JPS5882923A - Powder pneumatic transport method - Google Patents
Powder pneumatic transport methodInfo
- Publication number
- JPS5882923A JPS5882923A JP18099381A JP18099381A JPS5882923A JP S5882923 A JPS5882923 A JP S5882923A JP 18099381 A JP18099381 A JP 18099381A JP 18099381 A JP18099381 A JP 18099381A JP S5882923 A JPS5882923 A JP S5882923A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- hopper
- service
- pressure
- pulverized coal
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/40—Feeding or discharging devices
- B65G53/46—Gates or sluices, e.g. rotary wheels
- B65G53/4608—Turnable elements, e.g. rotary wheels with pockets or passages for material
- B65G53/4616—Turnable elements, e.g. rotary wheels with pockets or passages for material with axis of turning parallel to flow
Abstract
Description
【発明の詳細な説明】
この発明は、微粉炭、セメント、水処理剤などの粉末を
圧力空気のような気体で輸送する気送方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a pneumatic transportation method for transporting powder such as pulverized coal, cement, and water treatment agents using a gas such as pressurized air.
従来、前記のような気送方法では、大気に開放された計
量ホッパーからロータリ一式の自動定量粉末供給装置に
よって気送用混合器に重力で粉末を路下供給することが
一般に行われている。このような従来の気送方法では、
混合器と粉末供給装置、粉末供給装置と計量ホラ・や−
との間にシール機構を設けているが、完全なシールがで
きず、変動によシ粉末の供給量不均一とな)、また、気
圧差による気体の流れがあるため、この流れに粉末が混
入して、粉末供給装置などに摩耗が生じ易く、気送時に
脈動などが生じ、粉末を所定量に保って気送することが
困難であるという問題があった。Conventionally, in the above-mentioned pneumatic feeding method, powder is generally fed down the street by gravity from a metering hopper open to the atmosphere to a pneumatic mixer using a rotary set of automatic metering powder feeding device. In this conventional pneumatic method,
Mixer and powder feeding device, powder feeding device and measuring hole
Although a sealing mechanism is installed between the This causes problems such as abrasion of the powder supply device and the like, and pulsation during pneumatic feeding, making it difficult to maintain a predetermined amount of powder while pneumatically feeding the powder.
この発明は、計量ホツノヤー、粉末供給装置および気送
用混合器内の圧力をほぼ均等な圧力に保つことによシ、
前述した問題を解決して、粉末を所定量に確保しかつ安
定して気送できる方法を提供することを目的としている
。This invention achieves
It is an object of the present invention to provide a method that solves the above-mentioned problems and can secure a predetermined amount of powder and stably pneumatically convey it.
以下、この発明の一実施例につき図面を参照して説明す
る。Hereinafter, one embodiment of the present invention will be described with reference to the drawings.
第1図において、lは計量ホツノ9−で[Lこの計量ホ
ツノ譬−1上にはサービスホラ”−22>(設ケラれ、
サービスホッノぐ一2上Kt[’蔵ホッパー3が設けら
れている。サービスホッパー−2から計量ホツノや−1
への粉末供−口4aおよび貯蔵ホラA −3カラサービ
スホッパー2への粉末供給口4bにはグンノ4−パルプ
5,6がそれぞれ設けられ。In Fig. 1, l is a measurement point 9- [L on this measurement point example-1 is a service hora''-22> (setting,
Service Hotnoguichi 2 Kt [Kura hopper 3 is provided. From service hopper-2 to weighing hotsunoya-1
Gunno 4-pulp 5 and 6 are provided at the powder supply port 4a to the storage holster A-3 and the powder supply port 4b to the storage hopper A-3 color service hopper 2, respectively.
これらはアクチュエータ7.8で開閉されるようになっ
ている。また計量ホラ/#−1の下方には後述する自動
定量粉末供給装置9が設けlられ1:こO粉末供給装置
9の粉末吐出口10上には、混合器11を構成する空気
噴出筒12が設けられている。These are opened and closed by actuators 7.8. Further, an automatic quantitative powder supply device 9, which will be described later, is provided below the measuring hole/#-1. is provided.
前記貯蔵ホラ/# 3 *サービスホッパー −2h
ヨU空気噴出筐12はそれぞれ弁13.14および1
5を介して圧力空気源と接続されている。前記粉末吐出
口10下面が気送管16と連通され、気送管16は微粉
炭燃焼炉17に開口されている。前記粉末供給装置9は
、第1図、第2図に示すように、電動機18によシ変速
手段および減速機を介して駆動される縦軸20に多数の
羽犠21mを有するロータ21が嵌着され、前記羽根2
1i上には前記空気噴出筒12の下面と一体に摺切多板
19が配設され、これらは粉末供給装置9の周壁9aに
固定されている。また、前記縦軸2oにはサービスホッ
パー2および貯蔵ホッパー3の底と摺接する切出し翼2
2および23がそれぞれ嵌着されている。Said storage hopper/#3 *Service hopper -2h
The air outlet housing 12 has valves 13, 14 and 1, respectively.
5 to a source of pressurized air. The lower surface of the powder discharge port 10 communicates with a pneumatic pipe 16, and the pneumatic pipe 16 opens into a pulverized coal combustion furnace 17. As shown in FIGS. 1 and 2, the powder supply device 9 includes a rotor 21 having a large number of blades 21 m fitted to a vertical shaft 20 driven by an electric motor 18 via a speed change means and a speed reducer. and said feather 2
A sliding multi-plate 19 is disposed on 1i integrally with the lower surface of the air ejection cylinder 12, and these are fixed to the peripheral wall 9a of the powder supply device 9. Further, the vertical axis 2o is provided with a cutting blade 2 that is in sliding contact with the bottom of the service hopper 2 and the storage hopper 3.
2 and 23 are fitted respectively.
前述のように構成された気送装置を用い、この発明の一
゛実旌例による微粉炭の気送を行うには。To pneumatically transport pulverized coal according to an embodiment of the present invention using a pneumatic transporter constructed as described above.
まず弁1st−開いて、図示しないブロワ−などの圧力
空気源から圧力空気を空気噴出[12に供給すると共に
、電動機18を駆動させ、縦軸2oを介して粉末供給装
置90ロータ21を回転させる。First, the valve 1st is opened, and pressurized air is supplied from a pressure air source such as a blower (not shown) to the air jet [12], and the electric motor 18 is driven to rotate the powder supply device 90 rotor 21 via the vertical shaft 2o. .
このようにすると、計量ホッノや一1内の微粉炭がロー
タ21の羽根21a間に充填されて摺切シ板19で摺切
られ、重力と空気噴出筺12下面からの圧力空気の噴出
とにょシ所定量ずつ粉末吐出口10から気送管16に吐
出され、気送管16を経て微粉炭燃焼炉17に供給され
、ことで燃焼される。In this way, the pulverized coal in the metering tube 11 is filled between the blades 21a of the rotor 21 and rubbed off by the sliding plate 19, and due to gravity and the jetting of pressurized air from the bottom surface of the air jetting case 12, A predetermined amount of the powder is discharged from the powder discharge port 10 into the pneumatic pipe 16, and then supplied to the pulverized coal combustion furnace 17 through the pneumatic pipe 16, where it is combusted.
計量ホッパー1内の微粉炭が減少した場合にはこれをレ
ベル計などの適宜の手段で検出して、常閉の弁14を開
き、サービスホラ/ぐ一2内に圧力空気を供給し、サー
ビスホツノや一2内と計量ホツノぐ一1内の圧力が均尋
になった時にダン/4− /量ルプ5を開く、このよう
にすると、サービスホツノ譬−2内の微粉炭が前記縦軸
200回転に伴う切出し翼220回転によシ切出され、
粉末供給口4&から計量ホッパー1内に重力によって落
下し%供給される。そして、この場合に、ダン/#
/4ルブ5がML、ているため、サービスホラ・母−2
と大気側である貯蔵ホッパー3との連通が遮断されてお
L したがって、サービスホッパー−2および計量ホン
パー1と粉末供給装置9内は混合器11内すなわち空気
噴出1i12内とほぼ均岬な圧力に保って、微粉炭の補
給が行われる。ターイマーなどの作動によって、弁14
とダン/ぐ−)4ルプ5を閉じ。When the amount of pulverized coal in the weighing hopper 1 decreases, this is detected by an appropriate means such as a level meter, the normally closed valve 14 is opened, and pressurized air is supplied into the service hollow/gut 2 to start the service. When the pressure in the hot spring 1 2 and the measuring hot spring 1 become equal, open the Dan / 4 - / metering loop 5. If you do this, the pulverized coal in the service hot spring 2 will be transferred to the vertical axis. The cutting blade is cut out by 220 rotations due to 200 rotations,
The powder falls into the weighing hopper 1 from the powder supply port 4& and is supplied by gravity. And in this case, Dan/#
/4 Lube 5 is ML, so service horror/mother-2
Therefore, the pressure inside the service hopper 2, the weighing pumper 1, and the powder supply device 9 is almost equal to that inside the mixer 11, that is, the air jet 1i12. pulverized coal will be replenished. Valve 14 is activated by a timer or the like.
and dan/gu-) 4 Close loop 5.
サービスホッパー2から計量ホツノダー1への微粉炭の
供給は停止される。その後、常閉の弁13を開き、貯蔵
ホンパー3内に圧力空気を供給すると共に、メンノ臂−
パルブ6を開くと、貯東ホツノぐ一3内からサービスホ
ツノ中−2内に微粉炭が補給される。そして、この場合
に、サービスホツノ4−2の圧力は低下するが、ダンパ
ーパルプ5が閉じているので計量ホッパー1内は粉末供
給装置9.空気噴出筒12内とほぼ均勢な圧力に保持さ
れる。The supply of pulverized coal from the service hopper 2 to the weighing powder 1 is stopped. Thereafter, the normally closed valve 13 is opened to supply pressurized air into the storage pumper 3, and at the same time
When the valve 6 is opened, pulverized coal is replenished from the storage hot spring 3 into the service hot spring 2. In this case, the pressure in the service tube 4-2 decreases, but since the damper pulp 5 is closed, the powder supply device 9. The pressure is maintained at approximately the same level as the pressure inside the air jet cylinder 12.
タイマーなどの作動によって、弁13とダンパ−パルプ
6とを閉じ、貯蔵ホツノ母−3からサービスホッパー−
2への微粉炭の補給は停止される。なお、この実施例に
おいて、弁13.ダンノ々−パルプ6と、弁14.ダン
パーバルブ5と社、これらの一方が開いている際には他
方は必ず閉じておくものとする。The valve 13 and the damper pulp 6 are closed by the operation of a timer or the like, and the pulp is removed from the storage pulp 3 to the service hopper.
Supply of pulverized coal to No. 2 will be stopped. Note that in this embodiment, valve 13. Dunno pulp 6 and valve 14. When one of the damper valves 5 and 5 is open, the other must be closed.
なお、ξの発明において、前記粉末供給装置の吐出口に
エジェクタ一方式などの気送用混合器を接続し、粉末供
給装置は重力による落下、tたはこれと圧力空気の併用
によル微粉末を供給するものとしてもよい。In addition, in the invention of ξ, a pneumatic mixer such as a one-way ejector is connected to the discharge port of the powder supply device, and the powder supply device is caused to drop by gravity, or by a combination of this and pressurized air. It is also possible to supply powder.
また、この発明において、計量ホツノ9−とサービスホ
ツノ9−との圧力を検出する手段は、適宜の圧力針を両
ホッパーに設けて、これらによる検出信号でサービスホ
ッパーへの圧力空気供給通路に設は弁および、サービス
ホッパーの粉末供給口に設けたダンパーパルプを自動制
御し、あるいは計量ホラt? −トサービスホツノ4−
とをそれぞれロードセルを介して装置枠にフローティン
グ支持し。In addition, in this invention, the means for detecting the pressure in the weighing hot spring 9- and the service hot spring 9- is provided by providing appropriate pressure needles in both hoppers, and using detection signals from these needles to detect the pressure in the pressure air supply passage to the service hopper. automatically controls the valve and the damper pulp provided at the powder supply port of the service hopper, or the metering hole t? -To Service Hotsuno 4-
and are each floatingly supported on the equipment frame via load cells.
計量ホッパーとサービスホッパー、サービスホラ・量−
と貯蔵ホッパーとをフレキシブル継手を介して接続し、
計量ホッパや−とサービスホッパーの空気圧力をロード
セルで検出して、弁およびダンパ−パルプを制御するよ
うにしてもよい。Weighing hopper and service hopper, service hopper and quantity.
and the storage hopper are connected through a flexible joint,
The air pressure in the weighing hopper and the service hopper may be detected by a load cell to control the valve and damper pulp.
さらに、この発明は、前記笑施例のような微粉炭の気送
に限られることなく、セメント、水処理剤など他の粉末
の気送にも適用でき、気送用の圧力気体も例えば不活性
ガスなど空気以外の気体を用いてもよい。Furthermore, the present invention is not limited to the pneumatic conveyance of pulverized coal as in the embodiment described above, but can also be applied to the pneumatic conveyance of other powders such as cement and water treatment agents. Gases other than air, such as active gases, may also be used.
以上説明1−だように、この発明による粉末の気送方法
は、計量ホッパー、自動定量粉末供給装置および気送用
混合器内を大気圧力よル高い互にほぼ均等な圧力に保っ
て、計量ホラi+−かも前記粉末供給装置によって瓶定
量ずつ前記混合器に供給するようにしたので、気送する
以前に粉末を計量遂時の脈動が生ずることを防止でき、
したがって。As explained in Explanation 1-1 above, the powder pneumatic feeding method according to the present invention maintains the insides of the weighing hopper, automatic metered powder supply device, and pneumatic mixer at substantially equal pressures higher than atmospheric pressure, and performs weighing. Since the powder feeder supplies the powder to the mixer in fixed amounts in bottles, it is possible to prevent pulsation from occurring when the powder is measured before being air-fed.
therefore.
正確にかつ安定して所定量の粉末を気送できるという効
果がある。The effect is that a predetermined amount of powder can be pneumatically delivered accurately and stably.
第1図はこの発明の一実施例による粉末の気送方法を行
う装置を示す概略縦断面図、82図は第1図の■−■線
に沿う断面図である。
l・・・計量ホッパー、2・・・サービスホッパー、3
・・・貯蔵ホッパ4 、5 t 5・・・ダンパ−パ
ルプ。
9・・・自動定量粉末供給装置、11・・・気送用混合
器。
13.14,15・・・弁、16・・・気送管。
特許出願人 代理人FIG. 1 is a schematic longitudinal cross-sectional view showing an apparatus for performing a powder pneumatic feeding method according to an embodiment of the present invention, and FIG. 82 is a cross-sectional view taken along the line ■-■ in FIG. 1. l...Weighing hopper, 2...Service hopper, 3
...Storage hoppers 4, 5t5...Damper pulp. 9... Automatic quantitative powder supply device, 11... Pneumatic mixer. 13.14,15...Valve, 16...Pneumatic pipe. Patent applicant agent
Claims (2)
て気送用混合器に粉末を供給するに当シ、前記ホツノ譬
−9粉末供給装置および気送用混合器内を大気圧よシ高
い互にほぼ均等な圧力に保つことを特徴とする粉末の気
送方法。(1) When supplying powder from the measuring hot spring 4- to the pneumatic mixer by the automatic quantitative powder feeding device, the inside of the powder feeding device 9 and the pneumatic mixer must be kept above atmospheric pressure. A method of pneumatically feeding powder, which is characterized by maintaining almost uniform pressure.
−内の圧力を計量ホッパー内の圧力を均等にして、前記
両ホッパーの間に設けた弁番開き、サービスホツノ4−
から計量ホッパーへ粉末を補給することを特徴とする特
許請求の範囲第1項に記載し九粉末の気送方法。(2) Service Honno 4 to replenish powder to the weighing hopper
- Equalize the pressure in the measuring hopper, and open the valve number provided between the two hoppers, service hot spring 4-
A method for pneumatically feeding powder according to claim 1, characterized in that the powder is replenished from the measuring hopper to the measuring hopper.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18099381A JPS5882923A (en) | 1981-11-13 | 1981-11-13 | Powder pneumatic transport method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18099381A JPS5882923A (en) | 1981-11-13 | 1981-11-13 | Powder pneumatic transport method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5882923A true JPS5882923A (en) | 1983-05-18 |
Family
ID=16092856
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18099381A Pending JPS5882923A (en) | 1981-11-13 | 1981-11-13 | Powder pneumatic transport method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5882923A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101857144A (en) * | 2010-06-02 | 2010-10-13 | 三一重工股份有限公司 | Mortar transfer device |
CN102393164A (en) * | 2011-10-31 | 2012-03-28 | 江西佳联科技有限公司 | Quantitative explosive feeding device |
CN111412457A (en) * | 2020-03-27 | 2020-07-14 | 江苏理文造纸有限公司 | Can effectively reduce NOXVented boiler |
-
1981
- 1981-11-13 JP JP18099381A patent/JPS5882923A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101857144A (en) * | 2010-06-02 | 2010-10-13 | 三一重工股份有限公司 | Mortar transfer device |
WO2011150850A1 (en) * | 2010-06-02 | 2011-12-08 | 湖南三一智能控制设备有限公司 | Mortar transfer device |
CN102393164A (en) * | 2011-10-31 | 2012-03-28 | 江西佳联科技有限公司 | Quantitative explosive feeding device |
CN111412457A (en) * | 2020-03-27 | 2020-07-14 | 江苏理文造纸有限公司 | Can effectively reduce NOXVented boiler |
CN111412457B (en) * | 2020-03-27 | 2022-04-19 | 江苏理文造纸有限公司 | Can effectively reduce NOXVented boiler |
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