JP3704245B2 - Specific gravity beneficiation method of fine metal and its specific gravity beneficiation equipment - Google Patents

Specific gravity beneficiation method of fine metal and its specific gravity beneficiation equipment Download PDF

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JP3704245B2
JP3704245B2 JP30883098A JP30883098A JP3704245B2 JP 3704245 B2 JP3704245 B2 JP 3704245B2 JP 30883098 A JP30883098 A JP 30883098A JP 30883098 A JP30883098 A JP 30883098A JP 3704245 B2 JP3704245 B2 JP 3704245B2
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beneficiation
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pipe
concentrate
specific gravity
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JP2000126645A (en
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澄男 細川
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六鑛開發株式会社
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Description

【0001】
【発明の属する技術分野】
本発明は、微粒金属の比重選鉱方法及びそれを使用する比重選鉱装置の改良に関し、且つ詳しくは金銀粒を含む、別名含金土砂鉱等の濃縮を行う微粒金属の比重選鉱方法及び比重選鉱装置に関するものである。
【0002】
【従来の技術及びその問題点】
【0003】
砂金は、一般の川砂金の他に土砂中に単体で存在する自然金であるが、自然金は砂金に比べて粒子が細かく、多くは1mm以下でミクロン単位のものが多いが、金は比重が19と基本的に重いが、自然金には木の葉状の薄片のものがって水に流れやすいのと、水の表面張力によるものと思われるが、水に浮く性質を有している。
このような金粒の回収手段、金粒粗鉱の濃縮手段として、テーブル式選鉱機、スパイラル式選鉱機を用いた回収手段、濃縮手段が知られている。
前者のテーブル式選鉱機(樋流式水選機:実公昭35−609号公報参照)、(分級装置:特開昭55−157345号公報参照)で自然金を処理しようとすると、微粒のもの薄片のものはテーブルの振動で原液に発生する細かい波に大半が浮いて流れてしまい、金粒の回収、金粒の濃縮を効果的に行えない。
また、後者スパイラル式選鉱機には、螺管内に常時清澄液を流すように構成した砂金回収装置(特公昭40−21601号公報参照)がある。この先行技術は、比重と遠心力とを利用した選鉱機であるが、自然金を処理しようとすると、20ミクロン以上の微粒は清澄液の流速が速いことによって大半が流れてしまい、比重による沈降効果、遠心力による分離効果を受けることが少ない。
このような問題を解決する手段として本出願人は特公平6−26683号公報に開示する技術を提案している。
この先行技術は、少なくとも一つの外向角部を有する選鉱管を、その外向角部が下方を向くようにして多段棚の上段から下段に向かってジグザグ状に配設し、その選鉱管に原液を流して重鉱物をその外向角部に沈降させ、次に洗浄水を流して沈降精鉱表面の土砂を洗浄し、その後高圧水を注入して沈降精鉱を吐出するようにしている。
ところで、金、砂鉄等等級が高い精鉱は比重が大きいため沈降スピードが速く、等級が低い精鉱は砂状を呈し比重が小さく沈降スピードが遅い。ジグザグ状の選鉱管では上流側から等級が高い精鉱が多く停滞し、下流に行くに従って徐々に等級が高い精鉱が減少して等級が低い精鉱が多く停滞し、下流では最も等級が低い精鉱が停滞する。
しかしながら、高圧水をそのジクザク状の選鉱管内に注入して精鉱を回収すると、高低の等級の精鉱が混在し、分別を困難で煩雑なものにする。
また、選鉱管は複数本の全てを前記のように多段棚の上段から下段に向かってジクザク状に配設したレイアウト故に例えばある選鉱管がアクシデントで目詰まりした場合の修理や保守・管理が、選鉱管の入り組んだ配管経路が影響して非常に大変且つ危険であるし、複数本でしかもジクザク配管のため、製作労力もかかり、低廉な提供が難しい。
【0004】
【発明が解決しようとする課題】
本発明は上記従来事情に鑑みてなされたもので、その目的とする処は別名含金土砂鉱等の濃縮が効率的であり、しかも製作、メンテナンスも簡単に行える微粒金属の比重選鉱方法及び比重選鉱装置を提供することにある。
【0005】
【課題を解決するための手段】
上記目的を解決するために講じた技術的手段は、管内の内面全長に亘って少なくとも一つの外向角部を有する選鉱管を、その外向角部を下側に向けた状態で複数本並列した選鉱ユニットを複数体構成し、各選鉱ユニットを若干の勾配を有して段々状に配設し、各選鉱ユニットの連絡部を、最上段の選鉱ユニットに原液を流して重鉱物を各選鉱ユニットの外向角部に沈降させる時及び最上段の選鉱ユニットに洗浄水を流して沈降する各選鉱ユニットの精鉱表面の土砂を洗浄する時に連絡し且つその後高圧水を各選紘ユニット別に注入する時に各選紘ユニットの下端から別々に精鉱が吐出回収できるように非連絡とする構成とし、その高圧水を上段の選鉱ユニットの順から時間差をおいて各選紘ユニットごとに注入することを要旨とする。
そして、請求項1記載の連絡部は、上段の選鉱ユニットにおける選鉱管下端直下に位置する受水部を先端に備えた原液用連絡パイプを、下段の選鉱ユニットにおける選鉱管の上端に配置した構成とすることが好適である。
また、請求項2記載の高圧水と共に受水部上方を横切るように選鉱ユニットの下端から吐出される精鉱を受け止める回収手段を、更に備えている場合も有効である。
前記方法を具体的に実施する装置は、管内の内面全長に亘って少なくとも一つの外向角部を有する選鉱管を、その外向角部を下側に向けた状態で複数体並列して選鉱ユニットを複数構成、各選鉱ユニットを若干の勾配を有して段々状に配設し、最上段の選鉱ユニットに原液供給手段、洗浄水供給手段を連絡すると共に各選鉱ユニットごとに高圧水供給手段を連絡可能に設け、各選鉱ユニットの連絡部は、上段の選鉱ユニットにおける選鉱管下端直下に先端の受水部を配置した原液用連絡パイプと、各選鉱ユニットにおける選鉱管下端の前方位置に所定の間隔をおいて設置され、前記高圧水の圧力で吐出される精鉱を受け止める回収手段とを備え、前記原液用連絡パイプを下段の選鉱ユニットにおける選鉱管の上端に配置していることを要旨とする。
【0006】
(作用)前記技術的手段によれば下記の作用を奏する。
原液を最上段の選鉱ユニットから最下段の選鉱ユニットに行き渡るまで流すと、原液から沈降する重鉱物が各選鉱ユニットを構成する選鉱管の下向きな外向角部に停滞する。
金、砂鉄等等級が高い精鉱は比重が大きく沈降スピードが速い。それ故、最上段の選鉱ユニットから下段の選鉱ユニットに行くに従ってその停滞量は減少し、下段に至っては等級が最も低い砂状の精鉱が主に沈降し停滞する。
その後、洗浄水を流して沈降精鉱表面の土砂を洗浄し最下段の選鉱ユニット下端から排出する。
土砂を洗い落としの完了は最上段の選鉱ユニットから始まり、最下段の選鉱ユニットの土砂の洗い落し完了が最後になる。そして、全段の選鉱ユニットの洗い落しの完了を待っていたのでは、選鉱ユニットの勾配の影響で等級の高い精鉱が等級の低い精鉱を停滞する下段の選鉱ユニット側に落下してしまう虞れがあると共に、選鉱サイクルのアップが望めない。
それを防止するために、各選紘ユニットの下端から別々に精鉱が吐出回収できるように各選紘ユニットを非連絡とする状態で土砂の洗い落し完了が完了した上の段から順に時間差をおいて高圧水を注入してそこに停滞している精鉱をその下端から吐出させ、各選鉱ユニットごとに回収する。これによって等級別の精鉱の回収が可能となる。
この工程を順次繰り返す。
【0007】
【発明の実施の形態】
次に、本発明の実施の形態を図面に基づいて説明する。
図1乃至図4は本発明微粒金属の比重選鉱方法を実施する比重選鉱装置を示し、符号Aがその比重選鉱装置である。
【0008】
この比重選鉱装置Aは、複数本の選鉱管11…を並列して構成された選鉱ユニット1複数体、原液供給手段2、洗浄水供給手段3、高圧水供給手段4等を備えている。
【0009】
この選鉱ユニット1は、本実施の形態では4本の選鉱管11…を並列した場合を示し、各選鉱管11は、図4に示すように例えば角形、角波形、真円形、非真円形等少なくとも一つの外向角部11aを有する外観形状に成形され、その外向角部11aを下側に向けた状態で平行状、即ち川の字状にして適宜間隔をおいて支持台21に取付けてある。
【0010】
この選鉱ユニット1は、その長さを数十メートルとする長尺なものであり、平坦地や傾斜地等を利用し、若干の勾配(本実施の形態では2%)を有して段々状に配設して長尺状の選鉱機能部1Aを構成している。
【0011】
原液供給手段2は、原液タンクから直接供給するようにしても良いが、図1乃至図3に示すように本実施の形態ではコンクリートミキサー12、コンクリートポンプ22、密閉式混合室32等からなる鉱業用原鉱圧入式スラリー化装置を使用している。
【0012】
密閉式混合室32は、高さを5乃至100cm位の範囲から選択して決定し、図3に示すように脱着蓋32aを有し、運転時には閉蓋して密閉式として運転時の安全性を確保している。
また、この密閉式混合室32には2個の物質圧入口32b、32cが開設してあり、一方を原鉱用の物質圧入口32b、他方を水用の物質圧入口32cとし、原鉱用の物質圧入口32bを、水用の物質圧入口32cよりも大径にしてある。このように物質圧入口32b、32cの内径を異径にした理由は、大径の物質圧入口32bから内部に圧入される軟らかい原鉱が、小径の物質圧入口32cから内部に勢いよくほとばしり出る水によって効率良く溶解され、スラリー化されるようにするためであり、水用の物質圧入口32cに、水パイプ13、ポンプ23、水タンク33からなる洗浄水供給手段3が接続されている。
更に、この密閉式混合室32の底部近傍に横設されているのは篩32dであり、万が一原鉱に石、レキ、塵芥、虫が紛れ込んでもそこで選別し、前記選鉱機能部にそれら異物が流下しないようにする。符号32eは排出部である。
【0013】
コンクリートミキサー12は、一次処理された原鉱(採掘して得た原鉱を水洗いし、10メッシュの篩で選別されて一次処理されたもの)を投入して水分約30%位の比較的軟らかい練り状の土砂にしてホッパー22aを経由してコンクリートポンプ22に送り込むようになっている。
【0014】
コンクリートポンプ22は、その練り状の土砂を密閉式混合室32へ圧送し、物質圧入口32bから同密閉式混合室32に圧入する。
【0015】
密閉式混合室32内においては、圧入された比較的軟らかい練り状土砂が、勢いよくほとばしり出る水で簡単に溶解、スラリー化し、排出部を介してスラリー化した原液を最上段の選鉱ユニット1から流下させる。
【0016】
符号5が、密閉式混合室32の排出部32eから最上段の選鉱ユニット1に原液を流下させる原液パイプであり、図2に示すように下端から4本の選鉱管11…に分岐して接続されている。
前記分岐部よりも上方の原液パイプ5部分に接続されているのが、高圧水タンク14に接続する高圧水パイプ24であり、その高圧水パイプ24には電磁弁6、逆止弁7が、またその高圧水パイプ24との接続部よりも上流側の原液パイプ5部分には逆止弁7が各々装設されており、この高圧水パイプ24、高圧水タンク14、ポンプ34等で高圧水供給手段4を構成している。
【0017】
各選鉱ユニット1の連絡部8は、図1に示すように先端に、上段の選鉱ユニット1における選鉱管11…下端直下に位置して漏斗状に拡開した受水部18aを有する原液用連絡パイプ18と、各選鉱ユニット1における選鉱管11…下端前方位置に所定の間隔をおいて設置され、前記高圧水の圧力で吐出される精鉱を受け止める回収手段28とを備えている。
【0018】
詳しくは、図1に示すように各選鉱ユニット1の設置地面100の始端部分に内部を中空とする架台200を設置し、上段の選鉱ユニット1における選鉱管11…下端の直下に位置させて受水部18aを架台200で支持し、その受水部18aに上端を接続する原液用連絡パイプ18を前記原液パイプ5と同様に下端で分岐させて下段の選鉱ユニット1における選鉱管11…上端に連通状に接続し、更に上段の選鉱ユニット1における選鉱管11…下端の前方に所定の間隔Xを介して容器からなる回収手段28を架台200上に設置している。
高水圧パイプ24の接続、電磁弁6、逆止弁7の原液用連絡パイプ18等へのレイアウトは前記原液パイプ5の場合と同様になっている。
【0019】
即ち、前記密閉式混合室32の排出部32eから原液パイプ5を介して流下する原液は、最上段の選鉱ユニット1における選鉱管11…下端から受水部18a、原液用連絡パイプ18を介して次段の選鉱ユニット1に流れ込み、それを各選紘ユニット1ごとに繰り返して最下段の選鉱ユニット1における選鉱管11…まで原液を行き渡らせる。
洗浄水を流下させるのも同様な経路で行われる。
【0020】
一方、前記空間Xを所定に設定し、各選鉱ユニット1に前記電磁弁6を開弁して高圧水を供給すると、各選鉱ユニット1における選鉱管11…に沈降停滞している停滞物を、前記受水部18a上方を横切って回収手段28である収容箱にプッシュアウトできるようになる。
この空間Xの設定は、高圧水圧で決定することができる。
【0021】
最下段の選鉱ユニット1における選鉱管11…下端の前方には、前記所定の間隔Xを隔てて前記回収手段28を架台200で支持して設置し、また洗浄水の受水タンク9を同選鉱管11…下端の直下に備設している。
【0022】
本実施の形態では、3段の選鉱ユニット1で選鉱機能部1Aを構成した場合を示し、また前記回収手段28である回収箱に確実にプッシュアウト物が回収できるようにガイド筒28aを具備し、またその回収箱はキャスター28bで移動可能にするとと共に、フロート式排水弁を備えて、常時水分を排水パイプ28cで排水可能にしている。
【0023】
次ぎに、本実施の形態を使用する比重選鉱方法を説明すると、まず、コンクリートミキサー12、コンクリートポンプ22を経て軟らかい原鉱を密閉式混合室32に送り込むと同時に洗浄水供給手段3でポンプアップする水を物質圧入口32cから吐出してその原鉱をスラリー化させ、原液を、原液パイプ5、受水部18a、原液用連絡パイプ18を経て各選鉱ユニット(3段の選鉱ユニット)1に行き渡らせる。
金、砂鉄等等級が高い精鉱は比重が大きく沈降スピードが速い性質があり、最上段の選鉱ユニット1から下段の選鉱ユニット1に行くに従って等級が高い精鉱の停滞量は減少し、下段に至っては等級が最も低い砂状の精鉱が主に沈降し停滞する。
そして、コンクリートミキサー12、コンクリートポンプ22の作動を停止し、洗浄水供給手段3のみの作動を継続して洗浄水(水)を密閉式混合室32から原液と同じルートで流し込み、各選鉱ユニット1の精鉱表面の土砂を洗い落しつつ最下段の選鉱ユニット1における選鉱管11…下端からその洗浄水を受水タンク9で受水する。
精鉱は各選鉱管11…において下向きな外向角部11aに図4に示すように停滞し、比重があることも相乗して、洗浄水で流される虞れは少ない。
その洗浄の完了は最上段の選鉱ユニット1から始まり、最下段の選鉱ユニット1が最後になる。
それに合わせて最上段の選鉱ユニット1に連絡する電磁弁6を開弁して高圧水を圧入し、その段の沈降停滞している精鉱を選鉱管11の下端からプッシュアウトして前記ガイド筒28aから回収箱28に回収する。
このプッシュアウトは、各段の洗浄完了に合わせて各段ごとに時間差をおいて行う。
この一連の工程をワンサイクルとする。
【0024】
含金土砂鉱を対象とした実験の結果によると、一段目の選鉱ユニットでは等級1の精鉱が、また二段目の選鉱ユニットでは等級2の精鉱が、更には三段目の選鉱ユニットでは等級3の精鉱が主に回収される。
そして、全段で回収された金を100%とすると、一段目の選鉱ユニットでは86%、二段目の選鉱ユニットでは5%、三段目の選鉱ユニットでは9%沈降停滞していたことが解った。
【0025】
尚、本実施の形態では、前記連絡部8を、先端に、上段の選鉱ユニット1における選鉱管11…下端直下に位置して漏斗状に拡開した受水部18aを有する原液用連絡パイプ18と、各選鉱ユニット1における選鉱管11…下端前方位置に所定の間隔Xをおいて設置され、前記高圧水の圧力で吐出される精鉱を受け止める回収手段28とを備えた構成にしているが、例えば上流側の選鉱管の下端部に可撓性を持たせ、原液の流し時と洗浄水の流し時にその可撓性を利用して下流側の選鉱管と接続し、高水圧圧入時にはその接続を解除して可撓性を利用して回収手段に連結するようにする等。自由である。
【0026】
【発明の効果】
本発明は以上のように、最上段の選鉱ユニットに原液を流して重鉱物を各選鉱ユニットの外向角部に沈降させ更に洗浄水を流して沈降する精鉱表面の土砂を洗浄する時に各選紘ユニットを連絡し、その後高圧水を各段別に注入する時に各段の下端から別々に精鉱が吐出回収できるように各段を非連絡とし、高圧水を上段の選鉱ユニットの順から時間差をおいて各段ごとに注入するから、各段別、所謂等級別をもって精鉱を回収するに有効な比重選鉱方法であり、後作業となる等級別の分別作業が非常に楽になるし、金粒は特に最上端の選鉱ユニットに沈降停滞するから、分別作業に手を煩わせない金の高効率な回収を可能にする。
その上、全段が綺麗に洗浄されたのを待たずして各段別に回収するものであるから、最上段等の選鉱ユニットへの原液の供給(流し)と、例えば最下段等の選鉱ユニットの洗浄とを併行させることも可能となり、選鉱時間の無駄を無くし、効率的な選鉱が行える。
その上、本比重選鉱装置は選鉱ユニットを若干の勾配を有して段々状に配設した平面状を有し、選鉱管複数本の全てを多段棚の上段から下段に向かってジクザク状に配管した先行技術のように例えばある選鉱管がアクシデントで目詰まりした場合の修理や保守・管理が、選鉱管の入り組んだ配管経路が影響して非常に大変になったり、怪我をしたり、製作労力がかかって設備コストが高騰する等の様々な問題点を解決することができる。
その上、各段の連絡部を、先端に、上段の選鉱ユニットにおける選鉱管下端直下に位置して受水部を有する原液用連絡パイプと、各選鉱ユニットにおける選鉱管下端前方位置に所定の間隔をおいて設置され、前記高圧水の圧力で前記受水部上方を横切るように吐出される精鉱を受け止める回収手段とで構成しているから、機械的な機素構造や電気的構造で制御した場合に比べて構造的にも簡単であるし、故障も少なく、耐久的にも優れた比重選鉱装置を供し得る。
【図面の簡単な説明】
【図1】本微粒金属の比重選鉱方法を実施する比重選鉱装置の側面図で中間省略し、一部切欠して示す。
【図2】同平面図で一部切欠して示す。
【図3】密閉式混合室を示し、(a)は拡大正面図で一部切欠して示す。(b)はその(A)−(A)線拡大断面図。
【図4】図1の(B)−(B)線拡大断面図で選鉱管1本を示す。
【符号の説明】
A:比重選鉱装置 1:選鉱ユニット
11:選鉱管 11a:外向角部
8:連絡部 18a:受水部
18:原液用連絡パイプ 28:回収手段
2:原液供給手段 3:洗浄水供給手段
4:高圧水供給手段
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a specific gravity concentrating method for fine metals and a specific gravity concentrating device using the same, and more specifically, a specific gravity concentrating method and a specific gravity concentrating device for fine metals containing gold and silver grains, which is also known as gold-containing earth and sand ore. It is about.
[0002]
[Prior art and its problems]
[0003]
Gold dust is natural gold that exists alone in earth and sand in addition to general river gold, but natural gold has finer particles than gold dust, and most of them are 1mm or less in micron units, but gold has a specific gravity. However, natural gold has a leaf-like flake shape and is easy to flow into water, and it seems to be due to the surface tension of water, but it has the property of floating in water.
As such means for collecting gold grains and means for concentrating gold grain coarse ore, a table-type beneficiary machine, a collecting means using a spiral type beneficiary machine, and a concentrating means are known.
If you try to process natural gold with the former table-type beneficiation machine (current type water-separation machine: see Japanese Utility Model Publication No. 35-609), (classifier: see Japanese Patent Application Laid-Open No. 55-157345), Most of the flakes float and flow in the fine waves generated in the stock solution due to the vibration of the table, and it is not possible to effectively collect the gold grains and concentrate the gold grains.
In addition, the latter spiral type beneficiator includes a gold dust collecting device (see Japanese Patent Publication No. 40-21601) configured to always flow a clarified liquid into a screw tube. This prior art is a mineral separator using specific gravity and centrifugal force. However, when processing natural gold, most fine particles of 20 microns or more flow due to the high flow rate of the clear liquid, and sedimentation due to specific gravity. The effect and the separation effect by centrifugal force are rare.
As means for solving such a problem, the present applicant has proposed a technique disclosed in Japanese Patent Publication No. 6-26683.
In this prior art, a beneficiation pipe having at least one outward corner is arranged in a zigzag shape from the upper stage to the lower stage of the multistage shelf so that the outward angle part faces downward, and the stock solution is supplied to the beneficiation pipe. The heavy mineral is allowed to settle to the outward corners, and then the washing water is flowed to wash the sediment on the surface of the precipitated concentrate, and then high pressure water is injected to discharge the precipitated concentrate.
By the way, concentrates with high grades such as gold and iron sand have a high specific gravity, so the sedimentation speed is fast, while concentrates with low grades are sandy, have a low specific gravity and a slow sedimentation speed. In the zigzag-shaped beneficiation pipe, many concentrates with higher grades stagnate from the upstream side, and concentrates with higher grades gradually decrease and more concentrates with lower grades stagnate toward the downstream, and the lowest grades are downstream. The concentrate is stagnant.
However, when high-pressure water is injected into the zigzag-shaped beneficiation pipe and the concentrate is recovered, high- and low-grade concentrates are mixed, making separation difficult and cumbersome.
In addition, because of the layout in which all of the multiple beneficiary pipes are arranged in a zigzag shape from the top to the bottom of the multistage shelf as described above, for example, repair, maintenance, and management when a certain beneficiary pipe is clogged with an accident, The complicated piping route of the beneficiation pipe is very difficult and dangerous, and since it is a plurality of zigzag pipes, it takes a lot of production labor and is difficult to provide at low cost.
[0004]
[Problems to be solved by the invention]
The present invention has been made in view of the above-mentioned conventional circumstances, and its intended processing is also known as a gold-containing earth-and-sand ore, which is efficient in concentration, and can be produced and maintained easily. It is to provide a beneficiation device.
[0005]
[Means for Solving the Problems]
The technical means taken in order to solve the above-mentioned object is to prepare a beneficiation pipe in which a plurality of beneficiation pipes having at least one outward angle part over the entire inner surface in the pipe are arranged in parallel with the outward angle part facing downward. A plurality of units are configured, and each of the beneficiation units is arranged in a stepped manner with a slight gradient. The connecting portion of each of the beneficiation units is flown to the uppermost beneficiation unit, and the heavy mineral is supplied to each of the beneficiation units. Each time when sinking to the outward corner, and when washing the sediment on the concentrate surface of each beneficiation unit that flows by washing water flowing into the uppermost beneficiation unit, and when high pressure water is injected separately for each selection unit The gist is that the concentrate is disconnected so that the concentrate can be discharged and collected separately from the bottom of the selection unit, and the high-pressure water is injected into each selection unit at a time lag from the order of the upper selection unit. To do.
And the connection part of Claim 1 is the structure which has arrange | positioned the connection pipe for stock solutions which equipped the water receiving part located in the front-end | tip directly in the lower part of the beneficiation pipe in the upper stage beneficiation unit at the upper end of the beneficiation pipe in the lower stage beneficiation unit Is preferable.
In addition, it is also effective in the case of further comprising a recovery means for receiving the concentrate discharged from the lower end of the beneficiation unit so as to cross the upper portion of the water receiving unit together with the high pressure water described in claim 2.
An apparatus for concretely carrying out the above method is that a plurality of ore beneficiation pipes having at least one outward corner along the entire inner length of the inside of the pipe are arranged in parallel with the outward corner being directed downward. and a plurality of configurations, arranged terraced shape each beneficiation unit has a slight slope, solution feed means beneficiation unit of the uppermost stage, high-pressure water supply means for each concentrator unit with communicating the cleaning water supply means The connecting section of each beneficiation unit is predetermined at the position in front of the lower end of the beneficiation pipe in each beneficiation unit, and the connection pipe for stock solution in which the water receiving part at the tip is arranged immediately below the lower end of the beneficiation pipe in the upper beneficiation unit. And collecting means for receiving the concentrate discharged by the pressure of the high-pressure water, and the undiluted solution connection pipe is disposed at the upper end of the beneficiation pipe in the lower-stage beneficiation unit. To.
[0006]
(Operation) According to the above technical means, the following operation is provided.
When the stock solution is flowed from the uppermost processing unit to the lower processing unit, the heavy minerals that settle from the stock solution stagnate in the downward outward corners of the processing pipes that make up each processing unit.
Concentrates with high grades such as gold and iron sand have high specific gravity and fast sedimentation speed. Therefore, the amount of stagnation decreases as it goes from the uppermost processing unit to the lower processing unit, and the sandy concentrate with the lowest grade mainly settles and stays at the lower level.
Then, wash water is poured to wash the sediment on the surface of the settled concentrate, and it is discharged from the lower end of the lowest unit.
Completion of washing off the earth and sand starts from the top concentration unit, and the final removal of the earth and sand from the bottom concentration unit ends. And if we waited for the completion of the washing of all the beneficiation units, the concentrate of the higher grade falls to the lower beneficiation unit side where the lower grade concentrate stays due to the influence of the gradient of the beneficiation unit. There is a possibility that the beneficiation cycle cannot be improved.
To prevent it, the order time lag from the upper row of the wash-off completion of sediment is completed in a state in which concentrate separately from the lower end of each SenHiroshi unit is a non-contact Kakusen Hiroshi unit to allow the discharge recovery Then, the high-pressure water is poured into the concentrate, and the stagnation concentrate is discharged from the lower end of the concentrate and collected for each of the beneficiation units. This makes it possible to collect concentrates by grade.
This process is repeated sequentially.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
Next, embodiments of the present invention will be described with reference to the drawings.
1 to 4 show a specific gravity beneficiation apparatus for carrying out the specific gravity beneficiation method of the fine metal of the present invention, and symbol A is the specific gravity beneficiation apparatus.
[0008]
This specific gravity separation apparatus A is provided with a plurality of beneficiation units 1 composed of a plurality of beneficiation pipes 11.
[0009]
This mineral processing unit 1 shows the case where four mineral processing pipes 11 are arranged in parallel in this embodiment, and each mineral processing pipe 11 has, for example, a square shape, an angular waveform, a perfect circle, a non-true circle, etc. as shown in FIG. It is formed in an external shape having at least one outward corner portion 11a, and is attached to the support base 21 at an appropriate interval in a parallel shape, that is, in the shape of a river, with the outward corner portion 11a facing downward. .
[0010]
This beneficiation unit 1 is a long unit having a length of several tens of meters, and uses a flat land, an inclined land, etc., and has a slight gradient (2% in the present embodiment) in a stepwise manner. The long ore beneficiation function unit 1A is arranged.
[0011]
The stock solution supply means 2 may be directly supplied from the stock solution tank, but in this embodiment, as shown in FIGS. 1 to 3, the mining industry is composed of a concrete mixer 12, a concrete pump 22, a sealed mixing chamber 32, and the like. The raw ore press-fitting slurrying equipment is used.
[0012]
The sealed mixing chamber 32 has a height selected from a range of about 5 to 100 cm and has a desorption lid 32a as shown in FIG. Is secured.
The sealed mixing chamber 32 has two material pressure inlets 32b and 32c. One is a material pressure inlet 32b for raw ore and the other is a material pressure inlet 32c for water. The material pressure inlet 32b is made larger in diameter than the material pressure inlet 32c for water. The reason why the inner diameters of the material pressure inlets 32b and 32c are made different from each other is that the soft ore pressed into the inside from the large diameter material pressure inlet 32b explodes into the inside from the small diameter material pressure inlet 32c. This is because the water is efficiently dissolved and slurried, and the washing water supply means 3 including the water pipe 13, the pump 23, and the water tank 33 is connected to the water material pressure inlet 32c.
Further, a sieve 32d is installed in the vicinity of the bottom of the sealed mixing chamber 32, and even if stones, rakes, dust, and insects get mixed into the original ore, it is sorted there, and these foreign substances are put into the beneficiation function section. Do not run down. Reference numeral 32e denotes a discharge unit.
[0013]
The concrete mixer 12 is a relatively soft material having about 30% moisture by supplying primary processed ore (the raw ore obtained by mining, washed with water, selected by a 10 mesh sieve and subjected to primary processing). Kneaded earth and sand are fed into the concrete pump 22 via the hopper 22a.
[0014]
The concrete pump 22 pressure-feeds the kneaded earth and sand to the closed mixing chamber 32 and press-fits into the closed mixing chamber 32 from the material pressure inlet 32b.
[0015]
In the closed mixing chamber 32, the relatively soft dough-like soil that has been press-fitted is easily dissolved and slurried with water that spills out vigorously, and the stock solution slurried through the discharge section is discharged from the top-stage beneficiation unit 1. Let it flow down.
[0016]
Reference numeral 5 denotes a stock solution pipe for letting the stock solution flow down from the discharge part 32e of the closed mixing chamber 32 to the top-stage mineral processing unit 1, and as shown in FIG. Has been.
Connected to the undiluted solution pipe 5 portion above the branch portion is a high-pressure water pipe 24 connected to the high-pressure water tank 14, and the high-pressure water pipe 24 is provided with an electromagnetic valve 6 and a check valve 7. In addition, a check valve 7 is installed in each portion of the stock solution pipe 5 upstream of the connection with the high-pressure water pipe 24. The high-pressure water pipe 24, the high-pressure water tank 14, the pump 34, etc. The supply means 4 is comprised.
[0017]
As shown in FIG. 1, the connecting section 8 of each of the beneficiation units 1 is connected to the stock solution having a water receiving part 18 a that is located immediately below the lower end of the beneficiation pipe 11... A pipe 18 and a beneficiation pipe 11 in each of the beneficiation units 1 are provided at a position in front of the lower end with a predetermined interval, and are provided with a recovery means 28 for receiving the concentrate discharged by the pressure of the high-pressure water.
[0018]
Specifically, as shown in FIG. 1, a base 200 having a hollow interior is installed at the start end portion of the installation ground 100 of each mineral processing unit 1, and the mineral processing pipe 11 in the upper mineral processing unit 1 is positioned just below the lower end. The stock solution connecting pipe 18 that supports the water portion 18a with the gantry 200 and connects the upper end to the water receiving portion 18a is branched at the lower end in the same manner as the stock solution pipe 5 so that the beneficiation pipe 11 in the lower concentration unit 1. Further, the recovery means 28 made of a container is installed on the gantry 200 with a predetermined interval X in front of the beneficiation pipe 11 in the upper stage of the beneficiation unit 1.
The connection of the high water pressure pipe 24 and the layout of the electromagnetic valve 6 and the check valve 7 to the stock solution connecting pipe 18 are the same as those of the stock solution pipe 5.
[0019]
That is, the undiluted solution flowing down from the discharge part 32e of the closed mixing chamber 32 through the undiluted pipe 5 passes through the water receiving section 18a and the undiluted solution connecting pipe 18 from the lower end of the beneficiation pipe 11 in the uppermost beneficiation unit 1. flows into the next stage of the mineral processing unit 1, and it repeatedly for each SenHiroshi unit 1 disseminating beneficiation tube 11 ... concentrate until the beneficiation unit 1 of the lowest stage.
The washing water is made to flow down through a similar route.
[0020]
On the other hand, setting the space X to a predetermined, when supplying high-pressure water by opening the electromagnetic valve 6 to the mineral processing unit 1, a stagnation product that precipitated stagnant beneficiation tube 11 ... in each beneficiation unit 1, It becomes possible to push out to the storage box which is the collecting means 28 across the water receiving portion 18a.
The setting of the space X can be determined by high pressure water pressure.
[0021]
The beneficiation pipe 11 in the lowest-stage beneficiation unit 1 is installed in front of the lower end with the recovery means 28 supported by a gantry 200 at a predetermined interval X, and the wash water receiving tank 9 is also disposed in the same beneficiation unit. Tube 11 is provided just below the lower end.
[0022]
In the present embodiment, a case is shown in which the beneficiation function unit 1A is configured by a three-stage beneficiation unit 1, and a guide cylinder 28a is provided so that push-out items can be reliably collected in the collection box as the collection means 28. The recovery box can be moved by a caster 28b, and is provided with a float-type drain valve so that moisture can always be drained by a drain pipe 28c.
[0023]
Next, the specific gravity beneficiation method using the present embodiment will be described. First, the soft ore is fed into the sealed mixing chamber 32 through the concrete mixer 12 and the concrete pump 22 and simultaneously pumped up by the washing water supply means 3. Water is discharged from the material pressure inlet 32c to make the ore into a slurry, and the undiluted solution is distributed to each beneficiation unit (three-stage beneficiation unit) 1 through the undiluted solution pipe 5, the water receiving portion 18a, and the undiluted solution connecting pipe 18. Make it.
Concentrates with high grades such as gold and iron sand have a high specific gravity and a fast sedimentation speed. The stagnation amount of concentrates with higher grades decreases from the top-stage concentrate unit 1 to the lower-stage concentrate unit 1, The sandy concentrate with the lowest grade is mainly settled and stagnates.
Then, the operation of the concrete mixer 12 and the concrete pump 22 is stopped, the operation of only the cleaning water supply means 3 is continued, and the cleaning water (water) is poured from the sealed mixing chamber 32 through the same route as the raw solution, and each of the beneficiation units 1 Washing water is received in the water receiving tank 9 from the lower end of the beneficiation pipe 11 in the mineral processing unit 1 at the lowermost stage while washing away the sediment on the surface of the concentrate.
As shown in FIG. 4, the concentrate concentrates at the downward outward angle portion 11a in each of the beneficiation pipes 11 as shown in FIG.
Completion of the cleaning starts from the uppermost beneficiation unit 1 and the lowermost beneficiation unit 1 ends.
Correspondingly, the solenoid valve 6 connected to the top-stage beneficiation unit 1 is opened to inject high-pressure water, and the concentrate that has settled at that stage is pushed out from the lower end of the beneficiation pipe 11 and the guide cylinder It collects in the collection box 28 from 28a.
This push-out is performed with a time difference for each stage in accordance with the completion of cleaning of each stage.
This series of steps is defined as one cycle.
[0024]
According to the results of experiments with gold-bearing earth and sand mines, grade 1 concentrates are available in the first stage, unit 2 grades in the second stage, and third grade units. Then, grade 3 concentrate is mainly recovered.
Assuming 100% of the gold collected in all stages, it was 86% in the first stage beneficiation unit, 5% in the second stage beneficiation unit, and 9% in the third stage beneficiation unit. I understand.
[0025]
In the present embodiment, the connecting portion 8 has a water receiving portion 18a that is located at the tip and is located immediately below the lower end of the beneficiation pipe 11 in the upper concentration unit 1. And a beneficiation pipe 11 in each of the beneficiation units 1... Are disposed at a predetermined interval X at a position in front of the lower end, and have a recovery means 28 for receiving the concentrate discharged by the pressure of the high-pressure water. For example, make the lower end of the upstream beneficiation pipe flexible and connect it to the downstream beneficiation pipe using the flexibility at the time of flowing stock solution and washing water. For example, the connection is released and the flexible means is used to connect the collecting means. Be free.
[0026]
【The invention's effect】
As described above, according to the present invention, when the stock solution on the surface of the concentrate is washed by flowing the stock solution to the uppermost beneficiation unit and sinking heavy minerals to the outward corners of each beneficiation unit and then flowing wash water. When the dredging unit is connected and then high pressure water is injected into each step, each step is disconnected so that concentrate can be discharged and collected separately from the bottom of each step. This is a specific gravity separation method that is effective for recovering concentrate in each stage, so-called grades. In particular, because it settles in the uppermost beneficiation unit, it enables highly efficient recovery of gold without bothering the sorting work.
In addition, since it is collected in each stage without waiting for all the stages to be cleaned cleanly, the supply (sink) of the stock solution to the beneficiation unit such as the uppermost stage and the beneficiation unit such as the lowermost stage. It is also possible to carry out the cleaning together with the cleaning, eliminating waste of the beneficiation time and performing efficient beneficiation.
In addition, the specific gravity separator has a flat shape in which the mineral processing units are arranged in steps with a slight gradient, and all of the multiple mineral processing pipes are piped in a zigzag shape from the upper stage to the lower stage of the multistage shelf. For example, repairing, maintaining, and managing a beneficiation pipe that is clogged with an accident, such as the prior art described above, becomes very difficult due to the influence of the complicated piping route of the beneficiation pipe, and is injured. It is possible to solve various problems such as increased equipment costs due to the cost.
In addition, the connecting part of each stage is located at the tip at a predetermined interval at the front end of the beneficiation pipe at each of the beneficiation units, and the undiluted pipe connecting pipe for the stock solution having a water receiving part located immediately below the lower end of the beneficiation pipe in the upper beneficiation unit. And the recovery means that receives the concentrate discharged so as to cross over the water receiving part with the pressure of the high-pressure water, and is controlled by a mechanical element structure or electrical structure. Compared to the case, the specific gravity concentrating device is simpler in structure, less in failure, and superior in durability.
[Brief description of the drawings]
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is a side view of a specific gravity concentrator for carrying out the specific gravity beneficiation method of this fine metal, with the middle omitted and partially cut away.
FIG. 2 is a partially cutaway view in the same plan view.
FIG. 3 shows a closed mixing chamber, (a) is shown partially cut away in an enlarged front view. (B) is the (A)-(A) line expanded sectional view.
FIG. 4 is an enlarged sectional view taken along line (B)-(B) of FIG.
[Explanation of symbols]
A: Specific gravity concentrator 1: Concentration unit 11: Concentration pipe 11a: Outward angle section 8: Communication section 18a: Receiving section 18: Concentration pipe connection pipe 28: Recovery means 2: Stock solution supply means 3: Wash water supply means 4: High pressure water supply means

Claims (4)

管内の内面全長に亘って少なくとも一つの外向角部を有する選鉱管を、その外向角部を下側に向けた状態で複数本並列した選鉱ユニットを複数体構成し、各選鉱ユニットを若干の勾配を有して段々状に配設し、各選鉱ユニットの連絡部を、最上段の選鉱ユニットに原液を流して重鉱物を各選鉱ユニットの外向角部に沈降させる時及び最上段の選鉱ユニットに洗浄水を流して沈降する各選鉱ユニットの精鉱表面の土砂を洗浄する時に連絡し且つその後高圧水を各選紘ユニット別に注入する時に各選紘ユニットの下端から別々に精鉱が吐出回収できるように非連絡とする構成とし、その高圧水を上段の選鉱ユニットの順から時間差をおいて各選紘ユニットごとに注入することを特徴とする微粒金属の比重選鉱方法。A plurality of beneficiation units in which a plurality of beneficiation pipes having at least one outward angle part along the entire inner length of the pipe are arranged in parallel with the outward angle part facing downward, and each beneficiation unit is slightly inclined. The connecting section of each beneficiation unit is flown into the uppermost beneficiation unit and the heavy mineral is allowed to sink to the outward corner of each beneficiation unit. Contact when cleaning the sediment on the surface of each concentrate unit that sinks with wash water, and when high-pressure water is injected into each selected unit, concentrate can be discharged and collected separately from the bottom of each selected unit. In this way, the high-pressure water is injected into each selection unit at a time lag from the order of the upper unit, so that the specific gravity selection method for fine metal is characterized. 前記連絡部が、上段の選鉱ユニットにおける選鉱管下端直下に位置する受水部を先端に備えた原液用連絡パイプを、下段の選鉱ユニットにおける選鉱管上端に配置していることを特徴とする請求項1記載の微粒金属の比重選鉱方法。The said connection part has arrange | positioned the connection pipe for stock solutions which equipped the water receiving part located in the front-end | tip directly in the lower part of the beneficiation pipe in the upper stage beneficiation unit at the upper end of the beneficiation pipe in a lower beneficiation unit. Item 2. A specific gravity beneficiation method for fine metal according to Item 1. 前記高圧水と共に受水部上方を横切るように選鉱ユニットの下端から吐出される精鉱を受け止める回収手段を、更に備えていることを特徴とする請求項2記載の微粒金属の比重選鉱方法。The specific gravity ore concentration method for fine metal according to claim 2, further comprising a recovery means for catching the concentrate discharged from the lower end of the beneficiation unit so as to cross the upper part of the water receiving part together with the high-pressure water. 管内の内面全長に亘って少なくとも一つの外向角部を有する選鉱管を、その外向角部を下側に向けた状態で複数体並列して選鉱ユニットを複数構成、各選鉱ユニットを若干の勾配を有して段々状に配設し、最上段の選鉱ユニットに原液供給手段、洗浄水供給手段を連絡すると共に各選鉱ユニットごとに高圧水供給手段を連絡可能に設け、各選鉱ユニットの連絡部は、上段の選鉱ユニットにおける選鉱管下端直下に先端の受水部を配置した原液用連絡パイプと、各選鉱ユニットにおける選鉱管下端の前方位置に所定の間隔をおいて設置され、前記高圧水の圧力で吐出される精鉱を受け止める回収手段とを備え、前記原液用連絡パイプを下段の選鉱ユニットにおける選鉱管の上端に配置していることを特徴とする微粒金属の比重選鉱装置。The beneficiation tube having at least one of the outward corner over the inner surface the entire length of the tube, the outward corner and a plurality of constituting a plurality body parallel to beneficiation unit in a state of facing downward and slightly to the beneficiation unit It is arranged in a stepped manner with a gradient, and communicates stock solution supply means and washing water supply means to the top-stage beneficiation unit, and also provides high-pressure water supply means for each beneficiation unit so that each beneficiation unit can communicate. Are arranged at a predetermined interval at a position in front of the lower end of the beneficiation pipe in each of the beneficiation units, and a connecting pipe for the undiluted solution in which the water receiving part at the tip is arranged immediately below the lower end of the beneficiation pipe in the upper beneficiation unit. And a recovery means for receiving the concentrate discharged at a pressure of 1 to 5, wherein the concentrate connecting pipe is disposed at the upper end of the beneficiation pipe in the lower beneficiation unit.
JP30883098A 1998-10-29 1998-10-29 Specific gravity beneficiation method of fine metal and its specific gravity beneficiation equipment Expired - Fee Related JP3704245B2 (en)

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