JP2010149052A - Vertical mill - Google Patents

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JP2010149052A
JP2010149052A JP2008330092A JP2008330092A JP2010149052A JP 2010149052 A JP2010149052 A JP 2010149052A JP 2008330092 A JP2008330092 A JP 2008330092A JP 2008330092 A JP2008330092 A JP 2008330092A JP 2010149052 A JP2010149052 A JP 2010149052A
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coal
housing
roller
pressure roller
vertical mill
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Masahito Tamura
雅人 田村
Ryunosuke Itokazu
龍之介 糸数
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IHI Corp
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IHI Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To achieve improvement of grinding efficiency and inhibition of self-excited vibration in a vertical mill by improving a biting rate of supplied coal. <P>SOLUTION: The vertical mill includes the housing 3 forming a classification chamber 9, a grinding table 6 accommodated in the lower part of the housing and rotated and driven, a plurality of roller pressure devices 12 each for pressing the pressure roller 16 to the grinding table to grind coal on the grinding table, and a coal supply pipe 23 vertically installed in the center of the housing for supplying lump coal between the pressure rollers of the grinding table. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、石炭焚きボイラへ供給する石炭を粉砕する竪型ミルに関するものである。   The present invention relates to a vertical mill for pulverizing coal supplied to a coal-fired boiler.

石炭を燃料とする石炭焚きボイラでは、塊状の石炭を竪型ミルにより粉砕して微粉炭とし、微粉炭を1次空気と共に燃焼装置であるバーナに供給している。   In a coal-fired boiler using coal as fuel, massive coal is pulverized by a vertical mill into pulverized coal, and the pulverized coal is supplied together with primary air to a burner that is a combustion apparatus.

竪型ミルは、所定の回転数で回転する粉砕テーブルと、該粉砕テーブルに押圧される加圧ローラとを有し、前記粉砕テーブルには給炭管から塊状の石炭が前記粉砕テーブルの中心に落下され、供給される。供給された塊状の石炭は、前記粉砕テーブルの回転遠心力によって外周へと移動する。   The vertical mill has a crushing table that rotates at a predetermined number of revolutions, and a pressure roller that is pressed against the crushing table, and in the crushing table, lump coal is fed from a coal supply pipe to the center of the crushing table. Dropped and supplied. The supplied massive coal moves to the outer periphery by the rotational centrifugal force of the grinding table.

石炭が前記粉砕テーブルの外周に移動する過程で、前記加圧ローラと前記粉砕テーブルの間に噛込まれて粉砕される。粉砕された微粉炭は前記粉砕テーブル周囲の1次空気吹出し口より、吹上がる1次空気によって上昇し、1次空気と共にバーナに供給される。   In the process of moving the coal to the outer periphery of the pulverizing table, the coal is pulverized by being caught between the pressure roller and the pulverizing table. The pulverized pulverized coal rises from the primary air blowout port around the pulverization table, and is supplied to the burner together with the primary air.

上記した様に、前記粉砕テーブルに供給した塊状の石炭は前記粉砕テーブルの中心に供給され、遠心力によって外周に移動する過程で、前記加圧ローラに噛込まれ、粉砕されるので、供給された塊状の石炭の全てが直ちに前記加圧ローラに噛込まれず、一部はテーブル上で跳ね、或は前記加圧ローラの間をすり抜ける、或は前記粉砕テーブルの外周への移動が円滑に行われない等によって供給と粉砕との間に時間遅れ、即ち噛込み率の低下を生じる。更に、噛込み率の低下は、粉砕効率の低下を招く。   As described above, the lump coal supplied to the crushing table is supplied to the center of the crushing table and is engaged with the pressure roller and crushed in the process of moving to the outer periphery by centrifugal force. All of the lumped coal is not immediately caught by the pressure roller, part of it jumps on the table, passes between the pressure rollers, or smoothly moves to the outer periphery of the grinding table. Failure to do so causes a time delay between supply and pulverization, that is, a reduction in the biting rate. Furthermore, the reduction in the biting rate causes a reduction in the grinding efficiency.

又、前記粉砕テーブル上に形成される粉砕層は緩衝体としての機能があり、粉砕層の厚みが薄くなると、加圧ローラの自励振動が発生する。或は、塊状の石炭の噛込みが少なくなることで、粉砕層の粒径が揃い、自励振動を発生し易くなる。   The pulverization layer formed on the pulverization table functions as a buffer. When the pulverization layer is thin, self-excited vibration of the pressure roller is generated. Or since the biting of massive coal is reduced, the particle size of the pulverized layer is uniform, and self-excited vibration is likely to occur.

従って、噛込み率が低下することで、粉砕効率が低下し、更に加圧ローラの自励振動が発生し易くなり、自励振動が発生すると、粉砕効率が著しく低下する。   Accordingly, the reduction of the biting rate decreases the pulverization efficiency, and further the self-excited vibration of the pressure roller is likely to occur. When the self-excited vibration is generated, the pulverization efficiency is remarkably reduced.

特開2007−7594号公報JP 2007-7594 A

本発明は斯かる実情に鑑み、竪型ミルに於いて供給する石炭の噛込み率を向上させ、粉砕効率の向上を図ると共に自励振動の抑制を図るものである。   In view of such a situation, the present invention improves the biting rate of coal supplied in a vertical mill, improves the pulverization efficiency, and suppresses self-excited vibration.

本発明は、分級室を形成するハウジングと、該ハウジングの下部に収納され、回転駆動される粉砕テーブルと、該粉砕テーブルに加圧ローラを押圧し、前記粉砕テーブル上の石炭を粉砕する複数のローラ加圧装置と、塊状石炭を前記粉砕テーブルの前記加圧ローラの間に供給する給炭管とを具備する竪型ミルに係るものである。   The present invention includes a housing forming a classification chamber, a pulverizing table housed in a lower portion of the housing and driven to rotate, and a plurality of pulverizing coals on the pulverizing table by pressing a pressure roller against the pulverizing table. The present invention relates to a vertical mill that includes a roller pressure device and a coal supply pipe that supplies massive coal between the pressure rollers of the crushing table.

又本発明は、前記給炭管は前記ハウジングの中心に鉛直に設けられ、該給炭管の下端部は複数の給炭分岐管に分岐し、該給炭分岐管の下端部は前記加圧ローラと加圧ローラとの間に開口する竪型ミルに係り、又前記給炭管は前記ハウジングの前記ローラ加圧装置の間を貫通する様に設けられた竪型ミルに係り、又前記粉砕テーブルで飛跳ねた塊状石炭を弾返す飛跳防止部材を前記ローラ加圧装置の間に配設した竪型ミルに係り、更に又前記給炭分岐管の下端の軸心は、前記加圧ローラの噛込み位置に向って傾斜する竪型ミルに係るものである。   According to the present invention, the coal supply pipe is provided vertically at the center of the housing, the lower end portion of the coal supply pipe branches into a plurality of coal supply branch pipes, and the lower end portion of the coal supply branch pipe is the pressurizing member. A vertical mill that opens between a roller and a pressure roller; and the coal supply pipe relates to a vertical mill that is provided to penetrate between the roller pressure devices of the housing, and the crushing The present invention relates to a vertical mill in which a jump preventing member that bounces off massive coal that has jumped on a table is disposed between the roller pressurizing devices, and the shaft center of the lower end of the coal supply branch pipe is the press roller This relates to a vertical mill inclined toward the biting position.

本発明によれば、分級室を形成するハウジングと、該ハウジングの下部に収納され、回転駆動される粉砕テーブルと、該粉砕テーブルに加圧ローラを押圧し、前記粉砕テーブル上の石炭を粉砕する複数のローラ加圧装置と、塊状石炭を前記粉砕テーブルの前記加圧ローラの間に供給する給炭管とを具備するので、供給された塊状の石炭は直ちに加圧ローラによって粉砕され、噛込み率の向上、粉砕効率の向上が図れ、又塊状の石炭が加圧ローラに直接噛込まれる様に供給されるので、自励振動が抑制される。   According to the present invention, the housing forming the classification chamber, the crushing table housed in the lower part of the housing and driven to rotate, and the pressure roller pressed against the crushing table to crush the coal on the crushing table. Since it has a plurality of roller pressurizing devices and a coal supply pipe for supplying the bulk coal between the pressure rollers of the grinding table, the supplied bulk coal is immediately crushed by the pressure roller and bitten The rate and the pulverization efficiency can be improved, and the bulk coal is supplied so as to be directly bitten by the pressure roller, so that self-excited vibration is suppressed.

又本発明によれば、前記給炭管は前記ハウジングの中心に鉛直に設けられ、該給炭管の下端部は複数の給炭分岐管に分岐し、該給炭分岐管の下端部は前記加圧ローラと加圧ローラとの間に開口するので、又前記給炭管は前記ハウジングの前記ローラ加圧装置の間を貫通する様に設けられたので、塊状の石炭を直接粉砕テーブル上に供給することが可能となる。   According to the invention, the coal supply pipe is provided vertically in the center of the housing, the lower end of the coal supply pipe branches into a plurality of coal supply branch pipes, and the lower end of the coal supply branch pipe is Since it opens between the pressure roller and the pressure roller, and the coal supply pipe is provided so as to penetrate between the roller pressure devices of the housing, lump coal is directly placed on the grinding table. It becomes possible to supply.

又本発明によれば、前記粉砕テーブルで飛跳ねた塊状石炭を弾返す飛跳防止部材を前記ローラ加圧装置の間に配設したので、前記粉砕テーブルで飛跳ねた塊状の石炭も直ちに加圧ローラに噛込まれ、噛込み率の向上、粉砕効率の向上が図れる。   Further, according to the present invention, since the jump preventing member that repels the bulk coal jumped from the grinding table is disposed between the roller pressurizing devices, the bulk coal jumped from the grinding table is immediately added. By being caught by the pressure roller, the biting rate can be improved and the pulverization efficiency can be improved.

又本発明によれば、前記給炭分岐管の下端の軸心は、前記加圧ローラの噛込み位置に向って傾斜するので、供給された塊状の石炭がより加圧ローラに噛込み易くなり、噛込み率の向上が図れる等の優れた効果を発揮する。   Further, according to the present invention, the shaft center at the lower end of the coal supply branch pipe is inclined toward the pressure roller engagement position, so that the supplied massive coal is more easily engaged with the pressure roller. Excellent effects such as improvement of biting rate can be achieved.

以下、図面を参照しつつ本発明を実施する為の最良の形態を説明する。   The best mode for carrying out the present invention will be described below with reference to the drawings.

図1、図2は本発明が実施される竪型ミル1の一例を示す概略図である。   1 and 2 are schematic views showing an example of a vertical mill 1 in which the present invention is implemented.

中空構造又は脚構造の基台2に筒状のハウジング3が立設され、該ハウジング3の上側に給炭機4が設けられている。   A cylindrical housing 3 is erected on a base 2 having a hollow structure or a leg structure, and a coal feeder 4 is provided on the upper side of the housing 3.

前記基台2にはテーブル駆動装置5が収納され、該テーブル駆動装置5によって粉砕テーブル6が定速又は可変速で回転される様になっている。該粉砕テーブル6は前記ハウジング3の下部に収納されており、前記基台2の上端と前記ハウジング3の下端とは仕切られ、前記粉砕テーブル6の周囲には1次空気室7が形成され、前記ハウジング3内部の前記粉砕テーブル6より上方は、分級室9となっている。   A table driving device 5 is accommodated in the base 2, and the crushing table 6 is rotated at a constant speed or a variable speed by the table driving device 5. The crushing table 6 is housed in the lower part of the housing 3, the upper end of the base 2 and the lower end of the housing 3 are partitioned, and a primary air chamber 7 is formed around the crushing table 6, A classification chamber 9 is provided above the grinding table 6 inside the housing 3.

前記ハウジング3の下部には、1次空気供給口8が取付けられ、該1次空気供給口8は前記1次空気室7に連通している。前記粉砕テーブル6の周囲にはエアポート11が形成され、該エアポート11は前記1次空気供給口8と前記分級室9とを連通し、1次空気の吹出し口として機能する。   A primary air supply port 8 is attached to the lower portion of the housing 3, and the primary air supply port 8 communicates with the primary air chamber 7. An air port 11 is formed around the pulverizing table 6, and the air port 11 communicates with the primary air supply port 8 and the classification chamber 9 and functions as a primary air outlet.

前記ハウジング3の下部には、放射状に貫通する複数、例えば3組のローラ加圧装置12が設けられ、該ローラ加圧装置12は120°間隔で設けられ、主に液圧シリンダである加圧シリンダ13、水平軸14を中心に上下方向に回転可能な加圧ローラユニット15から構成され、更に該加圧ローラユニット15は回転自在な加圧ローラ16を具備している。前記加圧ローラユニット15の下面には前記エアポート11と対峙した位置にコールシールド(石炭衝突板)19が設けられ、該コールシールド19は、中心に向かう程水平面から離反する様な傾斜面となっている。該コールシールド19には前記エアポート11を通過する1次空気と共に吹上げられる石炭が衝突し、塊状の石炭を前記粉砕テーブル6上に戻す機能を有すると共に前記コールシールド19は前記加圧ローラユニット15への石炭衝突を防止し、前記加圧ローラユニット15の摩耗を防止する。   In the lower part of the housing 3, a plurality of, for example, three sets of roller pressurizing devices 12 penetrating radially are provided, and the roller pressurizing devices 12 are provided at intervals of 120 ° and are mainly pressurizing cylinders. The pressure roller unit 15 is rotatable up and down about a cylinder 13 and a horizontal shaft 14, and the pressure roller unit 15 further includes a pressure roller 16 that is rotatable. A coal shield (coal collision plate) 19 is provided on the lower surface of the pressure roller unit 15 at a position facing the air port 11, and the coal shield 19 has an inclined surface that is separated from the horizontal plane toward the center. ing. The call shield 19 collides with coal blown up with the primary air passing through the air port 11, and has a function of returning massive coal onto the crushing table 6, and the call shield 19 has the pressure roller unit 15. Coal collision is prevented, and wear of the pressure roller unit 15 is prevented.

前記粉砕テーブル6の上面にはリング上の凹部を形成するテーブルセグメント17が設けられ、前記加圧ローラ16は前記加圧シリンダ13によって前記テーブルセグメント17の凹部に押圧される。   A table segment 17 that forms a recess on the ring is provided on the upper surface of the grinding table 6, and the pressure roller 16 is pressed against the recess of the table segment 17 by the pressure cylinder 13.

前記ハウジング3の内壁の所要位置、図示では円周を3等分した位置(前記ローラ加圧装置12,12の中間位置)に飛跳防止板18が、後述する給炭分岐管28と干渉しない様に設けられる。該飛跳防止板18は、前記ハウジング3の内壁に取付けられた支持板21によって支持される。該支持板21は板形状であり、前記エアポート11を通過して吹上がる1次空気の流れを妨げない様鉛直に設けられている。   The jump preventing plate 18 does not interfere with a coal supply branch pipe 28 to be described later at a required position of the inner wall of the housing 3, a position where the circumference is equally divided into three in the drawing (an intermediate position between the roller pressure devices 12, 12). Provided. The jump prevention plate 18 is supported by a support plate 21 attached to the inner wall of the housing 3. The support plate 21 has a plate shape and is provided vertically so as not to hinder the flow of primary air that passes through the air port 11 and blows up.

前記飛跳防止板18は、前記加圧ローラ16,16との間隔を略塞ぐ水平方向の長さを有する矩形形状の板であり、上端が中心側に倒れる様に傾斜し、傾斜角度は前記飛跳防止板18に衝突した塊状の石炭が、効果的に前記テーブルセグメント17に落下する様になっている。尚、塊状の石炭を前記テーブルセグメント17に弾返せばよいので、傾斜せず垂直であってもよい。   The jump prevention plate 18 is a rectangular plate having a horizontal length that substantially closes the gap between the pressure rollers 16 and 16, and is inclined so that the upper end is tilted toward the center side. The massive coal that collides with the jump prevention plate 18 is effectively dropped onto the table segment 17. In addition, since it is sufficient to rebound the lump coal to the table segment 17, it may be vertical without being inclined.

又前記飛跳防止板18の下端は、少なくとも前記エアポート11よりも中心側に位置し、前記粉砕テーブル6上面との間に隙間を有している。   Further, the lower end of the jump preventing plate 18 is located at least on the center side with respect to the air port 11 and has a gap between the upper surface of the crushing table 6.

前記給炭機4は、出炭部ハウジング22及び該出炭部ハウジング22を貫通して前記ハウジング3の内部に延出するパイプ状の給炭管23に接続されている。   The coal feeder 4 is connected to a coal outlet housing 22 and a pipe-shaped coal feeder pipe 23 that penetrates the coal outlet housing 22 and extends into the housing 3.

前記出炭部ハウジング22の下端は開放され、前記分級室9に連通している。又、前記出炭部ハウジング22には微粉炭送給管24が接続され、該微粉炭送給管24はボイラのバーナ(図示せず)に接続されている。前記給炭管23は前記粉砕テーブル6の回転中心の延長上にあり、前記給炭管23の上端は前記給炭機4に接続されている。   The lower end of the coal output housing 22 is open and communicates with the classification chamber 9. In addition, a pulverized coal feed pipe 24 is connected to the coal outlet housing 22, and the pulverized coal feed pipe 24 is connected to a burner (not shown) of a boiler. The coal supply pipe 23 is on an extension of the rotation center of the crushing table 6, and the upper end of the coal supply pipe 23 is connected to the coal feeder 4.

前記給炭管23の下部は、3本の給炭分岐管28に分岐しており、該給炭分岐管28の下端は前記加圧ローラ16,16との間に位置され、前記テーブルセグメント17の凹部の上方に開口しており、前記給炭分岐管28の下端と前記テーブルセグメント17の上面との間には間隙が形成され、該間隙は前記テーブルセグメント17上に形成される粉砕層の最大厚みより更に大きくなっており、前記給炭分岐管28の下端が前記粉砕層に接触しない様になっている。   The lower portion of the coal supply pipe 23 is branched into three coal supply branch pipes 28, and the lower end of the coal supply branch pipe 28 is positioned between the pressure rollers 16 and 16, and the table segment 17 A gap is formed between the lower end of the coal supply branch pipe 28 and the upper surface of the table segment 17, and the gap is a crushing layer formed on the table segment 17. The thickness is further greater than the maximum thickness so that the lower end of the coal supply branch pipe 28 does not contact the pulverized layer.

前記給炭管23の中途部に分級機26が設けられ、該分級機26は前記分級室9の上部に位置し、前記出炭部ハウジング22の下端開口部に隣接している。前記分級機26は、回転駆動部25に連結され、該回転駆動部25によって回転される。   A classifier 26 is provided in the middle of the coal supply pipe 23, and the classifier 26 is located above the classifying chamber 9 and is adjacent to the lower end opening of the coal outlet housing 22. The classifier 26 is connected to the rotation drive unit 25 and is rotated by the rotation drive unit 25.

前記分級機26は短冊状のブレード27が円周方向に所要ピッチで配設され、前記給炭管23に支持されたものであり、前記ブレード27が円周上を回転する様になっている。   In the classifier 26, strip-shaped blades 27 are arranged at a required pitch in the circumferential direction and supported by the coal supply pipe 23, and the blades 27 rotate on the circumference. .

以下、前記竪型ミル1の作動について説明する。   Hereinafter, the operation of the vertical mill 1 will be described.

前記粉砕テーブル6が前記テーブル駆動装置5により回転され、前記1次空気供給口8より1次空気が導入された状態で、前記給炭機4より前記給炭管23に塊状の石炭が供給される。   The pulverizing table 6 is rotated by the table driving device 5, and lump coal is supplied from the coal feeder 4 to the coal supply pipe 23 in a state where primary air is introduced from the primary air supply port 8. The

該給炭管23を流下した塊状の石炭は前記給炭分岐管28により分岐され、各給炭分岐管28を流下して、前記テーブルセグメント17の前記加圧ローラ16,16との間に落下する。   The massive coal that has flowed down the coal supply pipe 23 is branched by the coal supply branch pipes 28, flows down the respective coal supply branch pipes 28, and falls between the pressure rollers 16 and 16 of the table segment 17. To do.

該加圧ローラ16の直前に落下した塊状の石炭は直ちに、該加圧ローラ16に噛込まれ、粉砕される。   The massive coal that has fallen immediately before the pressure roller 16 is immediately caught by the pressure roller 16 and crushed.

前記加圧ローラ16により粉砕された石炭は粉状となり、粉状の石炭は前記エアポート11を吹上がる1次空気に乗って上昇する。   The coal pulverized by the pressure roller 16 becomes powdery, and the powdered coal rises on the primary air blowing up the air port 11.

又、落下した際、前記粉砕テーブル6上で弾み、該粉砕テーブル6を跳越えようとした塊状の石炭は、前記飛跳防止板18によって弾かれて前記粉砕テーブル6上に戻され、直ちに粉砕される。従って、前記塊状の石炭が、前記給炭分岐管28から前記粉砕テーブル6に供給されて前記加圧ローラ16に噛込まれる迄の時間は著しく短縮され、噛込み率が向上する。   Further, when falling, the lump of coal that bounces on the crushing table 6 and tries to jump over the crushing table 6 is bounced by the jumping prevention plate 18 and returned to the crushing table 6 to be crushed immediately. Is done. Accordingly, the time from when the massive coal is supplied from the coal supply branch pipe 28 to the pulverization table 6 and caught by the pressure roller 16 is remarkably shortened, and the biting rate is improved.

又、塊状の石炭が、直接前記加圧ローラ16の噛込み位置に供給され、該加圧ローラ16は常に塊状の石炭を粉砕する状態となるので、該加圧ローラ16の自励振動の発生が抑制される。   In addition, the massive coal is directly supplied to the biting position of the pressure roller 16, and the pressure roller 16 is always in a state of pulverizing the massive coal, so that the self-excited vibration of the pressure roller 16 is generated. Is suppressed.

粉砕されて粉状となった石炭は、前記粉砕テーブル6の上面と前記飛跳防止板18との間を通過し、前記エアポート11を吹上がる1次空気に乗って上昇する(以下、1次混合空気と称す)。上記した様に、前記飛跳防止板18の少なくとも外側端は、1次混合空気の流れを妨げない様前記エアポート11よりも内側に位置し、前記飛跳防止板18を支える前記支持板21も又、1次混合空気の流れを妨げない様鉛直に設けられている。   The pulverized coal passes between the upper surface of the pulverization table 6 and the jump prevention plate 18 and rises on the primary air blowing up the air port 11 (hereinafter referred to as primary). Called mixed air). As described above, at least the outer end of the jump preventing plate 18 is located inside the air port 11 so as not to disturb the flow of primary mixed air, and the support plate 21 that supports the jump preventing plate 18 is also provided. Moreover, it is provided vertically so as not to obstruct the flow of the primary mixed air.

前記コールシールド19に対向する部分の前記エアポート11から吹上がった1次混合空気は、前記コールシールド19に衝突し、1次混合空気中の粉状石炭の内、粒径の大きなものは前記粉砕テーブル6上に落下し、更に粉砕される。   The primary mixed air blown up from the air port 11 at the portion facing the call shield 19 collides with the call shield 19, and among the pulverized coal in the primary mixed air, the one having a large particle diameter is pulverized. It falls on the table 6 and is further pulverized.

従って、前記粉砕テーブル6を跳越えようとした塊状の石炭は、前記飛跳防止板18によって前記粉砕テーブル6上に戻されて粉砕され、1次混合空気中の粉状石炭の内、粒径の大きなものは前記コールシールド19によって分離されるので、前記分級室9を上昇する過程で重力によって分離する分級に比べ、迅速に効率よく分級される。   Therefore, the lump coal that has jumped over the crushing table 6 is returned to the crushing table 6 by the jump prevention plate 18 and pulverized, and the particle size of the powdered coal in the primary mixed air is reduced. Are separated by the call shield 19, so that classification is performed more quickly and efficiently than classification by gravity in the process of ascending the classification chamber 9.

上昇した1次混合空気は、前記給炭管23を中心に回転する前記ブレード27を横切って前記分級機26内部に流入し、更に前記出炭部ハウジング22の下端開口部から該出炭部ハウジング22内部に流入する。   The raised primary mixed air flows into the classifier 26 across the blade 27 rotating around the coal supply pipe 23, and further from the lower end opening of the coal output portion housing 22. 22 flows into the interior.

1次混合空気が前記ブレード27を横切る際に粒径の大きい石炭粉は、前記ブレード27に衝突して落下する。粒径の小さい微粉炭のみが1次混合空気に乗って前記分級機26内に流入し、更に前記出炭部ハウジング22を経て、前記微粉炭送給管24より出炭され、ボイラのバーナ(図示せず)に供給される。   When the primary mixed air crosses the blade 27, the coal powder having a large particle size collides with the blade 27 and falls. Only pulverized coal with a small particle diameter rides on the primary mixed air and flows into the classifier 26, and further through the coal outlet housing 22, is discharged from the pulverized coal feed pipe 24, and the boiler burner ( (Not shown).

次に、前記給炭分岐管28の下端部の形状について説明する。   Next, the shape of the lower end portion of the coal supply branch pipe 28 will be described.

図3(A)は、給炭分岐管28の下端の切口を水平に形成したものである。又図3(B)は、給炭分岐管28の下端の切口を中心側が粉砕テーブル面から離反する様に傾斜させたものであり、更に外周側の管壁28aを垂直とし、流下した塊状の石炭が前記管壁28aに衝突して垂直に落下する様にしたものである。又、図3(C)は、給炭分岐管28の下端部を湾曲させ、下端での軸心が鉛直、又は略鉛直となる様にしたものである。   FIG. 3A shows a horizontal cut at the lower end of the coal supply branch pipe 28. FIG. 3 (B) shows the bottom end of the coal supply branch pipe 28 inclined so that the center side is separated from the pulverizing table surface, and the pipe wall 28a on the outer peripheral side is vertical, and the flowed-down lump-like shape. The coal collides with the pipe wall 28a and falls vertically. FIG. 3C shows a case where the lower end portion of the coal supply branch pipe 28 is curved so that the axial center at the lower end is vertical or substantially vertical.

前記給炭分岐管28の下端部を図3(B)、図3(C)の様にすることで、落下する塊状の石炭が鉛直に落下し、外周方向への飛跳ねを防止できる。又、前記給炭分岐管28下端部の軸心が前記加圧ローラ16の噛込み位置側に傾斜する様に傾斜させれば、塊状の石炭が噛込み位置に向って落下する様になり更に噛込み性が向上する。   By making the lower end portion of the coal supply branch pipe 28 as shown in FIGS. 3 (B) and 3 (C), falling lump coal falls vertically, and jumping in the outer peripheral direction can be prevented. Further, if the shaft center of the lower end portion of the coal supply branch pipe 28 is inclined so as to incline toward the biting position of the pressure roller 16, the lump coal is dropped toward the biting position. Biting property is improved.

尚、前記加圧ローラ16,16間への石炭の供給方法としては、前記ハウジング3を水平方向に貫通する給炭管を、前記ローラ加圧装置12,12との間に設け、スクリューフィーダ等の供給装置により塊状の石炭を供給する様にしてもよい。   As a method for supplying coal between the pressure rollers 16 and 16, a coal supply pipe penetrating the housing 3 in the horizontal direction is provided between the roller pressure devices 12 and 12, and a screw feeder or the like. You may make it supply lump coal with the supply apparatus of.

又、図示される前記給炭分岐管28は、3分岐であるが、前記加圧ローラ16が2つの場合は、2分岐とする等、前記加圧ローラ16の数に対応させて分岐する様にする。   The illustrated coal supply branch pipe 28 has three branches. However, when the number of the pressure rollers 16 is two, the number of the pressure rollers 16 may be branched. To.

本発明の実施の形態を示す立断面図である。It is an elevation sectional view showing an embodiment of the invention. 図1のA矢視図である。It is A arrow directional view of FIG. (A)(B)(C)は給炭分岐管下端部の形状を示す説明図である。(A) (B) (C) is explanatory drawing which shows the shape of a coal-feeding branch pipe lower end part.

符号の説明Explanation of symbols

1 竪型ミル
5 テーブル駆動装置
6 粉砕テーブル
8 1次空気供給口
9 分級室
11 エアポート
12 ローラ加圧装置
16 加圧ローラ
18 飛跳防止板
19 コールシールド
22 出炭部ハウジング
23 給炭管
24 微粉炭送給管
25 回転駆動部
26 分級機
28 給炭分岐管
28a 管壁
DESCRIPTION OF SYMBOLS 1 Vertical mill 5 Table drive device 6 Grinding table 8 Primary air supply port 9 Classification chamber 11 Airport 12 Roller pressurization device 16 Pressurization roller 18 Jump prevention plate 19 Call shield 22 Carburization part housing 23 Coal supply pipe 24 Fine powder Charcoal feed pipe 25 Rotation drive part 26 Classifier 28 Coal feed branch pipe 28a Pipe wall

Claims (5)

分級室を形成するハウジングと、該ハウジングの下部に収納され、回転駆動される粉砕テーブルと、該粉砕テーブルに加圧ローラを押圧し、前記粉砕テーブル上の石炭を粉砕する複数のローラ加圧装置と、塊状石炭を前記粉砕テーブルの前記加圧ローラの間に供給する給炭管とを具備することを特徴とする竪型ミル。   A housing forming a classification chamber, a crushing table housed in a lower part of the housing and driven to rotate, and a plurality of roller pressurizing devices that crush the coal on the crushing table by pressing a pressure roller against the crushing table And a coal feed pipe for supplying the bulk coal between the pressure rollers of the crushing table. 前記給炭管は前記ハウジングの中心に鉛直に設けられ、該給炭管の下端部は複数の給炭分岐管に分岐し、該給炭分岐管の下端部は前記加圧ローラと加圧ローラとの間に開口する請求項1の竪型ミル。   The coal supply pipe is vertically provided at the center of the housing, and a lower end portion of the coal supply pipe branches into a plurality of coal supply branch pipes, and a lower end portion of the coal supply branch pipe includes the pressure roller and the pressure roller. The vertical mill according to claim 1, which opens between the two. 前記給炭管は前記ハウジングの前記ローラ加圧装置の間を貫通する様に設けられた請求項1の竪型ミル。   The vertical mill according to claim 1, wherein the coal supply pipe is provided so as to penetrate between the roller pressing devices of the housing. 前記粉砕テーブルで飛跳ねた塊状石炭を弾返す飛跳防止部材を前記ローラ加圧装置の間に配設した請求項1の竪型ミル。   The vertical mill according to claim 1, wherein a jump preventing member that repels the massive coal that has jumped on the crushing table is disposed between the roller pressure devices. 前記給炭分岐管の下端の軸心は、前記加圧ローラの噛込み位置に向って傾斜する請求項2の竪型ミル。   The vertical mill according to claim 2, wherein an axis of a lower end of the coal supply branch pipe is inclined toward a biting position of the pressure roller.
JP2008330092A 2008-12-25 2008-12-25 Vertical mill Pending JP2010149052A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103071565A (en) * 2013-01-14 2013-05-01 莱歇研磨机械制造(上海)有限公司 Installation structure of grinding roller casing of roller type grinder
CN106179615A (en) * 2016-08-23 2016-12-07 南京凯盛国际工程有限公司 A kind of vertical mill feeding device
CN106563530A (en) * 2016-08-17 2017-04-19 合肥中亚建材装备有限责任公司 A detachable material layer stabilizing device for powder returning for a vertical type ash grinding hopper
CN109963654A (en) * 2016-11-15 2019-07-02 诺曼艾索工艺技术有限公司 Grinding machine

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103071565A (en) * 2013-01-14 2013-05-01 莱歇研磨机械制造(上海)有限公司 Installation structure of grinding roller casing of roller type grinder
CN106563530A (en) * 2016-08-17 2017-04-19 合肥中亚建材装备有限责任公司 A detachable material layer stabilizing device for powder returning for a vertical type ash grinding hopper
CN106179615A (en) * 2016-08-23 2016-12-07 南京凯盛国际工程有限公司 A kind of vertical mill feeding device
CN109963654A (en) * 2016-11-15 2019-07-02 诺曼艾索工艺技术有限公司 Grinding machine
CN109963654B (en) * 2016-11-15 2022-04-12 诺曼艾索工艺技术有限公司 Grinding machine

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