JP2003119453A - Antifouling agent - Google Patents

Antifouling agent

Info

Publication number
JP2003119453A
JP2003119453A JP2001313086A JP2001313086A JP2003119453A JP 2003119453 A JP2003119453 A JP 2003119453A JP 2001313086 A JP2001313086 A JP 2001313086A JP 2001313086 A JP2001313086 A JP 2001313086A JP 2003119453 A JP2003119453 A JP 2003119453A
Authority
JP
Japan
Prior art keywords
antifouling agent
butylcatechol
methylphenol
butyl
present
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
Application number
JP2001313086A
Other languages
Japanese (ja)
Other versions
JP3832305B2 (en
Inventor
Koichi Tanaka
浩一 田中
Katsutoshi Irie
勝利 入江
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP2001313086A priority Critical patent/JP3832305B2/en
Publication of JP2003119453A publication Critical patent/JP2003119453A/en
Application granted granted Critical
Publication of JP3832305B2 publication Critical patent/JP3832305B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To obtain an antifouling agent free from amines, with which fouling is effectively prevented with a small amount of its addition at a low treating cost in hydrocarbon-treating apparatus such as a crude oil pre-heater. SOLUTION: This antifouling agent contains 2,6-di-t-butyl-4-methylphenol and 4-t-butylcatechol.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、汚れ防止剤に関す
る。さらに詳しくは、本発明は、原油予熱器系などの炭
化水素を処理する装置において、アミン類を含有せず、
少ない添加量と処理コストで効率的に汚れの発生を防止
することができる汚れ防止剤に関する。
TECHNICAL FIELD The present invention relates to an antifouling agent. More specifically, the present invention is an apparatus for treating hydrocarbons such as a crude oil preheater system, which does not contain amines,
The present invention relates to a stain preventive agent which can efficiently prevent the generation of stains with a small amount added and a treatment cost.

【0002】[0002]

【従来の技術】近年、原油処理の効率化のために、多年
連続操業と高負荷運転が行われている。一方、原油は重
質化の傾向にあり、塩分、硫黄、懸濁物質、アスファル
テンなどが増加している。このために、原油予熱器系の
汚れが問題となっている。原油予熱器系に汚れが発生す
ると、熱交換器や配管の差圧上昇による運転障害、熱交
換器の総括伝熱係数の低下によるエネルギーの損失、加
熱炉入口温度の低下による燃料消費量の増大などのさま
ざまな障害を引き起こす。このような、汚れによる障害
は、原油予熱器系のみならず、ナフサ分解、合成ゴム製
造などのさまざまな石油化学プロセスにおいても発生し
ている。原油予熱器系などは、連続操業中は開放するこ
とができないので、汚れ防止剤の添加により汚れの発生
を抑えており、種々の汚れ防止方法が提案されている。
例えば、米国特許第3,148,225号明細書には、合
成ゴムの製造工程において、オレフィンの重合によるポ
ップコーンポリマーの生成を抑制するために、ジアルキ
ルヒドロキシルアミン類を添加する方法が提案されてい
る。米国特許第4,456,526号明細書には、石油処
理装置の汚れを防止するために、ジアルキルヒドロキシ
ルアミンとt−アルキルカテコールを添加する方法が提
案されている。また、米国特許第4,744,881号明
細書には、臭素価が10以上の炭化水素を扱い、酸素を
含む石油化学プロセスにおける汚れ防止方法として、立
体障害のないフェノール類と有機アミンのような強塩基
性物質を併用する方法が提案されている。さらに、特開
昭57−180692号公報には、ナフサ分解によるエ
チレン製造プロセスにおける汚れ防止剤として、アニリ
ン、パラトルイジン又はアニシジンと4−t−ブチルカ
テコールを含有する汚れ防止剤が提案されている。しか
し、汚れ防止剤としてアミン類を用いると、製品に着色
や変色を生じたり、後工程に触媒反応プロセスがある場
合には、アミン類が触媒毒になるおそれがある。また、
アミン類の添加量が多くなると、薬剤コストが嵩み、経
済性が損なわれるおそれがある。このために、アミン類
を含有しない有効な汚れ防止剤が求められていた。
2. Description of the Related Art In recent years, continuous operation and high load operation have been performed for many years in order to improve the efficiency of crude oil processing. On the other hand, crude oil tends to be heavier, and salinity, sulfur, suspended matter, and asphaltene are increasing. For this reason, contamination of the crude oil preheater system has become a problem. If the crude oil preheater system becomes dirty, the operation pressure will increase due to an increase in the differential pressure of the heat exchanger and piping, energy loss due to a decrease in the overall heat transfer coefficient of the heat exchanger, and increase in fuel consumption due to a decrease in the furnace inlet temperature. Cause various obstacles such as. Such troubles due to dirt occur not only in the crude oil preheater system but also in various petrochemical processes such as naphtha decomposition and synthetic rubber production. Since the crude oil preheater system and the like cannot be opened during continuous operation, the addition of a stain inhibitor suppresses the generation of stains, and various stain prevention methods have been proposed.
For example, U.S. Pat. No. 3,148,225 proposes a method of adding dialkylhydroxylamines in order to suppress the production of popcorn polymer by the polymerization of olefins in the production process of synthetic rubber. . U.S. Pat. No. 4,456,526 proposes a method of adding dialkylhydroxylamine and t-alkylcatechol to prevent fouling of petroleum processing equipment. Further, US Pat. No. 4,744,881 discloses that a hydrocarbon having a bromine number of 10 or more is treated as a stain prevention method in a petrochemical process containing oxygen, such as phenols and organic amines without steric hindrance. A method of using a strong basic substance in combination has been proposed. Further, JP-A-57-180692 proposes a stain preventive agent containing aniline, paratoluidine or anisidine and 4-t-butylcatechol as a stain preventive agent in the ethylene production process by naphtha decomposition. However, when amines are used as the antifouling agent, the products may be colored or discolored, or the amines may become a catalyst poison when there is a catalytic reaction process in the subsequent step. Also,
If the amount of amines added is large, the cost of chemicals will increase, and there is a risk that economic efficiency will be impaired. Therefore, an effective antifouling agent containing no amines has been demanded.

【0003】[0003]

【発明が解決しようとする課題】本発明は、原油予熱器
系などの炭化水素を処理する装置において、アミン類を
含有せず、少ない添加量と処理コストで効率的に汚れの
発生を防止することができる汚れ防止剤を提供すること
を目的としてなされたものである。
DISCLOSURE OF THE INVENTION The present invention, in an apparatus for treating hydrocarbons such as a crude oil preheater system, does not contain amines and efficiently prevents the generation of dirt with a small addition amount and a treatment cost. The purpose of the present invention is to provide an antifouling agent.

【0004】[0004]

【課題を解決するための手段】本発明者らは、上記の課
題を解決すべく鋭意研究を重ねた結果、2,6−ジ−t
−ブチル−4−メチルフェノールと4−t−ブチルカテ
コールを併用することにより、両者が相乗的に作用し
て、効果的に汚れの発生を防止し得ることを見いだし、
この知見に基づいて本発明を完成するに至った。すなわ
ち、本発明は、(1)2,6−ジ−t−ブチル−4−メ
チルフェノール及び4−t−ブチルカテコールを含有す
ることを特徴とする汚れ防止剤、及び、(2)2,6−
ジ−t−ブチル−4−メチルフェノール100重量部に
対し、4−t−ブチルカテコール0.1〜10重量部を
含有する第1項記載の汚れ防止剤、を提供するものであ
る。
Means for Solving the Problems As a result of intensive studies to solve the above problems, the present inventors have found that 2,6-di-t
It was found that by using -butyl-4-methylphenol and 4-t-butylcatechol in combination, both act synergistically and effectively prevent the generation of stains,
The present invention has been completed based on this finding. That is, the present invention provides (1) an antifouling agent containing 2,6-di-t-butyl-4-methylphenol and 4-t-butylcatechol, and (2) 2,6 −
The antifouling agent according to item 1, which contains 0.1 to 10 parts by weight of 4-t-butylcatechol with respect to 100 parts by weight of di-t-butyl-4-methylphenol.

【0005】[0005]

【発明の実施の形態】本発明の汚れ防止剤は、式[1]
で表される2,6−ジ−t−ブチル−4−メチルフェノ
ール及び式[2]で表される4−t−ブチルカテコール
を含有する。本発明の汚れ防止剤は、原油常圧蒸留塔、
原油減圧蒸留塔、水素化脱硫プロセス、流動接触分解プ
ロセス、エチレン製造プロセス、合成ゴム製造プロセス
などに好適に用いることができる。本発明の汚れ防止剤
は、2,6−ジ−t−ブチル−4−メチルフェノールと
4−t−ブチルカテコールの間で顕著な相乗効果が発現
し、少量の添加で効果的に汚れの発生を防止することが
できる。
BEST MODE FOR CARRYING OUT THE INVENTION The antifouling agent of the present invention has the formula [1]
2,6-di-t-butyl-4-methylphenol represented by the formula and 4-t-butylcatechol represented by the formula [2] are contained. The antifouling agent of the present invention is a crude oil atmospheric distillation column,
It can be suitably used for a crude oil vacuum distillation column, a hydrodesulfurization process, a fluid catalytic cracking process, an ethylene production process, a synthetic rubber production process and the like. The antifouling agent of the present invention exhibits a remarkable synergistic effect between 2,6-di-t-butyl-4-methylphenol and 4-t-butylcatechol, and the addition of a small amount effectively causes the generation of fouling. Can be prevented.

【化1】 本発明の汚れ防止剤において、2,6−ジ−t−ブチル
−4−メチルフェノールと4−t−ブチルカテコールの
割合に特に制限はないが、2,6−ジ−t−ブチル−4
−メチルフェノール100重量部に対して、4−t−ブ
チルカテコールが0.1〜10重量部であることが好ま
しく、0.5〜5重量部であることがより好ましい。2,
6−ジ−t−ブチル−4−メチルフェノール100重量
部に対する4−t−ブチルカテコールの割合が0.1重
量部未満であると、両者の相乗効果が十分に発現しない
おそれがある。2,6−ジ−t−ブチル−4−メチルフ
ェノール100重量部に対する4−t−ブチルカテコー
ルの割合は10重量部以下で十分に相乗効果が発現し、
通常は10重量部を超える4−t−ブチルカテコールを
含有させる必要はない。
[Chemical 1] In the antifouling agent of the present invention, the ratio of 2,6-di-t-butyl-4-methylphenol and 4-t-butylcatechol is not particularly limited, but 2,6-di-t-butyl-4.
The amount of 4-t-butylcatechol is preferably 0.1 to 10 parts by weight, and more preferably 0.5 to 5 parts by weight, based on 100 parts by weight of methylphenol. Two,
If the ratio of 4-t-butylcatechol to 100 parts by weight of 6-di-t-butyl-4-methylphenol is less than 0.1 part by weight, the synergistic effect of both may not be sufficiently exhibited. When the ratio of 4-t-butylcatechol to 100 parts by weight of 2,6-di-t-butyl-4-methylphenol is 10 parts by weight or less, a sufficient synergistic effect is exhibited,
Usually, it is not necessary to include more than 10 parts by weight of 4-t-butylcatechol.

【0006】本発明の汚れ防止剤を添加する場所に特に
制限はなく、例えば、原油常圧蒸留装置、減圧蒸留装
置、水素化精製装置、水素化脱硫装置、減圧フラッシン
グ装置、接触改質装置、接触分解装置、硫黄回収装置、
脱ろう装置、アスファルト製造装置、パラフィン製造装
置、エチレン製造装置、ジエン製造装置、芳香族炭化水
素抽出装置、重合装置などに添加することができる。本
発明の汚れ防止剤は、そのまま添加することができ、あ
るいは、ベンゼン、トルエン、キシレン、灯油などの有
機溶媒に溶解又は希釈して添加することもできる。本発
明の汚れ防止剤の添加量に特に制限はなく、対象となる
装置や運転状況などに応じて適宜選択することができる
が、通常は、プロセス流れに対して、汚れ防止剤の有効
成分として0.01〜1,000mg/Lであることが好ま
しく、0.1〜500mg/Lであることがより好まし
く、1〜300mg/Lであることがさらに好ましい。本
発明の汚れ防止剤は、必要に応じて、過酸化物捕捉剤、
ラジカル捕捉剤、金属不活性化剤、分散剤などの公知の
汚れ防止剤と併用することができる。本発明の汚れ防止
剤を用いることにより、少ない添加量で各種のプロセス
において発生する汚れを効果的に抑制することができ、
プラントの連続操業時間を大幅に延長することができ
る。
There is no particular limitation on the place where the antifouling agent of the present invention is added. For example, crude oil atmospheric distillation apparatus, vacuum distillation apparatus, hydrorefining apparatus, hydrodesulfurization apparatus, vacuum flushing apparatus, catalytic reforming apparatus, Catalytic cracking equipment, sulfur recovery equipment,
It can be added to dewaxing equipment, asphalt production equipment, paraffin production equipment, ethylene production equipment, diene production equipment, aromatic hydrocarbon extraction equipment, polymerization equipment and the like. The antifouling agent of the present invention can be added as it is, or can be added after being dissolved or diluted in an organic solvent such as benzene, toluene, xylene, or kerosene. The addition amount of the antifouling agent of the present invention is not particularly limited and can be appropriately selected depending on the target device and operating conditions, etc. The amount is preferably 0.01 to 1,000 mg / L, more preferably 0.1 to 500 mg / L, and further preferably 1 to 300 mg / L. The antifouling agent of the present invention, if necessary, a peroxide scavenger,
It can be used in combination with a known antifouling agent such as a radical scavenger, a metal deactivator, and a dispersant. By using the stain inhibitor of the present invention, it is possible to effectively suppress stains generated in various processes with a small addition amount,
The continuous operation time of the plant can be greatly extended.

【0007】[0007]

【実施例】以下に、実施例を挙げて本発明をさらに詳細
に説明するが、本発明はこれらの実施例によりなんら限
定されるものではない。 実施例1 容量200mLのステンレス鋼製オートクレーブにナフサ
100mLを入れ、2,6−ジ−t−ブチル−4−メチル
フェノール14.85mgと4−t−ブチルカテコール0.
15mgを添加し、気相部分を酸素ガスで置換して密封し
た。このオートクレーブを150℃で20時間加熱した
のち冷却し、ナフサをろ過し、生成した不溶解物を乾燥
して秤量した。不溶解物は、97.6mgであった。 実施例2 2,6−ジ−t−ブチル−4−メチルフェノール14.7
0mgと4−t−ブチルカテコール0.30mgを添加した
以外は、実施例1と同様にして、ナフサを加熱し、生成
した不溶解物を秤量した。不溶解物は、66.6mgであ
った。 比較例1 4−t−ブチルカテコールを添加することなく、2,6
−ジ−t−ブチル−4−メチルフェノールのみを15.
00mg添加した以外は、実施例1と同様にして、ナフサ
を加熱し、生成した不溶解物を秤量した。不溶解物は、
234.3mgであった。 実施例3 2,6−ジ−t−ブチル−4−メチルフェノール17.3
3mgと4−t−ブチルカテコール0.17mgを添加した
以外は、実施例1と同様にして、ナフサを加熱し、生成
した不溶解物を秤量した。不溶解物は、9.0mgであっ
た。 実施例4 2,6−ジ−t−ブチル−4−メチルフェノール17.1
5mgと4−t−ブチルカテコール0.35mgを添加した
以外は、実施例1と同様にして、ナフサを加熱し、生成
した不溶解物を秤量した。不溶解物は、6.0mgであっ
た。 比較例2 4−t−ブチルカテコールを添加することなく、2,6
−ジ−t−ブチル−4−メチルフェノールのみを17.
50mg添加した以外は、実施例1と同様にして、ナフサ
を加熱し、生成した不溶解物を秤量した。不溶解物は、
23.4mgであった。実施例1〜4及び比較例1〜2の
結果を、第1表に示す。
The present invention will be described in more detail below with reference to examples, but the present invention is not limited to these examples. Example 1 100 mL of naphtha was placed in a stainless steel autoclave having a capacity of 200 mL, and 14.65 mg of 2,6-di-t-butyl-4-methylphenol and 0.4-t-butylcatechol.
15 mg was added, and the gas phase part was replaced with oxygen gas and sealed. This autoclave was heated at 150 ° C. for 20 hours and then cooled, naphtha was filtered, and the produced insoluble matter was dried and weighed. The insoluble matter was 97.6 mg. Example 2 2,6-di-t-butyl-4-methylphenol 14.7
The naphtha was heated in the same manner as in Example 1 except that 0 mg and 0.30 mg of 4-t-butylcatechol were added, and the resulting insoluble matter was weighed. The insoluble matter was 66.6 mg. Comparative Example 1 2,6 without the addition of 4-t-butylcatechol
-Di-t-butyl-4-methylphenol only 15.
The naphtha was heated and the resulting insoluble matter was weighed in the same manner as in Example 1 except that 00 mg was added. Insoluble matter is
It was 234.3 mg. Example 3 2,6-di-t-butyl-4-methylphenol 17.3
The naphtha was heated in the same manner as in Example 1 except that 3 mg and 0.17 mg of 4-t-butylcatechol were added, and the resulting insoluble matter was weighed. The insoluble matter was 9.0 mg. Example 4 2,6-di-t-butyl-4-methylphenol 17.1
The naphtha was heated in the same manner as in Example 1 except that 5 mg and 0.35 mg of 4-t-butylcatechol were added, and the resulting insoluble matter was weighed. The insoluble matter was 6.0 mg. Comparative Example 2 2,6 without the addition of 4-t-butylcatechol
-Di-t-butyl-4-methylphenol only 17.
The naphtha was heated in the same manner as in Example 1 except that 50 mg was added, and the resulting insoluble matter was weighed. Insoluble matter is
It was 23.4 mg. The results of Examples 1 to 4 and Comparative Examples 1 and 2 are shown in Table 1.

【0008】[0008]

【表1】 [Table 1]

【0009】第1表に見られるように、薬剤の添加量が
同じである場合、2,6−ジ−t−ブチル−4−メチル
フェノールの1重量%を4−t−ブチルカテコールで置
き換えることにより、不溶解物の生成量は約60重量%
減少し、2,6−ジ−t−ブチル−4−メチルフェノー
ルの2重量%を4−t−ブチルカテコールで置き換える
ことにより、不溶解物の生成量は約70重量%減少す
る。
As can be seen in Table 1, replacing 1% by weight of 2,6-di-t-butyl-4-methylphenol with 4-t-butylcatechol when the amount of drug added is the same. Yields about 60% by weight of insoluble matter
By replacing 2% by weight of 2,6-di-t-butyl-4-methylphenol with 4-t-butylcatechol, the amount of insolubles produced is reduced by about 70% by weight.

【0010】[0010]

【発明の効果】本発明の汚れ防止剤は、2,6−ジ−t
−ブチル−4−メチルフェノールに少量の4−t−ブチ
ルカテコールを併用することにより、原油予熱器系など
の炭化水素を処理する装置において、アミン類を用いる
ことなく、少ない添加量と処理コストで効率的に汚れの
発生を防止することができる。
The antifouling agent of the present invention is 2,6-di-t.
-Butyl-4-methylphenol is used in combination with a small amount of 4-t-butylcatechol, so that in a device for treating hydrocarbons such as a crude oil preheater system, a small addition amount and a treatment cost can be achieved without using amines. It is possible to efficiently prevent the generation of dirt.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】2,6−ジ−t−ブチル−4−メチルフェ
ノール及び4−t−ブチルカテコールを含有することを
特徴とする汚れ防止剤。
1. An antifouling agent comprising 2,6-di-t-butyl-4-methylphenol and 4-t-butylcatechol.
【請求項2】2,6−ジ−t−ブチル−4−メチルフェ
ノール100重量部に対し、4−t−ブチルカテコール
0.1〜10重量部を含有する請求項1記載の汚れ防止
剤。
2. The antifouling agent according to claim 1, which contains 0.1 to 10 parts by weight of 4-t-butylcatechol based on 100 parts by weight of 2,6-di-t-butyl-4-methylphenol.
JP2001313086A 2001-10-10 2001-10-10 Antifouling agent for hydrocarbon treatment equipment Expired - Fee Related JP3832305B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001313086A JP3832305B2 (en) 2001-10-10 2001-10-10 Antifouling agent for hydrocarbon treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001313086A JP3832305B2 (en) 2001-10-10 2001-10-10 Antifouling agent for hydrocarbon treatment equipment

Publications (2)

Publication Number Publication Date
JP2003119453A true JP2003119453A (en) 2003-04-23
JP3832305B2 JP3832305B2 (en) 2006-10-11

Family

ID=19131634

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001313086A Expired - Fee Related JP3832305B2 (en) 2001-10-10 2001-10-10 Antifouling agent for hydrocarbon treatment equipment

Country Status (1)

Country Link
JP (1) JP3832305B2 (en)

Also Published As

Publication number Publication date
JP3832305B2 (en) 2006-10-11

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