JPH0445590B2 - - Google Patents
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- Publication number
- JPH0445590B2 JPH0445590B2 JP61047897A JP4789786A JPH0445590B2 JP H0445590 B2 JPH0445590 B2 JP H0445590B2 JP 61047897 A JP61047897 A JP 61047897A JP 4789786 A JP4789786 A JP 4789786A JP H0445590 B2 JPH0445590 B2 JP H0445590B2
- Authority
- JP
- Japan
- Prior art keywords
- component
- corrosion
- steam
- present
- composition
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/02—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in air or gases by adding vapour phase inhibitors
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Description
技術分野
本発明は蒸気発生系などにおける金属腐食を抑
制するための組成物、さらに詳しくは蒸気復水系
における皮膜性防食剤と中和性防食剤とを併用し
た蒸気系腐食抑制剤組成物に関する。
従来技術
ボイラー、濃縮缶などの蒸気を発生する装置で
は、供給水中に含まれていた酸素、二酸化炭素又
はその他の酸性物質の作用によるPHの低下に起因
して、蒸気及び凝縮水と接触する個所がしばしば
腐食する。この腐食防止対策としては供給水のイ
オン交換処理や脱気処理のほか、化学薬品による
処理が行なわれており、化学薬品としては主に長
鎖脂肪族アミンが使用されている。
ところで、長鎖脂肪族アミンが非水溶性であ
り、このものを直接水に均一に分散させることが
困難であるため、これを腐食抑制剤に用いる場合
の一方法として、当該アミンを酢酸塩のような可
溶性塩に変えて水溶液とするか、あるいは当該ア
ミンをそのままアルコール溶液として供給水に添
加する方法が知られている。しかし、これらの腐
食抑制剤溶液は供給水で希釈された際に、溶質が
供給水中に存在する電解質などの影響で凝集析出
して器壁や管壁に蓄積する不都合がある上、適切
な濃度管理が難しい欠点がある。
これに対し、長鎖脂肪族アミンを乳化分散液と
して用いる方法は、電解質などの影響を受けるこ
とがない。しかしながら、供給水で希釈された際
に、乳化分散状態が安定に保持されなければなら
ない点は、先の溶液状腐食抑制剤と変わりがない
上、これとは別に、乳化分散液であるが故に原液
のまま長期間保存しても、その乳化分散状態が安
定であることが要求される。これに加えて、近年
ボイラーが大型化し、かつプロセスが省力化され
ていることとの関係で、従来より大容量の貯水槽
が用いられるようになり、貯水槽中におけるボイ
ラー供給水の滞留時間も大幅に延長される傾向に
あるため、蒸気系腐食抑制剤には貯水槽中での経
時安定性が必要となつてきた。
そこでボイラーに供給された蒸気系腐食抑制剤
が蒸気とともに気化すること、及び蒸気は圧力調
整など種々の事情から大気中に放出される場合が
少なくないことから、蒸気系腐食抑制剤の成分は
安全性が高い程好ましいことを勘案し、人体に対
する安全性の高い乳化剤を用いて、蒸気系腐食抑
制剤としての要件を備えた乳化分散型の腐食抑制
剤が開発された(特開昭60−174884参照)。
しかしながら、これらの従来の皮膜性防食剤は
効果を発揮するまでの長期間(数ケ月以上)を要
し、その間に配管が腐食性ガス(CO2またはO2)
によつて腐食してしまう欠点があつた。すなわ
ち、皮膜性防食剤が十分な防食効果を発揮するた
めには配管全体に皮膜性物質(アルキルアミン)
が吸着をし、完全な防食皮膜を形成しなければな
らない。しかし、復水配管の面積が広く、蒸発量
が少ないプラントにおいては、防食皮膜を形成す
るまでには長期間(3ケ月以上)を要する。その
ためにCO2およびO2によつて配管の腐食が進行し
てしまい、特に、肉厚のうすいネジ切り部などの
腐食は防止できなかつた。
目 的
本発明は、これら従来の皮膜性防食剤の欠点を
解決するために、中和性防食剤と一剤化すること
によつて防食皮膜ができるまでの腐食(以下初期
腐食と称する)を防止することを目的としたもの
である。
構 成
本発明者は前記目的を達成するために鋭意研究
した結果、A炭素数10〜24の長鎖脂肪族アミン、
B炭素数8〜24の脂肪酸アルカリ金属塩及びC
式、
RO(−CH2)−oNH2(但し、RはH又はCH3を、
nは2又は3を示す)
で表わされる中和性アミンを含み、かつ組成物中
A成分が0.5〜20重量%、A成分:B成分が5:
1〜1:5(重量比)、C成分:A成分+B成分が
1:99〜99:1(重量%)である水性エマルジヨ
ンからなる蒸気系腐食抑制剤組成物を提供するこ
とによつて前記目的が達成できることを見出し
た。
すなわち、本発明は前記特開昭第60−174884号
に開示されている発明の改良発明であり、皮膜性
防食剤の防食皮膜ができるまでの腐食(すなわち
初期腐食)を防止するための皮膜性防食剤との併
用処理方法に関するものである。
本発明の蒸気系腐食抑制剤組成物は、式、
CH3(−CH2)−oNH2 (n=9〜23)
で表わされる炭素数10〜24の脂肪族アミン(A成
分)及び炭素数8〜24の脂肪酸アルカリ金属塩
(B成分)を、A成分を0.5〜20重量%、A成分と
B成分との重量比が5:1ないし1:5になるよ
うな割合で含有する水性エマルジヨンからなる皮
膜性防食剤に、式、RO(−CH2)−oNH2(R=Hま
たはCH3、n=2〜3)で表わされるアルカノー
ルアミン類をA成分とB成分の和に対して1:99
〜99:1(重量%)配合し一剤化とした。一剤化
することによつて従来の皮膜性防食剤と同様の注
入方法で自動的にドレン水PHを7.0以上に上昇さ
せることができ、これによつて防食皮膜が形成さ
れるまでに腐食性ガス(CO2またはO2)によつて
起こる初期腐食の防止を可能とした。
ここで、皮膜性アミンは、解離せず、そのまま
蒸気へ移行し、復水化されたときに管面に吸着さ
れて皮膜を形成する。一方、中和性アミンは水中
で解離して(水からHを奪つて)OHを放出し、
水中の酸性物質と反応して中和する。
本発明の蒸気系腐食抑制剤組成物においてA成
分として用いる長鎖脂肪族アミンは、炭素数10〜
24、好ましくは12〜20のアルキル基又はアルケニ
ル基を1〜3個、好ましくは1個有するものであ
る。これよりも炭素数が少ないアミンでは金属腐
食防止効果が劣り、またこれよりも炭素数が多い
アミンではゲル化など好ましくない現象を起す心
配がある。本発明に適した長鎖脂肪族アミンの具
体例としては、ドデシルアミン、トリデシルアミ
ン、テトラデシルアミン、ペンタデシルアミン、
ヘキサデシルアミン、ヘプタデシルアミン、オク
タデシルアミン、ノナデシルアミン、エイコシル
アミン、ドコシルアミンなどの飽和脂肪族アミ
ン、オレイルアミン、リシノレイルアミン、リノ
レイルアミン、リノレニルアミンなどの不飽和脂
肪族アミン、ヤシ油アミン、硬化牛脂アミンなど
の混合アミン及びこれらの混合物を挙げることが
できる。ちなみに、米国FDA規格においてボイ
ラー水用添加剤として使用が認められているオク
タデシルアミンをA成分として用いた場合には、
ボイラーから発生した蒸気が洩れて食品と接触し
ても安全性の面で問題がないので、食品製造業に
おいても使用できる利点を有する。A成分は組成
物全量に基づき0.5〜20重量%の割合で用いる。
これより少ない場合は組成物の安定性が劣り、一
方、これより多い場合はゲル化し易く、分散が困
難になるので好ましくない。
本発明で用いるB成分は炭素数8〜24、好まし
くは10〜22の脂肪酸アルカリ金属塩である。なか
でも食用油脂から製造される脂肪酸のナトリウム
塩及びカリウム塩が好ましく、特に炭素数14〜22
の不飽和脂肪酸からなる群から選ばれた少なくと
も1種の不飽和脂肪酸、ラウリン酸又はパルミチ
ン酸を25重量%以上含有する脂肪酸のアルカリ金
属塩が適している。また、本発明に使用できるB
成分として、カプリン酸、ラウリン酸、ミリスチ
ン酸、パルミチン酸、ステアリン酸、アラキン
酸、ベヘン酸、オレイン酸、エルカ酸、リノール
酸及びリノレン酸などの各アルカリ金属塩の1種
もしくは2種以上が例示される。
本発明においてはB成分は組成物全量に基づき
0.5〜30重量%使用されるが、特にA成分とB成
分を重量比で5:1ないし1:5の割合で用い
る。B成分の割合がこれより小さい場合は、組成
物を希釈した際の経時安定性が低下し、一方大き
い場合は組成物の長期保存安定性が低下し、貯蔵
中に相分離やゲル化が起りやすくなる。
本発明のC成分として使用される式、
RO(−CH2)−oNH2 (R=HまたはCH3、n=
2〜3)で表わされる中和性アミンであるアルカ
ノールアミン類の具体例としてはエタノールアミ
ン、プロパノールアミン、メトキシエタノールア
ミン、メトキシプロパノールアミンが挙げられ
る。
C成分は使用量は、0.5ppm以上、好ましくは
数10ppm以上で、上限は特にないが、経済性など
を考慮して決められる。
C成分と他の成分との割合は、通常C:A+B
=1:99〜99:1(重量%)で、好ましくは50:
50〜85:15である。
本発明の蒸気系腐食抑制剤組成物は腐食抑制成
分としてA成分を、乳化剤としてB成分を用いる
ので、それ自体長期保存安定性にすぐれ、水で希
釈した場合でも良好な分散安定性を示し、その安
定性は経時的に劣化してしまうこともない。これ
に加えて本発明の組成物は安全性が高いので、食
品工場などの安全性に対する制限が厳しい工場に
おいても支障なくボイラーなどに腐食抑制剤とし
て使用することができる。このような効果は腐食
抑制成分がアニオン性界面活性剤とコンプレツク
スを形成しやすい長鎖脂肪族アミンであることを
考慮すると全く予想外の効果であると言うことが
できる。
本発明の腐食抑制剤組成物はA、B及びCの3
成分を必須とするが、必要に応じて腐食抑制剤の
慣用成分やその他の補助添加成分を任意に含有す
ることができる。このような任意添加剤の例とし
ては、エチレングリコール、プロピレングリコー
ル、ブチレングリコール、ヘキシレングリコー
ル、ブリセリンなどの可溶化剤、金属イオン封鎖
剤、凍結防止剤などが挙げられる。
本発明の腐食抑制剤組成物は供給水又は蒸気に
対し、アミン含有量として0.1〜100ppm、好まし
くは1〜10ppmの濃度となるように連続的あるい
は断続的に添加することによつて金属部分の腐食
を抑制する。
本発明の腐食抑制剤組成物は使用濃度付近に希
釈したときに、その希釈分散液がPH9〜11程度の
塩基性を示すので、一般に塩基性を有するスケー
ル防止剤やその他の水処理剤を不都合なく併用す
ることができる。
効 果
本発明の長鎖脂肪族アミン、脂肪酸アルカリ金
属塩及び中和性アルカノールアミンの3成分系か
らなる蒸気系腐食抑制剤組成物は、従来の長鎖脂
肪族アミン及び脂肪酸アルカリ金属塩の2成分系
からなる組成物より初期における腐食防止効果が
はるかに優れている。
次に実施例により本発明をさらに詳細に説明す
る。
実施例1(保存安定性試験)
オクタデシルアミン1.4重量部、オレイン酸ソ
ーダ0.9重量部、エチレングリコール0.4重量部、
モノエタノールアミン40重量部及び純水57.3重量
部を十分混合した後、室温下で静置した。そして
7日後、1ケ月後及び3ケ月後に外観を見たが、
いずれの場合においても、相分離が認められず、
良好な乳化状態を示した。これから、本発明のC
成分を加えても乳化安定性は損なわれないことが
わかる。
実施例2(腐食試験)
蒸発量12.6/hの連続式蒸気発生型オートク
レーブにKOH30mg/、Na3PO435mg/及び
下記の表−1に示す組成物を270mg/添加した
軟水を給水し、圧力10Kg/cm2で蒸気を連続的に発
生させながら運転した。
この際、テストピース(軟鋼15×15×1)を蒸
気ドレン水中に浸漬し、腐食速度を測定した。得
られた結果を第1図に示す。
TECHNICAL FIELD The present invention relates to a composition for inhibiting metal corrosion in a steam generation system, and more particularly to a steam corrosion inhibitor composition that uses a combination of a film-forming corrosion inhibitor and a neutralizing corrosion inhibitor in a steam condensate system. Prior Art In equipment that generates steam, such as boilers and concentrators, points that come into contact with steam and condensed water are affected by a decrease in pH due to the action of oxygen, carbon dioxide, or other acidic substances contained in the feed water. often corrodes. Measures to prevent this corrosion include ion exchange treatment and deaeration treatment of the feed water, as well as treatment with chemicals, and long-chain aliphatic amines are mainly used as chemicals. By the way, long-chain aliphatic amines are water-insoluble, and it is difficult to directly and uniformly disperse them in water. One way to use them as corrosion inhibitors is to mix them with acetate. There are known methods in which the amine is converted into an aqueous solution by converting it into a soluble salt, or the amine is directly added to the feed water as an alcohol solution. However, when these corrosion inhibitor solutions are diluted with feed water, the solutes tend to coagulate and precipitate due to the influence of electrolytes present in the feed water, accumulating on the vessel walls and pipe walls. There are drawbacks that make it difficult to manage. On the other hand, the method of using a long-chain aliphatic amine as an emulsified dispersion is not affected by electrolytes and the like. However, the point that the emulsified dispersion state must be stably maintained when diluted with feed water is the same as the previous solution corrosion inhibitor, and apart from this, since it is an emulsified dispersion, It is required that the emulsified dispersion state is stable even if the undiluted solution is stored for a long period of time. In addition, in recent years, boilers have become larger and processes have become more labor-saving, so water tanks with larger capacities than before are being used, and the residence time of boiler supply water in the water tank has also increased. Due to the trend toward significantly longer retention times, steam-based corrosion inhibitors have become required to be stable over time in water tanks. Therefore, the ingredients of steam-based corrosion inhibitors are considered safe because the steam-based corrosion inhibitors supplied to the boiler vaporize together with the steam, and the steam is often released into the atmosphere due to various reasons such as pressure adjustment. Taking into account the fact that higher corrosion resistance is better, an emulsion-dispersed corrosion inhibitor was developed using an emulsifier that was highly safe for the human body and had the requirements as a vapor-based corrosion inhibitor (Japanese Patent Application Laid-Open No. 174884-1983). reference). However, these conventional film-based corrosion inhibitors require a long period of time (several months or more) to become effective, during which time the pipes are exposed to corrosive gases (CO 2 or O 2 ).
The drawback was that it corroded due to water. In other words, in order for a film-based corrosion inhibitor to exhibit sufficient corrosion-preventing effect, a film-forming substance (alkylamine) must be applied to the entire pipe.
must be adsorbed to form a complete anti-corrosion film. However, in plants where the area of condensate piping is large and the amount of evaporation is small, it takes a long time (3 months or more) to form an anticorrosive film. As a result, corrosion of the piping progressed due to CO 2 and O 2 , and corrosion, especially in thin-walled threaded sections, could not be prevented. Purpose In order to solve the drawbacks of these conventional film-forming corrosion inhibitors, the present invention aims to prevent corrosion until a corrosion-resistant film is formed (hereinafter referred to as initial corrosion) by combining it with a neutralizing corrosion inhibitor. The purpose is to prevent Composition As a result of intensive research in order to achieve the above object, the present inventor found that A long chain aliphatic amine having 10 to 24 carbon atoms;
B Fatty acid alkali metal salt having 8 to 24 carbon atoms and C
Formula, RO( -CH2 ) -oNH2 (where R is H or CH3 ,
n represents 2 or 3), and the composition contains 0.5 to 20% by weight of component A, and component A:component B is 5:
By providing a steam-based corrosion inhibitor composition comprising an aqueous emulsion in which the ratio of component C: component A + component B is 1:99 to 99:1 (weight %). I found out that I can achieve my goal. That is, the present invention is an improved invention of the invention disclosed in JP-A No. 60-174884, and the present invention is an improved invention of the invention disclosed in JP-A-60-174884. The present invention relates to a treatment method in combination with an anticorrosive agent. The vapor-based corrosion inhibitor composition of the present invention comprises an aliphatic amine having 10 to 24 carbon atoms (component A) represented by the formula: CH 3 (-CH 2 ) -o NH 2 (n=9 to 23); An aqueous solution containing fatty acid alkali metal salts of number 8 to 24 (component B) in a ratio such that the component A is 0.5 to 20% by weight and the weight ratio of the component A to the component B is 5:1 to 1:5. Add alkanolamines represented by the formula RO(-CH 2 ) -o NH 2 (R=H or CH 3 , n=2 to 3) to the film-forming anticorrosive agent made of emulsion to the sum of component A and component B. against 1:99
~99:1 (wt%) was blended to form a single agent. By combining it into a single agent, it is possible to automatically raise the pH of drain water to 7.0 or higher using the same injection method as conventional film-forming corrosion inhibitors. This makes it possible to prevent initial corrosion caused by gas (CO 2 or O 2 ). Here, the film-forming amine does not dissociate, but directly transfers to steam, and when it is condensed, it is adsorbed on the pipe surface to form a film. On the other hand, neutralizing amines dissociate in water (take H from water) and release OH,
Reacts with and neutralizes acidic substances in water. The long-chain aliphatic amine used as component A in the vapor-based corrosion inhibitor composition of the present invention has a carbon number of 10 to
24, preferably 12 to 20 alkyl or alkenyl groups, preferably 1 to 3, preferably 1. An amine having a lower number of carbon atoms than this is inferior in metal corrosion prevention effect, and an amine having a higher number of carbon atoms than this may cause undesirable phenomena such as gelation. Specific examples of long chain aliphatic amines suitable for the present invention include dodecylamine, tridecylamine, tetradecylamine, pentadecylamine,
Saturated aliphatic amines such as hexadecylamine, heptadecylamine, octadecylamine, nonadecylamine, eicosylamine, docosylamine, unsaturated aliphatic amines such as oleylamine, ricinoleylamine, linoleylamine, linolenylamine, coconut oil amine, hydrogenated Mention may be made of mixed amines such as tallow amine and mixtures thereof. By the way, if octadecylamine, which is approved for use as an additive for boiler water according to US FDA standards, is used as component A,
Since there is no safety problem even if the steam generated from the boiler leaks and comes into contact with food, it has the advantage that it can also be used in the food manufacturing industry. Component A is used in an amount of 0.5 to 20% by weight based on the total amount of the composition.
If the amount is less than this, the stability of the composition will be poor, while if it is more than this, it will tend to gel, making dispersion difficult, which is not preferred. Component B used in the present invention is an alkali metal salt of a fatty acid having 8 to 24 carbon atoms, preferably 10 to 22 carbon atoms. Among these, sodium salts and potassium salts of fatty acids produced from edible fats and oils are preferred, especially fatty acids having 14 to 22 carbon atoms.
An alkali metal salt of a fatty acid containing at least 25% by weight of at least one unsaturated fatty acid selected from the group consisting of unsaturated fatty acids, lauric acid or palmitic acid is suitable. Also, B that can be used in the present invention
Examples of ingredients include one or more of alkali metal salts such as capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, oleic acid, erucic acid, linoleic acid, and linolenic acid. be done. In the present invention, component B is based on the total amount of the composition.
It is used in an amount of 0.5 to 30% by weight, and in particular, component A and component B are used in a weight ratio of 5:1 to 1:5. If the proportion of component B is smaller than this, the stability over time will decrease when the composition is diluted, while if it is larger, the long-term storage stability of the composition will decrease, and phase separation or gelation may occur during storage. It becomes easier. The formula used as the C component of the present invention, RO( -CH2 ) -oNH2 (R=H or CH3 , n=
Specific examples of alkanolamines which are neutralizing amines represented by 2 to 3) include ethanolamine, propanolamine, methoxyethanolamine, and methoxypropanolamine. The amount of component C to be used is 0.5 ppm or more, preferably several tens of ppm or more, and although there is no particular upper limit, it is determined in consideration of economic efficiency and the like. The ratio of component C to other components is usually C:A+B
= 1:99 to 99:1 (wt%), preferably 50:
50-85:15. Since the vapor-based corrosion inhibitor composition of the present invention uses component A as a corrosion inhibiting component and component B as an emulsifier, it itself has excellent long-term storage stability and exhibits good dispersion stability even when diluted with water. Its stability does not deteriorate over time. In addition, since the composition of the present invention is highly safe, it can be used as a corrosion inhibitor in boilers and the like without any problems even in factories where safety restrictions are severe, such as food factories. This effect can be said to be completely unexpected considering that the corrosion-inhibiting component is a long-chain aliphatic amine that tends to form complexes with anionic surfactants. The corrosion inhibitor composition of the present invention comprises three of A, B and C.
Although these ingredients are essential, conventional ingredients for corrosion inhibitors and other auxiliary additive ingredients can be optionally included as needed. Examples of such optional additives include solubilizers such as ethylene glycol, propylene glycol, butylene glycol, hexylene glycol, and briselin, sequestering agents, antifreeze agents, and the like. The corrosion inhibitor composition of the present invention can be added continuously or intermittently to supplied water or steam so that the amine content is 0.1 to 100 ppm, preferably 1 to 10 ppm. Inhibits corrosion. When the corrosion inhibitor composition of the present invention is diluted to near the concentration used, the diluted dispersion exhibits basicity with a pH of about 9 to 11. Can be used together without any problems. Effects The steam-based corrosion inhibitor composition of the present invention, which consists of a three-component system of a long-chain aliphatic amine, a fatty acid alkali metal salt, and a neutralizing alkanolamine, has two components: a long-chain aliphatic amine, a fatty acid alkali metal salt, and a neutralizing alkanolamine. The initial corrosion prevention effect is far superior to that of compositions consisting of component systems. Next, the present invention will be explained in more detail with reference to Examples. Example 1 (storage stability test) 1.4 parts by weight of octadecylamine, 0.9 parts by weight of sodium oleate, 0.4 parts by weight of ethylene glycol,
After thoroughly mixing 40 parts by weight of monoethanolamine and 57.3 parts by weight of pure water, the mixture was allowed to stand at room temperature. I looked at the appearance after 7 days, 1 month and 3 months.
In either case, no phase separation was observed;
It showed a good emulsification state. From now on, C of the present invention
It can be seen that the emulsion stability is not impaired even if the ingredients are added. Example 2 (corrosion test) Soft water containing 30 mg of KOH, 35 mg of Na 3 PO 4 and 270 mg of the composition shown in Table 1 below was added to a continuous steam-generating autoclave with an evaporation rate of 12.6/h, and the pressure was increased. It was operated while continuously generating steam at 10 kg/cm 2 . At this time, a test piece (mild steel 15 x 15 x 1) was immersed in steam drain water and the corrosion rate was measured. The results obtained are shown in FIG.
【表】
第1図に示した結果からわかるように、本発明
の腐食抑制剤組成物()及び()は従来の腐
食抑制剤組成物()より初期における腐食抑制
効果がはるかに優れていることがわかる。
実施例3(腐食試験)
実施例2の運転方法において、表2に示す供試
試料を所定量添加した他は同一の操作を行つて腐
食試験を行つた。
48時間後にテストピースを抜き取り、腐食度を
測定した。その結果を表−2に示す。[Table] As can be seen from the results shown in Figure 1, the corrosion inhibitor compositions () and () of the present invention have a much better initial corrosion inhibition effect than the conventional corrosion inhibitor composition (). I understand that. Example 3 (Corrosion Test) A corrosion test was carried out in the same manner as in Example 2, except that a predetermined amount of the test sample shown in Table 2 was added. After 48 hours, the test piece was removed and the degree of corrosion was measured. The results are shown in Table-2.
【表】【table】
【表】
以上の結果よりわかるように、本発明の腐食抑
制組成物()は従来の腐食抑制薬より腐食抑制効
果が優れていることがわかる。
実施例4(腐食試験)
実施例2の運転方法において、表3に示す供
試々料を所定量添加した他は同一の操作を行つて
腐食試験を行つた。
1、2、3、4日後にテストピースを抜き取
り、腐食速度を測定した。結果を第2図に示す。
第2図から本発明の腐食抑制剤組成物は従来の
ものに比べて保存安定性が良く、かつ、初期にお
ける腐食防止効果が優れている。[Table] As can be seen from the above results, it can be seen that the corrosion inhibiting composition () of the present invention has a superior corrosion inhibiting effect than conventional corrosion inhibitors. Example 4 (Corrosion Test) A corrosion test was carried out in the same manner as in Example 2, except that a predetermined amount of the sample shown in Table 3 was added. After 1, 2, 3, and 4 days, the test piece was removed and the corrosion rate was measured. The results are shown in Figure 2. As can be seen from FIG. 2, the corrosion inhibitor composition of the present invention has better storage stability and excellent initial corrosion prevention effect than conventional compositions.
第1図及び第2図は本発明の腐食抑制剤と従来
の腐食抑制剤との腐食防止効果を経時的に比較し
たグラフを示す。
FIGS. 1 and 2 are graphs comparing the corrosion inhibiting effects of the corrosion inhibitor of the present invention and conventional corrosion inhibitors over time.
Claims (1)
式 RO(−CH2)−oNH2 (但し、RはH又はCH3を、nは2又は3を示
す) で表わされる中和性アミンを含み、かつ組成物
中、A成分が0.5〜20重量%、A成分:B成分が
5:1〜1:5(重量比)、C成分:A成分+B成
分が1:99〜99:1(重量%)である水性エマル
ジヨンからなる蒸気系腐食抑制剤組成物。[Scope of Claims] 1. A long chain aliphatic amine having 10 to 24 carbon atoms, B fatty acid alkali metal salt having 8 to 24 carbon atoms, and C
The composition contains a neutralizing amine represented by the formula RO(-CH 2 ) -o NH 2 (wherein R represents H or CH 3 and n represents 2 or 3), and the A component is 0.5 to 0. Steam-based corrosion consisting of an aqueous emulsion in which A component: B component is 5:1 to 1:5 (weight ratio) and C component: A component + B component is 1:99 to 99:1 (weight %). Inhibitor composition.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4789786A JPS62205292A (en) | 1986-03-05 | 1986-03-05 | Corrosion inhibitor composition for vapor system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4789786A JPS62205292A (en) | 1986-03-05 | 1986-03-05 | Corrosion inhibitor composition for vapor system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62205292A JPS62205292A (en) | 1987-09-09 |
| JPH0445590B2 true JPH0445590B2 (en) | 1992-07-27 |
Family
ID=12788191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4789786A Granted JPS62205292A (en) | 1986-03-05 | 1986-03-05 | Corrosion inhibitor composition for vapor system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62205292A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02209493A (en) * | 1989-02-09 | 1990-08-20 | Kurita Water Ind Ltd | Corrosion inhibitor for steam or condensate systems |
| US5641396A (en) * | 1995-09-18 | 1997-06-24 | Nalco/Exxon Energy Chemicals L. P. | Use of 2-amino-1-methoxypropane as a neutralizing amine in refinery processes |
| JP5092334B2 (en) * | 2006-10-03 | 2012-12-05 | 栗田工業株式会社 | Corrosion inhibitor |
| JP5928404B2 (en) * | 2013-05-01 | 2016-06-01 | 栗田工業株式会社 | Corrosion control method and corrosion inhibitor for water and steam plant |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5827350B2 (en) * | 1974-07-26 | 1983-06-08 | 栗田工業株式会社 | Kinzokufushiyokuboushizai |
| JPS60174884A (en) * | 1984-02-17 | 1985-09-09 | Lion Akzo Kk | Composition for corrosion inhibitor in steam phase |
-
1986
- 1986-03-05 JP JP4789786A patent/JPS62205292A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62205292A (en) | 1987-09-09 |
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