JPH1133494A - Method and device for adjusting classification ratio in fluidized-bed classifier - Google Patents
Method and device for adjusting classification ratio in fluidized-bed classifierInfo
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- JPH1133494A JPH1133494A JP18980897A JP18980897A JPH1133494A JP H1133494 A JPH1133494 A JP H1133494A JP 18980897 A JP18980897 A JP 18980897A JP 18980897 A JP18980897 A JP 18980897A JP H1133494 A JPH1133494 A JP H1133494A
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Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、コークス炉用石炭
を流動層式分級装置を用いて微粉炭と粗粒炭とに分級す
る方法および装置に関する。The present invention relates to a method and an apparatus for classifying coal for coke ovens into pulverized coal and coarse coal using a fluidized bed classifier.
【０００２】[0002]
【従来の技術】コークス生産に際し、コークスの品質向
上およびコークス炉での生産性向上を目的としてコーク
ス炉装入前に装入炭を乾燥することが行われている。こ
の乾燥した装入炭をコークス炉まで搬送するに際し、装
入炭に含まれる微粉炭が発塵し、またコークス炉内でも
装入炭の乾留時に発生するガスやタールにこの微粉炭が
随伴するいわゆるキャリーオーバー現象が発生する。こ
の発塵およびキャリーオーバー現象を防止するため、乾
燥した装入炭を発塵しやすい粒径の微粉炭とそれより粒
径の大きい粗粒炭に分級し、この微粉炭に添加剤を加え
て擬似粒子化した上でコークス炉に装入する方法が知ら
れている。2. Description of the Related Art In the production of coke, for the purpose of improving the quality of coke and the productivity in a coke oven, it has been practiced to dry the charged coal before charging the coke oven. The pulverized coal included in the charged coal is dusted when the dried charged coal is transported to the coke oven, and the pulverized coal accompanies the gas and tar generated during the dry distillation of the charged coal even in the coke oven. A so-called carryover phenomenon occurs. In order to prevent this dusting and carry-over phenomenon, the dry charged coal is classified into pulverized coal having a particle size that is easy to generate dust and coarse coal having a larger particle size, and additives are added to the pulverized coal. There is known a method of charging a coke oven after forming into pseudo particles.
【０００３】装入炭を微粉炭と粗粒炭に分級する方法と
しては、装入炭の乾燥前あるいは乾燥後にサイクロン分
級機等を用いて独立して分級のみを行う方法もあるが、
流動層式乾燥分級機等を用いて乾燥と分級を同時に行う
方法が知られており、乾燥と分級を独立に行う方法に比
較して合理的で効果の大きい方法である。特開昭６２−
１９２４８６号公報では、乾燥機能と分級機能を兼ね備
えた流動層式乾燥分級機を用い、前段階では乾燥を、後
段階では擬似粒子化物の破壊と微粉炭の分級を行う方法
が開示されている。また特開昭６３−７５０８９号公報
には、乾燥微粉炭をコークス炉に装入する場合に、装入
炭粒度分布や分級率により装入嵩密度が低下したり制御
ができなくなることに対して、分級粒子径を変化させ分
級率を調整して装入嵩密度を高める技術が開示されてい
る。As a method of classifying charged coal into pulverized coal and coarse coal, there is a method in which only classification is performed independently using a cyclone classifier or the like before or after drying of charged coal.
A method of simultaneously performing drying and classification using a fluidized bed type dry classifier or the like is known, and is a rational and effective method compared to a method in which drying and classification are performed independently. JP-A-62-2
Japanese Patent Application Laid-Open No. 192486 discloses a method in which a fluidized bed type dry classifier having both a drying function and a classification function is used, and drying is performed in a previous stage, and pseudo-particulate matter is broken and pulverized coal is classified in a later stage. Japanese Patent Application Laid-Open No. 63-75089 describes that when dry pulverized coal is charged into a coke oven, the charged bulk density is reduced or the control cannot be performed due to the charged coal particle size distribution or classification rate. A technique has been disclosed in which the classification density is adjusted by changing the classification particle size to increase the charged bulk density.
【０００４】[0004]
【発明が解決しようとする課題】流動層式乾燥分級機に
おいては、流動化と乾燥のために常温のあるいは予熱さ
れたガスが流動化部に供給され、このガスが流動化部の
上方のフリーボード部を上昇する際に微粉炭を伴い、そ
れによって微粉炭と粗粒炭が分級される。この供給ガス
量は、流動層形成に必要な流動化部での空塔速度や、流
動床の場合は更に石炭の搬送性を考慮して設定されなけ
ればならない。また、乾燥前の装入炭水分含有率と目標
とする乾燥後の装入炭水分含有率、更に供給ガスの温度
に応じて、乾燥のために必要な供給ガス量が決定され
る。一方、所定の目標粒径を境に微粉炭と粗粒炭とに分
級するには、フリーボード部を通過するガスの流速を調
整し、分級の目標粒径の装入炭のガス中降下速度を上昇
ガス流速と一致させる必要がある。従って、流動化部形
成および装入炭乾燥の条件によって供給ガス量が決定さ
れると、その供給ガス量において目標とする上昇ガス流
速が得られるようにフリーボード部の断面積を計算し、
流動層式乾燥分級機のフリーボード部をその断面積とな
るように製作する。In a fluidized bed type dry classifier, a gas at normal temperature or preheated is supplied to a fluidizing section for fluidization and drying, and the gas is supplied to a free space above the fluidizing section. The pulverized coal accompanies the ascending of the board part, whereby the pulverized coal and the coarse coal are classified. The amount of the supplied gas must be set in consideration of the superficial velocity in the fluidizing section necessary for forming the fluidized bed and, in the case of a fluidized bed, the transportability of coal. The supply gas amount required for drying is determined according to the charged coal moisture content before drying, the target charged coal moisture content after drying, and the temperature of the supplied gas. On the other hand, in order to classify the coal into pulverized coal and coarse coal based on a predetermined target particle size, the flow velocity of the gas passing through the freeboard section is adjusted, and the falling rate of the charged coal having the target particle size for classification in the gas is adjusted. Must match the rising gas flow rate. Therefore, when the supply gas amount is determined by the conditions of the fluidized portion formation and the charged coal drying, the cross-sectional area of the freeboard part is calculated so that a target ascending gas flow rate is obtained at the supply gas amount,
The free board part of the fluidized bed type dry classifier is manufactured to have the cross-sectional area.
【０００５】しかし、上記従来技術に基づいた流動層式
乾燥分級機においては、設計時に想定した装入炭処理
量、付着水分条件、乾燥後水分条件のままで操業する上
では問題は生じないが、同じ装置を用いて装入炭処理量
を増減したり水分条件が変動したりすると、供給すべき
ガス量が設計条件から変動してしまい、その結果フリー
ボード部でのガス流速が変動して分級すべき微粉炭の最
大粒子径が変動してしまうという不都合が生じる。ま
た、分級条件が変わり分級すべき微粉炭の最大粒子径を
後から変更しようとした場合、フリーボード部のガス流
速を変動しようとして供給ガス流量を変更すると、流動
化部形成ガス条件、乾燥ガス条件から外れてしまうとい
う不都合が生じる。[0005] However, in the fluidized bed type dry classifier based on the above-mentioned prior art, there is no problem in operating with the charged coal treatment amount, adhesion moisture condition, and moisture condition after drying assumed at the time of design. However, if the same equipment is used to increase or decrease the amount of coal to be treated or the moisture conditions fluctuate, the amount of gas to be supplied fluctuates from the design conditions, and as a result, the gas flow rate in the freeboard section fluctuates. The disadvantage is that the maximum particle size of the pulverized coal to be classified fluctuates. If the classification conditions change and the maximum particle size of the pulverized coal to be classified is changed later, if the supply gas flow rate is changed to change the gas flow rate in the freeboard section, the fluidization section formation gas conditions, dry gas The inconvenience of deviating from the condition occurs.
【０００６】[0006]
【課題を解決するための手段】本発明は、上記問題点を
解決するためになされたものであり、その要旨とすると
ころは以下の通りである。 （１）流動層式分級装置を用い微粉炭と粗粒炭とに分級
する工程を有するコークス炉に装入する石炭の事前処理
工程において、フリーボード部にフリーボード部空間を
１室の主分級室と１室又は２室以上の副分級室に分割す
る仕切り板を挿入し、かつそれぞれの室の上部に排気ダ
クトを設け、副分級室の上部にガス流量調整装置を設
け、該副分級室の排出ガス量の調整によって主分級室の
上昇ガス流速を調整することにより、分級する微粉炭の
最大粒径を調整することを特徴とする流動層式分級装置
における石炭分級粒径調整方法。 （２）流動層式分級装置を用い微粉炭と粗粒炭とに分級
する工程を有するコークス炉に装入する石炭の事前処理
工程において、フリーボード部にフリーボード部空間を
１室の主分級室と１室又は２室以上の副分級室に分割す
る仕切り板を挿入し、該仕切り板は移動可能であって主
分級室と副分級室の断面積を変更することが可能であ
り、かつそれぞれの室の上部に排気ダクトを設け、副分
級室の上部にガス流量調整装置を設け、主分級室と副分
級室の断面積の調整及び副分級室ガス流量調整装置の調
整によって主分級室の上昇ガス流速を調整することによ
り、分級する微粉炭の最大粒径を調整することを特徴と
する流動層式分級装置における石炭分級粒径調整方法。 （３）流動層式分級装置を用い微粉炭と粗粒炭とに分級
する工程を有するコークス炉に装入する石炭の事前処理
工程において、フリーボード部にフリーボード部空間を
１室の主分級室と１室又は２室以上の副分級室に分割す
る仕切り板を挿入し、該仕切り板は移動可能であって主
分級室と副分級室の断面積を変更することが可能であ
り、かつそれぞれの室の上部に排気ダクトを設け、副分
級室の上部にガス流量調整オリフィスを設け、主分級室
と副分級室の断面積の調整によって主分級室の上昇ガス
流速を調整することにより、分級する微粉炭の最大粒径
を調整することを特徴とする流動層式分級装置における
石炭分級粒径調整方法。SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and the gist thereof is as follows. (1) In the pre-treatment process of coal charged into a coke oven having a process of classifying into pulverized coal and coarse-grained coal using a fluidized bed classifier, a main classifier of a freeboard part space in a freeboard part in one room. A partition plate for dividing the chamber into one or two or more sub-classification chambers is inserted, and an exhaust duct is provided above each chamber, and a gas flow control device is provided above the sub-classification chamber. A method for adjusting the maximum gas diameter of the pulverized coal to be classified by adjusting the ascending gas flow rate of the main classification chamber by adjusting the amount of exhaust gas of the method. (2) In the pre-treatment process of coal charged into a coke oven having a process of classifying into pulverized coal and coarse-grained coal using a fluidized bed classifier, a main classifier in which the freeboard space is one room in the freeboard region A partition plate for dividing into a room and one or two or more sub-classification rooms is inserted, the partition plate is movable, and a cross-sectional area of the main classification room and the sub-classification room can be changed; and An exhaust duct is provided at the top of each chamber, and a gas flow control device is provided at the top of the sub-classification room. Adjustment of the cross-sectional area of the main classification room and sub-classification room and adjustment of the sub-classification room gas flow control device A method of adjusting the maximum particle size of pulverized coal to be classified by adjusting the ascending gas flow rate of the coal. (3) In the pre-treatment step of coal charged into a coke oven having a step of classifying into pulverized coal and coarse-grained coal using a fluidized bed classifier, a main classification of one freeboard part space in a freeboard part in a freeboard part A partition plate for dividing into a room and one or two or more sub-classification rooms is inserted, the partition plate is movable, and a cross-sectional area of the main classification room and the sub-classification room can be changed; and By providing an exhaust duct at the top of each chamber, providing a gas flow rate adjusting orifice at the top of the sub-classification chamber, and adjusting the ascending gas flow rate of the main classification chamber by adjusting the cross-sectional area of the main classification chamber and the sub-classification chamber, A method for adjusting the particle size of coal in a fluidized bed classifier, wherein the maximum particle size of the pulverized coal to be classified is adjusted.
【０００７】（４）流動層式分級装置を用い微粉炭と粗
粒炭とに分級するコークス炉に装入する石炭の事前処理
装置において、フリーボード部にフリーボード部空間を
１室の主分級室と１室又は２室以上の副分級室に分割す
る仕切り板を挿入し、かつそれぞれの室の上部に排気ダ
クトを設け、副分級室の上部にガス流量調整装置を設け
たことを特徴とする流動層式分級装置。 （５）流動層式分級装置の供給ガス量範囲の最大供給量
と最小供給量および主分級室のフリーボード部における
最高流速と最低流速を予め定め、主分級室のフリーボー
ド部の断面積は供給ガスの前記最小供給量のガスが主分
級室を通過したときに前記最高流速以上の流速が得られ
る断面積であり、主分級室と副分級室のフリーボード部
の全体断面積は供給ガスの前記最大供給量のガスが該全
体断面積の空間を通過したときにガス流速として前記最
低流速以下の流速が得られる断面積であることを特徴と
する上記（４）に記載の流動層式分級装置。 （６）流動層式分級装置を用い微粉炭と粗粒炭とに分級
するコークス炉に装入する石炭の事前処理装置におい
て、フリーボード部にフリーボード部空間を１室の主分
級室と１室又は２室以上の副分級室に分割する仕切り板
を挿入し、該仕切り板は移動可能であって主分級室と副
分級室の断面積を変更することが可能であり、かつそれ
ぞれの室の上部に排気ダクトを設け、副分級室の上部に
ガス流量調整装置を設けたことを特徴とする流動層式分
級装置。 （７）仕切り板の長さが変更可能であることを特徴とす
る上記（６）に記載の流動層式分級装置。 （８）副分級室のガス流量調整装置がガス流量調整ダン
パーであることを特徴とする上記（４）乃至（７）に記
載の流動層式分級装置。 （９）副分級室のガス流量調整装置がガス流量調整用オ
リフィスであることを特徴とする上記（６）又は（７）
に記載の流動層式分級装置。 （１０）副分級室の上部に排気ダクトとガス流量調整装
置を設置せず、ガスはもっぱら主分級室のみを通過する
ことを特徴とする上記（６）又は（７）に記載の流動層
式分級装置。(4) In a pretreatment apparatus for coal charged into a coke oven for classifying into pulverized coal and coarse coal using a fluidized bed type classification apparatus, a freeboard section has a freeboard section space of one chamber in a freeboard section. A partition plate for dividing the chamber into one or two or more sub-classification chambers is inserted, and an exhaust duct is provided at the top of each chamber, and a gas flow control device is provided at the top of the sub-classification chamber. Fluidized bed classifier. (5) The maximum supply amount and the minimum supply amount of the supply gas amount range of the fluidized bed type classifier and the maximum flow velocity and the minimum flow velocity in the free board part of the main classification chamber are determined in advance. The cross-sectional area at which a flow rate equal to or higher than the maximum flow rate is obtained when the gas with the minimum supply amount of the supply gas passes through the main classification chamber, and the total cross-sectional area of the free board portion of the main classification chamber and the sub-classification chamber is the supply gas The fluidized bed system according to the above (4), wherein when the gas of the maximum supply amount passes through the space having the entire cross-sectional area, a gas flow velocity is equal to or less than the minimum flow velocity. Classifier. (6) In a pretreatment device for coal charged into a coke oven for classifying into pulverized coal and coarse-grained coal using a fluidized bed classifier, a freeboard part has a freeboard part space and one main classification chamber. A partition plate for dividing into a room or two or more sub-classification rooms is inserted, the partition plate is movable, the cross-sectional area of the main classification room and the sub-classification room can be changed, and each room can be changed. A fluidized bed classifier, wherein an exhaust duct is provided at the upper part of the tank, and a gas flow controller is provided at the upper part of the sub-classifying chamber. (7) The fluidized bed classifier according to the above (6), wherein the length of the partition plate can be changed. (8) The fluidized-bed classifier according to any one of (4) to (7), wherein the gas flow control device in the sub-classification chamber is a gas flow control damper. (9) The gas flow control device of the sub-classification chamber is a gas flow control orifice (6) or (7).
2. A fluidized bed type classification device according to item 1. (10) The fluidized bed system according to the above (6) or (7), wherein the exhaust gas and the gas flow rate control device are not installed above the sub-classification chamber, and the gas passes only through the main classification chamber. Classifier.
【０００８】[0008]
【発明の実施の形態】流動層式分級装置には、バッチ運
転式と目皿上を石炭が移動する連続式流動床式の双方を
含み、そのどちらも本発明に適用することが可能であ
る。また、分級機能のみでなく、装入炭の乾燥機能ある
いは加熱機能を備えることができる。その場合、流動化
のための供給ガスが装入炭の乾燥あるいは加熱を行うこ
ととなる。フリーボード部とは、石炭の流動化部の上部
であってガスが一定速度で上昇し一定粒径以下の粒径の
微粉炭を上方に運搬する部分をいう。BEST MODE FOR CARRYING OUT THE INVENTION The fluidized bed classifier includes both a batch operation type and a continuous fluidized bed type in which coal moves on a perforated plate, and both of them can be applied to the present invention. . Further, not only a classification function but also a drying function or a heating function of the charged coal can be provided. In that case, the supply gas for fluidization will dry or heat the charged coal. The free board part is an upper part of the coal fluidization part, in which the gas rises at a constant speed and conveys pulverized coal having a particle size of a certain particle size or less upward.
【０００９】本発明は、装入炭処理量の変動、乾燥条件
（乾燥前付着水分条件、乾燥後水分条件）の変動に伴っ
て流動層式乾燥分級機への供給ガス量が変動した場合で
もフリーボード部の上昇ガス流速を一定に保つため、あ
るいは分級すべき微粉炭の最大粒径が変動してフリーボ
ード部の上昇ガス流速を変更する場合でも供給ガス量を
一定に保つための方法およびそれらの方法を実現するた
めの装置を含む。分級室を上昇する排ガス総流量は、ガ
ス供給量と発生した水蒸気との合計である。The present invention can be applied to a case where the amount of gas supplied to a fluidized bed type dry classifier fluctuates due to fluctuations in the amount of charged coal and fluctuations in drying conditions (adherent moisture conditions before drying and moisture conditions after drying). A method for maintaining a constant supply gas flow rate in order to keep the rising gas flow rate in the freeboard section constant or to change the rising gas flow rate in the freeboard section due to fluctuations in the maximum particle size of the pulverized coal to be classified; Includes equipment for implementing those methods. The total flow rate of the exhaust gas rising in the classification chamber is the sum of the gas supply amount and the generated steam.
【００１０】本発明の第１の実施態様を図１に示す。図
１はバッチ運転式流動層式分級装置を用いているが、連
続式流動床式分級装置を用いてもかまわない。供給ガス
と蒸発した水蒸気分を合計したガスが上昇するフリーボ
ード部３は、仕切り板６によって１室の主分級室４と１
室または２室以上の副分級室５とに分割される。それぞ
れの室の上部に排気ダクトを設け、副分級室５の上部に
はガス流量調整装置としてガス流量調整ダンパー１０を
設ける。主分級室４の上部にもガス流量調整ダンパー９
を設けてもよい。分級すべき微粉炭の最大粒径が定まる
と、その粒子径の粒子の終端速度と等しい速度として分
級のためのガス流速が定まる。本発明法においては、主
分級室４の上昇ガス流速をこの分級のためのガス流速と
一致させる。また、副分級室５は主分級室４のガス流速
を一定に保つための調整機能を担うが、副分級室５のガ
ス流速は常に主分級室４のガス流速と同等かそれよりも
低い値を維持する。これによって、副分級室５から排出
される微粉炭は常に分級すべき微粉炭の最大粒径よりも
小さい粒径のもののみとなり、分級条件を維持すること
ができることとなる。主分級室４のガス通過部の断面積
は一定なので、分級条件即ち分級すべき微粉炭の最大粒
径が決まれば主分級室４のガス流速が決まり、それに基
づいて主分級室４を通過するガス流量も定まる。排ガス
総流量を最初に設定する場合、あるいは装入炭処理量や
乾燥条件の変動によって排ガス総流量が変動した場合、
排ガス総流量から主分級室４を通過するガス流量を差し
引いた流量が副分級室５を通過すべきガス流量となる。
従って、副分級室上部のガス流量調整ダンパー１０の調
整によって副分級室５のガス流量を調整し、主分級室４
と副分級室５のガス流量の分配を調整することにより、
主分級室４のガス流速を調整し、主分級室４を経由して
分級される微粉炭の最大粒径を目標と一致させることが
可能になる。上述したように副分級室５のガス流速は常
に主分級室ガス流速よりも遅くする必要があるので、操
業条件の変動範囲に応じて副分級室５のガス通過部断面
積は十分に大きく設計する必要がある。主分級室４の上
部にもガス流量調整ダンパー９を設けることが可能であ
り、主分級室４と副分級室５の双方のダンパーの調整に
より、より容易にガス流量を分配することが可能にな
る。FIG. 1 shows a first embodiment of the present invention. Although FIG. 1 uses a batch operation type fluidized bed type classification device, a continuous type fluidized bed type classification device may be used. The freeboard section 3 in which the gas, which is the sum of the supply gas and the evaporated water vapor, rises, is divided into one main classification chamber 4 and 1 by a partition plate 6.
Room or two or more sub-classification rooms 5. An exhaust duct is provided above each of the chambers, and a gas flow control damper 10 is provided above the sub-classification chamber 5 as a gas flow control device. Gas flow control damper 9 is also located above main classifying chamber 4
May be provided. When the maximum particle size of the pulverized coal to be classified is determined, the gas flow rate for classification is determined as a speed equal to the terminal speed of the particles having the particle size. In the method of the present invention, the rising gas flow velocity in the main classification chamber 4 is made to coincide with the gas flow velocity for this classification. The sub-classification chamber 5 has an adjusting function for keeping the gas flow rate in the main classification chamber 4 constant, but the gas flow rate in the sub-classification chamber 5 is always equal to or lower than the gas flow rate in the main classification chamber 4. To maintain. As a result, the pulverized coal discharged from the sub-classification chamber 5 always has only a particle size smaller than the maximum particle size of the pulverized coal to be classified, and the classification conditions can be maintained. Since the cross-sectional area of the gas passage portion of the main classification chamber 4 is constant, if the classification condition, that is, the maximum particle size of the pulverized coal to be classified is determined, the gas flow velocity of the main classification chamber 4 is determined, and the gas passes through the main classification chamber 4 based on this. The gas flow rate is also determined. If the total exhaust gas flow rate is set first, or if the total exhaust gas flow rate fluctuates due to fluctuations in the amount of charged coal and drying conditions,
The flow rate obtained by subtracting the gas flow rate passing through the main classification chamber 4 from the exhaust gas total flow rate is the gas flow rate that should pass through the sub-classification chamber 5.
Therefore, the gas flow rate of the sub-classification chamber 5 is adjusted by adjusting the gas flow rate adjustment damper 10 above the sub-classification chamber, and
And the distribution of the gas flow rate in the sub-classification chamber 5
By adjusting the gas flow velocity in the main classification chamber 4, it becomes possible to make the maximum particle size of the pulverized coal classified through the main classification chamber 4 coincide with the target. As described above, the gas flow rate in the sub-classification chamber 5 must always be lower than the gas flow rate in the main classification chamber. There is a need to. A gas flow rate adjusting damper 9 can be provided also in the upper part of the main classifying chamber 4, and the gas flow rate can be more easily distributed by adjusting the dampers of both the main classifying chamber 4 and the sub-classifying chamber 5. Become.
【００１１】本実施態様においては、供給ガス量が最も
少なくなる場合は副分級室５のダンパー１０を閉として
副分級室ガス流量をゼロにした場合である。従って、主
分級室４のガス通過部の断面積は、考えられる操業変動
範囲内において排ガス総流量が最低になり、かつ主分級
室ガス流速が最大になる条件においてそのガス流速が維
持できる断面積を計算し、その計算された断面積よりも
実際の断面積を等しいか小さくすることが必要である。
また、副分級室５のガス通過部の断面積は、考えられる
操業変動範囲内において排ガス総流量が最大になり、か
つ主分級室ガス流速が最低になる条件において、副分級
室５のガス流速が主分級室４のガス流速を越えないよ
う、十分な断面積を確保する必要がある。このような条
件を満足するように装置を設計するためには、流動層式
分級装置の供給ガス量範囲の最大供給量と最小供給量お
よび主分級室のフリーボード部におけるガス流速範囲の
最高流速と最低流速を予め定め、主分級室のフリーボー
ド部の断面積は供給ガスの最小供給量のガスが主分級室
を通過したときに最高流速以上の流速が得られる断面積
であり、主分級室と副分級室のフリーボード部の全体断
面積は供給ガスの最大供給量のガスが該全体断面積の空
間を通過したときにガス流速として最低流速以下の流速
が得られる断面積であるように主分級室と副分級室のフ
リーボード部の断面積を決定することで実現することが
できる。In the present embodiment, the case where the supply gas amount is the smallest is the case where the damper 10 of the sub-classification chamber 5 is closed and the gas flow rate of the sub-classification chamber is set to zero. Therefore, the cross-sectional area of the gas passage portion of the main classification chamber 4 is a cross-sectional area that can maintain the gas flow rate under the condition that the total exhaust gas flow rate is the minimum and the gas flow rate of the main classification chamber is the maximum within the conceivable operating fluctuation range. It is necessary to calculate the actual cross-sectional area to be equal to or smaller than the calculated cross-sectional area.
Further, the cross-sectional area of the gas passage portion of the sub-classification chamber 5 is determined by the gas flow rate of the sub-classification chamber 5 under the condition that the total exhaust gas flow rate is maximum and the gas velocity of the main classification chamber is minimum within the conceivable operation fluctuation range. However, it is necessary to secure a sufficient cross-sectional area so that the gas flow rate does not exceed the gas flow velocity in the main classification chamber 4. In order to design the apparatus to satisfy such conditions, the maximum and minimum supply rates of the gas supply range of the fluidized bed type classification apparatus and the maximum flow rate of the gas flow rate range in the free board section of the main classification chamber are required. And the minimum flow velocity are determined in advance, and the cross-sectional area of the free board portion of the main classification chamber is a cross-sectional area at which a flow rate equal to or higher than the maximum flow velocity is obtained when the minimum supply amount of gas passes through the main classification chamber. The total cross-sectional area of the free board portion of the chamber and the sub-classification chamber is a cross-sectional area at which a gas flow rate equal to or lower than the minimum flow rate is obtained as the gas flow rate when the gas with the maximum supply amount of the supply gas passes through the space of the total cross-sectional area. It can be realized by determining the cross-sectional areas of the free board portions of the main classification room and the sub-classification room.
【００１２】本発明の第２の実施態様を図２に示す。図
２は連続式流動床式流動層分級装置を用いているが、バ
ッチ運転式流動層式分級装置を用いてもかまわない。主
分級室４と副分級室５を設けること、各分級室上部に排
気ダクトを設けること、副分級室上部にガス流量調整装
置としてガス流量調整ダンパー１０を設けることは第１
の実施態様と同様であり、さらに主分級室４と副分級室
５を分割する仕切り板６が移動可能に構成されており、
この仕切り板６の移動によってフリーボード部３におけ
る主分級室４と副分級室５の断面積を変更できることを
特徴としている。この各分級室の断面積の変更機能によ
り、操業条件の変動に伴う設定変更の幅をより広くとる
ことが可能となる。即ち、供給ガス量が増大した場合、
あるいは分級すべき微粉炭の最大粒径を小さくしたい場
合は、副分級室５のダンパー開度増大という手段に加
え、仕切り板６の位置を変動して主分級室４の断面積を
大きくすることにより、一層の大きな操業変動に対処が
可能となる。また、逆に供給ガス量が減少した場合、あ
るいは分級すべき微粉炭の最大粒径を大きくしたい場合
は、副分級室５のダンパー開度を小さくないし全閉とす
る手段に加え、仕切り板６の位置を変動して主分級室４
の断面積を小さく（副分級室５の断面積を大きく）する
ことにより、一層の大きな操業変動に対処が可能とな
る。図３に示すように、主分級室４の上部にもガス流量
調整ダンパー９を設けることが可能であり、主分級室４
と副分級室５の双方のダンパーの調整により、より容易
にガス流量を分配することが可能になる。FIG. 2 shows a second embodiment of the present invention. Although FIG. 2 uses a continuous fluidized bed type fluidized bed classification device, a batch operation type fluidized bed type classification device may be used. Providing the main classifying chamber 4 and the sub-classifying chamber 5, providing an exhaust duct above each classifying chamber, and providing a gas flow rate adjusting damper 10 as a gas flow rate adjusting device above the sub-classifying chamber are first.
The partition plate 6 for dividing the main classification chamber 4 and the sub-classification chamber 5 is configured to be movable.
It is characterized in that the cross-sectional area of the main classification chamber 4 and the sub-classification chamber 5 in the free board section 3 can be changed by the movement of the partition plate 6. The function of changing the cross-sectional area of each classifying chamber makes it possible to increase the range of setting change accompanying a change in operating conditions. That is, when the supply gas amount increases,
Alternatively, when it is desired to reduce the maximum particle size of the pulverized coal to be classified, in addition to the means of increasing the opening degree of the damper in the sub-classifying chamber 5, the position of the partition plate 6 is changed to increase the sectional area of the main classifying chamber 4. Thereby, it is possible to cope with even larger operation fluctuations. Conversely, when the supply gas amount is reduced or when it is desired to increase the maximum particle size of the pulverized coal to be classified, in addition to the means for making the damper opening of the sub-classification chamber 5 small or fully closed, the partition plate 6 Change the position of the main classification room 4
By making the cross-sectional area smaller (the cross-sectional area of the sub-classifying chamber 5 is made larger), it is possible to cope with even larger operation fluctuations. As shown in FIG. 3, it is possible to provide a gas flow rate adjustment damper 9 also in the upper part of the main classification chamber 4.
By adjusting the dampers of both the sub-classification chamber 5 and the sub-classification chamber 5, the gas flow rate can be more easily distributed.
【００１３】仕切り板６の位置変動を可能とするため、
分級装置フリーボード部３の上部および下部に仕切り板
固定梁１８を設け、仕切り板はこの固定梁の上に固定さ
れ、移動機構の動作で固定梁上を移動させることができ
る。In order to make the position of the partition plate 6 variable,
A partition plate fixing beam 18 is provided above and below the classifier free board unit 3, and the partition plate is fixed on the fixed beam, and can be moved on the fixed beam by the operation of the moving mechanism.
【００１４】図２のような連続式流動床式流動層分級乾
燥機を用いた場合、投入された石炭は図２の左から右へ
移動するに従って乾燥が進行する。そのため、副分級室
を経由して排気ダクトへ吸引される微粉炭は、主分級室
を経由する微粉炭に比較して湿分が高い場合がある。こ
のような場合、副分級室を経由した排気ガスは主分級室
経由の排気ガスと混合せず、主分級室経由の微粉炭のみ
をコークス炉へ装入することで装入炭品質を維持するこ
とが可能である。When a continuous fluidized bed type fluidized bed classification dryer as shown in FIG. 2 is used, drying of the fed coal proceeds as it moves from left to right in FIG. For this reason, pulverized coal sucked into the exhaust duct via the sub-classification chamber may have a higher moisture content than pulverized coal via the main classification chamber. In such a case, the exhaust gas that has passed through the sub-classification chamber is not mixed with the exhaust gas that has passed through the main classification chamber, and only the pulverized coal that has passed through the main classification chamber is charged into the coke oven to maintain the coal quality. It is possible.
【００１５】上記第１および第２の実施態様における副
分級室上部のガス流量調整装置として、図１、図２に示
す蝶型弁形状であって蝶型弁の角度を変更することによ
って流量を調整するガス流量調整ダンパー１０のほか、
穴を有する仕切り弁を有し該仕切り弁の位置を変更する
ことによって流量を調整する流量調整装置、開と閉の２
つの状態のうちどちらかを選択する遮断弁等から選択す
ることができ、いずれの調整装置においても、その流量
の調整のための動力として電動モーター、油圧モータ
ー、あるいは手動装置等から選択することができる。The gas flow control device in the upper part of the sub-classification chamber in the first and second embodiments has a butterfly valve shape as shown in FIGS. 1 and 2, and the flow is controlled by changing the angle of the butterfly valve. In addition to the gas flow rate adjustment damper 10 to be adjusted,
A flow control device having a gate valve having a hole and adjusting a flow rate by changing a position of the gate valve;
One of the two states can be selected from a shutoff valve or the like that selects one of the two states, and any of the adjusting devices can select an electric motor, a hydraulic motor, or a manual device as power for adjusting the flow rate. it can.
【００１６】上記第２の実施態様の応用として、本発明
の第３の実施態様においては、第２の実施態様における
副分級室５の上部のガス流量調整ダンパーにかえ、一定
の開口面積を有するガス流量調整用オリフィスを設け
る。この一定開口面積のオリフィスを設けることにより
副分級室５のガス流量が調整され、仕切り板６の位置を
変更することによって主分級室４と副分級室５にそれぞ
れ流れるガス流速を変更することが可能となる。As an application of the second embodiment, in the third embodiment of the present invention, instead of the gas flow rate adjusting damper on the upper part of the sub-classification chamber 5 in the second embodiment, the third embodiment has a fixed opening area. An orifice for gas flow adjustment is provided. By providing the orifice having this fixed opening area, the gas flow rate in the sub-classification chamber 5 is adjusted, and the gas flow rate flowing to the main classification chamber 4 and the sub-classification chamber 5 can be changed by changing the position of the partition plate 6. It becomes possible.
【００１７】さらに第２の実施態様の応用として、本発
明の第４の実施態様においては、第２の実施態様におけ
る副分級室５の上部には排気ダクト８を設けず、ガスは
もっぱら主分級室４のみを通過するものである。仕切り
板６の位置を変更することによって主分級室４のフリー
ボード部３の断面積を変更することができ、これによっ
て各操業条件における排ガス総流量に応じて必要な主分
級室フリーボード部３ガス流速を実現すべく主分級室４
の断面積を設定することが可能である。Further, as an application of the second embodiment, in the fourth embodiment of the present invention, the exhaust duct 8 is not provided above the sub-classification chamber 5 in the second embodiment, and the gas is exclusively used for the main classification. It passes only through the room 4. By changing the position of the partition plate 6, it is possible to change the cross-sectional area of the free board section 3 of the main classification chamber 4, and thereby, the main classification room free board section 3 required according to the total exhaust gas flow rate under each operating condition. Main classification room 4 to achieve gas flow rate
Can be set.
【００１８】分級精度すなわち目標粒径以上と以下の粒
子にきちんと分級する精度は、主分級室４内でのガス流
の乱れを少なくすることが有効であり、そのためには仕
切り板６の断面積を大きくして主分級室４の分級ゾーン
を広くすることが有効である。仕切り板６の上下方向長
さを延長する、すなわちフリーボード部長さを延長する
ことは、上昇するガスの整流効果があり、粒子とガスと
の重力分級性を高めることになるからである。仕切り板
６の上下方向の長さは、操業条件の変更に伴い、各操業
条件毎に最適化するために可変とすることができる。分
級装置の運転中に自動的に仕切り板６の長さを変更する
ように装置を設計することも可能であるが、通常は運転
休止時に手動操作で仕切り板６の長さを変更することで
十分にその目的を達成することができる。The classification accuracy, that is, the accuracy of properly classifying particles having a size equal to or larger than the target particle size, is effective to reduce the turbulence of the gas flow in the main classification chamber 4. It is effective to enlarge the classification zone of the main classification room 4 by increasing the size of the classification zone. This is because extending the length of the partition plate 6 in the vertical direction, that is, extending the length of the freeboard portion, has a rectifying effect on the rising gas, and enhances the gravitational classification of the particles and the gas. The length of the partition plate 6 in the up-down direction can be made variable to optimize for each operating condition in accordance with a change in operating conditions. Although it is possible to design the device to automatically change the length of the partition plate 6 during operation of the classifying device, it is usually possible to manually change the length of the partition plate 6 when the operation is stopped. The purpose can be sufficiently achieved.
【００１９】本発明は、ピンまたは羽根の攪拌機能付き
流動層式乾燥分級機あるいは、攪拌インペラー内蔵型流
動層式乾燥分級機においても適用することができる。The present invention can also be applied to a fluidized bed type dry classifier with a function of stirring pins or blades, or a fluidized bed type dry classifier with a built-in stirring impeller.
【００２０】[0020]
（実施例１）本実施例においては、図３に示す流動層式
乾燥分級機を採用した。図２の第２の実施態様に加え、
主分級室ガス流量調整ダンパー９を付加したことを特徴
とする。この装置において石炭付着水分を９％から５％
まで低下させ、また０．３ｍｍを目標分級粒子径とし、
これ以下の粒子径の粒子を排出ダクトを経て分級するこ
ととした。設備能力は石炭処理量１００ｔ／ｈ（湿炭基
準）としたが、操業変動幅として６０ｔ／ｈ（湿炭基
準）から１２０ｔ／ｈ（湿炭基準）まで許容させたいと
考えた。流動層の石炭流動化部床面積は１５ｍ2 とした
が、分級ゾーンとなるフリーボード部３の水平断面積
（主分級室４と副分級室５の合計）は３０ｍ2 とし、流
動層の石炭投入部から排出部に向かう長手方向のほぼ中
間部に、仕切り板６として鉄板を流れを遮るように設置
した。仕切り板６は天井部から懸下する方法でほぼ前段
と後段を仕切るように設置し、図２の左右方向に移動可
能で、移動によって主分級室４と副分級室５の断面積を
変更することが可能とした。(Example 1) In this example, a fluidized bed type dry classifier shown in FIG. 3 was employed. In addition to the second embodiment of FIG.
The main classifying chamber is characterized by adding a gas flow rate adjusting damper 9. 9% to 5% of coal adhesion moisture in this device
And 0.3 mm as the target classification particle diameter,
Particles having a particle diameter smaller than this were classified through a discharge duct. The facility capacity was set to 100 t / h of coal throughput (based on wet coal), but it was desired to allow the operation fluctuation range from 60 t / h (based on wet coal) to 120 t / h (based on wet coal). The floor area of the fluidized-bed coal fluidization section was 15 m 2 , but the horizontal cross-sectional area (total of the main classification chamber 4 and the sub-classification chamber 5) of the freeboard section 3 serving as a classification zone was 30 m 2 , An iron plate was installed as a partition plate 6 at a substantially intermediate portion in the longitudinal direction from the input portion to the discharge portion so as to block the flow. The partition plate 6 is installed so as to divide the front stage and the rear stage substantially by a method of suspending from the ceiling, and can be moved in the left-right direction in FIG. 2, and changes the cross-sectional area of the main classification room 4 and the sub-classification room 5 by moving. Made it possible.
【００２１】仕切ったフリーボード部３の上部にはそれ
ぞれ排気ダクト７、８を設け、その途中にそれぞれガス
流量調整ダンパー９、１０を内蔵した。このガス流量調
整ダンパー開度は、１００ｔ／ｈの石炭処理量において
水分乾燥量３％相当運転時に副分級室側ダンパー１０は
全閉、主分級室側ダンパー９は５０％開と初期設定を行
った。Exhaust ducts 7 and 8 are provided at the upper part of the partitioned free board section 3, respectively, and gas flow rate adjusting dampers 9 and 10 are respectively built in the middle thereof. The opening degree of the gas flow rate adjustment damper is initially set such that the sub-classification room side damper 10 is fully closed and the main classification room side damper 9 is 50% open at the time of operation corresponding to a moisture drying amount of 3% at a coal processing amount of 100 t / h. Was.
【００２２】６０ｔ／ｈのように低負荷で運転するとき
は、加熱ガス量は約６割に減少し、従ってフリーボード
部ガス流速は６割の速度となった。これでは分級粒子径
が小さくなってしまい発塵要因となる微粉炭を分級しき
れないことになった。そこで、仕切り板６を主分級室断
面積が小さくなるように移動、調整し、主分級室のフリ
ーボード部ガス流速を１００ｔ／ｈの場合と同程度にな
るまで上昇させた。この操作により、設備能力の半分の
６０ｔ／ｈという低負荷においても乾燥と分級の両機能
を同時に満足させることができた。When the operation was performed at a low load such as 60 t / h, the amount of the heated gas was reduced to about 60%, and the gas flow rate in the freeboard section was 60%. In this case, the classification particle diameter becomes small, so that the pulverized coal which causes dust generation cannot be classified. Therefore, the partition plate 6 was moved and adjusted so that the cross-sectional area of the main classification chamber was reduced, and the gas flow rate of the freeboard portion of the main classification chamber was increased until it became almost the same as that of 100 t / h. By this operation, both the drying and classification functions could be satisfied at the same time even at a low load of 60 t / h, which is half of the equipment capacity.
【００２３】１２０ｔ／ｈの高負荷で運転を行う場合、
乾燥に必要な熱量を供給する加熱ガス量は、基準の１０
０ｔ／ｈの場合に比較して２割増しとなる。この排気ガ
スがフリーボード部３を上昇することにより、主分級室
フリーボード部ガス流速は２０％速くなり、分級粒子径
は目標とした０．３ｍｍより大きな粒子となってしまっ
た。この段階では副分級室側のガス流量調整ダンパー１
０は全閉状態で運転していたが、主分級室側のガス流速
を低下させることを目的に副分級室側ガス流量調整ダン
パー開度を１５％開け、２０％相当分のガスを副分級室
側から排気することとした。副分級室のフリーボード部
３の断面積は、主分級室側とほぼ同程度に前提していた
ため、副分級室内のフリーボード部３のガス流速は主分
級室側のガス流速の５分の１程度であり、副分級室内で
ガスに同伴される粒子径は０．１ｍｍ以下の微細炭であ
り、全体の分級粒子径には影響を与えることなく乾燥も
分級も目標を満たす運転をすることができた。When operating at a high load of 120 t / h,
The amount of heating gas that supplies the amount of heat required for drying is 10
20% increase compared to the case of 0 t / h. When this exhaust gas rises in the freeboard section 3, the gas flow velocity in the freeboard section in the main classification chamber is increased by 20%, and the classified particle diameter becomes larger than the targeted 0.3 mm. At this stage, the gas flow rate adjustment damper 1
0 was operated in the fully closed state, but the gas flow rate adjustment damper opening on the sub-classification chamber side was opened by 15% to reduce the gas flow velocity on the main classification chamber side, and the gas equivalent to 20% was sub-classified. It was decided to exhaust air from the room side. Since the cross-sectional area of the free board section 3 of the sub-classification chamber was assumed to be substantially the same as that of the main classification chamber side, the gas flow rate of the free board section 3 in the sub-classification chamber was 5 minutes of the gas flow rate of the main classification chamber side. It is about 1 and the particle size entrained in the gas in the sub-classification chamber is fine coal of 0.1 mm or less, and the operation that satisfies the target for both drying and classification without affecting the overall classification particle size. Was completed.
【００２４】コークス炉に装入する石炭配合を上記の配
合から変更し、原料の粒度分布が微粉炭を多く配合する
ものに変更した。そのため、目標分級粒子径を０．２ｍ
ｍに下げて設定し、１００ｔ／ｈで運転した。水分条
件、処理石炭量は前記と同じなので、流動層に投入する
トータルの加熱ガス量は同じであったが、分級粒子径を
下げるためには主分級室４のフリーボード部３のガス流
速を下げなければならない。その具体的方法として、主
分級室ガス流量調整ダンパー９は初期設定のままとし、
副分級室側のダンパー１０を全閉から１０％開度に開け
た。これにより主分級室側フリーボード部３でのガス流
速が低下し、目標の０．２ｍｍ粒子を境に分級すること
が可能になった。この時の分級率は、微粉炭側約１５％
となり、処理後水分量は目標の５％に調整できた。The blending of the coal charged into the coke oven was changed from the above blending, and the particle size distribution of the raw material was changed to a blending more pulverized coal. Therefore, target classification particle diameter is 0.2m
m and set at 100 t / h. Since the water conditions and the amount of treated coal were the same as above, the total amount of the heated gas charged into the fluidized bed was the same. However, in order to reduce the particle size of the classification, the gas flow rate of the free board section 3 of the main classification chamber 4 was reduced. I have to lower it. As a specific method, the main classifying chamber gas flow rate adjustment damper 9 is left at the initial setting,
The damper 10 on the sub-classifying chamber side was opened from the fully closed position to a 10% opening degree. As a result, the gas flow velocity in the freeboard section 3 on the main classification chamber side was reduced, and it was possible to classify at the target 0.2 mm particles. The classification rate at this time is about 15% on the pulverized coal side.
And the water content after the treatment was adjusted to 5% of the target.
【００２５】（実施例２）実施例１の装置を用いて原炭
の粒度分布を粗くして運転したところ、粗粒炭部分が多
く含まれているため、流動化部での吹き抜け現象が時折
発生し、ガスに同伴されて粗粒炭が微粉炭側に飛散して
いく傾向が発生した。目標分級粒子径は０．３ｍｍで設
定し、１００ｔ／ｈで運転した。そこで、仕切り板６の
長さを実施例１の３ｍに対して４ｍに変更した設備を設
置し、運転を行ったところ、微粉炭中の粗粒炭の混炭比
率が１０％から６％に低下し、分級精度を向上すること
ができた。(Example 2) When the apparatus of Example 1 was operated with the raw coal having a coarse particle size distribution, a large amount of coarse coal was contained. Then, the coarse coal was scattered toward the pulverized coal with the gas. The target classification particle diameter was set at 0.3 mm, and the operation was performed at 100 t / h. Then, when the equipment which changed the length of the partition plate 6 to 4 m compared with 3 m of Example 1 was installed and operated, the mixture ratio of the coarse coal in the pulverized coal was reduced from 10% to 6%. And the classification accuracy could be improved.
【００２６】（実施例３）本実施例においては、図２に
示す流動層式乾燥分級機を採用した。主分級室ガス流量
調整ダンパーを付加していない点を除いては、実施例１
と同様の装置である。実施例１と同様の運転条件でコー
クスの乾燥と分級を行った。１００ｔ／ｈの石炭処理量
において、副分級室ガス流量調整ダンパー１０を全閉と
し、粒径０．３ｍｍ以下の微粉炭を分級すべく仕切り板
６の位置を調整し初期設定を行った。Embodiment 3 In this embodiment, a fluidized bed type dry classifier shown in FIG. 2 was employed. Example 1 except that a gas flow rate adjustment damper for the main classifying chamber was not added.
This is the same device as. The coke was dried and classified under the same operating conditions as in Example 1. At a coal throughput of 100 t / h, the sub-classification chamber gas flow rate adjustment damper 10 was fully closed, the position of the partition plate 6 was adjusted to classify pulverized coal having a particle size of 0.3 mm or less, and initial settings were made.
【００２７】６０ｔ／ｈの低負荷で運転するときは、加
熱ガス量の減少に応じて仕切り板６を主分級室断面積が
小さくなるように移動、調整し、主分級室のフリーボー
ド部ガス流速を１００ｔ／ｈの場合と同程度になるまで
上昇させ、目標とする粒径の微粉炭を分級することがで
きた。また、１２０ｔ／ｈの高負荷で運転を行う場合、
仕切り板６の位置は１００ｔ／ｈ時と同等とし、副分級
室ガス流量調整ダンパー１０の開度を１８％まで開け、
副分級室側からも排気することによって主分級室のガス
流速を調整し、目標とする粒径の微粉炭を分級すること
ができた。When operating at a low load of 60 t / h, the partition plate 6 is moved and adjusted so as to reduce the cross-sectional area of the main classifying chamber in accordance with the decrease in the amount of heating gas. The flow rate was increased to about the same level as in the case of 100 t / h, and pulverized coal having a target particle size could be classified. Also, when operating at a high load of 120 t / h,
The position of the partition plate 6 is equivalent to 100 t / h, the opening of the sub-classification chamber gas flow rate adjustment damper 10 is opened up to 18%,
By exhausting air also from the sub-classification chamber side, the gas flow velocity in the main classification chamber was adjusted, and the pulverized coal having the target particle size could be classified.
【００２８】[0028]
【発明の効果】本発明により、流動層式分級装置を用い
て微粉炭と粗粒炭とに分級し、必要に応じて石炭を乾燥
する工程を有するコークス炉に装入する石炭の事前処理
工程において、石炭処理量や乾燥条件が変動しても分級
する粒子径を一定に保つことが可能になり、また石炭処
理量や乾燥条件を一定に保ったままで分級する粒子径を
変更することが可能になった。Industrial Applicability According to the present invention, a pre-treatment step of coal to be charged into a coke oven having a step of classifying into pulverized coal and coarse coal using a fluidized bed classifier and drying the coal as required. It is possible to keep the particle diameter to be classified constant even if the coal processing amount and drying conditions fluctuate, and it is possible to change the particle diameter to classify while keeping the coal processing amount and drying conditions constant Became.
【図１】本発明の第１の実施態様の流動層式分級乾燥機
の縦断面図である。FIG. 1 is a longitudinal sectional view of a fluidized bed type classification dryer according to a first embodiment of the present invention.
【図２】本発明の第２の実施態様の流動層式分級乾燥機
の縦断面図である。FIG. 2 is a longitudinal sectional view of a fluidized bed type classification dryer according to a second embodiment of the present invention.
【図３】本発明の図２の実施態様に更に主分級室ガス流
量調整ダンパーを加えた流動層式分級乾燥機の縦断面図
である。FIG. 3 is a longitudinal sectional view of a fluidized-bed type classification dryer in which a gas flow control damper for adjusting a main classification chamber is added to the embodiment of FIG. 2 of the present invention.
１ 流動層式分級装置 ２ 流動化部 ３ フリーボード部 ４ 主分級室 ５ 副分級室 ６ 仕切り板 ７ 主分級室排気ダクト ８ 副分級室排気ダクト ９ 主分級室ガス流量調整ダンパー １０ 副分級室ガス流量調整ダンパー １１ 石炭投入口 １２ 粗粒炭排出口 １３ 供給ガス １４ 石炭 １５ 風箱 １６ 粗粒炭排出バルブ １７ 分散板 １８ 仕切り板固定梁 DESCRIPTION OF SYMBOLS 1 Fluidized bed classifier 2 Fluidization part 3 Free board part 4 Main classification room 5 Sub-classification room 6 Partition plate 7 Main classification room exhaust duct 8 Sub-classification room exhaust duct 9 Main classification room gas flow control damper 10 Sub-classification room gas Flow adjustment damper 11 Coal inlet 12 Coarse coal outlet 13 Supply gas 14 Coal 15 Wind box 16 Coarse coal discharge valve 17 Dispersion plate 18 Partition plate fixing beam
───────────────────────────────────────────────────── フロントページの続き (72)発明者 山口 晃 大分市大字西ノ州１番地 新日本製鐵株式 会社大分製鐵所内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Akira Yamaguchi, inventor, Oita 1
Claims (10)
とに分級する工程を有するコークス炉に装入する石炭の
事前処理工程において、フリーボード部にフリーボード
部空間を１室の主分級室と１室又は２室以上の副分級室
に分割する仕切り板を挿入し、かつそれぞれの室の上部
に排気ダクトを設け、副分級室の上部にガス流量調整装
置を設け、該副分級室の排出ガス量の調整によって主分
級室の上昇ガス流速を調整することにより、分級する微
粉炭の最大粒径を調整することを特徴とする流動層式分
級装置における石炭分級粒径調整方法。In a pretreatment process of coal charged into a coke oven having a process of classifying pulverized coal and coarse coal using a fluidized bed classifier, a freeboard part space is formed in a freeboard part. A partition plate for dividing into the main classification chamber and one or more sub-classification chambers is inserted, and an exhaust duct is provided in the upper part of each chamber, and a gas flow controller is provided in the upper part of the sub-classification chamber. Adjusting the maximum gas diameter of the pulverized coal to be classified by adjusting the ascending gas flow rate of the main classification chamber by adjusting the amount of exhaust gas of the classification chamber, the method for adjusting the particle diameter of coal classification in a fluidized bed type classification apparatus, characterized by .
とに分級する工程を有するコークス炉に装入する石炭の
事前処理工程において、フリーボード部にフリーボード
部空間を１室の主分級室と１室又は２室以上の副分級室
に分割する仕切り板を挿入し、該仕切り板は移動可能で
あって主分級室と副分級室の断面積を変更することが可
能であり、かつそれぞれの室の上部に排気ダクトを設
け、副分級室の上部にガス流量調整装置を設け、主分級
室と副分級室の断面積の調整及び副分級室ガス流量調整
装置の調整によって主分級室の上昇ガス流速を調整する
ことにより、分級する微粉炭の最大粒径を調整すること
を特徴とする流動層式分級装置における石炭分級粒径調
整方法。2. In a pretreatment process of coal charged into a coke oven having a process of classifying into pulverized coal and coarse coal using a fluidized bed classifier, a freeboard space is provided in a freeboard portion by one room. A partition plate for dividing into a main classification room and one or two or more sub-classification rooms is inserted, and the partition plate is movable, and the cross-sectional area of the main classification room and the sub-classification room can be changed. In addition, an exhaust duct is provided in the upper part of each chamber, a gas flow controller is provided in the upper part of the sub-classifying chamber, and the cross-sectional areas of the main and sub-classifying chambers are adjusted and the gas flow controller in the sub-classifying chamber is adjusted. A method for adjusting the particle size of coal in a fluidized bed type classification apparatus, wherein the maximum particle size of the pulverized coal to be classified is adjusted by adjusting the ascending gas flow rate in the classification chamber.
とに分級する工程を有するコークス炉に装入する石炭の
事前処理工程において、フリーボード部にフリーボード
部空間を１室の主分級室と１室又は２室以上の副分級室
に分割する仕切り板を挿入し、該仕切り板は移動可能で
あって主分級室と副分級室の断面積を変更することが可
能であり、かつそれぞれの室の上部に排気ダクトを設
け、副分級室の上部にガス流量調整オリフィスを設け、
主分級室と副分級室の断面積の調整によって主分級室の
上昇ガス流速を調整することにより、分級する微粉炭の
最大粒径を調整することを特徴とする流動層式分級装置
における石炭分級粒径調整方法。3. In a pre-treatment step of coal charged into a coke oven having a step of classifying pulverized coal and coarse coal using a fluidized bed classifier, a free board space is provided in a free board section. A partition plate for dividing into a main classification room and one or two or more sub-classification rooms is inserted, and the partition plate is movable, and the cross-sectional area of the main classification room and the sub-classification room can be changed. And an exhaust duct is provided at the top of each chamber, and a gas flow rate adjusting orifice is provided at the top of the sub-classification chamber.
Coal classification in a fluidized bed classifier characterized by adjusting the maximum particle size of pulverized coal to be classified by adjusting the ascending gas flow velocity in the main classification chamber by adjusting the cross-sectional area of the main classification chamber and the sub-classification chamber Particle size adjustment method.
とに分級するコークス炉に装入する石炭の事前処理装置
において、フリーボード部にフリーボード部空間を１室
の主分級室と１室又は２室以上の副分級室に分割する仕
切り板を挿入し、かつそれぞれの室の上部に排気ダクト
を設け、副分級室の上部にガス流量調整装置を設けたこ
とを特徴とする流動層式分級装置。4. A pre-treatment apparatus for coal charged into a coke oven for classifying into pulverized coal and coarse coal using a fluidized bed classifier, wherein a free board part has a free board space in a free board part. And a partition plate for dividing into one or more sub-classification chambers is inserted, and an exhaust duct is provided above each chamber, and a gas flow control device is provided above the sub-classification chamber. Fluidized bed classifier.
大供給量と最小供給量および主分級室のフリーボード部
における最高流速と最低流速を予め定め、主分級室のフ
リーボード部の断面積は供給ガスの前記最小供給量のガ
スが主分級室を通過したときに前記最高流速以上の流速
が得られる断面積であり、主分級室と副分級室のフリー
ボード部の全体断面積は供給ガスの前記最大供給量のガ
スが該全体断面積の空間を通過したときにガス流速とし
て前記最低流速以下の流速が得られる断面積であること
を特徴とする請求項４記載の流動層式分級装置。5. A maximum supply amount and a minimum supply amount in a supply gas amount range of a fluidized bed type classification device and a maximum flow rate and a minimum flow rate in a free board portion of a main classification room are determined in advance, and disconnection of a free board portion of the main classification room is performed. The area is a cross-sectional area at which a flow rate equal to or higher than the maximum flow rate is obtained when the gas with the minimum supply amount of the supply gas passes through the main classification chamber, and the total cross-sectional area of the free board portion of the main classification chamber and the sub-classification chamber is 5. The fluidized bed system according to claim 4, wherein the gas has a cross-sectional area at which a gas flow rate equal to or lower than the minimum flow rate is obtained when the gas having the maximum supply amount passes through the space having the total cross-sectional area. Classifier.
とに分級するコークス炉に装入する石炭の事前処理装置
において、フリーボード部にフリーボード部空間を１室
の主分級室と１室又は２室以上の副分級室に分割する仕
切り板を挿入し、該仕切り板は移動可能であって主分級
室と副分級室の断面積を変更することが可能であり、か
つそれぞれの室の上部に排気ダクトを設け、副分級室の
上部にガス流量調整装置を設けたことを特徴とする流動
層式分級装置。6. A pre-treatment device for coal charged into a coke oven for classifying into pulverized coal and coarse coal using a fluidized bed type classification device, wherein a free board portion space is provided in a free board portion as one main classification room. And a partition plate for dividing into one or two or more sub-classification chambers is inserted, the partition plate is movable, and the sectional area of the main classification chamber and the sub-classification chamber can be changed, and A fluidized bed type classification device, wherein an exhaust duct is provided in the upper part of the chamber and a gas flow rate adjusting device is provided in the upper part of the sub-classification chamber.
特徴とする請求項６記載の流動層式分級装置。7. The fluidized bed classification device according to claim 6, wherein the length of the partition plate can be changed.
調整ダンパーであることを特徴とする請求項４乃至７記
載の流動層式分級装置。8. The fluidized bed type classification device according to claim 4, wherein the gas flow control device of the sub-classification chamber is a gas flow control damper.
調整用オリフィスであることを特徴とする請求項６又は
７記載の流動層式分級装置。9. The fluidized bed type classification device according to claim 6, wherein the gas flow control device in the sub-classification chamber is an orifice for gas flow control.
量調整装置を設置せず、ガスはもっぱら主分級室のみを
通過することを特徴とする請求項６又は７記載の流動層
式分級装置。10. A fluidized bed type classification apparatus according to claim 6, wherein an exhaust duct and a gas flow control device are not provided above the sub-classification chamber, and the gas passes only through the main classification chamber. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18980897A JP3447520B2 (en) | 1997-07-15 | 1997-07-15 | Method and apparatus for adjusting coal particle size in fluidized bed classifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18980897A JP3447520B2 (en) | 1997-07-15 | 1997-07-15 | Method and apparatus for adjusting coal particle size in fluidized bed classifier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1133494A true JPH1133494A (en) | 1999-02-09 |
| JP3447520B2 JP3447520B2 (en) | 2003-09-16 |
Family
ID=16247561
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|---|---|---|---|
| JP18980897A Expired - Fee Related JP3447520B2 (en) | 1997-07-15 | 1997-07-15 | Method and apparatus for adjusting coal particle size in fluidized bed classifier |
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| WO2010055618A1 (en) * | 2008-11-17 | 2010-05-20 | 株式会社Ihi | Fluidized bed device |
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| WO2010055618A1 (en) * | 2008-11-17 | 2010-05-20 | 株式会社Ihi | Fluidized bed device |
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| CN102215947A (en) * | 2008-11-17 | 2011-10-12 | 株式会社Ihi | Fluidized bed device |
| AU2009315206B2 (en) * | 2008-11-17 | 2013-07-04 | Ihi Corporation | Fluidized bed device |
| JP2012026629A (en) * | 2010-07-22 | 2012-02-09 | Tsukishima Kikai Co Ltd | Horizontal type tumble drier |
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| JP3447520B2 (en) | 2003-09-16 |
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