JP2018089748A - Blasting method and device for internal surface of tube - Google Patents

Blasting method and device for internal surface of tube Download PDF

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JP2018089748A
JP2018089748A JP2016236508A JP2016236508A JP2018089748A JP 2018089748 A JP2018089748 A JP 2018089748A JP 2016236508 A JP2016236508 A JP 2016236508A JP 2016236508 A JP2016236508 A JP 2016236508A JP 2018089748 A JP2018089748 A JP 2018089748A
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pipe
processed
air
blasting
abrasive
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JP7007087B2 (en
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文明 羽渕
Fumiaki Hanebuchi
文明 羽渕
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Sankyo-Rikagaku Co Ltd
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Sankyo-Rikagaku Co Ltd
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Priority to CN201711231792.3A priority patent/CN108145615A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C3/00Abrasive blasting machines or devices; Plants
    • B24C3/32Abrasive blasting machines or devices; Plants designed for abrasive blasting of particular work, e.g. the internal surfaces of cylinder blocks
    • B24C3/325Abrasive blasting machines or devices; Plants designed for abrasive blasting of particular work, e.g. the internal surfaces of cylinder blocks for internal surfaces, e.g. of tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C7/00Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts
    • B24C7/0046Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C9/00Appurtenances of abrasive blasting machines or devices, e.g. working chambers, arrangements for handling used abrasive material
    • B24C9/006Treatment of used abrasive material

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Cleaning In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a blasting device for the internal surface of a tube, by which action for conveyance of a grinding material can speedily be caused over the entire tube being processed, regardless of the size of the pipe being processed.SOLUTION: A blasting device comprises: a suction device 7 that sucks air in a tube from the downstream end P1 of a pipe P being processed; and an injector 3 that injects a grinding material and air into the tube from the upstream end P2 of the pipe P in a sealed state. By virtue of this, strong forces for causing the grinding material and air to flow from an upstream side to a downstream side in a pipe are simultaneously act from both ends P1, P2 of the pipe P being processed. Therefore, the grinding material is securely conveyed over the entire length of the pipe P being processed, even in a case where it is difficult to cause action for conveyance of a grinding material over the entire length of the pipe P in a short time only with a negative-pressure suction force, such as a case where the inside diameter of the pipe P being processed is short or the entire length L of the pipe is long.SELECTED DRAWING: Figure 1

Description

本発明は、各種の管(被処理管)の内面を研掃・研磨・研削等する管内面のブラスト方法及び同装置、並びに同装置を含む管内面ブラストシステムに関するものである。 The present invention relates to a pipe inner surface blasting method and apparatus for polishing, polishing and grinding the inner surfaces of various pipes (processed pipes), and a pipe inner surface blasting system including the apparatus.

鋼管等の管(被処理管)の内面を研掃・研磨・研削等(以下、単に「研掃」という。)する管内面のブラスト方法として、高圧噴射式ブラスト方法と負圧吸引式ブラスト方法とが知られている。高圧噴射式ブラスト方法は、被処理管の内部に高圧で空気と研掃材とを吹き込むもの(特許文献1の図12及び[0004]〜[0018]参照)であり、負圧吸引式ブラスト方法は、被処理管内を負圧にすることで研掃材を管内に吸入するものである(特許文献1の図14及び[0026]〜[0032]参照)。経済性、省力・省エネルギー性、安全性、保守性、環境衛生等、様々な観点から、今日一般に負圧吸引式ブラスト方法に優位性があると言われている。 High-pressure injection blasting method and negative-pressure suction blasting method are used as blasting methods for the inner surface of pipes such as steel pipes (processed pipes) for scouring, polishing, grinding, etc. (hereinafter simply referred to as “scouring”). Is known. The high-pressure injection blasting method is a method in which air and a cleaning material are blown into a pipe to be processed at a high pressure (see FIG. 12 and [0004] to [0018] in Patent Document 1). In this method, the abrasive is sucked into the pipe by making the inside of the pipe to be treated into a negative pressure (see FIG. 14 and [0026] to [0032] in Patent Document 1). From various viewpoints such as economy, labor-saving / energy-saving, safety, maintainability, environmental hygiene, etc., it is generally said that the negative pressure suction blast method is generally superior today.

特開平7−1335号公報JP-A-7-1335 特開昭50−1562号公報JP 50-1562 A 特開平7−227762号公報JP 7-227762 A

しかしながら、被処理管の内径が小さい場合や被処理管の全長が長い場合には、圧力損失が大きくなるので、負圧による研掃材の搬送作用が被処理管の全長に対して及び難いという問題がある。負圧吸引に時間をかければ被処理管の全長に亘って研掃材の搬送作用を及ぼすことができる場合もあるが、それでは研掃処理効率が低下して作業性が悪くなってしまう。 However, when the inner diameter of the tube to be processed is small or the entire length of the tube to be processed is long, the pressure loss becomes large, so that it is difficult for the conveying action of the abrasive material due to negative pressure to reach the entire length of the tube to be processed. There's a problem. If time is taken for the negative pressure suction, there may be a case where the conveying action of the scouring material can be exerted over the entire length of the tube to be treated. However, the scouring process efficiency is lowered and workability is deteriorated.

従来の管内面のブラスト方法の中には、特許文献2に示されているように、被研掃パイプ22の下流端から被研掃パイプ22内の空気を吸引して被研掃パイプ22内を負圧化すると共に、被研掃パイプ22の上流端から研掃材14に加えてノズル11により圧縮空気を供給する方式も知られている。 In a conventional method for blasting the inner surface of a pipe, as shown in Patent Document 2, the air in the pipe to be cleaned 22 is sucked from the downstream end of the pipe to be cleaned 22 and the inside of the pipe to be cleaned 22 There is also known a system in which compressed air is supplied by the nozzle 11 in addition to the abrasive 14 from the upstream end of the polished pipe 22.

しかし、このものは、特許文献2の第1図に示されているように、被研掃パイプ22の上流端に接続される輸送管6の上流端24が開口しており、この開口部24から大気が吸引されるようになっている。このため、ノズル11から供給される圧縮空気は、あくまでも集塵機18による負圧吸引作用を補助する役割を奏するものでしかない。よって、被研掃パイプ22の口径に対して被研掃パイプの長さがきわめて長い場合には、被研掃パイプ22の全長に亘って研掃材の搬送作用が及ぶのに時間がかかってしまい、前記問題が十分に解決されるとは言い難い。 However, in this case, as shown in FIG. 1 of Patent Document 2, the upstream end 24 of the transport pipe 6 connected to the upstream end of the polished pipe 22 is open, and the opening 24 Atmosphere is sucked from. For this reason, the compressed air supplied from the nozzle 11 only plays a role of assisting the negative pressure suction action by the dust collector 18. Therefore, when the length of the pipe to be cleaned is very long with respect to the diameter of the pipe to be polished 22, it takes time for the conveying action of the polishing material to reach the entire length of the pipe to be polished 22. Therefore, it is difficult to say that the above problem is sufficiently solved.

また、管内面のブラスト方法の他の例として、特許文献3の[0028]に記載されているように、「研掃機15のブロア23がレシーバタンク22側から被処理管13に負圧吸引力を及ぼし、圧空ノズル24がサクションヘッド21側から旋回流の圧空を被処理管13に吹き込む。これにより、被処理管13の一端13Aから他端13Bに流れる研掃材の旋回流が被処理管13の内面を研掃する。」ものも知られている。 Further, as another example of the blasting method of the pipe inner surface, as described in [0028] of Patent Document 3, “the blower 23 of the scouring machine 15 sucks the negative pressure into the pipe 13 to be processed from the receiver tank 22 side. The compressed air nozzle 24 blows the swirled compressed air from the suction head 21 side into the processing tube 13. Thereby, the swirling flow of the polishing material flowing from the one end 13A to the other end 13B of the processing tube 13 is processed. The inner surface of the tube 13 is sharpened. "

しかし、特許文献3のものは、[0023],[0024]と図2,図3の記載から見て、負圧吸引力が有効に作用するように、また、研掃材タンクから研掃材が円滑に供給されるように、サクションヘッド21の上部が上向きに開口しているものと考えられる。そして、圧空ノズル24から供給される圧縮空気は、あくまでも旋回流を創出するためのものでしかない。よって、被処理管の口径に対して被処理管の長さがきわめて長い場合等には、被処理管の全長に亘って研掃材の搬送作用が及ぶのに時間がかかってしまい、前記問題が十分に解決されるとは言い難い。 However, in Patent Document 3, as seen from the description of [0023], [0024] and FIGS. 2 and 3, the negative pressure suction force acts effectively, and the abrasive is removed from the abrasive tank. It is considered that the upper portion of the suction head 21 is opened upward so that can be smoothly supplied. The compressed air supplied from the compressed air nozzle 24 is only for creating a swirling flow. Therefore, when the length of the pipe to be processed is very long with respect to the diameter of the pipe to be processed, it takes time for the polishing material to reach the entire length of the pipe to be processed. Is difficult to resolve.

本発明は前記のような事情に鑑みてなされたものである。本発明は、従来の負圧吸引式管内面ブラスト装置に使用されているような高出力の真空ブロアをもってしても圧力損失の問題で被処理管の上流端から研掃材搬送気流を引くことができないほど内径が小さいか全長が長い被処理管に対して研掃処理を行う場合に有効なものであり、被処理管のサイズにかかわらず、被処理管の全体に研掃材搬送作用を速やかに及ぼすことができる、管内面のブラスト方法及び同装置、並びに管内面ブラストシステムを提案しようとするものである。 The present invention has been made in view of the above circumstances. The present invention draws the abrasive conveying air flow from the upstream end of the pipe to be processed due to the problem of pressure loss even with a high-power vacuum blower used in a conventional negative pressure suction pipe inner surface blasting device. This is effective when performing a blasting process on a tube to be processed that has a small inner diameter or a long overall length. The present invention is intended to propose a method and apparatus for blasting the inner surface of a pipe, and a blasting system for a pipe inner surface, which can be applied quickly.

前記課題を解決するため、本発明に係る管内面のブラスト方法は、被処理管の下流端から管内の空気を吸引すると共に、研掃材と空気とを前記被処理管の上流端から密閉状態で管内に圧送することを特徴とする(請求項1)。 In order to solve the above-mentioned problem, the blasting method of the pipe inner surface according to the present invention sucks air in the pipe from the downstream end of the pipe to be processed and seals the abrasive and air from the upstream end of the pipe to be processed. And pumping into the pipe (claim 1).

本発明の方法によれば、被処理管の下流端から管内の空気が吸引されるとともに、研掃材と空気とが被処理管の上流端から密閉状態で管内に圧送される。これにより、研掃材を管内で上流から下流へ向けて流動させようとする強い力が被処理管の両端から同時に作用する。このため、被処理管の内径が小さい場合や被処理管の全長が長い場合等、負圧吸引作用のみによっては被処理管の全長に亘って研掃材の搬送作用を短時間で及ぼし難い場合であっても、被処理管の全長において研掃材が確実に搬送される。その結果、被処理管のサイズにかかわらず、被処理管の全長に亘って効率よく研掃効果を及ぼすことができる。 According to the method of the present invention, the air in the pipe is sucked from the downstream end of the pipe to be processed, and the abrasive and the air are pumped into the pipe in a sealed state from the upstream end of the pipe to be processed. As a result, a strong force that causes the abrasive to flow from upstream to downstream in the pipe acts simultaneously from both ends of the pipe to be processed. For this reason, when the inner diameter of the tube to be processed is small or when the entire length of the tube to be processed is long, it is difficult to exert the conveying action of the abrasive material over the entire length of the tube to be processed only by the negative pressure suction action. Even so, the abrasive is reliably conveyed over the entire length of the tube to be processed. As a result, regardless of the size of the tube to be processed, the scouring effect can be exerted efficiently over the entire length of the tube to be processed.

本発明の方法によれば、特許文献2,3のものとは異なり、研掃材と空気とが被処理管の上流端から密閉状態で管内に圧送されるので、管内の空気の吸引と相まって、管内での研掃材の搬送が効率的且つ確実に行われる。 According to the method of the present invention, unlike the ones in Patent Documents 2 and 3, the abrasive and the air are pumped into the pipe in a sealed state from the upstream end of the pipe to be treated, and therefore coupled with the suction of the air in the pipe. The abrasive is transported efficiently and reliably in the pipe.

好適な実施の一形態として、直管である前記被処理管が、次の式において、P,γ,V(80m/s以上)に具体的数値を代入し、且つ、L,Dのいずれかに具体的数値を代入することによって得られるD以下又はL以上のサイズである態様を例示する(請求項2)。
L/D=2P/(0.02×γ×V
L:被処理管の長さ m
D:被処理管の内径(直径) m
P:必要な圧力 Pa
γ:空気密度 kg/m
V:被処理管内の流速 m/s
As a preferred embodiment, the pipe to be processed, which is a straight pipe, substitutes specific numerical values for P, γ, and V (80 m / s or more) in the following formula and either L or D The aspect which is the size below D obtained by substituting a specific numerical value to L or L or more is illustrated (Claim 2).
L / D = 2P / (0.02 × γ × V 2 )
L: Length of pipe to be processed m
D: Inner diameter (diameter) of the pipe to be processed
P: Required pressure Pa
γ: air density kg / m 3
V: Flow velocity in the pipe to be processed m / s

この条件を満たすサイズの被処理管は、本発明に係るブラスト方法の適用対象として好適である。 A tube to be processed having a size satisfying this condition is suitable as an application target of the blasting method according to the present invention.

本発明に係る管内面のブラスト装置は、被処理管の下流端から管内の空気を吸引する吸引装置と、研掃材と空気とを前記被処理管の上流端から密閉状態で管内へと噴射する噴射装置と、を備えることを特徴とする(請求項3)。 A blasting device for a pipe inner surface according to the present invention includes a suction device for sucking air in a pipe from a downstream end of the pipe to be processed, and a cleaning material and air are injected into the pipe in a sealed state from the upstream end of the pipe to be processed. And an injection device that performs (claim 3).

本発明の装置によれば、吸引装置によって被処理管の下流端から管内の空気が吸引されるとともに、噴射装置によって被処理管の上流端から研掃材と空気とが密閉状態で管内に圧送される。これにより、研掃材と空気とを管内で上流から下流へ向けて流動させようとする強い力が被処理管の両端から同時に作用する。このため、被処理管の内径が小さい場合や被処理管の全長が長い場合等、負圧吸引作用のみによっては被処理管の全長に亘って研掃材の搬送作用を短時間で及ぼし難い場合であっても、被処理管の全長において研掃材が確実に搬送される。その結果、被処理管のサイズにかかわらず、被処理管の全長に亘って効率よく研掃効果を及ぼすことができる。 According to the apparatus of the present invention, air in the pipe is sucked from the downstream end of the pipe to be processed by the suction device, and the abrasive and air are pumped into the pipe in a sealed state from the upstream end of the pipe to be processed by the spraying device. Is done. As a result, a strong force for causing the abrasive and air to flow from upstream to downstream in the pipe acts simultaneously from both ends of the pipe to be processed. For this reason, when the inner diameter of the tube to be processed is small or when the entire length of the tube to be processed is long, it is difficult to exert the conveying action of the abrasive material over the entire length of the tube to be processed only by the negative pressure suction action. Even so, the abrasive is reliably conveyed over the entire length of the tube to be processed. As a result, regardless of the size of the tube to be processed, the scouring effect can be exerted efficiently over the entire length of the tube to be processed.

好適な実施の一形態として、直管である前記被処理管が、次の式において、P,γ,V(80m/s以上)に具体的数値を代入し、且つ、L,Dのいずれかに具体的数値を代入することによって得られるD以下又はL以上のサイズである態様を例示する(請求項4)。
L/D=2P/(0.02×γ×V
L:被処理管の長さ m
D:被処理管の内径(直径) m
P:必要な圧力 Pa
γ:空気密度 kg/m
V:被処理管内の流速 m/s
As a preferred embodiment, the pipe to be processed, which is a straight pipe, substitutes specific numerical values for P, γ, and V (80 m / s or more) in the following formula and either L or D The aspect which is a size below D or L obtained by substituting a specific numerical value for is illustrated.
L / D = 2P / (0.02 × γ × V 2 )
L: Length of pipe to be processed m
D: Inner diameter (diameter) of the pipe to be processed
P: Required pressure Pa
γ: air density kg / m 3
V: Flow velocity in the pipe to be processed m / s

この条件を満たすサイズの被処理管は、本発明に係るブラスト装置による研掃処理対象として好適である。 A tube to be processed having a size satisfying this condition is suitable as an object to be cleaned by the blasting apparatus according to the present invention.

好適な実施の一形態として、前記噴射装置は、前記研掃材と前記空気とを前記被処理管の上流端よりも上流側で混合させる混合部と、前記研掃材を貯留すると共に前記混合部へと研掃材を供給する密閉式のサーバタンクと、前記混合部内及び前記サーバタンク内へと空気を圧送する圧送装置と、前記混合部の内圧と等しいかそれ以上となるように前記サーバタンクの内圧を制御するレギュレータと、を備えることを特徴とする(請求項5)。この場合、混合部の内圧と等しいかそれ以上となるようにサーバタンクの内圧が制御されるので、サーバタンクから混合部へと研掃材がスムーズに供給される。 As a preferred embodiment, the injection device includes a mixing unit that mixes the scouring material and the air upstream of an upstream end of the processing target pipe, stores the scouring material, and mixes the scouring material. A sealed server tank for supplying the abrasive to the unit, a pumping device for pumping air into the mixing unit and the server tank, and the server so as to be equal to or higher than the internal pressure of the mixing unit And a regulator for controlling the internal pressure of the tank (claim 5). In this case, since the internal pressure of the server tank is controlled so as to be equal to or higher than the internal pressure of the mixing unit, the abrasive is smoothly supplied from the server tank to the mixing unit.

本発明に係る管内面ブラストシステムは、被処理管の移送ラインに沿う入側と出側とにそれぞれブラスト装置が配設され、前記入側ブラスト装置は、前記被処理管の一端から管内の空気を吸引する入側吸引装置と、研掃材と空気とを前記被処理管の他端から密閉状態で管内へと旋回流として噴射する入側噴射装置と、を備え、前記出側ブラスト装置は、前記被処理管の前記他端から管内の空気を吸引する出側吸引装置と、研掃材と空気とを前記被処理管の前記一端から密閉状態で管内へと旋回流として噴射する出側噴射装置と、を備えることを特徴とする(請求項6)。 In the pipe inner surface blasting system according to the present invention, a blasting device is provided on each of an inlet side and an outlet side along a transfer line of a pipe to be processed, and the inlet blasting apparatus is configured to send air in the pipe from one end of the pipe to be processed. An inlet-side suction device that sucks in, and an inlet-side injection device that injects the abrasive and air as a swirling flow into the pipe in a sealed state from the other end of the pipe to be processed. A discharge side suction device for sucking air in the pipe from the other end of the pipe to be processed, and a discharge side for injecting the polishing material and air into the pipe in a sealed state from the one end of the pipe to be processed And an injection device (claim 6).

本発明に係る管内面ブラストシステムは、研掃材の旋回流による研掃において、被処理管の両端間で管内面の研掃処理の効果に差が出てしまうという問題を解決しようとするものである。 The pipe inner surface blasting system according to the present invention is intended to solve the problem that the effect of the cleaning process on the inner surface of the pipe is different between both ends of the pipe to be processed in the cleaning by the swirling flow of the polishing material. It is.

本発明によれば、被処理管は、入側ブラスト装置で研掃処理を施され、その後、被処理管の移送ラインに沿って移送されて、出側ブラスト装置で研掃処理を施される。 According to the present invention, the tube to be processed is subjected to the blasting process by the inlet blast device, and then transferred along the transfer line of the tube to be processed, and the blasting process is performed by the outlet blast device. .

入側ブラスト装置においては、入側吸引装置によって被処理管の一端から管内の空気が吸引されると共に、入側噴射装置によって被処理管の他端から密閉状態で管内に研掃材と空気とが旋回流として噴射される。これにより、研掃材と空気とを管内で被処理管の他端から一端へ向けて流動させようとする強い力が被処理管の両端から同時に作用する。このため、被処理管の内径が小さい場合や被処理管の全長が長い場合等、負圧吸引作用のみによっては被処理管の全長に亘って研掃材の搬送作用を短時間で及ぼし難い場合であっても、被処理管の全長において研掃材が確実に搬送される。 In the inlet-side blasting apparatus, air in the pipe is sucked from one end of the pipe to be processed by the inlet-side suction apparatus, and the abrasive and air are sealed in the pipe in a sealed state from the other end of the pipe to be processed by the inlet-side injection apparatus. Are injected as a swirling flow. As a result, a strong force for causing the abrasive and air to flow in the tube from the other end of the tube to be processed to one end simultaneously acts from both ends of the tube to be processed. For this reason, when the inner diameter of the tube to be processed is small or when the entire length of the tube to be processed is long, it is difficult to exert the conveying action of the abrasive material over the entire length of the tube to be processed only by the negative pressure suction action. Even so, the abrasive is reliably conveyed over the entire length of the tube to be processed.

出側ブラスト装置においては、出側吸引装置によって被処理管の他端から管内の空気が吸引されると共に、出側噴射装置によって被処理管の一端から密閉状態で管内に研掃材と空気とが旋回流として噴射される。これにより、研掃材と空気とを管内で被処理管の一端から他端へ向けて流動させようとする強い力が被処理管の両端から同時に作用する。このため、被処理管の内径が小さい場合や被処理管の全長が長い場合等、負圧吸引作用のみによっては被処理管の全長に亘って研掃材の搬送作用を短時間で及ぼし難い場合であっても、被処理管の全長において研掃材が確実に搬送される。 In the outlet blast device, air in the pipe is sucked from the other end of the pipe to be processed by the outlet suction apparatus, and the abrasive and air are sealed in the pipe in a sealed state from one end of the pipe to be processed by the outlet jet apparatus. Are injected as a swirling flow. As a result, a strong force for causing the abrasive and air to flow in the pipe from one end to the other end of the pipe is simultaneously applied from both ends of the pipe. For this reason, when the inner diameter of the tube to be processed is small or when the entire length of the tube to be processed is long, it is difficult to exert the conveying action of the abrasive material over the entire length of the tube to be processed only by the negative pressure suction action. Even so, the abrasive is reliably conveyed over the entire length of the tube to be processed.

本発明においては、一つの被処理管に対して、吸引と噴射の作用方向(研掃材の流動方向)を逆にして研掃処理が二度施される。これにより、被処理管の両端間での旋回流による研掃処理の効果を均等化することが可能となる。加えて、入側ブラスト装置と出側ブラスト装置が被処理管の移送ラインに沿う入側と出側とに配置されるので、二度の研掃処理を施すに当たって被処理管を反転させる必要がない。よって、作業が楽に行え、処理効率も良い。 In the present invention, a single pipe to be treated is subjected to the blasting process twice with the action directions of suction and jetting (the flow direction of the scouring material) reversed. Thereby, it becomes possible to equalize the effect of the blasting process by the swirling flow between both ends of the pipe to be processed. In addition, since the inlet blasting device and the outlet blasting device are arranged on the inlet side and the outlet side along the transfer line of the pipe to be processed, it is necessary to invert the pipe to be processed in performing the two blasting processes. Absent. Therefore, work can be performed easily and processing efficiency is good.

好適な実施の一形態として、前記入側ブラスト装置が、前記被処理管の前記他端側に位置し且つ前記被処理管内に供給するための研掃材を貯留する入側サーバタンクと、前記被処理管の前記一端側に位置し且つ前記被処理管内を通過した研掃材を受け入れる入側レシーバタンクと、を備え、前記出側ブラスト装置が、前記被処理管の前記一端側に位置し且つ前記被処理管内に供給するための研掃材を貯留する出側サーバタンクと、前記被処理管の前記他端側に位置し且つ前記被処理管内を通過した研掃材を受け入れる出側レシーバタンクと、を備え、前記入側レシーバタンク内の研掃材を前記出側サーバタンク内へと移送できるように前記入側レシーバタンクと前記出側サーバタンクとが連結され、前記出側レシーバタンク内の研掃材を前記入側サーバタンク内へと移送できるように前記出側レシーバタンクと前記入側サーバタンクとが連結されることを特徴とする(請求項7)。 As one preferred embodiment, the entry-side blast device is located on the other end side of the tube to be treated and stores an abrasive for supplying the material to be fed into the tube to be treated; An inlet-side receiver tank that is located on the one end side of the pipe to be processed and receives the polishing material that has passed through the pipe to be processed, and the outlet blast device is located on the one end side of the pipe to be processed. And a delivery-side server tank that stores a polishing material to be supplied into the processing pipe, and a delivery-side receiver that is located on the other end side of the processing pipe and receives the polishing material that has passed through the processing pipe. A tank, wherein the inlet receiver tank and the outlet server tank are coupled so that the abrasive in the inlet receiver tank can be transferred into the outlet server tank, and the outlet receiver tank The abrasive material in the And the exit-side receiver tank and entering-side server tank so that it can transfer to the side server tank is characterized in that it is connected (claim 7).

この実施の形態によれば、入側ブラスト装置で被処理管の内面の研掃を終えた研掃材が出側ブラスト装置に再投入され、出側ブラスト装置で被処理管の内面の研掃を終えた研掃材が入側ブラスト装置に再投入され、これが繰り返される。研掃材が繰り返し循環するように使用されるので、経済的である。 According to this embodiment, the polishing material that has finished polishing the inner surface of the tube to be processed by the inlet blast device is reintroduced into the outlet blast device, and the inner surface of the tube to be processed is cleaned by the outlet blast device. The polishing material that has finished is re-introduced into the inlet blasting device, and this is repeated. Since the abrasive is used to circulate repeatedly, it is economical.

さらに、入側ブラスト装置を構成する入側レシーバタンクと出側ブラスト装置を構成する出側サーバタンクは、いずれも被処理管の一端側にある。また、出側ブラスト装置を構成する出側レシーバタンクと入側ブラスト装置を構成する入側サーバタンクは、いずれも被処理管の他端側にある。このため、入側レシーバタンクと出側サーバタンクとの間の研掃材移送路と、出側レシーバタンクと入側サーバタンクとの間の研掃材移送路とが、共に短くてすみ、研掃材移送路の配設レイアウトも簡素にできる。よって、研掃材移送路の配設コストが節約でき、一層経済的である。 Furthermore, the incoming receiver tank that constitutes the incoming blast device and the outgoing server tank that constitutes the outgoing blast device are both on one end side of the pipe to be processed. Further, both the outgoing receiver tank constituting the outgoing blast device and the incoming server tank constituting the incoming blast device are on the other end side of the pipe to be processed. For this reason, the polishing material transfer path between the inlet receiver tank and the outlet server tank and the abrasive transfer path between the outlet receiver tank and the inlet server tank can both be short and sharpened. The layout of the scavenging material transfer path can also be simplified. Therefore, the arrangement cost of the scouring material transfer path can be saved, which is more economical.

本発明の実施の一形態に係る管内面のブラスト装置の構成図である。It is a lineblock diagram of the blasting device of the pipe inner surface concerning one embodiment of the present invention. 図1のブラスト装置における噴射装置の拡大断面図である。It is an expanded sectional view of the injection apparatus in the blast apparatus of FIG. 本発明の実施の一形態に係る管内面ブラストシステムの概略平面図である。1 is a schematic plan view of a tube inner surface blast system according to an embodiment of the present invention.

以下、添付図面を参照して、本発明の実施の形態について説明する。 Embodiments of the present invention will be described below with reference to the accompanying drawings.

図1に示すように、本発明の実施の一形態に係る管内面のブラスト装置1は、被処理管Pの下流端P1から管内の空気を吸引するとともに研掃に関与した研掃材や研掃屑を回収する吸引回収装置2と、研掃材と空気とを被処理管Pの上流端P2から密閉状態で管内へと噴射する噴射装置3と、を備える。 As shown in FIG. 1, a blasting device 1 for an inner surface of a pipe according to an embodiment of the present invention sucks air in the pipe from a downstream end P1 of a pipe to be processed P and also uses an abrasive or a polishing material involved in the blasting. A suction recovery device 2 that recovers scraps, and an injection device 3 that injects the abrasive and air from the upstream end P2 of the processing pipe P into the pipe in a sealed state.

噴射装置3は、被処理管Pの上流端P2に密着する研掃作業位置(図1に示す位置)と、被処理管Pの上流端P2から離れる退避位置(図1に示す位置から左方へ移動した位置)とに移動自在とされる。そして、吸引回収装置2に対して被処理管Pの下流端P1を接続した後、退避位置にある噴射装置3を図1に示す研掃作業位置へと移動させることによって、噴射装置3と吸引回収装置2との間で被処理管Pを保持する。この保持状態にて被処理管Pに対して研掃処理が施される。研掃処理が終了したら、噴射装置3を退避位置へと移動させることで被処理管Pを解放し、被処理管Pを移送ライン(図1の紙面に対して垂直な方向)に沿って移送する。 The injecting device 3 has a polishing operation position (position shown in FIG. 1) that is in close contact with the upstream end P2 of the processing pipe P, and a retreat position (leftward from the position shown in FIG. 1) away from the upstream end P2 of the processing pipe P. The position can be moved freely. And after connecting the downstream end P1 of the to-be-processed pipe P with respect to the suction collection | recovery apparatus 2, the injection apparatus 3 and suction are moved by moving the injection apparatus 3 in a retracted position to the cleaning work position shown in FIG. The to-be-processed pipe | tube P is hold | maintained between the collection | recovery apparatuses 2. FIG. In this holding state, the to-be-processed pipe P is subjected to the blasting process. When the polishing process is completed, the processing pipe P is released by moving the injection device 3 to the retracted position, and the processing pipe P is transferred along the transfer line (direction perpendicular to the paper surface of FIG. 1). To do.

また、噴射装置3は、台車35に搭載される等して、被処理管Pの長さ方向に沿って大きく移動可能でもある。この構成により、長さの異なる被処理管Pの研掃処理に対応することができる。 Moreover, the injection device 3 can be moved largely along the length direction of the pipe P to be processed, for example, by being mounted on the carriage 35. With this configuration, it is possible to cope with the blasting process of the pipes P having different lengths.

噴射装置3は、サーバタンク4と、混合部5と、圧送装置6とを備える。サーバタンク4は、被処理管P内に供給するための研掃材を貯留し、この研掃材を混合部5へと供給する。混合部5は、研掃材と空気とを被処理管Pの上流端P2よりも上流側で混合させる。圧送装置6は、混合部5内及びサーバタンク4内へと圧縮空気を供給する。圧送装置6としては、例えばコンプレッサの他、吐出仕様のルーツブロワ等の送風機を用いることもできる。混合部5で混合された研掃材と搬送用の空気は、被処理管P内を上流P2から下流端P1へと高速で流動し、この流動過程で研掃材が被処理管Pの内面を研掃する。研掃に関与した研掃材は、搬送用の空気とともに吸引回収装置2によって負圧吸引されて被処理管Pの下流端P1から流出し、回収される。 The injection device 3 includes a server tank 4, a mixing unit 5, and a pressure feeding device 6. The server tank 4 stores a polishing material to be supplied into the processing pipe P, and supplies the polishing material to the mixing unit 5. The mixing unit 5 mixes the abrasive and the air upstream of the upstream end P2 of the pipe P to be processed. The pressure feeding device 6 supplies compressed air into the mixing unit 5 and the server tank 4. As the pumping device 6, for example, a blower such as a roots blower having a discharge specification can be used in addition to a compressor. The abrasive and the air for conveyance mixed in the mixing unit 5 flow at a high speed in the pipe P from the upstream P2 to the downstream end P1, and in this flow process, the abrasive is the inner surface of the pipe P to be processed. Clean up. The polishing material involved in the cleaning is suctioned with negative pressure by the suction recovery device 2 together with the air for conveyance, flows out from the downstream end P1 of the pipe P to be processed, and is recovered.

吸引回収装置2は吸引装置7と回収装置8とで構成される。吸引装置7としては、例えば乾式又は湿式ルーツブロワ等の真空ブロワや、真空ポンプが用いられる。吸引装置7と被処理管Pの下流端P1との間には、回収装置8が配設される。この回収装置8によって、被処理管Pの内面の研掃に関与した研掃材や、研掃に関与することで破砕した研掃材や、研掃屑等が回収される。回収装置8は、上流側から順に、レシーバタンク9と、サイクロンセパレータ10と、集塵機11と、を含んでいる。レシーバタンク9は、研掃を終えた研掃材を受け入れて、この研掃材の一部を収容する。サイクロンセパレータ10は、研掃後でも完全には破砕していない粒状の研掃材と搬送用の空気とを分離する。集塵機11は、破砕した研掃材や研掃屑と搬送用の空気とを分離する。そして、これらの異物を除去された清浄な空気は、吸引装置7の排気側に配設される排気サイレンサ12を通して大気中へと放出される。 The suction recovery device 2 includes a suction device 7 and a recovery device 8. As the suction device 7, for example, a vacuum blower such as a dry or wet roots blower or a vacuum pump is used. A recovery device 8 is disposed between the suction device 7 and the downstream end P1 of the processing pipe P. The recovery device 8 recovers the polishing material involved in the cleaning of the inner surface of the pipe P to be processed, the polishing material crushed by participating in the cleaning, the polishing scraps, and the like. The collection device 8 includes a receiver tank 9, a cyclone separator 10, and a dust collector 11 in order from the upstream side. The receiver tank 9 receives the scouring material that has finished scouring and accommodates a part of the scouring material. The cyclone separator 10 separates the granular polishing material that has not been completely crushed even after the polishing and the air for conveyance. The dust collector 11 separates the crushed abrasive or abrasive scraps from the air for conveyance. The clean air from which these foreign substances have been removed is released into the atmosphere through the exhaust silencer 12 disposed on the exhaust side of the suction device 7.

吸引装置7は、研掃に関与した研掃材を回収するのに必要な吸引力を有するだけでは足りない。従来の負圧吸引式管内面ブラスト装置に使用されているような、通常サイズの被処理管に対してであれば被処理管内の全体に短時間で研掃材搬送気流を生じさせることができるだけの負圧吸引力を有することを要する。すなわち、本実施の形態に係る管内面のブラスト装置1は、従来の負圧吸引式管内面ブラスト装置に使用されているような高出力の吸引装置をもってしても圧力損失の問題で被処理管Pの上流端P2から研掃材搬送気流を引くことができないほど内径が小さいか全長が長い被処理管Pに対して研掃処理を行う場合に有効な装置である。 It is not sufficient for the suction device 7 to have a suction force necessary for recovering the polishing material involved in the polishing. For normal pipes to be processed, such as those used in conventional negative pressure suction pipe inner surface blasting equipment, it is possible to generate an abrasive conveying airflow in the entire pipe in a short time. It is necessary to have a negative pressure suction force of In other words, the pipe inner surface blasting apparatus 1 according to the present embodiment has a high output suction device such as that used in the conventional negative pressure suction type pipe inner surface blasting apparatus, and is subject to pressure loss. This is an effective apparatus for performing the blasting process on the pipe P having a small inner diameter or a long total length so that the blast material conveying air current cannot be drawn from the upstream end P2 of P.

本実施の形態に係る管内面のブラスト装置1で研掃処理を行うのに適する被処理管Pの内径Dと長さLとの関係は、次のようにして定めることができる。 The relationship between the inner diameter D and the length L of the pipe P to be processed, which is suitable for performing the blasting process with the blasting device 1 on the pipe inner surface according to the present embodiment, can be determined as follows.

一般に、開口面積がA(=πD×1/4)(m)である直管(固有の損失係数ζ=0.02×L/D)内に、ある風量Q(m/min)の空気を流すために必要な圧力P(Pa)は、直管の内径(直径)D(m)及び長さL(m)と、空気密度γ(kg/m)(例えば、20℃大気圧の空気密度γ=1.2kg/m)と、管内を通る空気の速度V(=Q/60A)(m/s)とで、次のように決まる(ダルシー・ワイスバッハの式)。
P=ζ・γ・V/2・・・・・・(1)
P=0.02×L/D×γ×V/2・・・・・・(2)
Generally, an air volume Q (m 3 / min) within a straight pipe (inherent loss coefficient ζ = 0.02 × L / D) having an opening area A (= πD 2 × 1/4) (m 2 ). The pressure P (Pa) required for flowing the air of the straight pipe is the inner diameter (diameter) D (m) and length L (m) of the straight pipe, and the air density γ (kg / m 3 ) (for example, a large 20 ° C. Atmospheric air density γ = 1.2 kg / m 3 ) and air velocity V (= Q / 60A) (m / s) in the pipe are determined as follows (Darcy-Weissbach equation).
P = ζ · γ · V 2 /2 ······ (1)
P = 0.02 × L / D × γ × V 2/2 ······ (2)

ここで、P:必要な圧力(圧力損失) Pa
A:直管の断面積 m
(A=πD×1/4)
Q:風量 m/min
V:流速(V=Q/60A) m/s
γ:空気密度 kg/m
(20℃大気圧の空気密度γ=1.2kg/m
ζ:直管固有の損失係数(ζ=0.02×L/D)
D:直管の内径(直径) m
L:直管の長さ m
Where P: Required pressure (pressure loss) Pa
A: Cross section of straight pipe m 2
(A = πD 2 × 1/4)
Q: Air volume m 3 / min
V: Flow velocity (V = Q / 60A) m / s
γ: air density kg / m 3
(Air density γ = 1.2 kg / m 3 at 20 ° C atmospheric pressure)
ζ: loss factor specific to straight pipe (ζ = 0.02 × L / D)
D: Inner diameter (diameter) of straight pipe m
L: Length of straight pipe m

ところで、吸引装置7には、吸引圧力について固有の限界値がある。例えば、吸引装置7として乾式ルーツブロワを用いる場合には吸引圧力は60kPaが限界、湿式ルーツブロワを用いる場合には吸引圧力は95kPaが限界、真空ポンプを用いる場合には吸引圧力は101.3kPaが限界である。これらの限界値を前記必要な圧力が超える場合に、本実施の形態に係る管内面のブラスト装置1が有効となる。 Incidentally, the suction device 7 has an inherent limit value for the suction pressure. For example, when a dry roots blower is used as the suction device 7, the suction pressure is limited to 60 kPa, when a wet roots blower is used, the suction pressure is limited to 95 kPa, and when a vacuum pump is used, the suction pressure is limited to 101.3 kPa. is there. When the required pressure exceeds these limit values, the blast device 1 for the pipe inner surface according to the present embodiment is effective.

よって、前記(2)式において、管内を通る空気の速度Vを所望の値(後で述べるように、V=80m/s以上であるのが好ましい)に設定し、且つ、前記限界値を超える必要圧力を設定すれば、本実施の形態に係る管内面のブラスト装置1が有効となる被処理管Pの内径Dと長さLとの関係が定まる。例えば、被処理管Pの内径Dを一定値に決めれば被処理管Pの好ましい最短の長さLが決まり、被処理管Pの長さLを一定値に決めれば被処理管Pの好ましい最大の内径Dが決まる。 Therefore, in the equation (2), the velocity V of the air passing through the pipe is set to a desired value (preferably, V = 80 m / s or more, as will be described later), and exceeds the limit value. If the required pressure is set, the relationship between the inner diameter D and the length L of the pipe P to be processed in which the pipe inner surface blasting apparatus 1 according to the present embodiment is effective is determined. For example, if the inner diameter D of the pipe to be processed P is determined to be a constant value, the preferred shortest length L of the pipe to be processed P is determined, and if the length L of the pipe to be processed P is determined to be a constant value, the preferred maximum of the pipe to be processed P is determined. The inner diameter D is determined.

前記(2)式を変形して、
L/D=2P/(0.02×γ×V)・・・・・・(3)
前記(3)式において、例えば、
P=70kPa=70000Pa
V=80m/s
γ=1.2kg/m (20℃大気圧下)
とすると、
L/D≒911.46・・・・・・(4)
ここで、D=0.08(m)とすると、L≒72.92(m)
By transforming the equation (2),
L / D = 2P / (0.02 × γ × V 2 ) (3)
In the formula (3), for example,
P = 70 kPa = 70000 Pa
V = 80m / s
γ = 1.2 kg / m 3 (under 20 ° C atmospheric pressure)
Then,
L / D ≒ 911.46 (4)
Here, if D = 0.08 (m), L≈72.92 (m)

よって、被処理管Pの内径Dが0.08mの場合、その被処理管Pの長さLが72.92m以上であれば、従来の負圧吸引式管内面ブラスト装置では研掃処理ができないけれども、本実施の形態に係る管内面のブラスト装置1であれば研掃処理ができることになる。 Therefore, when the inner diameter D of the pipe to be processed P is 0.08 m, if the length L of the pipe to be processed P is 72.92 m or more, the conventional negative pressure suction type pipe inner surface blasting device cannot perform the blasting process. However, the blasting device 1 on the pipe inner surface according to the present embodiment can perform the blasting process.

また、前記(4)式において、
L=50(m)とすると、D≒0.055(m)。
よって、被処理管Pの長さLが50mの場合、その被処理管Pの内径Dが0.055m以下であれば、従来の負圧吸引式管内面ブラスト装置では研掃処理ができないけれども、本実施の形態に係る管内面のブラスト装置であれば研掃処理ができることになる。
In the above equation (4),
When L = 50 (m), D≈0.055 (m).
Therefore, when the length L of the pipe to be processed P is 50 m, if the inner diameter D of the pipe to be processed P is 0.055 m or less, the conventional negative pressure suction type pipe inner surface blasting apparatus cannot perform the polishing process. The blasting device for the pipe inner surface according to the present embodiment can perform the blasting process.

本実施の形態に係る管内面のブラスト装置1によれば、吸引装置7によって被処理管Pの下流端P1から管内の空気が吸引されるとともに、噴射装置3によって被処理管Pの上流端P2から研掃材と空気とが密閉状態で管内に圧送される。これにより、研掃材と空気とを管内で上流から下流へ向けて流動させようとする強い力が被処理管Pの両端から同時に作用する。このため、被処理管Pの内径Dが小さい場合や被処理管Pの全長Lが長い場合等、負圧吸引作用のみによっては被処理管Pの全長に亘って研掃材の搬送作用を短時間で及ぼし難い場合であっても、被処理管の全長において研掃材が確実に搬送される。その結果、被処理管のサイズにかかわらず、被処理管Pの全長に亘って効率よく研掃効果を及ぼすことができる。 According to the blast device 1 for the pipe inner surface according to the present embodiment, air in the pipe is sucked from the downstream end P1 of the pipe P to be processed by the suction device 7 and the upstream end P2 of the pipe P to be processed by the injection device 3. Then the abrasive and air are pumped into the tube in a sealed state. As a result, a strong force for causing the abrasive and air to flow from upstream to downstream in the pipe acts simultaneously from both ends of the pipe P to be processed. For this reason, when the inner diameter D of the pipe to be processed P is small, or when the total length L of the pipe to be processed P is long, the conveying action of the polishing material is shortened over the entire length of the pipe to be processed P only by the negative pressure suction action. Even if it is difficult to exert in time, the abrasive is reliably conveyed over the entire length of the tube to be processed. As a result, regardless of the size of the tube to be processed, the blasting effect can be exerted efficiently over the entire length of the tube to be processed P.

次に、前記噴射装置3の詳細について説明する。図2に示すように、サーバタンク4は上部にホッパ13を備える。このホッパ13を通してサーバタンク4内に研掃材が投入される。サーバタンク4の下面には研掃材流出パイプ14が下向きに配設される。この研掃材流出パイプ14は、調量バルブ15を介して下方に配設される混合部5へと連通する。したがって、研掃材流出パイプ14と調量バルブ15とを通して、サーバタンク4内の研掃材が混合部へと落下する。そして、調量バルブ15の操作コック16を回動操作することで、研掃材の混合部5への落下量を調整できる。 Next, the detail of the said injection apparatus 3 is demonstrated. As shown in FIG. 2, the server tank 4 includes a hopper 13 at the top. Abrasive material is introduced into the server tank 4 through the hopper 13. A polishing material outflow pipe 14 is disposed on the lower surface of the server tank 4 downward. The scouring material outflow pipe 14 communicates with the mixing unit 5 disposed below through a metering valve 15. Therefore, the abrasive in the server tank 4 falls to the mixing section through the abrasive outlet pipe 14 and the metering valve 15. Then, by turning the operation cock 16 of the metering valve 15, it is possible to adjust the amount of the abrasive material dropped onto the mixing portion 5.

混合部5には圧送装置6から圧縮空気が供給される。このため、何らの措置も講じないと、サーバタンク4から混合部5への研掃材の落下が妨げられる。そこで、圧送装置6からの圧縮空気をサーバタンク4内にも導入し、混合部5の内圧を検知する圧力センサ17を設け、この圧力センサ17の検知信号を受けて混合部5の内圧と等しいかそれ以上となるようにサーバタンク4の内圧を制御するレギュレータ18を設ける。これにより、サーバタンク4の内圧を混合部5の内圧と同じがそれ以上に制御することができ、サーバタンク4から混合部5への研掃材の円滑な落下が実現できる。 The mixing unit 5 is supplied with compressed air from the pressure feeding device 6. For this reason, if no measures are taken, the polishing material is prevented from dropping from the server tank 4 to the mixing section 5. Therefore, the compressed air from the pressure feeding device 6 is also introduced into the server tank 4 and a pressure sensor 17 for detecting the internal pressure of the mixing unit 5 is provided. The pressure sensor 17 receives a detection signal to equal the internal pressure of the mixing unit 5. A regulator 18 for controlling the internal pressure of the server tank 4 is provided so as to be more than that. As a result, the internal pressure of the server tank 4 can be controlled to be equal to or higher than the internal pressure of the mixing unit 5, and a smooth drop of the abrasive from the server tank 4 to the mixing unit 5 can be realized.

圧送装置6からの圧縮空気はエアドライヤ19を通してヘッダータンク20に圧送される。ヘッダータンク20は、主エア配管21を介して混合部5へと連通する。主エア配管21上にはエアバルブ22が配設される。また、ヘッダータンク20は、副エア配管23を介してサーバタンク4に連通する。副エア配管23上には、ヘッダータンク20側から順に、前記レギュレータ(電空レギュレータ)18と残圧排気弁24とが配設される。副エア配管23は、気密状態でサーバタンク4内に突入し、サーバタンク4内の上部中央位置で上向きに延びて開口している。この上向き開口部25には、傘形の弁体からなる密閉制御弁26が上下動自在に嵌合している。この密閉制御弁26は、上昇位置でホッパ13の下端開口部27を密閉し、下降位置でホッパ13の下端開口部27を開放する。副エア配管23を通してヘッダータンク20からサーバタンク4内へと空気が圧送されると、この空気が密閉制御弁26を上昇位置へと押し上げて、ホッパ13の下端開口部27を気密に閉じる。これにより、サーバタンク4は、研掃材流出パイプ14の部分を除いて密閉状態となる。 The compressed air from the pressure feeding device 6 is pressure fed to the header tank 20 through the air dryer 19. The header tank 20 communicates with the mixing unit 5 via the main air pipe 21. An air valve 22 is disposed on the main air pipe 21. Further, the header tank 20 communicates with the server tank 4 via the sub air pipe 23. On the sub air pipe 23, the regulator (electro-pneumatic regulator) 18 and the residual pressure exhaust valve 24 are disposed in this order from the header tank 20 side. The sub air pipe 23 enters the server tank 4 in an airtight state, and opens upward at an upper central position in the server tank 4. A sealing control valve 26 made of an umbrella-shaped valve body is fitted in the upward opening 25 so as to be movable up and down. The sealing control valve 26 seals the lower end opening 27 of the hopper 13 at the raised position and opens the lower end opening 27 of the hopper 13 at the lowered position. When air is pumped from the header tank 20 into the server tank 4 through the sub air pipe 23, the air pushes up the sealing control valve 26 to the raised position, and the lower end opening 27 of the hopper 13 is closed in an airtight manner. As a result, the server tank 4 is hermetically sealed except for the portion of the scouring material outflow pipe 14.

また、副エア配管23を通してサーバタンク4内に圧送される空気によって、サーバタンク4の内圧が上昇する。サーバタンク4の内圧は、電空レギュレータ18によって混合部5の内圧と同じがそれ以上に制御される。過剰な圧縮空気は残圧排気弁24から自然に排気される。 Further, the internal pressure of the server tank 4 increases due to the air pressure fed into the server tank 4 through the sub air pipe 23. The internal pressure of the server tank 4 is controlled by the electropneumatic regulator 18 to be equal to or higher than the internal pressure of the mixing unit 5. Excess compressed air is naturally exhausted from the residual pressure exhaust valve 24.

混合部5はサイクロンパイプ28に連通する。このサイクロンパイプ28の下流端には、被処理管Pへの接続部29が形成される。接続部29は、被処理管Pの様々な外径サイズに対応できるように、先端に近づくにつれて拡開する形状とされている。主エア配管21を通して混合部5に供給される圧縮空気は、同じく混合部5に供給される研掃材を含んだ状態で、サイクロンパイプ28の中心軸線Xの回りで旋回しながらサイクロンパイプ28内を下流側へと高速で流動する。この旋回流Aが研掃材搬送気流である。 The mixing unit 5 communicates with the cyclone pipe 28. At the downstream end of the cyclone pipe 28, a connection portion 29 to the processing pipe P is formed. The connecting portion 29 has a shape that expands toward the tip so that it can accommodate various outer diameter sizes of the pipe P to be processed. The compressed air supplied to the mixing unit 5 through the main air pipe 21 is swirled around the center axis X of the cyclone pipe 28 while containing the abrasive material supplied to the mixing unit 5. To the downstream side at high speed. This swirling flow A is the abrasive material conveying airflow.

本実施の形態では、サイクロンパイプ28に対して混合部5を偏心状態で接続することで、断面円形のサイクロンパイプ28内に旋回流Aを生じさせるようにしている。しかし、旋回流の形成手段はこれに限定されず、圧縮空気を旋回させるための回転翼やガイドを設けたりすることもできる。研掃材搬送気流を旋回させながら被処理管P内に圧送することで、被処理管Pの内面に対して研掃材が衝突しやすくなる。このため、被処理管Pの内面の全体に対して隈なく効果的な研掃作用を施すことができる。 In the present embodiment, the mixing portion 5 is connected to the cyclone pipe 28 in an eccentric state so that a swirl flow A is generated in the cyclone pipe 28 having a circular cross section. However, the means for forming the swirling flow is not limited to this, and a rotating blade or a guide for swirling the compressed air can be provided. By pumping the cleaning material transport air flow into the processing pipe P while swirling, the polishing material easily collides with the inner surface of the processing pipe P. For this reason, the entire inner surface of the pipe P to be processed can be effectively polished.

本実施の形態では、圧送装置6から混合部5へと供給される圧縮空気は、そのすべてが密閉状態で被処理管P内へと圧送される。加えて、被処理管Pの下流端P1側から、吸引装置7によって被処理管P内に負圧吸引力が作用する。このため、吸引装置7の負圧吸引力だけでは被処理管Pの上流端P2から研掃材搬送気流を引くことができないほど内径が小さいか又は全長が長い被処理管Pに対してであっても、流速80m/s以上の高速で研掃材搬送気流を流動させることができ、効率的に研掃処理を行うことができる。研掃材搬送気流の管内流速は、例えば、100m/s以上とするのが好ましく、120m/s以上とするのがさらに好ましい。 In the present embodiment, all of the compressed air supplied from the pumping device 6 to the mixing unit 5 is pumped into the processing pipe P in a sealed state. In addition, a negative pressure suction force acts in the pipe P to be processed by the suction device 7 from the downstream end P1 side of the pipe P to be processed. For this reason, the inner diameter is small or the total length is not long enough to draw the polishing material conveying air flow from the upstream end P2 of the processed pipe P only by the negative pressure suction force of the suction device 7. However, it is possible to flow the blast material conveying airflow at a high speed of 80 m / s or higher, and to efficiently perform the blasting process. The in-pipe flow velocity of the abrasive transporting airflow is preferably, for example, 100 m / s or more, and more preferably 120 m / s or more.

なお、本実施の形態では、研掃材と空気とが噴射装置3から密閉状態で被処理管P内に噴射されるので、被処理管P内への研掃材搬送気流の流入量が被処理管Pからの研掃材搬送気流の流出量よりも大きいと、装置の破損につながってしまう。このため、吸引装置7による研掃材搬送気流の吸入量が噴射装置3による研掃材搬送気流の圧送量よりも大きくなるように設定する。 In the present embodiment, since the abrasive and air are jetted from the injection device 3 into the treated pipe P in a sealed state, the amount of inflow of the abrasive conveying air flow into the treated pipe P is reduced. If it is larger than the outflow amount of the abrasive conveying airflow from the processing pipe P, it will lead to damage of the apparatus. For this reason, it sets so that the suction | inhalation amount of the scouring material conveyance airflow by the suction device 7 may become larger than the pumping amount of the scouring material conveyance airflow by the injection apparatus 3. FIG.

また、本実施の形態では、最もシンプルな例として、単一のサーバタンク4に対して混合部5及びサイクロンパイプ28を一系統設けたものについて説明したが、処理効率を高めるための他の例として、単一のサーバタンク4に対して混合部5及びサイクロンパイプ28を複数系統設けることも可能である。混合部5及びサイクロンパイプ28を複数系統設ける場合には、各系統に対して空気を安定供給するためのアキュムレータとして、前記ヘッダータンク20を設けることが特に有効となる。 In the present embodiment, as the simplest example, a description has been given of a single server tank 4 provided with one system of the mixing unit 5 and the cyclone pipe 28, but another example for increasing the processing efficiency. It is also possible to provide a plurality of mixing sections 5 and cyclone pipes 28 for a single server tank 4. In the case where a plurality of systems of the mixing unit 5 and the cyclone pipe 28 are provided, it is particularly effective to provide the header tank 20 as an accumulator for stably supplying air to each system.

次に、図3を参照して、前述した管内面のブラスト装置1を含む管内面ブラストシステムについて説明する。このシステムは、被処理管Pの両端P1,P2間で管内面の研掃処理の効果に差が出てしまうという問題を解決しようとするものである。すなわち、被処理管P内を流動する研掃材の旋回流Aは、上流端P2側では旋回の度合いが強くても下流端P1に近づくにつれて弱くなる。このため、被処理管Pの下流端P1側での研掃効果が低下するという問題がある。 Next, a pipe inner surface blasting system including the aforementioned pipe inner surface blasting device 1 will be described with reference to FIG. This system is intended to solve the problem that there is a difference in the effect of the blasting process on the inner surface of the pipe P1 between the both ends P1, P2. That is, the swirling flow A of the abrasive flowing in the processing pipe P becomes weaker as it approaches the downstream end P1 even if the degree of swirl is strong on the upstream end P2 side. For this reason, there exists a problem that the scouring effect in the downstream end P1 side of the to-be-processed pipe P falls.

この問題を解決するため、本実施の形態の管内面ブラストシステム30は、前記ブラスト装置1と同一構成のブラスト装置を二つ備える。そして、これらのブラスト装置(入側ブラスト装置1aと出側ブラスト装置1b)が被処理管Pの移送ラインに沿う入側と出側とに、互いに逆方向に作用するように配置される。 In order to solve this problem, the pipe inner surface blasting system 30 of the present embodiment includes two blasting apparatuses having the same configuration as the blasting apparatus 1. These blasting devices (the entry blasting device 1a and the exiting blasting device 1b) are arranged so as to act in opposite directions on the entry side and the exit side along the transfer line of the pipe P to be processed.

図3に示すように、入側ブラスト装置1aと出側ブラスト装置1bは、入側設備31aと出側設備31bとの間に配設される。入側設備1aと出側設備1bは、被処理管Pの移送ラインとなる移送コンベア32で互いに連結される。この移送コンベアに沿う入側に入側ブラスト装置1a、出側に出側ブラスト装置1bが配設される。 As shown in FIG. 3, the entry-side blast device 1a and the exit-side blast device 1b are disposed between the entry-side facility 31a and the exit-side facility 31b. The entrance-side facility 1a and the exit-side facility 1b are connected to each other by a transfer conveyor 32 serving as a transfer line for the pipe P to be processed. An entrance blast device 1a is disposed on the entry side along the transfer conveyor, and an exit blast device 1b is disposed on the exit side.

入側ブラスト装置1aは、被処理管Pの一端Paから管内の空気を吸引する入側吸引装置7aと、研掃材と空気とを被処理管Pの他端Pbから密閉状態で管内へと旋回流として噴射する入側噴射装置3aとを備える。一方、出側ブラスト装置1bは、被処理管Pの他端Pbから管内の空気を吸引する出側吸引装置7bと、研掃材と空気とを被処理管Pの一端Paから密閉状態で管内へと旋回流として噴射する出側噴射装置3bとを備える。入側吸引装置7aと出側吸引装置7bは、前述した吸引装置7と同一の構成である。同様に、入側噴射装置3aと出側噴射装置3bは、前述した噴射装置3と同一の構成である。 The inlet-side blast device 1a includes an inlet-side suction device 7a that sucks air in the pipe from one end Pa of the pipe P to be processed, and a polishing material and air from the other end Pb of the pipe P to be sealed in the pipe. And an inlet-side injection device 3a that injects as a swirling flow. On the other hand, the outlet blast device 1b includes an outlet suction device 7b that sucks air in the pipe from the other end Pb of the pipe to be processed P, and a polishing material and air in a sealed state from one end Pa of the pipe to be processed P. And an exit-side injection device 3b that injects as a swirling flow. The inlet suction device 7a and the outlet suction device 7b have the same configuration as the suction device 7 described above. Similarly, the inlet side injection device 3a and the outlet side injection device 3b have the same configuration as the injection device 3 described above.

本実施の形態のシステム30によれば、被処理管Pは、移送コンベア32によって入側設備31aから入側ブラスト装置1aへと供給され、入側ブラスト装置1aで研掃処理を施される。その後、被処理管Pは、移送コンベア32によって出側ブラス装置1bへと移送され、出側ブラスト装置1bで再び研掃処理を施される。研掃処理を終えた被処理管Pは、移送コンベア32によって出側設備31bへと送り出される。 According to the system 30 of the present embodiment, the pipe to be processed P is supplied from the entrance side equipment 31a to the entrance side blast apparatus 1a by the transfer conveyor 32, and is subjected to a polishing process by the entrance side blast apparatus 1a. Thereafter, the pipe P to be processed is transferred to the delivery side blasting apparatus 1b by the transfer conveyor 32, and subjected to the blasting process again by the delivery side blasting apparatus 1b. The pipe P to be processed after the blasting process is sent out to the delivery facility 31b by the transfer conveyor 32.

入側ブラスト装置1aにおいては、入側吸引装置7aによって被処理管Pの一端Paから管内の空気が吸引されると共に、入側噴射装置3aによって被処理管Pの他端Pbから密閉状態で管内に研掃材と空気とが旋回流Aとして噴射される。これにより、研掃材と空気とを管内で被処理管Pの他端Pbから一端Paへ向けて流動させようとする強い力が被処理管Pの両端から同時に作用する。このため、被処理管Pの内径が小さく全長が長い場合等、負圧吸引作用のみによっては被処理管Pの全長に亘って研掃材の搬送作用を短時間で及ぼし難い場合であっても、被処理管Pの全長において研掃材が確実に搬送される。 In the inlet-side blast device 1a, air in the pipe is sucked from the one end Pa of the pipe to be processed P by the inlet-side suction apparatus 7a, and the inside of the pipe is sealed from the other end Pb of the pipe to be processed P by the inlet-side injection device 3a. The cleaning material and air are jetted as a swirl flow A. As a result, a strong force for causing the abrasive and air to flow in the pipe from the other end Pb of the pipe to be processed P toward the one end Pa is simultaneously applied from both ends of the pipe to be processed P. For this reason, even when the inner diameter of the pipe to be processed P is small and the total length is long, even if it is difficult to exert the conveying action of the scouring material over the entire length of the pipe to be processed P only by the negative pressure suction action. The polishing material is reliably conveyed over the entire length of the pipe P to be processed.

出側ブラスト装置1bにおいては、出側吸引装置7bによって被処理管Pの他端Pbから管内の空気が吸引されると共に、出側噴射装置3bによって被処理管Pの一端Paから密閉状態で管内に研掃材と空気とが旋回流Aとして噴射される。これにより、研掃材と空気とを管内で被処理管Pの一端Paから他端Pbへ向けて流動させようとする強い力が被処理管Pの両端から同時に作用する。このため、被処理管Pの内径が小さく全長が長い場合等、負圧吸引作用のみによっては被処理管Pの全長に亘って研掃材の搬送作用を短時間で及ぼし難い場合であっても、被処理管Pの全長において研掃材が確実に搬送される。 In the outlet blast device 1b, air in the pipe is sucked from the other end Pb of the pipe to be processed P by the outlet suction apparatus 7b, and the inside of the pipe is sealed from the one end Pa of the pipe to be processed P by the outlet jetting apparatus 3b. The cleaning material and air are jetted as a swirl flow A. As a result, a strong force for causing the abrasive and air to flow in the pipe from one end Pa to the other end Pb of the pipe to be processed P acts simultaneously from both ends of the pipe to be processed P. For this reason, even when the inner diameter of the pipe to be processed P is small and the total length is long, even if it is difficult to exert the conveying action of the scouring material over the entire length of the pipe to be processed P only by the negative pressure suction action. The polishing material is reliably conveyed over the entire length of the pipe P to be processed.

本実施の形態においては、一つの被処理管Pに対して、吸引と噴射の作用方向(研掃材の流動方向A)を逆にして研掃処理が二度施される。これにより、被処理管Pの両端間での、旋回流Aによる研掃処理の効果を均等化することが可能となる。加えて、入側ブラスト装置1aと出側ブラスト装置1bが被処理管Pの移送ライン32に沿う入側と出側とに配置されるので、二度の研掃処理を施すに当たって被処理管Pを反転させる必要がない。よって、作業が楽に行え、処理効率も良い。 In the present embodiment, the single pipe P is subjected to the blasting process twice by reversing the action directions of suction and jetting (the flow direction A of the scouring material). Thereby, it becomes possible to equalize the effect of the blasting process by the swirling flow A between both ends of the pipe P to be processed. In addition, since the inlet blast device 1a and the outlet blast device 1b are arranged on the inlet side and the outlet side along the transfer line 32 of the pipe to be processed P, the pipe to be processed P is subjected to the blasting process twice. There is no need to invert. Therefore, work can be performed easily and processing efficiency is good.

さらに、図3の例では、入側ブラスト装置1aが、被処理管Pの他端Pb側に位置し且つ管内に供給するための研掃材を貯留する入側サーバタンク4aと、被処理管Pの一端Pa側に位置し且つ被処理管P内を通過した研掃材を受け入れる入側レシーバタンク9aと、を備える。また、出側ブラスト装置1bが、被処理管Pの一端Pa側に位置し且つ被処理管P内に供給するための研掃材を貯留する出側サーバタンク4bと、被処理管Pの他端Pb側に位置し且つ被処理管P内を通過した研掃材を受け入れる出側レシーバタンク9bと、を備える。そして、入側レシーバタンク9a内の研掃材を出側サーバタンク4b内へと移送できるように、入側レシーバタンク9aと出側サーバタンク4bとが研掃材移送路33で連結される。同様に、出側レシーバタンク9b内の研掃材を入側サーバタンク4a内へと移送できるように出側レシーバタンク9bと入側サーバタンク4aとが研掃材移送路34で連結される。 Further, in the example of FIG. 3, the inlet blast device 1a is positioned on the other end Pb side of the pipe P to be processed, and stores the abrasive for feeding into the pipe, and the pipe to be processed. An inlet-side receiver tank 9a that is located on the one end Pa side of P and that receives the polishing material that has passed through the pipe P to be processed. In addition, the outlet blasting device 1b is located on the one end Pa side of the pipe to be processed P, and stores an outlet server tank 4b for storing a polishing material to be supplied into the pipe to be processed P. And a delivery-side receiver tank 9b that receives the scouring material that is located on the end Pb side and that has passed through the processing pipe P. The incoming receiver tank 9a and the outgoing server tank 4b are connected by the abrasive transfer path 33 so that the abrasive in the incoming receiver tank 9a can be transferred into the outgoing server tank 4b. Similarly, the outlet-side receiver tank 9b and the inlet-side server tank 4a are connected by a polishing material transfer path 34 so that the abrasive in the outlet-side receiver tank 9b can be transferred into the inlet-side server tank 4a.

この構成によれば、入側ブラスト装置1aで被処理管Pの内面の研掃を終えた研掃材が出側ブラスト装置1bに再投入され、同様に、出側ブラスト装置1bで被処理管Pの内面の研掃を終えた研掃材が入側ブラスト装置1aに再投入され、これが繰り返される。研掃材が繰り返し循環するように使用されるので、経済的である。 According to this configuration, the polishing material that has finished the inner surface of the processing pipe P by the inlet blast device 1a is reintroduced into the outlet blast device 1b, and similarly, the processing pipe is processed by the outlet blast device 1b. The polishing material that has finished the polishing of the inner surface of P is reintroduced into the entry-side blast device 1a, and this is repeated. Since the abrasive is used to circulate repeatedly, it is economical.

さらに、入側ブラスト装置1aを構成する入側レシーバタンク9aと出側ブラスト装置1bを構成する出側サーバタンク4bは、いずれも被処理管Pの一端Pa側にある。また、出側ブラスト装置1bを構成する出側レシーバタンク9bと入側ブラスト装置1aを構成する入側サーバタンク4aは、いずれも被処理管Pの他端Pb側にある。このため、入側レシーバタンク9aと出側サーバタンク4bとの間の研掃材移送路33と、出側レシーバタンク9bと入側サーバタンク4aとの間の研掃材移送路34とが、共に短くてすみ、研掃材移送路33,34の配設レイアウトも簡素にできる。よって、研掃材移送路33,34の配設コストが節約でき、一層経済的である。 Further, the incoming receiver tank 9a constituting the incoming blasting device 1a and the outgoing server tank 4b constituting the outgoing blasting device 1b are both on the one end Pa side of the processing pipe P. Further, the outlet receiver tank 9b constituting the outlet blasting device 1b and the inlet server tank 4a constituting the inlet blasting device 1a are both on the other end Pb side of the pipe P to be processed. For this reason, the scouring material transfer path 33 between the inlet-side receiver tank 9a and the outlet-side server tank 4b and the scouring material transfer path 34 between the outlet-side receiver tank 9b and the inlet-side server tank 4a are: Both can be short, and the arrangement layout of the abrasive transfer paths 33 and 34 can be simplified. Therefore, the arrangement cost of the scouring material transfer paths 33 and 34 can be saved, which is more economical.

1 管内面のブラスト装置
1a 入側ブラスト装置
1b 出側ブラスト装置
3 噴射装置
3a 入側噴射装置
3b 出側噴射装置
4 サーバタンク
4a 入側サーバタンク
4b 出側サーバタンク
5 混合部
6 圧送装置
7 吸引装置
7a 入側吸引装置
7b 出側吸引装置
9a 入側レシーバタンク
9b 出側レシーバタンク
18 レギュレータ
P 被処理管
P1 被処理管の下流端
P2 被処理管の上流端
Pa 被処理管の一端
Pb 被処理管の他端
DESCRIPTION OF SYMBOLS 1 Pipe blasting device 1a Inlet side blasting device 1b Outlet side blasting device 3 Injection device 3a Inlet side injection device 3b Outlet side injection device 4 Server tank 4a Inlet side server tank 4b Outlet side server tank 5 Mixing part 6 Pumping device 7 Suction Device 7a Inlet side suction device 7b Outlet side suction device 9a Inlet side receiver tank 9b Outlet side receiver tank 18 Regulator P Pipe to be treated P1 Downstream end of pipe to be treated P2 Upstream end of pipe to be treated Pa One end of pipe to be treated Pb The other end of the tube

Claims (7)

被処理管の下流端から管内の空気を吸引すると共に、研掃材と空気とを前記被処理管の上流端から密閉状態で管内に圧送することを特徴とする、管内面のブラスト方法。 A method for blasting an inner surface of a pipe, wherein air in the pipe is sucked from the downstream end of the pipe to be processed, and the abrasive and air are pumped into the pipe in a sealed state from the upstream end of the pipe to be processed. 直管である前記被処理管が、次の式において、P,γ,V(80m/s以上)に具体的数値を代入し、且つ、L,Dのいずれかに具体的数値を代入することによって得られるD以下又はL以上のサイズである、請求項1に記載の管内面のブラスト方法。
L/D=2P/(0.02×γ×V
L:被処理管の長さ m
D:被処理管の内径(直径) m
P:必要な圧力 Pa
γ:空気密度 kg/m
V:被処理管内の流速 m/s
The pipe to be treated that is a straight pipe substitutes a specific numerical value for P, γ, V (80 m / s or more) and substitutes a specific numerical value for either L or D in the following equation. The method for blasting a tube inner surface according to claim 1, wherein the blasting method is a size of not more than D or not less than L obtained by.
L / D = 2P / (0.02 × γ × V 2 )
L: Length of pipe to be processed m
D: Inner diameter (diameter) of the pipe to be processed
P: Required pressure Pa
γ: air density kg / m 3
V: Flow velocity in the pipe to be processed m / s
被処理管の下流端から管内の空気を吸引する吸引装置と、研掃材と空気とを前記被処理管の上流端から密閉状態で管内へと噴射する噴射装置と、を備える、管内面のブラスト装置。 A suction device that sucks air in the pipe from the downstream end of the pipe to be processed, and an injection device that jets the polishing material and air into the pipe in a sealed state from the upstream end of the pipe to be processed. Blasting device. 直管である前記被処理管のサイズが、次の式において、P,γ,V(80m/s以上)に具体的数値を代入し、且つ、L,Dのいずれかに具体的数値を代入することによって得られるD以下又はL以上のサイズである、請求項3に記載の管内面のブラスト装置。
L/D=2P/(0.02×γ×V
L:被処理管の長さ m
D:被処理管の内径(直径) m
P:必要な圧力 Pa
γ:空気密度 kg/m
V:被処理管内の流速 m/s
For the size of the pipe to be processed, which is a straight pipe, substitute specific numerical values for P, γ, V (80 m / s or more) and substitute specific numerical values for either L or D in the following formula. The blasting device for an inner surface of a pipe according to claim 3, wherein the blasting apparatus has a size of D or less or L or more obtained by performing the process.
L / D = 2P / (0.02 × γ × V 2 )
L: Length of pipe to be processed m
D: Inner diameter (diameter) of the pipe to be processed
P: Required pressure Pa
γ: air density kg / m 3
V: Flow velocity in the pipe to be processed m / s
前記噴射装置は、前記研掃材と前記空気とを前記被処理管の上流端よりも上流側で混合させる混合部と、前記研掃材を貯留すると共に前記混合部へと研掃材を供給する密閉式のサーバタンクと、前記混合部内及び前記サーバタンク内へと空気を圧送する圧送装置と、前記混合部の内圧と等しいかそれ以上となるように前記サーバタンクの内圧を制御するレギュレータと、を備える、請求項3又は4に記載の管内面のブラスト装置。 The spraying device mixes the scouring material and the air upstream of the upstream end of the pipe to be processed, stores the scouring material, and supplies the scouring material to the mixing unit. A sealed server tank, a pumping device for pumping air into the mixing unit and the server tank, and a regulator for controlling the internal pressure of the server tank so as to be equal to or higher than the internal pressure of the mixing unit A blasting device for a pipe inner surface according to claim 3 or 4. 被処理管の移送ラインに沿う入側と出側とにそれぞれブラスト装置が配設され、前記入側ブラスト装置は、前記被処理管の一端から管内の空気を吸引する入側吸引装置と、研掃材と空気とを前記被処理管の他端から密閉状態で管内へと旋回流として噴射する入側噴射装置と、を備え、前記出側ブラスト装置は、前記被処理管の前記他端から管内の空気を吸引する出側吸引装置と、研掃材と空気とを前記被処理管の前記一端から密閉状態で管内へと旋回流として噴射する出側噴射装置と、を備える、管内面ブラストシステム。 A blasting device is provided on each of the inlet side and the outlet side along the transfer line of the pipe to be processed. The inlet blasting apparatus includes an inlet side suction device that sucks air in the pipe from one end of the pipe to be processed, and a grinding device. An inlet-side injection device that injects scavenging material and air as a swirling flow into the tube in a sealed state from the other end of the tube to be processed, and the outlet blast device is connected to the other end of the tube to be processed. A pipe inner surface blasting device comprising: an outlet side suction device that sucks air in the pipe; and an outlet side injection device that jets the abrasive and air as a swirling flow into the pipe in a sealed state from the one end of the treated pipe. system. 前記入側ブラスト装置が、前記被処理管の前記他端側に位置し且つ前記被処理管内に供給するための研掃材を貯留する入側サーバタンクと、前記被処理管の前記一端側に位置し且つ前記被処理管内を通過した研掃材を受け入れる入側レシーバタンクと、を備え、前記出側ブラスト装置が、前記被処理管の前記一端側に位置し且つ前記被処理管内に供給するための研掃材を貯留する出側サーバタンクと、前記被処理管の前記他端側に位置し且つ前記被処理管内を通過した研掃材を受け入れる出側レシーバタンクと、を備え、前記入側レシーバタンク内の研掃材を前記出側サーバタンク内へと移送できるように前記入側レシーバタンクと前記出側サーバタンクとが連結され、前記出側レシーバタンク内の研掃材を前記入側サーバタンク内へと移送できるように前記出側レシーバタンクと前記入側サーバタンクとが連結される、請求項6に記載の管内面ブラストシステム。 The entry side blasting device is located on the other end side of the pipe to be treated and stores an inlet side server tank for storing an abrasive to be supplied into the pipe to be treated, and on the one end side of the pipe to be treated. An inlet-side receiver tank that receives the polishing material that is positioned and passes through the processing pipe, and the outlet-side blasting device is positioned on the one end side of the processing pipe and is supplied into the processing pipe An exit side server tank for storing the abrasive for cleaning, and an exit side receiver tank that is located on the other end side of the pipe to be processed and that receives the abrasive that has passed through the pipe to be processed. The inlet receiver tank and the outlet server tank are connected so that the abrasive in the receiver receiver tank can be transferred into the outlet server tank, and the abrasive in the outlet receiver tank is inserted into the inlet receiver tank. Transfer to the server tank And the exit-side receiver tank and entering-side server tank is connected to hang, inner surface blasting system according to claim 6.
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