JPH03101855A - Pumice treating plant - Google Patents
Pumice treating plantInfo
- Publication number
- JPH03101855A JPH03101855A JP23682789A JP23682789A JPH03101855A JP H03101855 A JPH03101855 A JP H03101855A JP 23682789 A JP23682789 A JP 23682789A JP 23682789 A JP23682789 A JP 23682789A JP H03101855 A JPH03101855 A JP H03101855A
- Authority
- JP
- Japan
- Prior art keywords
- diameter
- pumice
- sand
- heavy sand
- belt conveyor
- 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.)
- Pending
Links
- 239000008262 pumice Substances 0.000 title claims abstract description 36
- 239000004576 sand Substances 0.000 claims abstract description 55
- 239000004575 stone Substances 0.000 claims abstract description 14
- 239000002245 particle Substances 0.000 claims description 22
- 239000000203 mixture Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 19
- 238000004062 sedimentation Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は原石から砂利、砂等を分級し、砂の中に含まれ
る軽石を除去して所定粒径の砂だけを取り出すようにし
た軽石処理プラントに関する。[Detailed Description of the Invention] (Industrial Application Field) The present invention is a pumice stone that classifies gravel, sand, etc. from raw stone, removes pumice contained in the sand, and extracts only sand with a predetermined particle size. Regarding treatment plants.
(従未の技術)
生コンクリートに混入させる砂利や砂を取るプラントで
は、取り出した砂の中に混入している軽石を除去するこ
とが重要である。(Previous technology) In plants that remove gravel and sand to be mixed into fresh concrete, it is important to remove pumice from the sand.
従来の軽石除去装置は流水の中に軽石混じりの砂を落下
させ、軽石の沈降速度と砂の沈降速度との差を利用して
選別するものであった。Conventional pumice removal equipment drops sand mixed with pumice into running water and sorts it out using the difference between the settling speed of pumice and the settling speed of sand.
(発明が解決しようとする課題)
ところが、上記従米公知のプラントによると、軽石と一
緒に比較的小径の砂まで除去してしまうと言う欠点があ
った。特に、生コンクリートに使用される砂においては
、所定範囲(例えば、0 . 1 5 la/w−
6 Ill/II1)の粒径が混合しているものでない
と製品コンクリートの仕上がりの面で好ましくないので
、このような比較的広い範囲の粒径の砂を必要とする。(Problems to be Solved by the Invention) However, the above-mentioned conventional plant has a drawback in that it removes even relatively small diameter sand together with pumice. In particular, the sand used for ready-mixed concrete must be within a certain range (for example, 0.15 la/w-
If the sand does not have a mixture of particle sizes of 6 Ill/II1), the finish of the finished concrete will be unfavorable, so sand with a relatively wide range of particle sizes is required.
(課題を解決するための手段)
本発明の特徴とする構或は、軽石の混入した原石から所
定の粒径以下を選別する受付ホツパーと、該受付ホッパ
ーによって選別された所定粒径以下の原石を大、中、小
の3種類の粒径に選別するトロンメルと、該トロンメル
にって選別された小の粒径の軽石及び重砂の混合物が導
入される第1のフライトセパレータと、該第1のフライ
トセパレータを溢流した所定径の軽石と重砂とが導入さ
れる振動ふるいと、該振動ふるいによって選別された所
定粒径以下の軽石と重砂とが導入される第2のフライト
セパレータと、該第2のフライトセパレータによって沈
澱選別された所定粒径以下の重砂と前記第1のフライト
セパレータによって沈澱選別された所定粒径の重砂とを
搬送するベルトコンベアと、からなることにあり、これ
によって比較的広い粒径範囲の製品砂を得るものである
。(Means for Solving the Problems) A structure characterized by the present invention includes a receiving hopper that sorts out rough stones with a predetermined particle size or less from raw stones mixed with pumice, and a receiving hopper that sorts rough stones with a predetermined particle size or below that are sorted by the receiving hopper. a first flight separator into which a mixture of pumice and heavy sand of small particle size sorted by the trommel is introduced; A vibrating sieve into which pumice and heavy sand of a predetermined diameter that overflowed the first flight separator are introduced, and a second flight separator into which pumice and heavy sand with a predetermined particle size or less that have been sorted by the vibrating sieve are introduced. and a belt conveyor for conveying heavy sand of a predetermined particle size or less that has been precipitated and sorted by the second flight separator and heavy sand of a predetermined particle size that has been precipitated and sorted by the first flight separator. This makes it possible to obtain product sand with a relatively wide particle size range.
(実施例)
以下、添付系統図によって本発明の一実施例を説明する
。(Example) Hereinafter, an example of the present invention will be described with reference to the attached system diagram.
原石Aは1 0 0 to/ +n目のメッシュを有す
る受付ホッパ−1を通され、100Io/]rl径以下
の砂利や砂だけが選別されてベルトコンベア2に給送さ
れる。該ベルトコンベア2は前記選別された砂利や砂を
トロンメル3へ給送するものである。トロンメル3は内
部に50+II/to口と6III/In目のメッシュ
を有しており、砂利を1 0 0 tn/ m径−50
m/m径の大形砂利Bと、5 0 ml +n径〜G
vn / +n径の小形砂利Cとに分級し、更に6 m
/ +n径以下の砂Dを選別するものである。大形砂
利Bはトロンメル3の端部がら落下排出されて山積サれ
、小形砂利Dはベルトコンベア4によって搬送されて山
積される。The rough stone A is passed through a reception hopper 1 having a mesh of 100 to/+nth mesh, and only gravel and sand with a diameter of 100 Io/]rl or less are sorted out and fed to a belt conveyor 2. The belt conveyor 2 feeds the selected gravel and sand to the trommel 3. Trommel 3 has a 50+II/to opening and a 6III/In mesh inside, and carries gravel at 100 tn/m diameter -50
m/m diameter large gravel B and 50 ml +n diameter ~ G
Vn / +n diameter small gravel C and further 6 m
This is to select sand D with a diameter of /+n or less. The large gravel B is discharged from the end of the trommel 3 and is piled up, and the small gravel D is conveyed by the belt conveyor 4 and piled up.
トロンメル3には配管5が設けられ、該配管5によって
水がシャワーされている。この水のシャワーは粉塵を吸
収除去すると同時に、前記選別された砂Dを水流によっ
て第1の7ライト?バレータ6へ搬送するものである。The trommel 3 is provided with a pipe 5 through which water is showered. This shower of water absorbs and removes dust, and at the same time, the sorted sand D is transferred to the first 7 lights by the water flow. It is conveyed to the valet 6.
選別された砂Dは、6 +n / +n径以下の軽石と
6 m / +nれ以下の通常使用される砂(以下、こ
れを重砂という)とが混合した状態となっている。The sorted sand D is a mixture of pumice with a diameter of 6 m/+n or less and commonly used sand (hereinafter referred to as heavy sand) with a diameter of 6 m/+n or less.
第1のフライトセパレータ6は流水中での沈降速度の差
を利用して選別する装置である。即ち、沈澱槽61の内
部に回転自在のドラム6■が配置され、該ドラム62の
左右に沈澱物をドラム6■側へ移送するラセン羽根63
が設けられている。ドラム6■の外周には沈澱物を掬い
上げて排出するパケットが設けられている。The first flight separator 6 is a device that performs sorting using the difference in sedimentation speed in flowing water. That is, a rotatable drum 6 is disposed inside the sedimentation tank 61, and helical blades 63 are provided on the left and right sides of the drum 62 to transfer the sediment to the drum 6.
is provided. A packet for scooping up and discharging sediment is provided on the outer periphery of the drum 6■.
水と一緒に砂Dが沈澱槽6、内へ導入され、該導入水は
沈澱Fff6,を溢れて左右から流出する。今、沈澱槽
61内での導入水の滞留時間を適宜に定めると、比重の
軽い軽石と比重は重いが粒径の小さい重砂とが水と一緒
に溢流する。Sand D is introduced into the settling tank 6 together with water, and the introduced water overflows the settling tank Fff6 and flows out from the left and right sides. Now, if the residence time of the introduced water in the settling tank 61 is set appropriately, pumice with a light specific gravity and heavy sand with a heavy specific gravity but a small particle size will overflow together with the water.
そして、粒径の大きい重砂だけが沈alff6,の底に
沈澱する。実験によると、6 m / +n径以下の軽
石を溢流させると、1n+/ω径以下の重砂が一緒に溢
流することが分かっている。尚、フライトセバレータ6
内への導入水量を調整して選別を制御するために、調整
用のボンブ6Pが設けられでいる。Then, only heavy sand with a large particle size settles to the bottom of the alff6. Experiments have shown that when pumice with a diameter of 6 m/+n or less is overflowed, heavy sand with a diameter of 1n+/ω or less is overflowed together. In addition, Flight Severator 6
In order to control the sorting by adjusting the amount of water introduced into the chamber, an adjustment bomb 6P is provided.
水と一緒に溢流した6 +Il/ m径以下の軽石と1
m/’Ifi径以下の重砂とは1+n/m目のメッシュ
を有する振動ふるい7に導入され、該メンシュにかけら
れて6m/m径〜1llI/1l径の軽石と、1+n/
m径以下の軽石及び重砂とに選別される。6 m /
tn径〜IIff/IIl径の軽石はベルトコンベア8
によって搬送されて山積される。1+o/+n径以下の
軽石と重砂とは第2のフライトセパレータ9へ導入され
る。6 + Il/ pumice with a diameter of less than m and 1
Heavy sand with a diameter of m/'Ifi or less is introduced into a vibrating sieve 7 having a 1+n/m mesh, and is passed through the vibrating sieve to separate pumice with a diameter of 6m/m to 1llI/1l and 1+n/m.
It is sorted into pumice and heavy sand with a diameter of m or less. 6 m/
Pumice with a diameter of tn to IIff/IIl is conveyed by belt conveyor 8.
are transported and piled up. Pumice and heavy sand having a diameter of 1+o/+n are introduced into the second flight separator 9.
$2のフライトセパレータ9は第1のフライトセパレー
タ6と同様な構或となっており、この$2のフライトセ
パレータ9によって1 rn / rn径以下の軽石と
0.15+++/1l径以下の重砂とを溢流させ、1+
n/m径− 0 . 1 5 to/+n径の重砂を
沈澱させる。溢流した1 m / m径以下の軽石と0
.1 5 m/ m径以下の重砂は分級代10にがけら
れ、沈澱したlm/+n径−0.15m/+n径の重砂
はバケットで掬い上げられてベルトコンベア11へ排出
される。尚、9Pはf52のフライトセパレータ9に導
入される水量を調整するための調整用のポンプである。The $2 flight separator 9 has the same structure as the first flight separator 6, and the $2 flight separator 9 separates pumice with a diameter of 1rn/rn or less and heavy sand with a diameter of 0.15+++/1l or less. and overflow, 1+
n/m diameter - 0. 1 5 to/+n diameter heavy sand is precipitated. Overflowing pumice with a diameter of 1 m/m or less and 0
.. 15 m/ Heavy sand with a diameter of 15 m or less is poured into a classification allowance 10, and the precipitated heavy sand with a diameter of lm/+n -0.15 m/+n is scooped up by a bucket and discharged to a belt conveyor 11. Note that 9P is an adjustment pump for adjusting the amount of water introduced into the flight separator 9 of the f52.
第1のフライトセパレータ6に沈澱した6m/IIl径
〜1+a/a+径の重砂はパケットによって掬い上げら
れてベルトコンベア12へ排出され、第2のフライトセ
パレータ9のベルトコンベア11の重砂も同ベルトコン
ベア12へ排出され、それらが該ベルトコンベア12に
て混合されて製品重砂Sとして山積される。ベルトコン
ベア12には必要に応じて洗浄のための水がシャワーさ
れ、混入している0 . 1 5 to/+n径以下
の重砂と一緒に該水を貯蔵槽13に排出貯蔵する。The heavy sand with a diameter of 6m/IIl to 1+a/a+ that has settled on the first flight separator 6 is scooped up by a packet and discharged to the belt conveyor 12, and the heavy sand on the belt conveyor 11 of the second flight separator 9 is also the same. They are discharged to the belt conveyor 12, where they are mixed and piled up as product heavy sand S. The belt conveyor 12 is showered with water for cleaning as needed to remove any mixed 0. The water is discharged and stored in a storage tank 13 together with heavy sand having a diameter of 15 to/+n or less.
該貯蔵Wl13の0 . 1 5 +n/ +n径以
下の重砂ヲホンプ13Pによって前記分級磯10へ導入
させる。0.0 of the storage Wl13. Heavy sand having a diameter of 1 5 +n/ +n or less is introduced into the classified rock 10 by the pump 13P.
分級磯10は1 +n / tI+径以下の軽石と0.
15In / Ill径以下の重砂とを分級除去するも
のであり、この分級m1 0によって選別された1 +
n / +n径以下の軽石と0.15m,/m径以下の
重砂とは排出されて山82される。又、分級成10の排
水は沈澱槽14に導入され、泥分が沈澱除去される。Classified rock 10 is made of pumice with a diameter of 1 + n / tI + or less and 0.
It is used to classify and remove heavy sand with a diameter of 15In/Ill or less, and 1+ selected by this classification m10.
Pumice with a diameter of n/+n or less and heavy sand with a diameter of 0.15 m or less are discharged into a pile 82. Further, the waste water from the classifier 10 is introduced into a settling tank 14, where mud is removed by settling.
該沈澱槽14の上澄水はポンプ14P1によって配管5
を介してトロンメル3にシャワーされ、必要に応じてベ
ルトコンベア12にシャワーされる。沈澱泥はポンプ1
4P2によって汚水処理装置15に送られ、脱水の後、
廃棄処理される。The supernatant water of the settling tank 14 is pumped to the pipe 5 by a pump 14P1.
The water is showered onto the trommel 3 via the trommel 3, and onto the belt conveyor 12 as required. Pump 1 for sedimentation mud
It is sent to the sewage treatment equipment 15 by 4P2, and after dehydration,
Will be disposed of.
以上の説明において、選別粒径は一例であって、必要に
応じて変更できる。例えば、フライトセパレータにる選
別粒径の変更は、調整用のポンプの水量を変更すること
によって行なうものである。又、その他の粒径の変更は
メッシュの目を変更すればよい。In the above description, the sorted particle size is just an example, and can be changed as necessary. For example, the particle size sorted by the flight separator is changed by changing the amount of water in the adjustment pump. Further, other changes in particle size can be made by changing the mesh size.
(発明の効果)
以上に説明した本発明によると、以下に説明するような
効果を奏する。(Effects of the Invention) According to the present invention described above, the following effects are achieved.
原石の中から、軽石だけを除去するものであるから、正
産量のアップとなる。Since only the pumice is removed from the raw stone, the production amount can be increased.
広い範囲の重砂が得られるので、仕上がりのよいコンク
リート製品が得られる。Since a wide range of heavy sand can be obtained, concrete products with a good finish can be obtained.
水が閉鎖サイクルで使用されるものでは、汚水が外部へ
排出されることがなく、クリーンな処理装置となる。When water is used in a closed cycle, wastewater is not discharged to the outside, resulting in a clean treatment device.
調整用ポンプを設けたものでは、沈澱させる粒径の制御
ができるものとなる。If a regulating pump is provided, the particle size to be precipitated can be controlled.
【図面の簡単な説明】
図は本発明の一実施例を示す系統図である。
A:原石 1:受付ホッパー
2:ベルトコンベア 3:トロンメル34:ベルトコン
ベア 5:配管
6:弟1のフライトセパレータ 7:振動ふるり)8:
ベルトコンベア
9:第2のフライトセパレータ 10:分級槻11:ベ
ルトコンベア 12:ベルトコンベア13:貯蔵槽 1
4:沈澱槽
15:汚水処理装置BRIEF DESCRIPTION OF THE DRAWINGS The figure is a system diagram showing an embodiment of the present invention. A: Raw stone 1: Reception hopper 2: Belt conveyor 3: Trommel 34: Belt conveyor 5: Piping 6: Brother 1's flight separator 7: Vibrating) 8:
Belt conveyor 9: Second flight separator 10: Classifier 11: Belt conveyor 12: Belt conveyor 13: Storage tank 1
4: Sedimentation tank 15: Sewage treatment equipment
Claims (1)
ホッパーと、該受付ホッパーによって選別された所定粒
径以下の原石を大、中、小の3種類の粒径に選別するト
ロンメルと、該トロンメルにって選別された小の粒径の
軽石及び重砂の混合物が導入される第1のフライトセパ
レータと、該第1のフライトセパレータを溢流した所定
径の軽石と重砂とが導入される振動ふるいと、該振動ふ
るいによって選別された所定粒径以下の軽石と重砂とが
導入される第2のフライトセパレータと、該第2のフラ
イトセパレータによって沈澱選別された所定粒径以下の
重砂と前記第1のフライトセパレータによって沈澱選別
された所定粒径の重砂とを搬送するベルトコンベアと、
からなることを特徴とする軽石処理プラント。A reception hopper that sorts out rough stones with a predetermined particle size or less from the raw stones mixed with pumice, a trommel that sorts the rough stones with a predetermined particle size or less that are sorted by the reception hopper into three types of particle sizes: large, medium, and small; A first flight separator into which a mixture of pumice and heavy sand of small particle size sorted by a trommel is introduced, and pumice and heavy sand of a predetermined diameter that overflowed the first flight separator are introduced. a second flight separator into which pumice and heavy sand with a predetermined particle size or less that have been sorted by the vibrating sieve are introduced; a belt conveyor that conveys sand and heavy sand of a predetermined particle size that has been precipitated and sorted by the first flight separator;
A pumice processing plant characterized by comprising:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23682789A JPH03101855A (en) | 1989-09-14 | 1989-09-14 | Pumice treating plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23682789A JPH03101855A (en) | 1989-09-14 | 1989-09-14 | Pumice treating plant |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03101855A true JPH03101855A (en) | 1991-04-26 |
Family
ID=17006372
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23682789A Pending JPH03101855A (en) | 1989-09-14 | 1989-09-14 | Pumice treating plant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03101855A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20150026826A (en) * | 2013-09-03 | 2015-03-11 | 씨디이 아시아 리미티드 | System device process for classification of various materials |
-
1989
- 1989-09-14 JP JP23682789A patent/JPH03101855A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20150026826A (en) * | 2013-09-03 | 2015-03-11 | 씨디이 아시아 리미티드 | System device process for classification of various materials |
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