JPS62723A - Pulverized coal feeding device - Google Patents
Pulverized coal feeding deviceInfo
- Publication number
- JPS62723A JPS62723A JP13904285A JP13904285A JPS62723A JP S62723 A JPS62723 A JP S62723A JP 13904285 A JP13904285 A JP 13904285A JP 13904285 A JP13904285 A JP 13904285A JP S62723 A JPS62723 A JP S62723A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- pulverized coal
- coal
- pulverized
- fed
- 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
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、原動機製品である産業用ボイラ又は各種燃焼
炉を装備した工場設備における微粉炭供給誌晋f藺子ス
−
備において、燃料に微粉炭を使用しようとする場合、そ
の微粉炭製造設備は高価で小容量向きではないため、工
場内の一個所で微粉炭を製造し、複数の微粉炭消費手段
に供給できれば便利である。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is directed to the use of pulverized coal as fuel in pulverized coal supply system in factory equipment equipped with industrial boilers or various combustion furnaces, which are prime mover products. When attempting to use pulverized coal, the pulverized coal production equipment is expensive and not suitable for small volumes, so it would be convenient if pulverized coal could be produced at one location within the factory and supplied to multiple pulverized coal consumption means.
しかるに、微粉炭は製造後は粉じん爆発を起し易い危険
物であることから、従来は適当な高安全度システムがな
く、このため微粉炭の使用には制約があった。However, since pulverized coal is a dangerous substance that is likely to cause a dust explosion after production, there has been no suitable high safety system in the past, and this has placed restrictions on the use of pulverized coal.
発明が解決しようとする問題点
そこで、本発明は、高度に安全化された微粉炭の集中製
造、供給システムを提供して、多数の比較的小容量の分
散された微粉炭消費手段を持つ工場設備(たとえば、製
油所、石油化学プラント等)においても微粉炭の採用が
容易に行なえるようにすることを目的とする。Problems to be Solved by the Invention Therefore, the present invention provides a highly secure centralized production and supply system for pulverized coal to enable a factory with a large number of relatively small volume decentralized pulverized coal consumption means. The purpose is to facilitate the adoption of pulverized coal in facilities (for example, refineries, petrochemical plants, etc.).
問題点を解決するだめの手段
本発明による微粉炭供給装置は、低酸素ガス発生炉と、
同低酸素ガス発生炉で生成され所定温度に調節された低
酸素ガスが供給される微粉炭機と、同微粉炭機から気体
搬送により送られる微粉炭を。Means for Solving the Problems The pulverized coal supply device according to the present invention includes a low oxygen gas generating furnace,
A pulverized coal machine is supplied with low-oxygen gas generated in the same low-oxygen gas generating furnace and adjusted to a predetermined temperature, and pulverized coal is sent from the same pulverized coal machine by gas transport.
気体から分離する分離器と、同分離器で分離された微粉
炭を所定量貯える第1の微粉炭ピンと、同第1の微粉炭
ビンに貯えられた微粉炭が前記分離器で分離された気体
の少なくとも一部で気体搬送により供給され、この供給
された微粉炭を気体から分離して貯えるとともに気体を
排出する、微粉炭消費手段の近くに設けられた第2の微
粉炭ビンとを具備する。A separator that separates the pulverized coal from the gas, a first pulverized coal pin that stores a predetermined amount of pulverized coal separated by the separator, and a gas that is separated from the pulverized coal stored in the first pulverized coal bin by the separator. a second pulverized coal bin provided near the pulverized coal consumption means, which is supplied at least in part by gas conveyance, and which stores the supplied pulverized coal separately from the gas and discharges the gas. .
作用
このような手段によれば、微粉炭の集中製造及び各消費
手段への配分、移送はすべて低酸素雰囲気の下に行なわ
れ、爆発限界からはずれることから、高度な安全性が達
成される。Operation: According to such a means, a high degree of safety is achieved because the centralized production of pulverized coal, its distribution to each consuming means, and its transfer are all carried out in a low-oxygen atmosphere and are outside the explosive limits.
実施例
以下図面を参照して本発明の一実施例について詳述する
。EXAMPLE Hereinafter, an example of the present invention will be described in detail with reference to the drawings.
単一の図面において、石炭バンカ1に貯蔵された塊炭は
、フィーダ2によって必要量だけ微粉炭機3へ供給され
る。乾燥した微粉炭を得るための乾燥用熱ガスは、低酸
素ガス発生炉4で生成される。すなわち、このガス発生
炉4には、燃料(重油)タンク5から燃料がポンプ6及
び調節弁7を通してまた空気が送風機8及び調節ダンパ
9を通して夫々供給されて燃焼され、高温の低酸素ガス
が生成される。その必要なガス量は、燃料調節弁7及び
空気調節ダンパ9で調節され、必要量だけ生成される。In a single figure, lump coal stored in a coal bunker 1 is fed by a feeder 2 to a pulverizer 3 in the required amount. A drying hot gas for obtaining dry pulverized coal is generated in a low-oxygen gas generating furnace 4. That is, fuel is supplied from a fuel (heavy oil) tank 5 through a pump 6 and a regulating valve 7, and air is supplied through a blower 8 and a regulating damper 9 to the gas generating furnace 4, and the gas is combusted to produce high-temperature, low-oxygen gas. be done. The required amount of gas is regulated by the fuel control valve 7 and the air control damper 9, and only the required amount is generated.
このガス発生炉出口のガス温度は高温すぎるため、必要
量の低温ガスが、微粉炭と排ガスとを分離するサイクロ
ン分離器10及びバグフィルタ11の出口から、ガス循
環ダンパ12により調節されて、循環ブロワ13により
かかる高温ガスに混入される。微粉炭機3で製造された
微粉炭は前述したサイクロン分離機10で排ガスから分
離される。さらに、この排ガス中に含まれる微粉炭がバ
グフィルタ11で分離され、システムで再使用の必要の
あるガスを除いた残シガスはダンパ14を通して大気中
へ放出される。Since the gas temperature at the outlet of the gas generating furnace is too high, the required amount of low-temperature gas is regulated by the gas circulation damper 12 from the outlet of the cyclone separator 10 and bag filter 11 that separate the pulverized coal and exhaust gas, and is circulated. The blower 13 mixes the high temperature gas. The pulverized coal produced by the pulverized coal machine 3 is separated from the exhaust gas by the cyclone separator 10 described above. Furthermore, the pulverized coal contained in this exhaust gas is separated by a bag filter 11, and the remaining gas, excluding gas that needs to be reused in the system, is discharged into the atmosphere through a damper 14.
一方、分離器10でガスと分離された微粉炭は、ダンパ
15を通してピン16へ落下する。このピン内の微粉炭
が一部レベルまで貯ったことをレベル検出器17が検出
すると、ダンパ15を締め、また他のダンパ18を開き
、ガス圧縮機19により1〜2気圧に圧縮された分離器
10からのガスをピン16内へ供給すると同時に、圧送
ダンパ20を開けば、微粉炭はガスに圧送され、微粉炭
製造設備から離れた位置にある複数の微粉炭ビン21へ
投入される。第1の微粉炭ビン16における一連の圧送
操作は、調節器22で制御される。On the other hand, the pulverized coal separated from the gas in the separator 10 passes through the damper 15 and falls onto the pin 16. When the level detector 17 detects that the pulverized coal in this pin has partially accumulated to a certain level, the damper 15 is tightened, the other damper 18 is opened, and the pulverized coal is compressed to 1 to 2 atmospheres by the gas compressor 19. When the gas from the separator 10 is supplied into the pin 16 and the pressure damper 20 is opened at the same time, the pulverized coal is pumped into the gas and thrown into a plurality of pulverized coal bins 21 located away from the pulverized coal manufacturing equipment. . The series of pumping operations in the first pulverized coal bin 16 is controlled by a regulator 22 .
そして、第2の微粉炭ビン21へ投入された微粉炭は、
ガス/微粉炭比が小さく、高濃度のため、ガスと容易に
分離し、ピン21に貯まる。これらのピン21内の微粉
炭量は夫々レベル検出器23により検出され、これによ
り微粉炭製造システム制御器24による微粉炭製造設備
の微粉炭製造量制御の入力信号が得られる。Then, the pulverized coal put into the second pulverized coal bin 21 is
Since the gas/pulverized coal ratio is small and the concentration is high, it is easily separated from the gas and accumulated in the pin 21. The amount of pulverized coal in these pins 21 is detected by a level detector 23, and thereby an input signal for controlling the amount of pulverized coal produced by the pulverized coal production equipment by a pulverized coal production system controller 24 is obtained.
これらのピン21に貯められた微粉炭は、それから、消
費手段である複数のボイラ又は燃焼炉25ヘフイーダ2
6を通して各個に供給される。この供給は、送風機27
及び調節ダンパ28を通して送られてくる空気による搬
送によっておこなわれる。The pulverized coal stored in these pins 21 is then sent to a plurality of boilers or combustion furnaces 25 and feeders 2 as consumption means.
6 to each individual. This supply is connected to the blower 27
This is carried out by air conveyance sent through the adjustment damper 28.
なお、29はと721内において微粉炭から分離された
ガスが大気中へ放出される前に通過するバグフィルタで
ある。Note that 29 is a bag filter through which the gas separated from the pulverized coal in the chamber 721 passes before being released into the atmosphere.
しかして、このような微粉炭供給システムにおいては、
その微粉炭機3から微粉炭消費手段25の近くに設けら
れている微粉炭ビン21にいたるシステム全体がガス発
生炉4から供給される低酸素ガスによって満されるため
、微粉炭は爆発限界に達し得す、安全に保たれる。However, in such a pulverized coal supply system,
Since the entire system from the pulverizer 3 to the pulverized coal bin 21 installed near the pulverized coal consumption means 25 is filled with low-oxygen gas supplied from the gas generator 4, the pulverized coal reaches the explosive limit. It can be achieved and it can be kept safe.
発明の効果
以上詳述したように、本発明によれば、微粉炭供給シス
テムがすべてガス発生炉で発生する低酸゛素ガスで満さ
れ、かつシステム全体は大気圧よりわずか高い圧力に保
たれるため、外部からの空気の侵入も起シ得ない。した
がって、システム内の微粉炭は爆発限界に達し得す、安
全である。このように安全性が確保されることによって
、高価な設備である微粉炭製造設備を1個所に集中せし
め、工場設備内に点在する各微粉炭消費手段へ安全に微
粉炭を供給することが可能となり、工場設備の石炭転換
への可能性が大きく向上するものである。Effects of the Invention As detailed above, according to the present invention, the pulverized coal supply system is entirely filled with low oxygen gas generated in the gas generating furnace, and the entire system is maintained at a pressure slightly higher than atmospheric pressure. Therefore, there is no possibility of air intrusion from outside. Therefore, the pulverized coal in the system can reach explosive limits and is safe. By ensuring safety in this way, it is possible to centralize expensive pulverized coal manufacturing equipment in one location and safely supply pulverized coal to various pulverized coal consumption means scattered within the factory equipment. This will greatly improve the possibility of converting factory equipment to coal.
図面は、本発明による微粉炭供給装置の一例を示す系統
図である。
3・・微粉炭機、4・・低酸素ガス発生炉、10・・分
離器、16・・第1の微粉炭ビン、21・・(ほか7名
)The drawing is a system diagram showing an example of a pulverized coal supply device according to the present invention. 3. Pulverized coal machine, 4. Low oxygen gas generator, 10. Separator, 16. First pulverized coal bin, 21. (7 others)
Claims (1)
定温度に調節された低酸素ガスが供給される微粉炭機と
、同微粉炭機から気体搬送により送られる微粉炭を気体
から分離する分離器と、同分離器で分離された微粉炭を
所定量貯える第1の微粉炭ビンと、同第1の微粉炭ビン
に貯えられた微粉炭が前記分離器で分離された気体の少
なくとも一部で気体搬送により供給され、この供給され
た微粉炭を気体から分離して貯えるとともに気体を排出
する、微粉炭消費手段の近くに設けられた第2の微粉炭
ビンとを具備する微粉炭供給装置。A low-oxygen gas generating furnace, a pulverized coal machine to which low-oxygen gas generated in the low-oxygen gas generating furnace and adjusted to a predetermined temperature is supplied, and the pulverized coal sent from the pulverized coal machine by gas conveyance is separated from the gas. a first pulverized coal bin that stores a predetermined amount of pulverized coal separated by the separator; and a first pulverized coal bin that stores at least a predetermined amount of pulverized coal separated by the separator. a second pulverized coal bin provided in the vicinity of the pulverized coal consumption means, which is partially supplied by gas conveyance and which stores the supplied pulverized coal separately from the gas and discharges the gas; Feeding device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13904285A JPS62723A (en) | 1985-06-27 | 1985-06-27 | Pulverized coal feeding device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13904285A JPS62723A (en) | 1985-06-27 | 1985-06-27 | Pulverized coal feeding device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62723A true JPS62723A (en) | 1987-01-06 |
Family
ID=15236097
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13904285A Pending JPS62723A (en) | 1985-06-27 | 1985-06-27 | Pulverized coal feeding device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62723A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102798132A (en) * | 2011-05-27 | 2012-11-28 | 中国电力工程顾问集团东北电力设计院 | Fan mill front counter flow type furnace-smoke drying dewatering direct blowing pulverization system |
CN102798133A (en) * | 2011-05-27 | 2012-11-28 | 中国电力工程顾问集团东北电力设计院 | Fan grinding hot blast powder feeding and pulverizing system utilizing flue gas drying and water recycling |
-
1985
- 1985-06-27 JP JP13904285A patent/JPS62723A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102798132A (en) * | 2011-05-27 | 2012-11-28 | 中国电力工程顾问集团东北电力设计院 | Fan mill front counter flow type furnace-smoke drying dewatering direct blowing pulverization system |
CN102798133A (en) * | 2011-05-27 | 2012-11-28 | 中国电力工程顾问集团东北电力设计院 | Fan grinding hot blast powder feeding and pulverizing system utilizing flue gas drying and water recycling |
CN102798132B (en) * | 2011-05-27 | 2015-04-01 | 中国电力工程顾问集团东北电力设计院 | Fan mill front counter flow type furnace-smoke drying dewatering direct blowing pulverization system |
CN102798133B (en) * | 2011-05-27 | 2015-06-17 | 中国电力工程顾问集团东北电力设计院 | Fan grinding hot blast powder feeding and pulverizing system utilizing flue gas drying and water recycling |
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