JPH04221007A - Method for dephosphorizing molten iron - Google Patents
Method for dephosphorizing molten ironInfo
- Publication number
- JPH04221007A JPH04221007A JP40446490A JP40446490A JPH04221007A JP H04221007 A JPH04221007 A JP H04221007A JP 40446490 A JP40446490 A JP 40446490A JP 40446490 A JP40446490 A JP 40446490A JP H04221007 A JPH04221007 A JP H04221007A
- Authority
- JP
- Japan
- Prior art keywords
- hot metal
- slag
- molten iron
- iron oxide
- cao
- 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
Links
- 238000000034 method Methods 0.000 title claims description 22
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title abstract description 20
- 229910052742 iron Inorganic materials 0.000 title abstract description 10
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 22
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 3
- 239000002184 metal Substances 0.000 claims description 37
- 229910052751 metal Inorganic materials 0.000 claims description 37
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 2
- 239000011574 phosphorus Substances 0.000 claims description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 abstract description 40
- 239000000292 calcium oxide Substances 0.000 abstract description 20
- 235000012255 calcium oxide Nutrition 0.000 abstract description 20
- 239000002893 slag Substances 0.000 abstract description 17
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 10
- 229910052681 coesite Inorganic materials 0.000 abstract description 5
- 229910052906 cristobalite Inorganic materials 0.000 abstract description 5
- 239000000377 silicon dioxide Substances 0.000 abstract description 5
- 235000012239 silicon dioxide Nutrition 0.000 abstract description 5
- 229910052682 stishovite Inorganic materials 0.000 abstract description 5
- 229910052905 tridymite Inorganic materials 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract 1
- 239000000843 powder Substances 0.000 abstract 1
- 238000007670 refining Methods 0.000 abstract 1
- 239000002699 waste material Substances 0.000 abstract 1
- 238000011282 treatment Methods 0.000 description 26
- 238000007664 blowing Methods 0.000 description 16
- 238000002474 experimental method Methods 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000010436 fluorite Substances 0.000 description 2
- 238000011276 addition treatment Methods 0.000 description 1
- 238000005261 decarburization Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- -1 etc. are used Substances 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Landscapes
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、溶銑の脱燐処理方法に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for dephosphorizing hot metal.
【0002】0002
【従来の技術】一般に、トピード等の溶銑収容容器内の
溶銑の脱燐処理では、酸化鉄と生石灰を主たる成分とす
る脱燐造滓剤とを溶銑浴中に吹き込んで脱燐処理を行な
っている。一方、脱燐剤の添加方法としては、特開昭5
9−47317号公報のように、脱燐造滓剤を溶銑浴中
に吹込み、同時に酸化鉄を浴面上に上添加する方法も行
なわれている。[Prior Art] Generally, in the dephosphorization treatment of hot metal in a hot metal storage container such as a topedo, a dephosphorization slag agent containing iron oxide and quicklime as the main components is blown into a hot metal bath to perform the dephosphorization treatment. There is. On the other hand, as a method of adding a dephosphorizing agent,
As in Japanese Patent No. 9-47317, there is also a method in which a dephosphorizing slag agent is blown into a hot metal bath and at the same time iron oxide is added onto the bath surface.
【0003】また、特開平2−93011号公報のよう
に、溶銑中に酸化鉄とCaOを主成分とする造滓剤とを
同時に同位置に吹込み、かつ、処理終了まで酸化鉄を溶
銑上面に連続的に上添加する方法もある。しかし、1)
酸化鉄とCaOを主体とする造滓剤とからなる脱燐
剤を溶銑浴中へ吹込むのみの方法では、脱燐剤使用量の
多い高Si溶銑では処理時間が長くなる。また、吹込み
のみではCaOの吹込量に限度があり脱Si期のスラグ
塩基度を上げることができず、スロッピングによる操業
阻害が発生する。低Si溶銑でもCaOを全量吹込むと
吹込時間が長くなる。[0003] Furthermore, as disclosed in Japanese Patent Application Laid-Open No. 2-93011, iron oxide and a slag-forming agent mainly composed of CaO are injected into the hot metal at the same time, and the iron oxide is kept on the top surface of the hot metal until the treatment is completed. There is also a method of continuously adding it to the top. However, 1)
In the method of simply injecting a dephosphorizing agent consisting of iron oxide and a slag-forming agent mainly composed of CaO into a hot metal bath, the treatment time becomes long for high-Si hot metal in which a large amount of dephosphorizing agent is used. In addition, if only by blowing, there is a limit to the amount of CaO injected, and it is not possible to increase the basicity of the slag during the desiliconization stage, resulting in operational inhibition due to slopping. Even in low-Si hot metal, if the entire amount of CaO is injected, the injecting time becomes longer.
【0004】2) 特開昭59−47317号公報に
開示された方法では、酸化鉄は上添加により溶銑面上に
供給され、造滓剤のみを吹込んでいるため、溶銑中での
酸化鉄とCの反応によるCOガス発生が少ないので、C
Oガスによる溶銑撹拌が不十分になり、脱燐反応を十分
に進行させることができない。
3) 特開平2−93011号公報に開示された方法
では、酸化鉄とCaOを主体する造滓剤とを吹込み、か
つ、酸化鉄のみを上添加しているので、CaOを主体と
する造滓剤の吹込時間が長いとともに、高Si溶銑を脱
燐処理する場合には、CaO供給が吹込みのみのため初
期のスラグの塩基度(CaO/SiO2 )を確保する
のが難しく、スロッピングが多発し操業阻害要因となる
。2) In the method disclosed in JP-A No. 59-47317, iron oxide is supplied onto the hot metal surface by top addition, and only the slag-forming agent is injected, so that iron oxide and iron oxide in the hot metal are injected. Since less CO gas is generated due to the reaction of C, C
Stirring of the hot metal by O gas becomes insufficient, and the dephosphorization reaction cannot proceed sufficiently. 3) In the method disclosed in JP-A-2-93011, iron oxide and a sludge-forming agent mainly composed of CaO are injected, and only iron oxide is added above, so that a sludge-forming agent mainly composed of CaO is not produced. In addition to the long blowing time of the slag agent, when dephosphorizing high-Si hot metal, it is difficult to maintain the basicity of the initial slag (CaO/SiO2) because CaO is supplied only by blowing, and slopping is difficult. This occurs frequently and becomes a factor that hinders operations.
【0005】[0005]
【発明が解決しようとする課題】本発明は、上記従来技
術における欠点を解決するために、操業阻害が発生せず
、処理時間が短く、酸化鉄が十分に脱燐反応を行う、新
規な溶銑脱燐方法を提供しようとするものである。[Problems to be Solved by the Invention] In order to solve the above-mentioned drawbacks of the prior art, the present invention provides a novel hot metal that does not cause operational interruption, has a short treatment time, and allows iron oxide to undergo a sufficient dephosphorization reaction. The purpose is to provide a method for dephosphorization.
【0006】[0006]
【課題を解決するための手段】本発明は上記課題を解決
するために、酸化鉄とCaOを主成分とする造滓剤とを
、溶銑浴中に吹込むとともに溶銑上面に上添加するもの
で、さらには溶銑上面への上添加を脱燐処理末期には停
止することができる。[Means for Solving the Problems] In order to solve the above problems, the present invention is directed to injecting a slag-forming agent mainly composed of iron oxide and CaO into a hot metal bath and adding it to the top surface of the hot metal. Furthermore, top addition to the top surface of hot metal can be stopped at the end of the dephosphorization process.
【0007】[0007]
【作用】本発明によれば、高Si溶銑を脱燐処理するに
当り、酸化鉄とCaOを主成分とする造滓剤とを、溶銑
中へ吹込むと同時に溶銑上面に上添加しているため、ス
ラグ塩基度(CaO/SiO2 )を初期から高くでき
Siの酸化反応を早く進行させることができ、また、C
aO/SiO2 で定義されるスラグ塩基度を早期に高
く維持することができるため、脱燐処理時間の短縮及び
高スラグ塩基度の確保によるスロッピングの防止ができ
るようになった。さらに、酸化鉄も吹込んでいるため、
溶銑中で脱炭反応により多量のCOガスを発生させるこ
とができ溶銑を十分に撹拌できるため、脱珪及び脱燐反
応を促進することも可能である。[Operation] According to the present invention, when high-Si hot metal is dephosphorized, iron oxide and a slag-forming agent mainly composed of CaO are blown into the hot metal and simultaneously added to the top surface of the hot metal. Therefore, the basicity of the slag (CaO/SiO2) can be increased from the beginning, and the oxidation reaction of Si can proceed quickly.
Since the slag basicity defined by aO/SiO2 can be maintained high at an early stage, it has become possible to shorten the dephosphorization treatment time and prevent slopping by ensuring a high slag basicity. Furthermore, since iron oxide is also injected,
Since a large amount of CO gas can be generated by the decarburization reaction in hot metal and the hot metal can be sufficiently stirred, it is also possible to promote desiliconization and dephosphorization reactions.
【0008】また、上添加された酸化鉄とCaOを主体
とする造滓剤とはすぐには反応に寄与しないが、脱燐処
理末期に上添加を停止して吹込みのみを継続して処理を
行うことにより、上添加された酸化鉄とCaOを主体と
する造滓剤とが十分に脱燐反応に寄与するまでの時間を
確保でき、脱燐酸素効率は従来の吹込みのみの場合より
も高くかつ脱燐処理時間の短縮が可能である。[0008]Although the iron oxide and CaO-based slag-forming agent added to the top do not immediately contribute to the reaction, the top addition is stopped at the end of the dephosphorization process and only the blowing is continued. By doing this, it is possible to secure time for the iron oxide added above and the slag-forming agent mainly composed of CaO to fully contribute to the dephosphorization reaction, and the dephosphorization oxygen efficiency is higher than in the case of conventional blowing only. The dephosphorization process time can be shortened.
【0009】なお、脱燐処理末期とは、脱燐処理終了前
の5〜10分程度の期間で溶銑中の燐濃度等を勘案して
適宜定められる。また、本発明における酸化鉄としては
、ミルスケール、鉄鉱石、製鋼ダスト等が用いられ、造
滓剤には蛍石、ソーダ灰等を添加してもよい。[0009] The final stage of the dephosphorization process is a period of about 5 to 10 minutes before the end of the dephosphorization process, and is appropriately determined in consideration of the phosphorus concentration in the hot metal. Further, as the iron oxide in the present invention, mill scale, iron ore, steelmaking dust, etc. are used, and fluorite, soda ash, etc. may be added to the slag forming agent.
【0010】0010
【実施例】350tスピードに溶銑280tを入れて溶
銑脱燐処理実験を実施した。表1に実験条件及び結果を
、表2に脱燐処理前後の溶銑成分(重量%)を示す。
なお、実験に際して若干の蛍石を添加した。[Example] A hot metal dephosphorization treatment experiment was carried out by putting 280 tons of hot metal into a 350 tons speed. Table 1 shows the experimental conditions and results, and Table 2 shows the hot metal components (% by weight) before and after the dephosphorization treatment. Note that a small amount of fluorite was added during the experiment.
【0011】[0011]
【表1】
─────────────────────────
──────────
CaO スケール 処理時
間 スロッピング滓
(kg/t) (kg/t) (分)
(kg/t)吹込みのみ 15.5
37.6 33
18.5吹込み+上添加 *8.5
20.6 18
1.2 ※7.
0 17.6──────────────
───────────────────── 註
*:吹込み ※:上添加[Table 1] ──────────────────────────
──────────
CaO scale processing time slopping slag
(kg/t) (kg/t) (min)
(kg/t) Blowing only 15.5
37.6 33
18.5 blowing + top addition *8.5
20.6 18
1.2 *7.
0 17.6──────────────
────────────────────── Note
*: Blowing *: Top addition
【0012】0012
【表2】
─────────────────────────
──────────
C Si Mn
P S脱燐処理前
4.5 0.30 0.20
0.115 0.030脱燐処理後 4.2
0.01 0.20 0.025
0.020──────────────────
─────────────────吹込み+上添加法
により、脱燐処理前溶銑Si濃度が0.30%でも脱燐
処理時間18分、スロッピング滓原単位1.2kg/t
で処理ができ、吹込みのみの従来法に比べて処理時間で
15分の短縮、スロッピング滓17.3kg/tの低減
が得られた。[Table 2] ──────────────────────────
──────────
C Si Mn
P Before dephosphorization treatment
4.5 0.30 0.20
0.115 0.030 After dephosphorization treatment 4.2
0.01 0.20 0.025
0.020──────────────────
──────────────────With the blowing + top addition method, even if the hot metal Si concentration before dephosphorization treatment is 0.30%, the dephosphorization treatment time is 18 minutes and the slopping slag consumption rate is reduced 1.2kg/t
The treatment time was shortened by 15 minutes and the slopping dregs were reduced by 17.3 kg/t compared to the conventional method using only blowing.
【0013】また、同様の溶銑量で処理前Si濃度0.
05%の溶銑についても実験を行なった。表3に処理前
後の成分濃度を表4に実験条件及び結果を示す。[0013] Also, with the same amount of hot metal, the Si concentration before treatment was 0.
Experiments were also conducted with 0.05% hot metal. Table 3 shows the component concentrations before and after the treatment, and Table 4 shows the experimental conditions and results.
【0014】[0014]
【表3】
─────────────────────────
──────────
C Si Mn
P S脱燐処理前
4.5 0.05 0.20
0.115 0.030脱燐処理後 4.2
0.01 0.20 0.025
0.020──────────────────
─────────────────[Table 3] ──────────────────────────
──────────
C Si Mn
P Before dephosphorization treatment
4.5 0.05 0.20
0.115 0.030 After dephosphorization treatment 4.2
0.01 0.20 0.025
0.020──────────────────
──────────────────
【0015】[0015]
【表4】
─────────────────────────
──────────
CaO スケール 処理時
間 スロッピング滓
(kg/t) (kg/t) (分)
(kg/t)吹込み 1
0.0 25.8 22
5.0吹込み+上添加 *5.0
15.0 12 0
※5.0
10.8───────────────────
────────────────註 *:吹込み
※:上添加処理前Si濃度0.05%では、上添
加法を行うことにより処理時間が10分短くなり処理時
間12分で、スロッピングは吹込みのみの従来法の5.
0kg/tに対して吹込+上添加の場合は全くなかった
。[Table 4] ──────────────────────────
──────────
CaO scale processing time slopping slag
(kg/t) (kg/t) (min)
(kg/t) Blowing 1
0.0 25.8 22
5.0 blowing + top addition *5.0
15.0 12 0
*5.0
10.8────────────────────
────────────────Note *: Voice-over
*: When the Si concentration before top addition treatment is 0.05%, the treatment time is 10 minutes shorter by performing the top addition method, and the treatment time is 12 minutes.
There was no case of blowing + top addition for 0 kg/t.
【0016】次に、上添加終了時期を変更して実験を行
なった。表5に実験条件を示すように、上添加終了時期
を吹込みによる脱燐処理終了時及びその4分前及び7分
前とした。Next, an experiment was conducted by changing the timing at which the top addition was completed. As shown in Table 5, the experimental conditions were such that the top addition was completed at the end of the dephosphorization treatment by blowing, and 4 minutes and 7 minutes before that.
【0017】[0017]
【表5】
─────────────────────────
────────── 実験A 吹込
みのみ 実験B 吹込み+処理終了ま
で上添加 実験C 吹込み+処理終了
4分前で上添加終了 実験D 吹込み
+処理終了7分前で上添加終了───────────
────────────────────────図
1に脱燐酸素効率に及ぼす上添加終了時期の影響を示す
。[Table 5] ──────────────────────────
────────── Experiment A Blow-in only Experiment B Blow-in + top addition until the end of treatment Experiment C Blow-in + top addition finished 4 minutes before the end of treatment Experiment D Blow + 7 minutes before end of treatment Top addition completed────────────
──────────────────────── Figure 1 shows the influence of the timing of the end of top addition on the dephosphorization oxygen efficiency.
【0018】従来方法である実験Aと比較して、本発明
方法の実験Bでは脱燐酸素効率は同程度であるが、上添
加を脱燐処理末期に停止した実験C及びDでは向上した
。なお、本実施例では吹込み及び溶銑表面への吹付ガス
として窒素を用い酸素を使用しない場合のみについて行
ったが、本発明はこれに限るものではなく、気体酸素の
吹込み又は溶銑表面への吹付けを併用してもよい。Compared to Experiment A, which is a conventional method, the oxygen efficiency for dephosphorization is about the same in Experiment B, which is a method of the present invention, but it is improved in Experiments C and D, in which the top addition is stopped at the end of the dephosphorization process. In this example, nitrogen was used as the gas for blowing and blowing onto the hot metal surface, and oxygen was not used. However, the present invention is not limited to this. Spraying may also be used.
【0019】[0019]
【発明の効果】本発明により、脱燐処理時間が短縮でき
、スロッピングも大幅に低減させることができた。また
、処理時間を短縮できるので、処理量を増大することが
できるだけでなく、脱燐処理後の温度も上昇し転炉歩留
の向上も達成できた。[Effects of the Invention] According to the present invention, the dephosphorization treatment time can be shortened and slopping can be significantly reduced. Furthermore, since the treatment time could be shortened, not only could the throughput be increased, but the temperature after the dephosphorization treatment could also be increased, and the converter yield could be improved.
【図1】実施例における脱燐酸素効率に及す上添加時間
の影響を示すグラフである。FIG. 1 is a graph showing the effect of top addition time on dephosphorization oxygen efficiency in Examples.
Claims (2)
とCaOを主成分とする造滓剤とを、溶銑浴中に吹込み
つつ溶銑上面にも添加することを特徴とする溶銑脱燐方
法。1. A hot metal dephosphorization process characterized in that, when dephosphorizing hot metal, a slag-forming agent containing iron oxide and CaO as main components is added to the upper surface of the hot metal while being blown into the hot metal bath. Phosphorus method.
期には停止する請求項1記載の溶銑脱燐方法。2. The method for dephosphorizing hot metal according to claim 1, wherein the top addition to the top surface of the hot metal is stopped at the end of the dephosphorization process.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2404464A JP3054199B2 (en) | 1990-12-20 | 1990-12-20 | Hot metal dephosphorization method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2404464A JP3054199B2 (en) | 1990-12-20 | 1990-12-20 | Hot metal dephosphorization method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04221007A true JPH04221007A (en) | 1992-08-11 |
JP3054199B2 JP3054199B2 (en) | 2000-06-19 |
Family
ID=18514133
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2404464A Expired - Fee Related JP3054199B2 (en) | 1990-12-20 | 1990-12-20 | Hot metal dephosphorization method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3054199B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007092181A (en) * | 1998-06-18 | 2007-04-12 | Jfe Steel Kk | Method for producing low phosphorus molten iron |
-
1990
- 1990-12-20 JP JP2404464A patent/JP3054199B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007092181A (en) * | 1998-06-18 | 2007-04-12 | Jfe Steel Kk | Method for producing low phosphorus molten iron |
Also Published As
Publication number | Publication date |
---|---|
JP3054199B2 (en) | 2000-06-19 |
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