JPH01293160A - Device for continuously injecting lining resin - Google Patents

Device for continuously injecting lining resin

Info

Publication number
JPH01293160A
JPH01293160A JP12278488A JP12278488A JPH01293160A JP H01293160 A JPH01293160 A JP H01293160A JP 12278488 A JP12278488 A JP 12278488A JP 12278488 A JP12278488 A JP 12278488A JP H01293160 A JPH01293160 A JP H01293160A
Authority
JP
Japan
Prior art keywords
resin
lining
pipe
launcher
valve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP12278488A
Other languages
Japanese (ja)
Other versions
JP2598303B2 (en
Inventor
Motoyuki Koga
基之 古賀
Nobukatsu Ike
宣勝 池
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hakko Co Ltd
Original Assignee
Hakko Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hakko Co Ltd filed Critical Hakko Co Ltd
Priority to JP12278488A priority Critical patent/JP2598303B2/en
Publication of JPH01293160A publication Critical patent/JPH01293160A/en
Application granted granted Critical
Publication of JP2598303B2 publication Critical patent/JP2598303B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Coating Apparatus (AREA)

Abstract

PURPOSE:To reduce the lining time by connecting one end of a charging cylinder to a low-pressure gas feeder through a stop valve, and connecting the other end to a supply launcher through a stop valve. CONSTITUTION:The supply launcher is connected to an existing pipeline A, and a lining starting command is given to a control unit 23. The gas compressed by a compressor 12 is sent by the control unit 23 to a resin tank 1 through a pipeline 17 to actuate a plunger 2, and hence the lining resin is packed in the charging cylinder 6 to constitute a resin body. When a specified amt. of resin is packed, a stop valve 4 is closed, and a stop valve 8 is opened. Consequently, the compressed air in an air tank 13 is introduced into the charging cylinder 6 through a flow control valve 14 and sent into the pipeline A through the launcher 11, and the inner surface of the pipe is lined.

Description

【発明の詳細な説明】[Detailed description of the invention] 【産業上の利用分野】[Industrial application field]

本発明は、地下に布設されたガス管、水道管などの既設
管に対し、その管内面に、布設状態のままで均一な樹脂
ライニングを施す管内面のライニング′FIAI@にお
いて、上記既設管への樹脂供給のための、ライニング用
樹脂の連続注入装置に関するものである。
The present invention applies a uniform resin lining to the inner surface of existing pipes such as gas pipes and water pipes installed underground in the pipe inner surface lining 'FIAI@', which applies a uniform resin lining to the inner surface of the existing pipes such as gas pipes and water pipes installed underground. This invention relates to a continuous injection device for lining resin for supplying resin.

【従来の技術】[Conventional technology]

一般に、ガス管、水道管などの地下に布設されている既
設配管は、経年によって、管にWJ蝕孔や継手部の弛み
が生じて、漏洩が起るおそれがあることから、その漏洩
予防、保全のため、施工後、所要の時期に、上記既設配
管に対し、その布設状態のまま管内面に対する@脂うイ
ニングによる補修が行なわれている。 そこで、特開昭63−65983号公報所載のように、
既設配管の一端側の管内に、管路内を充満閉塞するよう
に液状の樹脂団を充填し、上記樹脂団を所定の低圧気体
で流動させ、管内面に所要の膜厚のライニングを行なう
管内面のライニング補修工法が提唱された。ここでは、
開放された既設配管の一端にランチャを接続し、上記ラ
ンチャに接続された樹脂タンクからライニング用の樹脂
を充填してランチャ内に樹脂団を形成し、これをランチ
ャの自由端側から供給した低圧気体で既設管内へ供給し
ている。そして、既設管内で樹脂団が流動して、管内面
のライニングに樹脂が消費されると、再び樹脂タンクか
らランチャ内に樹脂を充填し、ランチャ内に樹脂団を形
成し、再び低圧気体で既設管内へ供給する。このような
作業を繰返して、所定長さについて、上記既設管の管内
面補修を行なうのである。
In general, with existing pipes such as gas pipes and water pipes installed underground, there is a risk of leakage due to the occurrence of WJ corrosion holes and loosening of joints over time. For maintenance purposes, the existing pipes are repaired by greasing the inner surface of the pipes at a required time after construction, while the pipes are still in their installed state. Therefore, as published in Japanese Patent Application Laid-open No. 63-65983,
The inside of the pipe at one end of the existing pipe is filled with a liquid resin group so as to fill and block the inside of the pipe, and the resin group is made to flow with a predetermined low-pressure gas to line the inner surface of the pipe with the required film thickness. A surface lining repair method was proposed. here,
A launcher is connected to one end of the opened existing piping, and a resin for lining is filled from a resin tank connected to the launcher to form a resin mass inside the launcher, which is then supplied from the free end of the launcher under low pressure. Gas is supplied into the existing pipes. When the resin mass flows inside the existing pipe and is consumed by the lining on the inner surface of the pipe, the launcher is filled with resin again from the resin tank, a resin mass is formed inside the launcher, and low-pressure gas is again applied to the existing pipe. Supply into the pipe. By repeating such operations, the inner surface of the existing pipe is repaired for a predetermined length.

【発明が解決しようとする課題】[Problem to be solved by the invention]

このような管内面のライニング補修工法では、ランチャ
に対して樹脂タンクより樹脂を充填している時間は、樹
脂ライニング作業が実質的に中断されることになり、時
間無駄を生じる。 そこで、本発明は、ランチャへの樹脂供給待ちをせずに
既設配管への樹脂団の供給が行なえるライニング用樹脂
の連続注入装置を提供しようとするものである。
In such a pipe inner lining repair method, the resin lining work is substantially interrupted during the time the launcher is being filled with resin from the resin tank, resulting in wasted time. SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a continuous injection device for lining resin that can supply a resin mass to an existing pipe without waiting for the resin to be supplied to the launcher.

【課題を解決するための手段】 このため、本発明では、樹脂タンクの出口通路を2つに
分岐してそれぞれ、開閉バルブを介して各別の充填筒に
連通ずると共に、上記充填筒の一端をそれぞれ開閉バル
ブを介して低圧気体供給装置に連通し、かつ上記充填筒
の他端をそれぞれ開閉バルブを介して供給ランチャに連
通してなり、一方の充填筒に樹脂タンクよりライニング
用の樹脂を充填している間に、他方の充填筒を上記低圧
気f41′供給装置および上記ランチャに連通して、充
填筒内の樹脂団を上記ランチャを介して既設配管内に送
り、管内面の樹脂ライニングを行なうように上記開閉バ
ルブの切換制御を行なう構成にしている。
[Means for Solving the Problems] Therefore, in the present invention, the outlet passage of the resin tank is branched into two, each of which is communicated with a separate filling cylinder via an on-off valve, and one end of the filling cylinder is are connected to a low-pressure gas supply device through on-off valves, and the other ends of the filling cylinders are connected to a supply launcher through on-off valves, respectively, and one filling cylinder is filled with resin for lining from a resin tank. During filling, the other filling cylinder is communicated with the low-pressure air f41' supply device and the launcher, and the resin mass in the filling cylinder is sent into the existing piping via the launcher, and the resin lining on the inner surface of the pipe is The switching control of the opening/closing valve is performed so as to perform the following.

【作   用】[For production]

したがって、一方の充填筒の樹脂団が供給ランチャを通
って既設配管中に所定低圧気体で送られて、管内面の樹
脂ライニングに供せられている過程で、他方の充填筒に
樹脂タンクからライニング用樹脂が充填されて樹脂団を
形成しているから、管内面のライニングに樹脂が消費つ
くされると、直ちに開閉バルブの切換えで、充填されて
いる方の充填筒へ低圧気体が供給され、ランチャを介し
てIeta配管中にライニング用樹脂を送り込むことが
でき、そのまま管内面のライニング作業に入る。 このため、ランチャへの樹脂充填に要する従来の無駄時
間が省かれ、可使時間を有効にライニング作業のために
活用できることになる。
Therefore, while the resin mass in one filling cylinder is being sent with predetermined low pressure gas into the existing piping through the supply launcher and being applied to the resin lining on the inner surface of the pipe, the other filling cylinder is being lined from the resin tank. Since the resin is filled to form a resin mass, as soon as the resin is consumed in the inner lining of the tube, low pressure gas is supplied to the filled cylinder by switching the on-off valve. The lining resin can be fed into the Ieta pipe through the launcher, and the work of lining the inner surface of the pipe can begin. Therefore, the conventional wasted time required for filling the launcher with resin is eliminated, and the usable time can be effectively utilized for lining work.

【実 施 例】【Example】

以下、本発明の一実施例を、図面を参照して具体的に説
明する。 図において、符号1は樹脂タンクであり、プランジャ2
を内装した円筒状をなしている。そして、上記タンク1
内には、ライニング用の液状樹脂が収容されており、2
つに分岐された出口通[i3を介して開閉バルブ4,5
に連通している。 上記ライニング用の樹脂は、例えば主剤と硬化剤とを調
合した常温2液硬化型の樹脂であり、このうち主剤は不
飽和ポリエステル樹脂、ビニルエステル樹脂、エポキシ
樹脂、ウレタン樹脂などを主成分とした組成物であり、
これに顔t1、揺変剤などを添加してチクソトロピー性
を有している(例えば300.0OOcpsでTIIO
2゜上記開閉バルブ4,5はそれぞれ、円筒状の充填筒
6,7の基端側−側において連通しており、上記充填筒
6,7の基端は開閉バルブ8,9を介して低圧気体供給
袋″j!lioに連通しており、また、その先端は7字
形に構成される供給ランチャ11にゲート式の開閉バル
ブ8a、 9aを介して連通されている。 上記低圧気体供給装置10はコンプレッサ12.エアタ
ンク13.流量調整バルブ14.15を具備しており、
また、コンプレッサ12の出力側に設けた三方切換弁1
6を介して上記樹脂タンク1に連通ずる管路17を具備
しており、更に、上記管路17には流量調整バルブ18
が設けである。また、上記低圧気体供給装置には、流量
計19.20および圧力計21.22が設けてあり、そ
の検出信号はコントロールユニット23に供給されるよ
うになっている。 また、上記コントロールユニット23は上記流量計19
.20.圧力計21.22の出力情報および制御ブログ
ラムに従って演算を行って、上記流量調整バルブ14.
15.18.更には開閉バルブ4,5,8゜9 、8a
、 9aの制御を行うようになっている。 そして、本発明の装置を用いてライニング補修を行なう
に際しては、支管あるいは本管(洪内管についても適用
できる)などの既設配管Aについて、所定長さの補修区
間に区切って、その両端を開放するため、対応する個所
に、第2図に示すような立坑B、Cを形成し、そこで既
設配管Aの端を、フランジの取外しあるいは切断で開放
する。 更に、この既設配管Aに連なる洪内管りについては、メ
ータ類を取外し、池上端を開口する。そして、上記支管
Aおよび洪内管りに圧力空気を通して、内部の塵埃など
の除去を行なうのである。 次いで、例えば供内管りを予め樹脂ライニングしく以下
に述べる既設配管への樹脂ライニング工法をそのまま適
用することができる)、その後、既設配管Aの樹脂ライ
ニングに備えて適当な樹脂侵入防止策を楕じておく。 しかして、供給ランチャ11をIet設配管Aに接続し
、コン1−ロールユニット23にライニング作業開始指
令をスイッチング操作などで与える。上記コントロール
ユニット23は初期段階では先づ1方の開閉バルブ4お
よび8aを開放して、流量調整バルブ18の開度を調整
し、三方切換弁16を切換えて、コンプレッサ12の市
きで生成された加圧気体(例えば圧力空気)を管路17
を介して樹脂タンク1に送り、プランジャ2を動作して
、ライニング用の樹脂を充填筒6内に充填し、この中に
樹脂団を構成する。時間および流Jl調整バルブの調整
値からmxされる所要の充填量になると、コントロール
ユニツI・23は、開閉バルブ4を閉じ、開閉バルブ8
を開放する。これによってエアタンク13に溜められた
加圧気体(例えば圧力空気)が流量調整バルブ14を経
由して充填筒6に流れ、充填筒G内の樹脂団を押して、
ランチャ11を経由して既設配管A内に送り、ここで樹
脂の流動速度に対応しな膜厚で管内面へのライニングを
実施することになる。 この時、開閉バルブ8aは開放されており、開閉バルブ
5 、9 、9aは閉じられている。樹脂団がランチャ
11を通過した段階で、開閉バルブ5および9aが開放
され、樹脂タンク1の樹脂は、管路17を介して与えら
れる圧力空気で充填筒7内に充填される。充填が完了す
ると、開閉バルブ5および9aは閉じられ、三方切換弁
16が切換えられてコンプレッサ12の加圧気体(例え
ば加圧空気)はエアタンク13に供給される。 このように充填fm71111への樹脂充填中およびそ
の後において、上記充填筒6を経由しての低圧気体(例
えば低圧空気)の供給制御は上記コントロールユニット
23で実現される。この場合、上記コントロールユニッ
ト23での演算基礎は下記の算式に依存している。 まず、既設配管A(直径D)に流入した低圧気体の量Q
1 、圧力P1 (例えば0.8kq/cn+1)とす
れば π/4・D2 ・λ1 ・P1=Q1 ・po・・・(
1)の関係にあるので、低圧気体による樹脂団の送り開
始の時刻T1におけるQl、po、plを測定すれば、
(1)式よりλ1を知ることができる。なお、ここで、
既設配管Aに流入した気体の量Q1とは、流量計19.
20の各計1111J値F1およびF2の差で得られる
。この場合、上記流量計19.20に質量流量計を使用
すると、気体の温度の影響がないので、演算し易い。ま
た、ここで11は時刻T1におけ ′る樹脂団の位置、
Po、Plは圧力計21.22の計測値、Dは上記既設
配管Aのライニング内径である。 同様にして、時刻T2における圧力P2および流入量Q
2を計測し、演算して得られる樹脂団の位置をfl、2
とすれば、樹脂団の流動遠度■は、■=Δλ/Δtとな
る。 但し、Δ2=12−21 Δt =72−’r1 とする。 したがって、所定時間間隔Δtをコントロールユニット
23内の発振器のクロックで設定し、その都度、流量計
19.20から管内に流入した流入気体量と圧力計21
.22からそれぞれの圧力を計測し、各瞬時の樹脂流動
速度■が一定の所定値に保持されるように、流量調整バ
ルブ14.15を制御するのである。 既設配管A内では、樹脂団の長さは管内面へのライニン
グに消費されるために減少するが、流動速度が一定であ
るので、押圧気体の圧力は略直線的に降下する(第3図
参照)。 樹脂団の樹脂が消費される過程で、樹脂団長は漸次、短
かくなると同時に、樹脂流動速筬を一定に保持するため
の押圧気体の圧力も略直線的に低くなり、樹脂団長が0
になれば、当然押圧気体の圧力も大気圧となる。 既設配管A内の樹脂ライニングが完了しないうちに樹脂
団が消費されるか、上記樹脂団が上記既設配管Aの他端
のレシーバ24内に導出されレシーバタンク25に受は
入れられると、低圧気体は管内を吹き抜けて、圧力の急
激な低下が起る。この時点でコントロールユニット23
は、樹脂ライニングが完了した位置までの長さ夕、その
時の気体の址Q、経過時間toなどをメモリに記憶し、
開閉バルブ8を閉じる。次に、開閉バルブ9および9a
を開放して、充填筒7に充填されている樹脂団を低圧気
体でランチャ11を経由して既設配管A内に送る。そし
、て、再び開閉バルブ4を開いて、三方切換弁16の切
換えで、コンプレッサ12の加圧空気を管路17を介し
て樹脂タンク1に与え、樹脂を充填間6に充填する。充
填が終れば、開閉バルブ4を閉じ、三方切換弁16を切
換えてコンプレッサ12の加圧空気をエアタンク13に
与える。そして、コントロールユニット23は演算の結
果にもとづいて、充填1!J7内の樹脂団のランチャ1
1を介して既設配管A内に送り込むが、このとき、ライ
ニング樹脂団が前回ライニングされた既設配管Aの中を
所定の速度Vで移動する間は管内のライニングのM厚は
変化なく、したがって、樹脂団の長さら減少することな
く、押圧気体の圧力も略一定値に保持される。 しかして、樹脂団が管Aの末だライニングされていない
位置に到達した後は、ライニングにより樹脂が消費され
、樹脂団の長さが減少し、したがって、押圧気体の圧力
も漸次低下しなからライニングが進行することは前述と
同様である。この場合、樹脂団長が略Oになり、押圧気
体の圧力が再び大気圧になるが、このときまでの経過時
間は略2toとなり、まなライニングの終了位置までの
長さも略2Lとなる。 このようにして、樹脂の充填と押圧によるライニングを
繰返しながら逐次ライニング長を延長してゆく。 既設配管Aのライニングが終了し、樹脂団の長さがまだ
残ったまま開放端に到達すると、樹脂団はレシーバ24
内に流入し、管A内α樹脂団の流動抵抗は急激に減少す
るので、コントロールユニット23で制御される押圧力
も急激に減少して大気圧になる。また押圧力が大気圧に
低下するまでの経過時間も、予定された(nXt)より
も短い(n−Bt、+t′ (但しt’<t)になる(
第3図参照)。 即ち、押圧力の急激な低下と経過時間と予測経過時間の
差から、樹脂団がレシーバ24内に到達しなと判定して
該当のlL?Q配管Aについてのライニング補修を終了
する。
Hereinafter, one embodiment of the present invention will be specifically described with reference to the drawings. In the figure, numeral 1 is a resin tank, and plunger 2
It has a cylindrical shape with an interior. And the above tank 1
A liquid resin for lining is stored inside, and 2
The outlet passage is branched into two opening/closing valves 4 and 5 via i3.
is connected to. The above-mentioned resin for lining is, for example, a two-component curing resin at room temperature, which is a mixture of a base resin and a hardening agent, of which the base resin is mainly composed of unsaturated polyester resin, vinyl ester resin, epoxy resin, urethane resin, etc. a composition,
It has thixotropic properties by adding face t1, thixotropic agent, etc. (for example, TIIO at 300.0OOcps).
2゜The on-off valves 4 and 5 communicate with the cylindrical filling cylinders 6 and 7 at their proximal end sides, respectively, and the proximal ends of the filling cylinders 6 and 7 are connected to low pressure via the on-off valves 8 and 9. It communicates with a gas supply bag "j!lio," and its tip communicates with a supply launcher 11 configured in a figure 7 shape via gate-type on-off valves 8a and 9a. The low-pressure gas supply device 10 is equipped with a compressor 12, an air tank 13, a flow rate adjustment valve 14, and 15.
In addition, a three-way switching valve 1 provided on the output side of the compressor 12
6 is provided with a pipe line 17 that communicates with the resin tank 1, and the pipe line 17 is further provided with a flow rate adjustment valve 18.
is the provision. Further, the low pressure gas supply device is provided with a flow meter 19.20 and a pressure gauge 21.22, the detection signals of which are supplied to the control unit 23. The control unit 23 also includes the flow meter 19.
.. 20. Calculations are performed according to the output information of the pressure gauges 21 and 22 and the control program, and the flow rate adjustment valve 14.
15.18. Furthermore, on-off valves 4, 5, 8°9, 8a
, 9a. When performing lining repair using the device of the present invention, the existing pipe A, such as a branch pipe or main pipe (applicable to the Hongnae pipe), is divided into repair sections of a predetermined length, and both ends are opened. In order to do this, vertical shafts B and C as shown in FIG. 2 are formed at corresponding locations, and the end of the existing pipe A is opened there by removing or cutting the flange. Furthermore, meters will be removed from the inner pipe connected to the existing pipe A, and the upper end of the pipe will be opened. Then, pressurized air is passed through the branch pipe A and the inner pipe to remove dust and the like inside. Next, for example, the in-service pipes may be lined with resin in advance and the resin lining method described below for existing pipes can be applied as is), and then appropriate measures to prevent resin intrusion are taken in preparation for resin lining of existing pipe A. Keep it. Then, the supply launcher 11 is connected to the Iet installation pipe A, and a lining work start command is given to the controller 1-roll unit 23 by a switching operation or the like. In the initial stage, the control unit 23 first opens one of the opening/closing valves 4 and 8a, adjusts the opening degree of the flow rate adjustment valve 18, and switches the three-way switching valve 16 so that the output of the compressor 12 is reduced. The pressurized gas (for example, pressurized air) is passed through the pipe 17.
The resin for lining is sent to the resin tank 1 through the cylinder 1, and the plunger 2 is operated to fill the filling cylinder 6 with resin for lining, thereby forming a resin mass therein. When the required filling amount mx is reached based on the adjustment value of the time and flow Jl adjustment valve, the control unit I.23 closes the on-off valve 4 and closes the on-off valve 8.
to open. As a result, the pressurized gas (for example, pressurized air) stored in the air tank 13 flows into the filling cylinder 6 via the flow rate adjustment valve 14, pushing the resin group inside the filling cylinder G,
The resin is sent into the existing pipe A via the launcher 11, where the inner surface of the pipe is lined with a film thickness that does not correspond to the flow rate of the resin. At this time, the on-off valve 8a is open, and the on-off valves 5, 9, and 9a are closed. At the stage where the resin mass passes through the launcher 11, the on-off valves 5 and 9a are opened, and the resin in the resin tank 1 is filled into the filling cylinder 7 with pressurized air applied via the pipe line 17. When filling is completed, the on-off valves 5 and 9a are closed, the three-way switching valve 16 is switched, and the pressurized gas (for example, pressurized air) from the compressor 12 is supplied to the air tank 13. In this way, during and after filling the filling fm71111 with resin, the supply control of low pressure gas (for example, low pressure air) via the filling cylinder 6 is realized by the control unit 23. In this case, the calculation basis in the control unit 23 depends on the following formula. First, the amount Q of low-pressure gas that has flowed into the existing pipe A (diameter D)
1, pressure P1 (for example, 0.8 kq/cn+1), then π/4・D2 ・λ1 ・P1=Q1 ・po...(
Since the relationship is as shown in 1), if Ql, po, and pl are measured at time T1 when the resin group starts to be fed by low-pressure gas, then
λ1 can be found from equation (1). Furthermore, here,
The amount Q1 of gas flowing into the existing pipe A is determined by the flowmeter 19.
20, each with a total of 1111J obtained by the difference between the values F1 and F2. In this case, if a mass flow meter is used as the flow meter 19, 20, the calculation will be easier because there will be no influence of gas temperature. In addition, here 11 is the position of the resin group at time T1,
Po and Pl are the measured values of the pressure gauges 21 and 22, and D is the inner diameter of the lining of the existing pipe A. Similarly, pressure P2 and inflow amount Q at time T2
The position of the resin group obtained by measuring and calculating 2 is fl, 2
Then, the flow distance (■) of the resin group becomes ■=Δλ/Δt. However, it is assumed that Δ2=12-21 Δt=72-'r1. Therefore, the predetermined time interval Δt is set by the clock of the oscillator in the control unit 23, and each time the amount of inflow gas flowing into the pipe from the flowmeter 19, 20 and the pressure gauge 21 are measured.
.. The respective pressures are measured from 22, and the flow rate regulating valves 14 and 15 are controlled so that each instantaneous resin flow rate (2) is maintained at a constant predetermined value. In the existing pipe A, the length of the resin aggregate decreases because it is consumed in lining the inner surface of the pipe, but since the flow rate is constant, the pressure of the pressurized gas decreases approximately linearly (Fig. 3). reference). In the process of consuming the resin in the resin group, the resin group length gradually becomes shorter, and at the same time, the pressure of the pressurizing gas for keeping the resin flow rate constant decreases almost linearly, until the resin group length reaches 0.
, the pressure of the pressurized gas naturally becomes atmospheric pressure. If the resin mass is consumed before the resin lining in the existing pipe A is completed, or if the resin mass is led out into the receiver 24 at the other end of the existing pipe A and received in the receiver tank 25, low-pressure gas blows through the pipe, causing a sudden drop in pressure. At this point, the control unit 23
stores in memory the length to the position where the resin lining is completed, the amount of gas at that time Q, the elapsed time to, etc.
Close the on-off valve 8. Next, open/close valves 9 and 9a
is opened, and the resin mass filled in the filling cylinder 7 is sent into the existing pipe A via the launcher 11 with low pressure gas. Then, the on-off valve 4 is opened again, and the three-way switching valve 16 is switched to supply pressurized air from the compressor 12 to the resin tank 1 via the pipe line 17, filling the filling gap 6 with resin. When filling is completed, the on-off valve 4 is closed and the three-way switching valve 16 is switched to supply pressurized air from the compressor 12 to the air tank 13. Based on the result of the calculation, the control unit 23 determines whether filling 1! Launcher 1 of the resin group in J7
1 into the existing pipe A, but at this time, while the lining resin mass moves at a predetermined speed V inside the previously lined existing pipe A, the thickness M of the lining inside the pipe does not change, therefore, The length of the resin group does not decrease further, and the pressure of the pressing gas is also maintained at a substantially constant value. After the resin mass reaches the unlined position at the end of the pipe A, the resin is consumed by the lining, the length of the resin mass decreases, and the pressure of the pressurized gas gradually decreases. The progress of lining is the same as described above. In this case, the resin aggregate becomes approximately O, and the pressure of the pressurized gas becomes atmospheric pressure again, but the elapsed time up to this point is approximately 2to, and the length to the end position of the manifold lining is also approximately 2L. In this way, the lining length is successively extended by repeating filling with resin and lining by pressing. When the lining of the existing pipe A is completed and the resin block reaches the open end with the length still remaining, the resin block passes through the receiver 24.
As the flow resistance of the α-resin group inside the pipe A rapidly decreases, the pressing force controlled by the control unit 23 also rapidly decreases to atmospheric pressure. Also, the elapsed time until the pressing force decreases to atmospheric pressure is shorter than the expected (nXt) (n-Bt, +t' (however, t'<t) (
(See Figure 3). That is, based on the sudden decrease in the pressing force and the difference between the elapsed time and the predicted elapsed time, it is determined that the resin group has not reached the receiver 24, and the corresponding lL? Finish the lining repair for Q pipe A.

【発明の効果】【Effect of the invention】

本発明は、以上詳述したようになり、一方の充填筒の樹
脂団が供給ランチャを通って既設配管中に低圧気体で送
られライニングを実施している過程で、他方の充填筒に
樹脂が充填されるから、こ ′の充填間の樹脂団を交互
に既設配管中へ送るなめ、ランチャへの樹脂充填に要す
る従来の無駄時間か省かれ、可使時間を有効にライニン
グ作業のために活用できる。
The present invention has been described in detail above, and during the process in which the resin mass in one filling cylinder is sent by low-pressure gas into the existing piping through the supply launcher and lining the other filling cylinder, the resin is transferred to the other filling cylinder. Since the resin is filled, the resin mass is alternately sent into the existing piping between fillings, which eliminates the conventional wasted time required to fill the launcher with resin, and allows the pot life to be effectively utilized for lining work. can.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例を示すi略構成図、第2図は
既設配管のライニング補修の状況を示す概略構成図、第
3図は樹脂ライニングの繰返し状況を示すタイムチャー
トである。 1・・・樹脂タンク、2・・・プランジャ、3・・・出
口通路、4 、5 、8 、8a、 9 、9a=−・
開閉バルブ、10−・・低圧気体供給装置。
FIG. 1 is a schematic block diagram showing an embodiment of the present invention, FIG. 2 is a schematic block diagram showing the state of lining repair of existing piping, and FIG. 3 is a time chart showing the state of repeating resin lining. DESCRIPTION OF SYMBOLS 1...Resin tank, 2...Plunger, 3...Outlet passage, 4, 5, 8, 8a, 9, 9a=--
Opening/closing valve, 10-...Low pressure gas supply device.

Claims (1)

【特許請求の範囲】[Claims] 樹脂タンクの出口通路を2つに分岐してそれぞれ、開閉
バルブを介して各別の充填筒に連通すると共に、上記充
填筒の一端をそれぞれ開閉バルブを介して低圧気体供給
装置に連通し、かつ上記充填筒の他端をそれぞれ開閉バ
ルブを介して供給ランチャに連通してなり、一方の充填
筒に樹脂タンクよりライニング用の樹脂を充填している
間に、他方の充填筒を上記低圧気体供給装置および上記
ランチャに連通して、充填筒内の樹脂団を上記ランチャ
を介して既設配管内に送り、管内面の樹脂ライニングを
行なうように上記開閉バルブの切換制御を行なう構成に
したことを特徴とするライニング用樹脂の連続注入装置
The outlet passage of the resin tank is branched into two, each of which communicates with a separate filling cylinder via an on-off valve, and one end of the filling cylinder is communicated with a low-pressure gas supply device via an on-off valve, and The other end of the filling cylinder is connected to the supply launcher via an on-off valve, and while one filling cylinder is being filled with lining resin from the resin tank, the other filling cylinder is supplied with the low pressure gas. It is characterized by being configured to be in communication with the apparatus and the launcher, and to control switching of the opening/closing valve so as to send the resin mass in the filling cylinder into the existing pipe through the launcher and to perform resin lining of the inner surface of the pipe. Continuous injection equipment for lining resin
JP12278488A 1988-05-18 1988-05-18 Continuous injection system for lining resin Expired - Lifetime JP2598303B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12278488A JP2598303B2 (en) 1988-05-18 1988-05-18 Continuous injection system for lining resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12278488A JP2598303B2 (en) 1988-05-18 1988-05-18 Continuous injection system for lining resin

Publications (2)

Publication Number Publication Date
JPH01293160A true JPH01293160A (en) 1989-11-27
JP2598303B2 JP2598303B2 (en) 1997-04-09

Family

ID=14844526

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12278488A Expired - Lifetime JP2598303B2 (en) 1988-05-18 1988-05-18 Continuous injection system for lining resin

Country Status (1)

Country Link
JP (1) JP2598303B2 (en)

Also Published As

Publication number Publication date
JP2598303B2 (en) 1997-04-09

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