JPS59118890A - Aqueous solution of descaling agent for replenishing oxidizing molten salt of alkali - Google Patents

Aqueous solution of descaling agent for replenishing oxidizing molten salt of alkali

Info

Publication number
JPS59118890A
JPS59118890A JP22692882A JP22692882A JPS59118890A JP S59118890 A JPS59118890 A JP S59118890A JP 22692882 A JP22692882 A JP 22692882A JP 22692882 A JP22692882 A JP 22692882A JP S59118890 A JPS59118890 A JP S59118890A
Authority
JP
Japan
Prior art keywords
alkali metal
alkali
weight
molten salt
aqueous solution
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
JP22692882A
Other languages
Japanese (ja)
Other versions
JPH0416553B2 (en
Inventor
Isao Saito
齋藤 勇郎
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.)
PARKER SHOJI KK
Original Assignee
PARKER SHOJI KK
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 PARKER SHOJI KK filed Critical PARKER SHOJI KK
Priority to JP22692882A priority Critical patent/JPS59118890A/en
Publication of JPS59118890A publication Critical patent/JPS59118890A/en
Publication of JPH0416553B2 publication Critical patent/JPH0416553B2/ja
Granted 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
    • C23G1/28Cleaning or pickling metallic material with solutions or molten salts with molten salts

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  • 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)

Abstract

PURPOSE:To enable use of a liquid alkali and to reduce cost by using an aq. soln. consisting of specific concns. of alkali metal hydroxide and alkali metal nitrate and preparing the same into the soln. having the solute concn. in a specific range. CONSTITUTION:An aq. soln. of descaling agent used for replenishing oxidizing molten salt of alkali for removing metallic oxide scale is formed of a uniform aq. soln. consisting, by wt%, of 6-41.4 alkali metal hydroxide, 2.5-20 alkali metal nitrate, and the balance water and having 10-56.9 solute concn. Otherwise, said soln. is formed of a uniform aq. soln. consisting of 5.8-32.8 alkali metal hydroxide, 2.2-19.1 alkali metal nitrate, 0.4-4 alkali metal chloride and the balance water and having 10-50.3 solute concn. Sodium, more particularly a commercially marketed liquid sodium hydroxide having about 50% concn. is used as the alkali metal in terms of cost.

Description

【発明の詳細な説明】 この発明は、金属酸化物スケールを脱スケールするため
の酸化性アルカリ溶融塩の補給に用いられる、脱スケー
ル剤水浴故に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a descaling agent water bath used for replenishing oxidizing alkali molten salt for descaling metal oxide scale.

ステンレス鋼、チタン、耐熱鋼、スーパーアロイなどの
各種合金の熱処理時に生じる表面スケールを除去する方
法は良く知られており、組成、性能等についても米国特
許A2,458,661ならびに特公昭45−1800
1号公報等に詳しく述べられている。前記特公昭45−
18001号公報では、水酸化カリウムを含有させるこ
とによってスケール除去性能の向上及び塩浴粘度の低下
に役立つ作用があることが述べられている。
Methods for removing surface scales that occur during heat treatment of various alloys such as stainless steel, titanium, heat-resistant steel, and super alloys are well known, and the composition, performance, etc. are also covered by U.S. Patent A2,458,661 and Japanese Patent Publication No. 45-1800.
It is described in detail in Publication No. 1, etc. Said Special Public Service 1977-
Publication No. 18001 states that the inclusion of potassium hydroxide has the effect of improving scale removal performance and lowering the viscosity of the salt bath.

通常この溶融塩は100℃以上であって500℃にも達
する温度に保たれ、事実上無水の状態にあるので、補給
する塩が水分を含んでいると、高温の溶融塩に触れた瞬
間に水の気化による急激な体積膨張に伴なって水蒸気爆
発が起こり甚だ危険であるため、絶対的に無水の状態で
補給しなければならなかった。従って、この補給に用い
る塩の調合は、この塩を構成する成分を混合させるか、
または予め#I融混合した塩をフレーク状またはその他
の固形状にしたものを用いていた。しかし、補給が固形
のものだけに限定されるので、作業者が高温の状態にあ
る溶融塩に近づき補給作業を行なう場合、補給する基金
固形のまま投入することによって溶融塩が飛び散り、怪
我をする危険性がある。
Normally, this molten salt is kept at a temperature of 100°C or higher, reaching as high as 500°C, and is virtually anhydrous, so if the salt to be replenished contains water, the moment it comes into contact with the high-temperature molten salt, The rapid volumetric expansion caused by water evaporation caused a steam explosion, which was extremely dangerous, so it had to be replenished in an absolutely anhydrous state. Therefore, the preparation of the salt used for this supplementation is either by mixing the ingredients that make up this salt, or by
Alternatively, a #I melt-mixed salt in the form of flakes or other solid forms was used. However, since replenishment is limited to solid materials, when workers approach molten salt at high temperatures and replenish it, the molten salt may splatter and cause injury due to the solid state of the replenishing funds. There is a risk.

また、自動供給を行なう場合でも、この溶融塩の主成分
の一つであるアルカリ金属水酸化物、例えば水酸化ナト
リウム、水酸化カリヮムなどは潮解性があり、空気中に
放置した場合、水、炭酸ガスを吸収し、半浴解状態にな
ったり変質したりすルタめ、ホッパーやフィーダーによ
って自動供給するには難点があるなどの種々の問題があ
った。
Furthermore, even when automatic supply is performed, alkali metal hydroxides, such as sodium hydroxide and potassium hydroxide, which are one of the main components of this molten salt, are deliquescent, and if left in the air, water, There were various problems such as absorbing carbon dioxide gas, turning it into a semi-liquid state or changing its quality, and that it was difficult to automatically feed it with a hopper or feeder.

一方、米国特許A4,113.511においては、補給
に固形塩を使用せず溶融塩槽中へ水溶液の状態で補給す
る方法と装置が提案されているが、この方法を金属の表
面スケール除去に用いられる酸化性アルカリ溶融塩に適
用するに当って、補給すべき水溶液の具体的な組成、濃
度、温度等の条件は全く開示されていない。
On the other hand, U.S. Pat. In applying the oxidizing alkali molten salt to be used, conditions such as the specific composition, concentration, temperature, etc. of the aqueous solution to be replenished are not disclosed at all.

本発明は、前記米国性J′l’ JK 4 、113 
、511に開示された方法と装置を、金属の表面スケー
ル除去に用いる酸化性アルカリ1容融塩の補給に適用す
るに際し、補給すべき塩の水溶液の適用可能組成及び最
適組成、4度等の諸条件を定量的に設定し提供すること
を目的とするものである。
The present invention relates to the above-mentioned American J'l' JK 4, 113
, 511 is applied to the replenishment of oxidizing alkali 1 volume molten salt used for removing scale from the surface of metals, the applicable composition and optimal composition of the aqueous solution of the salt to be replenished, such as 4 degrees, etc. The purpose is to quantitatively set and provide various conditions.

まず、本発明者等は、種々の試験、研究ならびに検討の
結果、塩を水溶液として補給することによって自動供給
が可能になり、補給作業での危険性がなくなるといった
予期される効果の他に次のような効果が得られることが
判った。
First, as a result of various tests, studies, and studies, the present inventors have discovered that by replenishing salt in the form of an aqueous solution, automatic supply becomes possible, and in addition to the expected effects of eliminating danger during replenishment work, It was found that the following effects can be obtained.

溶融塩の主成分の一つであるアルカリ金属水酸化物、例
えば水酸化大トリウムや水酸化カリウムに化学工場で゛
曲解により液状に生成され、その後、請縮工程を経て濃
度50%前後の液状アルカリとして市販されているのが
一般であり、従来は補給する塩は無水状態であることを
妥求されていたため、更に濃縮により無水化されて1史
用されていた。
Alkali metal hydroxides, which are one of the main components of molten salt, such as thorium hydroxide and potassium hydroxide, are produced in a liquid form by bending in a chemical factory, and then undergo a compression process to form a liquid with a concentration of around 50%. Generally, it is commercially available as an alkali, and conventionally the salt to be supplied was required to be anhydrous, so it was further made anhydrous by concentration and used for a long time.

本発明の方法によれば、Tff販の液状−アルカリを便
用し、更に適宜権釈して利用できるため、液状アルカI
J ’]l−わざわδ無水の状態にするための煮詰め工
程が省かれることによって原料の製造コス°;・も低減
できるといった効果が得ら1することを昶りた。そこで
、これらの原料金1史用でき、尚且つ溶融塩に補給混合
さJl、たものの脱スケール性aLが良好な補給用脱ス
ケール剤水溶液の組成、濃度等の諸条件を見い出すべく
試験′f:重ねた結果、浴質として使用する脱スケール
剤の配合については、米国特許屋2,458.661な
らびに特公昭45−18001号公報で公知の組成の配
合割合がスケール除去性能において最も優れていること
が判った。しかし、濃度、温度については、組成が一定
の割合で補給される仁と、及びこの水溶液をスプレーす
るために用いる際にノズルづまりがないようにするため
、均一溶液となるための条件を満足させるためには適切
な濃度、温度を選定する必要が生じた。
According to the method of the present invention, liquid alkali sold by Tff can be conveniently used and can be used with appropriate modifications.
By omitting the boiling process to make the product anhydrous, the manufacturing cost of raw materials can be reduced. Therefore, an experiment was conducted to find conditions such as the composition and concentration of an aqueous solution of a replenishing descaling agent that can be used for these raw materials and has good descaling properties when mixed with molten salt. : As a result of repeated studies, regarding the formulation of the descaling agent used as the bath material, the formulation ratio of the composition known in U.S. Patent Office 2,458.661 and Japanese Patent Publication No. 18001/1983 was found to be the most excellent in terms of scale removal performance. It turned out that. However, the concentration and temperature must be adjusted to ensure that the composition is replenished at a constant rate, to prevent nozzle clogging when using this aqueous solution for spraying, and to satisfy the conditions for a uniform solution. Therefore, it became necessary to select an appropriate concentration and temperature.

史に、本発明で最も注目すべきことは、溶融塩にこの脱
スケール剤水M液を繰り返し補給混合を行なったものと
、従来の無水固形塩のみをm融したものとを用い、金属
製品の脱スケール性能を比較した場合、水溶液として補
給混合した場合のt15が、優れた脱スケール性能が得
られる仁とである。これは、脱スケール剤水溶液を繰り
返し補給混合した溶融塩を分析、検討を行なった結果、
溶融塩中に3〜5%の水分が存在しており、この水分に
よって事実上溶融塩の粘度が低下するので、スケールの
表面から内部に向って溶融塩の浸透が促進され、反応性
が良くなることに依るものと考えられる。また、この含
有水分は、脱スケール剤水溶液の補給混合の回数及び補
給量には殆ど影響されず、はぼ一定の割合を保つことが
わかった。
Historically, the most noteworthy feature of the present invention is that metal products can be manufactured by using a molten salt in which this descaling agent water M solution is repeatedly replenished and a conventional molten salt containing only anhydrous solid salt. When comparing the descaling performance of , t15 when replenishing and mixing as an aqueous solution is the one that provides excellent descaling performance. This is the result of analyzing and studying molten salt that has been repeatedly replenished with an aqueous descaling agent solution.
Molten salt contains 3 to 5% water, and this water effectively reduces the viscosity of the molten salt, promoting penetration of the molten salt from the surface of the scale to the inside, improving reactivity. I think it depends on what happens. Furthermore, it was found that this water content was hardly affected by the number of times and the amount of replenishment of the aqueous descaling agent solution, and maintained an approximately constant ratio.

これらのことから、下記に示される濃度範囲の脱スケー
ル剤水溶液を用いること(よジ、以上の効果が全て達成
されることができる。このための脱スケール剤水浴液と
しては次の三種に大別できる。
For these reasons, all of the above effects can be achieved by using a descaling agent aqueous solution with a concentration range shown below. We can separate.

■、アルカリ金属水酸化物及びアルカリ金属硝酸塩から
成る脱スケール剤水溶液 アルカリ金属水酸化物    6.0〜41.4重量%
アルカリ金属硝酸塩    2.5〜20.8重量%溶
質濃度       10.0〜56.9重量%温度範
囲(均一溶液にするための) 8〜65℃上記のアルカ
リ金属化合物としては、比較的コストの安い点から、通
常はナトリウム化合物を用いることが多い。
■ Descaling agent aqueous solution consisting of alkali metal hydroxide and alkali metal nitrate Alkali metal hydroxide 6.0 to 41.4% by weight
Alkali metal nitrate 2.5-20.8% by weight Solute concentration 10.0-56.9% by weight Temperature range (to make a homogeneous solution) 8-65°C Compared to the above alkali metal compounds, the cost is relatively low. For this reason, sodium compounds are usually used.

■、アルカリ金属水酸化物、アルカリ金網硝酸塩及びア
ルカリ金属塩化物から成る脱スケール剤水溶液 アルカリ金属水酸化物     5.8〜32.2重量
%アルカリ金属硝酸塩    2.2〜19.1重量%
アルカリ金属塩化物    0.4〜4.0重蓋%溶質
濃度       10.0〜50.5重蓋%@度範囲
(均一溶液にするための) 10〜65℃上記のアルカ
リ金属化合物としては、比較的コストの安い点から、通
常はナトリウム化合物を用いることが多い。
(2) Descaling agent aqueous solution consisting of alkali metal hydroxide, alkali wire mesh nitrate and alkali metal chloride Alkali metal hydroxide: 5.8-32.2% by weight Alkali metal nitrate: 2.2-19.1% by weight
Alkali metal chloride 0.4 to 4.0 % solute concentration 10.0 to 50.5 % (to make a homogeneous solution) 10 to 65°C For the above alkali metal compounds, comparison Sodium compounds are usually used because of their low cost.

■、ステンレス鋼、チタン及びチタン合金等のスケール
除去に優れた性能を持つ、水酸化カリウムをも上記組成
に加えた場合の脱スケール剤水溶液の組成を下記に示す
(2) The composition of an aqueous descaling agent solution in which potassium hydroxide is also added to the above composition, which has excellent performance in removing scales from stainless steel, titanium, titanium alloys, etc., is shown below.

水酸化ナトリウム、アルカリ金属硝酸塩、アルカリ金属
塩化物及び水酸化カリウムから成る脱スケール剤水溶液 水酸化ナトリウム     8.0〜38.6重量%ア
ルカリ金属硝酸塩      0.8〜5.8重t%ア
ルカリ金属塩化物      0.5〜5.8 Jii
%水酸化カリウム    0.8〜7.8重量%溶質a
度         10.1〜49.4重量%@度範
囲(均一溶液にするための)15℃〜50℃■の脱スケ
ール剤水溶液の必須成分として水酸化ナトリウムと共に
水酸化カリウムが共存することが必要であり、残りのア
ルカリ金属硝酸塩とアルカリ金属塩化物については比較
的コストの安い点から通常はナトリウム化合物を用いる
ことが多い。
Descaling agent aqueous solution consisting of sodium hydroxide, alkali metal nitrate, alkali metal chloride and potassium hydroxide Sodium hydroxide 8.0-38.6 wt% Alkali metal nitrate 0.8-5.8 wt% alkali metal chloride Things 0.5-5.8 Jii
% potassium hydroxide 0.8-7.8 wt% solute a
Potassium hydroxide must coexist with sodium hydroxide as an essential component of the descaling agent aqueous solution at a temperature of 10.1 to 49.4% by weight (to make a homogeneous solution) from 15 to 50 degrees Celsius. As for the remaining alkali metal nitrates and alkali metal chlorides, sodium compounds are usually used because of their relatively low cost.

上記三種類の脱スケール剤水溶液において、上記溶質濃
度がそれぞれの上限値以上では実用上杵される温度内で
均一な溶液は得られない。またそれぞれの下限値以下の
溶質濃度でも使用は可能ではあるが、便用量を増加する
ことになるので経済的に有利でない。
In the above three types of descaling agent aqueous solutions, if the above-mentioned solute concentration exceeds each upper limit, a uniform solution cannot be obtained within the temperature at which the solute is practically punched. Although it is possible to use solute concentrations below the respective lower limits, it is not economically advantageous because the amount of stool increases.

本発明の脱スケール剤水溶液を貯蔵しパイプなどにより
補給する場合は、上記温度範囲内に保つ必要がある。
When storing the descaling agent aqueous solution of the present invention and replenishing it through a pipe or the like, it is necessary to maintain the temperature within the above-mentioned temperature range.

次にこの発明の実施例について述べる。Next, embodiments of this invention will be described.

実施例1 リ 供試材:8U85Q4  冷延鋼板(1,5,1厚
)焼鈍績 上記供試材を次の条件によりデスケーリングを行ない、
最終仕上酸洗所要時間の比較によりデスケーリング性能
を判断した。
Example 1 - Test material: 8U85Q4 Cold rolled steel plate (1, 5, 1 thickness) annealing results The above test material was descaled under the following conditions,
Descaling performance was determined by comparing the time required for final pickling.

2)溶融塩組成及び条件 ■ 水酸化す) IJウム12,6kg(混合割合65
%)、硝酸す) IJウム2.4ゆく混合割合12%)
、塩化す) IJウム2に9(混合割合10%)、水酸
化カリウム5時(混合割合15%)、総量20klil
が溶融混合された組成の、脱スケール剤水溶液を補給し
ない従来の溶融塩。
2) Molten salt composition and conditions ■ Hydroxide) IJum 12.6 kg (mixing ratio 65
%), nitric acid) IJum 2.4 (mixing ratio 12%)
, chloride) IJum 2 to 9 (mixing ratio 10%), potassium hydroxide 5 parts (mixing ratio 15%), total amount 20 kli
Conventional molten salt without supplementing with an aqueous descaling agent solution.

処理温度:420℃及び450℃ ■ ■で建浴した溶融塩に、48%液状水酸化ナトリウ
ム13.1kp (固体混合割合63,0%)、硝酸す
) IJウム1.2kg(固体混合割合12%)、塩化
ナトリウム1kg(固体混合割合1o%)、48%液状
水酸化カリウム3.1 y (固体混合割合15%)、
水2.8 kg、総溶質濃度47.2%、溶液温度50
℃に加温保持して均一溶液となっている本発明の補給用
脱スケール剤水溶液を26.517ninの割合で6時
間補給して得られた溶融塩。
Treatment temperature: 420°C and 450°C ■ To the molten salt prepared at %), 1 kg of sodium chloride (solid mixture ratio 10%), 48% liquid potassium hydroxide 3.1 y (solid mixture ratio 15%),
2.8 kg of water, total solute concentration 47.2%, solution temperature 50
A molten salt obtained by replenishing the replenishing descaling agent aqueous solution of the present invention, which has become a homogeneous solution by maintaining the temperature at ℃, at a rate of 26.517 nin for 6 hours.

処理温度:420℃及び450°C 6)酸洗液 予備酸洗:硫酸  104.9 ’/1.50℃仕上酸
洗:硝弗酸 HN(J、 58.8F −HF5.4’
/7.22℃ リ 処理順序及び処理時間 塩浴処理(15秒)→急冷水洗→硫酸酸洗(60秒)→
水洗→硝弗酸酸洗(必要時間) 5)脱スケール結果 実施例2 1)供試材:8US450  冷延鋼板(0,7,I厚
)焼純済 2)、5)は実施例1と同じ り 処理順序及び処理時間 塩浴処理(4秒)→急冷水洗→硫酸酸洗(60秒)−水
洗→硝弗酸酸洗(必要時間) 5)脱スケール結果 実施例1及び2に示される如く、本発明の補給用脱スケ
ール剤水溶液により従来に比べ処理時間が短縮され、脱
スケール作用が非常に優れていることがわかった。
Processing temperature: 420°C and 450°C 6) Pickling liquid Pre-pickling: Sulfuric acid 104.9'/1.50°C Final pickling: Nitrofluoric acid HN (J, 58.8F -HF5.4'
/7.22°C Processing order and processing time Salt bath treatment (15 seconds) → Rapid cooling water washing → Sulfuric acid pickling (60 seconds) →
Water washing → Nitrofluoric acid pickling (required time) 5) Descaling results Example 2 1) Test material: 8US450 cold rolled steel plate (0, 7, I thickness) sintered and purified 2) and 5) are the same as Example 1. Same treatment order and treatment time Salt bath treatment (4 seconds) → Rapid cooling water washing → Sulfuric acid pickling (60 seconds) - Water washing → Nitrofluoric acid pickling (required time) 5) Descaling results are shown in Examples 1 and 2. As can be seen, it has been found that the replenishing descaling agent aqueous solution of the present invention shortens the processing time compared to the conventional method and has an extremely excellent descaling effect.

なお、lで示したアルカリ金属水酸化物とアルカリ金属
水酸化物から成る脱スケール剤水溶液及びMで示したア
ルカリ金属水酸化物、アルカリ金属硝酸塩とアルカリ金
属塩化物から成る脱スケール剤水溶液については、従来
の無水状態で使用する溶融塩でのデスケーリング性能が
判明しているため、脱スケール剤水溶液による補給につ
いては1の場合だけにとどめた。
In addition, regarding the descaling agent aqueous solution consisting of alkali metal hydroxide and alkali metal hydroxide indicated by l and the descaling agent aqueous solution consisting of alkali metal hydroxide, alkali metal nitrate and alkali metal chloride indicated by M, Since the descaling performance with the conventional molten salt used in an anhydrous state has been known, replenishment with an aqueous descaling agent solution was limited to case 1 only.

以上述べたごとく、本発明によって、従来の金属酸化物
を脱スケールする塔融塩の固形状態での補給の不便ざ、
補結作業の危険性等の問題点を全て解決できるというこ
とは勿論、市販の液状アルカリを原料として使用できる
ことによる低コスト化及び溶融塩に補給混合された場合
の脱スケール作用の向上などの優れた効果を発揮し、酸
洗処理時間の短縮による作業能率の向上が図れるという
ことから、この発明は金桝製造工業にとって極めて有益
なものといえる。
As described above, the present invention eliminates the inconvenience of replenishing the conventional tower molten salt for descaling metal oxides in a solid state.
Not only can it solve all problems such as the danger of supplementary work, but it also has advantages such as lower costs because it can use commercially available liquid alkali as a raw material, and improved descaling effect when mixed with molten salt. This invention can be said to be extremely beneficial to the metal box manufacturing industry because it exhibits the following effects and improves work efficiency by shortening the pickling treatment time.

代理人 弁理士  藤 本    礒 手続補正書 昭和58年2月9日 特許庁長官゛      殿 1、事件の表示 昭和57年 特 許 願第226928号3、 補正を
する者 事(Itとの関係  特許出願人 4、代 理 人  〒105  電話05−274−3
4666、 補正により増/Jlける発明の数7、補正
の対象 補正の内容 (リ 明細書第10頁第8行の「組成の、」を「組成の
溶融塩、即ち」と訂正する。
Agent Patent Attorney Isao Fujimoto Procedural Amendment February 9, 1980 Commissioner of the Patent Office 1. Indication of the case 1981 Patent Application No. 226928 3. Person making the amendment (Relationship with It) Patent application Person 4, Agent Address: 105 Telephone: 05-274-3
4666, Number of inventions increased by amendment 7, Contents of amendment subject to amendment (li) "Composition of" in line 8 of page 10 of the specification is corrected to "composition of molten salt, ie."

(2)同第10頁第10行の「処理温度:420℃及び
45,0℃」を削除する。
(2) Delete "Processing temperature: 420°C and 45.0°C" on page 10, line 10.

(3)同第11貞第1行の「処理温度=420℃及び4
50℃」を削除する。
(3) "Processing temperature = 420℃ and 4
50℃" is deleted.

(り同第12貞第4行〜第8行に掲げた表の次に、「実
施例3 1)は実施例1と同じ 2)溶融塩組成及び条件 ■ 水酸化す) IJウム15kg(混合割合75%)
、硝酸ナトリウムs kp (混合割合25%)、総量
20ゆが溶融混合された組成の溶融塩、即ち脱スケール
剤水浴液を補給しない従来の溶融塩。
(Next to the table listed in the 4th to 8th lines of the 12th edition of the same publication, it is written as follows: ``Example 3 1) Same as Example 1 2) Molten salt composition and conditions (75%)
, sodium nitrate s kp (mixing ratio 25%), a total amount of 20 g, is melt-mixed, i.e., a conventional molten salt without replenishing the descaling agent water bath solution.

■ ■で建浴した溶融塩に、48%液状水酸化す) I
Jウム15.6に9(固体混合割合75.0%)、硝酸
ナトリウム2.5 kill (固体混合割合25%)
、総溶質濃度55.2%、溶液温度50℃に加温保持し
て均一溶液となっている本発明の補給用脱スケール剤水
m液f:、26.5’/、。inの割合で6時間補給し
て得られたm融塩。
■ Add 48% liquid hydroxide to the molten salt prepared in ■) I
Jum 15.6 to 9 (solid mixture ratio 75.0%), sodium nitrate 2.5 kill (solid mixture ratio 25%)
, total solute concentration 55.2%, solution temperature maintained at 50° C. to become a homogeneous solution, replenishment descaling agent water m liquid f:, 26.5′/,. m molten salt obtained by replenishing at a rate of in for 6 hours.

3)、4)は実施例1と同じ 5)脱スケール結果 実施例4 1)は実施例1と同じ 2)溶融塩組成及び条件 ■ 水酸化す) IJウム12.8 klil (混合
割合64%)、硝酸ナトリウム6.2 ):p (混合
割合51%)、塩化ナトリウム1kg(混合割合5%)
、総量20kgが溶融混合された組成の溶融塩、即ち脱
スケール剤水溶液を補給しない従来の溶融塩。
3) and 4) are the same as Example 1 5) Descaling results Example 4 1) are the same as Example 1 2) Molten salt composition and conditions ■ Hydroxylation) IJum 12.8 klil (mixing ratio 64% ), sodium nitrate 6.2):p (mixing ratio 51%), sodium chloride 1kg (mixing ratio 5%)
A molten salt having a composition in which a total amount of 20 kg is melt-mixed, that is, a conventional molten salt without replenishing an aqueous descaling agent solution.

■ ■で建浴した溶融塩に、48%液状水酸化ナトリウ
ム13.3 kg(固体混合割合64.0%)、硝酸ナ
トリウム3.1 kg(固体混合割合31%)、塩化ナ
トIJウムo、sl(固体混合割合5%)、水3に9.
総溶質濃度50.2%、溶液温度64℃に加温保持して
均一浴液となっている本発明の補給用脱スケール剤水溶
液を26”/minの割合で6時間補給して得られたm
融塩。
■ To the molten salt prepared in ■, 13.3 kg of 48% liquid sodium hydroxide (solid mixture ratio 64.0%), sodium nitrate 3.1 kg (solid mixture ratio 31%), sodium chloride, sl (solid mixture ratio 5%), 9 parts to 3 parts water.
Obtained by replenishing the replenishing descaling agent aqueous solution of the present invention, which has a total solute concentration of 50.2% and a solution temperature of 64° C. to form a uniform bath solution, at a rate of 26”/min for 6 hours. m
Molten salt.

3)、りは実施例1と同じ 5)脱スケール結果 を挿入する。3), ri are the same as Example 1 5) Descaling results Insert.

(5)同第12頁第9行の「実施例1及び2に示される
如く、」を「実施例に示される如く、」と訂正する。
(5) On page 12, line 9, "as shown in Examples 1 and 2" is corrected to "as shown in the examples."

(6)同第12頁第13行〜第13頁第1行の「なお、
・・・・・・・・・とどめto」を削除する。
(6) “In addition,” from page 12, line 13 to page 13, line 1,
・・・・・・・・・Delete "Totome to".

Claims (1)

【特許請求の範囲】 (リ 金属酸化物スケールを脱スケールする酸化性アル
カIJ M融塩の補給に用いられる脱スケール剤水浴液
であって: アルカリ金属水酸化物6.0〜41.4重
量%と、アルカリ金嬉硝酸塩2.5〜20.8重量%と
残部が水から成り、溶質濃度が10.0〜56.9重量
%の均一水溶液にされていることを特徴とする脱スケー
ル水溶液。 (2)金属酸化物スケールを脱スケールする酸化性アル
カリ溶融塩の補給に用いられる脱スケール剤水、容液で
あって: アルカリ金属水酸化物5.8〜32.2重量
%と、アルカリ金椙硝酸塩2.2〜19.1重量%と、
アルカリ金属塩化物0,4〜4,0重量%と残部が水か
ら成り、溶質#度が10.0〜50.6重量%の均一水
溶液にされていることを特徴とする脱スケール剤水溶液
。 (3)  金属酸化物スケールを脱スケールする酸化性
アルカリ溶融塩の補給に用いられる脱スケール剤水溶液
であって: 水酸化ナトリウム8.0〜38.6重量%
と、アルカリ金拠硝酸塩068〜5.8i31%と、ア
ルカリ金属塩化物0.5〜5.8重i%と、水酸化カリ
ウム0.8〜7.8重敞%と残部が水から成り、溶質濃
度が10.1〜49.4重量%の均一水溶液にされてい
ることを特徴とする脱スケール剤水溶液。
[Scope of Claims] (Li) A descaling agent water bath liquid used for replenishing oxidizing alkali IJM molten salt for descaling metal oxide scale, comprising: 6.0 to 41.4 weight of alkali metal hydroxide %, alkali gold nitrate 2.5 to 20.8% by weight, and the remainder water, and the descaling aqueous solution is made into a uniform aqueous solution with a solute concentration of 10.0 to 56.9% by weight. (2) Descaling agent water or liquid used for replenishing oxidizing alkali molten salt for descaling metal oxide scale, comprising: 5.8 to 32.2% by weight of alkali metal hydroxide, and alkali Kanasu nitrate 2.2 to 19.1% by weight,
1. A descaling agent aqueous solution comprising 0.4 to 4.0% by weight of an alkali metal chloride and the balance being water, and having a solute degree of 10.0 to 50.6% by weight. (3) A descaling agent aqueous solution used for replenishing oxidizing alkali molten salt for descaling metal oxide scale, comprising: 8.0 to 38.6% by weight of sodium hydroxide.
, 31% by weight of alkali metal nitrate, 0.5 to 5.8% by weight of alkali metal chloride, 0.8 to 7.8% by weight of potassium hydroxide, and the balance is water, 1. A descaling agent aqueous solution, characterized in that it is a homogeneous aqueous solution having a solute concentration of 10.1 to 49.4% by weight.
JP22692882A 1982-12-27 1982-12-27 Aqueous solution of descaling agent for replenishing oxidizing molten salt of alkali Granted JPS59118890A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22692882A JPS59118890A (en) 1982-12-27 1982-12-27 Aqueous solution of descaling agent for replenishing oxidizing molten salt of alkali

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22692882A JPS59118890A (en) 1982-12-27 1982-12-27 Aqueous solution of descaling agent for replenishing oxidizing molten salt of alkali

Publications (2)

Publication Number Publication Date
JPS59118890A true JPS59118890A (en) 1984-07-09
JPH0416553B2 JPH0416553B2 (en) 1992-03-24

Family

ID=16852795

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22692882A Granted JPS59118890A (en) 1982-12-27 1982-12-27 Aqueous solution of descaling agent for replenishing oxidizing molten salt of alkali

Country Status (1)

Country Link
JP (1) JPS59118890A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60262985A (en) * 1984-06-06 1985-12-26 コ−リン・コ−ポレ−シヨン Alkali metal composition aqueous solution and supplying method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2458661A (en) * 1944-01-29 1949-01-11 J H Shoemaker Process of cleaning metal surfaces and compositions therefor
US4113511A (en) * 1977-01-17 1978-09-12 Shoemaker Robert H Liquid additions to fused chemical baths

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2458661A (en) * 1944-01-29 1949-01-11 J H Shoemaker Process of cleaning metal surfaces and compositions therefor
US4113511A (en) * 1977-01-17 1978-09-12 Shoemaker Robert H Liquid additions to fused chemical baths

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60262985A (en) * 1984-06-06 1985-12-26 コ−リン・コ−ポレ−シヨン Alkali metal composition aqueous solution and supplying method

Also Published As

Publication number Publication date
JPH0416553B2 (en) 1992-03-24

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