JPH1133387A - Method and apparatus for batch granulation and coating - Google Patents
Method and apparatus for batch granulation and coatingInfo
- Publication number
- JPH1133387A JPH1133387A JP9211398A JP21139897A JPH1133387A JP H1133387 A JPH1133387 A JP H1133387A JP 9211398 A JP9211398 A JP 9211398A JP 21139897 A JP21139897 A JP 21139897A JP H1133387 A JPH1133387 A JP H1133387A
- Authority
- JP
- Japan
- Prior art keywords
- coating
- container
- bottom wall
- product
- hole
- 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
Landscapes
- Glanulating (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、流動する粉体に溶
液又は懸濁液からなる結合剤又はコーティング剤を噴霧
して造粒又はコーティングする回分造粒・コーティング
方法及びその装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a batch granulation / coating method for spraying a binder or a coating agent consisting of a solution or a suspension onto a flowing powder to granulate or coat, and an apparatus therefor.
【0002】[0002]
【従来の技術】従来、この種の回分造粒・コーティング
方法及びその装置としては、例えば特公平5−8729
3号公報、特公平7−102313号公報及び特開平7
−289877号公報記載のものが知られている。これ
らは、いずれも排気口を上部に設けた容器内に結合剤又
はコーティング剤を噴霧するスプレーノズルを配設し、
気体を上向きに吹き出す多孔性基板を容器の底壁に設
け、かつ容器の底壁近傍の側壁に製品の排出口を設けた
装置を用い、排気を上部で行いつつ容器内で結合剤又は
コーティング剤を噴霧しながら、多孔性基板から吹き出
す気体により上昇と下降を繰り返して粉体を循環流動さ
せ、造粒又はコーティング後に製品を側壁の排出口から
系外へ排出するようにしている。2. Description of the Related Art Conventionally, a batch granulation / coating method of this kind and an apparatus therefor are disclosed, for example, in Japanese Patent Publication No. 5-8729.
No. 3, JP-B-7-102313 and JP-A-7-102313.
The one described in -289877 is known. These are all provided with a spray nozzle for spraying a binder or a coating agent in a container provided with an exhaust port at the top,
Using a device in which a porous substrate that blows gas upward is provided on the bottom wall of the container, and a product outlet is provided on the side wall near the bottom wall of the container, and a binder or coating agent is used in the container while performing exhaustion at the top. While spraying, the powder circulates and flows repeatedly by rising and falling by the gas blown out from the porous substrate, and after granulation or coating, the product is discharged from the side wall outlet to the outside of the system.
【0003】[0003]
【発明が解決しようとする課題】しかし、従来のいずれ
の回分造粒・コーティング方法及びその装置でも、造粒
又はコーティング後の製品を底壁近傍の側壁に設けた排
出口から水平移動させて系外へ排出しているので、製品
が容器内に残留するおそれがあり、異種の粉体の造粒又
はコーティングに際し、容器内の清掃が困難となる不具
合がある。かかる傾向は、容器内の底部に攪拌羽根等が
ある場合に顕著となる。そこで、本発明は、製品の全量
排出を容易になし得る回分造粒・コーティング方法及び
その装置を提供することを主目的とする。However, in any of the conventional batch granulation / coating methods and apparatuses, the product after granulation or coating is horizontally moved from an outlet provided in a side wall near a bottom wall. Since the product is discharged to the outside, the product may remain in the container, and there is a problem that it is difficult to clean the inside of the container when granulating or coating different kinds of powder. Such a tendency becomes remarkable when a stirring blade or the like is provided at the bottom of the container. Accordingly, an object of the present invention is to provide a batch granulation / coating method and a device capable of easily discharging the entire amount of a product.
【0004】[0004]
【課題を解決するための手段】前記課題を解決するた
め、本発明の第1の回分造粒・コーティング方法は、排
気を上部で行う容器内で結合剤又はコーティング剤を噴
霧し、かつ容器の底壁中央部から上向きに吹き出す気体
により上昇と下降を繰り返して粉体を循環流動させ、造
粒又はコーティング後に底壁中央部を開口して製品を自
重により流下させて系外へ排出することを特徴とする。
第2の回分造粒・コーティング方法は、第1の方法にお
いて、前記排気中の微粒子を遠心力により捕集すること
を特徴とする。又、第3の回分造粒・コーティング方法
は、第2の方法において、前記捕集した微粒子を下降過
程の粉体中に戻すことを特徴とする。一方、本発明の第
1の回分造粒・コーティング装置は、排気口を上部に設
けた容器内に結合剤又はコーティング剤を噴霧するスプ
レーノズルを配設し、かつ容器の逆円錐筒状の底壁中央
部に透孔を設け、気体を上向きに吹き出す多孔性基板を
上下動して上記透孔に嵌脱可能に設けたことを特徴とす
る。第2の回分造粒・コーティング装置は、第1の装置
において、前記排気口にサイクロンを連結したことを特
徴とする。又、第3の回分造粒・コーティング装置は、
第2の装置において、前記サイクロンで捕集した微粒子
を容器内の下部周辺に戻すエジェクターを設けたことを
特徴とする。In order to solve the above-mentioned problems, a first batch granulation / coating method of the present invention is to spray a binder or a coating agent in a container in which air is exhausted at an upper part, and The process of circulating and flowing powder by repeating rising and falling by the gas blown upward from the bottom wall center, opening the bottom wall center after granulation or coating, and allowing the product to flow down by its own weight and discharge it out of the system. Features.
The second batch granulation / coating method is characterized in that, in the first method, the fine particles in the exhaust gas are collected by centrifugal force. A third batch granulation / coating method is characterized in that, in the second method, the collected fine particles are returned to the powder in the descending process. On the other hand, the first batch granulation / coating apparatus of the present invention is provided with a spray nozzle for spraying a binder or a coating agent in a container provided with an exhaust port on an upper portion, and an inverted conical cylindrical bottom of the container. A through hole is provided in the center of the wall, and a porous substrate for blowing gas upward is vertically movable so as to be fitted into and removed from the through hole. The second batch granulation / coating apparatus is characterized in that, in the first apparatus, a cyclone is connected to the exhaust port. The third batch granulation / coating device is
The second apparatus is characterized in that an ejector is provided for returning the fine particles collected by the cyclone to a lower portion in the container.
【0005】[0005]
【発明の実施の形態】以下、本発明の実施の形態につい
て図面を参照して説明する。図1、図2は本発明に係る
回分造粒・コーティング装置の実施の形態の一例を示す
断面図、図1の装置の要部の作用を示す断面図である。
図中1は段付き円筒状の垂直な容器で、この容器1は、
天井壁2によって上端を閉鎖された大径筒3と、大径筒
3の下端に連ねられた截頭逆円錐筒4と、截頭逆円錐筒
4に連ねられた小径筒5と、小径筒5の下端に連ねら
れ、中央部に下方に向って拡開するテーパ状の透孔6を
設けた逆円錐筒状の底壁7とから構成されている。容器
1の大径筒3には、排気口8が上部に設けられていると
共に、原料粉体を投入する原料投入口9が中間部に設け
られており、又、大径筒3内には、溶液又は懸濁液から
なる結合剤又はコーティング剤を気体(例えば空気)と
一緒に噴霧するスプレーノズル10が中間部の中央に配
設されている。Embodiments of the present invention will be described below with reference to the drawings. 1 and 2 are a cross-sectional view showing an example of an embodiment of a batch granulation / coating apparatus according to the present invention, and a cross-sectional view showing an operation of a main part of the apparatus shown in FIG.
In the figure, reference numeral 1 denotes a vertical cylindrical container having a step.
A large-diameter cylinder 3 whose upper end is closed by a ceiling wall 2, a truncated inverted conical cylinder 4 linked to the lower end of the large-diameter cylinder 3, a small-diameter cylinder 5 linked to the truncated inverted conical cylinder 4, and a small-diameter cylinder 5 and a bottom wall 7 having an inverted conical cylindrical shape provided with a tapered through-hole 6 which opens downward at the center portion. In the large-diameter cylinder 3 of the container 1, an exhaust port 8 is provided at an upper part, and a raw material input port 9 for supplying raw material powder is provided at an intermediate portion. A spray nozzle 10 for spraying a binder or a coating agent consisting of a solution or a suspension together with a gas (for example, air) is provided at the center of the intermediate portion.
【0006】一方、容器1の底壁7の透孔6には、その
内周面と対応するテーパを外周面に形成した断面山形の
円板状を呈し、かつ加熱された気体を上向きに吹き出す
多数の通気孔11を設けた多孔性基板12が上下動して
嵌合、離脱(嵌脱)可能に設けられている。多孔性基板
12は、各通気孔11に気体を送給すべくその下面に垂
設した給気管13をエアシリンダー等の昇降手段14を
介して昇降することによって上下動される。又、容器1
の底壁7の下面には、前記多孔性基板12の下降によっ
てその外周面と透孔6の内周面との間に形成される環状
の間隙15(図2参照)から排出される製品を一時的に
貯留するタンク16が、前記給気管13の気密かつ摺動
可能な挿通を許容して気密に垂設されており、このタン
ク16の下端部には、バルブ17を介在した製品排出口
18が設けられている。他方、容器1の排気口8には、
排気管19を上方に突設したサイクロン20が連結管2
1を介して連結されており、このサイクロン20の下端
には、捕集した微粒子を収容するホッパー22が連設さ
れている。ホッパー22の下部には、加熱された気体を
用いて微粒子を容器1の下部である小径筒5内に接線方
向から戻すエジェクター23が連結管24を介して連結
されている。On the other hand, the through hole 6 in the bottom wall 7 of the container 1 has a disc shape with a mountain-shaped cross section in which a taper corresponding to the inner peripheral surface is formed on the outer peripheral surface, and the heated gas is blown upward. A porous substrate 12 provided with a large number of air holes 11 is provided so as to be able to move up and down to be fitted and disengaged (fitted and disengaged). The porous substrate 12 is moved up and down by moving up and down an air supply pipe 13 vertically provided on the lower surface of the porous substrate 12 through an elevating means 14 such as an air cylinder so as to supply gas to each ventilation hole 11. Container 1
The product discharged from an annular gap 15 (see FIG. 2) formed between the outer peripheral surface of the porous substrate 12 and the inner peripheral surface of the through-hole 6 due to the lowering of the porous substrate 12 is provided on the lower surface of the bottom wall 7 of the substrate. A tank 16 for temporarily storing air is vertically provided in an airtight manner so as to allow an airtight and slidable insertion of the air supply pipe 13, and a product outlet through a valve 17 is provided at a lower end of the tank 16. 18 are provided. On the other hand, the exhaust port 8 of the container 1
The cyclone 20 having the exhaust pipe 19 projecting upward is connected to the connecting pipe 2.
1, a hopper 22 for accommodating the collected fine particles is connected to the lower end of the cyclone 20. An ejector 23 that returns the fine particles from the tangential direction into the small-diameter cylinder 5, which is a lower part of the container 1, using a heated gas is connected to a lower portion of the hopper 22 via a connecting pipe 24.
【0007】上記構成の回分造粒・コーティング装置を
用いて造粒又はコーティングするには、先ず、原料投入
口9から原料粉体を容器1に投入すると共に、給気管1
3から加熱した気体を送給し、多孔性基板12の各通気
孔11から気体を上向きに吹き出させ、かつスプレーノ
ズル10から気体を用いて結合剤又はコーティング剤を
噴霧し、更に、エジェクター23に加熱された気体を送
給する。この操作によって、原料粉体は、図1において
矢印Aで示すように、概ね多孔性基板12から吹き出す
気体による上昇と、自重等による下降とを繰り返して循
環流動されつつ造粒又はコーティング及び乾燥される。
一方、スプレーノズル10によるスプレーエリアを越え
て上昇し、フリーボートエリアに到達した微粒子は、一
部が自重により落下して循環流動され、残部が、図1に
おいて矢印B、Cで示すように、排気口8から気体と一
緒にサイクロン20に入り、遠心力により捕集されてホ
ッパー22に収容される。微粒子が除去された気体は、
排気管19から大気へ放出される。そして、ホッパー2
2に収容された微粒子は、エジェクター23によって容
器1の小径筒5の接線方向から下降過程の粉体中に戻さ
れる。このエジェクター23による微粒子の戻しに際
し、その気体流量を調節することにより、サイクロン2
0に適度な下方への気流が生じ、捕集効率が一層良好と
なる。次に、上述した造粒又はコーティング及び乾燥操
作が終了すると、給気管13による気体の送給、スプレ
ーノズル10による噴霧及びエジェクター23による微
粒子の戻しを停止した後、図2に示すように、多孔性基
板12を下降し、底壁7の透孔6から離脱させる。この
多孔性基板12の下動によって、その外周面と透孔6の
内周面との間に環状の間隙15が形成され、図2におい
て矢印Dで示すように、製品が外気に触れることなく容
器1の逆円錐筒状の底壁7面上を自重により流下して全
てタンク16に貯留され、製品排出口18から別の容器
(図示せず)等に収容される。In order to granulate or coat using the batch granulating / coating apparatus having the above structure, first, raw material powder is charged into the container 1 through the raw material charging port 9 and the air supply pipe 1 is charged.
3, the heated gas is supplied, the gas is blown upward from each of the air holes 11 of the porous substrate 12, and the binder or the coating agent is sprayed from the spray nozzle 10 using the gas. Delivers heated gas. As a result of this operation, the raw material powder is granulated or coated and dried while being circulated and flown, as shown by the arrow A in FIG. You.
On the other hand, the fine particles that have risen beyond the spray area by the spray nozzle 10 and have reached the freeboat area are partially dropped by their own weight and circulated and flowed, and the remainder is as shown by arrows B and C in FIG. The gas enters the cyclone 20 together with the gas from the exhaust port 8, is collected by centrifugal force, and is stored in the hopper 22. The gas from which the fine particles have been removed
It is released from the exhaust pipe 19 to the atmosphere. And hopper 2
The fine particles contained in 2 are returned by the ejector 23 into the powder in the process of descending from the tangential direction of the small-diameter cylinder 5 of the container 1. When returning the fine particles by the ejector 23, the cyclone 2 is adjusted by adjusting the gas flow rate.
A moderate downward airflow occurs at zero, and the collection efficiency is further improved. Next, when the above-described granulation or coating and drying operations are completed, the supply of gas by the air supply pipe 13, the spraying by the spray nozzle 10 and the return of fine particles by the ejector 23 are stopped, and as shown in FIG. The flexible substrate 12 is moved down and detached from the through hole 6 in the bottom wall 7. Due to the downward movement of the porous substrate 12, an annular gap 15 is formed between the outer peripheral surface and the inner peripheral surface of the through hole 6, and as shown by an arrow D in FIG. The liquid flows down on the surface of the inverted conical cylindrical bottom wall 7 of the container 1 by its own weight and is all stored in the tank 16, and is stored in another container (not shown) or the like from the product discharge port 18.
【0008】なお、上述した実施の形態においては、排
気中の微粒子をサイクロンを用い、遠心力によって捕集
する場合について説明したが、これに限定されるもので
はなく、容器内のフリーボードエリアに配設したバグフ
ィルター等を用いるようにしてもよい。又、サイクロン
で捕集した微粒子を容器の小径筒の接線方向からエジェ
クターを用いて下降過程の粉体中に戻す場合に限らず、
次の操作時に原料粉体と一緒にして容器に投入するよう
にしてもよい。更に、吐出ブロワーによる正圧運転の場
合について説明したが、これに限定されるものではな
く、吸引ブロワーによる負圧運転又は双方を使用して槽
内静圧を零として運転してもよい。In the above-described embodiment, a case has been described in which fine particles in exhaust gas are collected by a centrifugal force using a cyclone. However, the present invention is not limited to this. An arranged bag filter or the like may be used. Also, the method is not limited to returning the fine particles collected by the cyclone into the powder in the descending process using the ejector from the tangential direction of the small-diameter cylinder of the container,
At the time of the next operation, it may be put into the container together with the raw material powder. Furthermore, the case of the positive pressure operation by the discharge blower has been described, but the present invention is not limited to this, and the operation may be performed with the tank static pressure being zero by using the negative pressure operation by the suction blower or both.
【0009】[0009]
【発明の効果】以上説明したように、本発明の第1の回
分造粒・コーティング方法及びその装置によれば、製品
が逆円錐筒状の底壁面上を自重により流下してその中央
部の透孔から全て排出されるので、製品の全量排出を容
易に行うことができる。第2の回分造粒・コーティング
方法及びその装置によれば、第1の方法及びその装置の
作用効果の他、排気中の微粒子の捕集を効率良くできる
と共に、その構造を洗浄性の良い簡単なものとすること
ができる。又、第3の回分造粒・コーティング方法及び
その装置によれば、第2の方法及びその装置の作用効果
の他、原料粉体の無駄を省くことができ、又、粉体の循
環流動を阻害することなく、微粒子の戻しを行うことが
でき、更にエジェクターを用いることにより、サイクロ
ンの捕集効率を高めることができる。As described above, according to the first batch granulation / coating method and the apparatus of the present invention, the product flows down on the bottom wall surface of the inverted conical cylindrical shape by its own weight, and the product flows in the central portion. Since all of the product is discharged from the through hole, the entire amount of the product can be easily discharged. According to the second batch granulation / coating method and its apparatus, in addition to the function and effect of the first method and its apparatus, it is possible to efficiently collect fine particles in exhaust gas and to make the structure easy to clean. It can be. Further, according to the third batch granulation / coating method and its apparatus, in addition to the effects of the second method and its apparatus, waste of the raw material powder can be omitted, and the circulating flow of the powder can be reduced. The particles can be returned without hindrance, and the use of an ejector can increase the cyclone collection efficiency.
【図1】本発明に係る回分造粒・コーティング装置の実
施の形態の一例を示す断面図である。FIG. 1 is a sectional view showing an example of an embodiment of a batch granulation / coating apparatus according to the present invention.
【図2】図1の装置の要部の作用を示す断面図である。FIG. 2 is a sectional view showing an operation of a main part of the apparatus of FIG.
1 容器 6 透孔 7 底壁 10 スプレーノズル 12 多孔性基板 20 サイクロン 23 エジェクター DESCRIPTION OF SYMBOLS 1 Container 6 Through-hole 7 Bottom wall 10 Spray nozzle 12 Porous substrate 20 Cyclone 23 Ejector
Claims (6)
ーティング剤を噴霧し、かつ容器の底壁中央部から上向
きに吹き出す気体により上昇と下降を繰り返して粉体を
循環流動させ、造粒又はコーティング後に底壁中央部を
開口して製品を自重により流下させて系外へ排出するこ
とを特徴とする回分造粒・コーティング方法。1. A method in which a binder or a coating agent is sprayed in a container in which air is exhausted at an upper portion, and the powder is circulated and flowed by repeating rising and falling by a gas blown upward from a central portion of a bottom wall of the container. Alternatively, a batch granulation / coating method characterized in that a bottom wall center portion is opened after coating, and the product is caused to flow down by its own weight and discharged out of the system.
することを特徴とする請求項1記載の回分造粒・コーテ
ィング方法。2. The batch granulation / coating method according to claim 1, wherein the fine particles in the exhaust gas are collected by centrifugal force.
に戻すことを特徴とする請求項2記載の回分造粒・コー
ティング方法。3. The batch granulation / coating method according to claim 2, wherein the collected fine particles are returned to the powder in a descending process.
はコーティング剤を噴霧するスプレーノズルを配設し、
かつ容器の逆円錐筒状の底壁中央部に透孔を設け、気体
を上向きに吹き出す多孔性基板を上下動して上記透孔に
嵌脱可能に設けたことを特徴とする回分造粒・コーティ
ング装置。4. A spray nozzle for spraying a binder or a coating agent in a container provided with an exhaust port at an upper portion,
Batch granulation, characterized in that a through hole is provided in the center of the bottom wall of the inverted conical cylindrical shape of the container, and the porous substrate that blows out gas upwards and downwards is provided so as to be fitted into and detachable from the through hole. Coating equipment.
を特徴とする請求項4記載の回分造粒・コーティング装
置。5. The batch granulation / coating apparatus according to claim 4, wherein a cyclone is connected to the exhaust port.
内の下部周辺に戻すエジェクターを設けたことを特徴と
する請求項5記載の回分造粒・コーティング装置。6. The batch granulation / coating apparatus according to claim 5, further comprising an ejector for returning the fine particles collected by the cyclone to a lower portion of the container.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9211398A JPH1133387A (en) | 1997-07-22 | 1997-07-22 | Method and apparatus for batch granulation and coating |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9211398A JPH1133387A (en) | 1997-07-22 | 1997-07-22 | Method and apparatus for batch granulation and coating |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH1133387A true JPH1133387A (en) | 1999-02-09 |
Family
ID=16605316
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9211398A Pending JPH1133387A (en) | 1997-07-22 | 1997-07-22 | Method and apparatus for batch granulation and coating |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH1133387A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009104891A3 (en) * | 2008-02-18 | 2009-11-26 | 주식회사 참다운녹즙 | Device for producing granules from liquid materials |
CN108283912A (en) * | 2018-04-24 | 2018-07-17 | 遵义双河生物燃料科技有限公司 | Biological granular fuel granulation device |
-
1997
- 1997-07-22 JP JP9211398A patent/JPH1133387A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009104891A3 (en) * | 2008-02-18 | 2009-11-26 | 주식회사 참다운녹즙 | Device for producing granules from liquid materials |
CN108283912A (en) * | 2018-04-24 | 2018-07-17 | 遵义双河生物燃料科技有限公司 | Biological granular fuel granulation device |
CN108283912B (en) * | 2018-04-24 | 2023-11-03 | 遵义双河生物燃料科技有限公司 | Biological particle fuel pelletization device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3237596A (en) | Apparatus for coating discrete solids | |
CN112752621B (en) | Device and method for removing dust from bulk material | |
US4967688A (en) | Powder processing apparatus | |
RU2294795C2 (en) | Method of mixing of the bulk materials and the aerodynamic device for its realization | |
US3411480A (en) | Device for coating fine solids | |
JP3348280B2 (en) | Liquid substance drying method and liquid substance drying apparatus | |
CN205536898U (en) | Cyclone nozzle, vibratory liquefaction bed and vibrated fluidized bed drying system | |
JPH1133386A (en) | Method and apparatus for batchwise granulation-coating | |
WO2022001712A1 (en) | Fluidized bed | |
JPH1133387A (en) | Method and apparatus for batch granulation and coating | |
JP3126023B2 (en) | Continuous granulation and coating equipment | |
JP2004122057A (en) | Fluidized bed apparatus | |
JP3147225B2 (en) | Continuous granulation / coating method and apparatus | |
JPH05147734A (en) | Dust removing device | |
JPH08299701A (en) | Spray drying and fluidized granulating device | |
JPH1133385A (en) | Method and apparatus for granulation and coating | |
JP2003038948A (en) | Device for processing particle | |
PL204355B1 (en) | Spray-drying device | |
US3825190A (en) | Apparatus for treating granular material | |
TW202102306A (en) | Apparatus, kit and method for treatment of bulk materials | |
JP2645376B2 (en) | Particle coating method and particle coating apparatus | |
JPH031063Y2 (en) | ||
JPH0464732B2 (en) | ||
US5113598A (en) | Apparatus for powder falling gas-solid contacting operation | |
CN219318867U (en) | Material drying and dust removing system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A711 | Notification of change in applicant |
Free format text: JAPANESE INTERMEDIATE CODE: A711 Effective date: 20040716 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20050401 |
|
A621 | Written request for application examination |
Effective date: 20050401 Free format text: JAPANESE INTERMEDIATE CODE: A621 |
|
A521 | Written amendment |
Effective date: 20050404 Free format text: JAPANESE INTERMEDIATE CODE: A523 |
|
RD03 | Notification of appointment of power of attorney |
Effective date: 20061129 Free format text: JAPANESE INTERMEDIATE CODE: A7423 |
|
A521 | Written amendment |
Effective date: 20061201 Free format text: JAPANESE INTERMEDIATE CODE: A821 |
|
RD04 | Notification of resignation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7424 Effective date: 20061201 |
|
A131 | Notification of reasons for refusal |
Effective date: 20071204 Free format text: JAPANESE INTERMEDIATE CODE: A131 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20080303 |
|
A521 | Written amendment |
Effective date: 20080303 Free format text: JAPANESE INTERMEDIATE CODE: A523 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20080422 |
|
A601 | Written request for extension of time |
Effective date: 20080722 Free format text: JAPANESE INTERMEDIATE CODE: A601 |
|
A602 | Written permission of extension of time |
Effective date: 20080725 Free format text: JAPANESE INTERMEDIATE CODE: A602 |
|
A521 | Written amendment |
Effective date: 20080922 Free format text: JAPANESE INTERMEDIATE CODE: A523 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20081028 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20081117 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 3 Free format text: PAYMENT UNTIL: 20111121 |
|
R150 | Certificate of patent (=grant) or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
LAPS | Cancellation because of no payment of annual fees |