JPS6314065B2 - - Google Patents
Info
- Publication number
- JPS6314065B2 JPS6314065B2 JP22884383A JP22884383A JPS6314065B2 JP S6314065 B2 JPS6314065 B2 JP S6314065B2 JP 22884383 A JP22884383 A JP 22884383A JP 22884383 A JP22884383 A JP 22884383A JP S6314065 B2 JPS6314065 B2 JP S6314065B2
- Authority
- JP
- Japan
- Prior art keywords
- pickling
- acid
- metal
- pickling solution
- nox
- 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
Links
- 238000005554 pickling Methods 0.000 claims description 45
- 229910052751 metal Inorganic materials 0.000 claims description 18
- 239000002184 metal Substances 0.000 claims description 18
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 16
- 229910017604 nitric acid Inorganic materials 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 14
- IIACRCGMVDHOTQ-UHFFFAOYSA-N sulfamic acid group Chemical group S(N)(O)(=O)=O IIACRCGMVDHOTQ-UHFFFAOYSA-N 0.000 claims description 13
- 239000007789 gas Substances 0.000 claims description 11
- 150000001875 compounds Chemical class 0.000 claims description 10
- 239000002253 acid Substances 0.000 claims description 9
- FDDDEECHVMSUSB-UHFFFAOYSA-N sulfanilamide Chemical compound NC1=CC=C(S(N)(=O)=O)C=C1 FDDDEECHVMSUSB-UHFFFAOYSA-N 0.000 claims description 8
- 229940124530 sulfonamide Drugs 0.000 claims description 8
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 6
- 239000000243 solution Substances 0.000 description 22
- 239000007864 aqueous solution Substances 0.000 description 8
- 239000010935 stainless steel Substances 0.000 description 8
- 229910001220 stainless steel Inorganic materials 0.000 description 8
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- LNOPIUAQISRISI-UHFFFAOYSA-N n'-hydroxy-2-propan-2-ylsulfonylethanimidamide Chemical compound CC(C)S(=O)(=O)CC(N)=NO LNOPIUAQISRISI-UHFFFAOYSA-N 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- -1 ferrous metals Chemical class 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007769 metal material Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- QDWYPRSFEZRKDK-UHFFFAOYSA-M sodium;sulfamate Chemical class [Na+].NS([O-])(=O)=O QDWYPRSFEZRKDK-UHFFFAOYSA-M 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- RTQPZPWCYWVQCL-UHFFFAOYSA-N 1-[3-(2-methoxyethoxy)phenyl]piperazine Chemical compound COCCOC1=CC=CC(N2CCNCC2)=C1 RTQPZPWCYWVQCL-UHFFFAOYSA-N 0.000 description 1
- GEHMBYLTCISYNY-UHFFFAOYSA-N Ammonium sulfamate Chemical compound [NH4+].NS([O-])(=O)=O GEHMBYLTCISYNY-UHFFFAOYSA-N 0.000 description 1
- 229910001369 Brass Inorganic materials 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 229910000861 Mg alloy Inorganic materials 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 241000221561 Ustilaginales Species 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229910001448 ferrous ion Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 1
- KERTUBUCQCSNJU-UHFFFAOYSA-L nickel(2+);disulfamate Chemical compound [Ni+2].NS([O-])(=O)=O.NS([O-])(=O)=O KERTUBUCQCSNJU-UHFFFAOYSA-L 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 235000021110 pickles Nutrition 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
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
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/02—Cleaning or pickling metallic material with solutions or molten salts with acid solutions
- C23G1/08—Iron or steel
- C23G1/086—Iron or steel solutions containing HF
-
- 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
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/02—Cleaning or pickling metallic material with solutions or molten salts with acid solutions
- C23G1/10—Other heavy metals
- C23G1/103—Other heavy metals copper or alloys of copper
-
- 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
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/02—Cleaning or pickling metallic material with solutions or molten salts with acid solutions
- C23G1/10—Other heavy metals
- C23G1/106—Other heavy metals refractory metals
Description
〔産業上の利用分野〕
本発明は硝酸を含有する酸洗液で金属表面を酸
洗する方法に関する。
〔従来技術〕
高温加工や焼鈍を行なつた金属材料の表面には
酸化物のスケールが付着し、このスケールの除去
方法としては一般に硫酸、塩酸、燐酸または硝酸
等の無機酸による酸洗が行なわれている。
鉄鋼の酸洗には普通、温硫酸または冷塩酸水溶
液が使われるが炭素含有量の高い鋼やステンレス
鋼では酸洗後の金属表面に炭素が残つて所謂スマ
ツト(汚れ)と称せられるものが生じ易い。そこ
で特にステンレス鋼の酸洗には硝酸とフツ酸の混
液が用いられている。また硝酸は銅および真ちゆ
うあるいはマグネシウム合金等、非鉄金属の光沢
仕上げやアルミニウムおよびその合金のメツキ前
処理工程にも用いられている。
しかるに硝酸を含む酸液による金属の脱スケー
ルあるいは化学研磨等における問題点はNOxガ
スの激しい発生である。これは金属酸化物が溶け
たときに生成するHNO2が過飽和に達するとNO
とNO2の混合ガスが発生するためと考えられる。
このようなNOxが酸洗浴上の空気中に多量に含
まれて、そのまゝ大気中に放出されると直ちに環
境公害を生ずるので通常は湿式または乾式の脱硝
装置に導いて排気中のNOxの減少をはかつてい
る。
湿式脱硝法としてはアルカリ水溶液に吸収させ
る方法が一般的であるがタンク容量、吸収設備、
ブロワー等が大型化し、乾式脱硝法は酸化剤また
は還元剤等の薬剤の消耗が著しい。しかもこれら
の方法による場合、酸洗浴上の空気中のNOx濃
度は1500ppmが実用的限界である。
このように脱硝装置のみでは解決できないので
酸洗浴上に発生するNOx自体を減少させる方法
が試みられ例えば特開昭53−102232号に記載の如
く、浴中にスルフアミン酸を添加する方法がある
が、この方法は浴中に一時に多量のスルフアミン
酸が添加されてあるので多量のスルフアミン酸根
の存在下で酸洗が行なわれ酸洗後の金属表面にス
マツトが付着する。また過剰のスルフアミン酸と
亜硝酸との反応で生じた硫酸により浴中にFe2+
が存在し、使用後の酸洗液を廃棄する際にFe2+
をF3+に変換するためのエアレーシヨン(空気導
通による酸化処理)工程を要したり、また酸洗中
の酸洗浴に濃硝酸を補給する際に突沸現象が起る
という問題がある。
〔発明の目的〕
本発明は上記の問題点を解消し酸洗液中の
NOxの発生を抑制できる金属の硝酸洗方法の提
供を目的とするものである。
〔発明の構成〕
本発明者等は硝酸を含有する硝酸液中に存在す
るHNO2を消失させるためのスルフアミン酸根が
過剰にならなぬようにスルフアミン酸根化合物の
供給量を調節することにより酸洗浴上のNOxを
減少せしめ得ることを発見し、さらに研究を重ね
て本発明を完成した。
すなわち本発明の金属の硝酸酸洗方法は被酸洗
金属の表面積100m2当りスルフアミン酸根として
0.1ないし30Kgのスルフアミン酸根を有する化合
物を硝酸酸洗液中に少量づつ連続的または間欠的
に供給し、該酸洗液中にスルフアミン酸恨を残存
せしめないようにしたことを特徴とするものであ
る。
酸洗金属表面100m2当りのスルフアミン酸根が
0.1Kg以下では亜硝酸が酸洗液中に蓄積され下記
の反応式:
HNO2+NH2SO3 -→N2+H2SO4+OH-
で示されるような亜硝酸を直接、無害のN2に
変換する能力に不足する。また酸洗金属表面100
m2当りのスルフアミン酸根が30Kgを越えた場合に
はスルフアミン酸根を有する化合物の消耗費が増
加するばかりでなく酸洗液中に第一鉄イオンが生
成し空気吸込による酸化処理を要するなど経費増
加の原因となる。また未確認ではあるがステンレ
ス鋼等の表面につくスマツトの原因になるとも考
えられる。
一方、消費した硝酸分を追加するための濃硝酸
を時折、補給する必要があり、液中に多量のスル
フアミン酸根が残存した場合には突沸ガスの原因
となる。
このように酸洗液に添加するスルフアミン酸根
は被酸洗金属表面100m2当り0.1ないし30Kg、好ま
しくは1ないし10Kgである。
スルフアミン酸根を有する化合物としてはスル
フアミン酸及びその塩類、例えばスルフアミン酸
ナトリウム、−アンモニウム、−カリウム、−リチ
ウム、−カルシウム、−マグネシウム、−アルミニ
ウム、−ニツケル、−アルカノールアミン等の水溶
性塩及びスルフアミン酸尿素が挙げられる。
酸洗対象金属としてはステンレス鋼、チタン、
アルミニウム、銅等の金属またはその合金類が挙
げられる。
スルフアミン酸根を有する化合物を酸洗液中に
供給するには粉末のまゝ、または水溶液の形でよ
い。但し粉末を投入するには粉末供給機を必要と
し、設備費が高額になるうえ投入の際に酸洗液の
ミストが発生するという問題がある。これに対し
スルフアミン酸根を有する化合物は水に対する溶
解度が大きくて濃度の調整が容易なので水溶液と
して供給するのが有利である。因みにスルフアミ
ン酸根を有する主要化合物の25℃の水に対する溶
解度は次の通りである。
gr/100gr水
スルフアミン酸 23
スルフアミン酸ナトリウム 166
スルフアミン酸アンモニウム 193
スルフアミン酸ニツケル 70
スルフアミン酸バリウム 34.2
上記の如く1ないし50%水溶液が得られるが酸
洗液との水バランスから10ないし50%水溶液が好
ましく1%以下の濃度で添加するのは実際的でな
い。
スルフアミン酸根を有する化合物を水溶液まに
は粉体の形で酸洗液中に供給して金属表面を酸洗
するときに発生するNOxガス量は、酸洗液濃度、
酸洗液温度、金属材料の種類、酸洗スピード等に
より異なる。従つて酸洗液中のスルフアミン酸根
を0にまたは0に近い値に保てるように少量づつ
連続的に供給することが好ましいが、窒素酸化物
の発生量が少ない条件のものでは間欠的に供給す
ることもできる。
上記の如く、被酸洗金属の表面積100m2当りス
ルフアミン酸根含有化合物をスルフアミン酸根と
して0.1〜30Kg酸洗液に少量づつ加えると、酸洗
液中にスルフアミン酸根を殆ど存在させないでし
かもNOxガスの発生を浴上空気中1500ppm以下
に抑制できるが、この浴上の空気はそのまゝ大気
中に放出するには尚多量のNOxを含んでいる。
本発明は、上記の如く酸洗すると共に、この発生
NOxガスを含む浴上の空気を脱硝装置に導通す
ることによつて排ガス中のNOxを著しく減少せ
しめたものである。脱硝装置としては従来から使
われている型のもので充分であり、大型のものを
要しない。従つて、設備コストを低く済ませ得る
のみならず、酸洗スピードを高めても、浴上空気
中のNOx濃度は低いから通常の小型脱硝装置に
より効率よく脱硝することができる。
以下、実施例により本発明を説明する。
〔実施例〕
実施例1〜3及び6〜9
幅1.2m、厚さ1ないし5mmの帯状のステンレ
ス鋼を温度40ないし60℃の硝酸酸洗液を貯えた長
さ10mの縦長の酸洗槽中に10ないし30m/minの
速度で送り(滞留時間:20ないし60秒)該ステン
レス鋼に付着するスケールを除去した。酸洗液中
には7ないし18%のHNO3と2ないし4%のHF
が含まれており、さらに酸洗槽の所定の場所から
被酸洗金属表面積100m2当りスルフアミン酸根と
して0.5ないし10Kgのスルフアミン酸化合物を連
続的に供給した。
酸洗槽の上部はドラフトになつていてダクトを
介し、1500Nm3/hrの能力を有するブロワーで酸
洗槽の表面の空気を連続的に吸引し、3ないし6
%のNaOHの水溶液を吸収液とする脱硝装置に
より排気中のNOxを吸収除去した。下記の第1
表及び第2表に各実施例の酸洗条件と脱硝装置の
入口、出口におけるNOx濃度を示す。
次にスルフアミン酸根の供給量を本発明の範囲
外とした以外は前記実施例と同様な条件のもとで
酸洗を行ない比較例4〜5及び10〜11とした。そ
の結果を同じく下記の第1表及び第2表に記す。
[Industrial Application Field] The present invention relates to a method for pickling metal surfaces with a pickling solution containing nitric acid. [Prior art] Oxide scale adheres to the surface of metal materials that have been subjected to high-temperature processing or annealing, and the method for removing this scale is generally pickling with an inorganic acid such as sulfuric acid, hydrochloric acid, phosphoric acid, or nitric acid. It is. Warm sulfuric acid or cold hydrochloric acid aqueous solution is usually used to pickle steel, but with steel and stainless steel that have a high carbon content, carbon remains on the metal surface after pickling, causing what is called smut. easy. Therefore, a mixture of nitric acid and hydrofluoric acid is used especially for pickling stainless steel. Nitric acid is also used in the bright finishing of non-ferrous metals such as copper and brass or magnesium alloys, and in the pre-plating process of aluminum and its alloys. However, a problem with metal descaling or chemical polishing using an acid solution containing nitric acid is the intense generation of NOx gas. This is because when HNO 2 , which is produced when metal oxides melt, reaches supersaturation, NO
This is thought to be due to the generation of a mixed gas of NO 2 and NO 2 .
If a large amount of such NOx is contained in the air above the pickling bath and is released into the atmosphere, it will immediately cause environmental pollution, so normally a wet or dry denitrification device is introduced to remove NOx from the exhaust gas. It is on the decline. The common wet denitrification method is to absorb in an alkaline aqueous solution, but tank capacity, absorption equipment, etc.
As blowers and the like become larger, the dry denitrification method significantly consumes chemicals such as oxidizing agents and reducing agents. Moreover, when using these methods, the practical limit for the NOx concentration in the air above the pickling bath is 1500 ppm. Since this problem cannot be solved with a denitrification device alone, methods have been tried to reduce the NOx itself generated on the pickling bath. In this method, a large amount of sulfamic acid is added to the bath at once, so pickling is performed in the presence of a large amount of sulfamic acid groups, and smut adheres to the metal surface after pickling. In addition, sulfuric acid generated by the reaction between excess sulfamic acid and nitrous acid causes Fe 2+ in the bath.
exists, and when disposing of the pickling solution after use, Fe 2+
There are problems in that an aeration process (oxidation treatment through air passage) is required to convert F 3+ into F 3+ , and bumping occurs when concentrated nitric acid is supplied to the pickling bath during pickling. [Object of the invention] The present invention solves the above problems and improves the
The purpose of this invention is to provide a method for cleaning metal with nitric acid that can suppress the generation of NOx. [Structure of the Invention] The present inventors developed a pickling bath by adjusting the supply amount of a sulfamic acid group compound so that the sulfamic acid group for eliminating HNO 2 present in a nitric acid solution containing nitric acid did not become excessive. They discovered that the above NOx can be reduced, and after further research, they completed the present invention. In other words, the method of pickling metal with nitric acid of the present invention uses sulfamic acid radicals per 100 m2 of surface area of the metal to be pickled.
The method is characterized in that 0.1 to 30 kg of a compound having a sulfamic acid group is continuously or intermittently supplied into the nitric acid pickling solution in small amounts, so that no sulfamic acid residue remains in the pickling solution. be. Sulfamine acid radical per 100m2 of pickled metal surface
Below 0.1Kg, nitrous acid accumulates in the pickling solution, and the reaction formula is as follows: HNO 2 +NH 2 SO 3 - →N 2 +H 2 SO 4 +OH - The nitrite is directly converted into harmless N 2 . Lack of ability to convert. Also pickled metal surface 100
If the amount of sulfamic acid groups exceeds 30 kg per m2 , not only will the consumption cost of the compound with sulfamic acid groups increase, but also ferrous ions will be generated in the pickling solution, which will require oxidation treatment by air suction, which will increase costs. It causes Although unconfirmed, it is also thought to be the cause of smuts forming on the surfaces of stainless steel, etc. On the other hand, it is necessary to occasionally replenish concentrated nitric acid to replace the consumed nitric acid content, and if a large amount of sulfamic acid groups remain in the solution, this may cause bumping gas. The amount of sulfamine acid radical added to the pickling solution is 0.1 to 30 kg, preferably 1 to 10 kg, per 100 m 2 of the metal surface to be pickled. Examples of compounds having a sulfamic acid group include sulfamic acid and its salts, such as water-soluble salts of sodium sulfamate, -ammonium, -potassium, -lithium, -calcium, -magnesium, -aluminum, -nickel, and -alkanolamine, and sulfamic acid. Examples include urea. Metals to be pickled include stainless steel, titanium,
Examples include metals such as aluminum and copper, and alloys thereof. The compound having a sulfamic acid group may be supplied to the pickling solution in the form of a powder or in the form of an aqueous solution. However, a powder feeder is required to charge the powder, which increases the equipment cost and creates a mist of the pickling solution when the powder is charged. On the other hand, compounds having a sulfamic acid group have high solubility in water and the concentration can be easily adjusted, so it is advantageous to supply them as an aqueous solution. Incidentally, the solubility of the main compounds having a sulfamic acid group in water at 25°C is as follows. gr/100gr water Sulfamic acid 23 Sodium sulfamate 166 Ammonium sulfamate 193 Nickel sulfamate 70 Barium sulfamate 34.2 As mentioned above, a 1 to 50% aqueous solution can be obtained, but a 10 to 50% aqueous solution is preferable from the water balance with the pickling solution. It is impractical to add it at a concentration of less than 1%. The amount of NOx gas generated when a metal surface is pickled by supplying a compound having a sulfamic acid group to the pickling solution in the form of an aqueous solution or powder is determined by the concentration of the pickling solution,
It varies depending on the pickling solution temperature, type of metal material, pickling speed, etc. Therefore, it is preferable to continuously supply small amounts of sulfamine acid groups in the pickling solution to keep it at 0 or a value close to 0, but in cases where the amount of nitrogen oxides generated is small, it is preferably supplied intermittently. You can also do that. As mentioned above, if 0.1 to 30 kg of a sulfamine acid group-containing compound is added to the pickling solution little by little as sulfamine acid groups per 100 m2 of surface area of the metal to be pickled, almost no sulfamine acid groups will be present in the pickling solution, and NOx gas will be generated. However, the air above the bath still contains too much NOx to be released directly into the atmosphere.
The present invention not only performs pickling as described above, but also
By passing the air above the bath containing NOx gas through the denitration equipment, NOx in the exhaust gas is significantly reduced. As a denitrification device, a conventionally used type is sufficient, and a large one is not required. Therefore, not only can the equipment cost be reduced, but even if the pickling speed is increased, the NOx concentration in the air above the bath is low, so that the NOx can be efficiently removed using a conventional small-sized denitrification device. The present invention will be explained below with reference to Examples. [Example] Examples 1 to 3 and 6 to 9 A stainless steel strip with a width of 1.2 m and a thickness of 1 to 5 mm was placed in a vertical pickling tank with a length of 10 m in which a nitric acid pickling solution at a temperature of 40 to 60°C was stored. The scale adhering to the stainless steel was removed by feeding the stainless steel at a speed of 10 to 30 m/min (residence time: 20 to 60 seconds). 7 to 18% HNO 3 and 2 to 4% HF in the pickling solution
Furthermore, from a predetermined location in the pickling tank, 0.5 to 10 kg of a sulfamic acid compound was continuously supplied as a sulfamic acid radical per 100 m 2 of surface area of the metal to be pickled. The upper part of the pickling tank is a draft, and a blower with a capacity of 1500Nm 3 /hr continuously sucks air from the surface of the pickling tank through a duct.
NOx in the exhaust gas was absorbed and removed using a denitrification device using a % NaOH aqueous solution as the absorption liquid. 1st below
Table 2 shows the pickling conditions and NOx concentrations at the inlet and outlet of the denitrification equipment for each example. Comparative Examples 4 to 5 and 10 to 11 were then carried out under the same conditions as in the above Example except that the amount of sulfamic acid radicals supplied was outside the range of the present invention. The results are also shown in Tables 1 and 2 below.
【表】【table】
上記の如く本発明方法により酸洗液に添加する
スルフアミン酸根化合物の供給量を調節すること
によりNOxガスの発生を抑制することができ、
脱硝装置としては容量の増大を要しながら製造コ
スト節減の効果がある。従つて本発明はステンレ
ス鋼にとゞまらずアルミ、銅、チタンまたはそれ
らの合金等の酸洗にも適用し得るものである。
As described above, the generation of NOx gas can be suppressed by adjusting the supply amount of the sulfamine acid group compound added to the pickling solution according to the method of the present invention,
As a denitrification device, it has the effect of reducing manufacturing costs even though it requires an increase in capacity. Therefore, the present invention can be applied to pickling not only stainless steel but also aluminum, copper, titanium, and alloys thereof.
Claims (1)
ン酸根として0.1ないし30Kgのスルフアミン酸根
を有する化合物を硝酸酸洗液中に、少量づつ連続
的にまたは間欠的に供給し、該酸洗液中にスルフ
アミン酸根を残存せしめないようにすると共に、
発生した窒素酸化物ガスを含有する酸洗液上の空
気を脱硝装置に導通することを特徴とする金属の
硝酸酸洗方法。1. Continuously or intermittently feed a compound having 0.1 to 30 kg of sulfamic acid groups into a nitric acid pickling solution per 100 m2 of surface area of the metal to be pickled, and add sulfamine to the pickling solution. In addition to preventing acid roots from remaining,
A method for pickling metal with nitric acid, characterized in that air above a pickling solution containing generated nitrogen oxide gas is passed through a denitrification device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22884383A JPS60121283A (en) | 1983-12-03 | 1983-12-03 | Method for pickling metal with nitric acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22884383A JPS60121283A (en) | 1983-12-03 | 1983-12-03 | Method for pickling metal with nitric acid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60121283A JPS60121283A (en) | 1985-06-28 |
JPS6314065B2 true JPS6314065B2 (en) | 1988-03-29 |
Family
ID=16882730
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22884383A Granted JPS60121283A (en) | 1983-12-03 | 1983-12-03 | Method for pickling metal with nitric acid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60121283A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110079854A (en) * | 2019-04-14 | 2019-08-02 | 广州恒荣电子科技有限公司 | A kind of environment-friendly type nitric acid fog inhibitor |
-
1983
- 1983-12-03 JP JP22884383A patent/JPS60121283A/en active Granted
Also Published As
Publication number | Publication date |
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JPS60121283A (en) | 1985-06-28 |
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