JPS6235480B2 - - Google Patents

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Publication number
JPS6235480B2
JPS6235480B2 JP9399580A JP9399580A JPS6235480B2 JP S6235480 B2 JPS6235480 B2 JP S6235480B2 JP 9399580 A JP9399580 A JP 9399580A JP 9399580 A JP9399580 A JP 9399580A JP S6235480 B2 JPS6235480 B2 JP S6235480B2
Authority
JP
Japan
Prior art keywords
acid
nitrogen oxide
oxide gas
urea
pickling
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
Application number
JP9399580A
Other languages
Japanese (ja)
Other versions
JPS5719385A (en
Inventor
Masayoshi Kotake
Yoshihide Okumura
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.)
Nissan Chemical Corp
Original Assignee
Nissan Chemical Corp
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 Nissan Chemical Corp filed Critical Nissan Chemical Corp
Priority to JP9399580A priority Critical patent/JPS5719385A/en
Publication of JPS5719385A publication Critical patent/JPS5719385A/en
Publication of JPS6235480B2 publication Critical patent/JPS6235480B2/ja
Granted legal-status Critical Current

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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
    • C23G1/086Iron or steel solutions containing HF

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)

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は金属の硝酸酸洗浴用の窒素酸化物ガ
ス発生抑止剤の改良に関する。 硝酸あるいは硝酸を含む酸により、金属の酸洗
処理を行うとき酸浴から窒素酸化物ガスが発生す
るため、これの抑止に関して従来より、尿素(特
開昭54―123529)、スルフアミン酸((特開昭53―
102232)等、アミノ基をもつ化合物を酸液に添加
することが提案されている。 しかしながら、尿素を添加して窒素酸化物ガス
の発生を抑止する場合においては、酸洗浴中の尿
素の添加量が少な過ぎると抑止効果がなく、又、
添加量が多過ぎると爆発性のある硝酸尿素が析出
分離したり酸洗浴の老化が著しくなる等酸洗浴の
管理が非常に難かしいという問題がある。 又、スルフアミン酸を添加して抑止する場合に
おいては酸浴中の亜硝酸は、次式のようにスルフ
アミン酸により分解されて窒素となることが知ら
れているが、 HNO2+NH2SO3H→N2+H2SO4+H2O この場合には亜硝酸とスルフアミン酸は等モルず
つ反応に関与することよりスルフアミン酸を窒素
酸化物ガスの発生抑止剤として実用化するには、
このものを工業的に効率よく生産することが必要
である。 しかしながら、従来このスルフアミン酸の製造
法としては例えば尿素と化学量論量以上の無水硫
酸および硫酸とを反応させ、ついでスルフアミン
酸は70〜80%濃度の硫酸に対して最も溶解度が小
さいのでこの濃度まで稀釈し、さらに過晶析、
乾燥して製品とされる方法がとられていた。しか
し、この方法では使用する原料の価格および工程
数の多い製法などから製品がコスト高となること
は避けられない。 又、酸洗工程は一部の大規模工場においては、
連続酸洗ラインで充分なる浴管理のもとに行われ
ているが大部分を占める小、中規模の金属表面処
理工場においては回分式により酸洗が実施されて
いるのが実体である。 上記の様に尿素、スルフアミン酸などのアミノ
基をもつ化合物を酸浴に添加して窒素酸化物ガス
の発生を抑止する方法においては酸浴の管理の難
しさあるいは使用するアミノ化合物の製品コスト
高などからくる問題があつてこれまで実用的では
なかつた。 本発明者らは、硝酸と弗酸を含む酸浴に尿素、
あるいはスルフアミン酸などアミノ化合物を添加
した場合のステンレス鋼管の脱スケール性、仕上
り性、窒素酸化物ガスの発生抑止性等について
種々研究を重ねた結果、スルフアミン酸85〜95
%、酸性硫酸アンモニウム3〜10%、尿素0.1〜
5%及び硫酸2〜5%からなる組成物は酸浴に極
めて溶解しやすく、従つて脱スケールに伴ない液
中に生成する亜硝酸を速やかに窒素に分解するこ
と、生成する亜硝酸に対してスルフアミン酸とし
て等モル以上になるよう添加する限りその添加量
の多少の変動にかかわらず窒素酸化物ガス発生の
抑止効果が卓越していること、さらに脱ケース
性、仕上り性とも良好であること等、スルフアミ
ン酸あるいは尿素単独添加の場合に比較して実用
上すぐれた性能を有していることを見出し、本願
発明を完成した。 本発明の目的は、金属の硝酸酸洗浴の管理が容
易であり、従つて回分式の酸洗用にも卓越した窒
素酸化物ガスの発生抑止効果を示す添加剤を提供
することにあり、他の目的は硝酸酸洗浴に迅速に
溶解する金属の硝酸酸洗浴用窒素酸化物ガスの発
生抑止剤を提供することにある。 本発明の金属の硝酸酸洗浴用窒素酸化物ガスの
発生抑止剤は、主成分としてスルフアミン酸85〜
95重量%、酸性硫酸アンモニウム3〜10重量%、
尿素0.1〜5重量%及び硫酸2〜5重量%を含有
することを特徴とする。 本発明の窒素酸化物ガスの発生抑止剤を、硝酸
酸洗浴中に添加すると極めて迅速に溶解し、酸洗
すべき金属を多量に又は連続的に浴中に浸漬した
際にも、逐次補充添加することによつて、ほゞ完
全に窒素酸化物ガスの発生を抑止し得る。本発明
の窒素酸化物ガスの発生抑止剤に含有されるスル
フアミン酸は金属の硝酸酸洗時の亜硝酸の分解に
消費され、酸性硫酸アンモニウムは酸洗金属の仕
上り光沢度を向上させ、尿素は脱スケール性の向
上効果がある。 本発明の窒素酸化物ガスの発生抑止剤に含まれ
る4成分のうち、いずれかの成分が欠けても、ま
た含有率が不足しても本発明の目的が達成され
な。また、4成分のうち、いずれかの成分が過剰
に含まれても本発明の目的が好ましく達成されな
い。 本発明の窒素酸化物ガスの発生抑止剤は、尿
素、無水硫酸、硫酸をほぼ化学量論量の割合で反
応器に仕込み、粉体反応を行なわせた後、反応器
からそのまゝとり出すことにより、工業的製品と
して容易に得られる。即ち、この方法によれば、
廃硫酸処理の必要がないこと、製造工程数が少な
いこと、さらに、本発明の窒素酸化物ガスの発生
抑止剤中の成分比率は上記仕込原料の比率を変え
ることにより容易に変えることができ極めて効率
よく目的物を生産し得る。通常、上記方法で生産
するときは、本発明の窒素酸化物ガスの発生抑止
剤は顆粒状製品として得られが、このものを更
に、粉砕することにより微粉状品としたり、ある
いは錠形化することにより錠剤とすることもで
き、いずれも金属酸洗用に実用し得る。また、本
発明の窒素酸化物ガスの発生抑止剤には、本発明
の目的が達成される限り、他に任意の成分、例え
ば防錆剤、界面活性剤等を含ませ得る。 以下、比較対照と共に実施例を挙げて説明する
が、本発明の技術的範囲はこれに限定されるもの
ではない。 実施例 1 300c.c.のスチロール製容器に硝酸15%および弗
酸2%を含む酸液150gを入れ、これにスルフア
ミン酸90%、酸性硝酸アンモニウム5%、尿素2
%、及び硫酸3%からなる窒素酸化物ガスの発生
抑止剤を酸液に対し、2%となるように添加し
た。 酸洗前の外径8mm、内径3.7mmのSUS―304継ぎ
目なし管を50mmの長さに切断し、この10本をたば
ねて一束とした。 この一束の鋼材を上記酸液中に投入した後、容
器に蓋をし、脱スケールされるまで常温で浸漬し
た。浸漬終了時に検知管により容器内気相中の窒
素酸化物ガスの濃度を測定したのち、脱スケール
された鋼材を取り出し、別の一束を上記酸液に投
入した。このようにして鋼材の浸漬処理と窒素酸
化物ガスの濃度測定を繰り返た。比較対照として
上記抑止剤を添加しない場合、尿素、スルフアミ
ン酸(純度99%)を添加した場合について同様に
して浸漬処理と窒素酸化物ガスの濃度測定を行な
つた。 結果は、第1表に示す通り本発明の例では窒素
酸化物ガスの発生抑止効果が卓越していることが
わかる。
This invention relates to improvements in nitrogen oxide gas generation inhibitors for use in nitric acid pickling baths for metals. When pickling metals with nitric acid or an acid containing nitric acid, nitrogen oxide gas is generated from the acid bath. 1973-
It has been proposed to add compounds with amino groups, such as 102232), to acid solutions. However, when adding urea to suppress the generation of nitrogen oxide gas, if the amount of urea added in the pickling bath is too small, there will be no suppressing effect;
If the amount added is too large, there will be problems such as precipitation and separation of explosive urea nitrate and significant aging of the pickling bath, making it extremely difficult to manage the pickling bath. Furthermore, in the case of adding sulfamic acid to suppress the suppression, it is known that nitrous acid in the acid bath is decomposed by the sulfamic acid and becomes nitrogen as shown in the following equation, HNO 2 +NH 2 SO 3 H →N 2 +H 2 SO 4 +H 2 O In this case, since nitrous acid and sulfamic acid participate in the reaction in equal moles, in order to put sulfamic acid into practical use as a nitrogen oxide gas generation inhibitor,
It is necessary to produce this product industrially and efficiently. However, conventional methods for producing sulfamic acid involve, for example, reacting urea with sulfuric anhydride and sulfuric acid in a stoichiometric amount or more, and then reacting with sulfamic acid at a concentration of 70 to 80%, since sulfamic acid has the lowest solubility in sulfuric acid at a concentration of 70 to 80%. diluted to
The method used was to dry it and make it into a product. However, this method inevitably increases the cost of the product due to the price of the raw materials used and the manufacturing method that requires a large number of steps. In addition, the pickling process is carried out in some large-scale factories.
Although pickling is carried out in a continuous pickling line with sufficient bath control, pickling is actually carried out in batches in the majority of small and medium-sized metal surface treatment factories. As mentioned above, in the method of adding a compound having an amino group such as urea or sulfamic acid to an acid bath to suppress the generation of nitrogen oxide gas, it is difficult to manage the acid bath or the product cost of the amino compound used is high. Due to problems such as these, it has not been practical until now. The present inventors added urea to an acid bath containing nitric acid and hydrofluoric acid.
Also, as a result of various studies on the descaling properties, finishing properties, and suppression of nitrogen oxide gas generation of stainless steel pipes when amino compounds such as sulfamic acids are added, we found that sulfamic acids 85-95
%, acidic ammonium sulfate 3-10%, urea 0.1-
A composition consisting of 5% sulfuric acid and 2-5% sulfuric acid is extremely soluble in an acid bath, and therefore, it is possible to quickly decompose nitrous acid generated in the liquid during descaling into nitrogen, and to reduce the amount of nitrite generated. As long as it is added in equal moles or more as sulfamic acid, the effect of suppressing the generation of nitrogen oxide gas is excellent regardless of slight variations in the amount added, and the decasing property and finishing properties are also good. The present invention was completed based on the discovery that the present invention has superior performance in practice compared to the case where sulfamic acid or urea is added alone. An object of the present invention is to provide an additive that is easy to manage in a nitric acid pickling bath for metals and that exhibits an excellent nitrogen oxide gas generation suppressing effect even for batch pickling. The object of the present invention is to provide a nitrogen oxide gas generation inhibitor for use in a nitric acid pickling bath for metals, which dissolves rapidly in the nitric acid pickling bath. The nitrogen oxide gas generation inhibitor for metal nitric acid pickling bath of the present invention has sulfamic acid 85 to 85% as a main component.
95% by weight, acidic ammonium sulfate 3-10% by weight,
It is characterized by containing 0.1-5% by weight of urea and 2-5% by weight of sulfuric acid. When the nitrogen oxide gas generation inhibitor of the present invention is added to a nitric acid pickling bath, it dissolves extremely quickly, and even when a large amount of metal to be pickled is immersed in the bath or continuously, it can be added sequentially. By doing so, the generation of nitrogen oxide gas can be almost completely suppressed. The sulfamic acid contained in the nitrogen oxide gas generation inhibitor of the present invention is consumed in the decomposition of nitrous acid when metals are pickled with nitric acid, the acidic ammonium sulfate improves the finish gloss of pickled metals, and the urea is decomposed. It has the effect of improving scalability. Even if any one of the four components contained in the nitrogen oxide gas generation inhibitor of the present invention is missing or its content is insufficient, the object of the present invention will not be achieved. Further, even if any one of the four components is included in excess, the object of the present invention cannot be preferably achieved. The nitrogen oxide gas generation inhibitor of the present invention is prepared by charging urea, sulfuric anhydride, and sulfuric acid into a reactor in approximately stoichiometric proportions, causing a powder reaction, and then taking them out of the reactor as they are. Therefore, it can be easily obtained as an industrial product. That is, according to this method,
There is no need for waste sulfuric acid treatment, the number of manufacturing steps is small, and the ratio of components in the nitrogen oxide gas generation inhibitor of the present invention can be easily changed by changing the ratio of the above-mentioned raw materials. The target product can be produced efficiently. Normally, when produced by the above method, the nitrogen oxide gas generation inhibitor of the present invention is obtained as a granular product, but this product may be further crushed into a fine powder product or tablet-shaped. It can also be made into tablets, both of which can be put to practical use for metal pickling. Further, the nitrogen oxide gas generation inhibitor of the present invention may contain other arbitrary components such as rust preventives, surfactants, etc., as long as the object of the present invention is achieved. Examples will be described below along with comparisons, but the technical scope of the present invention is not limited thereto. Example 1 Put 150 g of an acid solution containing 15% nitric acid and 2% hydrofluoric acid into a 300 c.c. styrene container, add 90% sulfamic acid, 5% acidic ammonium nitrate, and 2% urea.
%, and a nitrogen oxide gas generation inhibitor consisting of 3% sulfuric acid was added to the acid solution at a concentration of 2%. Before pickling, SUS-304 seamless pipes with an outer diameter of 8 mm and an inner diameter of 3.7 mm were cut into lengths of 50 mm, and 10 of these were tied into a bundle. After this bundle of steel materials was placed in the acid solution, the container was covered with a lid, and the steel materials were immersed at room temperature until descaling. After the concentration of nitrogen oxide gas in the gas phase inside the container was measured using a detection tube at the end of the immersion, the descaled steel material was taken out and another bundle was put into the acid solution. In this way, the immersion treatment of the steel material and the measurement of the concentration of nitrogen oxide gas were repeated. As a comparison, immersion treatment and concentration measurement of nitrogen oxide gas were carried out in the same manner when the above-mentioned inhibitor was not added and when urea and sulfamic acid (purity 99%) were added. As shown in Table 1, the results show that the examples of the present invention have an outstanding effect of suppressing the generation of nitrogen oxide gas.

【表】 実施例 2 300c.c.のスチロール製容器に硝酸10%及び弗酸
5%を含む酸液100gを入れ、これにスルフアミ
ン酸85%、酸性硝酸アンモニウム10%、尿素1%
及び硫酸4%からなる窒素酸化物ガス発生抑止剤
を酸液に対し0.1%となるように添加した。 酸洗前の外径8mm×内径5mmのSUS―304溶接
管を50mmの長さに切断した。 このうち、一本の鋼材を上記酸液に入れ、容器
に蓋をし、脱スケールされるまで常温にて浸漬し
た。 検知管により容器内気相中の窒素酸化物の濃度
を測定したのち脱スケールされた鋼材を取り出
し、別の一本を上記酸液に入れた。このようにし
て鋼材の浸漬処理と窒素酸化物濃度の測定を繰り
返した。 比較対照として上記抑止剤を添加しない場合及
び尿素を添加した場合について同様にして浸漬処
理と窒素酸化物濃度の測定を行なつた。 結果は第2表に示す通り、本発明の実施例は窒
素酸化物ガスの発生抑止にすぐれていることがわ
かる。
[Table] Example 2 Put 100 g of an acid solution containing 10% nitric acid and 5% hydrofluoric acid into a 300 c.c. styrene container, and add 85% sulfamic acid, 10% acidic ammonium nitrate, and 1% urea.
A nitrogen oxide gas generation inhibitor consisting of 4% sulfuric acid was added to the acid solution at a concentration of 0.1%. A welded SUS-304 pipe with an outer diameter of 8 mm and an inner diameter of 5 mm before pickling was cut into a length of 50 mm. One of the steel materials was placed in the acid solution, the container was covered, and the steel material was immersed at room temperature until it was descaled. After measuring the concentration of nitrogen oxides in the gas phase inside the container using a detection tube, the descaled steel material was taken out and another one was placed in the acid solution. In this way, the immersion treatment of the steel material and the measurement of the nitrogen oxide concentration were repeated. As a comparison, the same immersion treatment and measurement of nitrogen oxide concentration were performed in the case where the above-mentioned inhibitor was not added and in the case where urea was added. As shown in Table 2, the results show that the examples of the present invention are excellent in suppressing the generation of nitrogen oxide gas.

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 主成分として、スルフアミン酸85〜95重量
%、酸性硫酸アンモニウム3〜10重量%、尿素
0.1〜5重量%及び硫酸2〜5重量%を含有する
ことを特徴とする硝酸酸洗浴用の窒素酸化物ガス
の発生抑止剤。
1 Main components: 85 to 95% by weight of sulfamic acid, 3 to 10% by weight of acidic ammonium sulfate, and urea.
A nitrogen oxide gas generation inhibitor for a nitric acid pickling bath, characterized by containing 0.1 to 5% by weight and 2 to 5% by weight of sulfuric acid.
JP9399580A 1980-07-11 1980-07-11 Gaseous nitrogen oxide generation inhibitor for nitric acid pickling bath Granted JPS5719385A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9399580A JPS5719385A (en) 1980-07-11 1980-07-11 Gaseous nitrogen oxide generation inhibitor for nitric acid pickling bath

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9399580A JPS5719385A (en) 1980-07-11 1980-07-11 Gaseous nitrogen oxide generation inhibitor for nitric acid pickling bath

Publications (2)

Publication Number Publication Date
JPS5719385A JPS5719385A (en) 1982-02-01
JPS6235480B2 true JPS6235480B2 (en) 1987-08-01

Family

ID=14097976

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9399580A Granted JPS5719385A (en) 1980-07-11 1980-07-11 Gaseous nitrogen oxide generation inhibitor for nitric acid pickling bath

Country Status (1)

Country Link
JP (1) JPS5719385A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60185173A (en) * 1984-03-05 1985-09-20 Hitachi Ltd Detection of connection stage of logical circuit
SE515806C2 (en) * 2000-01-19 2001-10-08 Avesta Polarit Ab Publ Long-term stable urea containing urea as well as ways of making it

Also Published As

Publication number Publication date
JPS5719385A (en) 1982-02-01

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