JP5812237B2 - Precipitation device for sediment in water tank - Google Patents
Precipitation device for sediment in water tank Download PDFInfo
- Publication number
- JP5812237B2 JP5812237B2 JP2010229054A JP2010229054A JP5812237B2 JP 5812237 B2 JP5812237 B2 JP 5812237B2 JP 2010229054 A JP2010229054 A JP 2010229054A JP 2010229054 A JP2010229054 A JP 2010229054A JP 5812237 B2 JP5812237 B2 JP 5812237B2
- Authority
- JP
- Japan
- Prior art keywords
- screw
- water
- sediment
- separation
- pressure
- 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.)
- Active
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 66
- 239000013049 sediment Substances 0.000 title claims description 33
- 238000001556 precipitation Methods 0.000 title description 6
- 238000000926 separation method Methods 0.000 claims description 33
- 239000010802 sludge Substances 0.000 claims description 29
- 238000004062 sedimentation Methods 0.000 claims description 10
- 239000002244 precipitate Substances 0.000 claims description 8
- 230000007717 exclusion Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 description 5
- 230000005484 gravity Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000011295 pitch Substances 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
Images
Landscapes
- Treatment Of Sludge (AREA)
Description
本発明は一般水槽や水処理設備の沈殿分離槽内の沈殿物を槽外に排除する装置に関するものである。 The present invention relates to an apparatus for removing precipitates in a sedimentation separation tank of a general water tank or a water treatment facility.
水槽内の沈殿物を排除、或いは回収するためには、チェーンやロープに掻き板を取付け一定方向に掻き寄せ、或いは、上半を開放したケースとスクリューで構成するスクリューコンベヤーで一定方向に移送集積した後、遠心ポンプや容積形ポンプで吸引、或いは垂直や傾斜して配設したスクリューコンベヤーを用いて水槽外に排除する等の方法がある。 In order to eliminate or collect sediment in the water tank, a scraper is attached to the chain or rope, scraped in a certain direction, or transported and accumulated in a certain direction by a screw conveyor consisting of a case and screw with the upper half open. After that, there is a method of suctioning with a centrifugal pump or a positive displacement pump, or removing it outside the water tank using a screw conveyor arranged vertically or inclined.
集積した沈殿物汚泥を遠心ポンプや容積形ポンプを使用して水槽外に排出する方法にあっては、集積汚泥量とポンプ排出量を終始一致させることは、検出技術が発達した今日においても非常に困難なことであり、沈殿物を沈殿状態以下の水分量で排除回収することは至難なことであり、結局、余分な水分も吸入させて排除しているのが現状である。 In the method of discharging accumulated sediment sludge to the outside of the water tank using a centrifugal pump or positive displacement pump, it is very important that the accumulated sludge amount matches the pump discharge amount throughout the day even when the detection technology has developed. It is difficult to eliminate and recover the precipitate with a water content below the precipitation state. In the present situation, excess water is also inhaled and removed.
垂直方向、或いは、傾斜したスクリューコンベヤーを用いる方法にあっても、凝集剤を使用して沈降分離するような軽質、微細粒子の沈殿物の場合においては、沈殿状態水分量のままでの排除は困難であり、スクリュー詰りも生じやすい。 Even in the case of using a screw conveyor that is vertical or inclined, in the case of a light and fine particle precipitate that is settled and separated using a flocculant, the moisture content in the precipitated state is not excluded. It is difficult and screw clogging is likely to occur.
沈殿物汚泥の水分量を減らすために、水平移送用スクリューコンベヤーの先端部に加圧部とフイルター機構を連接して、絞り機能を備えたものにあっては、取扱調整が煩雑であるばかりでなく、特に微細粒子を取扱う設備ではフイルタートラブルが多く好ましくない。 In order to reduce the amount of water in the sediment sludge, the handling and adjustment are just cumbersome if the pressurizing part and the filter mechanism are connected to the tip of the screw conveyor for horizontal transfer and have a throttling function. In particular, facilities that handle fine particles are not preferable because of many filter troubles.
また、重力式沈殿分離法の一種である横流れ方式の沈殿分離装置は、分離水槽内に、通水方向に対して平行で、通水方向に直角な平面内では大きく傾斜させた分離板を層状に多数配列して沈殿分離を早めるようにした装置であり、傾斜分離板下方には沈殿物貯留部を設けるのであるが、傾斜分離板を密集させた分離板間の被処理液の通水流路よりも、抵抗の少ない被処理水の流水路となるために、これを防止すべく通水方向に直角な粗流板を複数配列して区画する。 In addition, the cross-flow type sedimentation separation device, which is a type of gravity sedimentation separation method, has a layered separation plate in the separation water tank that is largely inclined in a plane parallel to the water flow direction and perpendicular to the water flow direction. In order to speed up the precipitation separation, a sediment reservoir is provided below the inclined separation plate, but the flow path of the liquid to be treated between the separation plates in which the inclined separation plates are closely packed In order to provide a flow channel for water to be treated with less resistance, a plurality of rough flow plates perpendicular to the water flow direction are arranged and partitioned to prevent this.
しかし、連続操業のできる装置とするためには、分離板長さ全範囲にわたる沈殿物の掻き寄せ等の移送設備が必要であり、該移送設備には、やむなく生じる通水方向の貫通したスペースがあり、流水抵抗も比較的少なくなりやすいために充分な沈降分離がなされないばかりでなく、傾斜分離板から沈降する分離汚泥を再混入させる流路(以下“くぐり水路”と呼ぶ)となり、傾斜分離板終端近くに再流入(以下“くぐり水”と呼ぶ)して処理水に混合流出し、分離性能を低下させる問題が実験結果から判明している。 However, in order to obtain a device that can be operated continuously, it is necessary to have a transfer facility such as scraping of sediment over the entire length of the separation plate, and the transfer facility has an unavoidably penetrating space in the water passage direction. In addition, since the resistance to running water is relatively low, not only is sufficient sedimentation separated, but it also becomes a channel that re-mixes the separated sludge that settles from the inclined separation plate (hereinafter referred to as “recessed channel”). From the experimental results, it has been found that there is a problem that the re-inflow near the end of the plate (hereinafter referred to as “kug water”) flows out into the treated water and deteriorates the separation performance.
沈殿分離水槽等の水槽底にほぼ水平に配設した移送用のスクリューコンベヤーは、ケースの上半が開放された長さ範囲では、水や沈殿物を移送する能力はあるけれども圧力を発生させることはできないが、スクリュー外周が全周囲われた状態では幾分かの圧力を発生させることができ、スクリューの断面積を漸減させることや、スクリューピッチを漸減させること等で更に加圧力を得ることができることは、スクリュー式ポンプやスクリュー式脱水濃縮機等の技術から容易に理解できるところである。 The screw conveyor for transfer installed almost horizontally at the bottom of the water tank such as a sedimentation water tank is capable of transporting water and sediment within the length range where the upper half of the case is open, but generates pressure. However, some pressure can be generated when the outer periphery of the screw is completely surrounded, and additional pressure can be obtained by gradually reducing the cross-sectional area of the screw or gradually decreasing the screw pitch. What can be done is easily understood from techniques such as a screw-type pump and a screw-type dewatering concentrator.
本発明では、水槽底にほぼ水平に配設したスクリューコンベヤーの上半が開放された範囲で水槽内沈殿物を先端側に移送集積し、スクリュー先端の一定長さ範囲を少ない隙間を設けた加圧ケースで囲い加圧力を得る構成にして、該加圧ケース端にはポンプやスクリューコンベヤー等の加圧、または、掻き揚げ手段を設けない排泥管を上方向に伸延させて連接し、上端を水槽内水位よりも高い位置で水槽外に開放する。
排泥管内水位は無加圧の状態では水槽内水位と同等であり、スクリューコンベヤーの稼動により幾分上昇する。
排泥管内に集積した沈殿物を水槽外に排出するためには、“排泥管水頭×排泥管内液の密度−水槽の水頭×水槽内液の密度+排泥管の流動抵抗”以上の加圧力が必要であるが、液頭差が主体の比較的小さな加圧力で沈殿物の排出を行うことができる。In the present invention, the sediment in the water tank is transported and accumulated on the tip side within the range where the upper half of the screw conveyor disposed almost horizontally at the bottom of the water tank is opened, and the fixed length range of the screw tip is reduced. The pressure case is configured to obtain a pressurizing pressure, and the end of the pressurization case is connected to the pressurization of a pump, screw conveyor, etc. Is opened outside the water tank at a position higher than the water level in the water tank.
The water level in the drainage pipe is equivalent to the water level in the tank in the non-pressurized state, and rises somewhat due to the operation of the screw conveyor.
In order to discharge the sediment accumulated in the sludge pipe to the outside of the water tank, it must be greater than or equal to “the sludge pipe head × the density of the liquid in the sludge pipe−the water head × the density of the liquid in the tank + the flow resistance of the sludge pipe”. Although a pressing force is required, the sediment can be discharged with a relatively small pressing force mainly composed of a liquid head difference.
スクリューコンベヤーにより移送され、排泥管内に集積される沈殿物汚泥は、スクリューの加圧力と沈殿物汚泥の自重によって圧蜜される。
圧蜜とともに沈殿物汚泥は粘度が上り、スクリューとケース間隙間の漏れ量減少の影響もあって加圧力は更に上昇しやすくなり、排泥管上端より濃縮された沈殿物汚泥が排出される。The sediment sludge transferred by the screw conveyor and accumulated in the sludge pipe is crushed by the pressure of the screw and the weight of the sediment sludge.
Along with the nectar, the sediment sludge increases in viscosity, and the pressure increases more easily due to the effect of a decrease in leakage between the screw and the case gap, and the concentrated sludge is discharged from the upper end of the exhaust pipe.
更に、水分量の少ない沈殿物汚泥を得るためには、ケース内のスクリュー先端に軸流ポンプの羽根車様の加圧羽根車を装着して、沈殿物の押し込み効果を高める。 Furthermore, in order to obtain a sediment sludge with a small amount of water, a pressure impeller like an impeller of an axial flow pump is attached to the screw tip in the case to enhance the effect of pushing the sediment.
横流れ方式の沈殿分離水槽においても前述と同様に、加圧部を備えたスクリューコンベヤーを分離水槽底に配設すると共に排泥管を連接し、沈殿物貯留部を区画する複数の阻流板下方端にはスクリュー外周に近接させた孔を開窄してスクリューを貫通させ、スクリューの移送方向を分離水槽の被処理水の通水方向と逆行する方向とすることにより、くぐり水に対向する水流を発生させてくぐり水を防止し、装置の分離精度の低下が防止できる。 Also in the cross-flow type sedimentation separation water tank, as described above, a screw conveyor equipped with a pressurizing unit is arranged at the bottom of the separation water tank, and a sludge pipe is connected, and a plurality of flow blocking plates below the sediment storage part. At the end, a hole close to the outer periphery of the screw is opened to allow the screw to pass therethrough, and the flow direction of the screw is opposite to the direction of water flow of the water to be treated in the separation water tank. Can be prevented from passing through water to prevent the separation accuracy of the apparatus from being lowered.
上述したように本発明装置は、加圧部を設けた水平方向の移送用スクリューコンベヤーのみで、垂直方向の揚送用ポンプやスクリューコンベヤー設備を用いる場合よりも濃縮された沈殿物を排除回収することができ、後段の運搬、脱水、乾燥、焼却等に与える省エネルギー効果、経済効果は大きい。
加えて、横流れ方式の沈殿分離装置においては、くぐり水を防止して装置の分離精度を向上できる効果は大きく、水処理分野装置のコンパクト化に大きく貢献できるものである。As described above, the apparatus of the present invention eliminates and collects concentrated precipitates only by using a horizontal transfer screw conveyor provided with a pressurizing unit, as compared with the case of using a vertical pump and screw conveyor equipment. The energy saving effect and economic effect on transportation, dehydration, drying, incineration, etc. in the latter stage are great.
In addition, in the cross-flow type sedimentation separation apparatus, the effect of preventing the passing water and improving the separation accuracy of the apparatus is great, and can greatly contribute to the downsizing of the apparatus in the water treatment field.
以下、本発明の実施形態を図1〜図8に基づいて説明する。 Hereinafter, embodiments of the present invention will be described with reference to FIGS.
本発明の第1実施例装置の重力式沈殿分離水槽である図1〜図3において、分離水槽1の流入樋2から流入した浮遊物を含む被処理水は分離エリアaで沈降分離され、流出樋3に流出する。
沈降する混入浮遊物は沈殿物貯留部bに沈殿し、上半を開放したスクリューコンベヤー11によって反駆動方向に移送され、筒状の加圧ケース5内を通り排泥管6のc部に吐出される。
排泥管6の上部は、上下方向に摺動可能にパッキング10で止水された上部排泥管7を備えて、上端を開放し、排泥管内における沈殿物自重での圧蜜と、水面より上方のd部分での脱水作用で濃縮された沈殿物汚泥が吐出され、シュート8から滑落排出する。In FIG. 1 to FIG. 3 which are gravity type precipitation separation water tanks of the first embodiment apparatus of the present invention, the water to be treated including suspended matters flowing from the inflow tank 2 of the
The settled suspended matter settled in the sediment reservoir b, transferred in the counter-drive direction by the
The upper part of the
スクリューコンベヤー11先端部の加圧ケース5内に内包されるスクリュー部分は、必要に応じてスクリューピッチを漸減させることや、スクリュー11と加圧ケース5の断面積を漸減させて加圧力の増加を図ることができる。 The screw part enclosed in the
上部排泥管7の上端開放位置は、沈殿物の性状に合せて、排出が可能な範囲でなるべく高く設定し、排出汚泥水分量の低減を計る。 The upper end open position of the upper sludge pipe 7 is set as high as possible within the range where discharge is possible in accordance with the properties of the sediment, and the amount of discharged sludge moisture is reduced.
第2実施例の横流れ方式の重力沈殿水槽装置を図4〜図6で説明する。
本実施例の場合、排泥管6の上下方向調整は不要なものの例であり、原水投入管17から投入された被処理水は、分離水槽1内に配設した傾斜分離板21を通過する間に沈降分離され、処理水は流出樋3に流出し、分離汚泥は沈殿物貯留部bに沈降する。
沈殿物貯留部b内は被処理水のくぐり水を防止するために、通水方向に直交した複数の阻流板23によって区画し、最下部にはスクリューコンベヤー11の回動に支障のない大きさの孔を開窄し、スクリュー11を貫通させる。A lateral flow type gravity sedimentation tank apparatus according to the second embodiment will be described with reference to FIGS.
In the case of the present embodiment, the vertical adjustment of the
The sediment reservoir b is partitioned by a plurality of
本実施例装置の阻流板23は、沈殿物貯留部bを完全区画して分離精度を維持したいのであるが、スクリュー11と阻流板23間の隙間、及び、スクリュー11のスクリュー自体の羽根ピッチ間の空隙からのくぐり水が生じるのであるが、スクリューコンベヤーの移送方向を被処理水の通水方向と逆方向とすることで、沈殿物の移送と共に、くぐり水と逆行する水流を発生させることによって、くぐり水を防止して装置の分離精度を維持する。 The
図7及び図8に示す実施例は、スクリュー11先端に3枚の羽根を持つ軸流ポンプの羽根車様の加圧羽根車31を装着し、ナット32で固定したものの実施態様を示す。
加圧羽根車31は、回転数の低い本実施例装置の場合、水力学的ポンプ作用よりも沈殿物汚泥を排泥管6内にヘラで押し込むような働きを期待するものであり、スクリュー11と別体に作ることによって、羽根枚数と羽根角度を自由に選べること、耐摩耗性の良い材質で製作できる利点がある。The embodiment shown in FIGS. 7 and 8 shows an embodiment in which an impeller-
The pressurizing
また、本発明装置の稼動停止時においては、排泥管6内に排除されない沈殿物汚泥が残る問題が発生するけれども、装置の稼動停止前に、一時的にスクリュー11の回転数を高くすることで、加圧羽根車31の水力学的加圧力を増大させ、軸流ポンプの羽根車が小水量ほど高い(締切り点で250〜300%)加圧力を示す特性もあり、排泥管内の沈殿物汚泥を排除することができる。 Further, when the apparatus of the present invention is stopped, there is a problem that the sediment sludge that is not excluded remains in the
本発明の水槽内沈殿物の排除装置は、自然な沈殿状態よりも濃縮した沈殿物汚泥を水槽外に排出することができ、加えて、従来必要とされていた沈殿物を槽外に排出するためのポンプや、垂直、或いは傾斜スクリューコンベヤーを不要にするものであり、水処理装置の沈殿水槽を始めとし、沈殿物の発生するあらゆる水槽や、河川、湖沼の汚泥の堆積しやすい場所にも利用することができる。 The apparatus for removing sediment in the water tank of the present invention can discharge the sediment sludge that is more concentrated than the natural sediment state to the outside of the water tank, and additionally discharges the sediment that has been conventionally required to the outside of the tank. Pumps and vertical or inclined screw conveyors are not required, including sedimentation tanks for water treatment equipment, any tank where sediment is generated, and places where sludge is likely to accumulate in rivers and lakes. Can be used.
1 分離水槽
2 流入樋
3 流出樋
4 スクリューコンベヤーのケース
5 加圧ケース
6 排泥管
7 上部排泥管
8 排泥用シュート
9 処理水接続口
10 パッキング
11 スクリューコンベヤーのスクリュー
12 軸受ケース
13 ベアリング
14 シール
15 スクリュー駆動用のモーター
16 チェーン
17 原水投入管
21 傾斜分離板
22 分離板押え
23 阻流板
31 加圧羽根車
32 加圧羽根車31の締付ナット
a 分離エリア
b 沈殿物貯留部
c 排泥管始端部
d 排泥管終端部
e 流入エリア
f 流出エリアDESCRIPTION OF
Claims (3)
The apparatus for removing precipitates according to any one of claims 1 and 2, wherein the rotational speed of the screw is temporarily increased before the apparatus is stopped or in order to prevent clogging of the drainage pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2010229054A JP5812237B2 (en) | 2010-09-21 | 2010-09-21 | Precipitation device for sediment in water tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2010229054A JP5812237B2 (en) | 2010-09-21 | 2010-09-21 | Precipitation device for sediment in water tank |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2012066233A JP2012066233A (en) | 2012-04-05 |
JP5812237B2 true JP5812237B2 (en) | 2015-11-11 |
Family
ID=46164132
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2010229054A Active JP5812237B2 (en) | 2010-09-21 | 2010-09-21 | Precipitation device for sediment in water tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP5812237B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104225977A (en) * | 2013-06-15 | 2014-12-24 | 颜可仁 | Automatic sediment cleaning device for slurry basin |
KR101384854B1 (en) * | 2013-12-31 | 2014-04-29 | 허종형 | Sludge excharging device for settling pond |
CN105854357B (en) * | 2016-05-04 | 2018-03-06 | 上海大学 | Skeleton symbol double buffering baffling sedimentation basin |
CN108970184B (en) * | 2018-09-21 | 2020-11-24 | 江苏广域化学有限公司 | Gravity settling separation equipment for chemical mixed liquid |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5331371U (en) * | 1976-08-25 | 1978-03-17 | ||
JPS53105059A (en) * | 1977-02-23 | 1978-09-12 | Sadao Shimazaki | Device for automatically discharging sludge in purifying tank |
JPS6150610A (en) * | 1984-08-16 | 1986-03-12 | Toru Matsuoka | Apparatus for treating waste water |
-
2010
- 2010-09-21 JP JP2010229054A patent/JP5812237B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
JP2012066233A (en) | 2012-04-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2501623C (en) | Clarifying tank | |
JP5812237B2 (en) | Precipitation device for sediment in water tank | |
JP2008136934A (en) | Grit separation | |
JP5944721B2 (en) | Sand settling equipment | |
CN104806183B (en) | Oil field flushing returns discharge opeing blood pressure lowering except device for silt | |
KR100922231B1 (en) | Oil separator for waste water treatment handling equipment | |
CN205461179U (en) | Sedimentation basin | |
FR2820734A1 (en) | WATER TREATMENT FACILITY BY FLOCKS LASTED BY A GRANULAR MATERIAL, COMPRISING INTEGRATED MEANS FOR DEGREASING | |
CN105431384B (en) | Sewage disposal device | |
CN210974372U (en) | Industrial wastewater sludge treatment device | |
KR20050009976A (en) | Method and device for flocculating setting | |
KR100824707B1 (en) | Waste-water Sedimentation Processing Apparatus Having Vertical-feeding Decanter | |
CN202107583U (en) | Downhole treatment device for sewage of mine | |
CN204034338U (en) | Multi-functional sedimentation basin | |
JP4981734B2 (en) | Sand basin | |
KR100986634B1 (en) | Pretreatment equipment of sludge or sewage | |
RU2465944C2 (en) | Device to separate phases in water-oil mix and inclined settler | |
CN203403506U (en) | Tail end rainwater purification well of flow splitting rainwater discharge system | |
JP4247840B2 (en) | Sludge dewatering unit and sludge suction and dewatering device using the same | |
CN202237414U (en) | Mud-sand discharging device for sedimentation tank | |
CN204162537U (en) | For the heavy water treating equipment of dense medium speed of underground coal mine | |
CN106669266A (en) | Rapid belt type oil-water separation apparatus | |
CN104841157B (en) | Countercurrent extraction pumping equipment | |
JP7524021B2 (en) | Floating matter recovery device | |
CN217246995U (en) | Desander with filtering performance |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20130909 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20140827 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20140916 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20141030 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20150414 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20150529 |
|
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: 20150901 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20150908 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 5812237 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
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 |