JPS6341625B2 - - Google Patents

Info

Publication number
JPS6341625B2
JPS6341625B2 JP10176383A JP10176383A JPS6341625B2 JP S6341625 B2 JPS6341625 B2 JP S6341625B2 JP 10176383 A JP10176383 A JP 10176383A JP 10176383 A JP10176383 A JP 10176383A JP S6341625 B2 JPS6341625 B2 JP S6341625B2
Authority
JP
Japan
Prior art keywords
fluid
dispersion
nozzle
flow
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.)
Expired
Application number
JP10176383A
Other languages
Japanese (ja)
Other versions
JPS59228964A (en
Inventor
Toshiharu Kumazawa
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

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  • Nozzles (AREA)
  • Evaporation-Type Combustion Burners (AREA)

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、
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1008187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、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、従つて流体が気液
混合燃料流体の場合にあつては、周囲の燃焼熱に
よつて乾燥したカーボン粒子となつて付着堆積
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。
Prior Art A fluid ejected from a nozzle nozzle is collided with and reflected by a fluid distributor provided on the downstream side of the nozzle nozzle.
A method and structure for colliding with the subsequent ejected fluid from the nozzle orifice and dispersing it to the outside in a thin film wide-angle umbrella shape are known as Japanese Patent No. 1008187 and Japanese Patent No. 941825. This conventional fluid disperser does not have a guide surface to guide the dispersed flow downstream, so at the moment the dispersed flow leaves the fluid disperser, fluid particles inside the dispersed flow are generated hydrodynamically 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 dry out and become deposited as carbon particles, which will be retained. This will result in interfering with the flame and stable combustion.

発明の目的 依つて本発明の目的は、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、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。
OBJECTS OF THE INVENTION Accordingly, an object of the present invention is to improve the above-mentioned conventional fluid dispersion device, which is particularly suitable for spray dispersion of gas-liquid mixed fuel, and to stabilize the shape of fuel spray dispersion into a combustion furnace.
An object of the present invention is to provide a fluid distributor that can prevent carbon contained in fuel from adhering to the outer periphery of the fluid distributor.

発明の構成、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, Effects of the Invention According to the present invention, in a fluid distributor provided on the downstream side of a fluid ejection nozzle, a circular collision surface with which fluid ejected from the fluid ejection nozzle collides is arranged approximately concentrically with the nozzle hole of the nozzle. a dispersion guide surface formed as a substantially conical inclined surface that expands downstream from the outer periphery of the circular collision surface, and whose angle formed by the inclined surface is set to a preselected dispersion angle; A circulation guide surface is provided that 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 a 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
つ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つて剥離すること
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、
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、
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。
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. and without separating a part of the fuel dispersed flow back to the negative pressure region hydrodynamically generated around and downstream of the fluid distributor by the dispersed flow along the periphery of the fluid distributor. The foreign matter adhering to the outer periphery of the fluid distributor is removed by guiding the fluid, and the foreign matter is re-involved in the fuel dispersion flow.
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, ultimately maintaining good combustion performance. below,
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、つまり空気
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
線に沿つて、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、
例えばスパイダ形保持具により係止されている。
流体分散器2は従つてノズル1の中心軸線と同心
に噴孔1aの下流側に設けられ、空洞Cを有する
衝突面4、この衝突面4の外周から下流に向つて
末広がりに形成された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。
Now, in FIG. 1, 1 is a nozzle having a nozzle hole 1a for ejecting a fluid, that is, a gas-liquid mixed fluid F of air or steam and fuel particles. A support rod 3 that supports the vessel 2 is inserted, and an appropriate holder is inserted deep inside.
For example, it is locked by a spider-shaped holder.
Therefore, the fluid distributor 2 is provided on the downstream side of the nozzle hole 1a concentrically with the central axis of the nozzle 1, and includes a collision surface 4 having a cavity C, and a collision surface 4 that is substantially widened toward the downstream from the outer periphery of the collision surface 4. Each part is provided with a conical dispersion guide surface 5 and a spherical guide tip 6 provided in a protruding shape further downstream of the dispersion guide surface 5.

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、分
散流S1となる。この分散流S1は分散案内面5によ
つて所望の分散角αを保つて安定に分散する。つ
まり末広がりの分散案内面5の案内作用で広角に
安定に進むのである。炉内Fにおいては、分散流
S1は燃焼し、燃焼後の高温ガスの一部が循環流S2
となつて突出先端6の球面に沿つて逆流し、該球
面に付着した未燃粒子を除去してS1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つて高温ガス
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の球面に沿つて剥
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(投影面積)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S1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、分散流S1の着火保
炎を連続的に安定におこなわしめる。
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 stream, receives a dispersion effect, and becomes a dispersed stream S1 . This dispersed flow S 1 is stably dispersed by the dispersion guide surface 5 while maintaining a desired dispersion angle α. In other words, the guide action of the dispersion guide surface 5 that widens toward the end allows it to move stably over a wide angle. In the furnace F, dispersed flow
S 1 is burned, and part of the high temperature gas after combustion is circulated through S 2
The particles then flow back along the spherical surface of the protruding tip 6, remove unburned particles attached to the spherical surface, and are drawn into S1 . This backflow circulation flow S 2 is generated when a part of the high temperature gas flows toward the negative pressure region generated around and downstream of the fluid distributor 2, and the circulation flow S 2 of the high temperature gas flows toward the protruding tip. Since it flows along the spherical surface of No. 6 without peeling off, it prevents the adhesion of carbon particles and removes the adhering particles. In addition, according to the spherical shape, the area (projected area) on which fuel particles adhere is made as large as possible on the F side of the furnace, making it easier to absorb the heat necessary for incineration of adhering unburned particles. It also exhibits the effect of Now, since the circulating flow S 2 caught up in the gas-liquid mixed fluid S 1 is a high-temperature gas containing flame, the ignition and flame holding of the dispersed flow S 1 is continuously and stably performed.

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、分散流S1′の内側に存在する
粒子が衝突面8の外周端9において、分散流
S1′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。従つてその分流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S2′が流体分散器7の周囲に沿つ
て流れる作用もなく、剥離してしまうので、周囲
に付着した燃料粒子やカーボン粒子を除去するこ
とは困難となり、第4図に示すようにカーボン粒
子の堆積塊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 dispersion flow S
S 1 ′ is scattered from the main stream like a branch stream S 3 and is drawn into the surrounding negative pressure area. Therefore, the fuel particles in the branched flow S 3 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 S 2 ' Since there is no flow action along the periphery of the disperser 7 and the particles are separated, it becomes difficult to remove the fuel particles and carbon particles adhering to the periphery, and as shown in FIG. This results in generation and growth, interfering with flame-holding and stable combustion.

以上の説明から明らかなように、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
より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噴霧流に形成され、か
つ突出案内面に沿つ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、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、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 downstream protruding guide surface having a spherical shape, so that a gas-liquid mixed flow is ejected. The fuel is formed into a dispersed spray stream that burns stably and efficiently in the furnace, and a portion of the high-temperature gas circulates along the protruding guide surface without peeling, which prevents and removes adhesion of carbon particles. At the same time, it effectively achieves ignition and flame holding to achieve complete combustion in the combustion furnace. It goes without saying that the collision surface of 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、S1……分散流、S2……循環流。
FIG. 1 is a longitudinal cross-sectional view of an embodiment of the fluid distributor according to the present invention, FIG. 2 is a cross-sectional view explaining the action of the fluid distributor, and FIG. 3 is a vertical cross-sectional view showing an example of a conventional fluid distributor. , FIG. 4 is a cross-sectional view showing the state of accumulation of carbon particles adhering to the conventional fluid disperser. DESCRIPTION OF SYMBOLS 1... Nozzle, 1a... Nozzle hole, 2... Fluid disperser, 4... Collision surface, 5... Dispersion guide surface, 6... Guide tip, 7... Conventional fluid disperser, F... Air Liquid mixed fluid, S 1 ... dispersed flow, S 2 ... circulation flow.

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に設
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 ejection nozzle, a circular collision surface with which fluid jetted from the nozzle collides is provided approximately concentrically with the nozzle hole of the nozzle, and the circular collision surface A dispersion guide surface is provided which is formed as a substantially conical inclined surface that widens from the outer periphery toward the downstream side, and the angle formed by the inclined surface is set to a preselected dispersion angle; A fluid dispersing device characterized by being provided with a circulation guide surface which is formed as a substantially spherical protruding surface that is connected to the side and protrudes toward the downstream direction, and allows a part of the dispersion flow to flow in close contact with the 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 cavity in 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 JPS59228964A (en) 1984-12-22
JPS6341625B2 true 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)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5336778B2 (en) * 2008-06-26 2013-11-06 アネスト岩田株式会社 Annular pattern 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
JPS59228964A (en) 1984-12-22

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