JP2002306939A - Fluid mixer - Google Patents

Fluid mixer

Info

Publication number
JP2002306939A
JP2002306939A JP2001114449A JP2001114449A JP2002306939A JP 2002306939 A JP2002306939 A JP 2002306939A JP 2001114449 A JP2001114449 A JP 2001114449A JP 2001114449 A JP2001114449 A JP 2001114449A JP 2002306939 A JP2002306939 A JP 2002306939A
Authority
JP
Japan
Prior art keywords
fluid
flow path
mixing device
dividing member
fluids
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
JP2001114449A
Other languages
Japanese (ja)
Other versions
JP4580580B2 (en
Inventor
一光 ▲たか▼西
Kazumitsu Takanishi
理 ▲くわ▼野
Osamu Kuwaya
Reina Tanaka
玲奈 田中
Satoshi Shishido
聡 宍戸
Masato Mukai
正人 向井
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.)
Kansai Electric Power Co Inc
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Kansai Electric Power Co Inc
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 Babcock Hitachi KK, Kansai Electric Power Co Inc filed Critical Babcock Hitachi KK
Priority to JP2001114449A priority Critical patent/JP4580580B2/en
Publication of JP2002306939A publication Critical patent/JP2002306939A/en
Application granted granted Critical
Publication of JP4580580B2 publication Critical patent/JP4580580B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a fluid mixer which reliably mixes fluids in the state of low pressure loss and discharges the fluids as a uniformly mixed fluid even when the fluids are inhomogeneous in composition, temperature and/or concentration. SOLUTION: The homogeneity of an outlet fluid 6 of this fluid mixer 7 is achieved by disposing short pipes 5 respectively on fluid emitting parts 3a-3d which are disposed on a fluid dividing member 2. The fluids 1 which flow out of the short pipes 5 directly collide against or interfere with one another and generate a flow region of violent turbulence in the neighborhood. Therefore, even when the fluids 1 are inhomogeneous in composition, temperature and/or concentration, the fluids are almost uniformly mixed by being subjected to a passage through the flow region of violent turbulence generated by the fluid dividing member 2.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、燃焼用空気同士、
燃焼用空気と排ガス、排ガス同士などの流体の混合装置
に係り、特に低い圧力損失で流体の混合を大幅に促進す
ることができる混合装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to combustion air,
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a mixing device for mixing fluid such as combustion air and exhaust gas, and between exhaust gases, and more particularly to a mixing device capable of greatly promoting mixing of fluids with low pressure loss.

【0002】[0002]

【従来の技術】特開平7−227528号公報に開示さ
れた従来の流体混合装置17は図7の斜視図及び図7の
断面図である図8に示されるような構造である。流体混
合装置17は流体流路となるダクト4と該ダクト4内の
流体流路を横断するように設置された四角錐状の流路分
割部材2からなり、前記流路分割部材2の四角錐部を形
成する各三角形状の板面にはそれぞれ流体噴出部3a〜
3dが設けられており、ダクト4内を流れる流体流は、
この流体噴出部3a〜3dを通り抜ける。
2. Description of the Related Art A conventional fluid mixing device 17 disclosed in Japanese Patent Application Laid-Open No. 7-227528 has a structure as shown in FIG. 7 which is a perspective view of FIG. 7 and a sectional view of FIG. The fluid mixing device 17 includes a duct 4 serving as a fluid flow path and a quadrangular pyramid-shaped flow path dividing member 2 installed so as to cross the fluid flow path in the duct 4. Each of the triangular plate surfaces forming the fluid ejection parts 3a to 3a
3d is provided, and the fluid flow flowing through the duct 4 is:
The fluid passes through the fluid ejection portions 3a to 3d.

【0003】組成成分、温度及び/又は濃度などの不均
質な流体1が流体混合装置17の流路分割部材2に設け
られた流体噴出部3a〜3dを通り抜けると、濃度の不
均質な流体1は互いに激しく衝突し、その周囲領域を相
互に攪拌する。このため、流体1は完全に混合され、均
質流体6となる。
When the fluid 1 having a non-uniform composition, temperature, and / or concentration passes through the fluid ejection portions 3a to 3d provided on the flow path dividing member 2 of the fluid mixing device 17, the fluid 1 having a non-uniform concentration is obtained. Collide violently with each other and agitate the surrounding areas with each other. For this reason, the fluid 1 is completely mixed and becomes a homogeneous fluid 6.

【0004】[0004]

【発明が解決しようとする課題】しかし、前記従来技術
の流体混合装置17では、その入口部での流体1の組成
成分、温度及び/又は濃度などがどのような分布を持っ
ているかについての配慮、及び流入流体1が四角錐状の
流路分割部材2で大きく圧力を損失することに対する配
慮がされていなかった。
However, in the fluid mixing device 17 of the prior art, consideration is given to the distribution of the composition, temperature, and / or concentration of the fluid 1 at the inlet. In addition, no consideration has been given to the fact that the inflow fluid 1 greatly loses pressure in the quadrangular pyramid-shaped flow path dividing member 2.

【0005】上記従来技術は、流体混合装置17の入口
部での流体1の組成成分、温度及び/又は濃度などの分
布について配慮がされていなかったため、前記入口部で
の流体1が異なる成分の組成分布、各成分の濃度分布及
び/又は温度分布などがある場合、流体混合装置出口流
体の均質性が悪くなるという問題があった。また流体混
合装置17で流体1の流れに大きな圧力損失があること
も問題であった。
In the above-mentioned prior art, the distribution of the composition, temperature, and / or concentration of the fluid 1 at the inlet of the fluid mixing device 17 is not considered, so that the fluid 1 at the inlet has different components. When there is a composition distribution, a concentration distribution of each component, and / or a temperature distribution, there is a problem that the homogeneity of the fluid at the outlet of the fluid mixing device is deteriorated. There is also a problem that the flow of the fluid 1 in the fluid mixing device 17 has a large pressure loss.

【0006】また流体噴出部3a〜3dを出た流体6は
流路が急に拡大するため、流体流れ方向を変え、流体6
の衝突による混合効果が緩和される。従って流路分割部
材2を出た均質流体6の均質度合いが低いという結果と
なる。
[0006] Further, since the flow path of the fluid 6 that has exited the fluid ejection portions 3a to 3d is suddenly expanded, the fluid flow direction is changed, and the fluid 6 is discharged.
The mixing effect due to collision of the particles is reduced. Therefore, the result is that the degree of homogeneity of the homogeneous fluid 6 that has exited the flow path dividing member 2 is low.

【0007】本発明の課題は、組成成分、温度及び/又
は濃度などの不均質な流体でも圧力損失の少ない状態で
確実に混合し、均質な混合流体として排出する流体混合
装置を提供することである。
[0007] An object of the present invention is to provide a fluid mixing device that ensures that even a heterogeneous fluid having a composition, temperature, and / or concentration, etc., is mixed with a small pressure loss and is discharged as a homogeneous mixed fluid. is there.

【0008】[0008]

【課題を解決するための手段】本発明の上記課題は、以
下の構成を持った混合装置により達成される。すなわ
ち、ダクト内で少なくとも組成成分、温度及び/又は濃
度が不均質な流体同士を混合する流体混合装置におい
て、前記ダクト中に流体の流路を一旦分割する錐状構造
の流路分割部材と該流路分割部材に流体を噴出する1以
上の流体噴出用開口部を設け、該流体噴出用開口部の下
流側の該開口部端部に短管を接続した流体混合装置であ
る。
The above object of the present invention is achieved by a mixing device having the following configuration. That is, in a fluid mixing device for mixing fluids having at least composition components, temperatures and / or concentrations that are inhomogeneous in a duct, a flow channel dividing member having a conical structure for temporarily dividing a fluid flow channel in the duct, and A fluid mixing apparatus in which one or more fluid ejection openings for ejecting a fluid are provided in a flow channel dividing member, and a short pipe is connected to an end of the opening on the downstream side of the fluid ejection opening.

【0009】本発明の流体分割部材流体の開口部端部と
短管との接続部は滑らかな曲面とすることで、流体は圧
力損失をすることなく開口部の下流側に流れ、混合され
る。
The connection between the opening end of the fluid dividing member fluid and the short pipe of the present invention has a smooth curved surface, so that the fluid flows downstream of the opening without pressure loss and is mixed. .

【0010】また、流体が圧力損失をすることなく開口
部の下流側に流れるように混合されるためには、流体分
割部材の流体噴出流路出口部以降の流路断面が急拡大し
ないように、流路断面が徐々に拡大するようにダクト壁
面を構成してもよい。
Further, in order for the fluid to be mixed so as to flow downstream of the opening without causing a pressure loss, the flow section of the fluid dividing member after the outlet of the fluid ejection flow path is not suddenly enlarged. Alternatively, the duct wall surface may be configured so that the cross section of the flow path gradually increases.

【0011】また、流体の少なくとも組成成分、温度及
び/又は濃度などの不均質の度合が大きい部分に対応す
る流路分割部材の開口部を他の流路分割部材の開口部よ
り上流側に設けることで、流体の混合効率が上がる。
In addition, the opening of the flow path dividing member corresponding to at least a portion where the degree of inhomogeneity such as at least the composition of the fluid, the temperature and / or the concentration is large is provided upstream of the openings of the other flow dividing members. This increases the fluid mixing efficiency.

【0012】本発明の流体は蒸気と空気などの異なる成
分、同じ流体であっても組成割合(酸素と窒素の組成割
合など)、温度及び/又は濃度などが異なる流体、又は
ガス体、液体のいずれかの流体からなる。
The fluid of the present invention may be composed of different components such as steam and air, fluids having the same composition but different composition ratios (such as the composition ratio of oxygen and nitrogen), temperature and / or concentration, or gaseous substances and liquids. Consists of any fluid.

【0013】また、本発明の錐状の流体分割部材とは、
三角錐状、四角錐状、多角錐状及び円錐状などの形状の
流体分割部材をいう。
[0013] The conical fluid dividing member of the present invention includes:
A fluid dividing member having a triangular pyramid, quadrangular pyramid, polygonal pyramid, or conical shape.

【0014】[0014]

【作用】本発明によれば、流体分割部材に設けられた一
対以上の流体噴出の開口部に短管を接続することによ
り、該短管から流出された流体は、直接衝突あるいは干
渉し、その周囲に極めて乱れの激しい流れ領域を生じ
る。そのため組成などが不均一な流体であっても、この
乱れの激しい流れ領域を通過することにより、ほぼ均一
に混合される。流体混合装置の入口流体の少なくとも組
成成分、温度及び/又は濃度などが不均質な場合は、組
成成分、温度及び/又は濃度が最も高い位置または低い
位置に当たる流体噴出開口部の位置を流体分割部材の前
流側に移動させることにより、組成成分、温度及び/又
は濃度が最も高い流体または低い流体が流体混合装置内
の中心部に流入するので、流体混合装置出口で均質な流
体になる。
According to the present invention, by connecting the short pipe to the opening of one or more fluid jets provided in the fluid dividing member, the fluid discharged from the short pipe directly collides or interferes, This creates a very turbulent flow area around it. Therefore, even a fluid having a non-uniform composition or the like is mixed almost uniformly by passing through the highly turbulent flow region. When at least the composition, temperature, and / or concentration of the inlet fluid of the fluid mixing device are not uniform, the position of the fluid ejection opening corresponding to the position where the composition, temperature, and / or concentration is highest or lowest is determined by the fluid dividing member. To the upstream side of the fluid mixing device, the fluid with the highest or lowest composition, temperature and / or concentration flows into the center of the fluid mixing device, resulting in a homogenous fluid at the fluid mixing device outlet.

【0015】また本発明では、流体混合装置に流入する
流体の圧力損失を、流体流路断面を徐々に変化させるこ
とによって低減させるので、全体として流入流体の圧力
損失が低減できる。
In the present invention, since the pressure loss of the fluid flowing into the fluid mixing device is reduced by gradually changing the cross section of the fluid flow path, the pressure loss of the flowing fluid can be reduced as a whole.

【0016】[0016]

【発明の実施の形態】本発明の実施の形態について図面
と共に説明する。本発明の実施の形態の流体混合装置7
は図1の斜視図及び図1の要部断面図である図2に示さ
れるような構造であり、図7、図8に示す従来の流体混
合装置17と同様に、流体流路となるダクト4と該ダク
ト4内の流体流路を横断するように設置された四角錐状
の流路分割部材2からなり、流路分割部材2の四角錐部
を形成する各三角形状の板面にはそれぞれ流体噴出部3
a〜3dが設けられており、この流体噴出部3a〜3d
を流体流が通り抜ける。
Embodiments of the present invention will be described with reference to the drawings. Fluid mixing device 7 according to an embodiment of the present invention
2 is a perspective view of FIG. 1 and a structure as shown in FIG. 2 which is a cross-sectional view of a main part of FIG. 1. As in the conventional fluid mixing device 17 shown in FIGS. 4 and a quadrangular pyramid-shaped channel dividing member 2 installed so as to traverse the fluid channel in the duct 4. Each triangular plate surface forming the quadrangular pyramid of the channel dividing member 2 has Fluid ejection part 3
a to 3d are provided, and the fluid ejection portions 3a to 3d
Through the fluid flow.

【0017】図1、図2に示す本発明の実施の形態の流
体混合装置7と図7、図8に示す前記従来技術の流体混
合装置17の違いは四角錐状の流路分割部材2に流体噴
出部3a〜3dに流体が流れ出る方向に短管5を接続し
たことである。
The difference between the fluid mixing device 7 according to the embodiment of the present invention shown in FIGS. 1 and 2 and the conventional fluid mixing device 17 shown in FIGS. That is, the short pipe 5 is connected in the direction in which the fluid flows out to the fluid ejection portions 3a to 3d.

【0018】そのため、流体が組成成分、温度、濃度な
どの少なくとも一つが全体に一様でない不均質流体1で
ある場合に、この不均質流体1がダクト4内に設置され
た四角錐状の流路分割部材2の流体噴出部3a〜3dを
通り抜けるとき、短管5の出口で互いに激しく衝突し、
短管5の出口の不均質流体8は相互に混ざり合う。この
ため、不均質流体1は完全に混合されて均質流体6とな
る。
For this reason, when the fluid is a heterogeneous fluid 1 in which at least one of the composition, temperature, concentration, etc. is not uniform throughout, the heterogeneous fluid 1 is a square pyramid-shaped flow installed in the duct 4. When passing through the fluid jetting portions 3a to 3d of the road dividing member 2, they violently collide with each other at the outlet of the short pipe 5,
The heterogeneous fluids 8 at the outlet of the short pipe 5 mix with each other. For this reason, the heterogeneous fluid 1 is completely mixed and becomes the homogeneous fluid 6.

【0019】図7、図8に示す従来技術の流体混合装置
17では流体噴出部3a〜3dに短管5が接続されてい
ないため、流体噴出部3a〜3dを出た流体8は流路拡
大により流れ方向を変え、衝突による混合効果が緩和さ
れ、均質流体6の均質度合いが低いが、図1、図2に示
す本発明の流体混合装置は、この従来技術に比べて格段
に均質流体6の均質度合いが高い。
In the prior art fluid mixing device 17 shown in FIGS. 7 and 8, since the short pipe 5 is not connected to the fluid ejection portions 3a to 3d, the flow of the fluid 8 exiting the fluid ejection portions 3a to 3d is enlarged. To reduce the mixing effect due to collisions, and the degree of homogeneity of the homogeneous fluid 6 is low. However, the fluid mixing apparatus of the present invention shown in FIGS. High degree of homogeneity.

【0020】図3には図1の流体混合装置の流体噴出部
3a〜3dの要部断面図の他の実施の形態を示す。図3
に示す例では、流体噴出部3a〜3dと短管5との接続
部9を滑らかな曲面にしたものである。このように接続
部9で流体噴出部3a〜3dと短管5を滑らかに接続す
ることにより、流路縮小による流体流れの圧力損失を低
減させることができる。
FIG. 3 shows another embodiment of a sectional view of the main parts of the fluid jetting parts 3a to 3d of the fluid mixing apparatus of FIG. FIG.
In the example shown in (1), the connecting portion 9 between the fluid ejection portions 3a to 3d and the short pipe 5 has a smooth curved surface. As described above, by smoothly connecting the fluid ejection portions 3a to 3d and the short pipe 5 with the connection portion 9, the pressure loss of the fluid flow due to the contraction of the flow path can be reduced.

【0021】図6には図3に示す例に類似した公知例
(特開平07−227528号公報)に開示された四角
錐状流体混合装置の流体噴出部のダクト部分の断面構造
を示す。この公知例は四角錐状流体混合装置の圧力損失
を低減するために、流体噴出部3a〜3dの上流側の面
に口金10を設け、その口金10の断面を徐々に縮小し
たものである。図6に示す公知例の場合には、流体流れ
は口金10部分での圧力損失が大きくなるため、図3に
示す本発明の実施の形態に比べて、流動抵抗が高くな
る。
FIG. 6 shows a sectional structure of a duct portion of a fluid jetting portion of a quadrangular pyramid-shaped fluid mixing device disclosed in a known example (Japanese Patent Application Laid-Open No. 07-227528) similar to the example shown in FIG. In this known example, in order to reduce the pressure loss of the quadrangular pyramidal fluid mixing device, a base 10 is provided on the upstream surface of the fluid ejection sections 3a to 3d, and the cross section of the base 10 is gradually reduced. In the case of the known example shown in FIG. 6, since the pressure loss of the fluid flow at the base 10 is large, the flow resistance is higher than that of the embodiment of the present invention shown in FIG.

【0022】本発明の他の実施の形態の構造図を図4
(図4は図1に示す側断面の変形例である)に示す。図
4に示す例は、図1または図3に示す流体混合装置7の
短管5出口部に流体流路断面積が徐々に拡大する出口ダ
クト11を接続した流体混合装置である。この出口ダク
ト11を設置することにより、短管5出口の流路が急に
拡大することによる圧力損失を低減できる。また図3に
示す流体混合装置7の短管5出口部に出口ダクト11を
接続することによっても、同様の効果が得られる。
FIG. 4 is a structural diagram of another embodiment of the present invention.
(FIG. 4 is a modification of the side section shown in FIG. 1). The example shown in FIG. 4 is a fluid mixing device in which an outlet duct 11 whose fluid flow path cross-sectional area gradually increases is connected to the outlet of the short pipe 5 of the fluid mixing device 7 shown in FIG. 1 or FIG. By installing this outlet duct 11, it is possible to reduce the pressure loss due to the sudden expansion of the flow path at the outlet of the short pipe 5. The same effect can be obtained by connecting the outlet duct 11 to the outlet of the short pipe 5 of the fluid mixing device 7 shown in FIG.

【0023】本発明の他の実施の形態の流体混合装置7
の構造図を図5(図5は図1に示す側断面の変形例であ
る)に示す。図5に示す実施の形態では、例えば流体濃
度分布12(矢印の長さで流体濃度の大きさを示すが、
濃度に限らず、組成分布、又は温度分布などでも良い)
を持つ不均質流体1がダクト4に設置された四角錐状の
流路分割部材2に設けられた流体噴出部3a〜3dを通
り抜ける際に、流体噴出部3bでは流体濃度分布12
が、平均より高濃度の流体濃度分布12に相当するた
め、流体噴出部3bは他の流体噴出部3a、3c、3d
より流路分割部材2の前流側に設けている。
A fluid mixing device 7 according to another embodiment of the present invention.
5 is shown in FIG. 5 (FIG. 5 is a modification of the side section shown in FIG. 1). In the embodiment shown in FIG. 5, for example, the fluid concentration distribution 12 (the magnitude of the fluid concentration is indicated by the length of the arrow,
Not limited to concentration, composition distribution or temperature distribution may be used.)
When the heterogeneous fluid 1 having the following shape passes through the fluid ejection portions 3a to 3d provided in the quadrangular pyramid-shaped flow path dividing member 2 installed in the duct 4, the fluid ejection portion 3b has a fluid concentration distribution 12
Correspond to the fluid concentration distribution 12 having a higher concentration than the average, so that the fluid ejecting portion 3b is connected to the other fluid ejecting portions 3a, 3c, 3d.
It is provided on the upstream side of the flow path dividing member 2.

【0024】このように流体濃度が高い部分の流体噴出
部3bを流体噴出部3a、3c、3dより流路分割部材
2の前流側に設けることにより、高濃度流体をより早
く、ダクト4の中心部に流入させて、流体濃度を全体に
均一に分布させることができる。また、流体濃度分布が
平均値よりも低濃度部が存在する場合にも、その部分に
相当する流体噴出部を流路分割部材2の前流側に移動さ
せることによって同様の均質性を得ることができる。図
5に示す構成は図1〜図4に示す流体混合装置7にも適
用できる。
By providing the fluid ejecting portion 3b of the portion having a high fluid concentration on the upstream side of the flow dividing member 2 with respect to the fluid ejecting portions 3a, 3c and 3d in this manner, the high-concentration fluid can be supplied to the duct 4 more quickly. By flowing into the center, the fluid concentration can be evenly distributed throughout. Further, even when a fluid concentration distribution has a lower concentration portion than the average value, the same homogeneity can be obtained by moving the fluid ejection portion corresponding to that portion to the upstream side of the flow path dividing member 2. Can be. The configuration shown in FIG. 5 can also be applied to the fluid mixing device 7 shown in FIGS.

【0025】上記本発明の実施の形態の構成により、流
体混合装置出口の均質流体6の均質性が得られる。
According to the configuration of the embodiment of the present invention, homogeneity of the homogeneous fluid 6 at the outlet of the fluid mixing device can be obtained.

【0026】[0026]

【発明の効果】本発明によれば不均質流体を低い圧力損
失で均質流体にすることができるため、ファンの動力を
低減できるという効果がある。
According to the present invention, since the heterogeneous fluid can be made into a homogeneous fluid with a low pressure loss, the power of the fan can be reduced.

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

【図1】 本発明の実施の形態の流体混合装置の斜視図
を示す。
FIG. 1 is a perspective view of a fluid mixing device according to an embodiment of the present invention.

【図2】 図1の要部断面図を示す。FIG. 2 is a sectional view of a main part of FIG.

【図3】 本発明の他の実施の形態の流体混合装置の側
断面図を示す。
FIG. 3 is a side sectional view of a fluid mixing device according to another embodiment of the present invention.

【図4】 本発明の他の実施の形態の流体混合装置の側
断面図を示す。
FIG. 4 is a side sectional view of a fluid mixing device according to another embodiment of the present invention.

【図5】 本発明の他の実施の形態の流体混合装置の側
断面図を示す。
FIG. 5 is a side sectional view of a fluid mixing device according to another embodiment of the present invention.

【図6】 従来の流体混合装置の流体噴出部のダクト部
分の断面構造図を示す。
FIG. 6 is a sectional structural view of a duct portion of a fluid ejection part of a conventional fluid mixing device.

【図7】 従来の流体混合装置の斜視図を示す。FIG. 7 is a perspective view of a conventional fluid mixing device.

【図8】 図7の流体混合装置の側断面図を示す。8 shows a side sectional view of the fluid mixing device of FIG.

【符号の説明】[Explanation of symbols]

1 不均質流体 2 流路分割部
材 3a、3b、3c、3d 流体噴出部 4 ダクト 5 短管 6 均質流体 7、17 流体
混合装置 8 短管出口不均質流体 9 接続部 10 口金 11 出口ダク
ト 12 流体濃度分布
DESCRIPTION OF SYMBOLS 1 Heterogeneous fluid 2 Channel dividing member 3a, 3b, 3c, 3d Fluid ejection part 4 Duct 5 Short pipe 6 Homogeneous fluid 7, 17 Fluid mixing device 8 Short pipe outlet heterogeneous fluid 9 Connection part 10 Base 11 Exit duct 12 Fluid Concentration distribution

フロントページの続き (72)発明者 ▲くわ▼野 理 大阪府大阪市北区中之島三丁目3番22号 関西電力株式会社内 (72)発明者 田中 玲奈 大阪府大阪市北区中之島三丁目3番22号 関西電力株式会社内 (72)発明者 宍戸 聡 広島県呉市宝町6番9号 バブコック日立 株式会社呉事業所内 (72)発明者 向井 正人 広島県呉市宝町6番9号 バブコック日立 株式会社呉事業所内 Fターム(参考) 4G035 AB02 AC01 Continuation of the front page (72) Inventor ▲ Kuwa Nori 3-2-2 Nakanoshima, Kita-ku, Osaka-shi, Osaka Inside Kansai Electric Power Co., Inc. (72) Inventor Reina Tanaka 3-3-1 Nakanoshima, Kita-ku, Osaka, Osaka 22 Kansai Electric Power Co., Inc. (72) Inventor Satoshi Shishido 6-9 Takaracho, Kure City, Hiroshima Prefecture Babcock Hitachi Co., Ltd. (72) Inventor Masato Mukai 6-9 Takaracho Kure City, Hiroshima Prefecture Babcock Hitachi, Ltd. F-term in Kure office (reference) 4G035 AB02 AC01

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 ダクト内で少なくとも組成成分、温度及
び/又は濃度が不均質な流体同士を混合する流体混合装
置において、 前記ダクト中に流体の流路を一旦分割する錐状構造の流
路分割部材と該流路分割部材に流体を噴出する一以上の
流体噴出用開口部を設け、該流体噴出用開口部の下流側
の該開口部端部に短管を接続したことを特徴とする流体
混合装置。
1. A fluid mixing apparatus for mixing fluids having at least composition components, temperatures and / or concentrations that are inhomogeneous in a duct, wherein a flow path of a conical structure for temporarily dividing a fluid flow path in the duct is provided. A fluid characterized in that one or more fluid ejection openings for ejecting a fluid are provided in the member and the flow path dividing member, and a short pipe is connected to an end of the opening on the downstream side of the fluid ejection opening. Mixing device.
【請求項2】 流体分割部材流体の開口部端部と短管と
の接続部は滑らかな曲面であることを特徴とする請求項
1記載の流体混合装置。
2. The fluid mixing device according to claim 1, wherein the connecting portion between the opening end of the fluid dividing member fluid and the short pipe has a smooth curved surface.
【請求項3】 流体分割部材の流体噴出流路出口部以降
の流路断面が急拡大しないように、流路断面が徐々に拡
大するダクト壁面を有することを特徴とする請求項1ま
たは2記載の流体混合設置。
3. The fluid dividing member according to claim 1, further comprising a duct wall having a gradually increasing flow path cross section so that the flow path cross section after the fluid ejection flow path outlet portion of the fluid dividing member does not suddenly expand. Fluid mixing installation.
【請求項4】 流体の不均質の度合が大きい部分に対応
する流路分割部材の開口部を他の流路分割部材の開口部
より上流側に設けたことを特徴とする流体混合装置。
4. A fluid mixing device, wherein an opening of a flow path dividing member corresponding to a portion where the degree of fluid heterogeneity is large is provided upstream of openings of other flow path dividing members.
JP2001114449A 2001-04-12 2001-04-12 Fluid mixing device Expired - Lifetime JP4580580B2 (en)

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Application Number Priority Date Filing Date Title
JP2001114449A JP4580580B2 (en) 2001-04-12 2001-04-12 Fluid mixing device

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JP2002306939A true JP2002306939A (en) 2002-10-22
JP4580580B2 JP4580580B2 (en) 2010-11-17

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005021885A (en) * 2003-06-10 2005-01-27 Yoshiro Wakimura Stirring apparatus
WO2013145867A1 (en) * 2012-03-29 2013-10-03 株式会社村田製作所 Exhaust gas treatment method, and exhaust gas treatment apparatus
JP2016203032A (en) * 2015-04-15 2016-12-08 三菱日立パワーシステムズインダストリー株式会社 Mixer of fluid and denitration device provided with the mixer of fluid
JP2020032391A (en) * 2018-08-31 2020-03-05 三菱日立パワーシステムズ株式会社 Exhaust gas purification device

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07227528A (en) * 1994-02-17 1995-08-29 Kansai Electric Power Co Inc:The Method for mixing fluid and device therefor
JP2001000849A (en) * 1999-06-22 2001-01-09 Takuma Co Ltd Premixer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07227528A (en) * 1994-02-17 1995-08-29 Kansai Electric Power Co Inc:The Method for mixing fluid and device therefor
JP2001000849A (en) * 1999-06-22 2001-01-09 Takuma Co Ltd Premixer

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005021885A (en) * 2003-06-10 2005-01-27 Yoshiro Wakimura Stirring apparatus
WO2013145867A1 (en) * 2012-03-29 2013-10-03 株式会社村田製作所 Exhaust gas treatment method, and exhaust gas treatment apparatus
JPWO2013145867A1 (en) * 2012-03-29 2015-12-10 株式会社村田製作所 Exhaust gas treatment method and exhaust gas treatment apparatus
JP2016203032A (en) * 2015-04-15 2016-12-08 三菱日立パワーシステムズインダストリー株式会社 Mixer of fluid and denitration device provided with the mixer of fluid
JP2020032391A (en) * 2018-08-31 2020-03-05 三菱日立パワーシステムズ株式会社 Exhaust gas purification device
KR20210035240A (en) * 2018-08-31 2021-03-31 미츠비시 파워 가부시키가이샤 Flue gas purification device
JP7182956B2 (en) 2018-08-31 2022-12-05 三菱重工業株式会社 Exhaust gas purifier
KR102491279B1 (en) 2018-08-31 2023-01-27 미츠비시 파워 가부시키가이샤 flue gas purifier

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