばスパイダ形保持具によ如係止されている。For example, it is locked by a spider-shaped holder.

流体分散器2は従ってノズル1の中心軸線と同心に噴孔
1aの下流側に設けられ、空洞0を有する衝突面4.こ
の衝突面4の外周から下流に向って末広がシに形成され
だ略錐形の分散案内面5およびその分散案内面5の更に
下流側に突出形状に設けられた球形の案内先端6の各部
を具備している。
The fluid distributor 2 is therefore provided on the downstream side of the nozzle hole 1a concentrically with the central axis of the nozzle 1 and has an impingement surface 4. Each part of a substantially conical dispersion guide surface 5 which is formed in a shape that widens toward the downstream from the outer periphery of the collision surface 4, and a spherical guide tip 6 provided in a protruding shape further downstream of the dispersion guide surface 5. Equipped with:

上述の構成によれば、第2図に示すように、ノズル1か
ら噴出する気液混合流体Fは円形の衝突面4に衝突反射
し、噴孔1aと円形衝突面4との間で後続の噴出流に衝
突して分散作用を受け1分散流Slとなる。この分散流
SRは分散案内面5によって所望の分散角αを保って安
定に分散する。
According to the above configuration, as shown in FIG. 2, the gas-liquid mixed fluid F ejected from the nozzle 1 collides with the circular collision surface 4 and is reflected, and the subsequent collision occurs between the nozzle hole 1a and the circular collision surface 4. It collides with the jet flow and undergoes a dispersion action, becoming one dispersed flow Sl. This dispersed flow SR is stably dispersed by the dispersion guide surface 5 while maintaining a desired dispersion angle α.

つまり末広がシの分散案内面5の案内作用で広角に安定
に進むのである。炉内Pにおいては1分散流S1は燃焼
し、燃焼後の高温ガスの一部が循環流S2となって突出
先端6の球面に沿って逆流し、該球面に付着した未燃粒
子を除去してS、に巻き込まれる。この逆流循環流S2
は、流体分散器2の周囲および下流側に発生する負圧領
域に向って高温ガスの一部が流れ込むことにより生ずる
もので、該高温ガスの循環流S2が突出先端6の球面に
沿って剥離することなく流れるからカーボン粒子の付着
を防止し、かつ付着したものはこれを除去するものであ
る。なお、球面形状に依れば、燃料粒子が付着する面積
(投影面@)を、可及的に炉内F側が大きくなるような
形状として、付着未燃粒子の焼却に必要な熱を吸収し易
くする作用も呈する。さて、気液混合流体slに巻き込
まれた循環流S2は火炎を含む高温ガスであるから1分
散流810着大保炎を連続的に安定におこなわしめる。
In other words, the guide action of the dispersion guide surface 5 that widens at the end allows it to move stably over a wide angle. In the furnace P, one dispersed flow S1 is burned, and a part of the high-temperature gas after combustion becomes a circulating flow S2 and flows back along the spherical surface of the protruding tip 6, removing unburned particles attached to the spherical surface. I get caught up in S. This reverse circulation flow S2
This occurs when a part of the high temperature gas flows toward the negative pressure area generated around and downstream of the fluid distributor 2, and the circulating flow S2 of the high temperature gas is separated along the spherical surface of the protruding tip 6. Since it flows without causing any damage, it prevents the adhesion of carbon particles and removes any adhering particles. In addition, according to the spherical shape, the area on which fuel particles adhere (projected surface @) is shaped so that it is as large as possible on the F side of the furnace to absorb the heat necessary to incinerate the attached unburned particles. It also has the effect of making it easier. Now, since the circulating flow S2 involved in the gas-liquid mixed fluid sl is a high-temperature gas containing a flame, it is possible to continuously and stably perform one dispersion flow 810 and a large holding flame.

ここで従来の流体分散器を参照すると、第3図に示すよ
うに、該流体分散器7は流体分散案内面を有しない。故
に1分散流sl′の内側に存在する粒子が衝突面8の外
周端9において1分散流B11本流から分流S3の如く
飛散して周囲の負圧領域に巻き込まれる。従ってその分
流s3中の燃料粒子が流体分散器7の周囲に付着し、ま
た流体分散器7の下流側の突出先端が筒状で球形面を有
しないから、循環流82′が流体分散器7の周囲に沿っ
て流れる作用もなく、剥離してしまうので1周囲に付着
した燃料粒子やカーボン粒子を除去することは困難とな
シ、第4図に示すようにカーボン粒子の堆積腕10が発
生成長し、保炎安定燃焼をさまたげる結果になる。
Referring now to a conventional fluid distributor, as shown in FIG. 3, the fluid distributor 7 does not have a fluid distribution guide surface. Therefore, the particles existing inside the single dispersion flow sl' are scattered from the main flow of the single dispersion flow B11 at the outer circumferential end 9 of the collision surface 8 like a branch flow S3, and are drawn into the surrounding negative pressure region. Therefore, the fuel particles in the branched flow s3 adhere to the periphery of the fluid distributor 7, and since the protruding tip on the downstream side of the fluid distributor 7 is cylindrical and does not have a spherical surface, the circulating flow 82' is transferred to the fluid distributor 7. It is difficult to remove the fuel particles and carbon particles attached to the surrounding area because the fuel particles and carbon particles peel off without flowing along the periphery of the carbon particle, and as shown in FIG. This results in growth and hinders flame-holding and stable combustion.

以上の説明から明らかなように1本発明によれば、流体
分散器が略錐形の分散案内面と球面形状を有した下流側
の突出案内面とを具備することによシ気液混合流として
噴出した燃料が炉内で安定かつ効率よく燃焼する分散v
it霧流に形成され、かつ突出案内面に沿って剥離を生
ずることなく高温ガスの一部が循環するのでカーボン粒
子の付着防止並びに付着除去を行いつつ1着火保炎を効
果的に達成して燃焼炉における完全燃焼を達成するので
ある。なお1本発明による流体分散器における衝突面は
特許第1008187号又は第941825号に開示さ
れた平面もしくは空洞を具えている構成のものに対して
も有効に適用できることは言うまでもない。また分散案
内面5がなす分散角度αは炉内容積等に応じて適宜選択
されるものである。
As is clear from the above description, according to the present invention, the fluid disperser is provided with a substantially conical dispersion guide surface and a protruding guide surface on the downstream side having a spherical shape. Dispersion v where the fuel ejected as combusts stably and efficiently in the furnace
It is formed into a mist flow, and a part of the high-temperature gas circulates along the protruding guide surface without causing separation, effectively achieving ignition and flame holding while preventing and removing carbon particles. Complete combustion is achieved in the combustion furnace. It goes without saying that the collision surface in the fluid distributor according to the present invention can also be effectively applied to those having a flat surface or a hollow structure as disclosed in Japanese Patent No. 1008187 or No. 941825. Further, the dispersion angle α formed by the dispersion guide surface 5 is appropriately selected depending on the internal volume of the furnace and the like.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明による流体分散器の実施例における縦断
面図、第2図は同流体分散器の作用を説明する断面図、
第3図は従来の流体分散器の一例を示す縦断面図、第4
図は同従来の流体分散器に付着するカーボン粒子の堆積
状態を示す断面図。 1・・・ノズル、    1a・・・噴孔。 2・・・流体分散器、  4・・・衝突面。 5・・・分散案内面、   6・・・案内先端、7・・
・従来の流体分散器、F・・・気液混合流体。 81・・・分散流、     82・・・循環流。 特許出願人 三菱グレシジョン株式会社 特許出願代理人 弁理士 青 木    朗 弁理士西舘和之 弁理士 中 山 恭 介 弁理士 山 口  昭 之 第1 回 一−ツー 一一一〜−一 第4図 n
FIG. 1 is a longitudinal sectional view of an embodiment of the fluid distributor according to the present invention, and FIG. 2 is a sectional view illustrating the action of the fluid distributor.
Figure 3 is a vertical sectional view showing an example of a conventional fluid distributor;
The figure is a cross-sectional view showing the state of accumulation of carbon particles attached to the conventional fluid disperser. 1... Nozzle, 1a... Nozzle hole. 2... Fluid disperser, 4... Collision surface. 5... Dispersion guide surface, 6... Guide tip, 7...
- Conventional fluid disperser, F... gas-liquid mixed fluid. 81... Dispersed flow, 82... Circulating flow. Patent Applicant Mitsubishi Grecision Co., Ltd. Patent Application Agent Akira Aoki Patent Attorney Kazuyuki Nishidate Patent Attorney Kyo Nakayama Patent Attorney Akira Yamaguchi 1st Part 1-2 111--1 Figure 4 n

Claims (1)

【特許請求の範囲】 1、流体噴出ノズルの下流側に設けた流体分散器におい
て、前記ノズルから噴出する流体が衝突する円形衝突面
を前記ノズルの噴孔と略同心傾設け、かつ前記円形衝突
面の外周から下流側に向けて略錐形に拡開する傾面とし
て形成されると共に該傾面の成す角度を予め選定した分
散角度に定めた分散案内面を設け、また前記分散案内面
の下流側に連設されかつ下流方面に向けて突出させた略
球形の突出面として形成され前記分散流の一部逆流循環
流を密着流動させる循環案内面を設けたことを特徴とす
る流体分散器。 2、前記円形衝突面が前記噴出流体に対向した平面とし
て形成された特許請求の範囲第1項に記載の流体分散器
。 3、前記円形衝突面がその中心部分に空洞部を有する特
許請求の範囲第1項に記載の流体分散器。
[Scope of Claims] 1. In a fluid distributor provided on the downstream side of a fluid ejecting nozzle, a circular collision surface with which fluid ejected from the nozzle collides is tilted approximately concentrically with the nozzle hole of the nozzle, and the circular collision surface A dispersion guide surface is provided, which is formed as an inclined surface that expands into a substantially conical shape from the outer periphery of the surface toward the downstream side, and the angle formed by the inclined surface is set to a preselected dispersion angle, and the dispersion guide surface is A fluid distributor characterized in that a circulation guide surface is provided, which is formed as a substantially spherical projecting surface that is connected to the downstream side and projects toward the downstream direction, and allows a part of the dispersed flow to closely flow a reverse circulation flow. . 2. The fluid distributor according to claim 1, wherein the circular collision surface is formed as a plane facing the ejected fluid. 3. The fluid distributor according to claim 1, wherein the circular collision surface has a hollow portion at its center.
JP10176383A 1983-06-09 1983-06-09 Fluid diffuser Granted JPS59228964A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10176383A JPS59228964A (en) 1983-06-09 1983-06-09 Fluid diffuser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10176383A JPS59228964A (en) 1983-06-09 1983-06-09 Fluid diffuser

Publications (2)

Publication Number Publication Date
JPS59228964A true JPS59228964A (en) 1984-12-22
JPS6341625B2 JPS6341625B2 (en) 1988-08-18

Family

ID=14309265

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10176383A Granted JPS59228964A (en) 1983-06-09 1983-06-09 Fluid diffuser

Country Status (1)

Country Link
JP (1) JPS59228964A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010005533A (en) * 2008-06-26 2010-01-14 Anest Iwata Corp Annular pattern atomization spray gun
CN105903585A (en) * 2016-06-17 2016-08-31 江苏永钢集团有限公司 Open-type spherical reflection nozzle

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010005533A (en) * 2008-06-26 2010-01-14 Anest Iwata Corp Annular pattern atomization spray gun
CN105903585A (en) * 2016-06-17 2016-08-31 江苏永钢集团有限公司 Open-type spherical reflection nozzle

Also Published As

Publication number Publication date
JPS6341625B2 (en) 1988-08-18

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