JP2567462B2 - Granular mixture divided take-out method and its mixing processing apparatus - Google Patents

Granular mixture divided take-out method and its mixing processing apparatus

Info

Publication number
JP2567462B2
JP2567462B2 JP63207328A JP20732888A JP2567462B2 JP 2567462 B2 JP2567462 B2 JP 2567462B2 JP 63207328 A JP63207328 A JP 63207328A JP 20732888 A JP20732888 A JP 20732888A JP 2567462 B2 JP2567462 B2 JP 2567462B2
Authority
JP
Japan
Prior art keywords
mixing container
mixing
granular mixture
granular
partition plate
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 - Lifetime
Application number
JP63207328A
Other languages
Japanese (ja)
Other versions
JPH0256228A (en
Inventor
直 宮崎
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.)
Canon Inc
Original Assignee
Canon Inc
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Filing date
Publication date
Application filed by Canon Inc filed Critical Canon Inc
Priority to JP63207328A priority Critical patent/JP2567462B2/en
Publication of JPH0256228A publication Critical patent/JPH0256228A/en
Application granted granted Critical
Publication of JP2567462B2 publication Critical patent/JP2567462B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B1/00Preparing the batches
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/60Mixing solids with solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F29/00Mixers with rotating receptacles
    • B01F29/40Parts or components, e.g. receptacles, feeding or discharging means

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Glass Melting And Manufacturing (AREA)
  • Accessories For Mixers (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、混合機により混合された粒状混合物を、そ
の均質性を損なうことなく分割取出しするための、粒状
混合物の分割取出し方法およびその混合処理装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method of dividing and taking out a granular mixture for dividing and taking out a granular mixture mixed by a mixer without impairing its homogeneity. Regarding a processing device.

(従来の技術及び発明が解決しようとする課題) 従来、混合機にて混合された粒状混合物は、混合後に
充分な均質性を有することがこの粒状混合物の各種用途
において要求されている。
(Problems to be Solved by Conventional Techniques and Inventions) Conventionally, it has been required for various uses of the granular mixture that the particles are mixed in a mixer to have sufficient homogeneity after mixing.

例えば、粒状混合物が粒状の光学ガラス原料(以下、
粒状ガラスと記す)である場合、混合後の粒状ガラスの
均質性が悪いとガラス成形品に脈理を生じ、屈折率等の
光学性能を劣化させる。従って、混合後の粒状ガラスが
完全な均質性を有するよう十分の混合を行ない、且つ混
合後の粒状ガラスの屈折率が目標とするガラスの屈折率
となるよう混合調節をする必要がある。
For example, a granular mixture is a granular optical glass raw material (hereinafter,
In the case of (granular glass)), if the homogeneity of the granular glass after mixing is poor, striae occur in the glass molded product, and the optical performance such as the refractive index is deteriorated. Therefore, it is necessary to perform sufficient mixing so that the granular glass after mixing has complete homogeneity, and to adjust the mixing so that the refractive index of the granular glass after mixing becomes the target refractive index of the glass.

ところで、粒状ガラス等の粒状物質を混合機から取出
すには、従来から混合機の下部に設けられた排出口より
排出するようにしている。しかるに、この排出動作にお
いて、粒状物質が混合機内にて充分の均質性を有するよ
う混合されていても、粒状物質の粒径或は比重等の相違
に起因して、例えば比重の大きい物質が小さい物質より
先に流出して排出されるという、いわゆる比重分離の現
象が生じる。
By the way, in order to take out a granular substance such as granular glass from a mixer, it has been conventionally performed to discharge it through an outlet provided in the lower part of the mixer. However, in this discharging operation, even if the granular materials are mixed so as to have sufficient homogeneity in the mixer, due to the difference in the particle size or the specific gravity of the granular materials, for example, the material having a large specific gravity is small. The phenomenon of so-called specific gravity separation occurs in which the substance flows out and is discharged before it.

ここで、この現象による実験例を説明する。 Here, an experimental example based on this phenomenon will be described.

下表は、粒状ガラス100Kgを混合機下部の排出口から2
0Kgずつ排出したサンプルを溶融して得たガラスの屈折
率の基準値(目的値)からのずれ(Δn)を示すもので
ある。
The table below shows 100 kg of granular glass from the outlet at the bottom of the mixer.
It shows the deviation (Δn) from the reference value (target value) of the refractive index of the glass obtained by melting the sample discharged by 0 kg each.

この表から、粒状ガラスの排出順位が小さくなるほど
比重が小さくなっており、上記したように、比重の大き
い物質から先に排出されることが理解できる。
From this table, it can be understood that the smaller the discharge order of the granular glass, the smaller the specific gravity, and as described above, the substance having the larger specific gravity is discharged first.

混合後の粒状ガラスの屈折率は、粒状ガラスのサンプ
リングから検知した平均値で与えられる。ところが、上
記のように排出時の粒状ガラスに比重分離が生じると、
屈折率の平均値を正確に知ることが不可能となる。
The refractive index of the granular glass after mixing is given by an average value detected from sampling of the granular glass. However, if the specific gravity separation occurs in the granular glass at the time of discharging as described above,
It becomes impossible to know the average value of the refractive index accurately.

本発明は、上記事情に基づいてなされたもので、混合
機により均質化された粒状混合物を、比重分離が生じな
い状態で、所望量で分割取出しができるようにして、各
分割部分の相互の、同じ均質性を確保するようにした粒
状混合物の分割取出し方法およびその混合処理装置を提
供することを目的とする。
The present invention has been made based on the above circumstances, in which a granular mixture homogenized by a mixer can be divided and taken out in a desired amount in a state where specific gravity separation does not occur, so that the divided portions are mutually separated. It is an object of the present invention to provide a method for dividing and taking out a granular mixture that ensures the same homogeneity, and a mixing processing apparatus therefor.

(課題を解決するための手段) このため、本発明では、混合容器内に粒状被混合物を
投入し、前記混合容器を回転することで、前記混合容器
内に均質化された粒状混合物を生成する混合処理におい
て、均質化の後、前記粒状混合物を、前記混合容器内で
の堆積状態のまま、上層側から所要量ずつ分割取出しす
ることを特徴とする。
(Means for Solving the Problems) Therefore, in the present invention, a homogenized granular mixture is produced in the mixing container by introducing the granular mixture into the mixing container and rotating the mixing container. In the mixing process, after homogenization, the granular mixture is divided and taken out in a required amount from the upper layer side in the state of being accumulated in the mixing container.

また、本発明では、混合容器内に粒状被混合物を投入
し、前記混合容器を回転することで、前記混合容器内に
均質化された粒状混合物を生成する混合処理において、
均質化の後、前記粒状混合物を、前記混合容器内での堆
積状態のまま、上下あるいは左右に層状に分割し、その
分割毎に取出しすることを特徴とする。
Further, in the present invention, the granular mixture is put into a mixing container, and by rotating the mixing container, in a mixing process for producing a homogenized granular mixture in the mixing container,
After the homogenization, the granular mixture is divided into upper and lower layers or left and right layers in the state of being accumulated in the mixing container, and each divided layer is taken out.

更に、本発明では、混合容器内に粒状被混合物を投入
し、前記混合容器を回転することで、前記混合容器内に
均質化された粒状混合物を生成する混合処理装置におい
て、前記混合容器には、仕切り板挿入口が設けてあり、
均質化の後、前記粒状混合物を、前記混合容器内での堆
積状態のまま、上下あるいは左右に層状に分割するため
の仕切板を、前記仕切板挿入口から前記混合容器内に挿
入できる構成にすると共に、各分割領域に対応して、前
記混合容器に排出口を装備したことを特徴とする。
Furthermore, in the present invention, in the mixing processing apparatus, the granular mixture is put into a mixing container, and the mixing container is rotated to generate a homogenized granular mixture in the mixing container. , A partition board insertion port is provided,
After the homogenization, the granular mixture, in the state of accumulation in the mixing container, a partition plate for dividing the granular mixture vertically or horizontally into a structure capable of being inserted into the mixing container from the partition plate insertion port. In addition, the mixing container is equipped with a discharge port corresponding to each divided region.

(作用) このような分割処理によれば、混合容器の回転で、均
質化された粒状混合物は、その所望量の分割取出しに際
して、例えば、スコップやバキュームの手段で、堆積状
態のままで取り出され、あるいは、堆積状態のままで各
領域に分割された後、それぞれ、取り出されるのであっ
て、従来のように、流動によって、所望量づつ分割排出
される際に、混合容器内で生じる比重分離(比重の大き
なものから落下する)が起こらないから、分割によって
得られた各取出し分は、ほぼ、同じ比重(分割された各
取出し分の総量の平均比重、それは、例えば、光学ガラ
スの屈折率を定める比重)を維持することができる。
(Operation) According to such a dividing process, the granular mixture homogenized by the rotation of the mixing container is taken out in the accumulated state by means of, for example, a scoop or vacuum when the desired amount of divided mixture is taken out. Alternatively, after being divided into respective regions in the deposited state, they are respectively taken out, and the specific gravity separation that occurs in the mixing container when dividedly discharged by a desired amount by a flow as in the conventional case ( Since the drop from the one with a large specific gravity does not occur, each of the taken out parts obtained by the division has almost the same specific gravity (the average specific gravity of the total amount of the divided taken out parts, which is, for example, the refractive index of the optical glass. The specific gravity can be maintained.

(実施例) 以下、本発明の実施例について図面を参照しながら説
明する。
(Example) Hereinafter, the Example of this invention is described, referring drawings.

第1図は、本発明の第1実施例で用いた混合機の縦断
面図である。
FIG. 1 is a vertical sectional view of a mixer used in the first embodiment of the present invention.

第2図(a)は、本発明の第2実施例で用いた混合機
の被混合物を収容していない状況の縦断面図である。
FIG. 2 (a) is a vertical cross-sectional view of the mixer used in the second embodiment of the present invention in a state where the material to be mixed is not housed.

第2図(b)は、第2図(a)に示した混合機の被混
合物を収容し仕切り板を装着した状況の容器のみの縦断
面図である。
Fig. 2 (b) is a vertical cross-sectional view of only the container in a state where the material to be mixed of the mixer shown in Fig. 2 (a) is accommodated and the partition plate is attached.

第3図(a)は、本発明の第3実施例で用いた混合機
の被混合物を収容していない状況の縦断面図である。
FIG. 3 (a) is a vertical cross-sectional view of the mixer used in the third embodiment of the present invention in a state in which the material to be mixed is not housed.

第3図(b)は、第3図(a)に示した混合機の被混
合物を収容し仕切り板を装着した状況の容器のみの縦断
面図である。
FIG. 3 (b) is a vertical cross-sectional view of only the container in a state where the material to be mixed of the mixer shown in FIG. 3 (a) is accommodated and the partition plate is attached.

第4図(a)は、本発明の第3実施例で用いた混合機
の被混合物を収容していない状況の縦断面図である。
FIG. 4 (a) is a vertical cross-sectional view of the mixer used in the third embodiment of the present invention in a state in which the material to be mixed is not housed.

第4図(b)は、第4図(a)に示した混合機の容器
内に被混合物を収容し仕切り板を装着してこの容器を倒
立状態にした縦断面図である。
FIG. 4 (b) is a vertical cross-sectional view of the container of the mixer shown in FIG. 4 (a) in which the material to be mixed is accommodated and a partition plate is attached to bring the container upside down.

(第1実施例) 第1図において、10はW型混合機であり、この混合機
は、試料投入口12とこの投入口と対象位置に排出口14を
有する混合容器11と、この容器を回転軸13について回転
させる不図示の電動機とを有し、電動機の起動停止はス
イッチ15で行なう構成とされている。
(First Embodiment) In FIG. 1, 10 is a W-type mixer, which comprises a sample inlet 12, a mixing container 11 having this inlet and an outlet 14 at a target position, and this container. An electric motor (not shown) for rotating the rotary shaft 13 is provided, and the switch 15 is used to start and stop the electric motor.

この混合機10を用いて例えば粒状の光学ガラス原料19
を混合するには、混合機10の投入口12から光学ガラス原
料19を100Kg(混合容器11内における充填量が40%と成
る程度)投入し、投入口12を閉塞してから混合機10を約
25分間回転させ、混合を終了する。
Using this mixer 10, for example, a granular optical glass raw material 19
For mixing, 100 kg of optical glass raw material 19 (about 40% of the filling amount in the mixing container 11) is charged from the charging port 12 of the mixer 10, and the charging port 12 is closed, and then the mixer 10 is turned on. about
Spin for 25 minutes to complete mixing.

次に、投入口12を開け、混合されたガラス原料の最上
部から不図示のスコップ或はバキューム等を用いて順次
所定量ごとに層状にガラス原料19を取出す。
Next, the charging port 12 is opened, and the glass raw materials 19 are sequentially taken out in layers in a predetermined amount from the top of the mixed glass raw materials using a scoop, a vacuum or the like (not shown).

このような取出し方法によれば、混合されたガラス原
料19が排出口14に向けて流動することがなく粒状混合物
の流動による比重分離が生じないから、混合後のガラス
原料19の均質性はほぼ一定に保たれる。従って、層状に
取出した各所定量ごとのガラス原料19による成形品の屈
折率はほぼ一定値を有することができる。
According to such a take-out method, the mixed glass raw material 19 does not flow toward the discharge port 14 and specific gravity separation due to the flow of the granular mixture does not occur, so that the homogeneity of the glass raw material 19 after mixing is almost equal. Is kept constant. Therefore, the refractive index of the molded product of the glass raw material 19 taken out in layers for each predetermined amount can have a substantially constant value.

又、本実施例によれば、混合されたガラス原料全体の
均質性を失うことがないため、例えば最上層から一定量
をサンプリングして作った成形品の屈折率を代表値と
し、この代表値を上記ガラス原料の屈折率の平均値とし
て用いることができる。
Further, according to the present example, since the homogeneity of the entire mixed glass raw material is not lost, for example, the refractive index of a molded product made by sampling a fixed amount from the uppermost layer is used as a representative value. Can be used as the average value of the refractive index of the glass raw material.

ちなみに、本実施例の実験結果について述べる。 By the way, the experimental results of this example will be described.

下表には、100Kgのガラス原料を混合し、これを各層
ごとに20Kgずつ取出したものと各層の上層部の任意位置
からまんべんなく合計量が1Kgになるようにサンプリン
グしたものとを夫々溶融してガラス成形品を作り、各々
の成形品から得られた屈折率と目標の屈折率とを比較し
た数値(×10-5)が示してある。
In the table below, 100 kg of glass raw materials were mixed, and 20 kg of each of these layers was taken out and each sample was sampled from an arbitrary position in the upper layer of each layer so that the total amount would be 1 kg. The numerical values (× 10 −5 ) obtained by making glass molded products and comparing the refractive index obtained from each molded product with the target refractive index are shown.

この表から、上記方法により各層におけるガラス原料
の屈折率はほぼ一致しており、ガラス原料全体の均質性
は一定であることが理解できる。
From this table, it can be understood that the refractive indexes of the glass raw materials in each layer are substantially the same by the above method, and the homogeneity of the entire glass raw material is constant.

又、各層からのサンプリングによる屈折率はほぼ一致
しており、第1層、即ち混合機内の最上層におけるサン
プリングによる屈折率を混合容器内全体における屈折率
の平均値として用いることができる。
Further, the refractive indices obtained by sampling from the respective layers are substantially the same, and the refractive index obtained by sampling in the first layer, that is, the uppermost layer in the mixer can be used as the average value of the refractive indices in the entire mixing container.

(第2実施例) この実施例に示す混合機20は、第2図(a)及び
(b)に示すように、混合容器21、試料投入口22、排出
口24、回転軸23、スイッチ25及び駆動源としての不図示
の電動機等については第1実施例と同様の構成である。
(Second Embodiment) As shown in FIGS. 2 (a) and 2 (b), the mixer 20 shown in this embodiment has a mixing container 21, a sample inlet 22, an outlet 24, a rotary shaft 23, and a switch 25. The electric motor and the like (not shown) as a drive source have the same configuration as that of the first embodiment.

ただし、本実施例においては、混合容器21に下方から
所定の容量ごと(例えば、20Kgずつ)に水平方向につい
て層状に仕切り板28を着脱できる仕切り板挿入口27が設
けられている。この挿入口27は、混合中には閉塞可能で
ガラス原料の混合の支障とならないようにされ、混合後
に仕切り板28を挿入して混合されたガラス原料29を上記
のように層状に仕切ることができる。
However, in the present embodiment, the mixing container 21 is provided with partition plate insertion openings 27 through which the partition plates 28 can be attached and detached in layers in the horizontal direction at a predetermined capacity (for example, 20 kg each). This insertion port 27 can be closed during mixing so as not to hinder the mixing of glass raw materials, and after mixing, a partition plate 28 may be inserted to partition the mixed glass raw materials 29 into layers as described above. it can.

この混合機20を用いて粒状の光学ガラス原料を混合す
るには、挿入口27に仕切り板28を取り付けていない状態
で、第1実施例と同様に混合機21の投入口22から光学ガ
ラス原料29を例えば100Kg(混合容器21内の充填量が40
%程度)投入し、投入口22を閉塞してから混合機20を約
25分間回転させ、混合を終了する。
In order to mix the granular optical glass raw material using this mixer 20, the optical glass raw material is supplied from the charging port 22 of the mixer 21 in the same manner as in the first embodiment without the partition plate 28 being attached to the insertion port 27. 29 is, for example, 100 kg (the filling amount in the mixing container 21 is 40
%), Close the input port 22 and then close the mixer 20
Spin for 25 minutes to complete mixing.

次に、挿入口27に仕切り板28を挿入し、混合されたガ
ラス原料29を20Kgずつ層状に分割し、投入口22を開け
て、この投入口から、先ず最上層のガラス原料29をスコ
ップ或はバキューム等を用いて取出す。この最上層のガ
ラス原料を完全に取出した後、最上層の仕切り板28を抜
き出し、次いで次の層のガラス原料を上記と同様の方法
で取出し、その後その層の仕切り板28を抜き出し、この
操作を下方の層について行なう。ただし最下層のガラス
原料の取出しは、排出口24から行なうようにしてもよ
い。なお、本実施例において、ガラス原料の各層(分割
領域)は、それぞれ、各別に流動排出されるが、それ自
体の総量としてみる時、各層相互の比重には差が無く、
従って、所望量ずつ分割された、分割分毎の光学ガラス
の屈折率では、均等性が確保できる。
Next, the partition plate 28 is inserted into the insertion port 27, the mixed glass raw material 29 is divided into layers of 20 kg each, the charging port 22 is opened, and the uppermost glass raw material 29 is first scooped from the charging port. Is taken out using a vacuum or the like. After completely removing the glass material of the uppermost layer, the partition plate 28 of the uppermost layer is extracted, then the glass material of the next layer is extracted in the same manner as above, and then the partition plate 28 of the layer is extracted, and this operation is performed. For the lower layer. However, the lowermost glass raw material may be taken out through the outlet 24. In this example, each layer (divided region) of the glass raw material is fluidized and discharged separately, but when viewed as the total amount of itself, there is no difference in specific gravity between the layers,
Therefore, uniformity can be ensured in the refractive index of the optical glass for each divided portion, which is divided by the desired amount.

この実施例においても、各層のガラス原料の取出し時
に流動が生ぜず、比重分離が起きないから各層について
のガラス原料は一定の均質性を有する。従って、ガラス
原料の平均値は、最上層からのサンプリングにより信頼
性の高い値が得られる。なお、本実施例におけるガラス
原料の取出しは、各層が仕切り板で仕切られているため
第1実施例よりも容易に行なうことができる。
Also in this example, since no flow occurs when the glass raw material of each layer is taken out, and specific gravity separation does not occur, the glass raw material for each layer has a certain homogeneity. Therefore, as for the average value of the glass raw material, a highly reliable value is obtained by sampling from the uppermost layer. It should be noted that the glass raw material in this embodiment can be taken out more easily than in the first embodiment because each layer is partitioned by partition plates.

(第3実施例) この実施例に示す混合機30は、第3図(a)及び
(b)に示すように、混合されたガラス原料39を所定の
容量ごとに縦方向について層状に仕切れるように構成さ
れている。このため第2実施例と異なり、仕切り板挿入
口37は各層について垂直方向に設けられ、この挿入口に
仕切り板37が着脱可能とされている。又、混合容器31に
は排出口34のほか各層について排出口36が夫々設けられ
ている。その他の構成は、第2実施例と同様である。
(Third Embodiment) As shown in FIGS. 3 (a) and 3 (b), the mixer 30 shown in this embodiment divides the mixed glass raw material 39 into layers in the longitudinal direction for each predetermined volume. Is configured. Therefore, unlike the second embodiment, the partition plate insertion port 37 is provided in the vertical direction for each layer, and the partition plate 37 can be attached to and detached from this insertion port. In addition to the discharge port 34, the mixing container 31 is provided with a discharge port 36 for each layer. Other configurations are similar to those of the second embodiment.

この混合機30を用いて粒状の光学ガラス原料を混合す
るには、第2実施例と同様に、仕切り板37を取り付けて
いない状態で混合機30の投入口32から光学ガラス原料を
例えば100Kg(混合容器31内の充填量が40%程度)投入
し、投入口32を閉塞してから混合機30を約25分間回転さ
せ、混合を終了する。
In order to mix the granular optical glass raw material using the mixer 30, as in the second embodiment, 100 kg of the optical glass raw material is fed from the charging port 32 of the mixer 30 without the partition plate 37. (The filling amount in the mixing container 31 is about 40%), the input port 32 is closed, and then the mixer 30 is rotated for about 25 minutes to complete the mixing.

次に、各挿入口37に仕切り板38を夫々挿入して混合さ
れたガラス原料39を層状に分割する。本実施例の仕切り
板38は、混合容器31の下方から縦状に各挿入口37につい
て取付ける構成とされているから、上記のように混合容
器31の40%程度のガラス原料39を仕切る程度の高さに挿
入可能のものでよい。次いで、各層の排出口34或は36を
順次開け、混合されたガラス原料39を各層から排出す
る。
Next, a partition plate 38 is inserted into each insertion port 37 to divide the mixed glass raw material 39 into layers. Since the partition plate 38 of the present embodiment is configured to be vertically attached to each insertion port 37 from below the mixing container 31, as much as 40% of the glass container 39 of the mixing container 31 is partitioned as described above. It can be inserted into the height. Then, the outlet 34 or 36 of each layer is sequentially opened, and the mixed glass raw material 39 is discharged from each layer.

この実施例においては、第2実施例と異なり、仕切り
板38が縦状に設けられているから、混合後のガラス原料
39を全ての層について排出口34或は36から排出でき、ス
コップ或はバキューム等の使用を不要とする点で取出し
作業を簡便に行なうことができる。ただし、上記したよ
うに本実施例の仕切り板38は挿入後各層の上方が開放す
るため、投入口32からバキュームを用いて各層について
ガラス原料39の取出しを行なうようにしてもよい。
In this embodiment, unlike the second embodiment, since the partition plate 38 is provided vertically, the glass raw material after mixing is
39 can be discharged from the discharge ports 34 or 36 for all the layers, and the use of scoops or vacuums is unnecessary, so that the extraction work can be performed easily. However, as described above, since the partition plate 38 of the present embodiment opens the upper side of each layer after insertion, the glass raw material 39 may be taken out from each layer using a vacuum from the charging port 32.

なお、本実施例において、ガラス原料の各層(分割領
域)は、それぞれ、各別に流動排出されるが、それ自体
の総量としてみる時、各層相互の比重には差が無く、従
って、光学ガラスの屈折率では、均等性が確保できる。
In this example, each layer (divided region) of the glass raw material is separately fluidized and discharged, but when viewed as the total amount of itself, there is no difference in the specific gravities between the layers, and therefore the optical glass The refractive index can ensure uniformity.

(第4実施例) この実施例の混合機40は、第4図(a)及び(b)に
示すように、仕切り板47が水平方向に挿入できることは
第2及び第3実施例と同様であるが、本実施例は混合容
器41全体が倒立可能に構成された点で上記実施例と異な
っている。即ち、混合容器41は、その回転軸43で混合の
ための回転が可能であり、さらに回転機構50でこの混合
容器41を倒立可能に構成してある。混合容器41が倒立状
態にされた時、仕切り板47も又倒立状態となり、この仕
切り板で分割された各層は縦状に分割された状態とな
る。又、混合容器41が倒立状態にされたとき各層ごとに
ガラス原料49を排出できるように各層について排出口44
が設けられている。
Fourth Embodiment The mixer 40 of this embodiment is similar to the second and third embodiments in that the partition plate 47 can be inserted horizontally as shown in FIGS. 4 (a) and 4 (b). However, the present embodiment is different from the above embodiment in that the entire mixing container 41 is configured to be upside down. That is, the mixing container 41 can be rotated by the rotating shaft 43 for mixing, and the rotating mechanism 50 can invert the mixing container 41. When the mixing container 41 is inverted, the partition plate 47 is also inverted, and the layers divided by this partition plate are vertically divided. Further, the discharge port 44 for each layer is provided so that the glass raw material 49 can be discharged for each layer when the mixing container 41 is inverted.
Is provided.

この実施例においては、第2及び第3実施例と同様に
ガラス原料49を投入して混合できるが、混合後のガラス
原料の取出し時において仕切り板48を各挿入口に取付け
た後に混合容器41を倒立し、然る後各層の排出口46から
ガラス原料49を排出するようにしている。
In this embodiment, the glass raw materials 49 can be charged and mixed in the same manner as in the second and third embodiments. However, when the glass raw materials after mixing are taken out, the partition plate 48 is attached to each insertion port and then the mixing container 41. The glass raw material 49 is discharged from the discharge port 46 of each layer.

この実施例によれば、各層のガラス原料49が仕切り板
48で完全に仕切られるほか、ガラス原料49の取出し時に
全ての層について排出口46から排出することができる。
According to this embodiment, the glass raw material 49 of each layer is a partition plate.
In addition to being completely partitioned by 48, all layers can be discharged from the discharge port 46 when the glass raw material 49 is taken out.

なお、上記各実施例では、混合機としてW型混合機を
用いてあるが、本発明はこれに限らずV型混合機を用い
ることもできる。
In each of the above embodiments, the W-type mixer is used as the mixer, but the present invention is not limited to this, and a V-type mixer can also be used.

(発明の効果) 以上説明したように、本発明によれば、混合機で混合
された粒状混合物を処理するにあたり、混合後の粒状混
合物を層状に分割して取出すことにより、従来の問題点
であった混合機内での粒状混合物の排出に伴う比重分離
を防止して混合後の粒状混合物の均質性を一定に保つこ
とができる。
(Effects of the Invention) As described above, according to the present invention, in treating the granular mixture mixed in the mixer, the granular mixture after mixing is divided into layers and taken out. It is possible to prevent the specific gravity from being separated due to the discharge of the granular mixture in the existing mixer, and to keep the homogeneity of the granular mixture after mixing constant.

又、混合後の粒状混合物全体の均質性が保たれること
から、最上層の任意位置からのサンプリングにより得た
成形品の屈折率を代表値としてこの値を混合物全体の平
均値として用いることができるから、粒状混合物の平均
値を正確且つ容易に求めることができる。
Further, since the homogeneity of the whole granular mixture after mixing is maintained, the refractive index of the molded product obtained by sampling from the arbitrary position of the uppermost layer is used as a representative value and this value can be used as the average value of the entire mixture. Therefore, the average value of the granular mixture can be accurately and easily obtained.

【図面の簡単な説明】[Brief description of drawings]

第1図は、本発明の第1実施例で用いた混合機の縦断面
図である。 第2図(a)は、本発明の第2実施例で用いた混合機の
被混合物を収容していない状況の縦断面図である。 第2図(b)は、第2図(a)に示した混合機の被混合
物を収容し仕切り板を装着した状況の容器のみの縦断面
図である。 第3図(a)は、本発明の第3実施例で用いた混合機の
被混合物を収容していない状況の縦断面図である。 第3図(b)は、第3図(a)に示した混合機の被混合
物を収容し仕切り板を装着した状況の容器のみの縦断面
図である。 第4図(a)は、本発明の第3実施例で用いた混合機の
被混合物を収容していない状況の縦断面図である。 第4図(b)は、第4図(a)に示した混合機の容器内
に被混合物を収容し仕切り板を装着してこの容器を倒立
状態にした縦断面図である。 10、20、30、40……混合機 11、21、31、41……混合容器 12、22、32、42……投入口 16、26、36、46……排出口 17、27、37、47……挿入口 18、28、38、48……仕切り板 19、29、39、49……ガラス原料 50……回転機構
FIG. 1 is a vertical sectional view of a mixer used in the first embodiment of the present invention. FIG. 2 (a) is a vertical cross-sectional view of the mixer used in the second embodiment of the present invention in a state where the material to be mixed is not housed. Fig. 2 (b) is a vertical cross-sectional view of only the container in a state where the material to be mixed of the mixer shown in Fig. 2 (a) is accommodated and the partition plate is attached. FIG. 3 (a) is a vertical cross-sectional view of the mixer used in the third embodiment of the present invention in a state in which the material to be mixed is not housed. FIG. 3 (b) is a vertical cross-sectional view of only the container in a state where the material to be mixed of the mixer shown in FIG. 3 (a) is accommodated and the partition plate is attached. FIG. 4 (a) is a vertical cross-sectional view of the mixer used in the third embodiment of the present invention in a state in which the material to be mixed is not housed. FIG. 4 (b) is a vertical cross-sectional view of the container of the mixer shown in FIG. 4 (a) in which the material to be mixed is accommodated and a partition plate is attached to bring the container upside down. 10, 20, 30, 40 …… Mixer 11, 21, 31, 41 …… Mixing container 12, 22, 32, 42 …… Input port 16, 26, 36, 46 …… Discharge port 17, 27, 37, 47 …… Insertion port 18,28,38,48 …… Partition plate 19,29,39,49 …… Glass material 50 …… Rotating mechanism

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】混合容器内に粒状被混合物を投入し、前記
混合容器を回転することで、前記混合容器内に均質化さ
れた粒状混合物を生成する混合処理において、均質化の
後、前記粒状混合物を、前記混合容器内での堆積状態の
まま、上層側から所要量ずつ分割取出しすることを特徴
とする粒状混合物の分割取出し方法。
1. In a mixing process for producing a homogenized granular mixture in the mixing container by introducing the granular mixture into the mixing container and rotating the mixing container, the granular material is homogenized after the homogenization. A method for dividing and taking out a granular mixture, wherein a required amount of the mixture is taken out from the upper layer side while being kept in the state of being accumulated in the mixing container.
【請求項2】混合容器内に粒状被混合物を投入し、前記
混合容器を回転することで、前記混合容器内に均質化さ
れた粒状混合物を生成する混合処理において、均質化の
後、前記粒状混合物を、前記混合容器内での堆積状態の
まま、上下あるいは左右に層状に分割し、その分割毎に
取出しすることを特徴とする粒状混合物の分割取出し方
法。
2. In a mixing process for producing a homogenized granular mixture in the mixing container by introducing the granular mixture into the mixing container and rotating the mixing container, the granular material is homogenized and then granulated. A method for dividing and taking out a granular mixture, characterized in that the mixture is divided into layers in the vertical and horizontal directions in the state of being accumulated in the mixing container, and taken out for each division.
【請求項3】混合容器内に粒状被混合物を投入し、前記
混合容器を回転することで、前記混合容器内に均質化さ
れた粒状混合物を生成する混合処理装置において、前記
混合容器には、仕切り板挿入口が設けてあり、均質化の
後、前記粒状混合物を、前記混合容器内での堆積状態の
まま、上下あるいは左右に層状に分割するための仕切板
を、前記仕切板挿入口から前記混合容器内に挿入できる
構成にすると共に、各分割領域に対応して、前記混合容
器に排出口を装備したことを特徴とする粒状混合物の混
合処理装置。
3. A mixing treatment apparatus for producing a homogenized granular mixture in the mixing container by charging the granular mixture into the mixing container and rotating the mixing container. A partition plate insertion port is provided, and after homogenization, the granular mixture is kept in the state of being accumulated in the mixing container, and a partition plate for dividing into layers vertically or horizontally from the partition plate insertion port. A mixing processing apparatus for a granular mixture, characterized in that the mixing container is configured to be inserted into the mixing container, and the mixing container is provided with an outlet corresponding to each divided region.
【請求項4】均質化後の粒状混合物が、前記仕切板によ
って上下に層状に分割される混合処理装置において、前
記混合容器を、各分割領域に対応する前記排出口が下側
に変位するように、倒立動作させる構造になっているこ
とを特徴とする請求項3に記載の粒状混合物の混合処理
装置。
4. A mixing treatment apparatus in which a homogenized granular mixture is divided into upper and lower layers by the partition plate so that the discharge port corresponding to each divided region of the mixing container is displaced downward. The apparatus for mixing a granular mixture according to claim 3, wherein the apparatus has an inverted structure.
JP63207328A 1988-08-23 1988-08-23 Granular mixture divided take-out method and its mixing processing apparatus Expired - Lifetime JP2567462B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63207328A JP2567462B2 (en) 1988-08-23 1988-08-23 Granular mixture divided take-out method and its mixing processing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63207328A JP2567462B2 (en) 1988-08-23 1988-08-23 Granular mixture divided take-out method and its mixing processing apparatus

Publications (2)

Publication Number Publication Date
JPH0256228A JPH0256228A (en) 1990-02-26
JP2567462B2 true JP2567462B2 (en) 1996-12-25

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ID=16537937

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2567462B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102378097B1 (en) * 2021-11-17 2022-03-25 (주)소망유리 A composition mixing method for manufacturing cosmetic glass container
KR102378094B1 (en) * 2021-11-17 2022-03-25 (주)소망유리 A composition mixing device for manufacturing cosmetic glass container

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5845936Y2 (en) * 1980-09-06 1983-10-19 本田技研工業株式会社 Hinge device for removable roof panels in vehicles
JPS6090177A (en) * 1983-10-24 1985-05-21 石川島播磨重工業株式会社 Vertical type tank for powdered and granular body

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102378097B1 (en) * 2021-11-17 2022-03-25 (주)소망유리 A composition mixing method for manufacturing cosmetic glass container
KR102378094B1 (en) * 2021-11-17 2022-03-25 (주)소망유리 A composition mixing device for manufacturing cosmetic glass container

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