JPH0448697B2 - - Google Patents
Info
- Publication number
- JPH0448697B2 JPH0448697B2 JP17214983A JP17214983A JPH0448697B2 JP H0448697 B2 JPH0448697 B2 JP H0448697B2 JP 17214983 A JP17214983 A JP 17214983A JP 17214983 A JP17214983 A JP 17214983A JP H0448697 B2 JPH0448697 B2 JP H0448697B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- dust
- mixing ratio
- flow rate
- granules
- 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
- 239000000843 powder Substances 0.000 claims description 19
- 239000008187 granular material Substances 0.000 claims description 13
- 238000011084 recovery Methods 0.000 claims description 5
- 239000000428 dust Substances 0.000 description 23
- 239000007789 gas Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000004482 other powder Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
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
- B65G53/66—Use of indicator or control devices, e.g. for controlling gas pressure, for controlling proportions of material and gas, for indicating or preventing jamming of material
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Air Transport Of Granular Materials (AREA)
- Cyclones (AREA)
Description
【発明の詳細な説明】
この発明は粉粒体の回収装置に係り、特に回収
効率を高めようとした装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a collection device for powder and granular materials, and particularly to a device intended to improve collection efficiency.
例えば発電所用大型ボイラにおいては燃焼ガス
中の灰分をはじめとするダストを除去するために
集塵装置を設けているが、この外に、脱硝装置、
節炭器、空気予熱器等においてもホツパ部を形成
しダストを慣性により除去しようとしている。こ
れら集塵器および各ホツパ部で集められた粉粒体
たるダストは回収装置によりサイロ等の集積部に
集められることになる。ダストの回収は各装置の
ホツパ部および集塵器のホツパ部に接続した管路
を経てサイクロン分離器側に吸引され集積部に集
中される。従来、この回収は真空ブロワ(吸引形
のブロワ)を一定の回転数で運転し、回収ライン
の真空度を検出し、この真空度に対応して各ホツ
パ部のダンパの開度を調節することにより制御し
ていた。しかしこの方法では空気流量の制御の幅
が狭く混合比(回収粉粒体量/搬送空気質量)を
一定にするのが困難である。混合比が増加すると
搬送空気量不足のためダスト回収時間が増加しか
つライン中でのダストの閉塞の虞れも生じる。一
方混合比が低下するとライン中の気体の速度が設
定値よりも高くなり、ライン中の摩耗が激しくな
る。 For example, large boilers for power plants are equipped with dust collectors to remove ash and other dust from the combustion gas, but in addition to this, denitrification equipment,
Hoppers are also formed in energy savers, air preheaters, etc. to remove dust by inertia. The dust collected in these dust collectors and each hopper section is collected in a collection section such as a silo by a collection device. The dust is collected through the hopper section of each device and the pipe line connected to the hopper section of the dust collector, and is sucked into the cyclone separator side and concentrated in the collection section. Conventionally, this recovery was done by operating a vacuum blower (suction type blower) at a constant rotation speed, detecting the degree of vacuum in the recovery line, and adjusting the opening degree of the damper in each hopper section in accordance with this degree of vacuum. It was controlled by. However, in this method, the control range of the air flow rate is narrow, and it is difficult to keep the mixing ratio (amount of recovered powder/granular material/mass of conveyed air) constant. When the mixing ratio increases, the dust recovery time increases due to the insufficient amount of conveying air, and there is also a risk of dust clogging in the line. On the other hand, when the mixing ratio decreases, the gas velocity in the line becomes higher than the set value, and wear in the line increases.
この発明の目的は上述した問題点に鑑み、常時
適正な混合比となるよう構成した粉粒体回収装置
を提供することにある。 SUMMARY OF THE INVENTION In view of the above-mentioned problems, an object of the present invention is to provide a powder and granular material recovery device that is configured to maintain a proper mixing ratio at all times.
要するにこの発明は各ホツパから排出される粉
粒体の量と、粉粒体分離後の気体の流量を検知す
ることにより粉粒体を含有する気体の混合比を算
出し、これに対応して真空ブロワの回転数を制御
して常時適正な混合比となるよう構成したもので
ある。 In short, this invention calculates the mixing ratio of the gas containing the powder by detecting the amount of powder and granules discharged from each hopper and the flow rate of gas after separating the powder and granules. The rotation speed of the vacuum blower is controlled so that an appropriate mixing ratio is maintained at all times.
以下この発明の実施例を説明する。 Examples of the present invention will be described below.
第1図において、1,2,3,4は集塵器、節
炭器、脱硝装置等に取り付けたダスト用のホツパ
であり、各ホツパ内には捕集したダストが入つて
いる。5は粉粒体輸送管路、6,7,8,9はこ
の管路に設けたエゼクタであり、各ホツパ1ない
し4と管路接続し、ホツパ内のダストを気流輸送
する。10,11,12,13は各ホツパから排
出されるダストの量を計測する計測器であり、こ
れら計測器は記憶と指令信号を発する制御箱14
に信号回路にとよつて接続している。15はサイ
クロン分離器、17はサイクロン分離器に取り付
けたダスト貯槽、16はサイクロン分離器15に
おいてダストを分離した空気を吸引する空気管
路、18はこの空気管路に設けた真空ブロワ、1
9はやはりこの管路に設けた流量計である。前記
制御箱14はこの流量計19の信号を入力し、か
つ真空ブロワ18のモータ18aの回転数制御を
するよう両者と信号回路により接続している。 In FIG. 1, 1, 2, 3, and 4 are dust hoppers attached to a dust collector, a carbon saver, a denitrification device, etc., and each hopper contains collected dust. Reference numeral 5 denotes a powder transport pipe, and numerals 6, 7, 8, and 9 designate ejectors provided in this pipe, which are connected to each of the hoppers 1 to 4 to transport the dust in the hopper with air flow. 10, 11, 12, and 13 are measuring instruments that measure the amount of dust discharged from each hopper, and these measuring instruments are connected to a control box 14 that stores and issues command signals.
is connected to the signal circuit. 15 is a cyclone separator; 17 is a dust storage tank attached to the cyclone separator; 16 is an air pipe line for sucking the air from which dust has been separated in the cyclone separator 15; 18 is a vacuum blower provided in this air pipe line;
9 is a flow meter provided in this conduit. The control box 14 receives the signal from the flowmeter 19 and is connected to both of them by a signal circuit so as to control the rotational speed of the motor 18a of the vacuum blower 18.
以上の構成の装置において、制御箱14に対し
ては各ダスト計測器10ないし13からのダスト
排出量が入力される。一方流量計19からはサイ
クロン分離器15においてダストを分離した空気
の流量が入力し、前記ダスト排出量とこの空気流
量とによりサイクロン分離器15の上流側の粉粒
体輸送管路5内の気体の混合比を算出する。この
演算の結果に基づいて制御箱14は真空ブロワ1
8の回転数制御を行い吸収すべき空気量を調節
し、これによつて粉粒体輸送管路5内の混合比を
適正な値に保持する。なお、サイクロン分離器1
5によつて分離されたダストはダスト貯槽17内
に貯蔵され、適宜排出処理される。 In the apparatus having the above configuration, the amount of dust discharged from each of the dust measuring devices 10 to 13 is input to the control box 14. On the other hand, the flow rate of the air from which dust has been separated in the cyclone separator 15 is inputted from the flow meter 19, and the gas in the powder transport pipe 5 on the upstream side of the cyclone separator 15 is determined by the amount of dust discharged and this air flow rate. Calculate the mixing ratio of Based on the result of this calculation, the control box 14 controls the vacuum blower 1.
8 to adjust the amount of air to be absorbed, thereby maintaining the mixing ratio in the powder transport pipe 5 at an appropriate value. In addition, cyclone separator 1
The dust separated by 5 is stored in a dust storage tank 17 and discharged as appropriate.
以上排ガスから捕集したダストを例に説明した
がこれに限るものではなく他の粉粒体に対しても
もとより効果的に実施できる。 Although the above description has been made using dust collected from exhaust gas as an example, the present invention is not limited to this, and can be carried out more effectively on other powder or granular materials.
この発明を実施することにより粉粒体を供給す
るライン中の混合比を常時適正に保持することが
できてラインの閉塞を防止すると共にラインの摩
耗も大幅に減少させる。 By carrying out this invention, the mixing ratio in the line for supplying powder and granules can be maintained at an appropriate level at all times, thereby preventing clogging of the line and greatly reducing wear on the line.
第1図はこの発明に係る装置の系統図である。
5……粉粒体輸送管路、10,11,12,1
3……粉粒体計測器、14……制御箱、15……
サイクロン分離器、18……真空ブロワ、19…
…流量計測器。
FIG. 1 is a system diagram of an apparatus according to the present invention. 5... Powder transport pipe, 10, 11, 12, 1
3... Powder measuring instrument, 14... Control box, 15...
Cyclone separator, 18... Vacuum blower, 19...
...Flow meter.
Claims (1)
送しかつ分離器でこの粉粒体を分離するものにお
いて、粉粒体を排出する管路に粉粒体排出量を計
測する計測器を、分離器下流側の管路に対しては
気体の流量を計測する計測器を各々設け、粉粒体
の排出量と気体の流量から求めた混合比に基づき
真空ブロワの回転数を制御し、粉粒体輸送管路内
の混合比を適正に保持するよう構成したことを特
徴とする粉粒体回収装置。 2 前記制御を記憶と指令信号を発する制御箱に
より行うことを特徴とする特許請求の範囲第1項
記載の粉粒体回収装置。[Scope of Claims] 1. In an apparatus in which powder and granules are sucked by a vacuum blower and transported by air flow, and the powder and granules are separated by a separator, the amount of powder and granules discharged is A measuring device is installed to measure the flow rate of the vacuum blower, and a measuring device to measure the gas flow rate is installed in the piping downstream of the separator, and the vacuum blower is adjusted based on the mixing ratio determined from the amount of powder discharged and the gas flow rate. A powder and granular material collection device characterized by being configured to control the rotation speed and maintain an appropriate mixing ratio in a powder and granular material transport pipe. 2. The powder and granular material recovery device according to claim 1, wherein the control is performed by a control box that stores and issues command signals.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17214983A JPS6067325A (en) | 1983-09-20 | 1983-09-20 | Granular powder collecting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17214983A JPS6067325A (en) | 1983-09-20 | 1983-09-20 | Granular powder collecting device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6067325A JPS6067325A (en) | 1985-04-17 |
| JPH0448697B2 true JPH0448697B2 (en) | 1992-08-07 |
Family
ID=15936469
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17214983A Granted JPS6067325A (en) | 1983-09-20 | 1983-09-20 | Granular powder collecting device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6067325A (en) |
Families Citing this family (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2651812B2 (en) * | 1987-08-12 | 1997-09-10 | 株式会社 松井製作所 | Metering, mixing, and transporting equipment for powders and granules |
| GB0512998D0 (en) * | 2005-06-27 | 2005-08-03 | Inbulk Technologies Ltd | Pneumatic conveying velocity control device |
| US7171913B1 (en) * | 2006-02-24 | 2007-02-06 | Amvac Chemical Corporation | Self-calibrating meter with in-meter diffuser |
| ITVR20070083A1 (en) | 2007-06-12 | 2008-12-13 | Moretto Spa | PLANT FOR PNEUMATIC TRANSPORT AT CONTROLLED SPEED OF GRANULAR MATERIAL AND PROCEDURE FOR THE CONTROL OF CONVEYANCE SPEED |
| KR100883272B1 (en) | 2007-08-03 | 2009-02-11 | 고등기술연구원연구조합 | Powder mixing device using fixed quantity conveyor |
| US8764350B2 (en) * | 2008-06-05 | 2014-07-01 | Alstom Technology Ltd | Conveyor for transporting powder, and a method for conveying powder |
| CN102152972B (en) * | 2011-03-24 | 2012-12-05 | 克莱德贝尔格曼华通物料输送有限公司 | Positive pressure pneumatic conveying system and method |
| CN102491093B (en) * | 2011-12-07 | 2014-03-26 | 克莱德贝尔格曼华通物料输送有限公司 | Positive pressure pneumatic transmission system and method |
| CN102815536B (en) * | 2012-08-30 | 2015-04-08 | 山东华建仓储装备科技有限公司 | Pneumatic lifting system and usage thereof |
| JPWO2014155655A1 (en) * | 2013-03-29 | 2017-02-16 | 株式会社松井製作所 | Material transport device and material transport method |
| JP2016023002A (en) * | 2014-07-16 | 2016-02-08 | Ihi運搬機械株式会社 | Cargo handling amount control device for pneumatic unloader |
| JP2016023004A (en) * | 2014-07-16 | 2016-02-08 | Ihi運搬機械株式会社 | Pneumatic unloader cargo handling display adjustment device |
| JP2016023005A (en) * | 2014-07-16 | 2016-02-08 | Ihi運搬機械株式会社 | Cargo handling amount detection device for pneumatic unloader |
| JP6341782B2 (en) * | 2014-07-16 | 2018-06-13 | Ihi運搬機械株式会社 | Pneumatic unloader power requirement controller |
| JP6341781B2 (en) * | 2014-07-16 | 2018-06-13 | Ihi運搬機械株式会社 | Pneumatic unloader cargo handling control device |
| CN105380291A (en) * | 2015-12-07 | 2016-03-09 | 广东生和堂健康食品股份有限公司 | Automatic material boiling system |
| US20200282652A1 (en) * | 2017-11-11 | 2020-09-10 | Hewlett-Packard Development Company, L.P. | Flow control in a pneumatic build material transport system |
-
1983
- 1983-09-20 JP JP17214983A patent/JPS6067325A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6067325A (en) | 1985-04-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH0448697B2 (en) | ||
| CN103884616B (en) | SCR catalyst tear strength proving installation | |
| CN107055099B (en) | Dense-phase conveying method and system for urea particles | |
| CN116513809A (en) | Positive and negative pressure combined conveying system for pebble coal of medium-speed coal mill | |
| CN206152623U (en) | Living beings flue gas multi -stage purification processing apparatus | |
| CN1289652A (en) | Quickly loaded separating system of powdered coal ash | |
| CN204086056U (en) | SCR catalyst tear strength proving installation | |
| CN111841176A (en) | A dust collector | |
| CN217248007U (en) | Novel indirect multiple spot feed of sodium bicarbonate device | |
| CN205328232U (en) | Device is failed to improved generation sodium bicarbonate collection | |
| CN212881505U (en) | Dust removal ash recovery device | |
| JP3605224B2 (en) | Granular material transport device | |
| JPH08200646A (en) | Equipment for pneumatic transportation of fly ash of refuse incinerator | |
| CN202844805U (en) | Acetylene slag recovery system applied to dry acetylene production | |
| JPS6061060A (en) | Method for increasing separation efficency of cyclone and cyclone type separator | |
| SU1164172A1 (en) | Method of pneumatic transportation of poweder-like and fine-grained materials and device for effecting same | |
| CN114955554A (en) | Powder production conveying system | |
| CN217200834U (en) | Active carbon conveyer in hazardous waste burns flue gas treatment | |
| CN1281549A (en) | Method and device for continuous dosing | |
| CN206746837U (en) | High pressure sealing baffle system | |
| JPS60223914A (en) | Adjusting device of pulverized coal-air ratio of pulverized coal manufacturing device | |
| CN218393088U (en) | Calcium-based dry desulfurization system for treating coking flue gas | |
| JPS62264121A (en) | Pneumatic transportation equipment for powder | |
| CN111365724A (en) | Smoke duct system and method for preventing horizontal section from accumulating dust | |
| CN212999110U (en) | Flue gas dust removal system and flue gas dust removal control system |