JP2939222B1 - Pretreatment cleaning method for boiler - Google Patents
Pretreatment cleaning method for boilerInfo
- Publication number
- JP2939222B1 JP2939222B1 JP10047746A JP4774698A JP2939222B1 JP 2939222 B1 JP2939222 B1 JP 2939222B1 JP 10047746 A JP10047746 A JP 10047746A JP 4774698 A JP4774698 A JP 4774698A JP 2939222 B1 JP2939222 B1 JP 2939222B1
- Authority
- JP
- Japan
- Prior art keywords
- boiler
- acid
- salt
- cleaning
- treatment
- 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 - Lifetime
Links
Landscapes
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- Cleaning By Liquid Or Steam (AREA)
Abstract
【要約】
【課題】 ボイラの稼働前の洗浄処理を行うに当たっ
て、洗浄廃液の無害化処理を必要とせず、また洗浄後に
特別な防食保存処理も必要でなく、処理作業の容易なボ
イラの前処理洗浄方法を提供する。
【解決手段】 本発明のボイラの前処理洗浄方法は、ア
スコルビン酸、エリソルビン酸又はそれらの塩から選ば
れた少なくとも1種と、アスパラギン酸又はその塩と、
水酸化カリウム又は水酸化ナトリウムとを含む処理液を
ボイラ内に仕込み、加熱処理することを特徴とするもの
であり、アスコルビン酸、エリソルビン酸又はそれらの
塩から選ばれた少なくとも1種に対して、アスパラギン
酸又はその塩を重量比で0.1〜100となるように添
加することが好ましい。Abstract: PROBLEM TO BE SOLVED: To perform a cleaning process before operating a boiler, does not require a detoxification process of a cleaning waste liquid, does not require a special anti-corrosion storage process after the cleaning, and pre-processes a boiler that is easy to process. Provide a cleaning method. SOLUTION: The pretreatment cleaning method of the boiler of the present invention comprises at least one selected from ascorbic acid, erythorbic acid or a salt thereof, aspartic acid or a salt thereof,
A treatment solution containing potassium hydroxide or sodium hydroxide is charged into a boiler and is characterized by being subjected to a heat treatment, and ascorbic acid, erythorbic acid or at least one selected from salts thereof, It is preferable to add aspartic acid or a salt thereof in a weight ratio of 0.1 to 100.
Description
【0001】[0001]
【発明の属する技術分野】本発明はボイラの前処理洗浄
方法に関し、特にボイラの新設や修理後にボイラ内部を
洗浄する前処理洗浄方法に関する。The present invention relates to a pretreatment cleaning method for a boiler, and more particularly to a pretreatment cleaning method for cleaning the inside of a boiler after newly installing or repairing a boiler.
【0002】[0002]
【従来の技術】新設したボイラ、或いは修理などで煙管
を交換したようなボイラの内部は、一般に油脂などで汚
れており、また異物などが付着していることが多い。そ
こでボイラの稼働運転に入る前に、内部の汚染物を除去
するために清掃を行うことが必要とされている。通常、
このようなボイラの清掃は、人手による掃除を行った後
に水による洗浄、アルカリ性洗浄液による洗浄、更に苛
性ソーダ水溶液を充満させて加熱する、所謂ソーダ煮な
どを行う方法で実施されることが多かった。2. Description of the Related Art The interior of a newly installed boiler or a boiler whose smoke tube has been replaced for repair or the like is generally contaminated with oil or the like, and foreign substances are often attached thereto. Therefore, it is necessary to clean the inside of the boiler in order to remove contaminants before the operation starts. Normal,
Such boiler cleaning is often performed by a method of performing cleaning with water, cleaning with water, cleaning with an alkaline cleaning liquid, and further filling with an aqueous solution of caustic soda and heating, so-called boiled soda.
【0003】このような従来方法によりボイラ洗浄を行
ったとき、洗浄後に直ちに稼働運転に入る場合は特に問
題はないが、すぐに稼働に入れない場合には、ボイラ内
面の鉄材の腐食が進行する危険があるため、例えばヒド
ラジンや亜硫酸ナトリウムなどの還元性薬剤等を用いた
防食保存処理をする必要があり、作業が煩雑であるとい
う問題があった。そしてまた、洗浄液などの強アルカリ
性の廃液が発生するために、中和などの処理が必要であ
って、コストが高く面倒な排水処理をその都度行わなけ
ればならない不便があった。[0003] When boiler cleaning is performed by such a conventional method, there is no particular problem when the operation starts immediately after the cleaning, but when the operation is not started immediately, the corrosion of the iron material on the inner surface of the boiler proceeds. Since there is a danger, it is necessary to perform anticorrosion preservation treatment using a reducing agent such as hydrazine or sodium sulfite, and there is a problem that the operation is complicated. Further, since a strong alkaline waste liquid such as a cleaning liquid is generated, a treatment such as neutralization is required, and there is an inconvenience that a costly and complicated wastewater treatment must be performed each time.
【0004】[0004]
【発明が解決しようとする課題】そこで本発明は、ボイ
ラの稼働前の洗浄処理を行うに当たって、洗浄廃液の無
害化処理を必要とせず、また洗浄後に特別な防食保存処
理も必要でなく、処理作業の容易なボイラの前処理洗浄
方法を提供することを目的とした。Accordingly, the present invention does not require the detoxification treatment of the washing waste liquid in performing the washing treatment before the operation of the boiler, and does not require any special anticorrosion storage treatment after the washing. It is an object of the present invention to provide a boiler pretreatment cleaning method that is easy to operate.
【0005】[0005]
【課題を解決するための手段】上記の目的を達成するこ
とができる本発明のボイラの前処理洗浄方法は、アスコ
ルビン酸、エリソルビン酸又はそれらの塩から選ばれた
少なくとも1種と、アスパラギン酸又はその塩と、水酸
化カリウム又は水酸化ナトリウムとを含む処理液をボイ
ラ内に仕込み、処理液を140〜210℃に保って1〜
3昼夜程度維持することを特徴とするものである。The pretreatment cleaning method for a boiler of the present invention, which can achieve the above object, comprises at least one selected from ascorbic acid, erythorbic acid or a salt thereof, aspartic acid or A treatment liquid containing the salt and potassium hydroxide or sodium hydroxide is charged into a boiler, and the treatment liquid is kept at 140 to 210 ° C. to 1 to
It is characterized by being maintained for about three days and nights .
【0006】[0006]
【発明の実施の形態】本発明のボイラの前処理洗浄方法
に使用する処理液は、アスコルビン酸、エリソルビン酸
又はそれらの塩から選ばれた少なくとも1種と、アスパ
ラギン酸又はその塩と、水酸化カリウム又は水酸化ナト
リウムとを含む薬液であるが、その配合割合は、アスコ
ルビン酸、エリソルビン酸又はそれらの塩から選ばれた
少なくとも1種の1重量部に対して、アスパラギン酸又
はその塩が0.1〜100重量部の範囲内にあることが
好ましい。BEST MODE FOR CARRYING OUT THE INVENTION The treatment liquid used in the boiler pretreatment cleaning method of the present invention comprises at least one selected from ascorbic acid, erythorbic acid or a salt thereof, aspartic acid or a salt thereof, It is a chemical solution containing potassium or sodium hydroxide. The mixing ratio of aspartic acid or a salt thereof is 0. 1 part by weight of at least one selected from ascorbic acid, erythorbic acid or a salt thereof. It is preferably in the range of 1 to 100 parts by weight.
【0007】更に、本発明に使用するかかる処理液に
は、本発明の効果を損なわない限りにおいて、他の防食
剤やスケール防止剤、例えばポリアクリル酸又はその
塩、ポリメタクリル酸又はその塩、アクリル酸とメタク
リル酸とのコポリマ又はその塩、ポリマレイン酸又はそ
の塩、スチレンスルホン酸とマレイン酸とのコポリマ又
はその塩、ヒドロキシエチリデンジホスホン酸又はその
塩、ホスホノブタントリカルボン酸又はその塩、アクリ
ル酸とアクリルアミドメチルプロピルスルホン酸とのコ
ポリマ又はその塩、亜硫酸塩、亜硝酸塩、亜鉛塩、錫
塩、ヒドラジン、タンニン、リグニン、リグニンスルホ
ン酸、モリブデン酸又はその塩、ホスフィン酸、オキシ
カルボン酸、燐酸又はその塩、糖類などを加えることが
できる。Further, such a processing solution used in the present invention contains other anticorrosives and scale inhibitors, such as polyacrylic acid or a salt thereof, polymethacrylic acid or a salt thereof, as long as the effects of the present invention are not impaired. Copolymer or salt thereof of acrylic acid and methacrylic acid, polymaleic acid or salt thereof, copolymer of styrenesulfonic acid and maleic acid or salt thereof, hydroxyethylidene diphosphonic acid or salt thereof, phosphonobutanetricarboxylic acid or salt thereof, acrylic Copolymer of acid and acrylamidomethylpropylsulfonic acid or salt thereof, sulfite, nitrite, zinc salt, tin salt, hydrazine, tannin, lignin, ligninsulfonic acid, molybdic acid or salt thereof, phosphinic acid, oxycarboxylic acid, phosphoric acid Alternatively, a salt, a saccharide or the like thereof can be added.
【0008】またかかる薬液は、水に溶解した水性液の
形態でボイラ内に仕込み、例えば140〜210℃の範
囲に加熱した状態を1〜3昼夜程度維持することによっ
て、洗浄処理を行うことができる。この際の洗浄液中の
薬剤濃度は、0.01〜1.0重量%の範囲内にあるこ
とが好ましい。[0008] Further, such a chemical solution is charged into a boiler in the form of an aqueous solution dissolved in water, and a cleaning treatment can be performed by maintaining a state of being heated to, for example, 140 to 210 ° C for about 1 to 3 days and nights. it can. At this time, the concentration of the drug in the cleaning liquid is preferably in the range of 0.01 to 1.0% by weight.
【0009】[0009]
【実施例】(第1試験例)表1に示す水質を有する軟化
水に対して、表2に示す濃度(g/L ) となるように、
それぞれアスコルビン酸(ASCA)、アスコルビン酸
ナトリウム(ASCN)、エリソルビン酸(ESB
A)、エリソルビン酸ナトリウム(ESBN)、アスパ
ラギン酸ナトリウム(APGN)、水酸化カリウム(K
OH)、水酸化ナトリウム(NaOH)を溶解して、本
発明のボイラ用前処理洗浄剤を含む処理液A〜Hを調製
した。EXAMPLES (First test example) Softened water having the water quality shown in Table 1 was prepared so that the concentration (g / L) shown in Table 2 was obtained.
Ascorbic acid (ASCA), sodium ascorbate (ASCN), erythorbic acid (ESB)
A), sodium erythorbate (ESBN), sodium aspartate (APGN), potassium hydroxide (K
OH) and sodium hydroxide (NaOH) were dissolved to prepare treatment solutions A to H containing the boiler pretreatment detergent of the present invention.
【0010】[0010]
【表1】軟化水の水質 pH : 7.5 電気伝導率 (μS/cm) : 390 Mアルカリ度 (mgCaCO3/L) : 50 全硬度 (mg/L) : <1 塩化物イオン (mgCl/L) : 62 シリカ (mgSiO2/L) : 5 鉄 (mgFe/L) : <0.05[Table 1] Water quality of softened water pH: 7.5 Electrical conductivity (μS / cm): 390 M alkalinity (mgCaCO 3 / L): 50 Total hardness (mg / L): <1 chloride ion (mgCl / L): 62 Silica (mgSiO 2 / L): 5 Iron (mgFe / L): <0.05
【0011】また比較のために、従来のソーダ煮の例と
して水酸化ナトリウム(NaOH)2.0g/L を含む処
理液X、従来の防食性洗浄剤の例として水酸化ナトリウ
ム(NaOH)2.0g/L 、ヒドラジン(HAZN)
0.5g/L 、燐酸ナトリウム(NPHS)2.0g/L を
含む処理液Y、及び従来の糖類系ボイラ用防食剤の例と
してグルコース(GULC)0.9g/L 、水酸化カリウ
ム(KOH)0.4g/L、燐酸ナトリウム(NPHS)
0.3g/L を含む処理液Zを用意した。For comparison, a treatment liquid X containing 2.0 g / L of sodium hydroxide (NaOH) is used as an example of conventional soda-boiled, and sodium hydroxide (NaOH) is used as an example of a conventional anticorrosive cleaning agent. 0g / L, hydrazine (HAZN)
Treatment solution Y containing 0.5 g / L, 2.0 g / L of sodium phosphate (NPHS), 0.9 g / L of glucose (GULC) as an example of a conventional anticorrosive for saccharide-based boilers, potassium hydroxide (KOH) 0.4 g / L, sodium phosphate (NPHS)
A processing solution Z containing 0.3 g / L was prepared.
【0012】[0012]
【表2】 [Table 2]
【0013】一方、処理液の金属に対する腐食性を評価
するために、研磨清浄化したSTPG鋼管を用意し、ま
た、処理液の洗浄力を評価するために、40mm×15mm
で厚さ2mmの磨き軟鋼板に、マシン油を均一に薄く塗布
(49mg/dm2)した試験片を用意した。On the other hand, a STPG steel pipe polished and cleaned is prepared to evaluate the corrosiveness of the processing liquid to metals, and 40 mm × 15 mm is used to evaluate the cleaning power of the processing liquid.
A test piece was prepared by uniformly and thinly applying machine oil (49 mg / dm 2 ) to a polished mild steel sheet having a thickness of 2 mm.
【0014】上記のSTPG鋼管を鞘として用いた電熱
式ヒーター(表面積154cm2 )を、水中に浸漬するよ
うにオートクレーブ(保有水量:1.5L )に取り付
け、更に上記の洗浄力評価用の試験片もオートクレーブ
に仕込んだ。そして、前記の処理液をそれぞれ仕込んだ
後、オートクレーブを密閉して表3に示す温度と時間で
運転を行い、処理液の試験前と試験後のpHと、STP
G鋼管の腐食面積(cm2)、ピッチング発生状況及び表
面の変色を調べた。An electric heater (surface area: 154 cm 2 ) using the above-mentioned STPG steel tube as a sheath was attached to an autoclave (water volume: 1.5 L) so as to be immersed in water, and a test piece for evaluating the detergency was further prepared. Was also charged to the autoclave. After each of the treatment liquids was charged, the autoclave was sealed and operated at the temperature and time shown in Table 3, and the pH of the treatment liquid before and after the test, the STP
The corrosion area (cm 2 ) of the G steel pipe, the occurrence of pitting, and the discoloration of the surface were examined.
【0015】また、オートクレーブから洗浄力評価用の
試験片を取り出して一旦乾燥し、次いで室温のヘキサン
を用いて充分に洗浄し、洗浄前後の重量差から試験片に
付着して残留していた油分(mg/dm2)を求めた。そして
これらの試験結果を、表3に併せて示した。Further, a test piece for evaluation of detergency is taken out from the autoclave, dried once, and then sufficiently washed with hexane at room temperature. (Mg / dm 2 ). These test results are also shown in Table 3.
【0016】[0016]
【表3】 [Table 3]
【0017】(第2試験例)第1試験例において、本発
明の処理液A、B、D並びに比較例の処理液X及びYを
用いて洗浄処理試験をしたSTPG鋼管を、電熱式ヒー
ターに再び鞘として取り付け、これらの電熱式ヒーター
を第1試験例と同様にそれぞれオートクレーブに取り付
けたのち、表4に示すような水質を有する腐食性人工ボ
イラ水をオートクレーブに仕込み、蒸気圧0.7MP
a、蒸気発生速度1.5kg/hr 、ブロー率10%で4時
間運転した後、稼働を停止して水温を60℃まで低下さ
せ、バルブを開放したまま翌日まで放置した。次の日に
は再び同様な運転を繰り返し、4日間同様な運転を反復
した後に、ヒーター鞘の表面の腐食面積とピッチングの
発生状況とを測定した。その結果を表5に併せて示し
た。(Second Test Example) In the first test example, a STPG steel pipe subjected to a cleaning treatment test using the treatment solutions A, B, and D of the present invention and the treatment solutions X and Y of the comparative example was used as an electric heater. After being attached again as a sheath, and these electric heaters were attached to the autoclave in the same manner as in the first test example, corrosive artificial boiler water having a water quality as shown in Table 4 was charged into the autoclave, and the vapor pressure was set to 0.7 MPa.
a, After operating for 4 hours at a steam generation rate of 1.5 kg / hr and a blow rate of 10%, the operation was stopped, the water temperature was lowered to 60 ° C., and the valve was left open until the next day with the valve open. On the next day, the same operation was repeated again, and after the same operation was repeated for 4 days, the corrosion area of the surface of the heater sheath and the occurrence of pitting were measured. The results are shown in Table 5.
【0018】[0018]
【表4】人工ボイラ水水質 Mアルカリ度 (mgCaCO3/L) : 500 塩化物イオン (mgCl/L) : 2000 硫酸イオン (mgSO4/L) : 100 シリカ (mgSiO2/L) : 100[Table 4] Artificial boiler water quality M alkalinity (mgCaCO 3 / L): 500 Chloride ion (mgCl / L): 2000 Sulfate ion (mgSO 4 / L): 100 Silica (mgSiO 2 / L): 100
【0019】[0019]
【表5】 [Table 5]
【0020】[0020]
【発明の効果】本発明のボイラの前処理洗浄方法によれ
ば、従来のボイラ用前処理剤を使用した場合に劣らない
洗浄効果を示すうえ、鉄系金属に対する腐食防止性も優
れているので、ボイラ内部の洗浄を行ったのちに防食な
どのための保存処理を施すことなく、そのまま待機する
ことができ、或いは直ちに稼働運転に入ることもでき
る。そのうえ、前処理後の廃液は中性に近くなっている
ので、中和処理を行うことなくそのまま一般的な排水処
理にかけることができ、前処理工程を大幅に簡素化する
ことができる効果がある。According to the boiler pretreatment cleaning method of the present invention, not only the cleaning effect is not inferior to the case of using the conventional boiler pretreatment agent, but also the anticorrosion of iron-based metals is excellent. After cleaning the inside of the boiler, the boiler can be kept on standby without performing a preservation process for corrosion prevention or the like, or can be put into operation immediately. In addition, the waste liquid after pre-treatment is almost neutral, so it can be subjected to general wastewater treatment without neutralization treatment, and the pre-treatment process can be greatly simplified. is there.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C23G 5/032 C23G 5/032 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI C23G 5/032 C23G 5/032
Claims (1)
れらの塩から選ばれた少なくとも1種と、アスパラギン
酸又はその塩と、水酸化カリウム又は水酸化ナトリウム
とを含む処理液をボイラ内に仕込み、処理液を140〜
210℃に保って1〜3昼夜程度維持することを特徴と
するボイラの前処理洗浄方法。1. A treatment liquid containing at least one selected from ascorbic acid, erythorbic acid or a salt thereof, aspartic acid or a salt thereof, and potassium hydroxide or sodium hydroxide is charged into a boiler, and the treatment liquid is charged. From 140 to
A pretreatment cleaning method for a boiler, wherein the method is maintained at 210 ° C. for about 1 to 3 days and nights .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10047746A JP2939222B1 (en) | 1998-02-27 | 1998-02-27 | Pretreatment cleaning method for boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10047746A JP2939222B1 (en) | 1998-02-27 | 1998-02-27 | Pretreatment cleaning method for boiler |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2939222B1 true JP2939222B1 (en) | 1999-08-25 |
JPH11241193A JPH11241193A (en) | 1999-09-07 |
Family
ID=12783923
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10047746A Expired - Lifetime JP2939222B1 (en) | 1998-02-27 | 1998-02-27 | Pretreatment cleaning method for boiler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2939222B1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008240089A (en) * | 2007-03-28 | 2008-10-09 | Kurita Water Ind Ltd | Treatment method of newly constructed boiler inside |
-
1998
- 1998-02-27 JP JP10047746A patent/JP2939222B1/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008240089A (en) * | 2007-03-28 | 2008-10-09 | Kurita Water Ind Ltd | Treatment method of newly constructed boiler inside |
Also Published As
Publication number | Publication date |
---|---|
JPH11241193A (en) | 1999-09-07 |
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