JPH0478420A - Method for preventing corrosion of stainless steel for stack gas desulfurizer - Google Patents
Method for preventing corrosion of stainless steel for stack gas desulfurizerInfo
- Publication number
- JPH0478420A JPH0478420A JP2190834A JP19083490A JPH0478420A JP H0478420 A JPH0478420 A JP H0478420A JP 2190834 A JP2190834 A JP 2190834A JP 19083490 A JP19083490 A JP 19083490A JP H0478420 A JPH0478420 A JP H0478420A
- Authority
- JP
- Japan
- Prior art keywords
- corrosion
- stainless steel
- manganese
- absorbent
- manganese oxide
- 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.)
- Pending
Links
- 230000007797 corrosion Effects 0.000 title claims abstract description 27
- 238000005260 corrosion Methods 0.000 title claims abstract description 27
- 229910001220 stainless steel Inorganic materials 0.000 title claims abstract description 19
- 239000010935 stainless steel Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title claims description 11
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 claims abstract description 35
- 238000010521 absorption reaction Methods 0.000 claims abstract description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000001301 oxygen Substances 0.000 claims abstract description 15
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 15
- 238000007664 blowing Methods 0.000 claims abstract description 11
- 239000007789 gas Substances 0.000 claims abstract description 8
- 150000002696 manganese Chemical class 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 7
- 238000006477 desulfuration reaction Methods 0.000 claims description 7
- 230000023556 desulfurization Effects 0.000 claims description 7
- 239000003546 flue gas Substances 0.000 claims description 7
- 239000011508 lime plaster Substances 0.000 claims description 3
- 239000011572 manganese Substances 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 10
- 230000001590 oxidative effect Effects 0.000 abstract description 5
- 229910052748 manganese Inorganic materials 0.000 abstract description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 abstract description 3
- 239000011248 coating agent Substances 0.000 abstract description 3
- 238000000576 coating method Methods 0.000 abstract description 3
- 239000000706 filtrate Substances 0.000 abstract description 2
- 238000005086 pumping Methods 0.000 abstract description 2
- 230000002745 absorbent Effects 0.000 abstract 4
- 239000002250 absorbent Substances 0.000 abstract 4
- 229910000831 Steel Inorganic materials 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000010959 steel Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 8
- 238000007689 inspection Methods 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 3
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 150000001805 chlorine compounds Chemical class 0.000 description 3
- 238000005536 corrosion prevention Methods 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 206010021143 Hypoxia Diseases 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229940043430 calcium compound Drugs 0.000 description 2
- 150000001674 calcium compounds Chemical class 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910000856 hastalloy Inorganic materials 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 150000002697 manganese compounds Chemical class 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910001069 Ti alloy Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- PPNAOCWZXJOHFK-UHFFFAOYSA-N manganese(2+);oxygen(2-) Chemical class [O-2].[Mn+2] PPNAOCWZXJOHFK-UHFFFAOYSA-N 0.000 description 1
- GEYXPJBPASPPLI-UHFFFAOYSA-N manganese(III) oxide Inorganic materials O=[Mn]O[Mn]=O GEYXPJBPASPPLI-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Chemical Treatment Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は石灰石膏法による排煙脱硫装置に用いられるス
テンレス鋼の防食方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for preventing corrosion of stainless steel used in flue gas desulfurization equipment using the lime plaster method.
石灰石膏法による排煙脱硫装置の吸収液には排煙中に含
まれる塩素化合物あるいは供給水(例えば工業用水、海
水)中に含まれる塩化物が蓄積し、ステンレス鋼の孔食
、デポジットアタックあるいは隙間腐食が発生して問題
となっている。このた約、従来は塩化物腐食の影響の少
ない高級ステンレス銅又はハステロイ〔さなどのニッケ
ル基合金あるいはチタン系合金などの使用あるいはゴム
ライニング又は樹脂ライニング等が用いられている。Chlorine compounds contained in flue gas or chlorides contained in supply water (e.g. industrial water, seawater) accumulate in the absorption liquid of flue gas desulfurization equipment using the lime plaster method, causing pitting corrosion of stainless steel, deposit attack, and Crevice corrosion has occurred, which has become a problem. To prevent this, conventionally, high-grade stainless copper, which is less affected by chloride corrosion, nickel-based alloys such as Hastelloy, titanium-based alloys, or rubber linings or resin linings have been used.
従来技術のうち、高級ステンレス鋼、ニッケル基合金、
チタン系合金などの材料は価格が高く装置建設費が高価
になる。すなわち、吸収液中の塩化物濃度が高くなる程
、高価な金属材料を選定使用する必要がある。一方、ゴ
ム及び樹脂ライニングでは施工不良に起因する欠陥の発
生、スラリ摩耗など耐久性の面で償頼性に欠けることも
多い。Among conventional technologies, high-grade stainless steel, nickel-based alloys,
Materials such as titanium alloys are expensive and equipment construction costs are high. That is, the higher the chloride concentration in the absorption liquid, the more expensive metal materials need to be selected and used. On the other hand, rubber and resin linings often lack reliability in terms of durability, such as defects caused by poor construction and slurry wear.
本発明はかかる欠点を解消するため、安価なステンレス
鋼を使用しても孔食あるいは隙間腐食等が防止できる防
食方法を提案しようとするものである。In order to eliminate such drawbacks, the present invention attempts to propose a corrosion prevention method that can prevent pitting corrosion, crevice corrosion, etc. even when inexpensive stainless steel is used.
本発明は弱酸性の前記吸収液に接するステンレス鋼の表
面に酸化性の被膜を形成させ、低級なステンレス銅であ
っても孔食、デポジットアタック及び隙間腐食を防止で
きる防食方法を提供するものであって、本発明は、前記
吸収液中に酸素を含むガスを吹き込みながら、1■/1
以上のマンガン塩を添加することにより、前記防食性に
秀れた酸化性の酸化マンガンを主体とする防食被膜をス
テンレス鋼表面に形成させて防食する方法である。The present invention provides a corrosion prevention method that forms an oxidizing film on the surface of stainless steel that comes into contact with the weakly acidic absorption liquid, thereby preventing pitting corrosion, deposit attack, and crevice corrosion even on low-grade stainless steel copper. Therefore, in the present invention, while blowing a gas containing oxygen into the absorption liquid,
This is a method of preventing corrosion by adding the above manganese salt to form an anticorrosive coating mainly composed of oxidizing manganese oxide, which has excellent anticorrosive properties, on the surface of stainless steel.
一般に、塩化物を含む弱酸性溶液中において、ステンレ
ス鋼の孔食、デポジットアタック及び隙間腐食はステン
レス鋼の表面に形成されている金属成分の酸化物からな
る不働態被膜の不均一性に起因する酸素濃淡電池、デポ
ジット部の酸素欠乏に起因する酸素濃淡電池、隙間部の
酸素欠乏に起因する酸素濃淡電池の形成によって生じる
が、塩化物が含まれる場合には前記腐食部にC1−イオ
ンが拡散し、更にH+が拡散するた約1腐食部のpHが
漸次低下し、腐食がますまず加速されると言われている
。In general, pitting corrosion, deposit attack, and crevice corrosion of stainless steel in weakly acidic solutions containing chlorides are caused by the non-uniformity of the passive film formed on the surface of the stainless steel, which is made of oxides of metal components. This occurs due to the formation of an oxygen concentration battery, an oxygen concentration battery due to oxygen deficiency in the deposit area, and an oxygen concentration battery due to oxygen deficiency in the gap, but if chloride is included, C1- ions diffuse into the corroded area. However, it is said that due to further diffusion of H+, the pH of approximately one corroded area gradually decreases, and corrosion is accelerated.
本発明の酸化マンガンの被膜は前記腐食の防止に次の作
用を有する。The manganese oxide film of the present invention has the following effect on preventing the above-mentioned corrosion.
酸化マンガンは酸化性があり、前記酸素欠乏部に酸素を
供給することにより、ステンレス鋼表面の不働態被膜を
強固にして酸素濃淡電池の形成を防止する作用を有する
。更に本発明で形成される酸化マンガン被膜はMnLが
主成分で、その他にMn2D3 、 MnOなどが含ま
れるが、前記酸素欠乏部に酸素を供給したあとは、例え
ばMnLは還元されで、MnJs 、 MnOに変化し
、腐食が生じやすい個所ではMn20s 、 Mn[l
が増加するが、Mn2O3は弱塩基性、Mn[]は塩基
性を示す酸化物であり、腐食部にC1−が拡散しp)l
が低下するのに対して、中和する作用及び塩基性にする
作用を有し腐食を抑制する。Manganese oxide has an oxidizing property, and by supplying oxygen to the oxygen-deficient portion, it has the effect of strengthening the passive film on the surface of the stainless steel and preventing the formation of an oxygen concentration battery. Furthermore, the main component of the manganese oxide film formed in the present invention is MnL, and also contains Mn2D3, MnO, etc., but after supplying oxygen to the oxygen-deficient area, for example, MnL is reduced and becomes MnJs, MnO. In places where corrosion is likely to occur, Mn20s, Mn[l
increases, but Mn2O3 is weakly basic and Mn[] is an oxide that shows basicity, and C1- diffuses into the corroded area, resulting in p)l
It has a neutralizing effect and a basicizing effect and suppresses corrosion.
6本発明の酸化マンガン被膜は酸素を含むガスを吹き込
むことによって、添加したマンガン塩が酸化され、不溶
性の酸化マンガンが析出することによって形成される。6. The manganese oxide film of the present invention is formed by blowing oxygen-containing gas into the film, whereby the added manganese salt is oxidized and insoluble manganese oxide is precipitated.
吹き込まれる酸素は前記酸化マンガンの析出に作用する
だけでなく、ステンレス鋼表面に形成された酸化マンガ
ンがステンレス鋼の酸化によって低価の酸化物に変るが
、この低価の酸化物と反応し再び高価の酸化物に変える
作用をも有する。従って、酸素を含むガスを常時吹き込
むことにより、ステンレス鋼の表面に形成した酸化マン
ガン被膜の酸化性を維持できるのである。The blown oxygen not only acts on the precipitation of the manganese oxide, but also the manganese oxide formed on the stainless steel surface changes into a low-value oxide by oxidation of the stainless steel, and reacts with this low-value oxide and regenerates. It also has the effect of converting it into expensive oxides. Therefore, by constantly blowing oxygen-containing gas into the stainless steel, the oxidizing properties of the manganese oxide film formed on the surface of the stainless steel can be maintained.
マンガン塩は装置運転初期において、酸化マンガン被膜
を早く形成させるた約高濃度で添加するのが望ましいが
、酸化マンガン被膜形成後には1 ppm程度添加すれ
ば防食効果を維持できる。マンガン塩は連続的に添加す
ること、間欠的に添加することもできる。It is desirable to add manganese salt at a high concentration in the early stage of equipment operation in order to quickly form a manganese oxide film, but after the manganese oxide film is formed, the anticorrosion effect can be maintained by adding about 1 ppm. Manganese salt can be added continuously or intermittently.
本発明を第1図の態様をなす一実施例を用いて具体的に
説明する。The present invention will be specifically explained using an embodiment shown in FIG.
第1図において、SO3を含んだ排ガスaは吸収塔1内
でカルシウム化合物を含有する吸収液と気液接触処理さ
れ脱硫されて吸収塔1から清浄排ガスbとして排出され
る。該吸収塔1内でSO3を亜硫酸塩として吸収した吸
収液は吸収塔1下部の循環タンク2中に落下する。該タ
ンク2内には前記亜硫酸塩を酸化して石膏化するために
空気供給ライン3より空気が吹き込まれている。In FIG. 1, an exhaust gas a containing SO3 is subjected to gas-liquid contact treatment with an absorption liquid containing a calcium compound in an absorption tower 1, is desulfurized, and is discharged from the absorption tower 1 as a clean exhaust gas b. The absorption liquid that has absorbed SO3 as sulfite in the absorption tower 1 falls into the circulation tank 2 at the bottom of the absorption tower 1. Air is blown into the tank 2 from an air supply line 3 in order to oxidize the sulfite and turn it into gypsum.
上記態様の湿式排煙脱硫装置において、5Oa1200
ppmを含んだ温度110℃の燃焼排ガスを毎時20
.0008m’吸収塔1に導入し、カルシウム化合物L
2 mol/i含有し、且つMn〜イオン2■/1含
有した吸収液を毎時350m3吸収ifI内に散布して
脱硫させ、該吸収塔1落下吸収液を貯留させる容積15
m3の循環タンク2には空気吹込ライン3から毎時30
0m’の空気を吹き込み、吸収塔1内でSO2の吸収に
よって生成した亜硫酸塩を酸化させている。さらに吸収
塔循環タンク2には該タンク2貯留吸収液の固相Mn化
合物を除いた濾液中のMn”+イオンが2■/1以上と
なるように管理分析を行い、間欠又は連続してマンガン
化合物の溶液を配管5から注入した。定常状態運転時に
は補給水と抜取り水量を調整して吸収液中のCI−濃度
が25.000ppmになるように運転した。In the wet flue gas desulfurization apparatus of the above aspect, 5Oa1200
Combustion exhaust gas containing ppm at a temperature of 110°C is generated at 20°C per hour.
.. 0008m' is introduced into the absorption tower 1, and the calcium compound L
The absorption liquid containing 2 mol/i and Mn ~ ion 2 /1 is sprayed every hour into 350 m3 of absorption ifI for desulfurization, and the volume 15 in which the absorbed liquid falling from the absorption tower 1 is stored is
30 m3 per hour from the air blowing line 3 to the circulation tank 2.
0 m' of air is blown into the absorption tower 1 to oxidize the sulfite produced by absorption of SO2. Furthermore, in the absorption tower circulation tank 2, control analysis is performed so that the Mn''+ ions in the filtrate excluding the solid phase Mn compounds of the absorption liquid stored in said tank 2 are 2■/1 or more, and manganese is A solution of the compound was injected through pipe 5. During steady state operation, the amounts of make-up water and water taken out were adjusted so that the CI concentration in the absorption liquid was 25.000 ppm.
以上の条件で運用されてなる実施態様例の第1図の循環
タンク2、空気吹込ライン3、吸収塔1への吸収液の揚
液ラインとしての配管7の材質としてオーテスナイト系
5IIS 304を用いて連続運転を行い、約700時
間経過時と8000時間経過時に開放点検を行った。約
700時間経過後の開放点検では前記循環タンク2、配
管7の各内壁及び空気吹込ライン3の表面に暗褐色のマ
ンガン酸化物が極く薄く沈着した状態が見られ、0.0
1 mm程度の孔食が認められた。引続き、8000時
間運転後の開放点検では暗褐色のマンガン酸化物の被膜
が強固に形成されており、該マンガン酸化物を洗浄除去
後材料表面の状態を調査した結果、約700時間経過時
の状態と同等で腐食の進行は認約られなかった。なお、
第1図中、6は循環ポンプである。In the example of the embodiment operated under the above conditions, the material of the circulation tank 2, the air blowing line 3, and the piping 7 serving as the pumping line for the absorption liquid to the absorption tower 1 in FIG. Continuous operation was performed, and overhaul inspections were conducted after approximately 700 hours and 8,000 hours had passed. After about 700 hours, an open inspection revealed that a very thin layer of dark brown manganese oxide had been deposited on the inner walls of the circulation tank 2, the piping 7, and the surface of the air blowing line 3.
Pitting corrosion of approximately 1 mm was observed. Subsequently, an open inspection after 8,000 hours of operation revealed that a dark brown manganese oxide film had formed firmly, and after washing and removing the manganese oxide, the condition of the material surface was investigated and the condition after approximately 700 hours had elapsed. The corrosion progress was not observed. In addition,
In FIG. 1, 6 is a circulation pump.
前記実施例と同装置で、マンガン化合物を注入しない条
件を除いては同条件で連続運転を行い、約700時間経
過後点検を行った結果、前記循環タンク2配管7の各内
壁及び空気吹込ライン3の材料には厳しい孔食が認とら
れた。The same equipment as in the above example was operated continuously under the same conditions except that the manganese compound was not injected, and an inspection was performed after about 700 hours. As a result, the inner walls of the circulation tank 2 piping 7 and the air blowing line were Severe pitting corrosion was observed in material No. 3.
(孔食深さ]、、 5 mmに達するものもあった。)
又、前記実施例と同仕様の装置で、マンガン化合物は注
入したが空気を吹込まない条件で、1000時間運転後
開放点検した結果、材料表面へのマンガン酸化物の付着
は全く認められず、材料の腐食状態は前記マンガンを添
加しなかった場合と同等の孔食を生じていた。(The depth of pitting corrosion reached 5 mm in some cases.)
In addition, as a result of an open inspection after 1000 hours of operation using a device with the same specifications as in the above example, injecting a manganese compound but not blowing air, no adhesion of manganese oxides to the material surface was observed. The corroded state of the material was pitting corrosion equivalent to the case where no manganese was added.
実施例に示したように本発明の防食方法を適用しない場
合には装置に用いる材料はハステロイC276等の高級
材料を用いなければ孔食、デポジットアタックあるいは
隙間腐食に耐えるのは難しい。本発明では5IJS 3
04 、 SO83]、6等の安価なステンレス鋼の仕
様が可能となり、その経済的効果は大きい。As shown in the examples, when the corrosion prevention method of the present invention is not applied, it is difficult to resist pitting corrosion, deposit attack, or crevice corrosion unless the material used for the device is a high-quality material such as Hastelloy C276. In the present invention, 5IJS 3
It becomes possible to use inexpensive stainless steels such as 04, SO83] and 6, which has a large economical effect.
第1図は本発明の詳細な説明するための概略図である。 第1 図 FIG. 1 is a schematic diagram for explaining the present invention in detail. Figure 1
Claims (1)
に酸素を含むガスを吹込みながら、該吸収液中に1mg
/l以上のマンガン塩を添加し、該排煙脱硫装置に用い
たステンレス鋼の表面に酸化マンガンを主成分とする被
膜を形成させることを特徴とする排煙脱硫装置用ステン
レス鋼の防食方法。While blowing oxygen-containing gas into the absorption liquid circulation tank of the flue gas desulfurization equipment using the lime plaster method, 1 mg of oxygen was added to the absorption liquid.
1. A method for preventing corrosion of stainless steel for flue gas desulfurization equipment, the method comprising: adding manganese salt in an amount of /l or more to form a film containing manganese oxide as a main component on the surface of the stainless steel used for the flue gas desulfurization equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2190834A JPH0478420A (en) | 1990-07-20 | 1990-07-20 | Method for preventing corrosion of stainless steel for stack gas desulfurizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2190834A JPH0478420A (en) | 1990-07-20 | 1990-07-20 | Method for preventing corrosion of stainless steel for stack gas desulfurizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0478420A true JPH0478420A (en) | 1992-03-12 |
Family
ID=16264541
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2190834A Pending JPH0478420A (en) | 1990-07-20 | 1990-07-20 | Method for preventing corrosion of stainless steel for stack gas desulfurizer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0478420A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115999349A (en) * | 2022-10-25 | 2023-04-25 | 上海电气集团国控环球工程有限公司 | Sulfur black tail gas alkali liquor absorption tower with anti-corrosion function |
-
1990
- 1990-07-20 JP JP2190834A patent/JPH0478420A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115999349A (en) * | 2022-10-25 | 2023-04-25 | 上海电气集团国控环球工程有限公司 | Sulfur black tail gas alkali liquor absorption tower with anti-corrosion function |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP1106237B1 (en) | Method of treating waste waters from a flue gas desulphuriser | |
| Özer et al. | A study on the Cr (VI) removal from aqueous solutions by steel wool | |
| KR100325571B1 (en) | REMOVAL OF NOx AND SOx EMISSIONS FROM PICKLING LINES FOR METAL TREATMENT | |
| JP3790383B2 (en) | Treatment method of flue gas desulfurization waste water | |
| US20170334752A1 (en) | Sulfate reduction in flue gas desulfurization system by barium precipitation | |
| JP3358926B2 (en) | Method for controlling oxidation of sulfite in flue gas desulfurization method | |
| DK153056B (en) | PROCEDURE FOR ABSORPTION OF SULFUR OXIDES FROM SEA GAS | |
| KR100848286B1 (en) | Antiscaling Agent and Descaling Method for Desulfurization Wastewater Treatment System Using Sodium Hypochlorite as Main Treatment | |
| JPH0824566A (en) | Method for controlling oxidation of sulfite | |
| JP2011072940A (en) | Treatment method of reducing selenium-containing waste water | |
| JP2014104430A (en) | Corrosion prevention method of sea water desulfurizer | |
| JP3473444B2 (en) | Method for treating chromium oxide-containing material | |
| JP3572233B2 (en) | Flue gas desulfurization method and flue gas desulfurization system | |
| US3349031A (en) | Method and composition for removal of manganese from water | |
| JP4415449B2 (en) | Method for producing surface-treated steel with excellent weather resistance | |
| EP3813983B1 (en) | Method for scrubbing chlorine-containing gases | |
| JPH11290643A (en) | Removal of acidic component of combustion gas by sea water | |
| ES2527424T3 (en) | Method in relation to steel production | |
| CA2055002C (en) | Method and apparatus for the removal of constituents from a waste gas | |
| KR20020049478A (en) | alkali recovering agent having corrosion inhibitor in reinforced concrete structure | |
| JP2004275795A (en) | How to remove sulfite ions | |
| WO2001041902A1 (en) | A process to increase the oxidation rate of dissolved sulphur dioxide in seawater | |
| EP0162491B1 (en) | Process for inhibiting corrosion of a metallic mass in contact with an acidic bath containing ferric ions | |
| JPS63137734A (en) | Fluorine control-type wet exhaust gas desulfurizer | |
| JPH09279371A (en) | Chemically cleaning method |