JPS5942114Y2 - Continuous automatic powder feeder - Google Patents
Continuous automatic powder feederInfo
- Publication number
- JPS5942114Y2 JPS5942114Y2 JP10998880U JP10998880U JPS5942114Y2 JP S5942114 Y2 JPS5942114 Y2 JP S5942114Y2 JP 10998880 U JP10998880 U JP 10998880U JP 10998880 U JP10998880 U JP 10998880U JP S5942114 Y2 JPS5942114 Y2 JP S5942114Y2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- rotary
- stage
- rotary supply
- transfer table
- 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
Links
Landscapes
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Furnace Charging Or Discharging (AREA)
Description
【考案の詳細な説明】
本考案は石炭−カーボン、活性炭等の粉体、特に流動性
の強い粉体を連続自動給粉する装置に関する。[Detailed Description of the Invention] The present invention relates to an apparatus for continuously and automatically feeding powders such as coal-carbon and activated carbon, especially highly fluid powders.
従来の連続自動給粉機は、複数個の放射状に設けた回転
羽根でもって粉体を定量に且つ連続的に給粉するロータ
リー型の給粉機であるが、羽根とケーシング内壁との間
に0.2〜0.3mのクリアランスを機械設計上必要と
していtうそのため、このクリアランスから流動性のあ
る粉体がリークして給粉精度が悪くなり、又ケーシング
内壁に粉体が付着し、この付着した粉体が羽根又は回転
する粉体と摩擦を引起し、その摩擦熱で化学反応を起し
て固化し、そのため、羽根の滑らかな回転を阻害して精
度を悪化せしめるという欠点があった。The conventional continuous automatic powder feeder is a rotary type powder feeder that continuously feeds powder in a fixed amount using multiple radially arranged rotating blades, but between the blades and the inner wall of the casing Since a clearance of 0.2 to 0.3 m is required in the mechanical design, fluid powder leaks from this clearance, resulting in poor powder feeding accuracy, and powder adheres to the inner wall of the casing. This adhering powder causes friction with the blade or the rotating powder, and the frictional heat causes a chemical reaction and solidifies, which has the disadvantage of interfering with the smooth rotation of the blade and deteriorating accuracy. Ta.
更に瞬間瞬間の給粉量は回転羽根の回転とともに脈動的
に変化している。Furthermore, the amount of powder fed at any moment changes pulsatingly as the rotary blade rotates.
そのため瞬間瞬間の給粉精度を要求される石炭粉、消石
灰、炭酸カルシュム等の給粉において不完全燃焼、不完
全反応を引起し、Co、HCl等の発生を増大せしめて
いた。This causes incomplete combustion and incomplete reaction when feeding coal powder, slaked lime, calcium carbonate, etc., which require moment-to-moment powder feeding precision, and increases the generation of Co, HCl, etc.
又連続自動給粉機としては実公昭47−17401号公
報に示される様に上位、下位の二つの収容筒を設け、粉
体を上位から下位に攪拌羽根で落下せしめ、下位収容筒
底にスクレーパ一方式の回転円盤を設けて定量供給する
ものが知られているが、これでは下位収容筒に収容され
る粉体量が定量供給量よりはるかに超える不定量である
ため下位収容筒における粉体圧の影響は充分に除去でき
ておらず、又上位、下位収容筒の段階で計量するもので
ないため回転円盤による一回計量であり充分に高い精度
が得にくいという欠点がある。As shown in Japanese Utility Model Publication No. 47-17401, a continuous automatic powder feeder is equipped with two storage cylinders, an upper one and a lower one, and the powder is dropped from the upper part to the lower part with a stirring blade, and a scraper is installed at the bottom of the lower storage cylinder. It is known that a one-sided rotating disk is installed to supply a fixed amount of powder, but in this case, the amount of powder stored in the lower storage cylinder is an indefinite amount that far exceeds the fixed amount of supply, so the amount of powder in the lower storage cylinder is The influence of pressure cannot be sufficiently eliminated, and since the measurement is not performed at the stage of the upper and lower housing cylinders, the measurement is performed once using a rotating disk, which has the disadvantage that it is difficult to obtain sufficiently high accuracy.
本考案はこれらの欠点を除去し脈動のない滑らかな給粉
を可能とした連続自動給粉機を提供せんとするものであ
る。The present invention aims to eliminate these drawbacks and provide a continuous automatic powder feeder that enables smooth powder feeding without pulsation.
この考案は全周部にわたって底なします1を複数個形成
した回転供給盤2を垂直筒体3内に複数段設けしかも下
段に従ってます1の容量を僅かずつ小さくし、又最下段
の回転供給盤2の下方に円周方向に区画されない環状粉
体収容棚4を有する回転移送テーブル5を設け、同回転
移送テーブルにスクレーパ6を備え、垂直筒体3の上方
開口を粉体導入口Tに又スクレーパ6下方を排出口8と
するとともに、最上段の回転供給盤2上方、回転供給盤
2間及び回転供給盤2と回転移送テーブル5との間に粉
体連通孔9を有する隔壁10を設け、且つ粉体連通孔9
が連続して同じ円周位置とならない様にその孔位置をず
らし、更に前記回転供給盤2及び回転移送テーブル5と
を所定速度で回転駆動せしめてなる連続自動給粉機に係
るものである。In this invention, a plurality of rotary supply plates 2 each having a plurality of bottomless bottoms 1 are provided in a vertical cylinder 3 in multiple stages, and the capacity of the rotary supply plates 1 is gradually reduced according to the lower stage. A rotary transfer table 5 having an annular powder storage shelf 4 that is not divided in the circumferential direction is provided below, and a scraper 6 is provided on the rotary transfer table, and the upper opening of the vertical cylinder 3 is connected to the powder introduction port T and the scraper A partition wall 10 having a powder communication hole 9 is provided above the uppermost rotary supply plate 2, between the rotary supply plates 2 and between the rotary supply plate 2 and the rotary transfer table 5, And powder communication hole 9
This relates to a continuous automatic powder feeder in which the positions of the holes are shifted so that the holes are not continuously at the same circumferential position, and the rotary supply plate 2 and the rotary transfer table 5 are driven to rotate at a predetermined speed.
なお、図中11は攪拌羽根、12は同攪拌羽根、回転供
給盤2、回転移送テーブル5とを回動せしめる回転軸、
13はシュート、14はウオームギア、15は駆動軸で
ある。In addition, in the figure, 11 is a stirring blade, 12 is a rotating shaft that rotates the stirring blade, the rotary supply board 2, and the rotary transfer table 5;
13 is a chute, 14 is a worm gear, and 15 is a drive shaft.
この考案では粉体は垂直筒体3の上方開口の粉体導入口
1より投入され、攪拌羽根8等の手段より最上段の隔壁
10の粉体連通孔9から第一段の回転供給盤2の底なし
ます1内に送られる。In this device, powder is introduced from the powder introduction port 1 at the upper opening of the vertical cylinder 3, and is passed through the powder communication hole 9 of the uppermost partition wall 10 by means such as stirring blades 8 to the first stage rotary supply plate 2. Sent within the bottomless box 1.
粉体は底なします10四方の周壁と上下の隔壁10に囲
まれる定量まず空間に充填され、回転供給盤2の回転と
ともに移送される。A fixed amount of powder is first filled into a space surrounded by a bottomless 10 square peripheral wall and upper and lower partition walls 10, and is transferred as the rotary supply plate 2 rotates.
しかしながらこの段階では垂直筒体3内の多量に収容さ
れた粉体による強い圧力は供給口であるその第一段目の
連通孔9を介して作用するので一段目の回転供給盤2の
底なします1内への充填では充分に垂直筒体3の粉体圧
の影響を避は得ていな()次に第一段目の回転供給盤2
の底なします1内の粉体は回転移送され、二段目の隔壁
10の連通孔9から二段目の回転供給盤2の底なします
1内に落し込まれる。However, at this stage, the strong pressure due to the large amount of powder contained in the vertical cylinder 3 acts through the first stage communication hole 9 which is the supply port, so the first stage rotary supply board 2 becomes bottomless. The influence of the powder pressure in the vertical cylinder 3 cannot be sufficiently avoided when filling the powder into the first stage.
The powder in the bottom chamber 1 is transferred by rotation and is dropped into the bottom chamber 1 of the second stage rotary supply plate 2 through the communication hole 9 of the second stage partition wall 10.
ここで二段目の隔壁10の連通孔9の位置は上位の隔壁
10の連通孔9の位置とは同じ円周位置になくずれた位
置にあるため垂直筒体3内の粉体圧が一段目の隔壁10
の連通孔9、一段目の回転供給盤2の底なします1と二
段目の隔壁10の連通孔9とを介して直接作用するとい
うことが避けることができ、第一段目の隔壁10によっ
て、垂直筒体3内の粉体圧が第二段目の回転供給盤2の
底なします1への粉体の充填に影響するのを完全に遮断
できるものである。Here, the position of the communication hole 9 of the second-stage partition wall 10 is not at the same circumferential position as the position of the communication hole 9 of the upper partition wall 10, but is shifted, so that the powder pressure inside the vertical cylinder 3 is lowered by one level. eye septum 10
It can be avoided that the communication hole 9 of the first stage rotary supply board 2 acts directly through the bottom 1 of the first stage rotary supply plate 2 and the communication hole 9 of the second stage partition wall 10, and the first stage partition wall 10 , it is possible to completely prevent the powder pressure inside the vertical cylinder 3 from affecting the filling of the powder into the bottom 1 of the second-stage rotary supply plate 2.
しかも第二段目の回転供給盤2の底なします1の容量は
第一段のものより小としており、ここにおいてより僅か
小さな定量まず空間に粉体が充填しなおされ、第二段の
回転供給盤20回転とともに移送され、第三段目の隔壁
10の連通孔9から下方の回転移送テーブル5の環状粉
体収容棚4上に落し込まれる。Moreover, the capacity of the bottomless chamber 1 of the second-stage rotary supply plate 2 is smaller than that of the first stage, and the powder is first refilled into the space with a slightly smaller fixed amount, and then the second-stage rotary supply It is transferred as the disk rotates 20 times, and is dropped onto the annular powder storage shelf 4 of the rotary transfer table 5 below through the communication hole 9 of the partition wall 10 of the third stage.
ここでます1の容量は下段に従って僅かずつ小としてい
るので粉体圧の影響を可及的に小さく押えながら粉体を
ます1に満すことができる。Here, since the capacity of each cell 1 is gradually decreased toward the bottom, it is possible to fill each cell with powder while minimizing the influence of powder pressure.
所定まず容量の粉体は環状粉体収容棚4上に落し込まれ
るが底なします1は区画されたものであるため、環状粉
体収容棚4上の粉体の円周方向の載置量分布は脈動状態
に変動している。First, a predetermined volume of powder is dropped onto the annular powder storage shelf 4, but it bottoms out.Since 1 is partitioned, the amount of powder placed on the annular powder storage shelf 4 in the circumferential direction is is fluctuating in a pulsating state.
次に粉体は回転移送テーブル50回転とともに回転移送
されスクレーパ6によって環状粉体収容棚4かも排出口
8へ連続的に移動され排出されるが、そのスクレーパ6
による連続排出によって粉体の排出口8からの排出流量
は平均化され、定量粉体が脈動なく連続的に次段装置へ
と給粉されることとなる。Next, the powder is rotationally transferred as the rotary transfer table 50 rotates, and the annular powder storage shelf 4 is continuously moved to the discharge port 8 by the scraper 6 and discharged.
Due to the continuous discharge, the discharge flow rate of powder from the discharge port 8 is averaged, and a fixed amount of powder is continuously supplied to the next stage device without pulsation.
粉体は、回転供給盤の移送過程で何ら垂直筒体3の内側
壁と接触しないので、この間のクリアランスから粉体が
リークすることも又付着して固化することもない。Since the powder does not come into contact with the inner wall of the vertical cylindrical body 3 during the transfer process of the rotary supply plate, the powder does not leak from the clearance between them, nor does it adhere and solidify.
又、回転移送テーブル5の過程で垂直筒体3の内側壁に
付着があっても羽根がないので摩擦熱が発生して固化す
ることがなく、実用上はとんど問題がない。Further, even if there is adhesion to the inner wall of the vertical cylindrical body 3 during the transfer process of the rotary transfer table 5, since there are no blades, frictional heat will not be generated and solidification will occur, so there is almost no problem in practice.
なお、実施例は回転供給盤2は二段となっているが三段
以上であってもよいことは勿論である。In the embodiment, the rotary supply board 2 has two stages, but it goes without saying that it may have three or more stages.
以上の様に、本考案によれば、回転供給盤の底なします
1内に粉体が定量収容され、垂直筒体3内側壁と直接粉
体は接触しないので粉体がリークしたり、又付着固化す
ることがなく、給粉の定量精度が高い。As described above, according to the present invention, a fixed amount of powder is stored in the bottom 1 of the rotary supply plate, and since the powder does not come into direct contact with the inner wall of the vertical cylinder 3, there is no possibility of powder leaking or adhesion. It does not solidify and the quantitative accuracy of powder feeding is high.
更に回転移送テーブル5によって定量に送られた粉体を
脈動なく連続的に且つ均−滑らかに給粉でき、特に石灰
粉、消石灰、炭酸カルシウム等の給粉におげろ給粉の脈
動的変化による不完全燃焼、不完全反応の発生をなくす
という効果がある。Furthermore, the powder fed in fixed quantities by the rotary transfer table 5 can be fed continuously and evenly without pulsation, and in particular, it is possible to feed powder such as lime powder, slaked lime, calcium carbonate, etc. due to pulsating changes in powder feeding. This has the effect of eliminating the occurrence of incomplete combustion and incomplete reactions.
又回転供給盤2を二段以上とし、しかもその隔壁10の
連通孔9が互にずれて連続して同じ円周位置にない様に
することによってもつとも強い影響を与える垂直筒体3
内の粉体による粉体圧を完全に遮断でき、よって高精度
の定量供給を可能としたという優れた効果を得ることが
できる。Furthermore, the vertical cylindrical body 3 has a very strong influence by having the rotary supply plate 2 in two or more stages, and by making sure that the communication holes 9 of the partition walls 10 are shifted from each other so that they are not continuously located at the same circumferential position.
It is possible to completely block out the powder pressure caused by the powder inside the container, thereby achieving the excellent effect of enabling highly accurate quantitative supply.
第1図は本考案連続自動給粉機の実施例を示す縦断面図
、第2図は同平面図である。
1:底なします、2:回転供給盤、3:垂直筒体、4:
環状粉体収容棚、5・・・回転移送テーブル、6:スク
レーパ T:粉体導入口、8:排出口、9:粉体連通孔
、
10:隔壁。FIG. 1 is a longitudinal sectional view showing an embodiment of the continuous automatic powder feeder of the present invention, and FIG. 2 is a plan view thereof. 1: Bottomless, 2: Rotating supply plate, 3: Vertical cylinder, 4:
Annular powder storage shelf, 5...rotary transfer table, 6: scraper T: powder introduction port, 8: discharge port, 9: powder communication hole, 10: partition wall.
Claims (1)
給盤3を垂直筒体3内に複数段設けしかも下段に従って
ます1の容量を僅かずつ小さくし、又最下段の回転供給
盤2の下方に円周方向に区画されない環状粉体収容棚4
を有する回転移送テーブル5を設け、同回転移送テーブ
ルにスクレーパ6を備え、垂直筒体3の上方開口を粉体
導入口1に又スクレーパ6下方を排出口8とするととも
に、最上段の回転供給盤2上方、回転供給盤2間及び回
転供給盤2と回転移送テーブル5との間に粉体連通孔9
を有する隔壁10を設け、且つ粉体連通孔9が連続して
同じ円周位置とならない様にその孔位置をずらし、更に
前記回転供給盤2及び回転移送テープ/I15とを所定
速度で回転駆動せしめてなる連続自動給粉機。A plurality of rotary supply plates 3 each having a plurality of bottomless bottoms 1 formed around the entire circumference are provided in the vertical cylinder 3 in multiple stages. Annular powder storage shelf 4 that is not divided in the circumferential direction
A rotary transfer table 5 having Powder communication holes 9 are provided above the plate 2, between the rotary supply plates 2 and between the rotary supply plate 2 and the rotary transfer table 5.
A partition wall 10 is provided, and the positions of the powder communication holes 9 are shifted so that they are not continuously located at the same circumferential position, and the rotary supply plate 2 and the rotary transfer tape/I15 are driven to rotate at a predetermined speed. Continuous automatic powder feeder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10998880U JPS5942114Y2 (en) | 1980-08-01 | 1980-08-01 | Continuous automatic powder feeder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10998880U JPS5942114Y2 (en) | 1980-08-01 | 1980-08-01 | Continuous automatic powder feeder |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5735740U JPS5735740U (en) | 1982-02-25 |
JPS5942114Y2 true JPS5942114Y2 (en) | 1984-12-07 |
Family
ID=29471149
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10998880U Expired JPS5942114Y2 (en) | 1980-08-01 | 1980-08-01 | Continuous automatic powder feeder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5942114Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008290045A (en) * | 2007-05-28 | 2008-12-04 | Chugoku Electric Power Co Inc:The | Quantitative feeder, apparatus for preparing slurry and method for preventing adhesion of powder |
-
1980
- 1980-08-01 JP JP10998880U patent/JPS5942114Y2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5735740U (en) | 1982-02-25 |
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