JPH07228878A - Apparatus for controlling kneading of coal/water mixture - Google Patents

Apparatus for controlling kneading of coal/water mixture

Info

Publication number
JPH07228878A
JPH07228878A JP2440994A JP2440994A JPH07228878A JP H07228878 A JPH07228878 A JP H07228878A JP 2440994 A JP2440994 A JP 2440994A JP 2440994 A JP2440994 A JP 2440994A JP H07228878 A JPH07228878 A JP H07228878A
Authority
JP
Japan
Prior art keywords
coal
kneading
water mixture
cwp
water
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
Application number
JP2440994A
Other languages
Japanese (ja)
Inventor
Hiroshi Takezaki
博 武▲崎▼
Susumu Yoshioka
進 吉岡
Yoshinori Otani
義則 大谷
Kazunori Satou
一教 佐藤
Katsuya Oki
勝弥 大木
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP2440994A priority Critical patent/JPH07228878A/en
Publication of JPH07228878A publication Critical patent/JPH07228878A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a kneading controller capable of efficiently kneading a mixture (CWP) of homogeneous coal with water, excellent in responsiveness and capable of carrying out control of its properties. CONSTITUTION:Crushed coal B is fed to a kneader 118 and a controlling agent C (either one or both of water and pulverized coal) is fed through the interior of a hollow rotating shaft 2 from a discharge hole 4. When the properties of CWP are detected in a CWP feed pipe and kneading and control of CWP are carried out, CWP torque detecting means is provided on the rotating shaft 2 and the controlling agent C is fed from the discharge hole 4 on the rotating shaft 2 side on the upstream side of a CWP kneading part to CWP kneading part to carry out property control of CWP. When the rotating shaft 2 having an agitating blade 127 mainly kneading the mixture and the rotating shaft 2 not shown in the figure and driving a means for detecting agitating torque of the mixture are respectively independently provided, stable control having good responsiveness can be carried out, because resistance loaded by the agitating blade 127 does not become a factor changing an agitating torque value in a torque detecting part.

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・水混合物を製造
し、供給する技術に係り、特に、燃焼炉に安定して供給
できる石炭・水ペースト状燃料の混練調整装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for producing and supplying a coal / water mixture, and more particularly to a kneading / adjusting device for coal / water paste fuel which can be stably supplied to a combustion furnace.

【0002】[0002]

【従来の技術】石炭を加圧流動層ボイラで燃焼し、蒸気
を発生させて蒸気タービンにより発電するとともに、加
圧流動層ボイラの流動層火炉で発生した高圧、高温の燃
焼ガスでガスタービンを駆動させて発電する加圧流動層
ボイラ複合発電プラントが知られている。加圧流動層ボ
イラの流動層火炉への石炭の供給方法として、石炭粒子
と水を混合してペースト状の流体(以下、oal−
ater aste;CWPと略す)とし、該CWP
をポンプで昇圧及び圧送して流動層火炉の噴霧ノズルに
供給する湿式供給方式がある。しかしながら、該CWP
中の水分は高い発電効率を維持する上で、できるだけ少
なくすることが必要である。添加水量が制限されたCW
Pは粘度が高く、しかも製造コスト低減のために石炭粒
子分散用の薬剤を添加しないので流動性に乏しいという
問題がある。流動性のよいCWPを得るためには、水分
調整だけでなく、粒度構成の調整も重要である。つま
り、流動性のよいCWPを得るためには、CWP中の石
炭粒子は数十μmの微粒子から最大10mm程度の粗粒
子までの幅広い粒径範囲で存在させる必要がある。
2. Description of the Related Art Coal is burned in a pressurized fluidized bed boiler to generate steam for power generation by a steam turbine, and a high pressure, high temperature combustion gas generated in a fluidized bed furnace of the pressurized fluidized bed boiler is used to generate a gas turbine. A pressurized fluidized bed boiler combined cycle power plant that drives and generates power is known. As the method of supplying coal to the fluidized bed furnace of pressurized fluid Doso boiler, a mixture of coal particles and water pasty fluid (hereinafter, C oal- W
ater P aste; abbreviated as CWP)
There is a wet supply method in which the pressure is increased and pumped by a pump to supply it to a spray nozzle of a fluidized bed furnace. However, the CWP
It is necessary to reduce the water content in the water as much as possible in order to maintain high power generation efficiency. CW with limited amount of added water
P has a problem that it has a high viscosity and is poor in fluidity because a chemical for dispersing coal particles is not added in order to reduce the manufacturing cost. In order to obtain a CWP having good fluidity, not only the water content adjustment but also the particle size composition adjustment is important. That is, in order to obtain a CWP having good fluidity, it is necessary that the coal particles in the CWP exist in a wide range of particle sizes from fine particles of several tens of μm to coarse particles of maximum 10 mm.

【0003】上記のような制約下でCWPを安定に輸送
するためには、CWPの粘度は5Pa・sから20Pa
・sの範囲に調整することが望ましい。CWPの粘度が
20Pa・s以上ではポンプの吸込口でCWPの閉塞及
び水分離現象が起こりやすく、ポンプでCWPを吸えな
いという問題がある。一方、CWPの粘度が5Pa・s
より低い場合、粗粒子が沈降し、配管内で閉塞する問題
がある。CWP中の水分量と石炭の粒度構成はCWPの
粘度への影響因子であり、それらによって、得られる粘
度が大きく変わる。したがって、CWPの性状を調整す
るにはCWP中の水分量と粒度構成を調整すれば良いこ
とになる。
In order to stably transport CWP under the above constraints, the viscosity of CWP is 5 Pa · s to 20 Pa.
・ It is desirable to adjust to the range of s. When the viscosity of CWP is 20 Pa · s or more, there is a problem that the CWP is likely to be clogged and water separation phenomenon occurs at the suction port of the pump, and the CWP cannot be sucked by the pump. On the other hand, the viscosity of CWP is 5 Pa · s
If it is lower, there is a problem that coarse particles settle and block in the pipe. The amount of water in the CWP and the particle size composition of the coal are factors that affect the viscosity of the CWP, and the viscosity obtained thereby greatly changes. Therefore, in order to adjust the properties of CWP, it is sufficient to adjust the water content and particle size composition in CWP.

【0004】CWPの製造方法としては、図11に示す
ように混練装置118の原料投入口128より、粉砕炭
B、水Dおよび脱硫剤Eを供給し、モータ126により
駆動する撹拌羽根127で前記原料を混練する。混練後
の石炭・水ペースト(CWP)は堰130を越えてシュ
ート129より貯留タンク(図示省略)へ送られる(特
開昭62−155433号等参照)。また、CWPを製
造して加圧流動層ボイラに供給する際のCWP性状の調
整方法として、従来、図12に示すように貯留タンク1
22と油圧装置125によって駆動するCWP供給ポン
プ124の間のCWP流路1内の中空回転軸2にCWP
のトルク検出器7を設け、検出された撹拌トルク値に応
じて制御装置12により貯留タンク122の導管の管壁
から水または微粉炭または微粉炭スラリの供給量を調整
しながら供給し、混練する方法が提案されている(特願
平5−67026号参照)。
As a method for producing CWP, as shown in FIG. 11, pulverized coal B, water D and desulfurizing agent E are supplied from a raw material inlet 128 of a kneading device 118, and a stirring blade 127 driven by a motor 126 is used to carry out the above-mentioned process. Knead the raw materials. The kneaded coal / water paste (CWP) is sent from a chute 129 to a storage tank (not shown) over the weir 130 (see Japanese Patent Laid-Open No. 62-155433). Further, as a method for adjusting the CWP property when manufacturing CWP and supplying it to the pressurized fluidized bed boiler, conventionally, as shown in FIG.
22 and the CWP supply pump 124 driven by the hydraulic device 125 to the hollow rotary shaft 2 in the CWP channel 1
The torque detector 7 is provided, and the control device 12 supplies water from the pipe wall of the conduit of the storage tank 122 while adjusting the supply amount of water or pulverized coal or pulverized coal slurry, and kneads the mixture. A method has been proposed (see Japanese Patent Application No. 5-67026).

【0005】[0005]

【発明が解決しようとする課題】しかしながら、CWP
の撹拌トルク値に応じて水、微粉炭等を混練する時に
は、CWPそのものの水分量が少なく粘度が高いため
に、微粒域の石炭粒子が水と混ざりにくく、石炭粒子と
水が均質に存在するCWPが製造できなかった。本発明
者らが特願平5−67026号で開示したCWP性状調
整装置を使用する場合にも、検出したCWPの撹拌トル
クに応じて水、微粉炭スラリなど(以下、調整剤とい
う)を供給するときのCWPの粘度が高いので調整剤は
CWP中に混合、分散されにくい。調整剤を効率よく混
合しようとすると多数の調整剤供給口を必要とし、調整
剤供給ラインが複雑になると共にコストが高くなるとい
う問題があった。また、CWPに供給した調整剤はCW
P流路管壁付近に偏在して、管路の中心にまでなかなか
到達せず、すみやかなCWPの性状改善効果が得られな
かった。その結果、調整剤供給口より後流のCWP流路
での撹拌トルクの検出の時間遅れが大きく、良好なCW
P性状の調整が行えなかった。また、検出値の時間的な
変動も大きく正確な検出が難しいという問題があった。
その結果、検出値の時間的な変動も大きく正確な検出が
難しいという問題があった。その結果、CWPの粘度が
極端に低下して供給ポンプ124内での閉塞を引き起こ
すという問題があった。本発明の目的は、均質な石炭と
水の混合物を効率良く混練し、その性状を調整する混練
調整装置を提供することにある。特に、CWPの性状を
CWP供給流路で検出して混練、調整する方法に対して
は、応答性に優れた性状調整の行える石炭・水混合物の
混練調整装置を提供することにある。
[Problems to be Solved by the Invention] However, CWP
When kneading water, pulverized coal, etc. according to the stirring torque value of, since the water content of CWP itself is low and the viscosity is high, the coal particles in the fine particle region are difficult to mix with water, and the coal particles and water are homogeneously present. CWP could not be manufactured. Even when the present inventors use the CWP property adjusting device disclosed in Japanese Patent Application No. 5-67026, water, pulverized coal slurry, etc. (hereinafter referred to as adjusting agent) are supplied according to the detected stirring torque of CWP. Since the viscosity of CWP at that time is high, the modifier is difficult to mix and disperse in CWP. When trying to mix the adjusting agent efficiently, a large number of adjusting agent supply ports are required, which causes a problem that the adjusting agent supply line becomes complicated and the cost increases. Also, the regulator supplied to the CWP is CW
It was unevenly distributed in the vicinity of the P channel pipe wall, and it did not easily reach the center of the pipe line, so that a quick CWP property improving effect could not be obtained. As a result, there is a large time delay in the detection of the stirring torque in the CWP flow path downstream of the adjusting agent supply port, and good CW is achieved.
The P property could not be adjusted. In addition, there is a problem that the detected value has a large temporal variation and it is difficult to accurately detect the value.
As a result, there has been a problem that the detected value has a large variation with time and accurate detection is difficult. As a result, there is a problem that the viscosity of the CWP is extremely lowered and causes blockage in the supply pump 124. An object of the present invention is to provide a kneading adjusting device for efficiently kneading a homogeneous mixture of coal and water and adjusting the properties thereof. In particular, for a method of detecting the properties of CWP in the CWP supply flow channel, and kneading and adjusting the properties, it is an object of the present invention to provide a kneading adjusting device for coal / water mixture which is capable of adjusting the properties with excellent responsiveness.

【0006】[0006]

【課題を解決するための手段】本発明の上記目的は次の
構成によって達成される。すなわち、石炭と水を混練し
て石炭・水混合物を調製する石炭・水混合物の混練調整
装置において、粉砕炭を供給する原料投入口を石炭・水
混合物の混練部の上流側に設け、中空構造の石炭・水混
合物混練用の回転軸の中空部先端に石炭・水混合物の性
状調整用の水と微粉炭スラリの少なくともいずれかから
なる調整剤を供給する調整剤供給導管を接続し、該中空
部内部に供給された調整剤を混練中または性状調整中の
石炭・水混合物中に流出させるための流出孔を回転軸表
面に設けた石炭・水混合物の混練調整装置である。上記
石炭・水混合物の混練調整装置の中空回転軸には流出孔
を混練部の上流側の領域にある中空回転軸側面に設け、
また、石炭・水混合物の混練用の撹拌羽根を設けること
ができる。
The above objects of the present invention can be achieved by the following constitutions. That is, in a coal / water mixture kneading adjusting device for kneading coal and water to prepare a coal / water mixture, a raw material charging port for supplying crushed coal is provided on the upstream side of the coal / water mixture kneading section, and has a hollow structure. At the tip of the hollow portion of the rotary shaft for kneading the coal / water mixture, a regulator supply conduit for supplying a regulator made of at least one of water and pulverized coal slurry for adjusting the properties of the coal / water mixture is connected, and the hollow It is a kneading / adjusting device for a coal / water mixture, which is provided with an outflow hole on the surface of a rotating shaft for letting out the adjusting agent supplied to the inside of the part into the coal / water mixture during kneading or property adjustment. The hollow rotating shaft of the coal / water mixture kneading adjusting device is provided with an outflow hole on the side surface of the hollow rotating shaft in the upstream region of the kneading section,
Further, a stirring blade for kneading the coal / water mixture can be provided.

【0007】本発明の上記目的は次の構成によって達成
される。すなわち、石炭と水を混練して石炭・水混合物
を調製する石炭・水混合物の混練調整装置において、粉
砕炭を供給する原料投入口を石炭・水混合物の混練部の
上流側に設け、中空構造の石炭・水混合物混練用の回転
軸の中空部先端に性状調整用の水と微粉炭スラリの少な
くともいずれかからなる調整剤を供給する調整剤供給導
管を接続し、該中空部内部に供給された調整剤を混練中
または性状調整中の石炭・水混合物中に流出させるため
の流出孔と石炭・水混合物混練用の撹拌羽根を回転軸表
面に設け、該撹拌羽根を用いて流送される石炭・水混合
物の撹拌トルクを検出するトルク検出器と、石炭・水混
合物のトルク検出値に応じて該中空回転軸の中空部を通
して行う調整剤の供給量を制御する調整剤供給量制御装
置を設けた石炭・水混合物の混練調整装置である。上記
石炭・水混合物の混練調整装置の中空回転軸には流出孔
を混練部の上流側の領域にある中空回転軸側面に設ける
ことができる。さらに、石炭・水混合物の混練調整装置
の中空回転軸は主に石炭・水混合物を混練するための撹
拌手段を備えた中空回転軸と主に石炭・水混合物の撹拌
トルク検出用の撹拌手段とを備えた中空回転軸をそれぞ
れ独立した構成とすることもできる。
The above object of the present invention is achieved by the following configurations. That is, in a coal / water mixture kneading adjusting device for kneading coal and water to prepare a coal / water mixture, a raw material charging port for supplying crushed coal is provided on the upstream side of the coal / water mixture kneading section, and has a hollow structure. At the tip of the hollow part of the rotary shaft for kneading the coal / water mixture, a conditioner supply conduit for supplying a conditioner containing at least one of water for property adjustment and pulverized coal slurry is connected, and the inside of the hollow part is supplied. An outlet hole for letting out the adjusting agent into the coal / water mixture during kneading or property adjustment, and a stirring blade for kneading the coal / water mixture are provided on the surface of the rotary shaft, and the mixture is fed using the stirring blade. A torque detector that detects the stirring torque of the coal / water mixture, and a regulator supply amount control device that controls the supply amount of the regulator through the hollow portion of the hollow rotary shaft according to the torque detection value of the coal / water mixture. Coal / water mixture provided A kneading adjustment device. The hollow rotary shaft of the coal / water mixture kneading adjusting device may be provided with an outflow hole on the side surface of the hollow rotary shaft in the upstream region of the kneading section. Further, the hollow rotating shaft of the coal / water mixture kneading adjusting device is mainly a hollow rotating shaft equipped with a stirring means for kneading the coal / water mixture and a stirring means mainly for detecting stirring torque of the coal / water mixture. The hollow rotary shafts provided with can also be independently configured.

【0008】[0008]

【作用】水分量の少ない石炭・水混合物は粘度が高く、
そもそも混練しにくい性状である。本発明によれば、こ
のような石炭・水混合物の高粘度状態において調整剤
(水や微粉炭スラリ)を、混練調整装置の回転する中空
回転軸表面の流出孔から周囲の石炭・水混合物中に効率
良く供給できる。さらに、供給された調整剤(水や微粒
スラリ)は前記流出孔の近傍に設置した撹拌羽根により
強制的に分散される。本発明は専ら石炭・水混合物を混
練する装置だけでなく、前記混練装置とCWPタンクと
の間またはCWPタンク直後のCWP供給導管部に設け
られたCWP性状を調整する調整装置に適用することも
できる。この場合には、以下のように作用する。
[Function] Coal / water mixture with low water content has high viscosity,
In the first place, it is difficult to knead. According to the present invention, in such a high viscosity state of the coal / water mixture, the adjusting agent (water or pulverized coal slurry) is introduced into the surrounding coal / water mixture through the outflow holes on the surface of the hollow rotating shaft of the kneading adjusting device which rotates. Can be supplied efficiently. Further, the supplied adjusting agent (water or fine particle slurry) is forcibly dispersed by a stirring blade installed near the outflow hole. The present invention can be applied not only to a device for kneading a coal / water mixture, but also to an adjusting device for adjusting the CWP property provided between the kneading device and the CWP tank or in the CWP supply conduit section immediately after the CWP tank. it can. In this case, it operates as follows.

【0009】前記供給導管内の石炭・水混合物の流れは
層流であり、該導管の中心部分では流速が最も大きくな
る。本発明によれば、中空の回転軸の内部からCWP供
給導管の中心部分へ調整剤が供給されるため、供給され
た調整剤は前記導管内の石炭・水混合物流れによって回
転軸上流側から下流側の方向へ推進力を得る。一方、調
整剤流出孔が回転軸と共に回転するため、回転軸の周囲
に効率よく調整剤を分散でき、調整剤流出孔を多数設け
たものと同等か、それ以上の混合効果が得られる。すな
わち、本発明では、従来法のようにCWP供給導管の流
路壁面から調整剤を供給する場合に比べると短時間で性
状改善が行われることになる。本発明のCWP性状の混
練調整装置において、主にCWPの混練用の撹拌羽根と
CWPのトルク検出用の撹拌羽根を駆動する中空回転軸
をそれぞれ独立させることで、主にCWP混練用の撹拌
羽根で受ける抵抗はトルク検出器で検出されないので、
調整剤を該CWP混練用の撹拌部で積極的に混合、分散
できる。その結果、トルク検出部での撹拌トルク値の変
動がほとんどなくなり、応答性がよくかつ安定な制御が
行われる。
The flow of the coal-water mixture in the feed conduit is laminar, with the highest velocity in the central part of the conduit. According to the present invention, the adjusting agent is supplied from the inside of the hollow rotating shaft to the central portion of the CWP supply conduit, so that the supplied adjusting agent is supplied from the upstream side of the rotating shaft to the downstream side by the flow of the coal-water mixture in the conduit. Get propulsion in the side direction. On the other hand, since the adjusting agent outflow hole rotates together with the rotating shaft, the adjusting agent can be efficiently dispersed around the rotating shaft, and a mixing effect equal to or more than that having a large number of adjusting agent outflow holes can be obtained. That is, in the present invention, the property is improved in a shorter time than in the case where the adjusting agent is supplied from the wall surface of the flow path of the CWP supply conduit as in the conventional method. In the CWP kneading adjusting device of the present invention, the stirring blade for mainly kneading CWP and the stirring blade for driving torque for CWP are made independent to each other, so that the stirring blade mainly for CWP kneading is provided. Since the resistance received at is not detected by the torque detector,
The modifier can be positively mixed and dispersed in the stirring unit for kneading the CWP. As a result, there is almost no fluctuation in the stirring torque value at the torque detection unit, and responsive and stable control is performed.

【0010】[0010]

【実施例】以下、実施例を用いて本発明を詳細に説明す
る。図1に本実施例の混練装置の断面概略図を示す。混
練装置118の原料投入口128より、粉砕炭B、水D
および脱硫剤Eを供給し、モータ126により駆動する
中空回転軸2の撹拌羽根127で前記原料を混ぜる。こ
のとき、石炭・水混合物の性状調整剤である微粉炭スラ
リCの供給用の導管5はジョイント9で撹拌羽根127
の中空回転軸2に接続されている。微粉炭スラリCは導
管5と中空回転軸2の内部を経由して流出孔4から混練
装置118内へ供給され、CWP(石炭・水ペースト)
が得られる。図2に図1の混練装置を用いたCWP製造
供給装置の系統図を示す。原炭バンカ101内の原炭A
はテーブルフィーダ102によって振動フルイ104に
供給される。振動フルイ104にはスクリーン105が
設置され、スクリーン105上の原炭Aは粗粉砕機10
6で粉砕され、再び振動フルイ104に戻される。振動
フルイ104内のスクリーン105を通過した粗粉炭B
(粒径約6mm以下の粗粒子)は、コンベア107によ
って定量フィーダ112まで移送される。一方、原炭バ
ンカ101にはさらに定量フィーダ103が設けられ、
定量フィーダ103で切り出された原炭Aは微粉砕機1
08で所定量の水Dとともに湿式粉砕され、微粉炭スラ
リCが製造される。この粉砕炭スラリCはタンク119
に一時的に保管された後、ポンプ120によって供給導
管5を経由して混練装置118に供給される。
EXAMPLES The present invention will be described in detail below with reference to examples. FIG. 1 shows a schematic cross-sectional view of the kneading device of this example. From the raw material inlet 128 of the kneading device 118, crushed coal B, water D
Then, the desulfurizing agent E is supplied, and the raw materials are mixed by the stirring blade 127 of the hollow rotary shaft 2 driven by the motor 126. At this time, the conduit 5 for supplying the pulverized coal slurry C, which is the property modifier for the coal / water mixture, is connected by the joint 9 to the stirring blade 127.
Is connected to the hollow rotary shaft 2. The pulverized coal slurry C is supplied from the outflow hole 4 into the kneading device 118 through the inside of the conduit 5 and the hollow rotating shaft 2, and is then fed into the kwp (coal / water paste).
Is obtained. FIG. 2 shows a system diagram of a CWP manufacturing / supplying device using the kneading device of FIG. Raw coal A in raw coal bunker 101
Are supplied to the vibrating screen 104 by the table feeder 102. A screen 105 is installed on the vibrating screen 104, and the raw coal A on the screen 105 is crushed by the coarse crusher 10.
It is crushed in 6 and returned to the vibrating screen 104 again. Coarse pulverized coal B that passed through the screen 105 in the vibrating screen 104
The (coarse particles having a particle size of about 6 mm or less) are transferred to the quantitative feeder 112 by the conveyor 107. On the other hand, the raw coal bunker 101 is further provided with a quantitative feeder 103,
Raw coal A cut out by the quantitative feeder 103 is a fine crusher 1
At 08, wet pulverization is performed together with a predetermined amount of water D to produce a pulverized coal slurry C. This crushed coal slurry C is in tank 119
After being temporarily stored in the kneading machine, it is supplied by the pump 120 to the kneading device 118 via the supply conduit 5.

【0011】原炭Aは計量器109と計量器110でそ
れぞれ計量され、制御装置111で粗粉炭Bと微粉炭ス
ラリCに分配される量が決まる。定量フィーダ112内
には石炭の計量器114が設置され、定量フィーダ11
2内の石炭中の水分を含む石炭重量を連続的に検知す
る。定量フィーダ112で計量された石炭はモータ11
3でその供給量が制御されて混練装置118に送られ
る。混練装置118には定量フィーダ112で切り出さ
れた粗粉炭B、ポンプ120より供給された微粉炭スラ
リC、給水バルブ117で供給された水Dおよび石灰石
タンク115から石灰石フィーダ116により切り出さ
れた石灰石Eがそれぞれ投入され、撹拌、混合されてC
WPが製造される。このようにして製造されたCWP
は、混練装置118とCWPタンク122の間の流路1
内を移送された後、CWPタンク122に備えた撹拌機
123で撹拌される。CWPタンク122と油圧装置1
25によって駆動するCWPポンプ124は流路11を
介して接続され、CWPポンプ124により製造したC
WPが火炉(図示は省略)へ圧送される。流路1内で
は、トルク検出器7を介して回転軸2がモータ6によっ
て回転される。ここで検出したトルク実測値が制御装置
12内に予め設定されているトルク設定値信号と比較さ
れ、この偏差が少なくなるように微粉炭スラリCがスラ
リポンプ121によって供給導管5を経由してトルク検
出器7を備えた検出部へ供給される。トルク検出器7と
同様のトルク検出手段は流路11に設けてもよく、特に
タンク122が大型化した場合には効果的である。
The raw coal A is weighed by a weighing device 109 and a weighing device 110, respectively, and the control device 111 determines the amount to be distributed to the pulverized coal B and the pulverized coal slurry C. A coal weighing device 114 is installed in the fixed quantity feeder 112, and
The weight of the coal containing water in the coal in 2 is continuously detected. The coal measured by the quantitative feeder 112 is the motor 11
In 3, the supply amount is controlled and sent to the kneading device 118. In the kneading device 118, coarse coal B cut out by the quantitative feeder 112, pulverized coal slurry C supplied by the pump 120, water D supplied by the water supply valve 117, and limestone E cut out by the limestone feeder 116 from the limestone tank 115. Are added, stirred and mixed to obtain C
WP is manufactured. CWP manufactured in this way
Is the flow path 1 between the kneading device 118 and the CWP tank 122.
After being transferred inside, it is agitated by an agitator 123 provided in the CWP tank 122. CWP tank 122 and hydraulic system 1
The CWP pump 124 driven by 25 is connected through the flow path 11, and the CWP pump 124 produces C
The WP is pumped to a furnace (not shown). In the flow path 1, the rotary shaft 2 is rotated by the motor 6 via the torque detector 7. The measured torque value detected here is compared with a torque set value signal preset in the control device 12, and the pulverized coal slurry C is torqued by the slurry pump 121 via the supply conduit 5 so as to reduce this deviation. It is supplied to the detection unit provided with the detector 7. A torque detecting means similar to the torque detector 7 may be provided in the flow path 11 and is particularly effective when the tank 122 becomes large.

【0012】図3に本実施例に係るCWP調整装置の拡
大図を示す。流路1内に設けられたCWP性状調整装置
は、内部が中空の回転軸2と撹拌羽根3並びに前記中空
回転軸2を駆動させるモータ6と、撹拌羽根3の撹拌時
に受けるトルク検出器7から構成されている。中空回転
軸2は軸受8によって流路1に固定される。また、中空
回転軸2はジョイント9によって微粉炭スラリCの供給
導管5と接続され、中空の回転軸2内に調整剤である微
粉炭スラリCを供給できる構造となっている。CWP性
状をオンラインで制御するには、調整剤の供給後にCW
Pが目標性状となっているか否かを短時間で再検出する
必要がある。回転軸2とともに回転する撹拌羽根3はC
WPから撹拌抵抗を受けるが、流路1内に撹拌羽根3を
設置すれば、流路1内は撹拌されない領域がほとんどな
くなるため、供給される微粉炭スラリCが調整すべきC
WP中に短時間に分散される。また、回転軸2が中空構
造となっているので、回転軸2を介して微粉炭スラリC
を流路1の中心部分に供給することが可能となる。すな
わち、回転軸2の側面の適宜の箇所に複数個設けた流出
孔4から流路1の中心部分近傍へ微粉炭スラリCが供給
されると、流路1の中心部分のCWPの流速を利用し
て、CWPの流れ方向への混合分散が実現される。同時
に微粉炭スラリCの流出孔4は回転軸2と共に回転する
ので、回転軸2の周囲に効率よく微粉炭スラリCを分散
でき、供給導管5を多数設けたのと同等か、それ以上の
混合効果を一本の供給導管5で得ることができる。
FIG. 3 shows an enlarged view of the CWP adjusting device according to this embodiment. The CWP property adjusting device provided in the flow path 1 includes a rotating shaft 2 having a hollow inside, a stirring blade 3, a motor 6 for driving the hollow rotating shaft 2, and a torque detector 7 received when the stirring blade 3 is stirred. It is configured. The hollow rotating shaft 2 is fixed to the flow path 1 by a bearing 8. The hollow rotary shaft 2 is connected to the supply conduit 5 for supplying the pulverized coal slurry C by a joint 9 so that the pulverized coal slurry C, which is an adjusting agent, can be supplied into the hollow rotary shaft 2. To control CWP properties online, use CW after supplying the modifier.
It is necessary to detect again in a short time whether P is the target property. The stirring blade 3 rotating with the rotating shaft 2 is C
Although it receives agitation resistance from WP, if the agitation blade 3 is installed in the flow path 1, there is almost no area in the flow path 1 that is not agitated, so the pulverized coal slurry C to be supplied should be adjusted to C
It is dispersed in WP for a short time. Further, since the rotary shaft 2 has a hollow structure, the pulverized coal slurry C is inserted through the rotary shaft 2.
Can be supplied to the central portion of the flow channel 1. That is, when the pulverized coal slurry C is supplied to the vicinity of the central portion of the flow passage 1 from the plurality of outflow holes 4 provided at appropriate places on the side surface of the rotary shaft 2, the flow velocity of CWP in the central portion of the flow passage 1 is used. Thus, the mixing and dispersion of the CWP in the flow direction is realized. At the same time, the pulverized coal slurry C outflow hole 4 rotates together with the rotary shaft 2, so that the pulverized coal slurry C can be efficiently dispersed around the rotary shaft 2 and the same or more mixing than the case where a large number of supply conduits 5 are provided. The effect can be obtained with a single supply conduit 5.

【0013】図4は前記流出孔4から微粉炭スラリCが
流出する様子を示している。流出孔4から流路1内に供
給される微粉炭スラリCを強制的にCWP中に分散する
ように撹拌羽根3のできるだけ近くに流出孔4が設けら
れる。前述のように、微粉炭スラリCを中空の回転軸2
を経て流路1の中心部分へ供給すれば、流路1の中心部
分のCWP流速を利用してCWP流れ方向への混合分散
が実現される。同時に、微粉炭スラリCの流出孔4は回
転軸2と共に回転するので、回転軸2の周囲に効率よく
微粉炭スラリCを分散できる。図5は本発明の混合装置
における応答性の改善効果を従来法と比較して示したも
のである。微粉炭スラリCがCWP性状の変化に応じて
所定量供給された場合、本発明法では曲線aで示される
ように短時間に目標の撹拌トルクに到達する。これに対
して、従来法では供給した微粉炭スラリCがCWPに混
ざりにくいために、曲線bに示すように目標の撹拌トル
クを得るまでに相当な時間がかかる。また、場合によっ
てはほとんど混合されず、曲線cのように全く性状に変
化が検出値に表れてこないことがある。曲線cのような
場合には、調整剤を過剰に供給することになるため、C
WPの粘度が極端に低下してポンプ124(図2)での
閉塞を引き起こす。本実施例では、微粉炭スラリCをモ
ータ6の反対側から供給しているが、図6に示すように
微粉炭スラリCをモータ6側から供給する構成にしても
同様の効果が得られる。
FIG. 4 shows how the pulverized coal slurry C flows out through the outflow holes 4. The outflow hole 4 is provided as close as possible to the stirring blade 3 so that the pulverized coal slurry C supplied from the outflow hole 4 into the flow path 1 is forcibly dispersed in the CWP. As described above, the pulverized coal slurry C is added to the hollow rotary shaft 2
If it is supplied to the central portion of the flow channel 1 via the above, the CWP flow velocity in the central portion of the flow channel 1 is utilized to realize mixing and dispersion in the CWP flow direction. At the same time, the outflow hole 4 of the pulverized coal slurry C rotates together with the rotary shaft 2, so that the pulverized coal slurry C can be efficiently dispersed around the rotary shaft 2. FIG. 5 shows the effect of improving the response in the mixing apparatus of the present invention in comparison with the conventional method. When the pulverized coal slurry C is supplied in a predetermined amount according to the change in the CWP property, the target stirring torque is reached in a short time in the method of the present invention as shown by the curve a. On the other hand, in the conventional method, the supplied pulverized coal slurry C is less likely to be mixed with CWP, so that it takes a considerable time to obtain the target stirring torque as shown by the curve b. Further, in some cases, there is almost no mixing, and there is a case where no change appears in the detected value in the property like the curve c. In the case of the curve c, since the regulator is excessively supplied, C
The viscosity of the WP drops dramatically causing blockage at the pump 124 (FIG. 2). In the present embodiment, the pulverized coal slurry C is supplied from the opposite side of the motor 6, but the same effect can be obtained by supplying the pulverized coal slurry C from the motor 6 side as shown in FIG.

【0014】図7は流路1内の中空回転軸2の内部に微
粉炭スラリCの供給導管5を挿入した場合の例である。
本実施例では、供給導管5の管内径を可能な限り小さく
でき、流出孔4から流出する微粉炭スラリCの初速を速
くできる。その結果、流路1内のCWPへの微粉炭スラ
リC流れの貫通力が増大して微粉炭スラリCのCWPへ
の分散が加速される。図8には本発明に係るCWP混練
装置の他の実施例を示した。本実施例では水Dを流路1
内のCWPに供給して撹拌する部分と撹拌後のCWPの
撹拌トルクを検出する部分が独立に存在している。調整
剤である水Dは供給導管5を経てスクリュ状の撹拌羽根
16を備えた中空回転軸15へ供給される。該中空回転
軸15はモータ12によって高速で回転できる機能を有
する。水Dが中空回転軸15の側面に開口した流出孔4
から流路1内のCWP中に供給されると同時に、高速回
転する撹拌羽根16により強撹拌される。この際、CW
P中に存在する石炭粒子の一部が粉砕されて微粒子が生
成する。すなわち、生成した石炭微粒子がCWPの性状
改善に寄与するという効果がある。
FIG. 7 shows an example in which the supply conduit 5 for the pulverized coal slurry C is inserted inside the hollow rotary shaft 2 in the flow path 1.
In this embodiment, the inner diameter of the supply conduit 5 can be made as small as possible, and the initial velocity of the pulverized coal slurry C flowing out from the outflow hole 4 can be increased. As a result, the penetrating force of the pulverized coal slurry C flow into the CWP in the flow path 1 is increased, and the dispersion of the pulverized coal slurry C into the CWP is accelerated. FIG. 8 shows another embodiment of the CWP kneading device according to the present invention. In this embodiment, the water D is used as the flow path 1
There is an independent portion for supplying and stirring to the CWP inside and a portion for detecting the stirring torque of the CWP after stirring. Water D, which is an adjusting agent, is supplied to the hollow rotating shaft 15 equipped with a screw-shaped stirring blade 16 through the supply conduit 5. The hollow rotary shaft 15 has a function of being rotated by the motor 12 at high speed. Outflow hole 4 in which water D opens on the side surface of hollow rotary shaft 15
Is supplied to the CWP in the flow path 1 from the above, and at the same time, is strongly stirred by the stirring blade 16 rotating at a high speed. At this time, CW
Part of the coal particles present in P are crushed to generate fine particles. That is, there is an effect that the generated coal fine particles contribute to the improvement of the properties of CWP.

【0015】図9はCWPを回分式で製造した実施例で
ある。混練装置20の原料投入口25より、粉砕炭Bお
よび脱硫剤Eを供給し、モータ21により駆動する撹拌
羽根22で前記原料を混ぜる。このとき、微粉炭スラリ
Cが導管24を経て、さらにジョイント26で接続され
ている中空回転軸28の内部を経由して流出孔23から
混練装置20へ供給され、CWP(石炭・水ペースト)
が得られる。回分式にてCWPを製造後、混練装置20
の底部に設けた排出口27より燃料として排出される。
図10は、図9で示した混練装置20で製造されるCW
Pの混練度の時間変化を従来例と比較した結果である。
本発明法によれば、従来法の約1/3の時間で高いCW
Pの混練度が得られるため混練装置の容積を縮小でき経
済的である。
FIG. 9 shows an embodiment in which the CWP is manufactured by the batch method. The crushed carbon B and the desulfurizing agent E are supplied from a raw material inlet 25 of the kneading device 20, and the raw materials are mixed by a stirring blade 22 driven by a motor 21. At this time, the pulverized coal slurry C is supplied to the kneading device 20 from the outflow hole 23 through the conduit 24 and the inside of the hollow rotary shaft 28 connected by the joint 26, and CWP (coal / water paste).
Is obtained. After manufacturing CWP by batch method, kneading device 20
It is discharged as fuel from a discharge port 27 provided at the bottom of the.
FIG. 10 shows a CW manufactured by the kneading device 20 shown in FIG.
It is the result of comparing the time change of the kneading degree of P with the conventional example.
According to the method of the present invention, a high CW can be achieved in about 1/3 the time of the conventional method.
Since the kneading degree of P is obtained, the volume of the kneading device can be reduced, which is economical.

【0016】[0016]

【発明の効果】以上説明したごとく本発明によれば、石
炭・水混合物の混練を短時間に行える。燃料性状のバラ
ツキが減少し、CWPを燃焼炉に安定して供給できる石
炭・水混合物燃料の供給設備を提供できる。
As described above, according to the present invention, the coal / water mixture can be kneaded in a short time. It is possible to provide a coal / water mixture fuel supply facility capable of stably supplying CWP to a combustion furnace by reducing variations in fuel properties.

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

【図1】 本発明の一実施例のCWP混練調整装置の概
略図である。
FIG. 1 is a schematic diagram of a CWP kneading adjustment device according to an embodiment of the present invention.

【図2】 図1の混練調整装置を用いたCWP製造供給
装置の系統図である。
FIG. 2 is a system diagram of a CWP manufacturing / supplying device using the kneading adjusting device of FIG.

【図3】 図2のCWP混練調整装置の拡大図である。FIG. 3 is an enlarged view of the CWP kneading adjustment device of FIG.

【図4】 図3のCWP混練調整装置の中空回転軸の流
出孔から調整剤が流出する状況を説明する図である。
FIG. 4 is a view for explaining a situation in which the adjusting agent flows out from an outflow hole of a hollow rotating shaft of the CWP kneading adjusting device of FIG.

【図5】 本発明法と従来法の応答性に関する比較例の
図である。
FIG. 5 is a diagram of a comparative example regarding the responsiveness of the method of the present invention and the conventional method.

【図7】 本発明の一実施例のCWP混練調整装置の概
略図である。
FIG. 7 is a schematic diagram of a CWP kneading adjustment device according to an embodiment of the present invention.

【図8】 本発明の一実施例のCWP混練調整装置の概
略図である。
FIG. 8 is a schematic diagram of a CWP kneading adjustment device according to an embodiment of the present invention.

【図6】 本発明の一実施例のCWP混練調整装置の概
略図である。
FIG. 6 is a schematic diagram of a CWP kneading adjustment device according to an embodiment of the present invention.

【図9】 本発明に係る回分式の混練調整装置の概略図
である。
FIG. 9 is a schematic view of a batch-type kneading adjustment device according to the present invention.

【図10】 本発明法と従来法の回分式混練調整装置に
関する比較図である。
FIG. 10 is a comparison diagram of a batch-type kneading adjusting device of the method of the present invention and a conventional method.

【図11】 従来のCWP混練装置の概略図である。FIG. 11 is a schematic view of a conventional CWP kneading device.

【図12】 従来のCWP貯留タンクとボイラへのCW
P供給ポンプとの間のCWP流路に設けたCWPの混練
調整装置の概略図である。
FIG. 12: CW for conventional CWP storage tank and boiler
It is a schematic diagram of the kneading adjustment device of CWP provided in the CWP channel between P supply pumps.

【符号の説明】[Explanation of symbols]

1、11…CWP流路、2、15、28…中空回転軸、
3、16、22、127…撹拌羽根、4、23…流出
孔、5…CWP供給導管、6…モータ、7…トルク検出
器、8…軸受、9、26…ジョイント、12…制御装
置、20、118…混練装置、24…微粉炭スラリ導
管、25、128…原料投入口、27…排出口、B…粉
砕炭、C…微粉炭スラリ、D…水、E…脱硫剤
1, 11 ... CWP channel, 2, 15, 28 ... Hollow rotating shaft,
3, 16, 22, 127 ... Stirring blades, 4, 23 ... Outflow holes, 5 ... CWP supply conduit, 6 ... Motor, 7 ... Torque detector, 8 ... Bearing, 9, 26 ... Joint, 12 ... Control device, 20 , 118 ... Kneading device, 24 ... Pulverized coal slurry conduit, 25, 128 ... Raw material input port, 27 ... Discharge port, B ... Pulverized coal slurry, C ... Pulverized coal slurry, D ... Water, E ... Desulfurizing agent

───────────────────────────────────────────────────── フロントページの続き (72)発明者 佐藤 一教 広島県呉市宝町3番36号 バブコック日立 株式会社呉研究所内 (72)発明者 大木 勝弥 広島県呉市宝町6番9号 バブコック日立 株式会社呉工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kazunori Sato 3-36 Takaracho, Kure-shi, Hiroshima Babcock Hitachi Kure Laboratory Co., Ltd. (72) Katsuya Oki 6-9 Takaracho, Kure-shi, Hiroshima Babcock Hitachi Stock Company Kure Factory

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 石炭と水を混練して石炭・水混合物を調
製する石炭・水混合物の混練調整装置において、粉砕炭
を供給する原料投入口を石炭・水混合物の混練部の上流
側に設け、中空構造の石炭・水混合物混練用の回転軸の
中空部先端に石炭・水混合物の性状調整用の水と微粉炭
スラリの少なくともいずれかからなる調整剤を供給する
調整剤供給導管を接続し、該中空部内部に供給された調
整剤を混練中または性状調整中の石炭・水混合物中に流
出させるための流出孔を回転軸表面に設けたことを特徴
とする石炭・水混合物の混練調整装置。
1. In a kneading and adjusting apparatus for a coal / water mixture for kneading coal and water to prepare a coal / water mixture, a raw material inlet for supplying crushed coal is provided upstream of a kneading section for the coal / water mixture. A connecting agent supply conduit for supplying an adjusting agent comprising at least one of water and pulverized coal slurry for adjusting the properties of the coal / water mixture is connected to the end of the hollow part of the rotary shaft for kneading the coal / water mixture having a hollow structure. A kneading adjustment of the coal / water mixture, characterized in that an outlet hole is provided on the surface of the rotating shaft for letting out the adjusting agent supplied into the hollow portion into the coal / water mixture during kneading or property adjustment. apparatus.
【請求項2】 流出孔は混練部の上流側の領域にある中
空回転軸側面に設けられ、また、中空回転軸には石炭・
水混合物の混練用の撹拌羽根が設けられていることを特
徴とする請求項1記載の石炭・水混合物の混練調整装
置。
2. The outflow hole is provided on the side surface of the hollow rotary shaft in the upstream region of the kneading section, and the hollow rotary shaft is provided with coal.
The kneading adjustment device for coal / water mixture according to claim 1, further comprising a stirring blade for kneading the water mixture.
【請求項3】 石炭と水を混練して石炭・水混合物を調
製する石炭・水混合物の混練調整装置において、粉砕炭
を供給する原料投入口を石炭・水混合物の混練部の上流
側に設け、中空構造の石炭・水混合物混練用の回転軸の
中空部先端に性状調整用の水と微粉炭スラリの少なくと
もいずれかからなる調整剤を供給する調整剤供給導管を
接続し、該中空部内部に供給された調整剤を混練中また
は性状調整中の石炭・水混合物中に流出させるための流
出孔と石炭・水混合物混練用の撹拌羽根を回転軸表面に
設け、該撹拌羽根を用いて流送される石炭・水混合物の
撹拌トルクを検出するトルク検出器と、石炭・水混合物
のトルク検出値に応じて該中空回転軸の中空部を通して
行う調整剤の供給量を制御する調整剤供給量制御装置を
設けたことを特徴とする石炭・水混合物の混練調整装
置。
3. A coal / water mixture kneading adjusting device for kneading coal and water to prepare a coal / water mixture, wherein a raw material charging port for supplying crushed coal is provided upstream of a coal / water mixture kneading section. , A hollow structure coal / water mixture kneading rotary shaft for rotation of the shaft is connected to the adjusting agent supply conduit for supplying an adjusting agent consisting of at least one of water for property adjustment and pulverized coal slurry, inside the hollow portion An outlet hole for letting the adjusting agent supplied into the mixture into the coal / water mixture during kneading or property adjustment and a stirring blade for kneading the coal / water mixture are provided on the surface of the rotary shaft, and the stirring blade is used to flow the mixture. A torque detector that detects the stirring torque of the coal / water mixture to be sent, and a regulator supply amount that controls the supply amount of the regulator performed through the hollow portion of the hollow rotary shaft according to the torque detection value of the coal / water mixture. It is characterized by having a control device A kneading adjustment device for coal and water mixture.
【請求項4】 流出孔は混練部の上流側の領域にある中
空回転軸側面に設けられていることを特徴とする請求項
3記載の石炭・水混合物の混練調整装置。
4. The kneading / adjusting device for a coal / water mixture according to claim 3, wherein the outflow hole is provided on a side surface of the hollow rotating shaft in an upstream region of the kneading section.
【請求項5】 主に石炭・水混合物を混練するための撹
拌手段を備えた中空回転軸と主に石炭・水混合物の撹拌
トルク検出用の撹拌手段とを備えた中空回転軸がそれぞ
れ独立していることを特徴とする請求項3または4のい
ずれかに記載の石炭・水混合物の混練調整装置。
5. A hollow rotary shaft mainly equipped with a stirring means for kneading a coal / water mixture and a hollow rotary shaft mainly equipped with a stirring means for detecting a stirring torque of a coal / water mixture are independent of each other. The kneading adjusting device for a coal / water mixture according to claim 3, wherein
JP2440994A 1994-02-22 1994-02-22 Apparatus for controlling kneading of coal/water mixture Pending JPH07228878A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2440994A JPH07228878A (en) 1994-02-22 1994-02-22 Apparatus for controlling kneading of coal/water mixture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2440994A JPH07228878A (en) 1994-02-22 1994-02-22 Apparatus for controlling kneading of coal/water mixture

Publications (1)

Publication Number Publication Date
JPH07228878A true JPH07228878A (en) 1995-08-29

Family

ID=12137375

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2440994A Pending JPH07228878A (en) 1994-02-22 1994-02-22 Apparatus for controlling kneading of coal/water mixture

Country Status (1)

Country Link
JP (1) JPH07228878A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100841765B1 (en) * 2002-06-25 2008-06-27 주식회사 포스코 Water injection device in pug mill
CN108671848A (en) * 2018-05-02 2018-10-19 拜城县众泰煤焦化有限公司 A kind of Automatic Control System for Mixing Coal and its blending method
KR20220052672A (en) 2020-10-21 2022-04-28 주식회사 포스코 Apparatus for mixing object and method for mixing object
CN115625824A (en) * 2022-11-02 2023-01-20 江苏三元轮胎有限公司 Normal-pressure desulfurization equipment for waste rubber

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100841765B1 (en) * 2002-06-25 2008-06-27 주식회사 포스코 Water injection device in pug mill
CN108671848A (en) * 2018-05-02 2018-10-19 拜城县众泰煤焦化有限公司 A kind of Automatic Control System for Mixing Coal and its blending method
KR20220052672A (en) 2020-10-21 2022-04-28 주식회사 포스코 Apparatus for mixing object and method for mixing object
CN115625824A (en) * 2022-11-02 2023-01-20 江苏三元轮胎有限公司 Normal-pressure desulfurization equipment for waste rubber
CN115625824B (en) * 2022-11-02 2023-10-13 江苏三元轮胎有限公司 Waste rubber normal pressure desulfurization equipment

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