JP2719599B2 - How to clean piping - Google Patents

How to clean piping

Info

Publication number
JP2719599B2
JP2719599B2 JP63038882A JP3888288A JP2719599B2 JP 2719599 B2 JP2719599 B2 JP 2719599B2 JP 63038882 A JP63038882 A JP 63038882A JP 3888288 A JP3888288 A JP 3888288A JP 2719599 B2 JP2719599 B2 JP 2719599B2
Authority
JP
Japan
Prior art keywords
aqueous solution
treatment
acid
pipe
washing
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.)
Expired - Lifetime
Application number
JP63038882A
Other languages
Japanese (ja)
Other versions
JPH01212786A (en
Inventor
幹彦 関口
久良 松岡
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.)
Neos Co Ltd
Original Assignee
Neos 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 Neos Co Ltd filed Critical Neos Co Ltd
Priority to JP63038882A priority Critical patent/JP2719599B2/en
Publication of JPH01212786A publication Critical patent/JPH01212786A/en
Application granted granted Critical
Publication of JP2719599B2 publication Critical patent/JP2719599B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions
    • C23G1/08Iron or steel
    • C23G1/088Iron or steel solutions containing organic acids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Cleaning In General (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は配管の改良された洗浄方法に関する。Description: FIELD OF THE INVENTION The present invention relates to an improved method of cleaning piping.

本明細書において使用する「配管」という用語は、各
種の油圧機器類の配管、化学プラントにおけるパイプラ
イン、各種の熱交換器や汽缶類、各種のタワーやタンク
類およびこれらに付属する各種のパイプ類等を総称す
る。
As used herein, the term “piping” refers to various hydraulic equipment piping, chemical plant pipelines, various heat exchangers and steam cans, various towers and tanks, and various pipes attached thereto. Generic name.

従来の技術 従来から配管の内部に経時的に生成するスケールや錆
等を除去する方法としては次の洗浄方法が一般的に採用
されている。
2. Description of the Related Art Conventionally, the following cleaning method has been generally adopted as a method for removing scale, rust, and the like generated over time in a pipe.

即ち、被処理配管の内部を塩酸やリン酸等の酸水溶液
を用いて洗浄し、空気や窒素ガス等を用いてブロー処理
をおこない、水洗後、さらにブロー処理をおこない、次
いでアルカリ水溶液を用いて中和した後、防錆処理をお
こなう方法が採用されている。
That is, the inside of the pipe to be treated is washed with an aqueous solution of an acid such as hydrochloric acid or phosphoric acid, and is subjected to a blow treatment using air or nitrogen gas. After neutralization, a method of performing rust prevention treatment is employed.

しかしながら、このような洗浄方法においては、酸洗
後のブロー処理と水洗処理を十分におこなわないと発錆
するので、多量の洗浄水を用いて水洗(通常は複数回お
こなう)しなければならないだけでなく、水洗処理時間
が長くなると発錆するので高い作業能率が要求されると
共に、水流の悪い部分、例えば高圧フランジとパイプの
接続部分等の間隙に残存する酸液の除去が極めて困難な
ために水洗処理後の発錆の危険性が高く、さらに、酸洗
処理によって生成する遊離の鉄等の金属がアルカリ水溶
液による処理工程において塩に変化して配管の内壁に沈
澱付着して発錆をもたらす(特に、該間隙部等において
は発錆率が高い。)という改良すべき問題点がある。
However, in such a washing method, rusting occurs if the blow treatment and the washing treatment after the acid washing are not sufficiently performed, so that the washing must be carried out with a large amount of washing water (usually, a plurality of washings). Rather, rusting occurs when the washing time becomes long, so high work efficiency is required, and it is extremely difficult to remove an acid solution remaining in a portion having a poor flow of water, for example, a gap between a high-pressure flange and a pipe. There is a high risk of rusting after washing with water.In addition, metals such as free iron generated by pickling change into salts in the treatment step with an alkaline aqueous solution, and precipitate and adhere to the inner wall of the pipe, causing rusting. (Particularly, the rusting rate is high in the gaps and the like).

発明が解決しようとする課題 本発明は、水洗工程を省略することによって作業工程
の簡素化と洗浄水の節減を計ると共に、発錆を効果的に
防止できる配管の改良された洗浄方法を提供するために
なされたものである。
DISCLOSURE OF THE INVENTION The present invention provides an improved method for cleaning piping, which simplifies work steps and saves cleaning water by omitting a water-washing step, and can effectively prevent rusting. It was done for.

課題を解決するための手段 即ち本発明は、被処理配管の内部を酸水溶液を用いて
洗浄し、ブロー処理をおこなった後、キレート化剤水溶
液を用いて処理し、次いでアンモニア水溶液を用いて洗
浄した後、防錆処理をおこなうことを特徴とする配管の
洗浄方法に関する。
Means for Solving the Problems That is, according to the present invention, the inside of the pipe to be treated is washed with an acid aqueous solution, blow-treated, treated with a chelating agent aqueous solution, and then washed with an ammonia aqueous solution. And then performing a rust prevention treatment.

本発明に使用する酸は従来から常用されているもの、
例えば塩酸、リン酸、スルファミン酸、硫酸等を適宜使
用すればよく、濃度は酸の種類および被処理配管の種類
や汚染度等に応じて左右され、特に限定的ではないが、
通常は約5〜15%である。
The acids used in the present invention are those conventionally used,
For example, hydrochloric acid, phosphoric acid, sulfamic acid, sulfuric acid, etc. may be used as appropriate, and the concentration depends on the type of acid and the type of pipe to be treated, the degree of contamination, and the like, but is not particularly limited,
Usually about 5 to 15%.

酸洗後、洗液を系外へ排出させ、次いで空気や窒素ガ
ス等のガスを用いてブロー処理をおこなう。この場合、
ブロー処理は不完全、例えば被処理配管の全内容積の約
10%程度の酸洗液が残存していても、その後のキレート
化剤水溶液を用いる処理によって発錆は抑制されるので
問題はない。
After the pickling, the washing liquid is discharged out of the system, and then a blow treatment is performed using a gas such as air or nitrogen gas. in this case,
Blow treatment is incomplete, for example, about
Even if about 10% of the pickling solution remains, there is no problem because rusting is suppressed by the subsequent treatment using the chelating agent aqueous solution.

ブロー処理をおこなった後、キレート化剤水溶液を用
いて処理する。従来法においては、酸洗処理によって生
成する鉄等の金属がアルカリ水溶液による処理工程にお
いて塩に変化して配管の内壁に沈澱付着して発錆の一つ
の原因となっていたが、本発明方法においては、該金属
類はキレート化剤によって捕獲されるので、このような
発錆原因は除去される。
After performing the blow treatment, the treatment is performed using an aqueous solution of a chelating agent. In the conventional method, a metal such as iron generated by the pickling treatment is converted into a salt in a treatment step using an alkaline aqueous solution, and precipitates and adheres to the inner wall of the pipe, which is one cause of rusting. In, the metal is captured by the chelating agent, so that such a cause of rust is eliminated.

キレート化剤としてはクエン酸、エチレンジアミン四
酢酸、ニトリロ三酢酸、グリシン、イミノ二酢酸または
これらの塩類が例示される。
Examples of the chelating agent include citric acid, ethylenediaminetetraacetic acid, nitrilotriacetic acid, glycine, iminodiacetic acid, and salts thereof.

キレート化剤水溶液の濃度は、上記の酸洗処理に使用
する酸の種類や濃度および被処理配管の種類や汚染度等
によって左右され、特に限定的ではないが、通常は約0.
2〜2%(経済的見地からは0.2〜0.5%)である。
The concentration of the chelating agent aqueous solution depends on the type and concentration of the acid used for the above pickling treatment, the type of the pipe to be treated, the degree of contamination, and the like, and is not particularly limited.
It is 2 to 2% (from economic point of view 0.2 to 0.5%).

上記のキレート化剤水溶液は被処理配管の内部に一度
張った後、排液するだけで発錆を有効に抑制することが
できる。
The above-mentioned chelating agent aqueous solution can be effectively suppressed from rusting by merely draining it once inside the pipe to be treated and then draining it.

キレート化剤水溶液を用いるリンス処理をおこなった
後は、ブロー処理をおこなわずに、アンモニア水溶液を
配管の内部に注入することによって中和処理をおこな
う。
After performing a rinsing treatment using an aqueous solution of a chelating agent, a neutralization treatment is performed by injecting an aqueous ammonia solution into a pipe without performing a blow treatment.

アンモニア水溶液の濃度および注入量は酸洗処理に使
用する酸の種類や濃度および配管の内部に残留する酸の
量等によって左右され、特に限定的ではないが、通常は
市販の25%のアンモニア水溶液を所望により適宜希釈し
て使用し、その注入量は、注入後の処理液のpHが約9〜
10になる量とする。
The concentration and the injection amount of the aqueous ammonia solution are not particularly limited, and depend on the type and concentration of the acid used in the pickling treatment, the amount of the acid remaining in the piping, and the like, but are usually limited to a commercially available 25% aqueous ammonia solution. Is appropriately diluted as required, and the injection amount is adjusted so that the pH of the treatment solution after the injection is about 9 to 9.
Assume the amount to be 10.

アンモニアは、従来法の中和処理に使用されるアルカ
リに比べて中和効率が高くて浸透性が強いので、酸の残
留しやすい部分、例えば高圧フランジとパイプの接続部
分等の間隙等にも有効に浸透して発錆を効果的に防止す
る。
Ammonia has a higher neutralization efficiency and a higher permeability than the alkali used in the conventional neutralization treatment, so it is also used in areas where acids tend to remain, for example, in gaps between high pressure flanges and pipes. It effectively penetrates and effectively prevents rust.

続いて中和処理液を系外へ排出させずに、配管の内部
は防錆処理に付される。防錆処理は、通常は自体公知の
防錆剤の水溶液を注入することによっておこなう。
Subsequently, the inside of the pipe is subjected to a rust preventive treatment without discharging the neutralization treatment liquid to the outside of the system. The rust preventive treatment is usually performed by injecting an aqueous solution of a known rust preventive.

この種の防錆剤としては、燐酸塩、亜硝酸塩、ヒドラ
ジン等が例示される。
Examples of this kind of rust inhibitor include phosphate, nitrite, hydrazine and the like.

防錆剤水溶液を系外へ排出させた後、所望により、空
気や窒素ガス等のガスを用いてブロー処理をおこなって
もよい。
After discharging the rust inhibitor aqueous solution out of the system, a blowing treatment may be performed using a gas such as air or nitrogen gas, if desired.

以下、本発明を実施例によってさらに説明する。 Hereinafter, the present invention will be further described with reference to examples.

実施例1 油圧装置の油圧パイプライン(材質:STPT 42 STPG3
8、内径:20〜50A、長さ3640m)の内部をリン酸水溶液
(濃度:10%)を用いて洗浄後、排液し、空気を用いて
ブロー処理をおこなった後(パイプラインの全内容積の
約10%の酸洗液が残存)、クエン酸水溶液(濃度:1%)
を用いて処理した後、続いてアンモニア水溶液(濃度:
0.25%)を注入して処理した。
Example 1 Hydraulic device hydraulic pipeline (material: STPT 42 STPG3
8. After cleaning the inside of inner diameter: 20-50A, length 3640m) using phosphoric acid aqueous solution (concentration: 10%), draining, and performing blow processing with air (all contents of pipeline) About 10% of the product remains), citric acid aqueous solution (concentration: 1%)
, Followed by an aqueous ammonia solution (concentration:
0.25%).

さらにアンモニア水溶液をパイプラインから排出せず
に、ネオスCM306(主成分:亜硝酸ソーダ)水溶液(濃
度:0.5%)を注入することによって防錆処理をおこなっ
た後、該防錆剤水溶液を排出させた。
Further, without discharging the aqueous ammonia solution from the pipeline, rust prevention treatment is performed by injecting an aqueous solution (concentration: 0.5%) of Neos CM306 (main component: sodium nitrite), and then the aqueous rust inhibitor solution is discharged. Was.

以上の各処理工程はいずれも周囲温度においておこな
った。
All of the above processing steps were performed at ambient temperature.

上記の洗浄処理に付したパイプラインの内部の洗浄効
果は良好で、従来の洗浄方式に比べ、作業時間は2分の
1ですみ、廃液は3分の2の減となる。又発錆も認めら
れなかった。
The cleaning effect of the inside of the pipeline subjected to the above-mentioned cleaning treatment is good, and the operation time is reduced by half and the waste liquid is reduced by two-thirds as compared with the conventional cleaning method. No rust was observed.

実施例2 第1図に示す洗浄ラインに従って熱交換器(7.5m3
(1)の洗浄をおこなった。
Example 2 A heat exchanger (7.5 m 3 ) according to the washing line shown in FIG.
The washing of (1) was performed.

処理液調製用ポンプ(6)を使用し、処理液調製槽
(2)内において酸水溶液(塩酸5〜10%および非イオ
ン活性剤0.05〜1%含有)を調製し、これを室温〜55℃
の温度で処理液循環槽(4)内へ移した後、循環ポンプ
(3)を用いて熱交換器(1)内を約6〜10時間循環さ
せ、次いで熱交換器(1)と配管内に存在する酸水溶液
をN2ガスを用いて廃液槽(5)内へ排出させた。
Using a treatment liquid preparation pump (6), an acid aqueous solution (containing 5 to 10% of hydrochloric acid and 0.05 to 1% of a nonionic activator) was prepared in the treatment liquid preparation tank (2), and this was kept at room temperature to 55 ° C.
After being transferred into the treatment liquid circulation tank (4) at a temperature of, the mixture is circulated in the heat exchanger (1) for about 6 to 10 hours using the circulation pump (3), and then the heat exchanger (1) and the pipe Was discharged into the waste liquid tank (5) using N 2 gas.

次に、クエン酸1%水溶液を酸水溶液の場合と同様に
して調製し、これを熱交換器(1)内において2〜3サ
イクル循環させた後、アンモニア0.25%水溶液を熱交換
器内に注入して中和処理をおこない、さらに防錆剤水溶
液を熱交換器内に注入し、2〜3サイクル循環させた。
Next, a 1% aqueous citric acid solution is prepared in the same manner as in the case of the aqueous acid solution, and after circulating it for 2 to 3 cycles in the heat exchanger (1), a 0.25% aqueous ammonia solution is injected into the heat exchanger. Then, a neutralization treatment was carried out, and an aqueous solution of a rust inhibitor was injected into the heat exchanger and circulated for 2 to 3 cycles.

最後に、N2ガスを用いて防錆剤水溶液の廃液槽(5)
内へ排出させた。
Finally, waste liquid tank of rust inhibitor aqueous solution using N 2 gas (5)
It was discharged inside.

上記の洗浄法によれば、従来法に比べて洗浄時間は約
半分で済み、廃液量は約60%に減少し、洗浄効果も良好
で従来法の場合に比べて全く遜色がなかった。
According to the above-mentioned cleaning method, the cleaning time was about half as compared with the conventional method, the amount of waste liquid was reduced to about 60%, the cleaning effect was good, and there was no inferiority to the conventional method.

実施例3 熱交換器の代わりに水ドラムと蒸気ドラムから成るボ
イラー(保有水量8.1m3)の水管を被処理対象とし、酸
水溶液としてリン酸7.5%水溶液を使用し、これを室温
で該水管内を4〜6時間循環させる以外は実施例1と同
様の処理操作をおこなった。
Example 3 Instead of a heat exchanger, a water pipe of a boiler (water volume: 8.1 m 3 ) composed of a water drum and a steam drum was used as an object to be treated, and a 7.5% phosphoric acid aqueous solution was used as an acid aqueous solution. The same processing operation as in Example 1 was performed except that the inside of the tube was circulated for 4 to 6 hours.

この場合も、従来法に比べて洗浄時間は約半分で済
み、廃液量は約60%減少し、洗浄効果も良好で、従来法
の場合に比べて全く遜色がなかった。
Also in this case, the cleaning time was about half as compared with the conventional method, the waste liquid amount was reduced by about 60%, the cleaning effect was good, and there was no inferiority to the conventional method.

発明の効果 本発明方法によれば、従来法における必須工程である
多量の洗浄水を使用する水洗工程を省略することができ
るので作業工程の簡素化と洗浄水の節減を計ることが可
能となるだけでなく、発錆も効果的に防止することがで
きる。
Effects of the Invention According to the method of the present invention, a washing step using a large amount of washing water, which is an essential step in the conventional method, can be omitted, so that the working process can be simplified and washing water can be saved. In addition, rusting can be effectively prevented.

【図面の簡単な説明】[Brief description of the drawings]

第1図は本発明を実施する洗浄ラインの一態様を示す模
式図である。 (1)は熱交換器、(2)は処理液調整槽、(3)は循
環ポンプ、(4)は処理液循環槽、(5)は排液槽、
(6)は処理液調整用ポンプを示す。
FIG. 1 is a schematic view showing one embodiment of a cleaning line for carrying out the present invention. (1) is a heat exchanger, (2) is a treatment liquid adjusting tank, (3) is a circulation pump, (4) is a treatment liquid circulation tank, (5) is a drain tank,
(6) shows a processing liquid adjusting pump.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】被処理配管の内部を酸水溶液を用いて洗浄
し、ブロー処理をおこなった後、キレート化剤水溶液を
用いて処理し、次いでアンモニア水溶液を用いて洗浄し
た後、防錆処理をおこなうことを特徴とする配管の洗浄
方法。
1. The inside of a pipe to be treated is washed with an acid aqueous solution, subjected to a blow treatment, treated with a chelating agent aqueous solution, then washed with an ammonia aqueous solution, and then subjected to rust prevention treatment. A method of cleaning piping characterized by performing:
【請求項2】キレート化剤水溶液がクエン酸、エチレン
ジアミン四酢酸、ニトリロ三酢酸、グリシン、イミノ二
酢酸またはこれらの塩の水溶液である請求項1に記載の
洗浄方法。
2. The method according to claim 1, wherein the aqueous solution of the chelating agent is an aqueous solution of citric acid, ethylenediaminetetraacetic acid, nitrilotriacetic acid, glycine, iminodiacetic acid or a salt thereof.
JP63038882A 1988-02-22 1988-02-22 How to clean piping Expired - Lifetime JP2719599B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63038882A JP2719599B2 (en) 1988-02-22 1988-02-22 How to clean piping

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63038882A JP2719599B2 (en) 1988-02-22 1988-02-22 How to clean piping

Publications (2)

Publication Number Publication Date
JPH01212786A JPH01212786A (en) 1989-08-25
JP2719599B2 true JP2719599B2 (en) 1998-02-25

Family

ID=12537581

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63038882A Expired - Lifetime JP2719599B2 (en) 1988-02-22 1988-02-22 How to clean piping

Country Status (1)

Country Link
JP (1) JP2719599B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5800629A (en) * 1997-03-06 1998-09-01 H.E.R.C. Products Incorporated Pipe system cleaning and in-line treatment of spent cleaning solution
JP4649808B2 (en) * 2001-09-20 2011-03-16 栗田エンジニアリング株式会社 New plant equipment and pipe cleaning method
JP2008089286A (en) * 2006-10-05 2008-04-17 Chugoku Electric Power Co Inc:The Superheater tube washing method
KR100808373B1 (en) * 2007-08-30 2008-02-27 (주)켐씨텍 Composition of ecological cleaning agents for cleaning service of indoor water supply pipes
US10689280B2 (en) * 2009-12-31 2020-06-23 Ecolab Usa Inc. Method for the removing and reducing scaling
JP6250971B2 (en) * 2013-08-02 2017-12-20 東北電力株式会社 Cleaning apparatus and cleaning method for plate heat exchanger

Also Published As

Publication number Publication date
JPH01212786A (en) 1989-08-25

Similar Documents

Publication Publication Date Title
US4789406A (en) Method and compositions for penetrating and removing accumulated corrosion products and deposits from metal surfaces
US4581074A (en) Method for cleaning internal heat transfer surfaces of boiler tubes
US3460989A (en) Method of treating ferrous metal surfaces
US5021096A (en) Method for removal of scale
US4045253A (en) Passivating metal surfaces
JP2719599B2 (en) How to clean piping
US5492629A (en) Method of cleaning scale and stains in water systems and related equipment
US3067070A (en) Cleaning method for industrial systems
US3510351A (en) Method for etching and cleaning of objects and plants,particularly tube systems and boiler plants,consisting of iron or steel
US5164015A (en) Method for cleaning a vessel
JPH01159388A (en) Method for chemically cleaning slightly soluble scale
CN106032575A (en) Boiler washing method
US3507795A (en) Composition for removal of copper and copper oxide scales from boilers
US3085915A (en) Method of removing rust from ironcontaining materials, particularly for the cleaning of boiler plants
JPS59189998A (en) Scale removing method
US4861386A (en) Enhanced cleaning procedure for copper alloy equipment
US3415692A (en) Method of passivating metal surfaces
US5264041A (en) Method for cleaning a vessel
JPS602389B2 (en) Chemical cleaning method for steel parts
JP3207636B2 (en) Smut remover
CN105987372A (en) Boiler cleaning method
JPH0445593B2 (en)
CN1036081C (en) Acid-pickling cleaning method for hydraulic ash conveyer pipe
JPS602390B2 (en) Chemical cleaning method for steel parts
JP2001062489A (en) Removing method of deposited scale in dust collecting water circulation line

Legal Events

Date Code Title Description
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

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071121

Year of fee payment: 10

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081121

Year of fee payment: 11

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081121

Year of fee payment: 11