JP3747101B2 - Method and apparatus for mixing and transferring rice cake or hanging raw material and liquid - Google Patents
Method and apparatus for mixing and transferring rice cake or hanging raw material and liquid Download PDFInfo
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- JP3747101B2 JP3747101B2 JP25303496A JP25303496A JP3747101B2 JP 3747101 B2 JP3747101 B2 JP 3747101B2 JP 25303496 A JP25303496 A JP 25303496A JP 25303496 A JP25303496 A JP 25303496A JP 3747101 B2 JP3747101 B2 JP 3747101B2
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Description
【0001】
【発明の属する技術分野】
本発明は、麹又は掛原料と液体とを混合して仕込む醸造製品の生産手段へこの麹又は掛原料を液体によって流体移送する装置に関する。
【0002】
【従来の技術】
従来から、製麹装置で作られた各種麹(例えば、大豆からなる醤油麹や白米からなる日本酒用麹等)又は掛原料は、醸造過程で加えるべき液体(例えば、塩水、汲水、アルコール等)を用いた流体移送によって生産手段へ移送されることが多い。麹又は掛原料と液体とは別々に移送され、生産手段(醸造タンク等)においてはじめて撹拌、混合されることもあるが、前記のような液体を用いた流体移送にすると、生産手段における撹拌、混合の手間が省けるだけでなく、混合状態が均一になるという利点がある。
【0003】
【発明が解決しようとする課題】
上記麹又は掛原料と液体とを混合させる流体移送(以下、混合移送)では、混合割合(麹又は掛原料の移送量と液体の流量との割合、ここにいう移送量とは「単位時間当たりの移送量」、流量とは「単位時間当たりの流量」をそれぞれ意味する、以下同じ)に関して次のような問題があった。例えば、麹又は掛原料が液体に対して過剰であると、移送経路である配管やポンプが閉塞してしまう。特に、醤油麹と塩水との混合移送では、移送中に塩水を吸水した醤油麹が配管中で膨潤するため、醤油麹の移送量が多いと流動性が低下し、配管抵抗も大きくなる結果、場合によってポンプ圧が足りなくなり、醤油麹が配管に詰まってしまうのである。
【0004】
また、麹又は掛原料に対する液体の流量の割合が多い場合には、流すべき液体の総量全部が麹又は掛原料よりも先に尽きてしまい、移送終了近くになって液体が足りなくなって麹又は掛原料を移送できなくなる場合がある。むしろ、移送終了間際まで配管に残る麹又は掛原料を押し流せるように、液体が一定量以上残っている必要がある(この液体を「押水」と呼ぶ)から、実際には移送中の液体の流量は必要以上に抑える傾向にある。この液体の流量の必要以上の抑制は、麹又は掛原料の流動性の低下を招くから、結果として配管径を大きくしたり、ポンプ圧を高めたりするなど、装置構成のコスト高を惹き起こしていた。
【0005】
更に、回転円盤式製麹装置から麹の移送を開始する場合、培養床からの出麹が堆積層から周回的に薄層として麹を取り出す排出スクリュー等を用いることが多く、排出スクリューが層間を移り変わる際に微妙に出麹量が増え、麹移送の流動性を低下させて、配管を閉塞させたりする。
【0006】
そこで、麹又は掛原料と液体との混合移送における生産効率の低下、設備コストの上昇などの問題を解決すべく、前記混合移送について検討することとした。
【0007】
【課題を解決するための手段】
検討の結果開発したものが、麹又は掛原料と液体とを混合して仕込む醸造製品の生産手段へ該麹又は掛原料を液体によって流体移送する方法において、麹又は掛原料の単位時間当たりの移送量を経時的に計測し、得られた麹又は掛原料の単位時間当たりの移送量の計測値に基づいて液体の単位時間当たりの流量を加減調整し、連続的に麹又は掛原料と液体の混合移送を行い、連続的に混合割合を維持した混合物を直接醸造製品の生産手段へ移送することを特徴とする麹又は掛原料と液体との混合移送方法である。この方法を実現する装置は、麹又は掛原料と液体とを混合して仕込む醸造製品の生産手段へ該麹又は掛原料を液体によって流体移送する装置において、麹又は掛原料の単位時間当たりの移送量の経時的な計測値を取得する移送量計測手段と、該計測値に基づいて液体の単位時間当たりの流量を加減する流量制御手段と、連続的に麹又は掛原料と液体を混合移送する混合移送手段と、連続的に混合割合を維持した混合物を直接醸造製品の生産手段へ移送する移送手段とを備えている。流量制御手段は、計測値に基づいて流量を決定する計算部(例えばコンピュータや調節計等、現時点での流量をフィードバックする流量計等を含む)と、この計算部によって制御、駆動される流量調節部(例えば各種開閉バルブや回転数を増減可能なポンプ等を用いる)とからなる。
【0008】
計測値は、麹又は掛原料の移送量を把握できる変数であれば限定せず、単位時間当たりに送られる体積又は重量を、アナログ値又はディジタル値として取得する。例えば、ベルトスケールを用いながら、このベルトスケールの計測値を連続的な重量の変化を表す計測値(アナログ値)として流量制御手段に出力したり、前記計測値から更に経時的な標本値(ディジタル値)を得て流量制御手段に出力するようにしても構わない。前記例で言えば、ベルトスケールからの連続的な重量の変化を計測値として調節計のような流量制御手段へ送り込む方が、装置構成が簡単になり、計測値の正確かつ即時性が実現されるので好ましい。
【0009】
流量制御手段の計算部としては、汎用又は専用のコンピュータが考えられるほか、市販の各種調節計が利用できる。流量調節部には、液体の供給流路に配したモータコントロールバルブやエア式コントロールバルブがあるが、エア式コントロールバルブは応答性が早いので、本発明に適している。また、インバータ制御により回転数を増減可能なポンプの使用も可能である。計算部と流量調節部とは一体であってもよい。計算部として調節計を用いた場合、更に液体の現時点における流量を監視する電磁流量計等からの出力を上記麹又は掛原料の移送量の計測値と共に調節計に入力し、換算値を用いて計測値から算出した目標値と電磁流量計等の出力とが一致するように、調節計がエア式コントロールバルブを開閉するようになる。
【0010】
【発明の実施の形態】
以下、本発明の実施形態について、図を参照しながら説明する。図1は醤油麹と塩水とを混合移送する装置の構成図である。通常、麹と液体とを混合移送する場合には、麹の元原料(醤油麹においては、小麦と脱脂大豆)の容積に対して液体の量の割合が決められる。本例の装置では、総出麹量が39t、総塩水量が54kLであり、塩水は23g/100mLの濃度で元原料に対して1.2倍の容積になるよう決定している。また、押水として3kLを用いるため、醤油麹の単位重量当たりに用いられる塩水の量は、(54−3)/39≒1.31kL/tとなり、この値を換算値とする。
【0011】
装置構成について説明する。図1に見られるように、製麹機1で作られた醤油麹は、培養床2から出麹スクリュー3によって表面から薄層に削られて順次ベルトスケール4へ送り出される。このため、送り出される醤油麹の量は、各薄層毎においても変動があるが、特に層の移り替わりにおいて大きく変動する。醤油麹は混合スクリュー5においてはじめて塩水と混合され、ポンプ6を用いて仕込タンク7まで混合移送される。混合移送に用いるポンプ6は容積式ポンプが好ましい。容積式ポンプは、高濃度の被搬送物を遠距離まで搬送するのに適し、特に本発明の混合移送に適している。
【0012】
本例は、図1に見られるように、流量制御手段の計算部として調節計8を用いている。調節計8は、ベルトスケール4から醤油麹の移送量をアナログ計測値として連続的に受け取る一方、塩水タンク9から混合スクリュー5へと送り出される塩水の流量を電磁流量計10から受け取り、移送量を上記換算値(1.31kL/t)で換算して得られる目標値と前記塩水の流量とを比較し、差分がなくなるように流量調節部であるエアー式コントロールバルブ11の開度を制御する。移送量、流量は共にアナログ値として得られるので、調節計8の制御は経時的に連続である。
【0013】
本例では、計測した移送量を換算値により換算して得られる目標値と現時点での流量とを比較するという手法を用いている。これは、醤油麹の移送量に対する塩水の流量を正確に制御するためであり、エアー式コントロールバルブ11の開閉量に対して塩水の流量が外因(水圧や外気温による微妙な配管径の拡縮等)により変動することを考慮したものである。仮に、エアー式コントロールバルブ11の開閉量に対して塩水の量が一義的に定まり、変動もなければ、塩水の現時点の流量を計測せず、醤油麹の移送量の計測値を換算値により換算して得られた制御値を基にしてエアー式コントロールバルブ11を開閉してもよい。
【0014】
図2は清酒掛米と汲水とを混合移送する装置の構成図である。本例の装置は、清酒掛米(蒸米)が1080kg(白米800kg)、汲水量が1500Lであるが、汲水のうち200Lを押水として用いるため、清酒掛米の単位重量当たりに用いられる汲水の量は、(1500-200)/1080≒1.2L/kgとなり、この値を換算値としている。清酒掛米は、蒸米機12へ浸漬米を送り込んで造り、放冷機13を経て、ベルトスケール4へ送られる。なお、ベルトスケール4より後については、仕込タンク7が醗酵タンク14に変わっただけで、構成的には違いはないので、説明は省略する。
【0015】
図3は味醂用麹とアルコールとを混合移送する装置の構成図である。本例の装置では、味醂用麹が600kg、35%アルコールが1900kgであるが、アルコールのうち400kgを押出アルコール(押水に相当)として用いるため、味醂用麹の単位重量当たりに用いられるアルコールの量は、(1900-400)/600=2.5kg/kgで、この値を換算値としている。装置構成は、塩水タンク9がアルコールタンク15になり、図1の電磁流量計10に代えて渦流量計17を用いているほかはほぼ図1の例と同じであるので説明は省略するが、混合移送の終端付近、仕込タンク7への入口前において、味醂用麹とアルコールとの混合物に掛原料として蒸糯米を加え、すべてを混合スクリュー16にて混合して仕込タンク7へ仕込んでいる。
【0016】
【発明の効果】
本発明により、麹又は掛原料と液体との混合移送において、両者の適切な割合維持が自動化できるようになり、生産効率が向上する。また、簡単な装置構成であるため設備コストの上昇を招く虞がなく、むしろ最適な混合移送が実現でき、麹又は掛原料と液体とがうまく混合された状態で仕込タンクや醗酵タンク等へ送られるため、製品品質の向上が図れるようになるから、生産に掛かる費用対効果を大幅に改善できるようになる。
【図面の簡単な説明】
【図1】醤油麹と塩水とを混合移送する装置の構成図である。
【図2】清酒掛米と汲水とを混合移送する装置の構成図である。
【図3】味醂用麹とアルコールとを混合移送する装置の構成図である。
【符号の説明】
1 製麹機
2 培養床
3 出麹スクリュー
4 ベルトスケール
5 混合スクリュー
6 ポンプ
7 仕込タンク
8 調節計
9 塩水タンク
10 電磁流量計
11 エアー式コントロールバルブ
12 蒸米機
13 放冷機
14 醗酵タンク
15 アルコールタンク
16 混合スクリュー
17 渦流量計[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an apparatus for fluidly transferring a koji or hanging raw material by means of a liquid to a production means of a brewed product in which the koji or hanging raw material is mixed with a liquid.
[0002]
[Prior art]
Conventionally, various types of koji (such as soy sauce koji made of soybeans and rice koji for sake made of white rice) made from koji making apparatus or liquids to be added in the brewing process (e.g. salt water, pumped water, alcohol etc.) ) Is often transferred to the production means by fluid transfer. The koji or hanging raw material and the liquid are transferred separately, and may be stirred and mixed for the first time in the production means (brewing tank etc.), but if the fluid transfer using the liquid as described above, the stirring in the production means, There is an advantage that not only the trouble of mixing can be saved, but also the mixing state becomes uniform.
[0003]
[Problems to be solved by the invention]
In the fluid transfer (hereinafter referred to as “mixed transfer”) that mixes the soot or hanging raw material with the liquid, the mixing ratio (the ratio between the transfer amount of the soot or hanging raw material and the flow rate of the liquid, the transfer amount referred to here is “per unit time”. "Transported quantity" and "flow rate" mean "flow rate per unit time", respectively, and so on). For example, if the soot or the hanging raw material is excessive with respect to the liquid, the piping or pump that is the transfer path is blocked. In particular, in the mixed transfer of soy sauce cake and salt water, the soy sauce cake that absorbed the salt water during the transfer swells in the pipe, so if the amount of soy sauce cake transferred is large, the fluidity decreases and the pipe resistance increases, In some cases, the pump pressure is insufficient, and soy sauce cake is clogged in the piping.
[0004]
In addition, when the ratio of the flow rate of the liquid to the soot or hanging raw material is large, the total amount of the liquid to be flowed out before the soot or hanging raw material, and the liquid becomes insufficient near the end of the transfer. It may become impossible to transfer the hanging material. Rather, a certain amount or more of the liquid needs to remain so that the soot or hanging material remaining in the pipe can be swept away until the end of the transfer (this liquid is called `` push water ''). The flow rate tends to be suppressed more than necessary. This excessive control of the flow rate of the liquid causes a decrease in the fluidity of the dredging or hanging material, and as a result, increases the cost of the apparatus configuration, such as increasing the pipe diameter or increasing the pump pressure. It was.
[0005]
Furthermore, when the transfer of the cocoons from the rotary disk-type slag-making apparatus is started, a discharge screw or the like that takes out the cocoons from the culture bed as a thin layer around the culture bed is often used. When changing, the amount of dredging increases slightly, reducing the flowability of dredging and closing the piping.
[0006]
In view of this, in order to solve problems such as a decrease in production efficiency and an increase in equipment cost in the mixed transfer of the koji or hanging raw material and liquid, the mixed transfer was examined.
[0007]
[Means for Solving the Problems]
Was developed result of examination is, koji or multiply material and the koji or multiply material and a liquid to the means of production of brewed products charged and mixed in a method of fluid transfer by the liquid, the transfer per unit time of koji or hanging material The amount of liquid is measured over time, and the flow rate per unit time of liquid is adjusted based on the measured value of the transferred amount of the soot or hanging material per unit time . and mixed and transported, it is mixed-transfer method of the koji or hanging material and a liquid, characterized in that transferring the mixture was maintained continuously mixing ratio directly brewed product production unit. An apparatus for realizing this method is a device for fluidly transferring the koji or hanging raw material by means of liquid to the production means of the brewed product in which the koji or hanging raw material and liquid are mixed, and transferring the koji or hanging raw material per unit time. a transfer amount measuring means for obtaining a temporal measurement of the amount, and flow control means for adjusting the flow rate per unit time of the liquid on the basis of the measurement value, continuously mixing transferring koji or hanging material and a liquid Mixing and transferring means, and transferring means for transferring the mixture, which is continuously maintained in the mixing ratio, directly to the brewing product producing means are provided. The flow rate control means includes a calculation unit that determines the flow rate based on the measured value (including a flow meter that feeds back the current flow rate, such as a computer or a controller), and a flow rate control that is controlled and driven by this calculation unit. Part (for example, using various open / close valves and a pump capable of increasing / decreasing the number of revolutions).
[0008]
The measured value is not limited as long as it is a variable that can grasp the transfer amount of the soot or hanging raw material, and the volume or weight sent per unit time is acquired as an analog value or a digital value. For example, while using a belt scale, the measurement value of the measurement value representing a continuous change in weight of the belt scale or output to the flow control means as (analog value), further over time sample value from the measured value (digital Value) may be obtained and output to the flow rate control means. In the above example, if the continuous weight change from the belt scale is sent as a measurement value to a flow rate control means such as a controller, the device configuration becomes simpler, and the measurement value is accurate and instantaneous. Therefore, it is preferable .
[0009]
As the calculation unit of the flow rate control means, a general purpose or dedicated computer can be considered, and various commercially available controllers can be used. The flow rate adjusting unit includes a motor control valve and an air control valve arranged in the liquid supply flow path. The air control valve is suitable for the present invention because of its quick response. It is also possible to use a pump that can increase or decrease the rotational speed by inverter control. The calculation unit and the flow rate adjustment unit may be integrated. When a controller is used as the calculation unit, the output from an electromagnetic flow meter or the like that monitors the current flow rate of the liquid is further input to the controller together with the measured value of the amount of the soot or hanging material transferred, and the converted value is used. The controller opens and closes the pneumatic control valve so that the target value calculated from the measured value matches the output of the electromagnetic flow meter or the like.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a configuration diagram of an apparatus for mixing and transferring soy sauce cake and salt water. Normally, when the koji and the liquid are mixed and transferred, the ratio of the amount of the liquid to the volume of the koji raw material (in the case of soy sauce koji, wheat and defatted soybean) is determined. In the apparatus of the present example, the total amount of dredging is 39 t, the total amount of salt water is 54 kL, and the salt water is determined to be 1.2 times the volume of the original raw material at a concentration of 23 g / 100 mL. In addition, since 3 kL is used as the pushing water, the amount of salt water used per unit weight of the soy sauce cake is (54-3) /39≈1.31 kL / t, and this value is used as a conversion value.
[0011]
The apparatus configuration will be described. As can be seen in FIG. 1, the soy sauce cake produced by the koji making machine 1 is cut into a thin layer from the surface by the tapping
[0012]
In this example, as shown in FIG. 1, a
[0013]
In this example, a method of comparing a target value obtained by converting the measured transfer amount with a conversion value and the current flow rate is used. This is to accurately control the flow rate of salt water relative to the transfer amount of soy sauce cake, and the flow rate of salt water is external to the open / close amount of the air control valve 11 (such as subtle expansion and contraction of pipe diameter due to water pressure and external temperature). ) Due to fluctuations. If the amount of salt water is uniquely determined with respect to the opening / closing amount of the
[0014]
FIG. 2 is a block diagram of an apparatus for mixing and transferring sake sake rice and pumped water. The apparatus of this example has a sake sake rice (steamed rice) of 1080 kg (white rice 800 kg) and a pumped water volume of 1500 L, but because 200 L of the pumped water is used as pushing water, the pumped water used per unit weight of sake sake rice The amount of is (1500-200) /1080≒1.2L/kg, and this value is the converted value. The sake rice cake is made by sending the soaked rice to the steamed
[0015]
FIG. 3 is a block diagram of an apparatus for mixing and transferring miso soup and alcohol. In the apparatus of this example, miso koji is 600 kg and 35% alcohol is 1900 kg, but 400 kg of alcohol is used as extruded alcohol (corresponding to pushing water), so the amount of alcohol used per unit weight of miso koji Is (1900-400) /600=2.5kg/kg, and this value is used as the conversion value. The apparatus configuration is substantially the same as the example of FIG. 1 except that the
[0016]
【The invention's effect】
According to the present invention, it becomes possible to automate the maintenance of an appropriate ratio of the straw or the hanging raw material and the liquid in the mixed transfer, thereby improving the production efficiency. Further, there is no fear that causes an increase in simple apparatus structure a is for equipment cost, rather optimal mixing transfer can be realized, koji or hanging material and a liquid and is Komita tank or fermentation tanks specification in admixture successfully Since the product quality can be improved, the cost-effectiveness of production can be greatly improved.
[Brief description of the drawings]
FIG. 1 is a configuration diagram of an apparatus for mixing and transferring soy sauce cake and salt water.
FIG. 2 is a configuration diagram of an apparatus for mixing and transferring sake sake rice and pumped water.
FIG. 3 is a configuration diagram of an apparatus for mixing and transferring miso miso and alcohol.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1
10 Electromagnetic flow meter
11 Pneumatic control valve
12 Steamed rice machine
13 Cooler
14 Fermentation tank
15 Alcohol tank
16 mixing screw
17 Vortex flowmeter
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25303496A JP3747101B2 (en) | 1996-09-25 | 1996-09-25 | Method and apparatus for mixing and transferring rice cake or hanging raw material and liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25303496A JP3747101B2 (en) | 1996-09-25 | 1996-09-25 | Method and apparatus for mixing and transferring rice cake or hanging raw material and liquid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH1095531A JPH1095531A (en) | 1998-04-14 |
JP3747101B2 true JP3747101B2 (en) | 2006-02-22 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25303496A Expired - Lifetime JP3747101B2 (en) | 1996-09-25 | 1996-09-25 | Method and apparatus for mixing and transferring rice cake or hanging raw material and liquid |
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JP (1) | JP3747101B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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JP4143992B2 (en) * | 2000-08-02 | 2008-09-03 | 永田醸造機械株式会社 | Method and apparatus for charging alcoholic beverages with alcoholic fermentation |
JP4916622B2 (en) * | 2001-05-25 | 2012-04-18 | 株式会社フジワラテクノアート | Apparatus and method for transferring tube of solid-liquid mixture |
JP5876656B2 (en) * | 2011-03-08 | 2016-03-02 | 株式会社フジワラテクノアート | How to transport the saltwater mixture |
JP6530908B2 (en) * | 2014-12-09 | 2019-06-12 | 株式会社フジワラテクノアート | Solid-liquid mixture transport apparatus and solid-liquid mixture transport method. |
-
1996
- 1996-09-25 JP JP25303496A patent/JP3747101B2/en not_active Expired - Lifetime
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Publication number | Publication date |
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JPH1095531A (en) | 1998-04-14 |
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