WO2016170679A1 - Mixing device - Google Patents

Mixing device Download PDF

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Publication number
WO2016170679A1
WO2016170679A1 PCT/JP2015/062526 JP2015062526W WO2016170679A1 WO 2016170679 A1 WO2016170679 A1 WO 2016170679A1 JP 2015062526 W JP2015062526 W JP 2015062526W WO 2016170679 A1 WO2016170679 A1 WO 2016170679A1
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Prior art keywords
materials
mixing
supplied
mixed
heating unit
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PCT/JP2015/062526
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French (fr)
Japanese (ja)
Inventor
佐藤 義雄
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株式会社長野セラミックス
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Priority to PCT/JP2015/062526 priority Critical patent/WO2016170679A1/en
Priority to JP2017513932A priority patent/JP6571762B2/en
Publication of WO2016170679A1 publication Critical patent/WO2016170679A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00Feeding or distributing other fuel to combustion apparatus
    • F23K5/02Liquid fuel
    • F23K5/08Preparation of fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00Feeding or distributing other fuel to combustion apparatus
    • F23K5/02Liquid fuel
    • F23K5/08Preparation of fuel
    • F23K5/10Mixing with other fluids
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00Feeding or distributing other fuel to combustion apparatus
    • F23K5/02Liquid fuel
    • F23K5/14Details thereof
    • F23K5/22Vaporising devices

Definitions

  • the present invention relates to a mixing device for reliably mixing a plurality of materials and increasing the closeness between the materials.
  • Patent Document 1 a configuration of a mixing apparatus for fuel oil and water. It has been. Specifically, an inner pipe in which a large number of pores are formed at regular intervals is attached, the inlet and the inner pipe are connected, and the liquid flowing from the inlet to the inner pipe passes through the pores and flows out from the outlet. A configuration is disclosed in which a plurality of atomizers provided in series are connected in series. With such a configuration, it is possible to continuously reduce the size of the liquid droplets.
  • the mixture begins to separate immediately after mixing, and when it reaches the burner, the separation proceeds and causes incomplete combustion.
  • the mixed state of the mixture after being discharged may be unstable and separated, and the mixture is discharged from the discharge port in an insufficiently mixed state, and the combustion of the mixture is not stable. There are challenges.
  • an object of the present invention is to provide a mixing apparatus capable of increasing the mixing state (closeness) between a plurality of materials to be mixed and making a good mixing state.
  • the mixing apparatus of the present invention has the following configuration. That is, the present invention is a mixing device for mixing a plurality of materials to increase the closeness between the materials, and has a heating means, heating a plurality of supplied materials to vaporize, and rotating A stirrer that is connected to a shaft and has a rotating blade that is rotatably arranged around the rotating shaft, is heated by the heating unit, is supplied with a plurality of vaporized materials, and is stirred by the rotating blade And a mixed material is produced. According to this configuration, it is possible to enhance the mixing action of a plurality of materials to be mixed and to generate a mixed material in a good mixed state.
  • the internal space of the heating unit may be heated to a temperature equal to or higher than the boiling point of the supplied material. According to this, since the material passes through the heating unit heated to the boiling point of the supplied material or more, the material is vaporized.
  • the material may be water and heavy oil A. According to this, even water and A heavy oil can be mixed uniformly, and the resulting mixed material is difficult to re-separate, and a stable flame can be obtained when burned.
  • the mixing apparatus of the present invention it is possible to increase the mixing state (closeness) between a plurality of materials to be mixed and to achieve a good mixing state.
  • FIG. 1 shows a schematic diagram of a mixing apparatus 10 according to the present embodiment.
  • the mixing apparatus 10 concerning this Embodiment has the heating part 20 and the stirring part 40, as shown in FIG.
  • the heating unit 20 includes a heating unit 24, and a plurality of materials supplied from the material supply port 22 are heated by the heating unit 20 and vaporized in the heating unit 20.
  • the heating unit 20 and the stirring unit 40 communicate with each other through the communication unit 30, and a plurality of materials heated and vaporized by the heating unit 20 pass through the communication unit 30 and are supplied to the stirring unit 40.
  • the stirring unit 40 includes a rotating blade 44 that is connected to a rotating shaft 42 and is disposed so as to be rotatable about the rotating shaft 42.
  • the plurality of materials supplied from the heating unit 20 are agitated by the rotary blades 44 together with the air flowing in from the air inlet 46, and are fed forward while being mixed, and the mixed material is discharged from the discharge port 48.
  • the stirrer 40 since the plurality of materials that are heated and vaporized are uniformly mixed, the closeness is increased, and the flame is stabilized even if the generated mixed material is burned.
  • the arrow in a heating part 20, the communication part 30, and the stirring part 40 in a figure, and the arrow of a dotted line show the flow of the substance in each inside.
  • the inside of the heating unit 20 is heated to a temperature close to or higher than the boiling point of the supplied material depending on the supplied material.
  • the heating means 24 can be heated to a temperature close to or higher than the boiling point of the supplied material, and is arranged in the heating unit 20 and has a structure in which there is a space through which the material can pass.
  • the heating means 24 shown in FIG. 1 is one, it is also possible to provide a plurality of heating means 24, which are connected to each other. The supplied material is sufficiently heated and vaporized while passing around the heating means 24.
  • the vaporized material When the supplied material is heated around the heating means 24, the vaporized material is added to the force of a plurality of materials supplied from the material supply port 22 and flows into the communication unit 30.
  • the plurality of materials before passing through the communication part 30 do not necessarily have the same vaporization temperature, so that there are some materials in which the vaporized materials are separated and others in a mixed state. In order to bring this separated vaporized product into a good mixed state, it is sent to the stirring unit 40 and stirred by the stirring unit 40.
  • the communication part 30 should just be a position and a structure which can pass the vaporized vapor, and in the mixing apparatus 10 of this embodiment, the communication part 30 is provided in the lower part of the stirring part 40.
  • the stirring unit 40 is provided with an air inlet 46 so that air is sent from outside the mixing device 10 into the stirring unit 40, and the air inlet 46 is arranged in the stirring unit 40 in an arrangement facing the communication unit 30. ing. Furthermore, a blower (not shown) may be provided in the air inlet 46. The vaporized material rises in the stirring unit 40 together with the air sent from the blower due to the pushing force of the vapor flowing into the stirring unit 40 and the high temperature of the vapor sent from the communication unit 30. It becomes the flow to do. And the discharge outlet 48 should just be located in the upper part of a side surface like FIG. In FIG.
  • the rotating shaft 42 is disposed so as to stand upright in the stirring unit 40, and each rotating blade 44 connected to the rotating shaft 42 rotates around the rotating shaft 42.
  • the rotating shaft 42 is not necessarily upright, and the rotating shaft 42 may be inclined with respect to the horizontal plane so that the vaporized substance rises in the stirring unit 40 and moves toward the discharge port 48.
  • FIG. 1 shows an example in which the internal space of the stirring unit 40 is divided into three mixing chambers.
  • the mixing chambers are a first mixing chamber 50, a second mixing chamber 52, and a third mixing chamber 54, respectively.
  • Above the first mixing chamber 50 there is a second mixing chamber 52, and above the second mixing chamber 52, there is a third mixing chamber 54, which are in communication with each other.
  • the vaporized material flowing in from the communication part 30 enters the first mixing chamber 50, and then the vaporized material flows upward in the order of the first mixing chamber 50, the second mixing chamber 52, and the third mixing chamber 54.
  • the whole blade in the stirring unit 40 is referred to as the rotary blade 44
  • the one in the first mixing chamber 50 is the rotary blade 60
  • the one in the second mixing chamber 52 is the rotary blade 62
  • the second one is distinguished as rotating blades 64.
  • the mixed material can be generated by the rotating blades 64 provided in the third mixing chamber 54 and the mixed material sufficiently mixed can be sent to the discharge port 48.
  • Each room has a different size, the first mixing chamber 50 being the largest, and then the second mixing chamber 52 being the largest.
  • the outer shape of the stirring unit 40 may be a cone shape or a truncated cone shape that decreases upward, and the inner space of the stirring unit 40 with respect to the direction along the flow path of the airflow. The cross-sectional area becomes smaller.
  • the size of the rotary blade 44 and the number of blades are different.
  • the first mixing chamber 50 has three rotary blades 60 with six blades
  • the second mixing chamber 52 has one rotary blade 62 with eight blades.
  • the rotating blades 62 in the second mixing chamber 52 have smaller blades and more blades than the rotating blades 60 in the first mixing chamber 50.
  • the rotary blade 60 of the first mixing chamber 50 and the rotary blade 62 of the second mixing chamber 52 are connected to the outer peripheral surface of the rotary shaft 42.
  • the uppermost third mixing chamber 54 is provided with one rotary blade 64 at the tip of the rotary shaft 42.
  • a plurality of rotary blades 44 are provided, and the size of the rotary blades 44 is reduced upward so as to increase the number of the rotary blades 44, whereby vaporized substances can be mixed more uniformly and finely. Since the obtained mixed material is difficult to separate and stable, a stable flame can be obtained by discharging from the discharge port 48 and igniting.
  • the stirring unit 40 the vaporized material flowing in from the communication unit 30 and a part of the stirred mixed gas may be aggregated, and a mixed material containing the mixed gas is generated.
  • the power of the rotating blades 44 and the rotating shaft 42 is the force that a plurality of materials supplied from the material supply port 22 flows in, that is, the force and the air flow that the vaporized material vaporized in the heating unit 20 flows into the stirring unit 40. This is due to the force of air flowing in from the inlet 46. For this reason, the rotary blade 44 and the rotary shaft 42 rotate naturally. Along with this, there is also added by the rising vapor of the warmed vapor.
  • the material supplied to the heating unit 20 may be either solid or liquid, and at least one material may be solid or liquid, and the state of other materials may be different.
  • the material supplied to the heating unit 20 is vaporized when heated by the heating unit 20, and at least one of the materials becomes fuel.
  • the heating temperature by the heating means 24 is 280 ° C. or higher, and can be raised to a temperature at which the supplied material is hard to be carbonized, more preferably 300 to 400 ° C.
  • the heating temperature is appropriately changed according to the supplied material.
  • water and A heavy oil can be cited. In this case, the heating means 24 heats the material to a boiling point higher than the boiling point of the A heavy oil having the highest boiling point among the supplied materials.
  • a plurality of material supply ports 22 of the heating unit 20 may be provided, or another material supply port 22 may be provided for each material.
  • a mixing nozzle may be provided in front of the material supply port 22 and a mixture of a plurality of materials may be supplied to the material supply port 22.
  • a nozzle may be provided at the discharge port 48, and the mixed material may be jetted and ignited to emit a flame.

Abstract

Provided is a mixing device capable of improving the mixed state (degree of closeness) of a plurality of materials serving as objects to be mixed, and achieving an excellent mixed state. This mixing device (10) is for mixing a plurality of materials and improving the degree of closeness therebetween. The mixing device (10) is equipped with: a heating unit (20) which has a heating means (24), and heats and vaporizes the supplied plurality of materials; and a stirring unit (40) which has a rotary vane (44) connected to a rotary shaft (42) and disposed so as to be rotatable about the rotary shaft (42), and is supplied with the plurality of materials heated by the heating unit (20), the plurality of materials being stirred by the rotary vane (44). The mixing device produces a mixed material.

Description

混合装置Mixing equipment
 本願発明は、複数の材料を確実に混合させて互いの材料どうしの密接度を高めるための混合装置に関する。 The present invention relates to a mixing device for reliably mixing a plurality of materials and increasing the closeness between the materials.
 従来、燃料油と水とを混合した後の混合物をバーナーに送って燃焼させる燃焼装置があり、燃料油と水との混合装置の構成として、特許文献1に開示されているような構成が知られている。具体的には、多数の細孔を一定間隔で形成した内管を取り付け、流入口と内管を接続して、流入口から内管へ流れ込んだ液体が細孔を通過して吐出口より流出可能に設けた細粒化器を直列に複数個連続させる構成が開示されている。このような構成により、液粒のサイズを連続的に小さくすることが可能とされている。 2. Description of the Related Art Conventionally, there is a combustion apparatus that sends a mixture after mixing fuel oil and water to a burner and combusts it, and a configuration disclosed in Patent Document 1 is known as a configuration of a mixing apparatus for fuel oil and water. It has been. Specifically, an inner pipe in which a large number of pores are formed at regular intervals is attached, the inlet and the inner pipe are connected, and the liquid flowing from the inlet to the inner pipe passes through the pores and flows out from the outlet. A configuration is disclosed in which a plurality of atomizers provided in series are connected in series. With such a configuration, it is possible to continuously reduce the size of the liquid droplets.
特開2008-164257号公報JP 2008-164257 A
 混合物は、混合した直後から分離し始め、バーナーに達したときは分離が進行して不完全燃焼の原因となる。特許文献1に開示されている混合装置では、吐出された後の混合物の混合状態が安定せず分離することがあり、不十分な混合状態で吐出口から吐出され、混合物の燃焼が安定しないという課題がある。 The mixture begins to separate immediately after mixing, and when it reaches the burner, the separation proceeds and causes incomplete combustion. In the mixing apparatus disclosed in Patent Literature 1, the mixed state of the mixture after being discharged may be unstable and separated, and the mixture is discharged from the discharge port in an insufficiently mixed state, and the combustion of the mixture is not stable. There are challenges.
 そこで、本願発明は、混合対象となる複数の材料どうしの混合状態(密接度)を高め、良好な混合状態にすることが可能な混合装置を提供することを目的としている。 Therefore, an object of the present invention is to provide a mixing apparatus capable of increasing the mixing state (closeness) between a plurality of materials to be mixed and making a good mixing state.
 上記の目的を達成するため、本発明の混合装置は次の構成を備える。すなわち本発明は、複数の材料を混合させて材料どうしの密接度を高めるための混合装置であって、加熱手段を有し、供給された複数の材料を加熱して気化させる加熱部と、回転軸に連結され、前記回転軸を中心に回転可能に配設された回転羽根を有し、前記加熱部で加熱され、気化された複数の材料が供給され、前記回転羽根によって撹拌される撹拌部とを具備し、混合材料を生成することを特徴とする。この構成によれば、混合対象となる複数の材料どうしの混合作用を高め、良好な混合状態の混合材料を生成することが可能である。 In order to achieve the above object, the mixing apparatus of the present invention has the following configuration. That is, the present invention is a mixing device for mixing a plurality of materials to increase the closeness between the materials, and has a heating means, heating a plurality of supplied materials to vaporize, and rotating A stirrer that is connected to a shaft and has a rotating blade that is rotatably arranged around the rotating shaft, is heated by the heating unit, is supplied with a plurality of vaporized materials, and is stirred by the rotating blade And a mixed material is produced. According to this configuration, it is possible to enhance the mixing action of a plurality of materials to be mixed and to generate a mixed material in a good mixed state.
 また、本発明において、前記加熱部の内部空間は、供給される前記材料の沸点以上の温度に加熱されてもよい。これによれば、材料は、供給される材料の沸点以上に加熱された加熱部を通過するので、材料が気化される。 In the present invention, the internal space of the heating unit may be heated to a temperature equal to or higher than the boiling point of the supplied material. According to this, since the material passes through the heating unit heated to the boiling point of the supplied material or more, the material is vaporized.
 また、本発明において、前記材料が水とA重油であってもよい。これによれば、水とA重油でも均一に混合でき、生成する混合材料が再分離しにくく、燃焼させた際には安定した炎が得られる。 In the present invention, the material may be water and heavy oil A. According to this, even water and A heavy oil can be mixed uniformly, and the resulting mixed material is difficult to re-separate, and a stable flame can be obtained when burned.
 本願発明の混合装置の構成によれば、混合対象となる複数の材料どうし混合状態(密接度)を高め、良好な混合状態にすることが可能になる。 According to the configuration of the mixing apparatus of the present invention, it is possible to increase the mixing state (closeness) between a plurality of materials to be mixed and to achieve a good mixing state.
本願発明の実施形態にかかる混合装置の概略構成を示す図である。It is a figure which shows schematic structure of the mixing apparatus concerning embodiment of this invention.
 以下、本願発明の混合装置10について実施形態に基づいて説明する。 Hereinafter, the mixing apparatus 10 of the present invention will be described based on the embodiments.
 図1に、本実施形態にかかる混合装置10の概略図を示す。本実施の形態にかかる混合装置10は、図1に示すように、加熱部20と撹拌部40とを有している。加熱部20は、加熱手段24を有し、材料供給口22から供給された複数の材料が加熱部20で加熱されて加熱部20内で気化する。加熱部20と撹拌部40とは連通部30で連通していて、加熱部20で加熱されて気化された複数の材料が連通部30を通過して撹拌部40に供給される。撹拌部40は、回転軸42に連結され、回転軸42を中心に回転可能に配設された回転羽根44を有している。加熱部20から供給された複数の材料は、空気流入口46から流入した空気と共に、回転羽根44によって撹拌され、混合されながら先送りされ、吐出口48から混合材料が吐出する。撹拌部40では、加熱して気化された複数の材料が均一に混合されるので、密接度が高まり、生成した混合材料を燃焼させても炎が安定する。なお、図中の加熱部20、連通部30、撹拌部40内にある矢印、点線の矢印は、ぞれぞれの内部での物質の流れを示したものである。 FIG. 1 shows a schematic diagram of a mixing apparatus 10 according to the present embodiment. The mixing apparatus 10 concerning this Embodiment has the heating part 20 and the stirring part 40, as shown in FIG. The heating unit 20 includes a heating unit 24, and a plurality of materials supplied from the material supply port 22 are heated by the heating unit 20 and vaporized in the heating unit 20. The heating unit 20 and the stirring unit 40 communicate with each other through the communication unit 30, and a plurality of materials heated and vaporized by the heating unit 20 pass through the communication unit 30 and are supplied to the stirring unit 40. The stirring unit 40 includes a rotating blade 44 that is connected to a rotating shaft 42 and is disposed so as to be rotatable about the rotating shaft 42. The plurality of materials supplied from the heating unit 20 are agitated by the rotary blades 44 together with the air flowing in from the air inlet 46, and are fed forward while being mixed, and the mixed material is discharged from the discharge port 48. In the stirrer 40, since the plurality of materials that are heated and vaporized are uniformly mixed, the closeness is increased, and the flame is stabilized even if the generated mixed material is burned. In addition, the arrow in a heating part 20, the communication part 30, and the stirring part 40 in a figure, and the arrow of a dotted line show the flow of the substance in each inside.
 加熱部20内は、供給される材料に応じて、供給される材料の沸点に近い、またはそれ以上の温度に加熱される。加熱手段24は、供給される材料の沸点に近く、またはそれ以上の温度に加熱できるものであり、加熱部20内に配置され、その周囲に材料が通過できる空間がある構成となっている。図1に示す加熱手段24は1台であるが、複数台の加熱手段24を設けることも可能であり、それぞれを連結させて配置する。供給された材料は、加熱手段24の周囲を通過しながら十分に加熱されて気化する。 The inside of the heating unit 20 is heated to a temperature close to or higher than the boiling point of the supplied material depending on the supplied material. The heating means 24 can be heated to a temperature close to or higher than the boiling point of the supplied material, and is arranged in the heating unit 20 and has a structure in which there is a space through which the material can pass. Although the heating means 24 shown in FIG. 1 is one, it is also possible to provide a plurality of heating means 24, which are connected to each other. The supplied material is sufficiently heated and vaporized while passing around the heating means 24.
 供給された材料が加熱手段24の周囲で加熱されると、気化された材料は材料供給口22から供給される複数の材料が流入してくる力も加わって気流となり、連通部30に送られる。連通部30を通過する前の複数の材料は、必ずしも気化温度が同じではないため、それぞれの気化物が分離している状態のものもあれば、混合している状態のものもある。この分離している気化物を良好な混合状態にさせるために撹拌部40に送り、撹拌部40で撹拌させる。連通部30は気化した気化物が通過できる位置および構成であればよく、本実施形態の混合装置10では、撹拌部40の下部に連通部30が設けられている。 When the supplied material is heated around the heating means 24, the vaporized material is added to the force of a plurality of materials supplied from the material supply port 22 and flows into the communication unit 30. The plurality of materials before passing through the communication part 30 do not necessarily have the same vaporization temperature, so that there are some materials in which the vaporized materials are separated and others in a mixed state. In order to bring this separated vaporized product into a good mixed state, it is sent to the stirring unit 40 and stirred by the stirring unit 40. The communication part 30 should just be a position and a structure which can pass the vaporized vapor, and in the mixing apparatus 10 of this embodiment, the communication part 30 is provided in the lower part of the stirring part 40. FIG.
 撹拌部40には混合装置10外から空気が撹拌部40内に送られるよう、空気流入口46が設けられ、空気流入口46は、連通部30と対向する配列で撹拌部40に配設されている。さらには、空気流入口46内に図示しない送風機が設けられていてもよい。撹拌部40に流入する気化物の流れる押出力があることと、連通部30から送られてくる気化物の温度が高いことにより、送風機から送られた空気と共に気化物は撹拌部40内では上昇する流れとなる。そして、吐出口48は図1のように側面上方にあり、撹拌部40の上部に位置すればよい。図1では回転軸42は撹拌部40内で直立するように配設され、回転軸42に連結されたそれぞれの回転羽根44は回転軸42を中心にして回転する。しかし、必ずしも回転軸42は直立ではなくてもよく、気化物が撹拌部40内で上昇して吐出口48に向かうよう、回転軸42は水平面に対して傾斜していてもよい。 The stirring unit 40 is provided with an air inlet 46 so that air is sent from outside the mixing device 10 into the stirring unit 40, and the air inlet 46 is arranged in the stirring unit 40 in an arrangement facing the communication unit 30. ing. Furthermore, a blower (not shown) may be provided in the air inlet 46. The vaporized material rises in the stirring unit 40 together with the air sent from the blower due to the pushing force of the vapor flowing into the stirring unit 40 and the high temperature of the vapor sent from the communication unit 30. It becomes the flow to do. And the discharge outlet 48 should just be located in the upper part of a side surface like FIG. In FIG. 1, the rotating shaft 42 is disposed so as to stand upright in the stirring unit 40, and each rotating blade 44 connected to the rotating shaft 42 rotates around the rotating shaft 42. However, the rotating shaft 42 is not necessarily upright, and the rotating shaft 42 may be inclined with respect to the horizontal plane so that the vaporized substance rises in the stirring unit 40 and moves toward the discharge port 48.
 図1に示すように、回転羽根44は回転軸42の複数箇所に連結されている。また、撹拌部40の内部空間は、複数の混合室に区分けされている。図1は一例として撹拌部40の内部空間を3部屋の混合室に区分けした形態を示している。混合室はそれぞれ第1混合室50、第2混合室52、第3混合室54とする。第1混合室50の上方には第2混合室52、第2混合室52の上方には第3混合室54があり、それぞれの混合室は互いに連通している。まず、連通部30から流入した気化物は第1混合室50に入り、その後、第1混合室50、第2混合室52、第3混合室54の順に気化物が上方に向けて流れる。なお、回転羽根について、撹拌部40にある全体のものについて述べるときは回転羽根44とし、第1混合室50にあるものは回転羽根60、第2混合室52にあるものは回転羽根62、第3混合室54にあるものは回転羽根64として区別する。第1混合室50に設けられた回転羽根60および第2混合室52に設けられた回転羽根62により、気化物は撹拌されながら搬送され、良好な混合状態の混合材料を生成することができる。第3混合室54に設けられた回転羽根64により混合材料を生成すると共に、吐出口48に十分に混合された混合材料を送ることができる。各部屋の大きさはそれぞれ異なり、第1混合室50が最も大きく、次いで第2混合室52が大きい。図示はしていないが、撹拌部40の外形状は、上方に向けて小さくなる錐体形状もしくは錐台形状であってもよく、気流の流路に沿った方向に対する撹拌部40の内部空間の断面積が小さくなる。 As shown in FIG. 1, the rotary blade 44 is connected to a plurality of locations of the rotary shaft 42. Moreover, the internal space of the stirring unit 40 is divided into a plurality of mixing chambers. FIG. 1 shows an example in which the internal space of the stirring unit 40 is divided into three mixing chambers. The mixing chambers are a first mixing chamber 50, a second mixing chamber 52, and a third mixing chamber 54, respectively. Above the first mixing chamber 50, there is a second mixing chamber 52, and above the second mixing chamber 52, there is a third mixing chamber 54, which are in communication with each other. First, the vaporized material flowing in from the communication part 30 enters the first mixing chamber 50, and then the vaporized material flows upward in the order of the first mixing chamber 50, the second mixing chamber 52, and the third mixing chamber 54. Regarding the rotary blades, the whole blade in the stirring unit 40 is referred to as the rotary blade 44, the one in the first mixing chamber 50 is the rotary blade 60, the one in the second mixing chamber 52 is the rotary blade 62, the second one. Those in the three mixing chambers 54 are distinguished as rotating blades 64. By the rotary blades 60 provided in the first mixing chamber 50 and the rotary blades 62 provided in the second mixing chamber 52, the vaporized material is conveyed while being stirred, and a mixed material in a good mixed state can be generated. The mixed material can be generated by the rotating blades 64 provided in the third mixing chamber 54 and the mixed material sufficiently mixed can be sent to the discharge port 48. Each room has a different size, the first mixing chamber 50 being the largest, and then the second mixing chamber 52 being the largest. Although not illustrated, the outer shape of the stirring unit 40 may be a cone shape or a truncated cone shape that decreases upward, and the inner space of the stirring unit 40 with respect to the direction along the flow path of the airflow. The cross-sectional area becomes smaller.
 回転羽根44の大きさ、羽根の枚数はそれぞれ異なる。図1に示す撹拌部40には、第1混合室50には6枚の羽根が付いた回転羽根60が3基、第2混合室52には8枚の羽根が付いた回転羽根62が1基ある。第2混合室52にある回転羽根62は、第1混合室50にある回転羽根60よりも羽根が小さく、羽根の枚数は多い。第1混合室50の回転羽根60と第2混合室52の回転羽根62は回転軸42の外周面に連結されている。また、最も上方にある第3混合室54には、回転軸42の先端部分に回転羽根64が1基設けられている。このような回転羽根44により、混合しながら吐出口48に混合気体を含む混合材料が送られる。複数の回転羽根44が設けられ、上方に向けて回転羽根44の大きさを小さくして枚数を多く配設することにより、気化物をより均一で細かく混合することができる。得られる混合材料は分離しにくく安定しているので、吐出口48から吐出させて点火すれば安定した炎が得られる。なお、撹拌部40内において、連通部30から流入してくる気化物、および撹拌された混合気体の一部が凝集していても構わなく、混合気体を含む混合材料を生成する。 The size of the rotary blade 44 and the number of blades are different. In the stirring unit 40 shown in FIG. 1, the first mixing chamber 50 has three rotary blades 60 with six blades, and the second mixing chamber 52 has one rotary blade 62 with eight blades. There are groups. The rotating blades 62 in the second mixing chamber 52 have smaller blades and more blades than the rotating blades 60 in the first mixing chamber 50. The rotary blade 60 of the first mixing chamber 50 and the rotary blade 62 of the second mixing chamber 52 are connected to the outer peripheral surface of the rotary shaft 42. The uppermost third mixing chamber 54 is provided with one rotary blade 64 at the tip of the rotary shaft 42. By such a rotary blade 44, the mixed material containing the mixed gas is sent to the discharge port 48 while mixing. A plurality of rotary blades 44 are provided, and the size of the rotary blades 44 is reduced upward so as to increase the number of the rotary blades 44, whereby vaporized substances can be mixed more uniformly and finely. Since the obtained mixed material is difficult to separate and stable, a stable flame can be obtained by discharging from the discharge port 48 and igniting. In the stirring unit 40, the vaporized material flowing in from the communication unit 30 and a part of the stirred mixed gas may be aggregated, and a mixed material containing the mixed gas is generated.
 回転羽根44および回転軸42の動力は、材料供給口22から供給される複数の材料が流入してくる力、すなわち、加熱部20で気化した気化物が撹拌部40へ流入する力および空気流入口46から空気が流入する力によるものである。このため、回転羽根44および回転軸42は自然に回転する。これと共に、温められた気化物の上昇気流によるものも加わる。 The power of the rotating blades 44 and the rotating shaft 42 is the force that a plurality of materials supplied from the material supply port 22 flows in, that is, the force and the air flow that the vaporized material vaporized in the heating unit 20 flows into the stirring unit 40. This is due to the force of air flowing in from the inlet 46. For this reason, the rotary blade 44 and the rotary shaft 42 rotate naturally. Along with this, there is also added by the rising vapor of the warmed vapor.
 なお、加熱部20に供給される材料は、固体、液体のどちらでもよく、少なくとも1つの材料が固体もしくは液体であり、他の材料の状態が異なっていてもよい。ただし、加熱部20に供給される材料は、加熱部20で加熱されたときに気化するものであり、少なくとも1つは燃料となるものである。加熱手段24による加熱温度は280℃以上であり、かつ供給された材料が炭化しにくい温度まで上げることができ、より好ましくは300~400℃である。加熱温度は供給される材料に応じて適宜変更する。供給される複数の材料の一例として、水とA重油が挙げられる。この場合は、加熱手段24により、供給される材料のうち最も高い沸点であるA重油の沸点以上に加熱される。 In addition, the material supplied to the heating unit 20 may be either solid or liquid, and at least one material may be solid or liquid, and the state of other materials may be different. However, the material supplied to the heating unit 20 is vaporized when heated by the heating unit 20, and at least one of the materials becomes fuel. The heating temperature by the heating means 24 is 280 ° C. or higher, and can be raised to a temperature at which the supplied material is hard to be carbonized, more preferably 300 to 400 ° C. The heating temperature is appropriately changed according to the supplied material. As an example of the plurality of materials to be supplied, water and A heavy oil can be cited. In this case, the heating means 24 heats the material to a boiling point higher than the boiling point of the A heavy oil having the highest boiling point among the supplied materials.
 加熱部20の材料供給口22は複数個設けてもよく、材料ごとに別の材料供給口22を設けてもよい。また他にも材料供給口22手前に混合ノズルを設け、複数の材料をあらかじめ混合したものを材料供給口22に供給してもよい。 A plurality of material supply ports 22 of the heating unit 20 may be provided, or another material supply port 22 may be provided for each material. In addition, a mixing nozzle may be provided in front of the material supply port 22 and a mixture of a plurality of materials may be supplied to the material supply port 22.
 吐出口48にはノズルを設けてもよく、混合材料が噴射され、着火されて炎が出るようにしてもよい。 A nozzle may be provided at the discharge port 48, and the mixed material may be jetted and ignited to emit a flame.

Claims (3)

  1.  複数の材料を混合させて材料どうしの密接度を高めるための混合装置であって、
     加熱手段を有し、供給された複数の材料を加熱して気化させる加熱部と、
     回転軸に連結され、前記回転軸を中心に回転可能に配設された回転羽根を有し、前記加熱部で加熱され、気化された複数の材料が供給され、前記回転羽根によって撹拌される撹拌部とを具備し、
     混合材料を生成することを特徴とする混合装置。
    A mixing device for mixing a plurality of materials to increase the closeness of the materials,
    A heating unit that has a heating means and heats and vaporizes the supplied materials;
    Stirring which is connected to a rotating shaft and has rotating blades arranged so as to be rotatable around the rotating shaft, and is heated by the heating unit and supplied with a plurality of vaporized materials and stirred by the rotating blades And comprising
    A mixing apparatus for producing a mixed material.
  2.  前記加熱部の内部空間は、供給される前記材料の沸点以上の温度に加熱されることを特徴とする請求項1に記載の混合装置。 The mixing apparatus according to claim 1, wherein the internal space of the heating unit is heated to a temperature equal to or higher than a boiling point of the supplied material.
  3.  前記材料が水とA重油であることを特徴とする請求項1または請求項2に記載の混合装置。 3. The mixing apparatus according to claim 1, wherein the materials are water and A heavy oil.
PCT/JP2015/062526 2015-04-24 2015-04-24 Mixing device WO2016170679A1 (en)

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JPS55158408A (en) * 1979-05-17 1980-12-09 Zink Co John Method of and apparatus for combusting liquid fuel with gas combustion burner
JPH0621732U (en) * 1992-08-21 1994-03-22 三菱重工業株式会社 Gas mixing equipment
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