JP2003053269A - Classifier for fine particle of crushed sand - Google Patents
Classifier for fine particle of crushed sandInfo
- Publication number
- JP2003053269A JP2003053269A JP2001244705A JP2001244705A JP2003053269A JP 2003053269 A JP2003053269 A JP 2003053269A JP 2001244705 A JP2001244705 A JP 2001244705A JP 2001244705 A JP2001244705 A JP 2001244705A JP 2003053269 A JP2003053269 A JP 2003053269A
- Authority
- JP
- Japan
- Prior art keywords
- crushed sand
- chamber
- main body
- classification
- fine powder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000004576 sand Substances 0.000 title claims abstract description 140
- 239000010419 fine particle Substances 0.000 title abstract 4
- 238000007873 sieving Methods 0.000 claims abstract description 26
- 239000000843 powder Substances 0.000 claims description 40
- 238000000605 extraction Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 abstract 3
- 239000002245 particle Substances 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002452 interceptive effect Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 102100029777 Eukaryotic translation initiation factor 3 subunit M Human genes 0.000 description 1
- 101001012700 Homo sapiens Eukaryotic translation initiation factor 3 subunit M Proteins 0.000 description 1
- 101001094026 Synechocystis sp. (strain PCC 6803 / Kazusa) Phasin PhaP Proteins 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B20/00—Use 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
- C04B20/0076—Use 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 characterised by the grain distribution
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、乾式製砂設備にお
いて用いられる分級機であって、破砕機により破砕され
た砕砂をJIS規格により規定された砕砂としてコンク
リート骨材に使用できるようにダストや脆弱部、不純物
等(以下、微粉等という)を取り除くことができるよう
にした砕砂微粉分級機に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a classifier used in a dry sand making facility, which is capable of using crushed sand crushed by a crusher as concrete crushed sand specified in JIS standard for concrete aggregate. The present invention relates to a crushed sand fine powder classifier capable of removing fragile portions, impurities and the like (hereinafter referred to as fine powder).
【0002】[0002]
【従来の技術】今日、山砂、海砂等の天然砂の採取が次
第に困難となり、天然砂に取って代わる骨材として砕砂
の需要が大きくなっている。乾式製砂設備では、破砕
機、選別機、分級機、集塵設備、搬送設備、機械駆動の
為の電力設備及び操作盤等、過大な設備投資が必要にな
る。また、湿式製砂設備であれば、更に汚水処理設備な
どが必要となるので、砕砂の普及に対して悪影響を及ぼ
している。特に、砕砂をコンクリート用骨材として使用
する為には、JIS規格によって規定された砕砂の粒度
と、洗い試験の条件を満たすことが最低限必要であり、
砕砂の生産業者には、更に性状の優れた砕砂を生産する
ことが要求されている。2. Description of the Related Art Today, it becomes increasingly difficult to collect natural sand such as mountain sand and sea sand, and demand for crushed sand as an aggregate to replace natural sand is increasing. Dry sand making equipment requires excessive capital investment such as a crusher, a sorter, a classifier, a dust collecting equipment, a transportation equipment, an electric power equipment for driving the machine and an operation panel. In addition, since wet-type sand making equipment requires additional sewage treatment equipment, it has an adverse effect on the spread of crushed sand. In particular, in order to use crushed sand as an aggregate for concrete, it is at least necessary to meet the crushed sand particle size specified by the JIS standard and the washing test conditions.
Crushed sand producers are required to produce crushed sand with even better properties.
【0003】本発明の出願人は、砕砂微粉分級機の設備
の簡素化と合理化を研究し、特願2000−32393
3号、更に特願2000−323935号において、新
規な砕砂微粉分級機を既に提案している。The applicant of the present invention has studied the simplification and rationalization of the equipment of a crushed sand fine powder classifier, and has filed Japanese Patent Application No. 2000-32393.
No. 3 and Japanese Patent Application No. 2000-323935 have already proposed a new crushed sand fine powder classifier.
【0004】[0004]
【発明が解決しようとする課題】先行技術としての特願
2000−323933号の発明では、原料砕砂が加振
機による振動で分級面上を上から下に向けて移動する際
に、各受板間に形成した空気流入路を経て空気が分級室
に吹き出される。そして、このようにして分級室内に吹
き飛ばされた微粉等は、空気とともに排気口からバクフ
イルタ等の集塵機に収集されて堆積回収され、又、微粉
等を取り除いた分級済砕砂は、分級面の下端部から落下
し、砕砂取出口から取り出されるようになっている。In the invention of Japanese Patent Application No. 2000-323933 as a prior art, when the raw material crushed sand moves from the top to the bottom on the classification surface by the vibration of the vibration exciter, each receiving plate Air is blown into the classification chamber through the air inflow path formed between them. Then, the fine powder and the like blown into the classification chamber in this way is collected together with the air from the exhaust port to a dust collector such as a bag filter, and collected and collected. It is designed to be dropped from the crushed sand extraction port.
【0005】ところで、一般的な乾式製砂設備にあって
は、破砕機のあとに選別機を設け、オーバーサイズを篩
い分ける。その後、分級機を通過させて微粉を取り除く
ようになっているが、比較的にオーバーサイズが少な
く、全体量も多くない場合には、篩い分けと分級の設備
を別々に設けると不経済であることも多い。この点にお
いて、前記した先行技術の砕砂微粉分級機についても、
砕砂に含まれる微粉等を除去させるための分級機能が主
であり、オーバーサイズの除去を目的とした篩い分け機
能は備えていないものであった。By the way, in a general dry sand making facility, a crusher is provided after the crusher to screen out oversize. After that, it passes through a classifier to remove fine powder, but if the oversize is relatively small and the total amount is not large, it is uneconomical to install separate sieving and classifying equipment. There are many things. In this regard, the above-mentioned prior art crushed sand fine powder classifier,
It mainly had a classification function for removing fine powder contained in crushed sand, and did not have a sieving function for the purpose of removing oversize.
【0006】本発明は、かかる点に鑑みなされたもの
で、篩い分け機と分級機の設備を別々に設けるのではな
く、砕砂に含まれる微粉等の除去を主目的としながら、
同時にオーバーサイズの除去ができる篩い分け機能を付
加することで、設備の経済負担の軽減及び作業能率の向
上ができるようにした砕砂微粉分級機を提供することを
課題としている。[0006] The present invention has been made in view of the above points. The main purpose of the present invention is to remove fine powder and the like contained in crushed sand, instead of separately providing facilities of a sieving machine and a classifier,
At the same time, it is an object of the present invention to provide a crushed sand fine powder classifier capable of reducing the economic burden on equipment and improving work efficiency by adding a sieving function capable of removing oversize.
【0007】[0007]
【課題を解決するための手段】上記の課題を解決するた
めに、本発明の砕砂微粉分級機(請求項1)は、スプリ
ングにより弾性支持された本体に振動を与える加振手段
と、本体内部に複数の受板を階段状に配設して、砕砂を
上段から下段へ向けて移動させるように形成された分級
面と、分級面の上端部に原料砕砂を供給するように本体
の一端部に形成された砕砂投入口と、分級面の下端部か
ら分級済砕砂を取り出すように本体の他端部に形成され
た砕砂排出室及びこの砕砂排出室の下方に開口するよう
に本体に形成された砕砂取出口と、分級面の上面側に形
成された分級室及びこの分級室の上方に開口するように
本体に形成された排気口と、分級面の下面側に形成され
た空気流入室及びこの空気流入室内に開口するように本
体に形成された空気取り入れ口と、前記各受板の先端部
から砕砂の移動方向に延長して設けられた網状体と、空
気流入室から網状体の下方に開口して分級室に連通する
ように各受板間に形成されている空気流入路とを備えて
いる砕砂微粉分級機において、砕砂排出室内に配置され
るように、最下段の受板の先端部に分級面とは別の網状
体である篩分け網が水平若しくは下り勾配になるように
取付けられ、前記砕砂取出口が、篩分け網の下方部分に
形成されたアンダーサイズ取出口と、篩分け網の先方下
方部分に形成されたオーバーサイズ取出口に区画されて
いる構成とした。In order to solve the above-mentioned problems, the crushed sand fine powder classifier (Claim 1) of the present invention comprises a vibrating means for vibrating a main body elastically supported by a spring and an inside of the main body. A plurality of receiving plates are arranged in a staircase, and the classification surface is formed so as to move the crushed sand from the upper level to the lower level, and one end of the main body for supplying the raw crushed sand to the upper end of the classification surface. The crushed sand input port formed in, and the crushed sand discharge chamber formed at the other end of the main body so as to take out the classified crushed sand from the lower end of the classification surface, and the main body formed so as to open below this crushed sand discharge chamber. Crushed sand outlet, a classification chamber formed on the upper side of the classification surface, an exhaust port formed on the main body so as to open above the classification chamber, an air inflow chamber formed on the lower surface side of the classification surface, An empty space formed in the main body to open into this air inflow chamber. An intake port, a net-like member extending from the tip of each of the receiving plates in the moving direction of the crushed sand, and a space between the receiving plates so that the air-inflow chamber opens below the net-like member and communicates with the classification chamber. In the crushed sand fine powder classifier equipped with the air inflow path formed in the above, the sieving which is a reticulated body different from the classification surface is provided at the tip of the bottom receiving plate so that it is placed in the crushed sand discharge chamber. The mesh is installed so as to be horizontal or downwardly inclined, and the crushed sand extraction port is an undersize extraction port formed in the lower part of the sieving mesh and an oversize extraction port formed in the lower front part of the sieving mesh. The structure is divided into.
【0008】本発明の砕砂微粉分級機において、分級室
を複数の分級小室に仕切るように、本体上面から概ね垂
直真下へ向けて、分級面上を移動する砕砂に接触しない
程度の範囲でバッフルプレートが垂設されると共に、各
分級小室にそれぞれ排気口が形成されている態様(請求
項2)がある。In the crushed sand fine powder classifier of the present invention, the baffle plate is divided into a plurality of classifying chambers so that the baffle plate is directed vertically downward from the upper surface of the main body and does not come into contact with crushed sand moving on the classifying surface. Is provided vertically, and an exhaust port is formed in each classification small chamber (claim 2).
【0009】又、本発明の砕砂微粉分級機において、分
級室と砕砂排出室との境部分に、本体上面から概ね垂直
真下へ向けて、分級面上を移動する砕砂に接触しない程
度の範囲でバッフルプレートが垂設されている態様(請
求項3)がある。Further, in the crushed sand fine powder classifier of the present invention, the boundary between the classification chamber and the crushed sand discharge chamber is directed vertically downward from the upper surface of the main body so that it does not come into contact with the crushed sand moving on the classification surface. There is a mode (claim 3) in which the baffle plate is vertically installed.
【0010】又、本発明の砕砂微粉分級機において、分
級室を複数の分級小室に仕切るように、本体上面から概
ね垂直真下へ向けて、分級面上を移動する砕砂に接触し
ない程度の範囲でバッフルプレートが垂設されると共
に、各分級小室にそれぞれ排気口が形成され、前記分級
室と砕砂排出室との境部分に、本体上面から概ね垂直真
下へ向けて、分級面上を移動する砕砂に接触しない程度
の範囲でバッフルプレートが垂設されている態様(請求
項4)がある。Further, in the crushed sand fine powder classifier of the present invention, the classifying chamber is divided into a plurality of classifying small chambers in a range that does not come into contact with the crushed sand moving on the classifying surface from the upper surface of the main body substantially vertically downward. A baffle plate is installed vertically, and an exhaust port is formed in each classifying chamber, and at the boundary between the classifying chamber and the crushed sand discharge chamber, the crushed sand moves on the classification surface from the upper surface of the main body to a position almost vertically downward. There is a mode (claim 4) in which the baffle plate is vertically installed within a range in which the baffle plate does not come into contact with.
【0011】又、本発明の砕砂微粉分級機において、バ
ッフルプレートの下端が、砕砂投入口側へ垂直から概ね
水平の範囲で屈曲している態様(請求項5)がある。Further, in the crushed sand fine powder classifier of the present invention, there is a mode in which the lower end of the baffle plate is bent toward the crushed sand inlet side in a range from vertical to substantially horizontal (claim 5).
【0012】[0012]
【発明の実施の形態】以下、本発明の実施の形態を図面
により詳述する。尚、本発明の具体的な構成は、以下の
実施の形態に限定されるものではない。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below with reference to the drawings. The specific configuration of the present invention is not limited to the following embodiments.
【0013】図1は本発明の実施の第1形態である砕砂
微粉分級機の断面図である。図において、1は本体で、
内部に傾斜状空間が形成された函体に形成され、図示省
略したスプリングにより弾性支持されている。この本体
1の下面部には振動手段としての加振機2が連結されて
いる。この加振機2は、その振動方向Bが砕砂の移動方
向(矢印A方向)に傾く状態で、本体1と加振機2を合
わせたほぼ重心部を通るように取り付けられている。FIG. 1 is a sectional view of a crushed sand fine powder classifier which is a first embodiment of the present invention. In the figure, 1 is a main body,
It is formed in a box body having an inclined space formed therein, and is elastically supported by a spring (not shown). A vibrator 2 as a vibrating unit is connected to the lower surface of the main body 1. The vibration exciter 2 is attached so that the vibration direction B thereof is inclined in the moving direction of the crushed sand (the direction of arrow A) so as to pass through substantially the center of gravity of the main body 1 and the vibration exciter 2.
【0014】本体1の内部には、複数の受板30を階段
状に配設して、前記加振機2による振動で砕砂を上から
下に向けて移動(矢印A方向)させるように形成された
分級面3が形成されている。Inside the main body 1, a plurality of receiving plates 30 are arranged in a step-like manner so that the crushed sand is moved from the top to the bottom (in the direction of arrow A) by the vibration of the vibrator 2. The classified surface 3 is formed.
【0015】この分級面3の上面側には分級室4が形成
されると共に、分級面3の裏面側には空気流入室5が形
成され、この空気流入室5から分級室4に連通するよう
に各受板30,30間に空気流入路31が形成されてい
る。そして、各受板30の先端部には、砕砂の移動方向
に延長して網状体32が設けられ、前記空気流入路31
がこの網状体32の下方に開口するように形成されてい
る。A classification chamber 4 is formed on the upper surface side of the classification surface 3 and an air inflow chamber 5 is formed on the back surface side of the classification surface 3 so that the air inflow chamber 5 communicates with the classification chamber 4. An air inflow passage 31 is formed between the receiving plates 30, 30. A net-like body 32 is provided at the tip of each receiving plate 30 so as to extend in the moving direction of the crushed sand.
Are formed so as to open below the mesh body 32.
【0016】又、本体1の上端部には砕砂投入口60が
形成されており、この砕砂投入口60から投入された原
料砕砂S1がガイド板61を経て分級面3の上端部に供
給されるようになっている。Further, a crushed sand input port 60 is formed at the upper end of the main body 1, and the raw material crushed sand S1 charged from the crushed sand input port 60 is supplied to the upper end of the classification surface 3 via the guide plate 61. It is like this.
【0017】又、本体1の上側端面には空気流入室5内
に開口するように空気取入口70が形成されている。こ
の空気取入口70の先方上方には、風向調整板71が設
けられ、この風向調整板71により空気流入室5内に流
入する空気の向きを調整することができるようになって
いる。An air intake 70 is formed on the upper end surface of the main body 1 so as to open into the air inflow chamber 5. An airflow direction adjusting plate 71 is provided above the air intake 70, and the direction of the air flowing into the air inflow chamber 5 can be adjusted by the airflow direction adjusting plate 71.
【0018】前記分級室4には、この分級室4を複数
(実施の形態では2つ)の分級小室4a,4aに仕切る
ように、本体1の上面から概ね垂直真下へ向けて、分級
面3上を移動する砕砂に接触しない程度の範囲で第1バ
ッフルプレート40が垂設されている。この第1バッフ
ルプレート40により仕切られた2つの分級小室4a,
4aには、それぞれ本体1の上面に開口するように排気
口41,41が形成されている。尚、本発明において、
分級室4を複数のバッフルプレートによって2つ以上の
分級小室に仕切るようにしてもよい。The classifying chamber 4 is divided into a plurality (two in the embodiment) of classifying small chambers 4a, 4a so that the classifying chamber 4 is divided into a plurality of classifying chambers 4 from the upper surface of the main body 1 substantially vertically downward. The first baffle plate 40 is vertically installed in such a range that it does not come into contact with the crushed sand moving above. Two classification chambers 4a partitioned by the first baffle plate 40,
Exhaust ports 41, 41 are formed in the upper surface 4a of the main body 1 respectively. In the present invention,
The classification chamber 4 may be divided into two or more classification small chambers by a plurality of baffle plates.
【0019】又、本体1の下端部には砕砂排出室8が形
成され、そして、この砕砂排出室8内に配置されるよう
に、最下段の受板32の先端部に分級面3とは別の網状
体である篩分け網80が下り勾配(水平でもよい)にな
るように取付けられている。尚、この篩分け網80は、
最下段の受板32から延長して、ガイドローラ81によ
り支持された篩フレーム82に取り付けられている。
又、砕砂排出室8の下方には、砕砂取出口9が形成さ
れ、この砕砂取出口9は、篩分け網80の下方部分に形
成されたアンダーサイズ取出口91と、篩分け網80の
先方下方部分に形成されたオーバーサイズ取出口92に
区画されている。従って、分級面3を移動してきた分級
済砕砂は、この分級面3の下端部から篩分け網80の上
に受け渡され、この篩分け網80によって所定の篩目寸
法よりもアンダーサイズの砕砂とオーバーサイズの砕砂
とに篩分けされ、アンダーサイズ砕砂S2は篩分け網8
0を通過して下方のアンダーサイズ取出口91から取り
出され、オーバーサイズ砕砂S3は篩分け網80上を移
行して先方のオーバーサイズ取出口92から取り出され
る。Further, a crushed sand discharge chamber 8 is formed at the lower end of the main body 1, and the classification surface 3 is provided at the tip of the lowermost receiving plate 32 so as to be arranged in the crushed sand discharge chamber 8. Another mesh-like body, a sieving net 80, is attached so as to have a downward slope (may be horizontal). In addition, this sieving net 80 is
It extends from the lowermost receiving plate 32 and is attached to a sieve frame 82 supported by guide rollers 81.
A crushed sand outlet 9 is formed below the crushed sand discharge chamber 8. The crushed sand outlet 9 is an undersize outlet 91 formed at a lower portion of the sieving net 80 and the end of the sieving net 80. It is partitioned into an oversize outlet 92 formed in the lower portion. Therefore, the classified crushed sand that has moved on the classification surface 3 is transferred from the lower end portion of the classification surface 3 onto the sieving net 80, and the sieving net 80 causes the crushed sand to have an undersize smaller than the predetermined mesh size. And the oversized crushed sand are sieved, and the undersized crushed sand S2 is sieved 8
After passing through 0, the oversized crushed sand S3 is taken out from the lower undersize outlet 91, moves over the sieving net 80, and is taken out from the former oversize outlet 92.
【0020】又、前記砕砂排出室8と分級室4との境部
分に、本体1の上面から概ね垂直真下へ向けて、分級面
3上を移動する砕砂に接触しない程度の範囲で第2バッ
フルプレート85が垂設されている。At the boundary between the crushed sand discharge chamber 8 and the classification chamber 4, a second baffle is provided in a range from the upper surface of the main body 1 to a position right below the crushed sand, which does not come into contact with the crushed sand moving on the classification surface 3. The plate 85 is vertically installed.
【0021】尚、前記第1バッフルプレート40及び第
2バッフルプレート85の下端には、砕砂投入口60側
へ概ね45°の角度で屈曲させた屈曲部42,86が形
成されている。At the lower ends of the first baffle plate 40 and the second baffle plate 85, bent portions 42, 86 bent at an angle of about 45 ° toward the crushed sand inlet 60 are formed.
【0022】次に、この砕砂微粉分級機の作用を説明す
る。砕砂投入口60から投入された原料砕砂S1は、ガ
イド板61を経て分級面3の上端部に供給され、加振機
2による振動で分級面3上を上から下に向けて移動す
る。Next, the operation of this crushed sand fine powder classifier will be described. The raw material crushed sand S1 charged from the crushed sand charging port 60 is supplied to the upper end portion of the classification surface 3 via the guide plate 61, and is moved from the top to the bottom on the classification surface 3 by the vibration of the vibrator 2.
【0023】この分級面3上での移動に際し、各受板3
0の先端部から砕砂の移動方向に延長して網状体32が
設けられているため、分級面3を移動する砕砂を、受板
30上から引き続き網状体32の上に移動させて、この
受板30及び網状体32の上でほぐしながら満遍なく分
散させることができる。そして、空気流入室5内には送
風機によって空気取入口70から空気が供給され、この
空気が各受板30,30間に形成した空気流入路31を
経て分級室4に吹き出される。このとき、空気流入路3
1が網状体32の下方に開口して分級室4に連通してい
るため、空気流入路31から吹き出される空気が網状体
32の下方から分級室4内に向けて吹き付けられる。こ
のように、網状体32の上で分散している砕砂に対して
下方から空気が吹き付けられるため、砕砂に含まれてい
る微粉等を分級室4内で効率よく吹き飛ばすことがで
き、効率のよい分級ができる。When moving on the classification surface 3, each receiving plate 3
Since the net-like body 32 is provided extending from the tip end of 0 in the moving direction of the crushed sand, the crushed sand moving on the classification surface 3 is continuously moved from the receiving plate 30 onto the net-like body 32, and It can be evenly dispersed while being loosened on the plate 30 and the mesh 32. Then, air is supplied from the air intake port 70 into the air inflow chamber 5 by the blower, and this air is blown out into the classification chamber 4 through the air inflow passage 31 formed between the receiving plates 30 and 30. At this time, the air inflow path 3
Since 1 is opened below the mesh body 32 and communicates with the classification chamber 4, the air blown out from the air inflow path 31 is blown toward the inside of the classification chamber 4 from below the mesh body 32. In this way, since air is blown from below against the crushed sand dispersed on the mesh body 32, the fine powder and the like contained in the crushed sand can be efficiently blown off in the classification chamber 4, resulting in high efficiency. Can classify.
【0024】この場合、前記受板30,30間に形成さ
れた各空気流入路31の間には、それぞれ段差が生じて
いるため、そこから分級室4へ流入する気流は、それぞ
れが多少ずつ干渉しあい、この結果、気流に乱れが生
じ、分級効率の低下につながるという問題がある。ま
た、分級室の容積が大きければ大きいほど気流そのもの
の拡散乱流が増え、吸入用の集塵機や、空気供給用の送
風機の圧力損失を増大させるという問題もある。In this case, since there is a step between the air inflow passages 31 formed between the receiving plates 30 and 30, the airflows flowing into the classification chamber 4 from there are slightly different. These interfere with each other, and as a result, turbulence occurs in the airflow, leading to a reduction in classification efficiency. There is also a problem that the larger the volume of the classification chamber is, the more the diffusion turbulence of the air flow itself is increased, and the pressure loss of the dust collector for suction and the blower for air supply is increased.
【0025】上記の問題に対し、この実施の形態のよう
に、分級室4に第1バッフルプレート40を設けると、
干渉しあう気流の数を制限することができるし、また、
第1バッフルプレート40によって分級室4を複数の分
級小室4a,4aに仕切ることができるため、気流の拡
散乱流を防ぐことができ、これにより効率の良い空気循
環が行われ、分級効率も向上する。また、各分級小室4
aごとに排気口41が形成されているため、排気口41
ごとの空気流量の調節が比較的容易となり、設備の実際
の施工・調整に有利となる。To solve the above problem, when the first baffle plate 40 is provided in the classification chamber 4 as in this embodiment,
You can limit the number of interfering airflows,
Since the classifying chamber 4 can be partitioned into a plurality of classifying small chambers 4a, 4a by the first baffle plate 40, diffusion turbulence of the air flow can be prevented, which allows efficient air circulation and improves classification efficiency. To do. In addition, each classification small room 4
Since the exhaust port 41 is formed for each a, the exhaust port 41
It is relatively easy to adjust the air flow rate for each unit, which is advantageous for the actual construction and adjustment of equipment.
【0026】又、分級室4と砕砂排出室8との境にも第
2バッフルプレート85を設けていることから気流は砕
砂排出室8へ向かわず、第2バッフルプレート85で跳
ね返り、排気口41へと向かう。更に、気流が一旦、第
2バッフルプレート85で跳ね返ることにより、気流の
中に多少大きめの砕砂の粒が混入していても、その粒は
第2バッフルプレート85に接触して分級面3に落下す
ることから、粒が排気口41に到達することを抑えるこ
とができ、一層、分級効率を向上させることができる。Further, since the second baffle plate 85 is also provided at the boundary between the classification chamber 4 and the crushed sand discharge chamber 8, the air flow does not go to the crushed sand discharge chamber 8 but bounces off at the second baffle plate 85 and the exhaust port 41 Head to. Furthermore, once the airflow bounces off the second baffle plate 85, even if a slightly larger particle of crushed sand is mixed in the airflow, the particle contacts the second baffle plate 85 and falls onto the classification surface 3. As a result, the particles can be prevented from reaching the exhaust port 41, and the classification efficiency can be further improved.
【0027】更に、第1バッフルプレート40及び第2
バッフルプレート85の下端は、砕砂の移動に差し支え
ない程度に分級面3の近くにあることから、砕砂取出口
9等の空気流入路以外の部分から空気が流入するのを制
限することができるので、理想に近い状態で空気流入路
31から進入して排気口41から出て行くように気流が
整う。このことは空気流入路31から進入する空気がよ
り効果的に砕砂を拡散させ、微粉を空中に飛散させる効
果がある。Further, the first baffle plate 40 and the second baffle plate 40
Since the lower end of the baffle plate 85 is close to the classification surface 3 to the extent that it does not interfere with the movement of the crushed sand, it is possible to restrict the inflow of air from a portion other than the air inflow path, such as the crushed sand outlet 9. The airflow is adjusted so that it enters from the air inflow path 31 and exits from the exhaust port 41 in a state close to the ideal. This has the effect that the air entering from the air inflow passage 31 more effectively diffuses the crushed sand and scatters fine powder into the air.
【0028】また、第1バッフルプレート40及び第2
バッフルプレート85の下端には、屈曲部42,86が
形成されているため、より円滑な気流を形成させること
ができ、更に乱流を防ぐことができる。The first baffle plate 40 and the second baffle plate 40
Since the bent portions 42 and 86 are formed at the lower end of the baffle plate 85, a smoother airflow can be formed and turbulence can be further prevented.
【0029】そして、上述のようにして分級室4内に吹
き飛ばされた微粉等S4は、空気とともに排気口41か
らバクフイルタ等の集塵機(図示せず)に収集されて堆
積回収される。又、微粉等を取り除いた分級済砕砂は、
分級面3の下端部から篩分け網80の上に受け渡され、
この篩分け網80によって所定の篩目寸法よりもアンダ
ーサイズの砕砂とオーバーサイズの砕砂とに篩分けさ
れ、アンダーサイズ砕砂S2は篩分け網80を通過して
下方のアンダーサイズ取出口91から取り出され、オー
バーサイズ砕砂S3は篩分け網80上を移行して先方の
オーバーサイズ取出口92から取り出され、これによ
り、所定の篩目寸法以下の砕砂中に、オーバーサイズ砕
砂S3が混入するのを防止することができる。The fine powder S4 blown into the classifying chamber 4 as described above is collected together with air from the exhaust port 41 to a dust collector (not shown) such as a bag filter to be collected and collected. Also, the classified crushed sand from which fine powder etc. have been removed is
From the lower end of the classification surface 3 is transferred onto the sieving net 80,
The sieving net 80 screens crushed sand of undersize and oversize crushed sand smaller than a predetermined mesh size, and the undersize crushed sand S2 passes through the sieving net 80 and is taken out from an undersize outlet 91 below. Then, the oversized crushed sand S3 moves on the sieving net 80 and is taken out from the oversize unloading port 92 of the other side, whereby the oversized crushed sand S3 is prevented from being mixed into the crushed sand having a predetermined mesh size or less. Can be prevented.
【0030】[0030]
【発明の効果】以上説明してきたように、本発明の砕砂
微粉分級機にあっては、砕砂を受板及び網状体の上でほ
ぐしながら満遍なく分散させた上で、空気流入路から吹
き出される空気を網状体の下方から分級室内に向けて吹
き付けることができる。このように、網状体の上で分散
している砕砂に対して下方から空気を吹き付けるため、
砕砂に含まれている微粉等を分級室内で効率よく吹き飛
ばすことができ、高効率の分級ができる。As described above, in the crushed sand fine powder classifier of the present invention, the crushed sand is evenly dispersed while being unraveled on the receiving plate and the mesh body, and then blown out from the air inflow path. Air can be blown into the classification chamber from below the mesh. In this way, to blow air from below against the crushed sand dispersed on the mesh,
The fine powder contained in the crushed sand can be efficiently blown out in the classification chamber, and the classification can be performed with high efficiency.
【0031】また、最下段の受板の先端部に、分級面と
は別の網状体である篩分け網が取付けられているため
(請求項1)、砕砂に含まれる微粉等の除去を主目的と
しながら、同時にオーバーサイズの除去ができる篩い分
け機能が付加された砕砂微粉分級機となり、これによ
り、篩い分け機と分級機の設備を別々に設けた場合に比
べて、大幅に設備の経済負担の軽減及び作業能率の向上
を図ることができる。Further, since a sieving net, which is a reticulated body different from the classification surface, is attached to the tip of the bottom receiving plate (Claim 1), removal of fine powder contained in the crushed sand is mainly performed. Although it is a purpose, it becomes a crushed sand fine powder classifier with a sieving function that can remove oversize at the same time, which greatly reduces the equipment cost compared to the case where the sieving machine and classifier equipment are provided separately. The burden can be reduced and the work efficiency can be improved.
【0032】また、分級室を複数の分級小室に仕切るよ
うにバッフルプレートを垂設したので(請求項2)、干
渉しあう気流の数を制限することができるし、また、気
流の拡散乱流を防ぐことができ、これにより効率の良い
空気循環が行われ、分級効率も向上する。また、各分級
小室ごとに排気口が形成されているため、排気口ごとに
空気流量の調節が比較的容易となり、設備の実際の施工
・調整に有利となる。Further, since the baffle plate is vertically installed so as to divide the classification chamber into a plurality of classification small chambers (Claim 2), the number of interfering airflows can be limited, and the diffusion turbulence of the airflows can be limited. Can be prevented, which enables efficient air circulation and improves classification efficiency. Further, since the exhaust port is formed for each classifying small chamber, it becomes relatively easy to adjust the air flow rate for each exhaust port, which is advantageous for the actual construction and adjustment of the equipment.
【0033】又、分級室と砕砂排出室との境にもバッフ
ルプレートを設けているので(請求項3)、気流がバッ
フルプレートで跳ね返り、微粉等を排気口へと導くこと
ができるし、気流の中に多少大きめの砕砂の粒が混入し
ていても、その粒をバッフルプレートによって分級面に
落下させることができ、粒が排気口に到達することを抑
えて、一層、分級効率を向上させることができる。Further, since a baffle plate is also provided at the boundary between the classification chamber and the crushed sand discharge chamber (claim 3), the air flow bounces off the baffle plate, and fine powder and the like can be guided to the exhaust port. Even if a little larger particles of crushed sand are mixed in, the particles can be dropped to the classification surface by the baffle plate, suppressing the particles from reaching the exhaust port and further improving the classification efficiency. be able to.
【0034】更に、バッフルプレートの下端は、砕砂の
移動に差し支えない程度に分級面の近くにあることか
ら、砕砂取出口等の空気流入路以外の部分から空気が流
入するのを制限することができ、理想に近い状態で空気
流入路から進入して排気口から出て行くように気流を整
流させることができ、これにより空気流入路から進入す
る空気で効果的に砕砂を拡散させ、微粉を空中に飛散さ
せることができる。Further, since the lower end of the baffle plate is near the classification surface to the extent that it does not interfere with the movement of the crushed sand, it is possible to restrict the inflow of air from a portion other than the air inflow path such as the crushed sand outlet. The airflow can be rectified so that it enters from the air inflow path and exits from the exhaust port in a state close to ideal, which effectively diffuses the crushed sand with the air entering from the air inflow path to generate fine powder. Can be scattered in the air.
【0035】また、第1バッフルプレート及び第2バッ
フルプレートの下端には、屈曲部が形成されているため
(請求項5)、より円滑な気流を形成させることがで
き、更に乱流を防ぐことができる。Further, since the bent portions are formed at the lower ends of the first baffle plate and the second baffle plate (claim 5), a smoother air flow can be formed and turbulent flow can be prevented. You can
【図1】本発明の実施の第1形態である砕砂微粉分級機
の断面図である。FIG. 1 is a sectional view of a crushed sand fine powder classifier that is a first embodiment of the present invention.
1 本体 2 加振機 3 分級面 30 受板 31 空気流入路 32 受板 32 網状体 4 分級室 4a 分級小室 40 第1バッフルプレート 41 排気口 42 屈曲部 5 空気流入室 60 砕砂投入口 61 ガイド板 70 空気取入口 71 風向調整板 8 砕砂排出室 80 篩分け網 81 ガイドローラ 82 篩フレーム 85 第2バッフルプレート 86 屈曲部 9 砕砂取出口 91 アンダーサイズ取出口 92 オーバーサイズ取出口 S1 原料砕砂 S2 アンダーサイズ砕砂 S3 オーバーサイズ砕砂 S4 微粉等 1 body 2 shaker 3 classification plane 30 support plate 31 Air inflow path 32 support plate 32 mesh 4 classification room 4a Classroom 40 First Baffle Plate 41 Exhaust port 42 Bend 5 Air inflow chamber 60 Crushed sand input port 61 Guide plate 70 Air intake 71 Wind direction adjustment plate 8 Crushed sand discharge chamber 80 sieving mesh 81 Guide roller 82 sieve frame 85 Second Baffle Plate 86 Bend 9 Crushed sand outlet 91 Undersize outlet 92 Oversize outlet S1 raw material crushed sand S2 undersize crushed sand S3 Oversized crushed sand S4 fine powder, etc.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 團 健一郎 佐賀県武雄市朝日町大字甘久2246番地の1 株式会社中山鉄工所内 (72)発明者 井上 伸介 佐賀県武雄市朝日町大字甘久2246番地の1 株式会社中山鉄工所内 Fターム(参考) 4D021 AA03 CA03 EB01 FA09 GA02 GA13 GA17 GB01 GB02 HA01 ─────────────────────────────────────────────────── ─── Continued front page (72) Inventor Kenichiro Dan 1 of 2246, Amaku, Asahi-cho, Takeo-shi, Saga Nakayama Iron Works Co., Ltd. (72) Inventor Shinsuke Inoue 1 of 2246, Amaku, Asahi-cho, Takeo-shi, Saga Nakayama Iron Works Co., Ltd. F-term (reference) 4D021 AA03 CA03 EB01 FA09 GA02 GA13 GA17 GB01 GB02 HA01
Claims (5)
振動を与える加振手段と、 本体内部に複数の受板を階段状に配設して、砕砂を上段
から下段へ向けて移動させるように形成された分級面
と、 分級面の上端部に原料砕砂を供給するように本体の一端
部に形成された砕砂投入口と、 分級面の下端部から分級済砕砂を取り出すように本体の
他端部に形成された砕砂排出室及びこの砕砂排出室の下
方に開口するように本体に形成された砕砂取出口と、 分級面の上面側に形成された分級室及びこの分級室の上
方に開口するように本体に形成された排気口と、 分級面の下面側に形成された空気流入室及びこの空気流
入室内に開口するように本体に形成された空気取り入れ
口と、 前記各受板の先端部から砕砂の移動方向に延長して設け
られた網状体と、 空気流入室から網状体の下方に開口して分級室に連通す
るように各受板間に形成されている空気流入路とを備え
ている砕砂微粉分級機において、 砕砂排出室内に配置されるように、最下段の受板の先端
部に分級面とは別の網状体である篩分け網が水平若しく
は下り勾配になるように取付けられ、 前記砕砂取出口が、篩分け網の下方部分に形成されたア
ンダーサイズ取出口と、篩分け網の先方下方部分に形成
されたオーバーサイズ取出口に区画されていることを特
徴とする砕砂微粉分級機。1. A vibrating means for vibrating a main body elastically supported by a spring, and a plurality of receiving plates arranged stepwise inside the main body so as to move crushed sand from an upper stage to a lower stage. The classified surface, the crushed sand inlet formed at one end of the main body to supply the raw crushed sand to the upper end of the classified surface, and the other end of the main body to take out the classified crushed sand from the lower end of the classified surface. The crushed sand discharge chamber formed on the main body, the crushed sand discharge port formed on the main body so as to open below the crushed sand discharge chamber, the classification chamber formed on the upper side of the classification surface, and the opening above the classification chamber. The exhaust port formed in the main body, the air inlet chamber formed on the lower surface side of the classification surface and the air intake port formed in the main body so as to open into the air inlet chamber, and from the tip of each receiving plate. Reticulate body extended in the moving direction of crushed sand In the crushed sand fine powder classifier, the crushed sand fine powder classifier is provided with an air inflow path formed between the receiving plates so as to open from the air inflow chamber to below the mesh and communicate with the classification chamber. As described above, a sieving net, which is a reticulated body different from the classification surface, is attached to the tip of the lowermost receiving plate so as to be horizontal or have a downward slope, and the crushed sand extraction port is a lower part of the sieving net. The crushed sand fine powder classifier is characterized in that it is divided into an undersize outlet formed in the above and an oversize outlet formed in the front lower portion of the sieving net.
て、 分級室を複数の分級小室に仕切るように、本体上面から
概ね垂直真下へ向けて、分級面上を移動する砕砂に接触
しない程度の範囲でバッフルプレートが垂設されると共
に、各分級小室にそれぞれ排気口が形成されている砕砂
微粉分級機。2. The crushed sand fine powder classifier according to claim 1, wherein the classifying chamber is divided into a plurality of classifying small chambers so that it does not come into contact with the crushed sand moving on the classifying surface substantially vertically downward from the upper surface of the main body. A crushed sand fine powder classifier in which a baffle plate is hung vertically within the range and an exhaust port is formed in each class chamber.
て、 分級室と砕砂排出室との境部分に、本体上面から概ね垂
直真下へ向けて、分級面上を移動する砕砂に接触しない
程度の範囲でバッフルプレートが垂設されている砕砂微
粉分級機。3. The crushed sand fine powder classifier according to claim 1, wherein a boundary portion between the classification chamber and the crushed sand discharge chamber is positioned so that it does not come into contact with crushed sand moving on the classification surface substantially vertically downward from the upper surface of the main body. A crushed sand fine powder classifier with baffle plates installed vertically in the range.
て、 分級室を複数の分級小室に仕切るように、本体上面から
概ね垂直真下へ向けて、分級面上を移動する砕砂に接触
しない程度の範囲でバッフルプレートが垂設されると共
に、各分級小室にそれぞれ排気口が形成され、 前記分級室と砕砂排出室との境部分に、本体上面から概
ね垂直真下へ向けて、分級面上を移動する砕砂に接触し
ない程度の範囲でバッフルプレートが垂設されている砕
砂微粉分級機。4. The crushed sand fine powder classifier according to claim 1, wherein the classifying chamber is divided into a plurality of classifying small chambers so as not to come into contact with the crushed sand moving on the classifying surface substantially vertically downward from the upper surface of the main body. A baffle plate is vertically installed within the range, and an exhaust port is formed in each classifying chamber, and it moves on the classifying surface from the upper surface of the main body to a position almost vertically right below the boundary between the classifying chamber and the sand crushing chamber. The crushed sand fine powder classifier has a baffle plate installed to the extent that it does not come into contact with the crushed sand.
砂微粉分級機において、バッフルプレートの下端が、砕
砂投入口側へ垂直から概ね水平の範囲で屈曲している砕
砂微粉分級機。5. The crushed sand fine powder classifier according to claim 2, wherein a lower end of the baffle plate is bent in a range from a vertical direction to a crushed sand inlet side in a substantially horizontal direction. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001244705A JP3560574B2 (en) | 2001-08-10 | 2001-08-10 | Crushed sand fine powder classifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001244705A JP3560574B2 (en) | 2001-08-10 | 2001-08-10 | Crushed sand fine powder classifier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2003053269A true JP2003053269A (en) | 2003-02-25 |
| JP3560574B2 JP3560574B2 (en) | 2004-09-02 |
Family
ID=19074595
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001244705A Expired - Fee Related JP3560574B2 (en) | 2001-08-10 | 2001-08-10 | Crushed sand fine powder classifier |
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| CN112933829A (en) * | 2021-01-29 | 2021-06-11 | 山东交通学院 | Dust collector among aggregate screening process |
| CN114669353A (en) * | 2022-03-25 | 2022-06-28 | 柞水县宝华矿业有限公司 | Processing method of barite powder |
| CN116328929A (en) * | 2023-04-17 | 2023-06-27 | 华能煤炭技术研究有限公司 | A fluidized reverse screening device and method for fine particle classification |
| CN116618295A (en) * | 2023-06-01 | 2023-08-22 | 金路(唐山)智能装备有限公司 | Belt conveyor with fine sand recovery |
| CN116944016A (en) * | 2023-09-12 | 2023-10-27 | 韶关核力重工机械有限公司 | Screening type belt feeding machine |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49106054A (en) * | 1973-02-14 | 1974-10-08 | ||
| JPS6142380A (en) * | 1984-08-02 | 1986-02-28 | 長谷 輝美 | Dry type sorter |
-
2001
- 2001-08-10 JP JP2001244705A patent/JP3560574B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49106054A (en) * | 1973-02-14 | 1974-10-08 | ||
| JPS6142380A (en) * | 1984-08-02 | 1986-02-28 | 長谷 輝美 | Dry type sorter |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018119980A1 (en) * | 2016-12-30 | 2018-07-05 | 佛山市多悦贸易有限公司 | Novel sand making machine |
| CN112933829A (en) * | 2021-01-29 | 2021-06-11 | 山东交通学院 | Dust collector among aggregate screening process |
| CN114669353A (en) * | 2022-03-25 | 2022-06-28 | 柞水县宝华矿业有限公司 | Processing method of barite powder |
| CN114669353B (en) * | 2022-03-25 | 2022-12-09 | 柞水县宝华矿业有限公司 | Processing method of barite powder |
| CN116328929A (en) * | 2023-04-17 | 2023-06-27 | 华能煤炭技术研究有限公司 | A fluidized reverse screening device and method for fine particle classification |
| CN116618295A (en) * | 2023-06-01 | 2023-08-22 | 金路(唐山)智能装备有限公司 | Belt conveyor with fine sand recovery |
| CN116618295B (en) * | 2023-06-01 | 2023-10-27 | 金路(唐山)智能装备有限公司 | Belt conveyor with fine sand recovery |
| CN116944016A (en) * | 2023-09-12 | 2023-10-27 | 韶关核力重工机械有限公司 | Screening type belt feeding machine |
| CN116944016B (en) * | 2023-09-12 | 2024-04-05 | 韶关核力重工机械有限公司 | Screening type belt feeding machine |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3560574B2 (en) | 2004-09-02 |
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