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JP2008049306A - Apparatus for mixing gas - Google Patents

Apparatus for mixing gas Download PDF

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Publication number
JP2008049306A
JP2008049306A JP2006229996A JP2006229996A JP2008049306A JP 2008049306 A JP2008049306 A JP 2008049306A JP 2006229996 A JP2006229996 A JP 2006229996A JP 2006229996 A JP2006229996 A JP 2006229996A JP 2008049306 A JP2008049306 A JP 2008049306A
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gas
conduit
gas mixing
fluid
mixing device
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Takehiro Matsumoto
健宏 松本
Masayuki Sato
雅之 佐藤
Takehiko Kowatari
武彦 小渡
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Hitachi Ltd
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Hitachi Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To solve such a problem that the size of a system becomes larger or the output of the system is decreased since a main conduit of a long section is required or several devices are arranged in the main conduit to cause a pressure loss in a fluid when two fluids are mixed almost uniformly with each other. <P>SOLUTION: An auxiliary conduit is arranged through which an additional gas is made to pass and an outlet of the auxiliary conduit is arranged to be opened to the vicinity of the center of the main conduit through which a main gas is made to pass. A plate for dispersing the additional gas in the radial direction or a frustum-like structure, the cross-sectional area of which is made larger as the cross section near the auxiliary conduit is parted from the auxiliary conduit, is arranged in the vicinity of the center of the main conduit just after the outlet of the auxiliary conduit. A whirling member having a plurality of stator blades or rotor blades for forming a whirling flow in a current of the main gas is arranged for promoting the mixing of the additional gas with the main gas. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、産業機械の流体処理装置に係り、主たるガス流体を導く主導管内に添加ガスを供給して当該2種類のガス流体を主導管内で混合するガス混合装置の構造に関する。   The present invention relates to a fluid processing apparatus for an industrial machine, and relates to a structure of a gas mixing apparatus that supplies an additive gas into a main conduit for guiding a main gas fluid and mixes the two kinds of gas fluids in the main conduit.

大型トラック,バス等のディーゼルエンジンから、排出される排気ガスに含まれる窒素酸化物(以下、NOxと記す)は、光化学スモッグの原因となる物質である。NOxを排出する車両に対するNOxの排出規制の強化に伴い、排気ガス管内への脱硝装置の設置が提案されている。その除去(脱硝)方法として、毒性の無い尿素を還元剤として使用し、NOxを高効率で低減し得るようにすることが検討されている。   Nitrogen oxides (hereinafter referred to as NOx) contained in exhaust gas discharged from diesel engines such as large trucks and buses are substances that cause photochemical smog. With the strengthening of NOx emission regulations for vehicles that emit NOx, it has been proposed to install a denitration device in the exhaust gas pipe. As a removal (denitration) method, it has been studied to use non-toxic urea as a reducing agent so that NOx can be reduced with high efficiency.

たとえば、還元剤に尿素水を利用し、比較的低い温度領域から高いNOx低減率を得られるようにするために排気管内に配設されたNOx還元触媒を装備し、且つNOx還元触媒の上流側に還元剤として尿素水を添加するように構成した排気浄化装置において、排気管の長手方向における尿素水の添加位置とNOx還元触媒との間に尿素分解触媒を設け、尿素水を前段の尿素分解触媒にてアンモニアと二酸化炭素に分解させ、これにより得られた反応性の高いアンモニアによりNOxを効率良く還元処理したことにより、尿素水をそのままNOxと反応させる場合よりも比較的低い温度領域からNOxを還元浄化させることを可能とした排気浄化装置がある(例えば、特許文献1参照)。   For example, urea water is used as a reducing agent, and a NOx reduction catalyst disposed in the exhaust pipe is provided in order to obtain a high NOx reduction rate from a relatively low temperature range, and upstream of the NOx reduction catalyst In the exhaust gas purification apparatus configured to add urea water as a reducing agent, a urea decomposition catalyst is provided between the urea water addition position in the longitudinal direction of the exhaust pipe and the NOx reduction catalyst, and the urea water is decomposed in the preceding stage. The catalyst is decomposed into ammonia and carbon dioxide, and the NOx is efficiently reduced by the highly reactive ammonia obtained thereby, so that the NOx is released from a relatively low temperature range compared with the case where urea water is reacted with NOx as it is. There is an exhaust purification device that can reduce and purify the exhaust gas (for example, see Patent Document 1).

また、上記排気浄化装置の尿素分解触媒を配設しない排気浄化装置として、尿素SCRシステムがある(例えば、非特許文献1参照)。   Moreover, there is a urea SCR system as an exhaust purification device that does not include the urea decomposition catalyst of the exhaust purification device (for example, see Non-Patent Document 1).

特表2003−505638Special table 2003-505638 小高松男著「超低エミッションディーゼル機関への挑戦」日本機械学会誌、2002.10 Vol.105 No.1007、P.23Kodaka Matsuo “Challenge to Ultra Low Emission Diesel Engine” Journal of the Japan Society of Mechanical Engineers, 2002.10 Vol. 105 No. 1007, p. 23

従来の技術は、2種類の流体をほぼ均一に混合させる場合、長区間の主導管が必要であるか、主導管内にいくつかの装置を配して流体に圧力損失を与え、それにより混合を促進させる方法がとられてきた。   In the prior art, when two kinds of fluids are mixed almost uniformly, a long section main conduit is required, or several devices are arranged in the main conduit to give pressure loss to the fluid, thereby mixing the fluid. A way to promote it has been taken.

しかし、例えばトラック,バスなどに搭載する排気ガス処理装置は、長区間の主導管が必要である場合システムの大型化を招き好ましくない。また、当システムの圧力損失が大きい場合エンジンの出力低下につながってしまう。このためどの場合も車に搭載するには好ましくない。また他の産業機械においても同様の課題が発生することが予想される。   However, for example, an exhaust gas treatment device mounted on a truck, a bus or the like is not preferable because a large-sized main conduit is required, resulting in an increase in the size of the system. In addition, if the pressure loss of this system is large, the engine output will be reduced. It is not preferable to be mounted in any case the car for this purpose. In addition, similar problems are expected to occur in other industrial machines.

本発明は、短区間で効率よく2種類のガスを混合することができるガス混合装置を提供することを目的とする。好適には2種類ガス流体をほぼ均一に混合させ、かつコンパクトな構成で圧力損失を抑えることの可能なガス混合装置を提供することを目的とする。   An object of this invention is to provide the gas mixing apparatus which can mix two types of gas efficiently in a short area. An object of the present invention is to provide a gas mixing apparatus that can mix two kinds of gas fluids substantially uniformly and can suppress pressure loss with a compact configuration.

本発明においては上記目的を達成するために以下のように構成した。   In order to achieve the above object, the present invention is configured as follows.

なお、主たるガスが通過する主導管の中心付近に、主たるガスの流れに沿う方向に添加ガスを吐出する開口を備えた補助導管の出口開口を配置する。   An outlet opening of the auxiliary conduit having an opening for discharging the additive gas in a direction along the flow of the main gas is disposed near the center of the main conduit through which the main gas passes.

好適には、補助導管出口に対面する位置に、添加ガスを半径方向へ分散するための円環状板、もしくは主たるガスの流れに直角な面で断面したときの断面積が補助導管の出口から離れるに従い大きくなる錐台構造体を配設する。   Preferably, an annular plate for radially dispersing the additive gas at a position facing the auxiliary conduit outlet, or a cross-sectional area when crossed by a plane perpendicular to the main gas flow is separated from the outlet of the auxiliary conduit. A frustum structure that increases in size is disposed.

さらに、添加ガスと主たるガスの混合を促進するため、流れに旋回流を形成するための複数枚の静翼もしくは動翼を持つ旋回部材を配設する。   Further, in order to promote the mixing of the additive gas and the main gas, a swirling member having a plurality of stationary blades or moving blades for forming a swirling flow is provided.

本明細書中で言うガスとは、気体だけでなく微粒な液滴が混合したニ相流も含まれる。   The gas referred to in this specification includes not only a gas but also a two-phase flow in which fine droplets are mixed.

本発明によれば、
異なる2流体の流速の高低にかかわらず、効率良く短区間で均一に混合可能なガス混合装置が提供できる。
According to the present invention,
Regardless of the flow rate of two different fluids, it is possible to provide a gas mixing apparatus that can efficiently mix uniformly in a short section.

以下、本発明の実施例を図1乃至図8に示す図面を用いて説明する。   Embodiments of the present invention will be described below with reference to the drawings shown in FIGS.

本発明の第1の実施例を図1乃至図2を用いて説明する。図1は、本発明に係る第1の実施例を示すガス混合装置の一部断面図である。   A first embodiment of the present invention will be described with reference to FIGS. FIG. 1 is a partial cross-sectional view of a gas mixing apparatus showing a first embodiment according to the present invention.

添加ガスが通過する補助導管2が、主たるガスが通過する主導管1の側面から内部中心付近まで延び、その先端開口部(通路出口)が、主導管1を流れる主たるガスの軸流の下流方向に向けてL字型に屈曲して配設されている。   The auxiliary conduit 2 through which the additive gas passes extends from the side surface of the main conduit 1 through which the main gas passes to the vicinity of the inner center, and the tip opening (passage outlet) is downstream of the axial flow of the main gas flowing through the main conduit 1. It is bent and arranged in an L shape toward the head.

また、補助導管2の出口3の直後の主導管の中心付近に、補助導管2近傍の断面が補助導管2から離れるに従い断面積が大きくなる錐台構造体5が配設されている。錐台構造体5には錐台面にガスの流れを主導管1の中心部から放射状に均一に分散させるための所定高さを持った複数個の導板7が配設されている。   In addition, a frustum structure 5 whose cross-sectional area increases as the cross section near the auxiliary conduit 2 moves away from the auxiliary conduit 2 is disposed near the center of the main conduit immediately after the outlet 3 of the auxiliary conduit 2. The frustum structure 5 is provided with a plurality of guide plates 7 having a predetermined height for uniformly distributing the gas flow radially from the center of the main conduit 1 on the frustum surface.

また、錐台構造体5の下流側に、流れに旋回流を形成するための複数枚の静翼6Aを持つ旋回部材6が配設されている。ここで静翼6Aは12枚配設されているが、その枚数は導管に大きさ,ガス流の流速などによって適宜選択される。静翼6Aは主たる主導管1内のガス流の流線に対して傾けられており、実施例では錐台構造体5の外周部に等間隔に
12枚配置されている。
A swirling member 6 having a plurality of stationary blades 6A for forming a swirling flow in the flow is disposed downstream of the frustum structure 5. Here, twelve stationary blades 6A are arranged, and the number is appropriately selected depending on the size of the conduit, the flow rate of the gas flow, and the like. The stationary blades 6A are inclined with respect to the streamlines of the gas flow in the main main conduit 1. In the embodiment, twelve blades 6A are arranged at equal intervals on the outer periphery of the frustum structure 5.

次に補助導管2の効果について説明する。添加ガスを主導管1に導く補助導管2は主導管1の中心付近で主たるガスの下流側に向けて開口する。これにより添加ガスは主導管1および主導管1を通る主たるガスの中心付近に排出される。その結果、添加ガスや主たるガスの流速にかかわらず安定して添加ガスは主導管1の中心付近に安定供給されることになる。   Next, the effect of the auxiliary conduit 2 will be described. The auxiliary conduit 2 for guiding the additive gas to the main conduit 1 opens toward the downstream side of the main gas near the center of the main conduit 1. As a result, the added gas is discharged near the center of the main gas passing through the main conduit 1 and the main conduit 1. As a result, the additive gas is stably supplied near the center of the main conduit 1 regardless of the flow rate of the additive gas or the main gas.

次に錐台構造体5の効果について説明する。補助導管2の出口3の直後の主導管1の中心付近に、その断面が補助導管2から離れるに従い断面積が大きくなる錐台構造体5を配設することにより、主導管の中心部に供給された添加ガスは、主導管1の半径方向へ360°ほぼ均一に分散させられる。また、錘台面上に配設された導板7は添加ガスを均一分散させる効果を助長する。分散した添加ガスは主導管1を通る主たるガスと混合される。また、錐台構造体5直後の空間は、その抵抗のため渦が発生し、ガスの混合がより促進される。   Next, the effect of the frustum structure 5 will be described. By supplying a frustum structure 5 whose cross-sectional area increases as the distance from the auxiliary conduit 2 increases in the vicinity of the center of the main conduit 1 immediately after the outlet 3 of the auxiliary conduit 2, supply to the center of the main conduit 1 The added gas is distributed almost uniformly 360 ° in the radial direction of the main conduit 1. Further, the guide plate 7 disposed on the frustum surface promotes the effect of uniformly dispersing the additive gas. The dispersed additive gas is mixed with the main gas passing through the main conduit 1. Further, a vortex is generated in the space immediately after the frustum structure 5 due to its resistance, and gas mixing is further promoted.

次に旋回部材6の効果について説明する。補助導管2出口の直後の主導管1に、複数枚の静翼6Aを持つ旋回部材6を配設することにより、ガス流れに旋回流を形成し、添加ガスと主たるガスが攪拌され混合が促進される。なお、効率よく混合するためには静翼6Aの枚数は多いほどよく、8枚以上とすることが好ましい。また同様に効率よく混合するために静翼6Aの取り付け角度(傾斜角度)は主導管1の軸流方向(ガス流の流線方向)に対して45°以上とすることが好ましい。また、静翼6Aは傾きの調整可能な動翼によって構成することもできる。   Next, the effect of the turning member 6 will be described. A swirling member 6 having a plurality of stationary blades 6A is arranged in the main conduit 1 immediately after the outlet of the auxiliary conduit 2, thereby forming a swirling flow in the gas flow, and the additive gas and the main gas are stirred to promote mixing. Is done. For efficient mixing, the larger the number of stationary blades 6A, the better. Similarly, for efficient mixing, the attachment angle (tilt angle) of the stationary blade 6A is preferably 45 ° or more with respect to the axial flow direction (streamline direction of the gas flow) of the main conduit 1. The stationary blade 6A can also be configured by a moving blade whose inclination can be adjusted.

次に図3,図4に基づき本発明の第2の実施例について説明する。第2実施例では実施例1で構成される錐台構造体を円盤状の板4に変更し、システム構成部品の単純化を図ったものである。この場合、補助導管2の出口3から主導管1の中心部に供給された添加ガスは板4にほぼ垂直に衝突する。衝突した添加ガスは、板4の表層に沿って主導管1の半径方向へ360°ほぼ均一に分散させられる。このように単純な円盤形状でも実施例1と同等の効果が得られる。その後方に静翼6Aを備えた旋回部材6を配設し、ガスの流れに旋回力を与え、添加ガスと主たるガスが攪拌され混合を促進するのは実施例1と同様である。   Next, a second embodiment of the present invention will be described with reference to FIGS. In the second embodiment, the frustum structure configured in the first embodiment is changed to a disk-shaped plate 4 to simplify the system components. In this case, the additive gas supplied from the outlet 3 of the auxiliary conduit 2 to the central portion of the main conduit 1 collides with the plate 4 almost vertically. The impinging additive gas is distributed almost uniformly by 360 ° along the surface layer of the plate 4 in the radial direction of the main conduit 1. Even in such a simple disk shape, the same effect as in the first embodiment can be obtained. Similar to the first embodiment, the swirling member 6 provided with the stationary blade 6A is disposed on the rear side, the swirling force is applied to the gas flow, and the additive gas and the main gas are stirred to promote mixing.

次に図5,図6に基づき本発明の第3の実施例について説明する。第3実施例では実施例2で構成される円盤状の板4を旋回部材6と一体化し、更なるシステム構成部品の単純化を図ったものである。これによりシステムのコンパクト化,組み立て性向上を図ることができる。実施例3の性能はほぼ実施例2と同等である。   Next, a third embodiment of the present invention will be described with reference to FIGS. In the third embodiment, the disk-like plate 4 configured in the second embodiment is integrated with the swivel member 6 to further simplify system components. As a result, the system can be made compact and the assembly can be improved. The performance of the third embodiment is almost the same as that of the second embodiment.

具体的には、補助導管2の出口3に対面する位置に円盤状の端面を有する筒状体4Aを設け、この筒状体の周囲に静翼6Aを固定するものである。   Specifically, a cylindrical body 4A having a disc-shaped end face is provided at a position facing the outlet 3 of the auxiliary conduit 2, and the stationary blade 6A is fixed around the cylindrical body.

次に図7,図8に基づき本発明の第4の実施例について説明する。第4実施例では補助導管2の出口3に小型の錐台構造体8を配設したものである。これにより実施例1の錐台構造体を省略することができ、システムのコンパクト化を図ることができる。実施例4の性能はほぼ実施例2と同等である。なお、錐台構造体8の周囲には添加ガス出口8Aが複数個、半径方向外側に向かって開口している。   Next, a fourth embodiment of the present invention will be described with reference to FIGS. In the fourth embodiment, a small frustum structure 8 is disposed at the outlet 3 of the auxiliary conduit 2. Thereby, the frustum structure of Example 1 can be omitted, and the system can be made compact. The performance of Example 4 is almost the same as that of Example 2. In addition, a plurality of additive gas outlets 8A are opened around the frustum structure 8 toward the radially outer side.

なお、第3,4実施例において、筒状体4Aを回転可能に主導管1あるいは補助導管2に支持することで、旋回部材6を主導管1内で回転させることも可能である。この場合より一層ガスの混合が促進される。   In the third and fourth embodiments, the turning member 6 can be rotated in the main conduit 1 by rotatably supporting the cylindrical body 4A on the main conduit 1 or the auxiliary conduit 2. In this case, gas mixing is further promoted.

以上の各実施例に拠れば、異なる2種類の流体を均一に混合させるガス混合装置において、添加ガスと主たるガスとの混合を効果的に、省スペースで達成させることができる。   According to each of the embodiments described above, in the gas mixing device that uniformly mixes two different types of fluids, the mixing of the additive gas and the main gas can be effectively achieved in a space-saving manner.

実施例の態様を整理すると以下の通りである。
(1)請求項1記載のガス混合装置において、
添加ガスは導管を用いて、主たるガスが通過する主導管の中心付近に排出され、補助導管出口は、主導管の中心付近に開口することを特徴としたガス混合装置。
(2)前記ガス混合装置において、
前記補助導管出口下流の主導管内の中心付近に、添加ガスが主導管内の中心付近から半径方向へ分散するための板もしくは導管近傍の断面が導管から離れるに従い断面積が大きくなる錐台構造体を配設することを特徴としたガス混合装置。
(3)前記ガス混合装置において、
添加ガスが通過する補助導管出口の直後の主導管に、主導管内を通過する流体に旋回流を形成するための複数枚の静翼もしくは動翼を持つ旋回部材が配設されることを特徴としたガス混合装置。
The modes of the examples are summarized as follows.
(1) In the gas mixing device according to claim 1,
A gas mixing device characterized in that the additive gas is discharged near the center of the main conduit through which the main gas passes, and the auxiliary conduit outlet opens near the center of the main conduit.
(2) In the gas mixing device,
A plate for dispersing the additive gas in the radial direction from the vicinity of the center in the main conduit downstream from the outlet of the auxiliary conduit or a frustum structure having a cross-sectional area that increases in cross section as the distance from the conduit increases. A gas mixing device characterized by being arranged.
(3) In the gas mixing device,
A swirling member having a plurality of stationary blades or moving blades for forming a swirling flow in the fluid passing through the main conduit is disposed in the main conduit immediately after the auxiliary conduit outlet through which the additive gas passes. Gas mixing device.

実施例のガス混合装置に拠れば以下の作用効果が得られる。   According to the gas mixing apparatus of the embodiment, the following effects can be obtained.

主導管の中心付近に開口している導管を通じて、添加ガスは主導管の中心付近に効果的に排出される。   The additive gas is effectively discharged near the center of the main conduit through a conduit that opens near the center of the main conduit.

さらに、前記補助導管出口下流の主導管内の中心付近に、板もしくは導管近傍の断面が導管から離れるに従い断面積が大きくなる錐台構造体を配設することにより、添加ガスを主導管内の中心付近から半径方向へ分散させる。   Further, by arranging a plate or a frustum structure whose cross-sectional area increases as the distance from the conduit increases near the center in the main conduit downstream of the auxiliary conduit outlet, the additive gas is disposed near the center in the main conduit. To the radial direction.

さらに、補助導管出口の直後の主導管に、主導管内を通過する流体に旋回流を形成するための複数枚の静翼もしくは動翼を持つ旋回部材を配設することにより、添加ガスと主たるガスを攪拌し、効率的に混合を促進する。   Furthermore, the main gas immediately after the outlet of the auxiliary conduit is provided with a swirling member having a plurality of stationary blades or moving blades for forming a swirling flow in the fluid passing through the main conduit. To promote efficient mixing.

本発明をディーゼルエンジンで排出されるNOxを脱硝する尿素触媒装置に実施することにより、コンパクトな装置でありながら、効率良く排気ガスとアンモニアをミキシングできるため、高い脱硝率でNOxを除去することが可能である。   By implementing the present invention in a urea catalyst device that denitrates NOx discharged from a diesel engine, exhaust gas and ammonia can be mixed efficiently while being a compact device, so NOx can be removed at a high denitration rate. Is possible.

この場合、上記各実施例において補助導管2の上流には、尿素を気化させてアンモニアにする装置が取り付けられ、主たるガスはディーゼルエンジンの排気ガスであり、主導管1の上流端はディーゼルエンジンの排気管に接続され、下流端は、NOxを脱硝する尿素触媒装置に接続される。   In this case, in each of the above-described embodiments, a device for vaporizing urea into ammonia is attached upstream of the auxiliary conduit 2, the main gas is exhaust gas of the diesel engine, and the upstream end of the main conduit 1 is the diesel engine exhaust gas. Connected to the exhaust pipe, the downstream end is connected to a urea catalyst device for denitrating NOx.

よって、ディーゼルエンジンを使用する自動車産業をはじめとする種々の産業へ利用できる。また、それに類する工業機器へ使用した場合でもコンパクト化・高効率化の点で充分な効果が期待できる。   Therefore, it can utilize for various industries including the automobile industry which uses a diesel engine. In addition, even when used in industrial equipment similar to that, a sufficient effect can be expected in terms of compactness and high efficiency.

上記解決手段により、異なる2流体の流速の高低にかかわらず、効率良く短区間で均一に混合可能なガス混合装置の実現が可能になる。すなわち、主たるガスが通過する主導管中央に添加ガスが排出され、さらに、補助導管出口直後の主導管内の中心付近に、板もしくは錐台構造体により、添加ガスを主導管内の中心付近から半径方向へ分散させる。さらに、板もしくは錐台構造体直後の旋回部材により、添加ガスと主たるガスを攪拌し、効率的に混合を促進する。これにより、異なる2流体の流速の高低にかかわらず、効率良く短区間で均一に混合することが実現可能になった。   By the above solution, it is possible to realize a gas mixing device that can efficiently and uniformly mix in a short section regardless of the flow rates of two different fluids. That is, the additive gas is discharged to the center of the main conduit through which the main gas passes, and further, the additive gas is moved radially from the vicinity of the center of the main conduit by a plate or a frustum structure near the center of the main conduit immediately after the outlet of the auxiliary conduit. To disperse. Further, the additive gas and the main gas are agitated by the swiveling member immediately after the plate or the frustum structure, and the mixing is efficiently promoted. This makes it possible to achieve efficient and uniform mixing in a short section regardless of the flow rates of the two different fluids.

本発明は、異なる2種類のガス流体を短区間で均一に混合させるガス混合装置に係わるものである。ディーゼルエンジン車,ボイラなどに利用できる。   The present invention relates to a gas mixing apparatus that uniformly mixes two different types of gas fluids in a short section. It can be used for diesel engine cars and boilers.

本発明に係る第1の実施例のガス混合装置を示す図である。It is a figure which shows the gas mixing apparatus of the 1st Example which concerns on this invention. 本発明に係る図1に示したガス混合装置の鳥瞰図・一部断面図である。It is a bird's-eye view and a partial sectional view of the gas mixing apparatus shown in FIG. 1 according to the present invention. 本発明に係る実施例2で、図1の錘台構造体5を分散板4に置き換えた実施例を示す図である。FIG. 6 is a diagram showing an embodiment in which the frustum structure 5 of FIG. 1 is replaced with a dispersion plate 4 in Embodiment 2 according to the present invention. 本発明に係る図3に示したガス混合装置の鳥瞰図・一部断面図である。It is a bird's-eye view and a partial sectional view of the gas mixing apparatus shown in FIG. 3 according to the present invention. 本発明に係る実施例3で、実施例2で構成される板を旋回部材と一体化した実施例を示す図である。In Example 3 which concerns on this invention, it is a figure which shows the Example which integrated the board comprised in Example 2 with the turning member. 本発明に係る図5に示したガス混合装置の鳥瞰図・一部断面図である。It is a bird's-eye view and a partial sectional view of the gas mixing apparatus shown in FIG. 5 according to the present invention. 本発明に係る実施例4で、小型の錘台構造体を補助導管の出口に配設した実施例を示す図である。In Example 4 which concerns on this invention, it is a figure which shows the Example which has arrange | positioned the small frustum structure to the exit of an auxiliary | assistant conduit | pipe. 本発明に係る図7に示したガス混合装置の鳥瞰図・一部断面図である。It is a bird's-eye view and a partial sectional view of the gas mixing apparatus shown in FIG. 7 according to the present invention.

符号の説明Explanation of symbols

1…主導管、2…補助導管、3…補助導管の出口、4…板、5,8…錘台構造体、6…旋回部材、7…導板。   DESCRIPTION OF SYMBOLS 1 ... Main conduit, 2 ... Auxiliary conduit, 3 ... Exit of auxiliary conduit, 4 ... Plate, 5, 8 ... Frustum structure, 6 ... Turning member, 7 ... Guide plate.

Claims (20)

第一流体が流れる導管内に設置され、前記第一流体の流れに沿った方向に第二流体を供給するノズルを備えたものにおいて、
前記ノズルに設けられた前記第二流体の出口開口に対面して設置され、前記ノズルから供給される前記第二流体を前記導管の内壁方向に向かって導く流体分散機構を設けた
ことを特徴とするガス混合装置。
A nozzle that is installed in a conduit through which the first fluid flows and supplies a second fluid in a direction along the flow of the first fluid;
A fluid dispersion mechanism is provided to face the outlet opening of the second fluid provided in the nozzle and guide the second fluid supplied from the nozzle toward the inner wall of the conduit. Gas mixing device.
請求項1に記載したものにおいて、
さらに、前記分散機構によって分散された第二流体を前記第一流体に混合させる混合機構を前記分散機構の下流側の周囲に備えた
ことを特徴とするガス混合装置。
In claim 1,
Furthermore, the gas mixing apparatus characterized by having the mixing mechanism which mixes the 2nd fluid disperse | distributed by the said dispersion | distribution mechanism with the said 1st fluid around the downstream of the said dispersion | distribution mechanism.
請求項2に記載したものにおいて、
前記混合機構が前記分散機構を中心として、前記分散機構と前記導管の内壁との間に放射状に延び、かつ前記第一流体の流れに対して傾斜角度を有する複数枚の傾斜ブレードを含んで構成されている
ことを特徴とするガス混合装置。
In what is described in claim 2,
The mixing mechanism includes a plurality of inclined blades extending radially between the dispersing mechanism and the inner wall of the conduit around the dispersing mechanism and having an inclined angle with respect to the flow of the first fluid. A gas mixing device characterized by being made.
請求項1ないしは3のいずれかに記載のものにおいて、
前記分散機構が円盤部材を含んで構成される
ことを特徴とするガス混合装置。
In the thing in any one of Claim 1 thru | or 3,
The gas mixing apparatus, wherein the dispersion mechanism includes a disk member.
請求項1ないしは3のいずれかに記載のものにおいて、
前記分散機構が、前記ノズルに設けられた前記第二流体の出口開口に対面する位置にその頂点部を有する円錐面部材を含んで構成される
ことを特徴とするガス混合装置。
In the thing in any one of Claim 1 thru | or 3,
The gas mixing apparatus, wherein the dispersion mechanism includes a conical surface member having a vertex portion at a position facing the outlet opening of the second fluid provided in the nozzle.
請求項5に記載のものにおいて、
前記円錐面部材の表面であって、前記ノズルの出口開口に対面する頂点位置から半径方向外側に向かって放射状に伸びる複数枚のガイドブレードが設けられている
ことを特徴とするガス混合装置。
The thing of Claim 5 WHEREIN:
A gas mixing apparatus, comprising: a plurality of guide blades radially extending from an apex position facing the outlet opening of the nozzle and radially outward from the surface of the conical surface member.
第一流体を導く導管、
当該導管内に設置され、前記第一流体の流れに沿った方向に第二流体を供給する開口を備えたノズル、
当該開口に対面した位置に設けられ、前記第二流体を放射方向に分散させるガイド部材を備えた
ガス混合装置。
A conduit leading the first fluid,
A nozzle installed in the conduit and having an opening for supplying a second fluid in a direction along the flow of the first fluid;
A gas mixing device provided with a guide member provided at a position facing the opening and dispersing the second fluid in a radial direction.
請求項7に記載したものにおいて、
さらに、前記ガイド部材の下流側の周囲に設けられ、前記ガイド部材によって分散された第二流体を前記第一流体に混合させる混合機構を備える
ガス混合装置。
What is described in claim 7,
Furthermore, a gas mixing device provided with a mixing mechanism that is provided around the downstream side of the guide member and mixes the second fluid dispersed by the guide member with the first fluid.
請求項8に記載したものにおいて、
前記混合機構が、前記分散機構を中心として前記分散機構と前記導管の内壁との間に放射状に延び、かつ前記第一流体の流れに対して傾斜角度を有する複数枚の傾斜ブレードを備える
ガス混合装置。
What is described in claim 8,
Gas mixing comprising a plurality of inclined blades, the mixing mechanism extending radially between the dispersing mechanism and the inner wall of the conduit around the dispersing mechanism and having an inclined angle with respect to the flow of the first fluid apparatus.
請求項7に記載のものにおいて、
前記分散機構が、前記ノズルに設けられた前記第二流体の出口開口に対面する位置にその頂点部を有する円錐面部材を含んで構成される
ガス混合装置。
The thing of Claim 7 WHEREIN:
The gas mixing apparatus, wherein the dispersion mechanism includes a conical surface member having an apex portion at a position facing an outlet opening of the second fluid provided in the nozzle.
請求項7に記載のものにおいて、
前記ガイド部材が、前記ノズルの第二流体を供給する開口に対面して配置された円盤部材を備える
ものであるガス混合装置。
The thing of Claim 7 WHEREIN:
The gas mixing device, wherein the guide member includes a disk member arranged to face an opening for supplying the second fluid of the nozzle.
請求項10に記載のものにおいて、
前記円錐面部材は、前記ノズルの出口開口に対面する頂点位置から半径方向外側に向かって放射状に伸びる複数枚のガイドブレードを有する
ガス混合装置。
The thing of Claim 10 WHEREIN:
The conical member has a plurality of guide blades extending radially outward from a vertex position facing an outlet opening of the nozzle.
異なる2種類のガス流体を混合させるガス混合装置であり、
添加ガスを導く補助導管の出口が、主たるガスが通過する主導管の中心付近に開口して、当該開口から前記主たるガスの流れに沿った方向に前記添加ガスが供給されるよう構成されており、
さらに、前記補助導管の出口に対面する位置に添加ガスを放射方向に分散する分散機構を設けたことを特徴とするガス混合装置。
It is a gas mixing device that mixes two different types of gas fluids,
The outlet of the auxiliary conduit for guiding the additive gas opens near the center of the main conduit through which the main gas passes, and the additive gas is supplied from the opening in a direction along the flow of the main gas. ,
Furthermore, the gas mixing apparatus characterized by providing the dispersion | distribution mechanism which disperse | distributes addition gas to a radial direction in the position facing the exit of the said auxiliary | assistant conduit | pipe.
請求項13に記載のガス混合装置において、
前記分散機構は前記補助導管の出口の下流近傍にあって、前記主たるガスの流れに交差する面内に設置された円盤状の分散板である
ことを特徴とするガス混合装置。
The gas mixing device according to claim 13.
The gas mixing device according to claim 1, wherein the dispersion mechanism is a disc-like dispersion plate installed in a plane near the outlet of the auxiliary conduit and intersecting the main gas flow.
請求項13記載のガス混合装置において、
前記分散機構が、前記補助導管の出口に設けられた、主導管に対して放射状に前記添加ガスを吐出する複数個の開口によって構成されていることを特徴とするがス混合装置。
The gas mixing device according to claim 13.
The gas mixing device is characterized in that the dispersion mechanism is constituted by a plurality of openings provided at the outlet of the auxiliary conduit to discharge the additive gas radially to the main conduit.
請求項13記載のガス混合装置において、
前記添加ガスが吐出される前記補助導管の出口に対面して配置され、前記主たるガスの流れに直角な面で断面した時の断面積が前記補助導管の出口から離れるに従い大きくなる錐台構造体を有することを特徴とするガス混合装置。
The gas mixing device according to claim 13.
A frustum structure that is arranged to face the outlet of the auxiliary conduit through which the additive gas is discharged and has a cross-sectional area that increases as the distance from the outlet of the auxiliary conduit increases when the cross section is taken along a plane perpendicular to the flow of the main gas. A gas mixing apparatus comprising:
請求項13記載のガス混合装置において、
前記補助導管の出口の下流側に、前記主たるガスの流れに対して傾斜角度を持って放射状に配置された複数枚の静翼有することを特徴とするガス混合装置。
The gas mixing device according to claim 13.
A gas mixing apparatus comprising a plurality of stationary blades arranged radially at an inclination angle with respect to the main gas flow on the downstream side of the outlet of the auxiliary conduit.
請求項16記載のガス混合装置において、
前記錐台構造体の錐台面に前記添加ガスを径方向外側に導くための複数個の仕切り板を植立したことを特徴とするガス混合装置。
The gas mixing device according to claim 16, wherein
A gas mixing apparatus, wherein a plurality of partition plates for guiding the additive gas radially outward are planted on a frustum surface of the frustum structure.
請求項15記載のガス混合装置において、
前記補助導管の出口部に前記添加ガスの流れに対して上流側が凸となる円錐構造体を配設したことを特徴とするガス混合装置。
The gas mixing device according to claim 15, wherein
A gas mixing apparatus characterized in that a conical structure having a convex portion on the upstream side with respect to the flow of the additive gas is disposed at the outlet of the auxiliary conduit.
請求項18記載のガス混合装置において、
前記錐台構造体の仕切り板を前記錐台構造体の中心軸に対して傾斜角度を有する傾斜翼とし、かつ前記錐台構造体がその中心軸周りに回転可能に構成したことを特徴とするガス混合装置。
The gas mixing device according to claim 18,
The partition plate of the frustum structure is an inclined wing having an inclination angle with respect to the central axis of the frustum structure, and the frustum structure is configured to be rotatable around the central axis. Gas mixing device.
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