| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 101 | 給鉱設備および給鉱方法 | JP2014260527 | 2014-12-24 | JP2016070483A | 2016-05-09 | 菊谷 英生; 岡田 尚之; 越智 大司; 中村 壮志; 佐藤 健司 |
| 【課題】安定した給鉱量を確保することができる給鉱設備および給鉱方法を提供する。 【解決手段】本発明の給鉱設備は、鉱石スラリーを貯留する貯留部21と、貯留部21から鉱石スラリーを排出する配管部22と、配管部22に設けられ、エラストマーから成る管状の弁体を変形させることにより配管部22の流路の断面積を変化させる調節弁30と、調節弁30の内部に配置され、調節弁30が流路の断面積が最小となるように調節された際に流路を完全に封止する封止手段24とを備えることを特徴とする。 【選択図】図3 |
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| 102 | テーブル比重選鉱機の給水樋 | JP2014260524 | 2014-12-24 | JP2016068073A | 2016-05-09 | 菊谷 英生; 越智 大司; 中村 壮志 |
| 【課題】揺動テーブルの上面を流れる鉱石スラリーと添加水との流量の偏りを抑制して、揺動テーブルの上面の全面に流れを形成させる。 【解決手段】給水部23から上面21aに供給された水をテーブル比重選鉱機1のテーブル2に供給する樋本体20と、樋本体20の下面21bに取り付けられ、樋本体20の上面21aから流れ落ちてテーブル比重選鉱機1のテーブル2に供給される水と当接して整流する整流部材30とを備える。 【選択図】図2 |
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| 103 | 簡易有用鉱物分離装置及びこれを用いた有用鉱物分離方法 | JP2014179035 | 2014-09-03 | JP5848809B2 | 2016-01-27 | ヒョンチョル キム |
| 104 | JP1534860S - | JP2014028864 | 2014-12-24 | JP1534860S | 2015-10-13 | |
| 105 | JP1534363S - | JP2014028859 | 2014-12-24 | JP1534363S | 2015-10-05 | |
| 106 | ワーク分離装置 | JP2012548782 | 2011-12-13 | JPWO2012081565A1 | 2014-05-22 | 章全 柳川; 浩史 粕谷; 恭太 小竹; 秋元 暁; 暁 秋元; 庸二 竹内; 梅夫 露▲崎▼; 貴裕 茂木 |
| ワークと加工屑の混合物を液流内に安定して投入し、正確にかつ効率よく分離するワーク分離装置を提供すること。投入筒(120)が分離容器(110)内に挿入配置され液体供給手段(130)が投入筒(120)の下端よりも下方から分離容器(110)に液体を供給し、分離容器(110)内に発生する液流によって上端から液体が溢れて流出し、投入筒(120)内では、液面が上昇し上端から液体が流出しないこと。 | ||||||
| 107 | Particle separation apparatus and method | JP2009112487 | 2009-05-07 | JP2009274064A | 2009-11-26 | LEAN MENG H; SEO JEONGGI; KOLE ASHUTOSH; VOLKEL ARMIN R; HSIEH H BEN |
| <P>PROBLEM TO BE SOLVED: To intensify separation performance of the flow at the outlet of a particle separation apparatus. <P>SOLUTION: The particle separation apparatus comprises an inlet B for receiving a fluid containing particles dispersed therein, at least one curved channel C for generating a field for stream containing a first portion and a second portion, and an outlet 10 containing a mechanism 11 for dividing the stream so that the first portion flows through a first path 14 and the second portion flows through a second path 16. <P>COPYRIGHT: (C)2010,JPO&INPIT | ||||||
| 108 | Method and device for refining bean sprout | JP2007178168 | 2007-07-06 | JP2009011261A | 2009-01-22 | KAWAKAMI SANJI |
| PROBLEM TO BE SOLVED: To provide a method for refining bean sprouts for sufficiently applying refining operation for bean sprouts such as alfalfa sprouts in a simple structure. SOLUTION: The method for refining bean sprouts is provided with a bean sprout-refining water tank 30 having a water-reserving tank 40 having an overflow drainage part 41 and a refining container 50 housed in the water reserving tank 40 while keeping intervals between the inner surface of the water reserving tank 40 and provided with a porous part 51 at its bottom part and a porous part 52 at least at part of its side part; a bean sprout-loosening/supplying device 5 supplying the bean sprouts to be refined into dispersed condition to the bean sprout refining tank 30, and a water supply device 70 supplying water to the bean sprout refining tank 30 from an obliquely upper part. The supply device 70 is structured so that the water supply angle changes around a pin 73. COPYRIGHT: (C)2009,JPO&INPIT | ||||||
| 109 | Apparatus for separating solids from a fluid | JP2008511071 | 2006-05-10 | JP2008540099A | 2008-11-20 | ベルクホウト，シモン・ペーター・マリア; レム，ペーター・カルロ |
| 本発明は、幾つかの物質からなる物質の流れを分離するための装置及び方法に関する。 分離されるべき物質は、異なる密度又は密度範囲を有しており、最も高密度の物質が装置のスクリーンを介して排出することができる一方で、最も低密度の物質が液体の頂部近くに配置された第一の出口を介して排出することができるようになされている。 中間の密度の物質は、スクリーンの上方及び近くの位置に配置された第二の出口を介して排出される。 分離されるべき物質の流れと反対方向の流れに向けられた余分な液体の供給によって、最も低密度の物質の効率の良い除去が確保される。 | ||||||
| 110 | Method of separating different products, including household waste | JP2007552504 | 2006-01-31 | JP2008528261A | 2008-07-31 | ベルゲ・ホルム・クリステンセン; レナ・ホルム・ゲアラーシュ |
| 家庭廃棄物（ＨＷ）に含まれた異種生成物の分離方法であって、生成物は、液体を含んでいる分別容器内で分離されている。 廃棄物は、成分を含んでおり、その成分の少なくとも幾つかは、液体中で浮くことができる。 成分は、分別容器内の液体フローによって行使される、第１方向（Ｄ１）の本質的に水平方向の第１力（Ｐ１）と、第１方向（Ｄ１）と実質的に異なる第２方向（Ｄ２）の本質的に水平方向の第２力（Ｐ２）と、に晒される。 成分への力（Ｐ１、Ｐ２）の結合された衝撃が、浮いている成分を拡げ、且つ、それらを少なくとも２つの収集領域へと導く。 異なる浮力の生成物は、分かれて、扱われる。 | ||||||
| 111 | Method and apparatus for collecting the soft plastic thin film than life garbage | JP2006508408 | 2004-05-07 | JP2006525890A | 2006-11-16 | チェ スティーブン |
| 【課題】生活ゴミより軟質プラスチック薄膜を回収する方法とその装置を提供する。
【解決手段】本発明は一種の生活ゴミより軟質プラスチック薄膜を回収する方法とその装置に関わるもので、主に生活ゴミはラップ、プラスチック袋などの軟質プラスチック薄膜が大量に含まれている。 これらの軟質プラスチック薄膜は他のプラスチック製品の材質と違うため、一緒に回収すると色々な問題が起きる。 このため、軟質プラスチック薄膜の柔軟性および水中における隔離性、平坦性、水の付着性などの特性に従い、一種の有効、かつ、自動的に様々な生活ゴミより軟質プラスチック薄膜を分類、収集する方法とその装置を開発した。 |
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| 112 | Small trash and organic matter collected classification method and apparatus | JP2006508407 | 2004-05-07 | JP2006525868A | 2006-11-16 | チェ スティーブン |
| 【課題】小型ゴミと有機物の分類、収集方法と装置を提供する。
【解決手段】本発明は一種の小型ゴミと有機物の分類、収集方法と装置に関わるもので、主に水の比重性、流動性、浮き沈む性などの特性を利用し、一種の水を仲介質とし、数回の篩ろ過つかみ機構により、ゴミ中の浮遊物、有機物およびゴミ沈殿物の選別を行い、有効な分類処理方法と装置を実現する。 |
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| 113 | Tangential solid separation device | JP2000594576 | 1999-08-25 | JP2004519318A | 2004-07-02 | トラバウニズ ゲオルゲ; ニームツェジック ベルンハルト; メンケ ルカス; ヘインッ ロベルト |
| The invention relates to a device and a method for chemically and physically separating solid materials from a suspension using flotation. A rotationally symmetrical flocculation/flow reactor is provided with outlets in the lower part thereof and is arranged in a separating tank. At least one suspension inlet extends eccentrically into said reactor. The supplied suspension is guided into said reactor. The supplied suspension is guided into the upper area of the flocculation reactor via the suspension inlet. A circular flow is thus created which drains off from the flocculation reactor downwards in a tangential and radial manner over the outer circumference into circularly arranged distribution cells which reinforce the tangential component of the suspension flow when said flow is delivered into the separating tank. In prior art, the flow of the mixture consisting of the suspension and air-sacs extends radially outwards. One advantage of the invention is that said flow of the mixture has to travel a longer way to the outlets in the area of the wall of the tank due to the tangential flow component. The solid matter can be separated more effectively by virtue of the longer travel path or the longer presence in the separating tank. | ||||||
| 114 | Sample recovery device for sedimentation classifier | JP18235194 | 1994-08-03 | JPH0838930A | 1996-02-13 | NISHIYAMA YUGO |
| PURPOSE:To automatically transfer a sample to the next process in a germfree environment even during classification. CONSTITUTION:The 1st piping 15 is vertically fitted downward to a partition part 6 of a classifying tank 4, and forks into two branches halfway. One branch is connected to a solid-liquid separating pipe 29, and the 3rd solenoid valve 23 is arranged halfway. The other branch is connected to the discharge side of a pump 24, and the 2nd solenoid valve 22 is arranged halfway. The suction side of the pump 24 is connected to a liquid storage tank 25 by the piping 15, and a flow control valve 32 is installed halfway. The other end of the 2nd piping 16 connected to the top of the solid-liquid separating pipe 29 is immersed in the liquid in the liquid storage tank 25. The 3rd piping 17 is connected to the solid-liquid separating pipe 29 vertically downwards, and the 4th solenoid valve 30 and the 5th solenoid valve 31 are arranged in the piping 17 at an interval. | ||||||
| 115 | JPS6331278B2 - | JP16181780 | 1980-11-17 | JPS6331278B2 | 1988-06-23 | FURIIDORIHI KAARU SHUMITSUTO |
| In a flotation basin a flotation zone and a pure liquid zone are formed which are separated by filter means. A liquid containing suspended matter is introduced into the flotation zone via an inlet and subjected to pressure release flotation by saturating pure liquid with pressurized gas under a pressure in the range of 3 to 8 bar and injecting the pressurized gas saturated liquid into the flotation zone in the region of the inlet. The flotated mud accumulating at the surface of the liquid is removed laterally by removal means coacting with the filter means or is removed by means of a combined filtering and removing device together with non-flotatable suspended matter on a filter web circulated or passed through the flotation basin. The mud is predried on the filter web and separated therefrom by redirecting its run, if desired, with assistance by a scraper. The mud falls into a collecting container separated from the flotation basin or its contents by a partition. The outlet is disposed in the pure liquid zone downstream from the filter web or between the runs thereof with respect to the direction of liquid flow. The pure liquid is discharged by a pump controlled in dependence on the inflow. | ||||||
| 116 | Device and method of flotation separation using spray nozzle | JP1190982 | 1982-01-29 | JPS57147461A | 1982-09-11 | JIEEMUZU DATSUTERA; REIMONDO PII JIEFURIIZU SAADO; DEBITSUDO MATESON; AREKISANDAA ZENTORATSUROI; FUIRITSUPU EBARETSUTO MATSUKUG; DEBITSUDO EDOWAADO HAAMAN |
| An improved method and apparatus for froth flotation separation of the components of a slurry, having particular utility for the beneficiation of coal by the flotation separation of coal particles from impurities associated therewith such as ash and sulfur. In this arrangement, a spray nozzle is positioned above a flotation tank having a water bath therein, and sprays an input slurry through an aeration zone into the surface of the water. The spraying operation creates a froth on the water surface in which a substantial quantity of particulate matter is floating, while other components of the slurry sink into the water bath. A skimming arrangement skims the froth from the water surface as a cleaned or beneficiated product. | ||||||
| 117 | Device for setting fixed flow rate distribution rule in liquid current | JP11789181 | 1981-07-29 | JPS5765326A | 1982-04-20 | JIYORUJIYU TOREISA |
| In separating solids from a liquid by settling or flotation, the liquid is made to flow generally horizontally through a tank, and means at the inlet or outlet zone of the tank impose a velocity gradient on the flow. In settling, the velocity increases upwards in the tank (Fig. 3), and in flotation the velocity will decrease upwards to enhance separation. Fig. 3 shows a baffle with holes of various sizes at the inlet, but other embodiments involve equivalent means at the outlet zone, namely a single annular baffle with holes of various sizes (Fig. 6) and arrays of vertical outlet tubes with holes of various sizes (Figs. 4, 5) and internal divisions and overflow weirs (Figs. 7, 8). <IMAGE> | ||||||
| 118 | JPS57500185A - | JP50073981 | 1981-02-13 | JPS57500185A | 1982-02-04 | |
| 119 | Device for simultaneously and continuously supplying powdered solid or liquid into treating machine | JP6430781 | 1981-04-30 | JPS5710325A | 1982-01-19 | DEIITAA MERUTSU; FUIRITSUPU SHIYUMITSUTO; PEETAA BUAIDENHANMAA |
| 120 | Filter doubling as flotation and filtering method doubling as flotation | JP16181780 | 1980-11-17 | JPS5684682A | 1981-07-10 | FURIIDORIHIIKAARU SHIYUMITSUTO |
| In a flotation basin a flotation zone and a pure liquid zone are formed which are separated by filter means. A liquid containing suspended matter is introduced into the flotation zone via an inlet and subjected to pressure release flotation by saturating pure liquid with pressurized gas under a pressure in the range of 3 to 8 bar and injecting the pressurized gas saturated liquid into the flotation zone in the region of the inlet. The flotated mud accumulating at the surface of the liquid is removed laterally by removal means coacting with the filter means or is removed by means of a combined filtering and removing device together with non-flotatable suspended matter on a filter web circulated or passed through the flotation basin. The mud is predried on the filter web and separated therefrom by redirecting its run, if desired, with assistance by a scraper. The mud falls into a collecting container separated from the flotation basin or its contents by a partition. The outlet is disposed in the pure liquid zone downstream from the filter web or between the runs thereof with respect to the direction of liquid flow. The pure liquid is discharged by a pump controlled in dependence on the inflow. | ||||||
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