JPS5849593B2 - Method for cleaning sulfur-adhered blockages in coke oven gas desulfurization equipment - Google Patents
Method for cleaning sulfur-adhered blockages in coke oven gas desulfurization equipmentInfo
- Publication number
- JPS5849593B2 JPS5849593B2 JP55063188A JP6318880A JPS5849593B2 JP S5849593 B2 JPS5849593 B2 JP S5849593B2 JP 55063188 A JP55063188 A JP 55063188A JP 6318880 A JP6318880 A JP 6318880A JP S5849593 B2 JPS5849593 B2 JP S5849593B2
- Authority
- JP
- Japan
- Prior art keywords
- coke oven
- oven gas
- blockages
- cleaning
- adhered
- 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
Landscapes
- Treating Waste Gases (AREA)
- Industrial Gases (AREA)
Description
【発明の詳細な説明】
本発明はコークス炉ガス脱硫設備の硫黄付着閉塞物の洗
浄方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for cleaning sulfur-adhered blockages in coke oven gas desulfurization equipment.
従来コークス炉ガス中の硫化水素を除去するレドツクス
反応型の湿式脱硫法に於では、触媒を含む吸収液とガス
を接触させて硫化水素を吸収液に吸収させる工程と、そ
の硫化水素を吸収した吸収液に酸素を含むガスと接触さ
せ、硫化水素を単体硫黄まで酸化すると同時に吸収液の
アルカリと触媒を再生する工程とから戒り立っている。Conventionally, the redox reaction type wet desulfurization method for removing hydrogen sulfide from coke oven gas involves the process of bringing gas into contact with an absorption liquid containing a catalyst to absorb hydrogen sulfide into the absorption liquid, and the process of absorbing the hydrogen sulfide. The process involves bringing the absorption liquid into contact with a gas containing oxygen, oxidizing hydrogen sulfide to elemental sulfur, and at the same time regenerating the alkali and catalyst in the absorption liquid.
ところがこの吸収液とガスが接触する工程ではガス中に
微量の油分や不飽和炭化水素を含むためこれらの物質が
単体硫黄と粘性の混合物或はガム質を形成し、脱硫塔の
充填層や熱交換器などに強固に付着して閉塞現象を起し
、ついには脱硫が不能となることがあった。However, in the process where the absorbing liquid and gas come into contact, the gas contains trace amounts of oil and unsaturated hydrocarbons, and these substances form a viscous mixture or gum with elemental sulfur, which can cause damage to the packed bed of the desulfurization tower and heat. In some cases, it adheres strongly to exchangers and other parts, causing blockage, and eventually making desulfurization impossible.
この対策には装置の運転を一時停止し、充填層或は熱交
換器などの閉塞部を解体掃除後再び運転を開始する必要
があり、その期間の予備器の設置や脱硫率の低下、掃除
のための環境上の問題、費用など問題点の多いものであ
った。To counter this, it is necessary to temporarily stop the operation of the equipment, dismantle and clean the blocked parts such as the packed bed or heat exchanger, and then restart the operation. There were many problems such as environmental problems and costs.
本発明は、これらの問題点を解決するためコークス炉か
ら発生する安水にフェノール又はタール酸を添加した混
合液でコークス炉ガス脱硫設備の硫黄付着物を洗浄する
方法を確立したもので極めて経済的に、これらの問題を
解決したものである。In order to solve these problems, the present invention establishes a method of cleaning sulfur deposits from coke oven gas desulfurization equipment using a mixture of ammonium water generated from coke ovens and phenol or tar acid, which is extremely economical. In short, these problems have been solved.
即ち、従来、この硫黄付着閉塞物は解体して閉塞箇所の
充填層を取出して高圧ジェット水洗或は熱水洗浄を行っ
た後再び元の設備に入れて組立てる方法を取っており、
解体取出作業、洗浄作業、再組立作業と多犬の労力費用
を必要とするものであった。That is, conventionally, this sulfur-adhered blockage has been dismantled, the packed bed at the blockage location has been taken out, and after being washed with high-pressure jet water or hot water, it is put back into the original equipment and reassembled.
This required disassembly, removal, cleaning, reassembly, and the labor costs of multiple dogs.
本発明はこの硫黄付着物を安水とフェノール或は安水と
クール酸との混合液で洗浄すると硫黄を強固に付着させ
ている粘結性物質が溶解し簡単に剥離することを利用し
たもので、設備を解体することなくコークス炉ガス脱硫
設備の吸収液に代えて安水にフェノールを0.1〜20
%添加した混合液或は安水にタール酸を0.1〜20%
添加した混合液を循環するだけで極めて経済的にこれら
の問題点を解結したものである。The present invention takes advantage of the fact that when this sulfur deposit is washed with a mixture of ammonium water and phenol or ammonium water and cool acid, the caking substance that firmly adheres the sulfur dissolves and is easily peeled off. By adding 0.1 to 20% phenol to ammonium water instead of the absorption liquid in coke oven gas desulfurization equipment without dismantling the equipment.
% of tar acid in a mixed solution or ammonium water with 0.1 to 20% of tar acid
These problems can be solved extremely economically by simply circulating the added liquid mixture.
図面は本発明の実施例を示す脱硫塔の断面図であり、1
はコークス炉ガスと吸収液が向流接触する脱硫塔、2は
充填層でプラスチック製の充填物が入っており硫黄が付
着し閉塞状態となっている。The drawing is a sectional view of a desulfurization tower showing an embodiment of the present invention, and 1
2 is a desulfurization tower in which the coke oven gas and the absorption liquid are in countercurrent contact, and 2 is a packed bed containing plastic packing, which is clogged with adhesion of sulfur.
9も充填層でプラスチック製の充填物が入っているが閉
塞していない。No. 9 is also a packed bed with a plastic filler in it, but it is not blocked.
3はタンクで、この中には本発明に係る安水にタール酸
10%添加した液を入れてあって加温コイル8で60〜
70℃にスチームで加温しこの液をポンプ4で循環ライ
ン5を経て塔頂から流下洗浄し、タンク3に戻り再循環
させる。3 is a tank, which contains a solution of ammonium water according to the present invention with 10% tar acid added thereto, and a heating coil 8 is used to heat the solution from 60 to 60%.
The liquid is heated to 70° C. with steam and washed down from the top of the column via a circulation line 5 by a pump 4, and returned to the tank 3 for recirculation.
6は塔底ブローライン、8は加温用コイルである。6 is a tower bottom blow line, and 8 is a heating coil.
該充填物に付着している硫黄閉塞物は、上記安水とフェ
ノール混合液により剥離されて塔底に該混合液と一緒に
流下し、1昼夜の循環洗浄で完全に各段この閉塞物は洗
浄され、剥離した硫黄滓は閉塞していない充填層9の各
段を通過し、塔底からタンク3の底部に溜った。The sulfur blockages adhering to the packings are removed by the ammonium water and phenol mixture and flow down to the bottom of the tower together with the mixture, and the blockages are completely removed from each stage by circulating cleaning for one day and night. The washed and peeled sulfur slag passed through each stage of the unblocked packed bed 9 and accumulated at the bottom of the tank 3 from the bottom of the tower.
このタンク底の硫黄滓はブローライン7で抜出され焼却
炉による焼却又はコークス炉への装入などにより処理さ
れる。This sulfur slag at the bottom of the tank is extracted through a blow line 7 and treated by incineration in an incinerator or charging into a coke oven.
安水・タール酸混合液による洗浄法によれば剥離した閉
塞硫黄滓の充填層への再付着を防止する効果もある。The cleaning method using a mixed solution of ammonium water and tar acid also has the effect of preventing detached blocked sulfur slag from re-adhering to the packed bed.
即ち、従来の洗浄法のように熱水のみで洗浄を行うと下
段の充填層9の部分に上段2の充填層から剥離した閉塞
滓が付着して洗浄が一層困難になる。That is, if cleaning is performed using only hot water as in the conventional cleaning method, clogging sludge separated from the upper filling layer 2 will adhere to the lower filling layer 9, making cleaning even more difficult.
本発明に係る安水とタール酸との混合液の代りに安水と
フェノールとの混合液を使用しても全く同様の効果を得
ることが出来る。Exactly the same effect can be obtained by using a mixture of ammonium water and phenol instead of the mixture of ammonium water and tar acid according to the present invention.
又安水に添加するフェノール又はタール酸の量は0.1
〜20%望ましくは3〜10%で、0.1%より濃度が
低いと洗浄効果が少く20%より高いと経済的負担が大
きいことと、発生した閉塞硫黄滓混合物の量が増加する
ので採用できない。Also, the amount of phenol or tar acid added to ammonium water is 0.1
-20% Preferably 3 to 10%. If the concentration is lower than 0.1%, the cleaning effect will be low, and if it is higher than 20%, it will be a heavy economic burden and the amount of clogging sulfur slag mixture will increase, so this is adopted. Can not.
又、洗浄する温度は低いと洗浄効果が下り、高いと加温
費用がかかり、又設備上の制限もあるので50〜80℃
が望ましい。In addition, if the cleaning temperature is low, the cleaning effect will decrease, and if it is high, heating costs will increase, and there are restrictions on equipment, so the cleaning temperature should be 50 to 80℃.
is desirable.
以上述べたように本発明方法によれば、コークス炉ガス
脱硫設備の硫黄付着閉塞物を設備の解体することなく安
価な安水、自製可能なタール酸、フェノールの混合液で
完全に洗浄することが出来るので洗浄時間の短縮、解体
掃除費用の節減など多犬の経済的効果が得られる。As described above, according to the method of the present invention, sulfur-adhered blockages in coke oven gas desulfurization equipment can be completely cleaned with a mixture of cheap ammonium water, self-produced tar acid, and phenol without dismantling the equipment. This allows for economical benefits of having multiple dogs, such as shortening cleaning time and reducing disassembly and cleaning costs.
図面は本発明の実施態様例を示す脱硫塔の断面図である
。
1:脱硫塔、2:充填層、3:タンク、4:ポンプ、5
:循環ライン、6:塔底ブローライン、7:ブローライ
ン、8:加温用コイル、9:充填層。The drawing is a sectional view of a desulfurization tower showing an embodiment of the present invention. 1: Desulfurization tower, 2: Packed bed, 3: Tank, 4: Pump, 5
: circulation line, 6: bottom blow line, 7: blow line, 8: heating coil, 9: packed bed.
Claims (1)
、コークス炉ガス中の硫化水素を除去する設備に於で、
その設備の硫黄付着閉塞物を安水とフェノール混合液、
安水とタール酸混合液のうちいずれかで洗浄することを
特徴とするコークス炉ガス脱硫設備の硫黄付着閉塞物洗
浄方法。1 In equipment that removes hydrogen sulfide from coke oven gas by contacting coke oven gas with an alkali-containing absorption liquid,
Remove sulfur-adhered blockages from the equipment using a mixture of ammonium water and phenol.
A method for cleaning sulfur-adhered blockages in coke oven gas desulfurization equipment, the method comprising cleaning with either ammonium water or a tar acid mixture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55063188A JPS5849593B2 (en) | 1980-05-13 | 1980-05-13 | Method for cleaning sulfur-adhered blockages in coke oven gas desulfurization equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55063188A JPS5849593B2 (en) | 1980-05-13 | 1980-05-13 | Method for cleaning sulfur-adhered blockages in coke oven gas desulfurization equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56166295A JPS56166295A (en) | 1981-12-21 |
JPS5849593B2 true JPS5849593B2 (en) | 1983-11-05 |
Family
ID=13222000
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55063188A Expired JPS5849593B2 (en) | 1980-05-13 | 1980-05-13 | Method for cleaning sulfur-adhered blockages in coke oven gas desulfurization equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5849593B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61108695A (en) * | 1984-11-02 | 1986-05-27 | Nippon Steel Corp | Removal of sulfur deposit adherent to coke oven gas desulfurizer |
JP2018176122A (en) * | 2017-04-19 | 2018-11-15 | 一般財団法人電力中央研究所 | Recycling system of impurity removal agent |
JP7192803B2 (en) * | 2020-01-08 | 2022-12-20 | Jfeスチール株式会社 | Method for suppressing deposition of solid matter and method for operating desulfurization tower |
-
1980
- 1980-05-13 JP JP55063188A patent/JPS5849593B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS56166295A (en) | 1981-12-21 |
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