JP2017075381A - Spray coating material pressure feeding device - Google Patents
Spray coating material pressure feeding device Download PDFInfo
- Publication number
- JP2017075381A JP2017075381A JP2015204300A JP2015204300A JP2017075381A JP 2017075381 A JP2017075381 A JP 2017075381A JP 2015204300 A JP2015204300 A JP 2015204300A JP 2015204300 A JP2015204300 A JP 2015204300A JP 2017075381 A JP2017075381 A JP 2017075381A
- Authority
- JP
- Japan
- Prior art keywords
- ejector
- thermal spray
- pipe
- gas
- spray material
- 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
Links
- 239000000463 material Substances 0.000 title claims abstract description 73
- 238000005507 spraying Methods 0.000 title abstract description 11
- 239000007789 gas Substances 0.000 claims description 59
- 239000007921 spray Substances 0.000 claims description 48
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 238000002347 injection Methods 0.000 claims description 8
- 239000007924 injection Substances 0.000 claims description 8
- 239000012298 atmosphere Substances 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 238000002485 combustion reaction Methods 0.000 claims description 5
- 238000005086 pumping Methods 0.000 claims description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 239000000843 powder Substances 0.000 description 20
- 230000008439 repair process Effects 0.000 description 12
- 230000000694 effects Effects 0.000 description 11
- 238000000034 method Methods 0.000 description 9
- 238000007751 thermal spraying Methods 0.000 description 9
- 230000001603 reducing effect Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- 239000012159 carrier gas Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000011819 refractory material Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000011863 silicon-based powder Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Abstract
Description
本発明は耐火物ライニングの補修技術に関し、特に溶射補修に供せられる溶射材圧送装置に関するものである。 The present invention relates to a refractory lining repair technique, and more particularly to a thermal spray material feeding device used for thermal spray repair.
鉄鋼をはじめ、非鉄金属製錬、セメント製造やガラス製造、ゴミの焼却溶融などの産業用の窯炉において各種耐火物が広く使用されている。これら耐火物は化学反応や機械的、熱的衝撃により損耗を生じ、損耗部は吹き付け材などの不定形耐火物で補修される。 Various refractories are widely used in industrial kilns such as iron and steel, non-ferrous metal smelting, cement and glass manufacturing, and incineration and melting of garbage. These refractories are worn out by chemical reaction, mechanical and thermal shock, and the worn portions are repaired with an irregular refractory such as a spraying material.
窯炉の中で、コークス炉においては溶射補修が広く実施されており、その中でも、耐火性粉末と金属Si粉末の混合体からなる溶射材を、酸素をキャリアガスとして搬送し高温の被補修部位に吹き付けることによって金属Siと酸素を反応させ、反応によって発生する熱で耐火性粉末を溶融して被補修部に溶着させる方法が一般的となっている。 Among the kilns, thermal spray repair is widely performed in coke ovens. Among them, thermal spray material consisting of a mixture of refractory powder and metal Si powder is transported using oxygen as a carrier gas and repaired parts at high temperatures. In general, a method is used in which metal Si and oxygen are reacted by spraying, and the refractory powder is melted by heat generated by the reaction to be welded to the repaired portion.
溶射材の被補修面への搬送は図６に示すような溶射装置を用いて行われる。すなわち、溶射装置１０により燃焼補助ガスに混合された溶射材はフレキシブルホース６に供給され、ホースの先端に接続したランスパイプ７を通って先端のノズル８から被補修面に噴出される。 The thermal spray material is transported to the surface to be repaired using a thermal spraying apparatus as shown in FIG. That is, the thermal spray material mixed with the combustion auxiliary gas by the thermal spraying device 10 is supplied to the flexible hose 6 and is jetted from the nozzle 8 at the tip to the surface to be repaired through the lance pipe 7 connected to the tip of the hose.
溶射装置１０としては、開放されたホッパに貯蔵された溶射材を重力で落下させエジェクタを用いて搬送する図３（後述）に示すエジェクタ方式と密閉容器の中に溶射材を貯蔵し、容器内を加圧することで溶射材を搬送する密閉方式があるが、装置が小型・軽量化できる点と溶射材を連続的に供給できる点から開放エジェクタ式の溶射装置が選択される場合が多い。 As the thermal spraying device 10, the thermal spray material stored in an open hopper is dropped by gravity and transported using an ejector. The thermal spray material is stored in an ejector system shown in FIG. There is a sealing method in which the thermal spray material is conveyed by pressurizing, but an open ejector type thermal spraying device is often selected because the device can be reduced in size and weight and the thermal spray material can be continuously supplied.
近年、コークス炉の老朽化の進行に伴い耐火物の損傷範囲が広がっていることから溶射補修の効率向上のため溶射材の吐出速度を増大させることが必要になってきている。そのため、エジェクタ構造として高速噴流を噴出するエジェクタノズルとディフューザからなる図５、図６に示すような構造が一般的に選択される。この場合、エジェクタノズル３から噴出する燃焼補助ガス（酸素）に、当該エジェクタノズル３の先端付近にホッパ１から導入管１１１を介して落下する補修材を巻き込んでディフューザ５で受ける構造になっている。この構成では、エジェクタノズル３からの高圧噴流の噴射方向の中心軸をディフューザ５の断面の中心軸に一致させることで高い吐出量が得られることが知られている。 In recent years, with the progress of aging of coke ovens, the scope of damage to refractories has expanded, and it has become necessary to increase the spraying rate of the thermal spray material in order to improve the efficiency of thermal spray repair. Therefore, as the ejector structure, a structure as shown in FIGS. 5 and 6 composed of an ejector nozzle for ejecting a high-speed jet and a diffuser is generally selected. In this case, the combustion assisting gas (oxygen) ejected from the ejector nozzle 3 includes a repair material that falls from the hopper 1 through the introduction pipe 111 around the tip of the ejector nozzle 3 and is received by the diffuser 5. . In this configuration, it is known that a high discharge amount can be obtained by matching the central axis in the injection direction of the high-pressure jet from the ejector nozzle 3 with the central axis of the cross section of the diffuser 5.
このようなエジェクタ構造を用いた上で、更に吐出速度を増大させるためにはホース以降の圧力損失を小さくすることが有効で、ホースやランス（配管部材）を短くしたり直径を大きくしたりすることは効果がある。この方法は、配管における圧力損失を低減することでエジェクタの吸引力を高める方法であるが、ホースやランスの長さを短くすると補修可能範囲が狭小になり、補修が必要な部位まで配管が到達しなくなるため、一定値以上は短くすることが困難である。また、ホースやランスの径を太くすることは配管部材が重くなり、配管部材を人力で保持する補修には好ましくない。 In order to further increase the discharge speed using such an ejector structure, it is effective to reduce the pressure loss after the hose, shortening the hose or lance (pipe member) or increasing the diameter. That is effective. This method is to increase the suction force of the ejector by reducing the pressure loss in the piping. However, if the length of the hose or lance is shortened, the repairable range becomes narrower and the piping reaches the part that needs repairing. Therefore, it is difficult to shorten the value above a certain value. Also, increasing the diameter of the hose or lance makes the piping member heavier, which is not preferable for repairs that hold the piping member manually.
これに対して、エジェクタによる溶射材料の吸引力が同等であってもホッパからエジェクタへの粉体流れを円滑化することで粉体供給量を増やす方法も有効である。ホッパからエジェクタへの粉体供給量を増やす方法は、大きくわけて２つの方法が知られていた。一方はホッパからエジェクタへ溶射材を導く導入管の部分（絞り部）で粉末の流れを促進させる方法であり、他方はホッパの出口以降における粉末の流動を促進する方法である。 On the other hand, a method of increasing the powder supply amount by smoothing the powder flow from the hopper to the ejector is effective even if the spraying force of the sprayed material by the ejector is equal. There are two known methods for increasing the amount of powder supplied from the hopper to the ejector. One is a method for promoting the flow of powder at the portion of the introduction pipe (squeezed portion) for guiding the spray material from the hopper to the ejector, and the other is a method for promoting the flow of powder after the outlet of the hopper.
図５に示した従来技術では、稼動時にホッパ１からエジェクタ４へ粉体を供給する導入管１１１は溶射材で満たされており、溶射材が吐出されてエジェクタ４内部の溶射材が減ると重力とエジェクタ４の吸引力によって溶射材がホッパ１からエジェクタ４に供給される。このとき、導入管１１が単管であるため、溶射材は単管の内壁から摩擦抵抗を受けることになる。 In the prior art shown in FIG. 5, the introduction pipe 111 for supplying powder from the hopper 1 to the ejector 4 during operation is filled with the thermal spray material, and when the thermal spray material is discharged and the thermal spray material in the ejector 4 is reduced, gravity is reduced. Then, the spray material is supplied from the hopper 1 to the ejector 4 by the suction force of the ejector 4. At this time, since the introduction pipe 11 is a single pipe, the sprayed material receives frictional resistance from the inner wall of the single pipe.
このため、以下の特許文献１〜４に開示するように、ホッパの導入管での摩擦抵抗を減らす工夫がなされている。 For this reason, as disclosed in the following Patent Documents 1 to 4, a device for reducing the frictional resistance in the introduction pipe of the hopper has been devised.
特許文献１（実開昭６２−１４４８３２）には、粉体をエジェクタに供給する粉体供給管（導入管）の外周にエアチャンバを有し、粉体の出口側に向かって穿設された空気吐出孔を通してエアチャンバ内の圧縮空気を高速噴流として供給する構成が開示されており、粉体の安定した定量供給が可能になったとしている。 In Patent Document 1 (Japanese Utility Model Laid-Open No. 62-144832), an air chamber is provided on the outer periphery of a powder supply pipe (introduction pipe) for supplying powder to an ejector, and is drilled toward the outlet side of the powder. A configuration in which compressed air in an air chamber is supplied as a high-speed jet through an air discharge hole is disclosed, and it is said that stable quantitative supply of powder has become possible.
特許文献２（特許第４６２７８５４号）には、粉体がエジェクタに供給される縮径部（導入管）の上流側から空気を導入することで縮径部への粉体付着を抑制し安定輸送を図る構成が開示されている。 In Patent Document 2 (Japanese Patent No. 4627854), air is introduced from the upstream side of the reduced diameter portion (introducing pipe) to which the powder is supplied to the ejector, thereby suppressing powder adhesion to the reduced diameter portion and stable transportation. The structure which aims at is disclosed.
特許文献３（特開２００２−２６５０４６）には、二重構造ホッパを用い、重力で落下する粉粒体と同じ方向に送られる輸送用空気を導入することで乱流の発生によるエネルギーロスや輸送効率の低下を低減する構成が開示されている。 Patent Document 3 (Japanese Patent Application Laid-Open No. 2002-265046) uses a double hopper and introduces transportation air that is sent in the same direction as the granular material falling by gravity, thereby causing energy loss and transportation due to the occurrence of turbulence. A configuration for reducing the decrease in efficiency is disclosed.
さらに特許文献４（特開２００２−３０８４２７）には、高圧気体室を設け、供給される輸送用空気を高圧とする構成が開示されている。 Further, Patent Document 4 (Japanese Patent Application Laid-Open No. 2002-308427) discloses a configuration in which a high-pressure gas chamber is provided and the supplied transportation air has a high pressure.
前記特許文献１（実開昭６２−１４４８３２）に開示の構成は、穿設された細孔から高速噴流を吹き出さなければならず、そのためにはチャンバー内のエアをかなり高い圧力に維持する必要があり、ホッパ下部に屈強なエアチャンバを設けることになるため、装置が大きく、重くなる。また、穿設された細孔から吹き出したガスによって粉体供給側を積極的に負圧にするためには空気吐出孔から比較的多量の空気を供給しなければならない。少量の粉体を多量のガスで圧送する、すなわち粉体濃度の低い場合の空気輸送においては有効であるが、溶射材を高い濃度で圧送することを目的とする溶射材圧送装置に適用すると、エジェクタノズルから噴出されるガスと、ホッパの粉体出口側からのガスがディフューザで干渉し、高圧噴流の噴射方向の中心軸とディフューザ断面の中心軸にブレが生じ、却って吐出量を低下させることになる。 In the configuration disclosed in the above-mentioned Patent Document 1 (Japanese Utility Model Publication No. Sho 62-144432), a high-speed jet must be blown out from the perforated pores, and for that purpose, the air in the chamber needs to be maintained at a considerably high pressure. Since a strong air chamber is provided at the lower part of the hopper, the apparatus becomes large and heavy. Further, in order to make the powder supply side negative pressure positively by the gas blown out from the formed fine holes, a relatively large amount of air must be supplied from the air discharge holes. It is effective in pneumatic transportation when a small amount of powder is pumped with a large amount of gas, that is, when the powder concentration is low, but when applied to a thermal spray material feeding device intended to pump a thermal spray material at a high concentration, The gas ejected from the ejector nozzle and the gas from the powder outlet side of the hopper interfere with each other at the diffuser, causing blurring between the central axis in the injection direction of the high-pressure jet and the central axis of the diffuser cross section, thereby reducing the discharge amount. become.
さらに、溶射施工において酸素は単なるキャリアガスではなく、Siを酸化させる反応剤であり、溶射材の吐出量と酸素の流量は適正な比に保たれることが必要であるが、上記の構成によれば酸素が過剰にならざるを得ず、燃焼温度が低下することで緻密な施工体が得られなくなったり溶射時のリバウンドが増大したりする。 Furthermore, in thermal spraying, oxygen is not a mere carrier gas but a reactive agent that oxidizes Si, and it is necessary to maintain a proper ratio between the sprayed material discharge rate and the oxygen flow rate. According to this, oxygen must be excessive, and when the combustion temperature is lowered, a dense construction body cannot be obtained or rebound during spraying is increased.
特許文献２（特許第４６２７８５４号）に開示の構成は、付着性を有する粉体を微量空気輸送する場合であって、輸送量が小さいときに生じる輸送不安定を解消するものである。この構成を、吐出量を増やすことを目的とする溶射材圧送装置に適用して多量の空気を導入すると、高圧噴流の噴射方向の中心軸とディフューザの断面の中心軸にブレが生じ、却って吐出量が低下する結果となる。 The configuration disclosed in Patent Document 2 (Patent No. 4627854) is a case where a small amount of powder having adhesiveness is transported by pneumatic air and eliminates transport instability that occurs when the transport amount is small. When this configuration is applied to a thermal spray material pumping device for the purpose of increasing the discharge amount and a large amount of air is introduced, the central axis in the injection direction of the high-pressure jet and the central axis of the cross section of the diffuser are blurred, and instead the discharge The result is a reduced amount.
特許文献３（特開２００２−２６５０４６）に開示された構成、さらに特許文献４（特開２００２−３０８４２７）に開示された構成は、輸送用空気を二重構造ホッパより供給するもので、ホッパ下部で粉粒体と空気を混合しないので、少量搬送にしか適用できず、溶射施工で求められている高濃度多量吐出には適用できない。 The configuration disclosed in Patent Document 3 (Japanese Patent Application Laid-Open No. 2002-265046) and the configuration disclosed in Patent Document 4 (Japanese Patent Application Laid-Open No. 2002-308427) supply transportation air from a double structure hopper. Since the powder and air are not mixed with each other, it can be applied only to a small amount of conveyance, and cannot be applied to a high concentration and large volume discharge required in thermal spraying.
本発明は、溶射による耐火物補修に使用する溶射材圧送装置において、ホースやランスなど作業者が取り回しをする配管径を大きくすること無く、また、装置の大型化、重量化を伴わずに、溶射材の吐出量を高めることができる溶射材圧送装置を提供することを目的としたものである。 The present invention is a thermal spray material pumping device used for refractory repair by thermal spraying, without increasing the pipe diameter that the operator handles such as a hose or lance, and without increasing the size and weight of the device, An object of the present invention is to provide a thermal spray material feeding device capable of increasing the discharge amount of the thermal spray material.
本発明は、ホッパから導入された溶射材と、エジェクタノズルから噴出される燃焼補助ガスとをエジェクタで混合し、ディフューザを介してランス先端のノズルから噴出する溶射材圧送装置であって、下記内管と、外管と、ガス導入口とより構成される。 The present invention is a thermal spray material feeding device in which a thermal spray material introduced from a hopper and a combustion auxiliary gas ejected from an ejector nozzle are mixed by an ejector and ejected from a nozzle at the tip of a lance through a diffuser. It consists of a pipe, an outer pipe, and a gas inlet.
内管は、ホッパからエジェクタへ溶射材を導入するとともに、エジェクタの材料投入孔より所定の距離上または下の位置に開口する。外管は、前記内管を、当該内管と所定の距離を保って覆うとともに、前記エジェクタの材料投入孔に連通する。更に、ガス導入口は、前記内管の開口位置より所定距離上のまたは下の位置に開口する。 The inner pipe introduces the thermal spray material from the hopper to the ejector and opens at a position above or below a predetermined distance from the material charging hole of the ejector. The outer tube covers the inner tube at a predetermined distance from the inner tube, and communicates with the material insertion hole of the ejector. Further, the gas introduction port opens at a position above or below a predetermined distance from the opening position of the inner tube.
前記内管の内径(di)と外管(do)の内径の比(di/do)は0.5〜0.9、好ましくは0.6〜0.8で、内管の開口端とエジェクタの材料投入孔の距離(l1) と導入外管の内径(do)の比(l1/ do)は1.5以下、好ましくは1.0以下である。 The ratio of the inner diameter of the inner diameter of the inner pipe (d i) and the outer tube (d o) (d i / d o) is 0.5 to 0.9, preferably at 0.6 to 0.8, the open end of the inner tube and the ejector material charging hole of The ratio (l 1 / d o ) between the distance (l 1 ) and the inner diameter (d o ) of the introduction outer tube is 1.5 or less, preferably 1.0 or less.
前記内管と外管の間に前記ガス導入口から供給されるガス流量は、エジェクタノズルに供給される溶射材搬送ガス流量の1/2以下、好ましくは1/3以下である。 The gas flow rate supplied from the gas introduction port between the inner tube and the outer tube is 1/2 or less, preferably 1/3 or less, of the spray material transfer gas flow rate supplied to the ejector nozzle.
更に、前記ガス導入口から供給されるガス種は、大気、酸素、窒素、アルゴン、から選択される少なくとも１種類である。従って、前記ガス導入口は、大気に開放されることでもよい。 Furthermore, the gas species supplied from the gas inlet is at least one selected from the atmosphere, oxygen, nitrogen, and argon. Therefore, the gas inlet may be opened to the atmosphere.
本発明により、耐火物の溶射補修に使用する溶射材圧送装置において、ホースやランスなど作業者が取り回しをする配管径を大きくすること無く、また、装置の大型化、重量化を伴わずに、溶射材の吐出量を高めることができ、溶射補修の効率を向上させることができる。 According to the present invention, in the thermal spray material feeding device used for thermal spray repair of the refractory, without increasing the pipe diameter to be handled by the operator such as a hose or lance, and without increasing the size and weight of the device, The discharge amount of the thermal spray material can be increased, and the efficiency of the thermal spray repair can be improved.
図１は本発明が適用された溶射材圧送装置の概念図であり、図２は本発明の要部を示す図である。 FIG. 1 is a conceptual diagram of a thermal spray material feeding device to which the present invention is applied, and FIG. 2 is a diagram showing a main part of the present invention.
ホッパ１の導入管１１が絞り部に連続する内管３１と、当該内管３１に対して、径方向に所定の間隔を保って覆う外管３２とより構成される。 The introduction pipe 11 of the hopper 1 includes an inner pipe 31 that is continuous with the throttle portion, and an outer pipe 32 that covers the inner pipe 31 at a predetermined interval in the radial direction.
前記内管３１の開口端はエジェクタ４の材料投入孔３４の上側の位置に開口し、前記外管３２の上端は前記ホッパ１下部の絞り部に気密に取り付けられ、下端はエジクタ３の材料投入孔３４に連通する。更に、前記外管３２の前記内管３１の開口端より上の位置にガズ導入口３３を設けた構成となっている。 The opening end of the inner pipe 31 opens at a position above the material charging hole 34 of the ejector 4, the upper end of the outer pipe 32 is airtightly attached to the throttle portion at the lower part of the hopper 1, and the lower end is the material charging of the ejector 3. It communicates with the hole 34. Further, a gas introduction port 33 is provided at a position above the opening end of the inner tube 31 of the outer tube 32.
従来のように、内管３１（図５の導入管１１１）が単管である場合、溶射材は単管である内管３１の内壁から摩擦抵抗を受けることになるが、上記の構成のように、内管３１に対して外管３２を被せて二重管とすると、図３に示すように、内管３１あるいは外管３２の管壁部の材料表面の僅かな範囲に、内管３１と外管３２の間から供給されるガスが混入し、それによって摩擦抵抗が軽減され、エジェクタ４への円滑な材料供給に寄与することになる。 When the inner pipe 31 (introduction pipe 111 in FIG. 5) is a single pipe as in the prior art, the thermal spray material receives frictional resistance from the inner wall of the inner pipe 31 which is a single pipe. Further, when the inner tube 31 is covered with the outer tube 32 to form a double tube, the inner tube 31 or the inner tube 31 is disposed within a slight range of the material surface of the tube wall portion of the inner tube 31 or the outer tube 32 as shown in FIG. The gas supplied from between the outer pipe 32 and the outer pipe 32 is mixed, thereby reducing the frictional resistance and contributing to a smooth material supply to the ejector 4.
上記構成において、前記内管３１の内径(di)と外管３２(do)の内径の比(di/ do)は、比(di/do)は0.5〜0.9である。この比より内管３１の径が大きいとガス導入口３３から導入されるガスの混入量が少なく十分な効果が得られない。また、内管３１の径が上記の比より小さいと、外管３２、およびエジェクタ４の材料投入孔３４の径が大きくなり過ぎ、装置全体が大型化するため好ましくない。好ましくは0.6〜0.8である。 In the above structure, the ratio of the inner diameter of the inner diameter (di) and the outer tube 32 of the inner tube 31 (d o) (di / d o) , the ratio (di / d o) is 0.5 to 0.9. If the diameter of the inner pipe 31 is larger than this ratio, the amount of gas introduced from the gas inlet 33 is small and a sufficient effect cannot be obtained. Further, if the diameter of the inner tube 31 is smaller than the above ratio, the diameters of the outer tube 32 and the material injection hole 34 of the ejector 4 are excessively large, which is not preferable because the entire apparatus is enlarged. Preferably it is 0.6-0.8.
また、前記内管３１の開口端とエジェクタ４の材料投入孔３４の距離(l1) と外管３２の内径(do)の比(l1/do)は1.5以下である。内管３１の下端の開口端がエジェクタ４の材料投入孔３４からの距離が、上記の比より大きいと管壁との摩擦低減効果がエジェクタ４に到達する前に失われるため好ましくない。より、好ましくは1.0以下である。このとき、距離(l1)が マイナス、すなわち内管３１の開口端がエジェクタ４の材料投入孔３４のレベルより下方にあってもよい。 The ratio (l 1 / d o ) of the distance (l 1 ) between the opening end of the inner pipe 31 and the material injection hole 34 of the ejector 4 to the inner diameter (d o ) of the outer pipe 32 is 1.5 or less. If the distance between the opening end of the lower end of the inner pipe 31 and the material input hole 34 of the ejector 4 is larger than the above ratio, the friction reducing effect with the pipe wall is lost before reaching the ejector 4, which is not preferable. More preferably, it is 1.0 or less. At this time, the distance (l 1 ) may be negative, that is, the opening end of the inner tube 31 may be below the level of the material charging hole 34 of the ejector 4.
また、ガス導入口３３から供給されるガス量（ｍ３/h）が、エジェクタノズル３から供給される溶射材搬送ガス量（ｍ３/h）の1/2以下とする。当該ガス量がエジェクタノズル３より供給される溶射材搬送ガス量の1/2より多いと、エジェクタノズル３とディフューザ５の間でガス同士が干渉し、エジェクタノズル３からの高圧噴流の噴射方向の中心軸とディフューザ５の断面の中心軸にブレが生じ、却って吐出量を低下させることになる。従って、好ましくは上記ガス量は溶射材搬送ガス量の1/4以下であることが望ましい。 Further, the gas amount (m 3 / h) supplied from the gas inlet 33 is set to be ½ or less of the thermal spray material transport gas amount (m 3 / h) supplied from the ejector nozzle 3. If the amount of gas is larger than 1/2 of the spray material carrying gas amount supplied from the ejector nozzle 3, the gases interfere with each other between the ejector nozzle 3 and the diffuser 5, and in the injection direction of the high-pressure jet from the ejector nozzle 3. The center axis and the center axis of the cross section of the diffuser 5 are blurred, and the discharge amount is reduced instead. Therefore, it is preferable that the gas amount is 1/4 or less of the thermal spray material transport gas amount.
エジェクタ４に供給されるガス種はエジェクタノズル３から導入されるメインの搬送ガスであり、かつ溶射補修の際の反応ガスである酸素であることが好ましい。溶射補修において酸素濃度が低下することで、反応効率が低下するためである。 The gas species supplied to the ejector 4 is preferably the main carrier gas introduced from the ejector nozzle 3 and oxygen, which is a reactive gas during spraying repair. This is because the reaction efficiency is lowered by reducing the oxygen concentration in the thermal spray repair.
しかし、本発明のガス導入口３３から供給されるガスの場合、導入量が少ないため空気や窒素など、メインの搬送ガスと異なる組成のガスも適用可能である。また、ガス導入口３３から導入するガスは前記メインのガスが逆流しない限り低い圧力とすることができる。一般に、エジェクタ４の効果により導入管１１の付近は負圧になるので、前記ガス導入口３３から導入するガスは大気圧でも本発明の効果は得られる。これらより、ガス導入口３３は大気に開放された状態であっても本発明の効果を得ることが可能である。 However, in the case of the gas supplied from the gas inlet 33 of the present invention, since the introduction amount is small, a gas having a composition different from that of the main carrier gas, such as air or nitrogen, can be applied. The gas introduced from the gas inlet 33 can be at a low pressure as long as the main gas does not flow backward. In general, since the vicinity of the introduction pipe 11 becomes negative due to the effect of the ejector 4, the effect of the present invention can be obtained even if the gas introduced from the gas introduction port 33 is atmospheric pressure. As a result, the effects of the present invention can be obtained even when the gas inlet 33 is open to the atmosphere.
なお、本発明はホース７やランス８などの配管径を大きくすることなく吐出量を増大するものであるが、配管径の増大と組み合わせることでさらに高い効果が得られる。すなわち、作業方法や治具の工夫、ロボットの導入などで作業負荷を軽減し、配管径を大きくして吐出量を増大させることを否定するものではない。 In addition, although this invention increases discharge amount, without enlarging piping diameters, such as the hose 7 and the lance 8, a still higher effect is acquired by combining with the increase in piping diameter. That is, there is no denying that the work load is reduced by devising work methods and jigs, introducing robots, etc., and increasing the discharge amount by increasing the pipe diameter.
また、図４に示すごとく、ホッパ１と導入管１１の二重管部との間に材料の供給を調整するシャッタ１２やバタフライ弁（図示せず）を設置することも可能である。更に、シャッタ１２やバタフライ弁などのバルブに限らず、一般的に公知の配管部材を設置することが可能である。 Further, as shown in FIG. 4, a shutter 12 and a butterfly valve (not shown) for adjusting the supply of material can be installed between the hopper 1 and the double pipe portion of the introduction pipe 11. Furthermore, it is not limited to valves such as the shutter 12 and the butterfly valve, and generally known piping members can be installed.
この場合、内管３１の上部には外管３２を被せない構成とし、その部分に前記シャッタ１２等を配置し、当該シャッタ１２等の下側の位置の内管３２に外管３２の上端が気密に取り付けられ二重管部とする。図１の場合と同様、外管３２の下端はエジクタ３の材料投入孔３４に連通する。また、当然のことながら、ガス導入孔３３は、外管３２の内管３１との取り付け部より下の位置で、内管３１の下端より上の位置に設けられることになる。 In this case, the outer tube 32 is not covered with the upper portion of the inner tube 31, the shutter 12 or the like is disposed in that portion, and the upper end of the outer tube 32 is connected to the inner tube 32 at a lower position of the shutter 12 or the like. It is airtightly attached to a double pipe part. As in the case of FIG. 1, the lower end of the outer tube 32 communicates with the material charging hole 34 of the ejector 3. As a matter of course, the gas introduction hole 33 is provided at a position below the attachment portion of the outer tube 32 with the inner tube 31 and at a position above the lower end of the inner tube 31.
本発明の効果を表わす実験は図１に示す溶射装置を用いて行った。実施例、および比較例を表１〜表３にまとめる。 An experiment showing the effect of the present invention was performed using the thermal spraying apparatus shown in FIG. Examples and Comparative Examples are summarized in Tables 1 to 3.
表１は内管内径(di)と外管内径(do)の比di/ doの影響を例示したものである。比較例1はガスを導入しない例であるが、di/ doが0.5から0.9の範囲でガスを導入することで吐出量が増大すること、その効果はdi/ doが0.6〜0.8の範囲で顕著であることがわかった。 Table 1 illustrates the influence of the ratio di / d o between the inner pipe inner diameter (di) and the outer pipe inner diameter (d o ). While Comparative Example 1 is an example not to introduce gas, the di / d o is the discharge amount is increased by introducing a gas in the range of 0.5 to 0.9, the range the effect is di / d o is 0.6 to 0.8 It turned out to be remarkable.
表２は内管の開口端とエジェクタの材料投入孔の距離(l1) と外管の内径(do)の比(l1/ do)の効果を例示したものである。ガス導入しない比較例４に対して、l1/ doが1.5以下の範囲でガスを導入することで吐出量が増大すること、また、その効果はl1/ doが1.0以下の範囲で顕著であることがわかる。 Table 2 exemplifies the effect of the ratio (l 1 / d o ) between the distance (l 1 ) between the opening end of the inner tube and the material injection hole of the ejector and the inner diameter (d o ) of the outer tube. Compared with Comparative Example 4 in which no gas is introduced, the amount of discharge is increased by introducing gas in a range where l 1 / d o is 1.5 or less, and the effect is that l 1 / d o is in a range of 1.0 or less. It turns out that it is remarkable.
表３は導入ガス量の影響を例示したものである。また、ガス導入せず大気に開放した例も表３に示した。表３のデータは表２と同じ仕様で採取したものでガスを導入しない比較例４との比較によってその効果がわかる。表3からわかるように、エジェクタに導入するガスの1/2以下のガス量を導入することで吐出量の向上を図ることができ、その効果は1/3以下で著しい。 Table 3 illustrates the influence of the amount of introduced gas. Table 3 also shows an example in which the gas was not introduced and opened to the atmosphere. The data in Table 3 was collected with the same specifications as in Table 2, and its effect can be seen by comparison with Comparative Example 4 in which no gas was introduced. As can be seen from Table 3, the discharge amount can be improved by introducing a gas amount of 1/2 or less of the gas introduced into the ejector, and the effect is remarkable at 1/3 or less.
さらに、実施例１８に示されるように、ガスを導入するのではなく大気に開放することでも吐出量の向上を図ることが可能である。実施例１８の場合の大気の流入量は測定していないが、大気吸入部に手をかざしたところ、極僅かであることが確認された。 Furthermore, as shown in Example 18, it is possible to improve the discharge amount by opening to the atmosphere instead of introducing gas. Although the amount of inflow of air in Example 18 was not measured, it was confirmed that it was extremely small when a hand was held over the air suction portion.
以上説明したように本発明は、作業者が取り回しをする配管径を大きくすること無く、また、装置の大型化、重量化を伴わずに、溶射材の吐出量を高めることができ、溶射補修の効率を向上させることができる。 As described above, the present invention can increase the discharge amount of the sprayed material without increasing the diameter of the pipes that the operator handles, and without increasing the size and weight of the apparatus, and spraying repair. Efficiency can be improved.
１． ホッパ
２． エジェクタノズル
４． エジェクタ
１１．導入管
１２．シャッタ
３１．内管
３２．外管
３３．ガズ導入口
３４．材料投入孔
1. Hopper Ejector nozzle 4. Ejector 11. Introduction pipe 12. Shutter 31. Inner pipe 32. Outer tube 33. Gas inlet 34. Material input hole
Claims (6)
ホッパからエジェクタへ溶射材を導入するとともに、エジェクタの材料投入孔より所定の距離上または下の位置に開口する内管と、
前記内管を、当該内管と所定の距離を保って覆うとともに、前記エジェクタの材料投入孔に連通する外管と、
前記内管の開口位置より上の位置の外管内部に開口したガス導入口と、
を備え、
前記内管の内径(di)と外管の内径(do)の比(di/do)は0.5〜0.9で、内管下端とエジェクタの材料投入孔の距離(l1) と導入外管の内径(do)の比(l1/do)は1.5以下である
ことを特徴とする溶射材圧送装置。 In the thermal spray material feeding device in which the thermal spray material introduced from the hopper and the combustion auxiliary gas ejected from the ejector nozzle are mixed by the ejector, and ejected from the nozzle at the tip of the lance through the diffuser,
Introducing a thermal spray material from the hopper to the ejector, and an inner tube that opens at a predetermined distance above or below the material injection hole of the ejector,
Covering the inner tube with a predetermined distance from the inner tube, and an outer tube communicating with the material input hole of the ejector;
A gas inlet opening inside the outer pipe at a position above the opening position of the inner pipe;
With
The ratio (d i / d o ) between the inner diameter (d i ) of the inner pipe and the inner diameter (d o ) of the outer pipe is 0.5 to 0.9, and the distance (l 1 ) between the lower end of the inner pipe and the material input hole of the ejector is introduced. A thermal spray material feeding device characterized in that the ratio (l 1 / d o ) of the inner diameter (d o ) of the outer tube is 1.5 or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2015204300A JP6481583B2 (en) | 2015-10-16 | 2015-10-16 | Thermal spray material feeding device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2015204300A JP6481583B2 (en) | 2015-10-16 | 2015-10-16 | Thermal spray material feeding device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2017075381A true JP2017075381A (en) | 2017-04-20 |
| JP6481583B2 JP6481583B2 (en) | 2019-03-13 |
Family
ID=58551011
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2015204300A Active JP6481583B2 (en) | 2015-10-16 | 2015-10-16 | Thermal spray material feeding device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP6481583B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2020059899A (en) * | 2018-10-12 | 2020-04-16 | 黒崎播磨株式会社 | Flame spraying method |
| CN114506691A (en) * | 2022-02-17 | 2022-05-17 | 无锡云科机械有限公司 | High-efficient environmental protection weightless formula feeding machine |
| KR20220087725A (en) * | 2020-12-18 | 2022-06-27 | 주식회사 포스코 | Ejector apparatus for mixing viscous fluid |
| JP7182743B1 (en) * | 2022-07-25 | 2022-12-02 | 黒崎播磨株式会社 | Spray equipment and spray material |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4989876U (en) * | 1972-11-27 | 1974-08-03 | ||
| JP2002265046A (en) * | 2001-03-09 | 2002-09-18 | Tsukasa Kogyo Kk | Double structure hopper for pneumatic transportation of particulate |
| JP2002308427A (en) * | 2001-04-19 | 2002-10-23 | Tsukasa Kogyo Kk | Server for powder and granular material air power transportation |
| JP2004513044A (en) * | 2000-11-03 | 2004-04-30 | ソティック・メカニーク | Device for transporting fine powder material and its application to supply of fine powder material to molten metal |
| US20100313570A1 (en) * | 2006-10-20 | 2010-12-16 | Ihi Corporation | Gas turbine combustor |
| JP4915905B2 (en) * | 2006-03-06 | 2012-04-11 | 日本特殊炉材株式会社 | Thermal spray equipment |
| JP2015034321A (en) * | 2013-08-08 | 2015-02-19 | 日本特殊炉材株式会社 | Spray coating apparatus |
-
2015
- 2015-10-16 JP JP2015204300A patent/JP6481583B2/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4989876U (en) * | 1972-11-27 | 1974-08-03 | ||
| JP2004513044A (en) * | 2000-11-03 | 2004-04-30 | ソティック・メカニーク | Device for transporting fine powder material and its application to supply of fine powder material to molten metal |
| JP2002265046A (en) * | 2001-03-09 | 2002-09-18 | Tsukasa Kogyo Kk | Double structure hopper for pneumatic transportation of particulate |
| JP2002308427A (en) * | 2001-04-19 | 2002-10-23 | Tsukasa Kogyo Kk | Server for powder and granular material air power transportation |
| JP4915905B2 (en) * | 2006-03-06 | 2012-04-11 | 日本特殊炉材株式会社 | Thermal spray equipment |
| US20100313570A1 (en) * | 2006-10-20 | 2010-12-16 | Ihi Corporation | Gas turbine combustor |
| JP2015034321A (en) * | 2013-08-08 | 2015-02-19 | 日本特殊炉材株式会社 | Spray coating apparatus |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2020059899A (en) * | 2018-10-12 | 2020-04-16 | 黒崎播磨株式会社 | Flame spraying method |
| KR20220087725A (en) * | 2020-12-18 | 2022-06-27 | 주식회사 포스코 | Ejector apparatus for mixing viscous fluid |
| KR102507729B1 (en) | 2020-12-18 | 2023-03-07 | 주식회사 포스코 | Ejector apparatus for mixing viscous fluid |
| CN114506691A (en) * | 2022-02-17 | 2022-05-17 | 无锡云科机械有限公司 | High-efficient environmental protection weightless formula feeding machine |
| CN114506691B (en) * | 2022-02-17 | 2023-02-03 | 无锡云科机械有限公司 | High-efficient environmental protection feeding machine |
| JP7182743B1 (en) * | 2022-07-25 | 2022-12-02 | 黒崎播磨株式会社 | Spray equipment and spray material |
| WO2024024539A1 (en) * | 2022-07-25 | 2024-02-01 | 黒崎播磨株式会社 | Spraying apparatus and spraying material |
Also Published As
| Publication number | Publication date |
|---|---|
| JP6481583B2 (en) | 2019-03-13 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP6481583B2 (en) | Thermal spray material feeding device | |
| JP2019026483A (en) | Mixed feeding method and mixed feeding equipment of powdery and granular material, mixed feeding-adding method of steel refining agent and steel refining method | |
| CN103114169A (en) | Converter wet spray repair technique | |
| CN111926280A (en) | High-entropy alloy coating of long-life spray gun for Isa smelting and preparation method thereof | |
| CN101265513A (en) | Austenite stainless heat-resisting seamless steel pipe internal wall shot-blasting strengthening technique and device | |
| CN104357615A (en) | Dephosphorization method for molten iron in converter by blowing dust removal ash | |
| CN105220102B (en) | It is a kind of to extend the method in oxygen gun sprayer life-span by reducing oxygen gun sprayer dry slag | |
| CN105775754A (en) | Injection tank pressure relief device for positive pressure pneumatic conveying | |
| CN111926281A (en) | Long-life spray gun ceramic coating for pizza smelting and preparation method thereof | |
| JP6422101B2 (en) | Thermal spray repair method for furnace wall | |
| CN100384540C (en) | Method for coating solids in a low-temperature zone | |
| JP2017132639A (en) | Powder conveyance mechanism | |
| CN210357639U (en) | Non-stop double-powder-feeding device of cold spray coating device | |
| JP2015113490A (en) | Spray coating apparatus | |
| CN201147902Y (en) | Steel shot reclaiming airproof bin apparatus for steel pipe inner wall reinforced shot blasting | |
| CN103771139B (en) | A kind of blast-furnace coal powder continuous-feeding dense phase pneumatic conveying system and technique | |
| CN111169825A (en) | Blockage clearing and flow assisting device for air cannon | |
| CN205652842U (en) | Malleation air conveying's jetting jar pressure relief device | |
| CN216998485U (en) | LF refining furnace diffusion deoxidier jetting device | |
| CN215287075U (en) | Purified ash conveying device | |
| CN110631372A (en) | Intermittent feeding device for metallurgical furnace | |
| CN214529187U (en) | Device for conveying argon to liquid level of non-ferrous metal in smelting equipment and smelting equipment | |
| CN211803798U (en) | Silicon-manganese molten iron ladle transport vehicle capable of reducing emission of diffused gas | |
| JP5694633B2 (en) | Gas replacement method in piping and gas replacement device in piping | |
| CN213388847U (en) | Powder spraying system for preparing multi-element alloy |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20170919 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20180525 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20180703 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20180802 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20190115 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20190128 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 6481583 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |