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JP4342782B2 - Aggregate production method and apparatus - Google Patents
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JP4342782B2 - Aggregate production method and apparatus - Google Patents

Aggregate production method and apparatus Download PDF

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Publication number
JP4342782B2
JP4342782B2 JP2002274461A JP2002274461A JP4342782B2 JP 4342782 B2 JP4342782 B2 JP 4342782B2 JP 2002274461 A JP2002274461 A JP 2002274461A JP 2002274461 A JP2002274461 A JP 2002274461A JP 4342782 B2 JP4342782 B2 JP 4342782B2
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Prior art keywords
crushed
crushed stone
size range
predetermined size
sand
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JP2003117430A (en
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正記 浜口
耕児 皆川
啓之 結城
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Earthtechnica Co Ltd
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Earthtechnica Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B20/00Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
    • C04B20/02Treatment
    • C04B20/026Comminuting, e.g. by grinding or breaking; Defibrillating fibres other than asbestos

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は,コンクリート等に用いられる骨材を,採石などの破砕により生産する骨材の生産方法及びその装置に係り,特にローラミルを用いた骨材の生産方法及びその装置に関するものである。
【0002】
【従来の技術】
近年における天然の骨材(砂利,砂)の枯渇化や採取制限などに伴い,採石を破砕して生産される人工の骨材(砕石,砕砂)の需要はますます増大している。このような原料の破砕による骨材の生産には,例えば,原料とロッド(鋼棒)が投入されたミル胴体を回転させ,上記ロッドを落下させて原料に衝撃と摩擦を与えることにより原料を破砕するロッドミルなどが従来から広く用いられてきた。しかしながら,上記ロッドミルの場合,ロッドによる衝撃破砕であるため,振動や騒音が大きく,また得られる砕石,砕砂の粒形は天然のものに比べて悪く,更にランニングコストが高いなど,その性能は必ずしも満足できるものではなかった。
そこで,低振動,低騒音,低ランニングコストで粒形の良い砕砂が得られるローラミルタイプの破砕機が注目されている。このようなローラミルタイプの破砕機を用いた砕砂製造方法が,例えば特開平7−51591号公報に提案されている。この砕砂製造方法は,粒度30−0mm,或いは5−2.5mm程度の比較的細かい原料をローラミルに投入し,砕砂を製品として得るものである。
【0003】
【発明が解決しようとする課題】
しかしながら,上記従来のローラミルを用いた骨材生産方法は,砕砂のみを製品として取り出す用途にしか用いられていなかったため,製品歩留りは50〜60%程度の低い値に留まっており,原料サイズが大きいほどその値は低くなっていた。従って,プラントの合理化のためにサイズが大きな原料を用いようとすると,歩留りは悪くなり,逆に効率を悪くしてしまう問題があった。
また,例えば砕砂製品に加えて,更に砕石製品を取り出す場合には,例えば図4に示すようなプラントを組むことで対応していた。
図4に示すプラントA0では,まずサージパイル51から供給された最大300mm程度の原料を,2次コーンクラッシャ52により最大80〜60mm程度まで破砕して篩53で分級し,比較的大きなサイズの破砕物を再度3次コーンクラッシャ54で破砕し,20−0mm程度の破砕物を得る。コーンクラッシャによる破砕物は一般に粒形が悪い(角張っている)ため,上記篩53の篩下の一部(更にその一部は路盤材として用いられる場合もある)と上記3次コーンクラッシャ54で得られた破砕物は,その一部が整粒機55によって形が整えられた後,20−5mmの砕石製品が取り出される。また,上記整粒機55に送られなかった残りの破砕物は,ローラミル56で破砕され,湿式分級機57により微粉が洗い流されて製品砕砂が取り出される。
以上のように,上記従来のローラミルを用いた骨材生産方法を用いて砕砂製品と砕石製品とを取り出す場合には,2次コーンクラッシャで得られた最大80〜60mm程度の原料から砕石製品及び砕砂製品を得るまでに,3次コーンクラッシャ,整粒器,ローラミルの3台の破砕機を具備する非常に大がかりなプラントが必要となる。
本発明は上記事情に鑑みてなされたものであり,その目的とするところは,プラントの構成を合理化しつつ,砕砂製品と砕石製品とを効率的に生産することが可能な骨材生産方法及びその装置を提供することである。
【0004】
【課題を解決するための手段】
上記目的を達成するために本発明の方法は,砕石プラントにおける2次破砕物からなる原料を,所定のサイズ範囲の上限以下になるまでローラミルで繰り返し破砕することにより砕砂と砕石とを同時に生産する骨材生産方法であって,前記原料を上記ローラミルに投入して破砕する破砕工程と,上記破砕工程で得られた破砕物を,5mmを下限とする所定サイズ範囲の砕石と,上記所定サイズ範囲の上限より大きな破砕物と,上記所定サイズ範囲の下限より小さな5mm以下の破砕物とに分級し,上記所定サイズ範囲の上限より大きな砕石を上記ローラミルへと再投入し,且つ上記5mmを下限とする所定サイズ範囲の砕石を更に粉砕することなくそのまま取り出す砕石取得工程と,所定の分級手段により,上記砕石取得工程で分級された上記所定サイズ範囲の下限より小さな粉砕物より微粉を取り除いて砕砂を取り出す砕砂取得工程とを備え,上記分級手段により取り出した砕砂を前記砕石取得工程で取り出された前記砕石とは混合することなく別に貯留してなることを特徴とする骨材生産方法として構成されている。
このように構成することにより,例えば2次破砕物を原料として砕石製品及び砕砂製品を,ローラミルのみを用いて同時に取り出すことが可能となり,プラントの構成を合理化することができると共に,両製品を合わせた歩留りを高くできるため,効率的な骨材生産を行うことが可能となる。
ここに前記原料の最大寸法の下限値が,前記砕石取得工程で得られる砕石の最大粒径以上となるように上記原料の選定と砕石取得工程における分級レベルが設定されてなることが望ましい。
また,上記目的を達成するために本発明の装置は,砕石プラントにおける2次破砕物からなる原料を,所定のサイズ範囲の上限以下になるまでローラミルで繰り返し破砕することにより砕砂と砕石とを同時に生産する骨材生産装置であって,前記原料を上記ローラミルに投入して破砕する破砕手段と,上記破砕手段で得られた破砕物を,5mmを下限とする上記所定サイズ範囲の砕石と,上記所定サイズ範囲の上限より大きな破砕物と,上記所定サイズ範囲の下限より小さな5mm以下の破砕物とに分級し,上記所定サイズ範囲の上限より大きな破砕物を上記ローラミルへと再投入し,且つ上記5mmを下限とする上記所定サイズ範囲の砕石を更に粉砕することなくそのまま取り出す砕石取得手段と,所定の分級手段により,上記砕石取得手段で分級された上記所定サイズ範囲の下限より小さな破砕物より微粉を取り除いて砕砂を取り出す砕砂取得手段とを備え,上記分級手段により取り出した砕砂を前記砕石取得工程で取り出された前記砕石とは混合することなく別に貯留してなることを特徴とする骨材生産装置として構成されている。
上記骨材生産方法は,全てこの装置上で実現可能である。
【0005】
【発明の実施の形態】
以下,添付図面を参照して本発明の実施の形態及び実施例につき説明し,本発明の理解に供する。尚,以下の実施の形態及び実施例は,本発明を具体化した一例であって,本発明の技術的範囲を限定する性格のものではない。
ここに,図1は本発明の実施の形態に係るプラントA1の概略構成を示すブロック図,図2は上記プラントA1におけるローラミル8の詳細構成を示す側面要部断面図,図3は上記ローラミル8における,動力原単位と砕砂,20−5砕石の生産比率との関係を示したグラフである。
【0006】
本実施の形態に係るプラントA1は,本発明に係る骨材生産装置を,20−5mm砕石製品と砕砂製品とを生産する砕石プラントとして具体化したものであり,図1に示すような全体構成を有する。また,このプラントA1の主要構成要素であるローラミル8は図2に示すように構成されている。
まず,図2を用いて上記ローラミル8の構成及び破砕動作について簡単に説明する。
ローラミル8は,直円筒状のハウジング21を有する。ハウジング21内には,鉛直回転軸を有するテーブル22が配置される。このテーブル22は,その下方に設けられた減速機23を介してモータ24によって回転駆動される。
上記テーブル22上には,周方向に間隔をあけて複数のローラ25が,その周面を上記テーブル22に近接させた状態で配置される。上記ローラ25は,その回転軸を上記テーブル22の半径方向に向けてアーム26に枢支される。上記アーム26は水平回転軸28を有するスイングレバー27と一体的に構成されており,上記スイングレバー27の下端部には油圧シリンダ29が接続される。従って,上記ローラ25は上記油圧シリンダ29の伸縮に応じて上記水平回転軸28を中心に揺動される。上記油圧シリンダ29を縮小すると,上記ローラ25は上記テーブル22の上面に向かって押し付けられる。
上記ハウジング21内上部には,上記テーブル22の回転軸に一致して投入シュート30が設けられている。被破砕物(原料)である採石は,この投入シュート30内に,矢印Y1のように投入され,回転駆動される上記テーブル22の中央部に供給される。上記テーブル22の中央部に供給された被破砕物は,遠心力によって上記テーブル22の半径方向に移動し,上記テーブル22と上記ローラ25との間の隙間に噛み込まれる。
上記テーブル22と上記ローラ25との間で破砕された破砕物は,テーブル22の遠心力によって更に外方に運ばれ,上記テーブル22の外周に沿って上向きに突設されたダム22aを超えてケーシング31上に落下する。ケーシング31上に落下した破砕物は,上記テーブル22に取り付けられたスクレーパ22bにより掻き取られ,上記ケーシング31上に設けられた図外の排出シュートから排出される。
【0007】
続いて,図1を用いて,プラントA1の全体構成,及び処理の流れについて説明する。本プラントA1は,上述した図4に示すプラントA0における3次コーンクラッシャ54,整粒器55,ローラミル56の3台の破砕機を1台のローラミル8に置き換えた上で,上記プラントA0と同様の処理(20−5mm砕石製品と砕砂製品の生産)を可能としたものである。
図1に示すプラントA1では,まずサージパイル1からフィーダ2を介して供給された最大300mm程度の原料が,2次コーンクラッシャ3で最大80〜40mmまで破砕される。得られた破砕物は,必要に応じてその一部が篩4で篩われてその篩下が路盤材5として取り出され,残りがホッパ6に投入される。ホッパ6に投入された最大80〜40mmの破砕物は,フィーダ7を介して上述したローラミル8に所定の投入量に基づいて投入される。上記ローラミル8は,所定の動力原単位で運転され,投入された原料の破砕処理が行われる。ここで,上記ホッパ6,フィーダ7,及びローラミル8により破砕手段の一例が構成される。上記ローラミル8から排出された破砕物は,図1に1点鎖線で囲った2つの分級装置21,22の何れかで処理される。21はエアセパレータ10を用いた乾式の分級装置であり,22は湿式分級機12を用いた湿式の分級装置である。実際には通常これらの内のいずれか一方のみが設置される。
乾式分級装置21を用いる場合には,上記ローラミル8から排出された破砕物は分級器9(砕石取得手段の一例)で分級され,20mm(所定範囲の上限の一例)以上のものは再度上記ホッパ6へ投入され,20〜5mm(所定範囲の一例)のものは20−5mmの砕石製品として取り出され,5mm(所定範囲の下限の一例)以下のものはエアセパレータ10に投入される。エアセパレータ10(砕砂取得手段の一例)では,空気により破砕物から微粉(−75μm程度)が取り除かれ,砕砂製品として取り出される。
一方,湿式分級装置22を用いる場合には,上記ローラミル8から排出された破砕物は分級器11(砕石取得手段の一例)で分級され,20mm(所定範囲の上限の一例)を超えるものは再度上記ホッパ6へ投入され,20〜5mm(所定範囲の一例)のものは20−5mmの砕石製品として取り出され,5mm(所定範囲の下限の一例)以下のものは湿式分級機12に投入される。湿式分級機12(砕砂取得手段の一例)では,水を用いて破砕物から微粉(−75μm程度)が濁水として取り除かれ,砕砂製品が取り出される。
ここで,最大原料寸法の下限は砕石製品の最大粒径以上が好ましい。原料最大寸法の下限を砕石製品の最大粒径以下とした場合,所定の粒度規格を満たさない。尚,原料最大寸法の上限は,ローラによって噛込可能な寸法以下とすればよい。
【0008】
続いて,製品として取り出される砕石と砕砂との比率について説明する。
最終的に取り出される20−5mm砕石製品と砕砂製品との比率は,ローラミル8の原料投入量ベースの動力原単位を変化させることで調整できる。これは,例えば動力原単位を下げると砕砂の生産比率が低くなり,砕石の生産比率が高くなるためである。図3は,動力原単位を変化させたときの砕砂製品と20−5mm砕石製品それぞれの全体量に対する生産量の変化を,40−0,40−20,80−0の3種類の原料について示したものである。例えば,40−0原料の場合,動力原単位が1kWh/tonの時に砕石と砕砂との生産比率は1:1(両者とも約44%)であり,動力原単位を上げるに従って砕砂の比率が上昇し,砕石の比率が下降している。その他の原料についてもその傾向は変わらない。図3より,本プラントA1の場合,動力原単位を1〜8kWh/tonの範囲で調整することにより,20−5mm砕石製品と砕砂製品との比率を1:1〜1:3の範囲で生産することが可能であることがわかる。
尚,上記ローラミル8の動力原単位は,例えばローラ25による加圧力,テーブル22の回転数,ダム22aの高さ,原料のフィード量などを調整することにより変化させることが可能である。即ち,上記ローラ25による加圧力,テーブル22の回転数,ダム22aの高さ,原料のフィード量のうちの少なくとも1つを調整することにより,上記砕石と砕砂との生産比率を調整することが可能である。
【0009】
次に,プラントA1のローラミル8における製品の歩留りについて検証する。図3より明らかなように,砕砂,砕石を合わせた製品の歩留り(砕砂製品率と20−5製品率の和)はそれぞれ87〜88%,76〜89%,74〜85%と極めて高い。
以上説明したように,本実施の形態に係るプラントA1では,2次破砕物を原料として,ローラミルのみを用いて砕石製品及び砕砂製品を共に取り出すことができ,また両製品を合わせた歩留りを高くできるため,プラントの構成を合理化しつつ,効率的な骨材生産を行うことが可能となる。また,動力原単位を変化させることにより,上記砕石と砕砂との生産比率を容易に変化させることが可能である。
【0010】
【実施例】
上記実施の形態では,本発明を砕石プラントに適用した例を示したが,砂利プラントにおいても同様に適用可能であることは言うまでもない。
また,生産する製品も砕砂に対し20−5mm砕石に限定されるものではなく,任意の製品に対応できる。
【0011】
【発明の効果】
以上説明したように,本発明は,砕石プラントにおける2次破砕物からなる原料を,所定のサイズ範囲の上限以下になるまでローラミルで繰り返し破砕することにより砕砂と砕石とを同時に生産する骨材生産装置であって,原料を上記ローラミルに投入して破砕する破砕手段と,上記破砕手段で得られた破砕物を,5mmを下限とする上記所定サイズ範囲の砕石と,上記所定サイズ範囲の上限より大きな破砕物と,上記所定サイズ範囲の下限より小さな5mm以下の破砕物とに分級し,上記所定サイズ範囲の上限より大きな破砕物を上記ローラミルへと再投入し,且つ上記5mmを下限とする所定サイズ範囲の砕石を更に粉砕することなくそのまま取り出す砕石取得手段と,所定の分級手段により,上記砕石取得手段で分級された上記所定サイズ範囲の下限より小さな破砕物より微粉を取り除いて砕砂を取り出す砕砂取得手段とを備え,上記分級手段により取り出した砕砂を前記砕石取得工程で取り出された前記砕石とは混合することなく別に貯留してなることを特徴とする骨材生産装置として構成されているため,例えば2次破砕物を原料として,ローラミルのみを用いて砕石製品及び砕砂製品を共に取り出すことができ,プラントの構成を合理化することができると共に,両製品を合わせた歩留りを高くできるため,効率的な骨材生産を行うことが可能となる。
【図面の簡単な説明】
【図1】 本発明の実施の形態に係るプラントA1の概略構成を示すブロック図。
【図2】 上記プラントA1におけるローラミル8の詳細構成を示す側面要部断面図。
【図3】 上記ローラミル8における,動力原単位と砕砂,20−5砕石の生産比率との関係を示したグラフ。
【図4】 従来のプラントA0の概略構成を示すブロック図。
【符号の説明】
3…2次コーンクラッシャ
6…ホッパ
7…フィーダ
8…ローラミル
9…分級機
10…エアセパレータ
11…分級機
12…湿式分級機
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an aggregate production method and apparatus for producing aggregate used for concrete or the like by crushing quarrying, and more particularly to an aggregate production method and apparatus using a roller mill.
[0002]
[Prior art]
With the recent depletion of natural aggregates (gravel, sand) and restrictions on collection, demand for artificial aggregates (crushed stone, crushed sand) produced by crushing quarry is increasing. In the production of aggregates by crushing such raw materials, for example, the mill body into which raw materials and rods (steel bars) are charged is rotated, and the rods are dropped to give impact and friction to the raw materials. Conventionally, a rod mill for crushing has been widely used. However, in the case of the above-mentioned rod mill, since it is impact crushing with a rod, the vibration and noise are large, and the obtained crushed stone and crushed sand are not as good as natural ones, and the running cost is high. It was not satisfactory.
In view of this, roller mill type crushers that can obtain crushed sand with good grain shape with low vibration, low noise, and low running cost are attracting attention. A method for producing crushed sand using such a roller mill type crusher has been proposed in, for example, Japanese Patent Application Laid-Open No. 7-51591. In this crushed sand production method, a relatively fine raw material having a particle size of about 30-0 mm or about 5-2.5 mm is charged into a roller mill to obtain crushed sand as a product.
[0003]
[Problems to be solved by the invention]
However, the aggregate production method using the conventional roller mill has been used only for the purpose of taking out only the crushed sand as a product, so that the product yield remains as low as about 50 to 60%, and the raw material size is large. The value was low. Therefore, when trying to use raw materials with a large size for rationalization of the plant, there is a problem that the yield deteriorates and conversely the efficiency deteriorates.
Further, for example, in addition to the crushed sand product, when the crushed stone product is further taken out, for example, a plant as shown in FIG. 4 is set up.
In the plant A0 shown in FIG. 4, first, a raw material having a maximum size of about 300 mm supplied from the surge pile 51 is crushed to a maximum size of about 80 to 60 mm by a secondary cone crusher 52 and classified by a sieve 53, and a relatively large size crushing is performed. The material is crushed again by the third cone crusher 54 to obtain a crushed material of about 20-0 mm. Since the crushed material by the cone crusher generally has a poor particle shape (angular), a part of the sieve 53 below the sieve 53 (and a part thereof may be used as a roadbed material) and the third cone crusher 54 Part of the obtained crushed material is trimmed by the granulator 55, and then a crushed stone product of 20-5 mm is taken out. The remaining crushed material that has not been sent to the granulator 55 is crushed by the roller mill 56, and the fine powder is washed away by the wet classifier 57, and the product crushed sand is taken out.
As described above, when taking out the crushed sand product and the crushed stone product using the above-described conventional aggregate production method using a roller mill, the crushed stone product and the crushed stone product from the maximum 80-60 mm obtained by the secondary corn crusher, In order to obtain a crushed sand product, a very large plant equipped with three crushers, a tertiary corn crusher, a granulator, and a roller mill, is required.
The present invention has been made in view of the above circumstances, and its object is to produce an aggregate production method capable of efficiently producing a crushed sand product and a crushed stone product while rationalizing the configuration of the plant, and It is to provide such a device.
[0004]
[Means for Solving the Problems]
In order to achieve the above object, the method of the present invention simultaneously produces crushed sand and crushed stone by repeatedly crushing a raw material composed of secondary crushed material in a crushed stone plant with a roller mill until it falls below the upper limit of a predetermined size range. a aggregate production method, a crushing step of crushing the raw material was charged into the roller mill, the crushed product obtained in the above crushing step, and crushed stone of a given size range that the lower limit 5 mm, the predetermined size Classification into crushed material larger than the upper limit of the range and crushed material less than 5 mm smaller than the lower limit of the predetermined size range, re-entering the crushed stone larger than the upper limit of the predetermined size range into the roller mill, and lower limit of 5 mm and the crushed stone acquisition step of taking intact without further grinding the crushed stone of a predetermined size range which, by a predetermined classification means, after being classified by the crushed stone acquisition step Serial and a crushed sand acquisition step of removing the fine powder taken out crushed sand smaller ground product than the lower limit of the predetermined size range, separately without mixing with the crushed stone a crushed sand with retrieved by the crushed stone acquisition step removed by the classification means It is configured as an aggregate production method characterized by being stored.
With this configuration, for example, a crushed stone product and a crushed sand product can be taken out simultaneously using only a roller mill using secondary crushed material as a raw material, the plant configuration can be streamlined, and both products can be combined. Therefore, it is possible to increase the production yield.
Here, it is desirable that the selection of the raw material and the classification level in the crushed stone obtaining step are set so that the lower limit value of the maximum dimension of the raw material is not less than the maximum particle size of the crushed stone obtained in the crushed stone obtaining step.
In order to achieve the above object, the apparatus of the present invention is capable of simultaneously breaking crushed sand and crushed stone by repeatedly crushing a raw material consisting of secondary crushed material in a crushed stone plant with a roller mill until it falls below the upper limit of a predetermined size range. a aggregate production apparatus for producing a crushing means for crushing the raw material was charged into the roller mill, the crushed product obtained in the above pulverizing means, and crushed stone of the predetermined size range of the lower limit 5 mm, Classifying the crushed material larger than the upper limit of the predetermined size range and the crushed material of 5 mm or less smaller than the lower limit of the predetermined size range, re-injecting the crushed material larger than the upper limit of the predetermined size range into the roller mill, and and crushed stone acquisition means for retrieving it without further grinding crushed stones of the predetermined size range to limit the 5 mm, by a predetermined classification means, the crushed stone get hands Remove the fines smaller crushed than the lower limit of the classified the predetermined size range stage and a crushed sand acquiring means for taking the crushed sand, and the said crushed stones taken out of crushed sand extracted by the classifying means in the crushed stone acquisition step It is constituted as an aggregate production device characterized by being stored separately without mixing .
All the above-mentioned aggregate production methods can be realized on this device.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments and examples of the present invention will be described with reference to the accompanying drawings to provide an understanding of the present invention. It should be noted that the following embodiments and examples are examples embodying the present invention, and do not limit the technical scope of the present invention.
FIG. 1 is a block diagram showing a schematic configuration of the plant A1 according to the embodiment of the present invention, FIG. 2 is a side sectional view showing a detailed configuration of the roller mill 8 in the plant A1, and FIG. It is the graph which showed the relationship between the power basic unit, crushed sand, and the production ratio of 20-5 crushed stone.
[0006]
A plant A1 according to the present embodiment embodies the aggregate production apparatus according to the present invention as a crushed stone plant that produces a 20-5 mm crushed stone product and a crushed sand product, and has an overall configuration as shown in FIG. Have Moreover, the roller mill 8 which is a main component of the plant A1 is configured as shown in FIG.
First, the configuration and crushing operation of the roller mill 8 will be briefly described with reference to FIG.
The roller mill 8 has a right cylindrical housing 21. A table 22 having a vertical rotation axis is disposed in the housing 21. The table 22 is rotationally driven by a motor 24 via a speed reducer 23 provided below the table 22.
On the table 22, a plurality of rollers 25 are arranged at intervals in the circumferential direction with their circumferential surfaces being close to the table 22. The roller 25 is pivotally supported by the arm 26 with its rotating shaft directed in the radial direction of the table 22. The arm 26 is formed integrally with a swing lever 27 having a horizontal rotation shaft 28, and a hydraulic cylinder 29 is connected to the lower end of the swing lever 27. Accordingly, the roller 25 is swung around the horizontal rotation shaft 28 according to the expansion and contraction of the hydraulic cylinder 29. When the hydraulic cylinder 29 is reduced, the roller 25 is pressed toward the upper surface of the table 22.
A throwing chute 30 is provided in the upper part of the housing 21 so as to coincide with the rotational axis of the table 22. The quarry, which is the material to be crushed (raw material), is input into the input chute 30 as indicated by an arrow Y1, and is supplied to the central portion of the table 22 that is rotationally driven. The object to be crushed supplied to the central portion of the table 22 moves in the radial direction of the table 22 by centrifugal force, and is caught in the gap between the table 22 and the roller 25.
The crushed material crushed between the table 22 and the roller 25 is further transported outward by the centrifugal force of the table 22 and exceeds the dam 22a protruding upward along the outer periphery of the table 22. It falls on the casing 31. The crushed material dropped on the casing 31 is scraped off by a scraper 22b attached to the table 22 and discharged from a discharge chute (not shown) provided on the casing 31.
[0007]
Then, the whole structure of plant A1 and the flow of a process are demonstrated using FIG. This plant A1 is the same as the above plant A0 after replacing the three crushers of the tertiary cone crusher 54, the granulator 55, and the roller mill 56 in the plant A0 shown in FIG. 4 with one roller mill 8. (Production of crushed stone product and crushed sand product).
In the plant A1 shown in FIG. 1, the raw material having a maximum of about 300 mm supplied from the surge pile 1 through the feeder 2 is first crushed by the secondary cone crusher 3 to a maximum of 80 to 40 mm. A part of the obtained crushed material is sieved with a sieve 4 as necessary, and the sieved material is taken out as a roadbed material 5 and the rest is put into a hopper 6. A maximum of 80 to 40 mm of crushed material charged into the hopper 6 is charged into the above-described roller mill 8 through the feeder 7 based on a predetermined charging amount. The roller mill 8 is operated at a predetermined power unit, and the input raw material is crushed. Here, an example of the crushing means is constituted by the hopper 6, the feeder 7 and the roller mill 8. The crushed material discharged from the roller mill 8 is processed by one of the two classifiers 21 and 22 surrounded by a one-dot chain line in FIG. 21 is a dry classifier using the air separator 10, and 22 is a wet classifier using the wet classifier 12. In practice, usually only one of these is installed.
When the dry classifier 21 is used, the crushed material discharged from the roller mill 8 is classified by the classifier 9 (an example of the crushed stone obtaining means), and those having a size of 20 mm (an example of the upper limit of the predetermined range) or more are again classified into the hopper. 6, 20 to 5 mm (an example of the predetermined range) is taken out as a crushed stone product of 20-5 mm, and 5 mm (an example of the lower limit of the predetermined range) or less is put into the air separator 10. In the air separator 10 (an example of the crushed sand acquisition means), fine powder (about -75 μm) is removed from the crushed material by air and is taken out as a crushed sand product.
On the other hand, when the wet classifier 22 is used, the crushed material discharged from the roller mill 8 is classified by the classifier 11 (an example of the crushed stone obtaining means), and those exceeding 20 mm (an example of the upper limit of the predetermined range) are again used. It is thrown into the hopper 6 and 20 to 5 mm (an example of a predetermined range) is taken out as a crushed stone product of 20-5 mm, and a piece of 5 mm (an example of the lower limit of the predetermined range) or less is put into a wet classifier 12. . In the wet classifier 12 (an example of the crushed sand acquisition means), fine powder (about -75 μm) is removed from the crushed material as turbid water using water, and the crushed sand product is taken out.
Here, the lower limit of the maximum raw material size is preferably equal to or greater than the maximum particle size of the crushed stone product. If the lower limit of the maximum raw material size is less than or equal to the maximum particle size of the crushed stone product, the specified particle size standard is not satisfied. Note that the upper limit of the maximum raw material size may be set to a size that can be bitten by the roller.
[0008]
Subsequently, the ratio of crushed stone and crushed sand taken out as a product will be described.
The ratio of the 20-5 mm crushed stone product and the crushed sand product finally taken out can be adjusted by changing the power unit of the roller mill 8 based on the amount of raw material input. This is because, for example, when the power unit is lowered, the production rate of crushed sand is lowered and the production rate of crushed stone is raised. Fig. 3 shows the change in the production amount with respect to the total amount of each of the crushed sand product and the 20-5 mm crushed stone product when the power unit is changed for the three types of raw materials 40-0, 40-20, and 80-0. It is a thing. For example, in the case of 40-0 raw material, when the power unit is 1 kWh / ton, the production ratio of crushed stone and crushed sand is 1: 1 (both are about 44%), and the ratio of crushed sand increases as the power unit increases. However, the ratio of crushed stone is decreasing. The trend does not change for other raw materials. According to FIG. 3, in the case of this plant A1, the ratio of 20-5 mm crushed stone product to crushed sand product is produced in the range of 1: 1 to 1: 3 by adjusting the power unit in the range of 1 to 8 kWh / ton. You can see that it is possible.
The power unit of the roller mill 8 can be changed by adjusting the pressure applied by the roller 25, the rotational speed of the table 22, the height of the dam 22a, the feed amount of the raw material, and the like. That is, the production ratio of the crushed stone and the crushed sand can be adjusted by adjusting at least one of the pressure applied by the roller 25, the rotational speed of the table 22, the height of the dam 22a, and the feed amount of the raw material. Is possible.
[0009]
Next, the product yield in the roller mill 8 of the plant A1 will be verified. As is apparent from FIG. 3, the yield of the product combining crushed sand and crushed stone (sum of the crushed sand product rate and 20-5 product rate) is 87 to 88%, 76 to 89%, and 74 to 85%, respectively.
As described above, in the plant A1 according to the present embodiment, the crushed stone product and the crushed sand product can be taken out using only the roller mill using the secondary crushed material as a raw material, and the combined yield of both products is high. Therefore, efficient aggregate production can be performed while rationalizing the plant configuration. Moreover, it is possible to easily change the production ratio of the crushed stone and crushed sand by changing the power unit.
[0010]
【Example】
In the said embodiment, although the example which applied this invention to the crushed stone plant was shown, it cannot be overemphasized that it can apply similarly to a gravel plant.
Further, the product to be produced is not limited to 20-5 mm crushed stone with respect to crushed sand, and any product can be handled.
[0011]
【The invention's effect】
As described above, the present invention is an aggregate production that simultaneously produces crushed sand and crushed stone by repeatedly crushing a raw material consisting of secondary crushed material in a crushed stone plant with a roller mill until it falls below the upper limit of a predetermined size range. an apparatus comprising: crushing means for crushing the raw material was charged into the roller mill, the crushed product obtained in the above pulverizing means, and crushed stone of the predetermined size range of the lower limit 5 mm, the upper limit of the predetermined size range Classify into larger crushed material and crushed material of 5 mm or less smaller than the lower limit of the predetermined size range, re-inject the crushed material larger than the upper limit of the predetermined size range into the roller mill, and set the lower limit to 5 mm. and crushed stone acquisition means for retrieving it without further grinding the crushed stone of a predetermined size range, by a predetermined classification means, the classified the predetermined service by the crushed stone acquiring means And a crushed sand acquiring means for taking the crushed sand by removing fines smaller crushed than the lower limit of the size range, separately from the reservoir without mixing with the crushed stone a crushed sand with retrieved by the crushed stone acquisition step removed by the classification means Since it is configured as an aggregate production device characterized by the above, for example, it is possible to take out both crushed stone products and crushed sand products using only a roller mill using secondary crushed material as a raw material, thereby streamlining the plant configuration In addition, it is possible to increase the yield of both products together, thus enabling efficient aggregate production.
[Brief description of the drawings]
FIG. 1 is a block diagram showing a schematic configuration of a plant A1 according to an embodiment of the present invention.
FIG. 2 is a side sectional view showing a detailed configuration of a roller mill 8 in the plant A1.
FIG. 3 is a graph showing the relationship between the power unit, the crushed sand, and the production ratio of 20-5 crushed stone in the roller mill 8;
FIG. 4 is a block diagram showing a schematic configuration of a conventional plant A0.
[Explanation of symbols]
3 ... Secondary cone crusher 6 ... Hopper 7 ... Feeder 8 ... Roller mill 9 ... Classifier 10 ... Air separator 11 ... Classifier 12 ... Wet classifier

Claims (3)

砕石プラントにおける2次破砕物からなる原料を,所定のサイズ範囲の上限以下になるまでローラミルで繰り返し破砕することにより砕砂と砕石とを同時に生産する骨材生産方法であって,
前記原料を上記ローラミルに投入して破砕する破砕工程と,
上記破砕工程で得られた破砕物を,5mmを下限とする上記所定サイズ範囲の砕石と,上記所定サイズ範囲の上限より大きな破砕物と,上記所定サイズ範囲の下限より小さな5mm以下の破砕物とに分級し,上記所定サイズ範囲の上限より大きな破砕物を上記ローラミルへと再投入し,且つ上記5mmを下限とする上記所定サイズ範囲の砕石を更に粉砕することなくそのまま取り出す砕石取得工程と,
所定の分級手段により,上記砕石取得工程で分級された上記所定サイズ範囲の下限より小さな破砕物より微粉を取り除いて砕砂を取り出す砕砂取得工程とを備え,
上記分級手段により取り出した砕砂を前記砕石取得工程で取り出された前記砕石とは混合することなく別に貯留してなることを特徴とする骨材生産方法。
An aggregate production method for simultaneously producing crushed sand and crushed stone by repeatedly crushing a raw material composed of secondary crushed material in a crushed stone plant with a roller mill until it falls below the upper limit of a predetermined size range ,
A crushing step of crushing the raw material was charged into the roller mill,
The crushed product obtained in the above crushing step, and crushed stone of the predetermined size range of the lower limit 5mm, large crushed than the upper limit of the predetermined size range and a small 5mm below crushed than the lower limit of the predetermined size range If you binary class, and it is taken out crushed stone acquisition step without large crushed than the upper limit of the predetermined size range on again into the roller mill, and further pulverized crushed stone of the predetermined size range to limit the 5mm ,
A crushed sand obtaining step of removing pulverized sand from a crushed material smaller than the lower limit of the predetermined size range classified in the crushed stone obtaining step by a predetermined classification means;
Aggregate production method characterized by comprising pooled separately without mixing with the crushed stone a crushed sand extracted by the classifying means has been removed by the crushed stone acquisition step.
前記原料の最大寸法の下限値が,前記砕石取得工程で得られる砕石の最大粒径以上となるように上記原料の選定と砕石取得工程における分級レベルが設定されてなる請求項1に記載の骨材生産方法。  The bone according to claim 1, wherein the selection of the raw material and the classification level in the crushed stone obtaining step are set so that the lower limit of the maximum dimension of the raw material is equal to or greater than the maximum particle size of the crushed stone obtained in the crushed stone obtaining step. Material production method. 砕石プラントにおける2次破砕物からなる原料を,所定のサイズ範囲の上限以下になるまでローラミルで繰り返し破砕することにより砕砂と砕石とを同時に生産する骨材生産装置であって,
前記原料を上記ローラミルに投入して破砕する破砕手段と,
上記破砕手段で得られた破砕物を,5mmを下限とする上記所定サイズ範囲の砕石と,上記所定サイズ範囲の上限より大きな破砕物と,上記所定サイズ範囲の下限より小さな5mm以下の破砕物とに分級し,上記所定サイズ範囲の上限より大きな破砕物を上記ローラミルへと再投入し,且つ上記5mmを下限とする上記所定サイズ範囲の砕石を更に粉砕することなくそのまま取り出す砕石取得手段と,
所定の分級手段により,上記砕石取得手段で分級された上記所定サイズ範囲の下限より小さな破砕物より微粉を取り除いて砕砂を取り出す砕砂取得手段とを備え,
上記分級手段により取り出した砕砂を前記砕石取得手段で取り出された前記砕石とは混合することなく別に貯留してなることを特徴とする骨材生産装置。
An aggregate production apparatus that simultaneously produces crushed sand and crushed stone by repeatedly crushing a raw material composed of secondary crushed material in a crushed stone plant with a roller mill until it falls below the upper limit of a predetermined size range ,
A crushing unit for crushing the raw material was charged into the roller mill,
The resulting crushed material in the crushing unit, and crushed stone of the predetermined size range of the lower limit 5mm, large crushed than the upper limit of the predetermined size range and a small 5mm below crushed than the lower limit of the predetermined size range Crushed material larger than the upper limit of the predetermined size range is reintroduced into the roller mill, and the crushed stone obtaining means for taking out the crushed stone in the predetermined size range with the lower limit of 5 mm as it is without further pulverization;
Crushed sand acquisition means for removing fine powder from crushed material smaller than the lower limit of the predetermined size range classified by the crushed stone obtaining means and taking out crushed sand by predetermined classification means,
Aggregate production apparatus characterized by being stored separately without mixing with the crushed stone retrieved the crushed sand extracted by the classifying means in the crushed stone acquisition means.
JP2002274461A 2002-09-20 2002-09-20 Aggregate production method and apparatus Expired - Fee Related JP4342782B2 (en)

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