JPH05123563A - Continuous feeder of flocculating particulate material - Google Patents

Continuous feeder of flocculating particulate material

Info

Publication number
JPH05123563A
JPH05123563A JP28849191A JP28849191A JPH05123563A JP H05123563 A JPH05123563 A JP H05123563A JP 28849191 A JP28849191 A JP 28849191A JP 28849191 A JP28849191 A JP 28849191A JP H05123563 A JPH05123563 A JP H05123563A
Authority
JP
Japan
Prior art keywords
cone
particulate material
main body
powder
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.)
Withdrawn
Application number
JP28849191A
Other languages
Japanese (ja)
Inventor
Masaki Sasaki
正樹 佐々木
Mitsuhiro Sakawa
坂輪光弘
Toshiji Kikuchi
菊池利治
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP28849191A priority Critical patent/JPH05123563A/en
Publication of JPH05123563A publication Critical patent/JPH05123563A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/002Feeding of the particles in the reactor; Evacuation of the particles out of the reactor with a moving instrument

Abstract

PURPOSE:To uniformly and continuously supply a flocculating particulate material even when the particle size and moisture content thereof change by providing a spiral pleat to the inner surface of a cone-shaped part from the lower part of said part to the upper part thereof and providing a vibration element to a particulate material feeder partitioning the upper part of the pleat. CONSTITUTION:A spiral pleat is provided to the inner surface of the cone-shaped part 2 of a main body from the lower part of said part 2 to the upper part thereof and a partition plate 3 is provided to the upper part of the spiral pleat and a particulate material falling port 4 is provided to the uppermost part of the spiral pleat behind the partition plate 3. A vibration element 1 imparting vibration to the main body is provided. When a particulate material is charged in the cone-shaped part 2 of the main body, it is sent out upward little by little along the spiral pleat while vibrated. Therefore, even a flocculating particulate can be continuously and quantitatively supplied.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、石炭を始めとする凝集
性のある粉粒体の連続供給装置に関するものである。例
えば石炭を急速に熱分解し、固体(チャー、コーク
ス)、液体(タール)、気体を作り分ける石炭熱分解法
において、石炭を均一且つ連続的に供給することがポイ
ントになる。また、他の凝集性粉粒体を取扱う場合に
も、同様に、均一且つ連続的に供給することがポイント
になる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous feeding device for agglomerates, such as coal, which has a cohesive property. For example, in a coal pyrolysis method in which coal is rapidly pyrolyzed to produce solid (char, coke), liquid (tar), and gas, the point is to supply coal uniformly and continuously. Also, when handling other cohesive powders, the point is to similarly and continuously supply the same.

【0002】[0002]

【従来の技術】粉粒体の連続的供給法には、従来からテ
ーブルフィーダ法、スクリューフィーダー法などがあ
る。しかし、石炭のような凝集性のある粉粒体は、粒子
形状や水分量などの条件によって容易に凝集する場合が
あり、必ずしも満足できる法とは言えなかった。
2. Description of the Related Art Conventionally, a table feeder method, a screw feeder method, and the like have been known as a continuous supply method of powder and granules. However, a cohesive powdery substance such as coal may be easily agglomerated depending on the conditions such as the particle shape and the water content, and it cannot be said that the method is always satisfactory.

【0003】[0003]

【発明が解決しようとする課題】本発明はこのような従
来技術の現状に鑑み、凝集性粉粒体が有する性質に対応
して、安定してこれを供給できるようにしたものであ
る。
In view of the state of the art as described above, the present invention provides a stable supply of cohesive powder particles in accordance with their properties.

【0004】すなわち従来の粉粒体供給法では、粉粒体
の粒子形状や水分含有量により、粒子同士が凝集し、均
一且つ連続的供給を困難にしていた。そこでこの粒子同
士の凝集をいかに防いで凝集性のある粉粒体を供給する
かが課題であり、本発明は、それに適した連続供給装置
を提供する。
That is, in the conventional powder and granular material supplying method, the particles are aggregated depending on the particle shape and the water content of the granular material, and it is difficult to supply the particles uniformly and continuously. Therefore, how to prevent the particles from agglomerating and to supply a powdery or granular material having a cohesive property is a problem, and the present invention provides a continuous feeding device suitable for that.

【0005】[0005]

【課題を解決するための手段】本発明は、粉粒体粒子同
士の凝集を防ぐため、振動素子を付加し、バイブレーシ
ョンさせながら粉粒体を供給する装置を発明したもので
ある。
DISCLOSURE OF THE INVENTION The present invention invents a device for supplying powder particles while vibrating to add a vibrating element in order to prevent the particles of the powder particles from aggregating.

【0006】すなわち、本発明の凝集性粉粒体の連続供
給装置は、内面が上方に向かって開いたコーン形状とな
っている本体と、該本体に振動を付与する振動素子と、
本体に設けられた粉粒体落下口より取出される粉粒体を
導くためのパイプとからなる粉粒体の連続供給装置であ
って、本体のコーン形状内面には下部から上部に向かう
螺旋状のひだを有し、該螺旋状ひだ上部に仕切り板を設
け、且つ該仕切り板後方の螺旋状ひだ最上部に粉粒体落
下口を設けたことを特徴としている。
That is, the continuous feeding device for cohesive powder particles of the present invention comprises a main body having a cone shape whose inner surface opens upward, and a vibrating element for imparting vibration to the main body.
A continuous supply device for powder and granules, which comprises a pipe for guiding powder and granules taken out from a powder and granule dropout provided in the main body, and a spiral shape from the bottom to the top of the cone-shaped inner surface of the main body. And a partition plate is provided on the upper part of the spiral fold, and a powdery or granular material dropping port is provided on the uppermost part of the spiral fold behind the partition plate.

【0007】[0007]

【作用】粉粒体供給装置に振動素子を付加し、バイブレ
ーションさせながら粉粒体を供給させることにより、粉
粒体粒子同士の凝集を防ぎ、均一に且つ連続的に石炭を
供給することができる。
[Operation] By adding a vibrating element to the powder and granular material supply device and supplying the powder and granular materials while vibrating, agglomeration of the powder and granular particles can be prevented and coal can be supplied uniformly and continuously. .

【0008】特に本発明では、内面が上方に向かって開
いたコーン形状となっている本体に振動を直接付与する
点が特徴的であり、それによって、凝集性粉粒体の連続
的な定量供給が可能となる。
In particular, the present invention is characterized in that vibration is directly applied to the cone-shaped main body whose inner surface is open upward, whereby a continuous fixed amount of cohesive powder is supplied. Is possible.

【0009】[0009]

【実施例】以下、本発明である凝集性粉粒体の連続供給
装置の詳細について、図1に示す実施例装置を参照し、
粉粒体の動きを辿りながら説明する。
EXAMPLES The details of the continuous feeding apparatus for cohesive powder and granular material according to the present invention will be described below with reference to the apparatus shown in FIG.
An explanation will be given while following the movement of the granular material.

【0010】まず、粉粒体は、本装置本体のコーン形状
部分2に装入される。このコーン形状部分2は、振動素
子1によって振動を付与され、それによって粉粒体の定
量切出しを行なうための装置であるとともに、それ相当
の容量を持たせ得るため、ホッパー(貯槽)としての機
能も有している。
First, the granular material is loaded into the cone-shaped portion 2 of the main body of the apparatus. The cone-shaped portion 2 is a device for vibrating by the vibrating element 1 to perform quantitative cut-out of powder and granules, and since it can have a considerable capacity, it functions as a hopper (storage tank). I also have.

【0011】次に、コーン形状部分2に挿入された粉粒
体は、振動を付与させることにより、その内面下部から
上部に向かって設けられている螺旋状のひだに沿って少
しずつ上方へ送り出されて行く。その送り出される粉粒
体の量は、螺旋状ひだのコーン内面からの高さと、落下
口にいたる途中の仕切り板3の張出し長さによって制約
を受ける。すなわち螺旋状ひだのコーン内面からの高さ
が高ければ、あるいは仕切り板3の張出し長さが短けれ
ば、それだけ粉粒体送り出し量も増加する。なお、仕切
り板3は、定量切り出しに対して有効に作用する。
Next, the granular material inserted into the cone-shaped portion 2 is gradually fed upward along a spiral fold provided from the lower portion of the inner surface toward the upper portion by applying vibration. Go away. The amount of the powder or granules to be sent out is restricted by the height of the spiral fold from the inner surface of the cone and the protruding length of the partition plate 3 on the way to the drop port. That is, the higher the height of the spiral fold from the inner surface of the cone or the shorter the overhanging length of the partition plate 3, the more the amount of powder or granules delivered. The partition plate 3 effectively acts on the quantitative cutout.

【0012】こうして、粉粒体落下口4まで到達した粉
粒体は、該落下口4の下に接続されているパイプ5に流
れ込み、こうして連続的定量供給が可能となる。
In this way, the powder or granules that have reached the powder or granule dropping port 4 flow into the pipe 5 connected under the drop port 4, thus making it possible to continuously supply a fixed amount.

【0013】なお、本発明では、振動を付与することに
よって凝集性を有する粉粒体の凝集を防いでおり、同時
に一旦凝集した粉粒体の分散も図っている。
In the present invention, vibration is applied to prevent agglomerates of agglomerates from being agglomerated, and at the same time, the once agglomerated particles are dispersed.

【0014】次に図1に示す実施例装置の使用例につい
て説明する。100メッシュ以下80%の石炭50gを
図1の連続供給装置に装入する。振動素子1の振動強さ
5段階の内3に合わせて連続供給試験を行なった。図2
はこのときの経過時間に対する石炭供給量をプロットし
たものである。縦軸は石炭の供給量、横軸は経過時間、
勾配は石炭の供給速度を示す。また、図の中の直線の数
字は振動素子の振動強さを表すもので、数字の多い方が
振動の強いことを示す。この図において、勾配は直線で
あることから、供給速度が一定であることがわかる。振
動素子1の振動強さ5段階を2、5にした場合も図2に
合わせて載せた。この結果から振動素子1の振動強さを
変えることによって石炭の供給量を制御できることもわ
かった。
Next, an example of use of the embodiment apparatus shown in FIG. 1 will be described. 50 g of coal having 100 mesh or less and 80% is charged into the continuous feeding apparatus shown in FIG. The continuous supply test was conducted according to 3 out of 5 vibration intensities of the vibration element 1. Figure 2
Is a plot of the coal supply amount with respect to the elapsed time at this time. The vertical axis is the coal supply amount, the horizontal axis is the elapsed time,
The gradient shows the coal feed rate. In addition, the straight line numbers in the figure represent the vibration strength of the vibration element, and the larger the number, the stronger the vibration. In this figure, since the gradient is a straight line, it can be seen that the supply rate is constant. When the vibration intensity of the vibrating element 1 was set to 2 and 5 in 5 steps, the vibration element 1 was also placed according to FIG. From this result, it was also found that the supply amount of coal can be controlled by changing the vibration intensity of the vibration element 1.

【0015】また本発明の装置を用いれば水分10%の
石炭と乾燥炭とで供給速度に差のないこともわかった。
50メッシュおよび200メッシュの石炭についても同
じような結果が得られ、やはり供給速度に差がなかっ
た。
It was also found that there was no difference in the feed rate between coal having a water content of 10% and dry coal by using the apparatus of the present invention.
Similar results were obtained with 50 mesh and 200 mesh coal, again no difference in feed rate.

【0016】さらに本装置を高圧容器内にいれて同様の
試験を行なったが、高圧下でも石炭を均一且つ連続して
供給できることがわかった。
Further, the same test was carried out by putting the present apparatus in a high pressure vessel, and it was found that coal can be supplied uniformly and continuously even under high pressure.

【0017】[0017]

【発明の効果】以上説明してきたように、本装置は凝集
性粉粒体の粒子径、水分含有量が変化しても均一に且つ
連続して石炭を供給できる顕著な効果が得られる。
As described above, the present apparatus has a remarkable effect that coal can be supplied uniformly and continuously even if the particle size and the water content of the cohesive powder are changed.

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

【図1】本発明の実施例凝集性粉粒体の連続供給装置を
示す図で、(a)は正面図、(b)は側面図。
FIG. 1 is a diagram showing a continuous feeding device for cohesive powdery particles according to an embodiment of the present invention, in which (a) is a front view and (b) is a side view.

【図2】実施例の石炭の供給速度を示す図。FIG. 2 is a diagram showing a coal supply rate according to an embodiment.

【符号の説明】[Explanation of symbols]

1…振動素子 2…コーン形状部分 3…仕切り板 4…落下口 5…粉粒体供給パイプ DESCRIPTION OF SYMBOLS 1 ... Vibrating element 2 ... Cone-shaped part 3 ... Partition plate 4 ... Drop port 5 ... Powder supply pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 内面が上方に向かって開いたコーン形状
となっている本体と、該本体に振動を付与する振動素子
と、本体に設けられた粉粒体落下口より取出される粉粒
体を導くためのパイプとからなる粉粒体の連続供給装置
であって、本体のコーン形状内面には下部から上部に向
かう螺旋状のひだを有し、該螺旋状ひだ上部に仕切り板
を設け、且つ該仕切り板後方の螺旋状ひだ最上部に粉粒
体落下口を設けたことを特徴とする凝集性粉粒体の連続
供給装置。
1. A body having a cone shape whose inner surface opens upward, a vibrating element for imparting vibration to the body, and a granular material taken out from a granular material drop opening provided in the main body. Is a continuous supply device of powder and granules consisting of a pipe for guiding the, the cone-shaped inner surface of the main body has a spiral fold from the lower part to the upper part, the partition plate is provided on the spiral fold upper part, Further, a continuous feeding device for cohesive powder particles, characterized in that a powder particle dropping port is provided at the uppermost portion of the spiral fold behind the partition plate.
JP28849191A 1991-11-05 1991-11-05 Continuous feeder of flocculating particulate material Withdrawn JPH05123563A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28849191A JPH05123563A (en) 1991-11-05 1991-11-05 Continuous feeder of flocculating particulate material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28849191A JPH05123563A (en) 1991-11-05 1991-11-05 Continuous feeder of flocculating particulate material

Publications (1)

Publication Number Publication Date
JPH05123563A true JPH05123563A (en) 1993-05-21

Family

ID=17730903

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28849191A Withdrawn JPH05123563A (en) 1991-11-05 1991-11-05 Continuous feeder of flocculating particulate material

Country Status (1)

Country Link
JP (1) JPH05123563A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013052344A (en) * 2011-09-02 2013-03-21 Toyo Tanso Kk Powder processing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013052344A (en) * 2011-09-02 2013-03-21 Toyo Tanso Kk Powder processing device

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Legal Events

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Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 19990204