JPS6057910B2 - Internal/external mixing type atomizer - Google Patents

Internal/external mixing type atomizer

Info

Publication number
JPS6057910B2
JPS6057910B2 JP10447879A JP10447879A JPS6057910B2 JP S6057910 B2 JPS6057910 B2 JP S6057910B2 JP 10447879 A JP10447879 A JP 10447879A JP 10447879 A JP10447879 A JP 10447879A JP S6057910 B2 JPS6057910 B2 JP S6057910B2
Authority
JP
Japan
Prior art keywords
flow path
medium
fluid
mixed fluid
atomized
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
JP10447879A
Other languages
Japanese (ja)
Other versions
JPS5628669A (en
Inventor
祐哉 山畑
克典 高橋
智 姉帯
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 JP10447879A priority Critical patent/JPS6057910B2/en
Publication of JPS5628669A publication Critical patent/JPS5628669A/en
Publication of JPS6057910B2 publication Critical patent/JPS6057910B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は内外部混合式霧化器に関し、特に重質油のよう
な比較的高粘度の燃料を高速度で噴出する加圧蒸気等と
混合して微粒化し、ボイラ燃料として利用できるように
するための霧化器に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an internal/external mixing type atomizer, in particular, which atomizes relatively high viscosity fuel such as heavy oil with pressurized steam ejected at high speed, and This invention relates to an atomizer for use as fuel.

現在、燃料油をはじめとする各種流体を微粒化する方法
として、内部混合式、外部混合式、圧力噴射式、回転キ
ャップ式、衝突式、超音波式などが知られている。
Currently, known methods for atomizing various fluids such as fuel oil include an internal mixing method, an external mixing method, a pressure injection method, a rotating cap method, a collision method, and an ultrasonic method.

しかし、これらの方法は、いずれも流体の粘度が50℃
で500センチポイズ以下の低粘性流体にしか適用でき
ないのが現状であつた。特にボイラ燃料の場合十分な微
粒化を要し、その適用粘度は更に低下していた。従来の
霧化器をバーナーに供して、高粘性燃料を霧化燃焼させ
ると微粒化が悪いため、供給燃料の一部が未着火の粗粒
となつて飛散したり、火炎が不安定になるなど数多くの
問題が発生し、実用化が困難であつた。
However, in both of these methods, the viscosity of the fluid is 50°C.
Currently, it can only be applied to low viscosity fluids of 500 centipoise or less. Particularly in the case of boiler fuel, sufficient atomization is required, and its applied viscosity is further reduced. When a conventional atomizer is used in a burner to atomize and burn highly viscous fuel, atomization is poor, so some of the supplied fuel becomes unignited coarse particles and scatters, and the flame becomes unstable. Many problems such as these occurred, making it difficult to put it into practical use.

このため、十分な熱量を有していながら、粘性が高いと
いう理由でボイラ燃料に利用できないものが多数存在す
るのである。本発明は従来の内部混合式霧化器を改良し
、外部混合式霧化機構を組合わせることにより、高粘性
の燃料を十分に微粒化し、ボイラ燃料として利用できる
ようにするためのバーナーを提供することを目的とし、
次ような構成をとる。即ち、本発明は被霧化流体流路、
第1次霧化媒体流路、被霧化流体と第1次霧化媒体とが
混合される混合室、混合流体が噴出する混合流体噴出流
路および該混合流体噴出流路の外周部に開孔する第2次
霧化媒体噴出流路からなる内外部混合式霧化器において
、混合室は前記混合流体噴出流路の中心軸と同一軸の円
筒または半球形状を有し、第1次霧化媒体流路は該混合
室内に前記第1次霧化媒体の旋回流が起るように該混合
室の前流側で該混合室の周壁に対して接線方向に設けら
れ、被霧化流体流路は第1次霧化媒体流路に略直角に交
叉して開孔しており、かつ第2次霧化媒体噴出流路は第
2次霧化媒体が前記混合流体噴出流路から噴出した混合
流体とその噴出直後に60流以下の角度て交叉して噴出
するように設けられたことを特徴とする内外部混合式霧
化器である。
For this reason, there are many fuels that have a sufficient amount of heat but cannot be used as boiler fuel because of their high viscosity. The present invention improves the conventional internal mixing atomizer and combines it with an external mixing atomizer to provide a burner that sufficiently atomizes highly viscous fuel so that it can be used as boiler fuel. with the aim of
It has the following structure. That is, the present invention provides a fluid flow path to be atomized;
A primary atomization medium flow path, a mixing chamber where the fluid to be atomized and the primary atomization medium are mixed, a mixed fluid jet flow path through which the mixed fluid is jetted, and an opening in the outer periphery of the mixed fluid jet flow path. In an internal/external mixing type atomizer consisting of a secondary atomizing medium jetting passage with holes, the mixing chamber has a cylindrical or hemispherical shape coaxial with the central axis of the mixed fluid jetting passage, and the mixing chamber has a cylindrical or hemispherical shape coaxial with the central axis of the mixed fluid jetting passage; The atomizing medium flow path is provided on the upstream side of the mixing chamber in a tangential direction to the peripheral wall of the mixing chamber so that a swirling flow of the primary atomizing medium occurs in the mixing chamber, and the atomizing medium flow path The flow path is opened to intersect with the primary atomization medium flow path at a substantially right angle, and the secondary atomization medium jetting flow path is configured such that the secondary atomization medium is jetted from the mixed fluid jetting flow path. The present invention is an internal/external mixing type atomizer, characterized in that the mixed fluid is disposed so as to be ejected at an angle of 60 degrees or less immediately after the mixed fluid is ejected.

以下、図面を参照して本発明を具体的に説明する。Hereinafter, the present invention will be specifically described with reference to the drawings.

第1図は本発明の一実施例を示す断面図で、燃料等の被
霧化流体が通る被霧化流体供給路1および被霧化流体流
路2、加圧蒸気等の第1次霧化媒体が通る第1次霧化媒
体供給路3および第1次霧化媒体流路4、被霧化流体と
第1次霧化媒体が混合される一個の混合室5、ここで得
られた混合流体が噴出する混合流体噴出流路6およびこ
の噴出流路6の外周部に開孔する第2次霧化媒体噴出流
路7から基体的に構成されている。また第1図に示す実
施例の組立構造は被霧化流体供給管A1第1次霧化媒体
供給管B、ミキシングノズルC1ミキシングチップDお
よびキャップEの部品から組立てられており、被霧化流
体供給管Aは被霧化流体供給路1を形成すると同時にミ
キシングノズルCを支持しており、第1次霧化媒体供給
管Bは第1次霧化媒体供給路3を形成すると同時にミキ
シングノズルC1ミキシングチップDおよびキャップE
を固定している。
FIG. 1 is a cross-sectional view showing one embodiment of the present invention, showing an atomized fluid supply path 1 and an atomized fluid flow path 2 through which a fluid to be atomized such as fuel passes, and a primary mist such as pressurized steam. A primary atomizing medium supply path 3 and a primary atomizing medium flow path 4 through which the atomizing medium passes, a mixing chamber 5 in which the fluid to be atomized and the primary atomizing medium are mixed; It basically consists of a mixed fluid jetting channel 6 through which the mixed fluid is jetted, and a secondary atomizing medium jetting channel 7 that is opened in the outer periphery of this jetting channel 6. Furthermore, the assembly structure of the embodiment shown in FIG. 1 is assembled from parts such as a fluid to be atomized supply pipe A1, a primary atomization medium supply pipe B, a mixing nozzle C, a mixing tip D, and a cap E, and the fluid to be atomized is The supply pipe A forms the atomized fluid supply path 1 and at the same time supports the mixing nozzle C, and the primary atomization medium supply pipe B forms the primary atomization medium supply path 3 and at the same time supports the mixing nozzle C1. Mixing tip D and cap E
is fixed.

またミキシングノズルCは被霧化流体流路2および第1
次霧化媒体供給路4を有し、ミキシングチップDは混合
室および混合流体噴出流路6を有し、ミキシングチップ
Dの外周壁とキャップEの内周壁とで第2次霧化媒体噴
出流路7を形成している。混合室5は混合流体噴出流路
6の中心軸と同一ー軸の円筒形状(第3図参照)または
半球形状(第4図参照)を有している。
Further, the mixing nozzle C is connected to the atomized fluid flow path 2 and the first
The mixing chip D has a mixing chamber and a mixed fluid jet flow path 6, and the outer peripheral wall of the mixing chip D and the inner peripheral wall of the cap E create a secondary atomizing medium jet flow. It forms road 7. The mixing chamber 5 has a cylindrical shape (see FIG. 3) or a hemispherical shape (see FIG. 4) having the same axis as the central axis of the mixed fluid jet flow path 6.

第2図はミキシングノズルCを示す図であり、第1次霧
化媒体流路4は第2図bに示すように混合室5内(第1
,3図参照)に旋回流が起こるよ.うに混合室5の前流
側において、混合室5の周壁に対して接線方向に設けら
れている。
FIG. 2 is a diagram showing the mixing nozzle C, and the primary atomized medium flow path 4 is located inside the mixing chamber 5 (the first
, see Figure 3), a swirling flow occurs. It is provided on the upstream side of the mixing chamber 5 in a tangential direction to the peripheral wall of the mixing chamber 5.

また、被霧化流体流路2は第2図A,bに示すように第
1次霧化媒体流路4の適当な位置に開孔し、第1次霧化
媒体流路4の中心軸に対して直角・に近い角度で交叉す
るように設けられている。
Further, the atomized fluid flow path 2 is opened at an appropriate position of the primary atomized medium flow path 4, as shown in FIGS. 2A and 2B. It is provided so that it intersects at an angle close to a right angle.

第2次霧化媒体流路7は第1図に示すように混合流体噴
出流路6の外周部に円形スリット状で外部に開孔し、こ
こから噴出される第2次霧化媒体が混合流体噴出流路6
からの噴出流と600以下の角度で交叉するように設け
られている。第1図および第3図では第2次霧化媒体流
路7がミキシングチップDの外周壁とキャップEの内周
壁とで形成された1個の円形スリット状の例を示したが
、第5図に示すようにミキシングチップとキャップが一
体物で形成され、それに開けられた多数の穴から第2次
霧化媒体を噴出させることもできる。
As shown in FIG. 1, the secondary atomizing medium flow path 7 has a circular slit-shaped opening on the outer periphery of the mixed fluid jetting flow path 6, and the secondary atomizing medium ejected from this hole is mixed. Fluid jet flow path 6
It is provided so that it intersects the jet stream from the jet at an angle of 600 degrees or less. In FIGS. 1 and 3, an example in which the secondary atomized medium flow path 7 has a circular slit shape formed by the outer circumferential wall of the mixing tip D and the inner circumferential wall of the cap E is shown. As shown in the figure, the mixing tip and the cap are integrally formed, and the secondary atomizing medium can be ejected from a number of holes formed therein.

また、第1図ては第1次霧化媒体流供給路3を流れる霧
化媒体が霧化器内で第1次霧化媒体と第2次霧化媒体と
に分れる例を示したが、この他、第2次霧化媒体を別の
供給路から導入し、単独に流量を調節することもできる
Further, FIG. 1 shows an example in which the atomizing medium flowing through the primary atomizing medium flow supply path 3 is divided into a primary atomizing medium and a secondary atomizing medium within the atomizer. In addition to this, it is also possible to introduce the secondary atomization medium from another supply path and adjust the flow rate independently.

したがつて、第1次、第2次霧化媒体は夫々、異なつた
種類の流体を使用することもできる。被霧化流体流路2
の流路面積はその流速が0.5〜3.0TrLISeC
の範囲になるよう設計されるのが好ましい。
Therefore, different types of fluids may be used as the primary and secondary atomizing media. Atomized fluid flow path 2
The flow path area is 0.5 to 3.0 TrLISeC.
It is preferable that the design is within the range of .

第1次霧化媒体流路4、第2次霧化媒体噴出流路7およ
び混合流体噴出流路6の流路面積は、それぞれの流速が
音速または音速に近い速度になるように、かつ第1次霧
化媒体の流量が被霧化流体の流量に対して重量比で0.
1〜1.@、第2次霧化媒体の流量が被霧化流体に対し
て0.1〜1.0倍の範囲に入るよう設計されるのが好
ましい。これらの条件は被霧化流体の物性、霧化媒体の
供給圧力および要求される微粒噴流の形状等に応じて決
定される。第2次霧化媒体噴出流路7の傾斜角度は混合
流体噴出流路6の中心軸に対して60角以下にする必要
があり、好ましくは10〜600である。混合室5の直
径は混合流体噴出流路6の直径の1.5〜4.@、その
流出方向の長さは、その直径の0.5〜1j倍の範囲に
入るよう設計されるのが好ましい。本発明の霧化器は被
霧化流体流路2が霧化媒体流路4と交叉して開孔する位
置で、流出する被霧化流体がその方向に対して直角また
はそれに近い角度で、かつ音速またはそれに近い速度で
流れる第1次霧化媒体によつて、第1段目の微粒化作用
を受け、次いで旋回する混合流体と化した後、混合流体
噴出流路6から旋回流を持ちながら音速またはそれに近
い速度で噴出することにより、第2段目の別粒化作用を
受け、さらにこの直後に60以下の角度をもつて音速ま
たはそれに近い速度で噴出する第2次霧化媒体に衝突し
て第3段目の別粒化作用を受けるという3段階の別粒化
機構を1つの霧化器に組込んだものである。
The flow area of the primary atomization medium flow path 4, the secondary atomization medium jet flow path 7, and the mixed fluid jet flow path 6 is set so that the respective flow velocities become the sonic speed or a speed close to the sonic speed. The flow rate of the primary atomization medium is 0.0% by weight relative to the flow rate of the fluid to be atomized.
1-1. It is preferable that the flow rate of the secondary atomization medium is designed to be in the range of 0.1 to 1.0 times the flow rate of the fluid to be atomized. These conditions are determined depending on the physical properties of the fluid to be atomized, the supply pressure of the atomizing medium, the required shape of the fine particle jet, etc. The angle of inclination of the secondary atomizing medium jetting channel 7 needs to be 60 degrees or less with respect to the central axis of the mixed fluid jetting channel 6, preferably 10 to 600 degrees. The diameter of the mixing chamber 5 is 1.5 to 4. It is preferable that the length in the outflow direction is designed to be in the range of 0.5 to 1j times the diameter. In the atomizer of the present invention, at a position where the atomized fluid flow path 2 intersects with the atomized medium flow path 4 and opens, the outflowing atomized fluid is perpendicular to that direction or at an angle close to that direction. And after receiving the first stage atomization effect by the primary atomization medium flowing at the speed of sound or a speed close to it, and then turning into a swirling mixed fluid, a swirling flow is generated from the mixed fluid jetting channel 6. However, by ejecting at the speed of sound or close to it, it is subjected to the second stage of separate atomization, and immediately after this, the second atomization medium is ejected at the speed of sound or close to it at an angle of 60 or less. This atomizer incorporates a three-stage separate granulation mechanism in which particles collide and are subjected to the separate granulation action of the third stage.

また、第1次霧化媒体と第2次霧化媒体は共に被霧化流
体を別粒化する作用を有しているが、さらに、本霧化器
をバーナーとして用いた場合、第1次霧化媒体は得られ
る火炎を太くて短かい形状に、第2次霧化媒体は逆に細
く長い形状にする性質を有する。
In addition, both the primary atomizing medium and the secondary atomizing medium have the function of dividing the fluid to be atomized into separate particles, but in addition, when this atomizer is used as a burner, the primary atomizing medium The atomizing medium has the property of making the resulting flame thick and short, and the secondary atomizing medium has the property of making the flame narrow and long.

したがつて、第1次および第2次霧化媒体の流量を調節
することによつて炉形式に応じた火炎形状を容易に決定
することができる。本発明の霧化器からなるバーナーを
使用することにより、従来技術では不可能であつた10
000センチポイズ(50℃)以上の高粘性燃料まで十
分に微粒化でき、安定した火炎を提供できるのでボイラ
燃料の選択域が極めて広くなる。また従来、高粘性のた
め燃料化できなかつた重質油、アスファルト、ピッチ等
もボイラ燃料とすることができ、エネルギーの有効利用
が大巾に促進される。図面の簡単な説明第1図は本発明
の内外部混合式霧化器を示す断面図、第2図A,bはミ
キシングノズルの断面図および正面図、第3図A,bは
ミキシングチップの断面図および正面図、第4図は変形
されたミキシングチップの断面図、第5図は他の実施例
を示す正面図てある。
Therefore, by adjusting the flow rates of the primary and secondary atomizing media, it is possible to easily determine the flame shape depending on the type of furnace. By using the burner consisting of the atomizer of the present invention, it is possible to achieve 10
It can sufficiently atomize fuel with a high viscosity of 000 centipoise (50°C) or more and provide a stable flame, so the range of boiler fuel selection is extremely wide. Furthermore, heavy oil, asphalt, pitch, etc., which conventionally could not be converted into fuel due to their high viscosity, can be used as boiler fuel, and the effective use of energy is greatly promoted. BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a sectional view showing the internal/external mixing type atomizer of the present invention, Figures 2A and b are sectional views and front views of the mixing nozzle, and Figures 3A and b are views of the mixing tip. A sectional view and a front view, FIG. 4 is a sectional view of a modified mixing chip, and FIG. 5 is a front view showing another embodiment.

1・・・・・・被霧化流体供給路、2・・・・・・被霧
化流体流路、3・・・・・・霧化媒体供給路、4・・・
・・・第1次霧化媒体流路、5・・・・・・混合室、6
・・・・・・混合流体噴出流路、7・・・・・・第2次
霧化媒体噴出流路。
1... Atomized fluid supply path, 2... Atomized fluid flow path, 3... Atomized medium supply path, 4...
. . . Primary atomization medium flow path, 5 . . . Mixing chamber, 6
...Mixed fluid jetting channel, 7...Second atomizing medium jetting channel.

Claims (1)

【特許請求の範囲】[Claims] 1 被霧化流体流路、第1次霧化媒体流路、被霧化流体
と第1次霧化媒体とが混合される混合室、混合流体が噴
出する混合流体噴出流路よび該混合流体噴出流路の外周
部に開孔する第2次霧化媒体噴出流路からなる内外部混
合式霧化器において、混合室は前記混合流体噴出流路の
中心軸と同一軸の円筒または半球形状を有し、第1次霧
化媒体流路は該混合室内に前記第1次霧化媒体の旋回流
が起るように該混合室の前流側で該混合室の周壁に対し
て接線方向に設けられ、被霧化流体流路は第1次霧化媒
体流路に略直角に交叉して開孔しており、かつ第2次霧
化媒体噴出流路は第2次霧化媒体が前記混合流体噴出流
路から噴出した混合流体とその噴出直後に60゜以下の
角度で交叉して噴出するように設けられたことを特徴と
する内外部混合式霧化器。
1 A fluid to be atomized channel, a primary atomizing medium channel, a mixing chamber where the fluid to be atomized and the primary atomizing medium are mixed, a mixed fluid ejection channel from which the mixed fluid is ejected, and the mixed fluid In an internal/external mixing type atomizer consisting of a secondary atomizing medium jetting passage opened on the outer periphery of the jetting passage, the mixing chamber has a cylindrical or hemispherical shape coaxial with the central axis of the mixed fluid jetting passage. and the primary atomizing medium flow path is tangential to the peripheral wall of the mixing chamber on the upstream side of the mixing chamber so that a swirling flow of the primary atomizing medium occurs in the mixing chamber. The atomized fluid flow path is opened to cross the primary atomization medium flow path at a substantially right angle, and the secondary atomization medium ejection flow path is formed so that the secondary atomization medium flows through the secondary atomization medium flow path. An internal/external mixing type atomizer, characterized in that the mixed fluid jetted from the mixed fluid jetting flow path and the mixed fluid jetted out intersect with each other at an angle of 60 degrees or less immediately after jetting out.
JP10447879A 1979-08-16 1979-08-16 Internal/external mixing type atomizer Expired JPS6057910B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10447879A JPS6057910B2 (en) 1979-08-16 1979-08-16 Internal/external mixing type atomizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10447879A JPS6057910B2 (en) 1979-08-16 1979-08-16 Internal/external mixing type atomizer

Publications (2)

Publication Number Publication Date
JPS5628669A JPS5628669A (en) 1981-03-20
JPS6057910B2 true JPS6057910B2 (en) 1985-12-17

Family

ID=14381667

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10447879A Expired JPS6057910B2 (en) 1979-08-16 1979-08-16 Internal/external mixing type atomizer

Country Status (1)

Country Link
JP (1) JPS6057910B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3161981B2 (en) * 1996-09-27 2001-04-25 日石三菱株式会社 Nozzle for combustion of waste oil mixed type liquid fuel and combustion method
JP3161982B2 (en) * 1996-09-27 2001-04-25 日石三菱株式会社 Nozzle for combustion of waste oil mixed type liquid fuel and combustion method
JP6347432B2 (en) * 2016-01-20 2018-06-27 パナソニックIpマネジメント株式会社 Spraying equipment
JP7182104B2 (en) * 2019-03-28 2022-12-02 パナソニックIpマネジメント株式会社 spraying device

Also Published As

Publication number Publication date
JPS5628669A (en) 1981-03-20

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