JP2008119600A - Method for mixing powder and powder mixer - Google Patents
Method for mixing powder and powder mixer Download PDFInfo
- Publication number
- JP2008119600A JP2008119600A JP2006306435A JP2006306435A JP2008119600A JP 2008119600 A JP2008119600 A JP 2008119600A JP 2006306435 A JP2006306435 A JP 2006306435A JP 2006306435 A JP2006306435 A JP 2006306435A JP 2008119600 A JP2008119600 A JP 2008119600A
- Authority
- JP
- Japan
- Prior art keywords
- wall
- powder
- water
- activated carbon
- water stream
- 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
- 239000000843 powder Substances 0.000 title claims abstract description 59
- 238000000034 method Methods 0.000 title claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 109
- 230000007423 decrease Effects 0.000 claims description 6
- 238000002347 injection Methods 0.000 claims description 6
- 239000007924 injection Substances 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 122
- 239000000203 mixture Substances 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Images
Abstract
Description
本発明は、粉末混合方法および粉末混合器に関し、さらに詳しくは、粉末が水上に浮いてしまうことを抑制し、好適に粉末を水に混合することが出来る粉末混合方法および粉末混合器に関する。 The present invention relates to a powder mixing method and a powder mixer, and more particularly to a powder mixing method and a powder mixer capable of suppressing powder from floating on water and suitably mixing the powder with water.
従来、流水上に粉末活性炭を落下させながら、落下する粉末活性炭に向けて斜め上から下向きに水を噴射して、粉末活性炭と水とを混合する混合器が知られている(例えば、特許文献1参照。)。
上記従来の混合器では、水上に粉末活性炭を落下させただけでは粉末活性炭が水上に浮いてしまうため、落下する粉末活性炭に向けて水を噴射することにより噴射水で粉末活性炭を押さえ込んでいる。
しかし、粉末活性炭が上から連続して落下してくるため、噴射水で粉末活性炭を完全に押さえ込むことが出来ず、一部の粉末活性炭が水上に浮いてしまう問題点があった。
そこで、本発明の目的は、粉末が水上に浮いてしまうことを抑制し、好適に粉末を水に混合することが出来る粉末混合方法および粉末混合器を提供することにある。
In the conventional mixer, since the powdered activated carbon floats on the water simply by dropping the powdered activated carbon on the water, the powdered activated carbon is pressed down with the spray water by spraying water toward the powdered activated carbon.
However, since the powdered activated carbon falls continuously from above, the powdered activated carbon cannot be completely pressed down with the jet water, and there is a problem that some powdered activated carbon floats on the water.
Therefore, an object of the present invention is to provide a powder mixing method and a powder mixer capable of suppressing powder from floating on water and suitably mixing the powder with water.
第1の観点では、本発明は、第1の水流を混合容器の上部内壁に沿って旋回しながら落下させる第1のステップと、前記旋回する第1の水流に対して上方から粉末を落下させる第2のステップと、前記上部内壁に沿って旋回しながら前記粉末を搬送する前記第1の水流に対して上方から第2の水流を被せるように合流させる第3のステップと、前記合流した水流を前記混合容器の下部内壁に沿って旋回させながら落下させる第4のステップとを有することを特徴とする粉末混合方法を提供する。
上記第1の観点による粉末混合方法では、第1の水流上に粉末(粉末活性炭や消石灰など)を落下させた後、その上に第2の水流を被せ、第1の水流と第2の水流の間に粉末が挟まれるため、粉末が水上に浮いてしまうことを抑制できる。そして、第1の水流と粉末と第2の水流とが旋回することにより混合されるから、好適に粉末を水に混合することが出来る。
In the first aspect, the present invention provides a first step of dropping the first water stream while swirling along the upper inner wall of the mixing container, and dropping the powder from above with respect to the swirling first water stream. A second step, a third step for joining the first water flow for conveying the powder while swirling along the upper inner wall so as to cover the second water flow from above, and the combined water flow And a fourth step of dropping while swirling along the lower inner wall of the mixing container.
In the powder mixing method according to the first aspect, after a powder (powdered activated carbon, slaked lime, etc.) is dropped on the first water stream, the second water stream is put on the powder, and the first water stream and the second water stream are covered. Since the powder is sandwiched between them, it can be suppressed that the powder floats on the water. Since the first water stream, the powder, and the second water stream are mixed by swirling, the powder can be suitably mixed with water.
第2の観点では、本発明は、水平断面円形の内壁を有する混合容器と、前記混合容器の上部内壁に沿って旋回しながら落下するように前記上部内壁に向けて第1の水流を噴射する第1の給水ノズルと、前記旋回する第1の水流に対して上方から粉末を落下させる粉末注入管と、前記上部内壁に沿って旋回しながら前記粉末を搬送する前記第1の水流に対して上方から第2の水流を被せるように合流させる第2の給水ノズルと、前記合流した水流が旋回しながら落下する前記混合容器の下部内壁とを具備したことを特徴とする粉末混合器を提供する。
上記第2の観点による粉末混合器では、前記第1の観点による粉末混合方法を好適に実施できる。
In a second aspect, the present invention injects a first water flow toward the upper inner wall so as to fall while swirling along the upper inner wall of the mixing container, and a mixing container having a circular inner wall with a horizontal section. For a first water supply nozzle, a powder injection tube for dropping powder from above with respect to the swirling first water flow, and for the first water flow for conveying the powder while swirling along the upper inner wall Provided is a powder mixer comprising a second water supply nozzle for joining so as to cover a second water flow from above, and a lower inner wall of the mixing container in which the joined water flow falls while swirling. .
In the powder mixer according to the second aspect, the powder mixing method according to the first aspect can be suitably implemented.
第3の観点では、本発明は、前記第2の観点による粉末混合器において、前記上部内壁が円筒状であり、前記下部内壁は前記上部内壁よりも内径が小さい円筒状であり、それらの中間部は漏斗状になっていることを特徴とする粉末混合器を提供する。
上記第3の観点による粉末混合器では、混合容器の上部で第1の水流と粉末と第2の水流の旋回流を作り、その旋回流を混合容器の下部へ向けて半径を絞り込むことで周速度を高速化し、全体を好適に混合することが出来る。また、構造的に製造し易い。
In a third aspect, the present invention provides the powder mixer according to the second aspect, wherein the upper inner wall is cylindrical, and the lower inner wall is cylindrical with an inner diameter smaller than that of the upper inner wall. The powder mixer is characterized in that the part has a funnel shape.
In the powder mixer according to the third aspect, a swirl flow of the first water flow, the powder, and the second water flow is created in the upper part of the mixing container, and the swirl flow is directed toward the lower part of the mixing container to reduce the radius. The speed can be increased and the whole can be suitably mixed. Moreover, it is easy to manufacture structurally.
第4の観点では、本発明は、前記第2の観点による粉末混合器において、前記上部内壁から前記下部内壁まで内径が徐々に小さくなる漏斗状であることを特徴とする粉末混合器を提供する。
上記第4の観点による粉末混合器では、混合容器の上部で第1の水流と粉末と第2の水流の旋回流を作り、その旋回流を混合容器の下部へ向けて半径を絞り込むことで周速度を高速化し、全体を好適に混合することが出来る。また、内壁に粉末が付着・堆積し難い。
In a fourth aspect, the present invention provides the powder mixer according to the second aspect, wherein the powder mixer has a funnel shape in which the inner diameter gradually decreases from the upper inner wall to the lower inner wall. .
In the powder mixer according to the fourth aspect, a swirl flow of the first water flow, the powder, and the second water flow is formed at the upper part of the mixing container, and the swirl flow is directed toward the lower part of the mixing container to reduce the radius. The speed can be increased and the whole can be suitably mixed. In addition, it is difficult for powder to adhere to and accumulate on the inner wall.
第5の観点では、本発明は、前記第2の観点による粉末混合器において、前記上部内壁が下方へ向けて内径が徐々に小さくなる漏斗状であり且つ前記下部内壁は円筒状であることを特徴とする粉末混合器を提供する。
上記第5の観点による粉末混合器では、混合容器の上部で第1の水流と粉末と第2の水流の旋回流を作り、その旋回流を混合容器の下部へ向けて半径を絞り込むことで周速度を高速化し、全体を好適に混合することが出来る。また、構造的に製造しやすい。
In a fifth aspect, the present invention provides the powder mixer according to the second aspect, wherein the upper inner wall has a funnel shape in which an inner diameter gradually decreases downward, and the lower inner wall has a cylindrical shape. A powder mixer is provided.
In the powder mixer according to the fifth aspect, a swirl flow of the first water flow, the powder, and the second water flow is created at the upper part of the mixing container, and the swirl flow is directed toward the lower part of the mixing container to reduce the radius. The speed can be increased and the whole can be suitably mixed. Moreover, it is easy to manufacture structurally.
本発明の粉末混合器によれば、粉末が水上に浮いてしまうことを抑制し、好適に粉末を水に混合することが出来る。 According to the powder mixer of the present invention, the powder can be prevented from floating on the water, and the powder can be suitably mixed with water.
以下、図に示す実施の形態により本発明をさらに詳細に説明する。なお、これにより本発明が限定されるものではない。 Hereinafter, the present invention will be described in more detail with reference to embodiments shown in the drawings. Note that the present invention is not limited thereby.
図1は、実施例1に係る粉末活性炭混合器100の縦断面図である。また、図2は、同上面図である。
この粉末活性炭混合器100は、上部内壁1aが円筒状であり且つ下部内壁1bは上部内壁1aよりも内径が小さい円筒状であり且つそれらの中間部1cは漏斗状になっている混合容器1と、混合容器1の上部内壁1aに沿って旋回しながら落下するように上部内壁1aに向けて第1の水流(図3のW1)を噴射する第1の給水ノズル2と、旋回する第1の水流(図3のW1)に対して上方から粉末活性炭(図3のP)を落下させる粉末活性炭注入管3と、上部内壁1aに沿って旋回しながら粉末活性炭Pを搬送する第1の水流(図3のW1)に対して上方から第2の水流(図3のW2)を合流させる第2の給水ノズル4とを具備している。
FIG. 1 is a longitudinal sectional view of a powdered activated
This powder activated
図3および図4に示すように、第1の給水ノズル2から上部内壁1aに向けて第1の水流W1を噴射すると、第1の水流W1は上部内壁1aに沿って旋回しながら落下する。その旋回しながら落下する第1の水流W1上に粉末活性炭注入管3から粉末活性炭Pを落下させると、第1の水流W1が粉末活性炭Pを乗せて上部内壁1aに沿って旋回しながら落下する。
図5に示すように、第2の給水ノズル4から上部内壁1aに向けて第2の水流W2を噴射すると、粉末活性炭Pを乗せて旋回しながら落下する第1の水流W1上の粉末活性炭Pの上に第2の水流W2が被さり(そうなるように配置してある)、第1の水流W1と第2の水流W2の間に粉末活性炭Pが挟まれる。
そして、第1の水流W1と粉末活性炭Pと第2の水流W2とが中間部1cや下部内壁1bに沿って高速周速度で旋回することにより、好適に粉末活性炭Pを水に混合することが出来る。
As shown in FIGS. 3 and 4, when the first water flow W1 is injected from the first
As shown in FIG. 5, when the second water flow W2 is sprayed from the second
The first activated water stream W1, the powdered activated carbon P, and the second activated water stream W2 are swirled at a high speed peripheral speed along the intermediate portion 1c and the lower inner wall 1b, so that the powdered activated carbon P can be suitably mixed with water. I can do it.
なお、粉末活性炭混合器100は浄水施設における着水井の上方に設置されており、粉末活性炭Pと水の混合流は着水井の注入点に放出される。
The powdered activated
実施例1の粉末活性炭混合器100によれば、粉末活性炭Pが水上に浮いてしまうことを抑制し、好適に粉末活性炭Pを水に混合することが出来る。また、製造し易い構造の混合容器1になっている。
According to the powdered activated
図6は、実施例2に係る粉末活性炭混合器200の縦断面図である。また、図7は、同上面図である。
この粉末活性炭混合器200では、上部内壁1aから下部内壁1bまで内径が徐々に小さくなる漏斗状の混合容器1を用いている。他の構成は実施例1と同様である。
FIG. 6 is a longitudinal sectional view of the powdered activated
The powdered activated
実施例2の粉末活性炭混合器200によれば、粉末活性炭Pが水上に浮いてしまうことを抑制し、好適に粉末活性炭Pを水に混合することが出来る。また、粉末活性炭Pが付着・堆積し難い構造の混合容器1になっている。
According to the powdered activated
図8は、実施例3に係る粉末活性炭混合器300の縦断面図である。また、図9は、同上面図である。
この粉末活性炭混合器300では、上部内壁1aは下方へ向けて内径が徐々に小さくなる漏斗状になっており且つ下部内壁1bは円筒状になっている混合容器1を用いている。他の構成は実施例1と同様である。
FIG. 8 is a longitudinal sectional view of the powdered activated
In the powdered activated
実施例3の粉末活性炭混合器300によれば、粉末活性炭Pが水上に浮いてしまうことを抑制し、好適に粉末活性炭Pを水に混合することが出来る。また、構造的に製造しやすい。
According to the powdered activated
第2の水流を被せた旋回流にさらに第3の水流を被せる第3の給水ノズルを設けてもよい。
同様に、さらに水流を被せる第4の給水ノズル等を設けてもよい。
You may provide the 3rd water supply nozzle which covers a swirl flow which covered the 2nd water flow further, and covers a 3rd water flow.
Similarly, you may provide the 4th water supply nozzle etc. which cover a water flow further.
本発明の粉末混合器は、例えば浄水施設で粉末活性炭や消石灰を水に混合するのに利用できる。 The powder mixer of the present invention can be used, for example, to mix powdered activated carbon or slaked lime with water in a water purification facility.
1 混合容器
1a 上部内壁
1b 下部内壁
1c 中間部
2 第1の給水ノズル
3 粉末活性炭注入管
4 第2の給水ノズル
100,200 粉末活性炭混合器
P 粉末活性炭
W1 第1の水流
W2 第2の水流
DESCRIPTION OF
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006306435A JP4889452B2 (en) | 2006-11-13 | 2006-11-13 | Powder mixing method and powder mixer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006306435A JP4889452B2 (en) | 2006-11-13 | 2006-11-13 | Powder mixing method and powder mixer |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2008119600A true JP2008119600A (en) | 2008-05-29 |
JP4889452B2 JP4889452B2 (en) | 2012-03-07 |
Family
ID=39504939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2006306435A Active JP4889452B2 (en) | 2006-11-13 | 2006-11-13 | Powder mixing method and powder mixer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP4889452B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101934159A (en) * | 2009-06-30 | 2011-01-05 | 江苏瀚深水业科技发展有限公司 | Powdery active carbon (PAC) tiptronic wet-type feeding device and dust absorption device thereof |
CN101935084A (en) * | 2009-06-30 | 2011-01-05 | 江苏瀚深水业科技发展有限公司 | Dust absorbing device for storage hopper in wet powdered activated carbon dosing equipment |
CN101935083A (en) * | 2009-06-30 | 2011-01-05 | 江苏瀚深水业科技发展有限公司 | Dust absorbing device of mixing barrel in automatic wet powdery activated carbon adding equipment |
CN101935082A (en) * | 2009-06-30 | 2011-01-05 | 江苏瀚深水业科技发展有限公司 | Dust absorption device for mixing drum in powder activated carbon manual wet-type feeding device |
JP2012082110A (en) * | 2010-10-13 | 2012-04-26 | Bio Coke Lab Co Ltd | Hydrogen generation apparatus |
JP2013193033A (en) * | 2012-03-21 | 2013-09-30 | Kureha Ecology Management Co Ltd | Method for producing activated carbon slurry |
JP2016218048A (en) * | 2015-05-21 | 2016-12-22 | 株式会社堀場製作所 | Sample introduction device |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4712203Y1 (en) * | 1968-07-31 | 1972-05-06 | ||
JPS56136631A (en) * | 1980-12-13 | 1981-10-26 | Osaka Gas Co Ltd | Mixing device |
JPS5771628A (en) * | 1980-10-20 | 1982-05-04 | Osaka Gas Co Ltd | Mixer |
JPS5796022A (en) * | 1980-10-20 | 1982-06-15 | Hoechst Ag | Method of dispersing and dissolving polymer powder and device therefor |
JPS60168533A (en) * | 1984-02-13 | 1985-09-02 | Inoue Japax Res Inc | Apparatus for synthesis of polishing particle |
JPH04227836A (en) * | 1990-06-06 | 1992-08-17 | Uk Atomic Energy Authority | Method and device for mixing liquid and solid |
JPH05234A (en) * | 1991-06-24 | 1993-01-08 | Catalysts & Chem Ind Co Ltd | Apparatus for mixing powder into liquid |
JP2003205228A (en) * | 1997-12-30 | 2003-07-22 | Hirobumi Onari | Turning type fine bubbles production apparatus |
WO2004076042A1 (en) * | 2003-02-28 | 2004-09-10 | Okutama Kogyo Co., Ltd. | Mixing device and slurrying device |
-
2006
- 2006-11-13 JP JP2006306435A patent/JP4889452B2/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4712203Y1 (en) * | 1968-07-31 | 1972-05-06 | ||
JPS5771628A (en) * | 1980-10-20 | 1982-05-04 | Osaka Gas Co Ltd | Mixer |
JPS5796022A (en) * | 1980-10-20 | 1982-06-15 | Hoechst Ag | Method of dispersing and dissolving polymer powder and device therefor |
JPS56136631A (en) * | 1980-12-13 | 1981-10-26 | Osaka Gas Co Ltd | Mixing device |
JPS60168533A (en) * | 1984-02-13 | 1985-09-02 | Inoue Japax Res Inc | Apparatus for synthesis of polishing particle |
JPH04227836A (en) * | 1990-06-06 | 1992-08-17 | Uk Atomic Energy Authority | Method and device for mixing liquid and solid |
JPH05234A (en) * | 1991-06-24 | 1993-01-08 | Catalysts & Chem Ind Co Ltd | Apparatus for mixing powder into liquid |
JP2003205228A (en) * | 1997-12-30 | 2003-07-22 | Hirobumi Onari | Turning type fine bubbles production apparatus |
WO2004076042A1 (en) * | 2003-02-28 | 2004-09-10 | Okutama Kogyo Co., Ltd. | Mixing device and slurrying device |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101934159A (en) * | 2009-06-30 | 2011-01-05 | 江苏瀚深水业科技发展有限公司 | Powdery active carbon (PAC) tiptronic wet-type feeding device and dust absorption device thereof |
CN101935084A (en) * | 2009-06-30 | 2011-01-05 | 江苏瀚深水业科技发展有限公司 | Dust absorbing device for storage hopper in wet powdered activated carbon dosing equipment |
CN101935083A (en) * | 2009-06-30 | 2011-01-05 | 江苏瀚深水业科技发展有限公司 | Dust absorbing device of mixing barrel in automatic wet powdery activated carbon adding equipment |
CN101935082A (en) * | 2009-06-30 | 2011-01-05 | 江苏瀚深水业科技发展有限公司 | Dust absorption device for mixing drum in powder activated carbon manual wet-type feeding device |
CN101934159B (en) * | 2009-06-30 | 2013-02-13 | 江苏瀚深水业科技发展有限公司 | Powdery active carbon (PAC) tiptronic wet-type feeding device and dust absorption device thereof |
CN101935083B (en) * | 2009-06-30 | 2013-02-13 | 江苏瀚深水业科技发展有限公司 | Dust absorbing device of mixing barrel in automatic wet powdery activated carbon adding equipment |
JP2012082110A (en) * | 2010-10-13 | 2012-04-26 | Bio Coke Lab Co Ltd | Hydrogen generation apparatus |
JP2013193033A (en) * | 2012-03-21 | 2013-09-30 | Kureha Ecology Management Co Ltd | Method for producing activated carbon slurry |
JP2016218048A (en) * | 2015-05-21 | 2016-12-22 | 株式会社堀場製作所 | Sample introduction device |
Also Published As
Publication number | Publication date |
---|---|
JP4889452B2 (en) | 2012-03-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP4889452B2 (en) | Powder mixing method and powder mixer | |
UA102979C2 (en) | Modular planetary concrete mixer for concrete production | |
CN207871876U (en) | A kind of wet desulphurization swirling flow atomizing spray equipment | |
CN208771380U (en) | For being distributed the system and reaction chamber of gas phase and/or liquid phase in the reaction chamber | |
CN203291984U (en) | Two-in-one nozzle | |
CN103979665A (en) | Double-fluid micro-bubble spraying generating device | |
CN106823763A (en) | A kind of spray equipment for rotating arrangement | |
NO20064529L (en) | Drikkeroreanordning. | |
CN201500604U (en) | Two-fluid spray nozzle | |
CN102228784A (en) | Fluidized bed semidry flue gas purifier | |
CN103041689A (en) | Liquid distribution device for absorption tower | |
CN202315693U (en) | Slurry bottom flow type wet desulphurization device | |
CN101992159B (en) | Two-fluid nozzle | |
CN202161917U (en) | Fluidized bed semidry-method smoke purifying device | |
CN205269988U (en) | Flue gas deacidification atomizer | |
CN211753908U (en) | Slurry redistribution ring for desulfurizing tower | |
JP2008168263A (en) | Mixing method of powder with liquid and its device | |
CN209396924U (en) | Multichannel three-phase nozzle | |
CN102728212B (en) | Desulfurizing absorption tower provided with high-potential energy unpowered slurry mixing device | |
CN206881964U (en) | A kind of modifying agent atomising device | |
CN203794684U (en) | Dual-fluid microbubble jet generation device | |
CN106257140A (en) | Flue gas processing device and method and stove conduit | |
CN206631431U (en) | A kind of desulfurizing tower with desulfurization spray servicing unit | |
CN204824670U (en) | A fuel sprayer for producing ammonium nitrate fuel oil explosive | |
CN207872180U (en) | Supercritical oxidation reactor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20090522 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20101220 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20110712 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20110804 |
|
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: 20111213 |
|
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: 20111213 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 4889452 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20141222 Year of fee payment: 3 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |