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JPS606204B2 - Sorting and separation equipment for ceramic raw materials - Google Patents
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JPS606204B2 - Sorting and separation equipment for ceramic raw materials - Google Patents

Sorting and separation equipment for ceramic raw materials

Info

Publication number
JPS606204B2
JPS606204B2 JP3642578A JP3642578A JPS606204B2 JP S606204 B2 JPS606204 B2 JP S606204B2 JP 3642578 A JP3642578 A JP 3642578A JP 3642578 A JP3642578 A JP 3642578A JP S606204 B2 JPS606204 B2 JP S606204B2
Authority
JP
Japan
Prior art keywords
separation chamber
drum
chamber
chute
chambers
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.)
Expired
Application number
JP3642578A
Other languages
Japanese (ja)
Other versions
JPS54127908A (en
Inventor
悦三 鵜飼
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP3642578A priority Critical patent/JPS606204B2/en
Publication of JPS54127908A publication Critical patent/JPS54127908A/en
Publication of JPS606204B2 publication Critical patent/JPS606204B2/en
Expired legal-status Critical Current

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  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)

Description

【発明の詳細な説明】 本発明は泥濁状態とした窯業原料から蓬砂等の粗粒物と
キラ(徴砂廃棄物)等の微粒物とを選別すると共に*占
士を含んだ胸±水のような泥液を分離する装置に関する
DETAILED DESCRIPTION OF THE INVENTION The present invention separates coarse grains such as mint sand and fine grains such as Kira (sand waste) from muddy ceramic raw materials, and The present invention relates to a device for separating mud liquid such as water.

従来、泥濁状窯業原料から珪砂、キラ、陶土水を分離す
るには夫々独立した装置が必要であってその設備に多額
な費用を要し、またドラックベルトのような水槽中で使
用するものについてはその保守が困難な欠点があった。
Conventionally, in order to separate silica sand, Kira, and china clay water from muddy ceramic raw materials, separate equipment was required for each, which required a large amount of cost, and equipment that was used in a water tank such as a drag belt. The drawback was that it was difficult to maintain.

そこで本発明はドラムを回転させるだけで珪砂、キラ、
陶土水を一度に分離できる装置を提供するものであり、
以下本発明の図示実施例について説明する。第1図乃至
第3図に示す本例において、1はドラムであり本体フレ
ーム2に装着したローラ8に回転可能に支持されている
。ドラム1の内部は壁板3,・・・・・…・によって5
個の室に縦状に区切りされ、一方側から2個の粗粒物洗
浄室Sb,Sc、第1分離室Sa、第2分離室Ka、微
粒物洗浄室Kbの順となっている。laはドラム1の孔
を密閉させる部材である。夫々の室にはその周壁となる
ドラム1の内周面に多数の掬い部4,・・・・・…・が
周設されている。該掬い部4,・・・・・・・・・はド
ラム1の内周面に並設した孔4a付きリング板4b,4
b間に網状プレート4c,・・・・・・・・・を配議し
て構成されている。またドラム1の外周には所定間隔毎
に突出片5,・・・・・・・・・を溶接して一巡設けて
ありガイドフレーム6でカバーされている。Mはモータ
であって本体フレーム2に固定され、突出片5と係脱す
るチェン7に駆動してドラム1を回転させるのである。
R群は減速モータ、プーリ、ガイドローラである。9は
洗浄室Sb、Sc及び第1分離室Saに配置したシュー
トであり、夫々その上部9aを広くして上端を夫々室S
a,Sb,Scの上部に開□させると共に該シュート9
,………を傾斜させて壁板3の中央孔3aから隣接した
洗浄室Sbの下部にシュート9の下端排出口9bを臨ま
せている。
Therefore, the present invention can remove silica sand by simply rotating the drum.
It provides a device that can separate china clay water at once.
DESCRIPTION OF THE PREFERRED EMBODIMENTS Illustrated embodiments of the invention will be described below. In this example shown in FIGS. 1 to 3, 1 is a drum, which is rotatably supported by a roller 8 attached to a main body frame 2. In the example shown in FIGS. The inside of drum 1 is 5 by wall plate 3,...
The chamber is vertically divided into separate chambers, and the order from one side is two coarse particle washing chambers Sb and Sc, a first separation chamber Sa, a second separation chamber Ka, and a fine particle washing chamber Kb. la is a member that seals the hole in the drum 1; A large number of scooping parts 4, . The scooping parts 4, . . . are ring plates 4b, 4 with holes 4a arranged in parallel on the inner peripheral surface of the drum 1.
It is constructed by disposing mesh plates 4c, . . . between b. Further, on the outer periphery of the drum 1, welded protrusions 5, . Reference numeral M designates a motor which is fixed to the main body frame 2 and rotates the drum 1 by driving a chain 7 that engages and disengages from the projecting piece 5.
The R group includes a deceleration motor, a pulley, and a guide roller. Reference numeral 9 denotes a chute arranged in the cleaning chambers Sb, Sc and the first separation chamber Sa, and the upper part 9a thereof is widened, and the upper end is connected to the chamber S, respectively.
Open □ at the top of a, Sb, Sc and the chute 9
, . . . are inclined so that the lower end discharge port 9b of the chute 9 faces from the center hole 3a of the wall plate 3 to the lower part of the adjacent cleaning chamber Sb.

但し一外側の洗浄室Scのシュート9はその排出口9b
′をドラム1の外に関口させている。また第1分離室S
aには泥状原料を供給する供給管18が導入されている
。11はシュート9の上部9aから下方に懐斜状で固定
した傾斜板である。
However, the chute 9 of the outer cleaning chamber Sc is its outlet 9b.
' is connected to the outside of drum 1. Also, the first separation chamber S
A supply pipe 18 for supplying slurry raw material is introduced into a. Reference numeral 11 denotes an inclined plate fixed downward from the upper part 9a of the chute 9 in the form of a slant.

12は第2分離室Kaと微粒物洗浄室Kbに配置した振
動コンベヤであって両側に案内板12aを設けると共に
その排出端を中央孔3aを介して隣接する微粒物洗浄室
Kbの下部に臨ませている。
Reference numeral 12 denotes a vibrating conveyor placed in the second separation chamber Ka and the particulate cleaning chamber Kb, which is provided with guide plates 12a on both sides and whose discharge end faces the lower part of the adjacent particulate cleaning chamber Kb through the central hole 3a. I'm letting you do it.

但し最外側の洗浄室Kbのコンベヤ翼2′の排出ロー2
bをドラム1の外に配置させている。13はコンベヤ亀
2の案内板12aから下方に傾斜させて備えた傾斜板で
ある。
However, the discharge row 2 of the conveyor blade 2' of the outermost cleaning chamber Kb
b is placed outside the drum 1. Reference numeral 13 denotes an inclined plate that is inclined downward from the guide plate 12a of the conveyor turtle 2.

14は送水管であり、ドラム1の両外側の洗浄室Sc,
Kbに配置したシュート9及びコンベヤ12を除いた他
のシュート9及びコンベヤ12の上端に放水できるよう
配管されている。
14 is a water pipe, and cleaning chambers Sc on both sides of the drum 1,
Piping is provided so that water can be sprayed onto the upper ends of the chutes 9 and conveyors 12 other than the chute 9 and conveyor 12 placed in Kb.

なおシュート9、コンベヤ12及び送水管14はフレー
ム2に固定されておりドラムーと一体に回転しない。ま
た15a,15b,16は夫々粗粒物洗浄室Sc,Sb
「微粒物洗浄室Kbのオーバーフローした泥液を集める
採集管であり、原料を泥状とするための水として利用し
ている。17は微粒物を除いた泥液の排出管である。
Note that the chute 9, conveyor 12, and water pipe 14 are fixed to the frame 2 and do not rotate together with the drum. Further, 15a, 15b, 16 are coarse particle cleaning chambers Sc, Sb, respectively.
``This is a collection pipe that collects the overflowing slurry from the particulate cleaning chamber Kb, and is used as water for turning raw materials into slurry.17 is a discharge pipe for the slurry from which particulates have been removed.

次に本例装置を使用するに際しては、まず第1分離室S
aへ供給管10から窯業原料を泥状にした泥状原料を一
定の水位Tになるまで供給して槌粒物を沈降させて分級
する。
Next, when using this example device, first the first separation chamber S
A slurry raw material obtained by turning ceramic raw materials into slurry is supplied to a from the supply pipe 10 until a certain water level T is reached, and the mallet grains are settled and classified.

なお邪魔板18を挿入して槌粒物を沈降効果を促進させ
ている。このような状態でモータMを駆動すればチェン
7が減速されてドラム1の突出片5に係合しドラム1を
回転させる。これにより全ての室Sa,Sb,Sc,K
a,Kbの掬い部47 ………も一体に回転するため、
まず第1分離室Saに沈降している粗粒物(以下、本例
では珪砂とする)を掬い部4で掬いあげて上昇する。こ
の際泥水は掬い部4の網目や孔4aから流れ出るため珪
砂の水切りができる。ドラムーの回転につれ掬い部4が
上昇して反転状態になると第2図で示すように掬い上げ
た珪砂がシュート9内に自然落下する。なおシュート9
の外に落下した珪砂は額斜板翼1上に落下して再びいず
れかの掬い部4に落下することになり直接下方に落下す
ることはない。該シュート9内に落下した珪砂は送水管
14からシャワー状に放水される新水によって洗浄され
ながら次の洗浄室Sbに落下する。該洗浄室Sb‘こお
ける動作も同機に掬い部4,………で達砂を掬いあげシ
ュート9に落下させ送水管14からの洗浄水と共にドラ
ム最外側の洗浄室Scに送られる。しかしながら洗浄室
Scではシュート9に洗浄水が放水されないためシュー
ト9の排出口gb′からは洗浄済の珪砂だけが排出され
ることになる。なお洗浄室Sb,Scには洗浄水が溜ま
るため一定量をすぎるとオーバーフローさせて夫々の採
集管15a,………からドラム1の外へ導いて窯業原料
を泥状にするための水として利用している。一方第1分
離室Saでは雛粒物である珪砂が沈降するのみで微粒物
であるキラ(徴砂)は紙士を含んだ泥液中に存在してい
る。したがって壁板3の中央孔3a′から第2分離室K
aにオーバーフローするものは泥液とキラだけとなる。
第2分離室Kaでは比重分離によってキラが沈降し、キ
うを除いた陶土水(粘土分の泥液で脱水して製品用粘土
となるもの)がオーバーフローして排出管17からドラ
ム1の外へ排出されタンク(図示せず)に導かれること
になる。なおフレーム2に取付けた邪魔板19によって
キラの沈降効果を良好にしている。また沈降したキラは
掬い部4,…・・・・・・によって振動コンベヤー2に
落下し、送水管14からの洗浄水によって付着した粘土
分を洗い落しながら最外側の洗浄室Kbに送られるので
ある。洗浄室Kbでは洗浄水と分離されたキラが掬い部
4,・・…・…によりコンベヤ12′上に落下されその
排出端12bからドラム1外に排出されることになる。
なお洗浄室Kbのオーバーフローした泥液は採集管16
からドラム1の外へ導かれて前記と同様にして窯業原料
を泥状にするための水として利用されることになる。こ
のように本例によるとドラムの回転のみで泥状窯業原料
から珪砂、キラ及び陶土水を得ることができることにな
る画期的な効果が得られるのである。またドラム一回転
で数回の珪砂、キラが洗浄ができ得られた珪砂、キラを
再び洗浄する必要はない。本例は上記のように構成した
が本発明においてはこれに限定されず、例えばドラムを
回転させる手段は問わず、またドラム内に区分けする粗
粒物洗浄室及び微粒物洗浄室の数も限定されない。
Note that a baffle plate 18 is inserted to promote the settling effect of the hammer particles. When the motor M is driven in this state, the chain 7 is decelerated and engages the protruding piece 5 of the drum 1 to rotate the drum 1. As a result, all chambers Sa, Sb, Sc, K
Since the scooping parts 47 of a and Kb also rotate together,
First, the coarse particles (hereinafter referred to as silica sand in this example) that have settled in the first separation chamber Sa are scooped up by the scooping section 4 and lifted up. At this time, the muddy water flows out from the mesh of the scooping part 4 and the holes 4a, so that the silica sand can be drained. As the drum rotates, the scooping part 4 rises and becomes inverted, and the scooped silica sand naturally falls into the chute 9 as shown in FIG. Furthermore, shoot 9
The silica sand that falls outside falls onto the forehead swash plate blade 1 and falls again onto one of the scooping parts 4, and does not fall directly downward. The silica sand that has fallen into the chute 9 is washed by fresh water sprayed from the water pipe 14 in the form of a shower, and falls into the next washing chamber Sb. The operation of cleaning the cleaning chamber Sb' is also carried out by the same machine, in which the scooping section 4, . However, in the cleaning chamber Sc, since no cleaning water is discharged into the chute 9, only the cleaned silica sand is discharged from the discharge port gb' of the chute 9. Note that cleaning water accumulates in the cleaning chambers Sb and Sc, so when it exceeds a certain amount, it overflows and is guided out of the drum 1 through the respective collection pipes 15a, . . . and used as water for turning the ceramic raw materials into mud. are doing. On the other hand, in the first separation chamber Sa, only the silica sand, which is a granular material, settles, and the fine granular material, silica sand, is present in the slurry containing the silica. Therefore, from the central hole 3a' of the wall plate 3 to the second separation chamber K.
The only thing that overflows into a is mud and Kira.
In the second separation chamber Ka, the clay settles due to specific gravity separation, and the china clay water (which is dehydrated with clay slurry and becomes product clay) from which the clay is removed overflows from the discharge pipe 17 to the outside of the drum 1. and will be led to a tank (not shown). Note that the baffle plate 19 attached to the frame 2 improves the settling effect of Kira. Further, the sedimented debris falls onto the vibrating conveyor 2 by the scooping section 4, and is sent to the outermost cleaning chamber Kb while washing off the adhering clay with the cleaning water from the water pipe 14. be. In the washing chamber Kb, the waste separated from the washing water is dropped onto the conveyor 12' by the scooping section 4, and is discharged to the outside of the drum 1 from the discharge end 12b.
The overflowing mud from the cleaning chamber Kb is collected in the collection pipe 16.
The water is led out of the drum 1 and used as water for turning ceramic raw materials into slurry in the same manner as described above. As described above, according to this example, an epoch-making effect can be obtained in that silica sand, silica, and china clay water can be obtained from muddy ceramic raw materials simply by rotating the drum. In addition, the silica sand and dirt can be washed several times with one rotation of the drum, and there is no need to wash the obtained silica sand and dirt again. Although this example is configured as described above, the present invention is not limited to this. For example, the means for rotating the drum is not limited, and the number of coarse particle cleaning chambers and fine particle cleaning chambers divided into the drum is also limited. Not done.

さらに掬い部の構成も問わず、キラを送出する送出体も
コンベヤの他シュート等適宜のものが採用できる。要す
るに本発明は回転ドラム内を縦に区分けして適宜教室の
粗粒物洗浄室、第1分離室、第2分離室及び適宜数個の
微粒物洗浄室の順序で設けると共に夫々の室の周壁とな
るドラムの内周壁に多数個の掬い部を周設し、第1分離
室に泥状原料を供給する手段を設け、第1分離室と粗粒
物洗浄室とに夫々上端を関口したシュートを備えて該シ
ュートの排出口を隣接する粗粒物洗浄室に臨ませると共
に一外側の粗粒物洗浄室のシュートの排出口をドラムの
外に配置させ、また第1分離室で沈降した粗粒物を除い
た泥液を第2分離室に導く手段を設け、第2分離室及び
微粒物洗浄室に夫々上端を閉口したコンベヤ等の送出体
を備えて該送出体の排出部を隣接する微粒物洗浄室に臨
ませると共に最外側の微粒物洗浄室の送出体をドラムの
外に配置させ、ドラム両外側の洗浄室に配置したシュー
ト又は送出体を除いた他のシュート又は送出体に給水で
きる送水手段とドラムを回転させる手段を備え、第2分
離室内の微粒物を除いた泥液をドラムの外に導く排出管
を設けて成る窯業原料の選別分離装置である。したがっ
て従来別工程で行なわれていた珪砂等の粗粒物の分級、
キラ等の微粒物の分級、陶土水等の泥液を分離する工程
が一工程でできる効果が大きく、このため設備費用も安
価になること、密閉状態の回転ドラム方式であるため衛
生的であること、ドラム一回転によって同時に数回もの
粗粒物、微粒物の洗浄ができること等の利点も有する画
期的な発明であり、特に窯業原料の選別分離に好適とい
える。
Furthermore, regardless of the configuration of the scooping section, an appropriate delivery body such as a conveyor or chute for sending out the Kira can be adopted. In short, the present invention vertically divides the interior of the rotating drum into a classroom coarse particle cleaning chamber, a first separation chamber, a second separation chamber, and an appropriate number of fine particle cleaning chambers in this order, and the peripheral wall of each chamber. A number of scooping parts are installed around the inner peripheral wall of the drum, a means for supplying slurry raw material to the first separation chamber is provided, and a chute is provided with an entrance at the upper end of the drum to the first separation chamber and the coarse particle cleaning chamber. The outlet of the chute faces the adjacent coarse particle washing chamber, and the outlet of the chute of the outer coarse particle washing chamber is located outside the drum, and the coarse particles settled in the first separation chamber are A means is provided for guiding the slurry from which particulate matter has been removed to a second separation chamber, and a delivery body such as a conveyor having a closed upper end is provided in the second separation chamber and the particulate matter cleaning chamber, and the discharge portions of the delivery bodies are adjacent to each other. In addition to facing the particulate matter washing chamber, the delivery body of the outermost particulate matter washing chamber is placed outside the drum, and water is supplied to other chutes or delivery bodies other than the chutes or delivery bodies placed in the washing chambers on both sides of the drum. This is a sorting and separation apparatus for ceramic raw materials, which is equipped with a water supply means that can rotate the drum, a means for rotating the drum, and a discharge pipe that leads the slurry from which fine particles have been removed from the second separation chamber to the outside of the drum. Therefore, the classification of coarse particles such as silica sand, which was previously done in a separate process,
The process of classifying fine grains such as clay and separating muddy liquids such as china clay water in one step is highly effective, which reduces equipment costs, and is hygienic because it uses a closed rotating drum system. In addition, it is a revolutionary invention that has the advantage of being able to wash coarse particles and fine particles several times at the same time with one rotation of the drum, and is particularly suitable for sorting and separating ceramic raw materials.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明の実施例を示すもので第1図はその縦断正
面図、第2図は第1図におけるA一A断面図、第3図は
第1図におけるB−B断面図である。 1:ドラム、2:フレーム、3:壁板、3a:中央孔、
4:掬い部、9:シュート、9a:上端開ロ部、9b:
排出口、10三原料供給管、12:送出体、12b:排
出口、14:送水管、15a,15b,16:採集管、
17;排出管、Sa:第1分離室、Sb,Sc:相粒物
洗浄室、Ka:第2分離室、Kb:微粒物洗浄室、M:
モータ。 第1図第2図 第3図
The drawings show an embodiment of the present invention, and FIG. 1 is a longitudinal sectional front view thereof, FIG. 2 is a sectional view taken along line A--A in FIG. 1, and FIG. 3 is a sectional view taken along line BB in FIG. 1. 1: Drum, 2: Frame, 3: Wall plate, 3a: Center hole,
4: Scooping part, 9: Chute, 9a: Upper end opening part, 9b:
Discharge port, 10 three raw material supply pipes, 12: Sending body, 12b: Discharge port, 14: Water pipe, 15a, 15b, 16: Collection pipe,
17; Discharge pipe, Sa: first separation chamber, Sb, Sc: phase particle cleaning chamber, Ka: second separation chamber, Kb: fine particle cleaning chamber, M:
motor. Figure 1 Figure 2 Figure 3

Claims (1)

【特許請求の範囲】[Claims] 1 回転ドラム1内に縦に区分けして適宜数室の粗粒物
洗浄室Sb,Sc……第1分離室Sa、第2分離室Ka
及び適宜数個の微粒物洗浄室Kb,……の順序で設ける
と共に夫々の室の周壁となるドラム1の内周壁に多数個
の掬い部4,……を周設し、第1分離室Saに泥状原料
を供給する手段10を設け、第1分離室Saと粗粒物洗
浄室Sb,Sc,……とに夫々上端9a,……を開口し
たシユート9,……の排出口9b,……を隣接する粗粒
物洗浄室Sb,Sc,……に臨ませると共に一外側の粗
粒物洗浄室Scのシユート9の排出口9b′をドラム1
内の外に配置させ、また第1分離室Saで沈降した粗粒
物を除いた泥液を第2分離室Kaに導く手段を設け、第
2分離室Ka及び微粒物洗浄室Kb,……に夫々上端を
開口したコンベヤ等の送出体12を備えて該送出体12
の排出部を隣接する微粒物洗浄室Kb,……に臨ませる
と共に最外側の微粒物洗浄室Kbの送出体12をドラム
1の外に配置させ、ドラム両外側の洗浄室に配置したシ
ユート又は送出体を除いた他のシユート9又は送出体1
2に給水できる送水手段14とドラム1を回転させる手
段を備え、第2分離室内の微粒物を除いた泥液をドラム
1の外に導く排出管17を設けて成る窯業原料の選別分
離装置。
1 The rotary drum 1 is divided vertically into several coarse particle cleaning chambers Sb, Sc...first separation chamber Sa, second separation chamber Ka
and an appropriate number of fine particle washing chambers Kb, . . . are provided in this order, and a large number of scooping portions 4, . A means 10 for supplying muddy raw material is provided to the first separation chamber Sa and the coarse particle washing chambers Sb, Sc, . . . , and discharge ports 9b, . ... facing the adjacent coarse particle cleaning chambers Sb, Sc, ..., and the discharge port 9b' of the chute 9 of the outer coarse particle cleaning chamber Sc to the drum 1.
A means is provided for guiding the slurry from which coarse particles precipitated in the first separation chamber Sa have been removed to a second separation chamber Ka, and the second separation chamber Ka and the fine particle cleaning chamber Kb, . . . The delivery body 12 is provided with a delivery body 12 such as a conveyor having an open upper end at each of the sides.
The discharge part of the particulate matter washing chamber Kb facing the adjacent particulate matter washing chamber Kb, . Other chute 9 or sending body 1 excluding the sending body
This apparatus for sorting and separating ceramic raw materials is equipped with a water supply means 14 capable of supplying water to a second separation chamber, a means for rotating a drum 1, and a discharge pipe 17 for guiding the slurry from which fine particles in a second separation chamber have been removed to the outside of the drum 1.
JP3642578A 1978-03-29 1978-03-29 Sorting and separation equipment for ceramic raw materials Expired JPS606204B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3642578A JPS606204B2 (en) 1978-03-29 1978-03-29 Sorting and separation equipment for ceramic raw materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3642578A JPS606204B2 (en) 1978-03-29 1978-03-29 Sorting and separation equipment for ceramic raw materials

Publications (2)

Publication Number Publication Date
JPS54127908A JPS54127908A (en) 1979-10-04
JPS606204B2 true JPS606204B2 (en) 1985-02-16

Family

ID=12469464

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3642578A Expired JPS606204B2 (en) 1978-03-29 1978-03-29 Sorting and separation equipment for ceramic raw materials

Country Status (1)

Country Link
JP (1) JPS606204B2 (en)

Also Published As

Publication number Publication date
JPS54127908A (en) 1979-10-04

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