JPH08266830A - Method of reducing unburned coal in coal ash - Google Patents
Method of reducing unburned coal in coal ashInfo
- Publication number
- JPH08266830A JPH08266830A JP9786095A JP9786095A JPH08266830A JP H08266830 A JPH08266830 A JP H08266830A JP 9786095 A JP9786095 A JP 9786095A JP 9786095 A JP9786095 A JP 9786095A JP H08266830 A JPH08266830 A JP H08266830A
- Authority
- JP
- Japan
- Prior art keywords
- unburned
- coal ash
- content
- ash
- louver
- 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.)
- Granted
Links
- 239000003245 coal Substances 0.000 title claims abstract description 14
- 239000010883 coal ash Substances 0.000 title claims description 30
- 238000000034 method Methods 0.000 title claims description 11
- 239000002245 particle Substances 0.000 claims abstract description 20
- 238000000926 separation method Methods 0.000 claims abstract description 20
- 238000002407 reforming Methods 0.000 claims abstract description 4
- 239000000843 powder Substances 0.000 claims description 50
- 238000002485 combustion reaction Methods 0.000 claims description 5
- 239000002956 ash Substances 0.000 claims description 4
- 239000010419 fine particle Substances 0.000 abstract description 6
- 238000010304 firing Methods 0.000 abstract 1
- 239000010881 fly ash Substances 0.000 description 4
- 239000004568 cement Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 238000009841 combustion method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000011946 reduction process Methods 0.000 description 2
- 238000004088 simulation Methods 0.000 description 2
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Combined Means For Separation Of Solids (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、粒径が概略数μm〜百
数十μmの範囲に分布している未燃炭素(以下、未燃分
という。)残留石炭灰(原粉)を分級することにより捕
集した微粉中の未燃分含有率を総じて低減するようにし
た石炭灰の未燃分低減方法及び装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention classifies unburned carbon (hereinafter referred to as unburned content) residual coal ash (raw powder) having a particle size distributed in the range of approximately several μm to hundreds of tens of μm. The present invention relates to a method and an apparatus for reducing unburned content of coal ash, which is capable of generally reducing the unburned content content in the fine powder collected.
【0002】[0002]
【従来の技術】従来より、粉体の分級を含む集塵装置と
しては、適用される分離粒径に応じて100μm以上の
分級では篩装置、10μm以下の分級ではサイクロン装
置(遠心集塵装置)及び前記適用粒径を補うものとして
ルーバー分級装置(慣性集塵装置)等が知られている。2. Description of the Related Art Conventionally, as a dust collector including classification of powder, a sieve device is used for classification of 100 μm or more according to the applied separation particle size, and a cyclone device (centrifugal dust collection device) for classification of 10 μm or less. A louver classifier (inertial dust collector) or the like is known as a means for supplementing the applicable particle size.
【0003】本発明で取り扱おうとしている微粉炭燃焼
ボイラから排出されるフライアッシュは、その粒径が概
略数μm〜百数十μmの範囲に分布しており、使用原料
によって多寡があるが3〜6%程度の未燃分が残留して
いる。このためJIS規格灰としてセメント混和材,コ
ンクリート混合材等に使用されるのはその一部にすぎな
い。The fly ash discharged from the pulverized coal combustion boiler to be handled in the present invention has a particle size distributed in the range of several μm to hundreds of tens of μm, and it depends on the raw material used. About 3 to 6% of unburned matter remains. For this reason, only a part of it is used as a JIS standard ash in cement admixtures, concrete admixtures, and the like.
【0004】つまり、未燃分が多いままコンクリート混
合材に使用すると、品質を低下させるメチレンブルー吸
着量が増加し、未燃分が空気連行剤(AE剤)を吸着す
るため、空気量の管理が困難となりヒビ割れが生じやす
い等の問題が利用拡大を阻害している。That is, when the unmixed component is used in the concrete mixture with a large amount, the adsorbed amount of methylene blue which deteriorates the quality increases, and the unburned component adsorbs the air entraining agent (AE agent). Problems such as difficulty and easy cracking prevent the expansion of use.
【0005】現状では石炭灰(特にフライアッシュ)は
以下〜に示す態様で処理されている。 埋立て用とする。 セパレーターで分級して高未燃分石炭灰粒子を除去し
全体の未燃分含有率を低下させて良質なセメント混和材
等に改質する。 燃焼性の良好な石炭を使用して残留未燃分の発生を阻
止するとともに石炭灰の未燃分含有率を低下させて良質
なセメント混和材等に改質する。At present, coal ash (particularly fly ash) is treated in the following modes. For landfill. Classifying with a separator to remove high unburned coal ash particles and reduce the overall unburned content to improve the quality of cement admixture. Coal with good flammability is used to prevent the generation of residual unburned matter and to reduce the unburned matter content of coal ash to reform it into a high-quality cement admixture.
【0006】[0006]
【発明が解決しようとする課題】しかしながら、上述し
た従来処理については以下(イ)〜(ハ)に示すような
問題点があった。 (イ)埋立て用としての処理量には限度があり、不使用
の石炭灰が無用な廃棄物となってしまう。 (ロ)セパレーターで分級して高未燃分石炭灰粒子を除
去するには、高価なセパレーターや分級する手間(工
数)を要する。 (ハ)燃焼性の良好な石炭を使用すると、ボイラの運転
コストが上昇する。However, the conventional processing described above has the following problems (a) to (c). (B) There is a limit to the amount of landfill that can be processed, and unused coal ash becomes useless waste. (B) In order to remove high unburned coal ash particles by classifying with a separator, an expensive separator and time (man-hour) for classifying are required. (C) The use of coal with good combustibility increases the operating cost of the boiler.
【0007】こうしたなかで、本発明に関しては石炭灰
の性質及び設備コストの点から先述したルーバー分級装
置〔上記(ロ)の改善〕の適用が有効であると考慮され
るが、石炭灰の物理的・機械的処理において、分級点を
変更して原粉中の未燃分粒子を含む粗大粒子を微小粒子
と分離し、微小粒子(微粉)を精度よく捕集することで
未燃分を低減することができるという知見又は着目はな
かった。Under the circumstances, it is considered that the application of the above-mentioned louver classifier (improvement of the above (b)) is effective for the present invention in view of the properties of coal ash and the equipment cost, but the physical properties of coal ash In mechanical and mechanical processing, the classification point is changed to separate coarse particles containing unburned particles in raw powder from fine particles, and fine particles (fine powder) are collected with high accuracy to reduce unburned content. There was no knowledge or attention that they could.
【0008】本発明者らは、石炭を燃料とする発電所か
ら排出される多量の石炭灰を有効利用するために高品質
化(改質)に関し鋭意研究を重ねた結果上記知見を有
し、石炭灰(原粉)を分級することにより捕集した微粉
中の未燃分含有率を総じて低減する手法を開発するに至
った。The inventors of the present invention have the above findings as a result of earnest studies on quality improvement (reforming) in order to effectively use a large amount of coal ash discharged from a coal-fired power plant. We have developed a method to reduce the content of unburned matter in fine powder collected by classifying coal ash (raw powder).
【0009】本発明はこのような事情に鑑みなされたも
のであって、上記課題を解消し、未燃分残留石炭灰(原
粉)を分級することにより捕集した微粉中の未燃分含有
率を総じて低減するようにした石炭灰の未燃分低減方法
及び装置を提供することを目的とするものである。The present invention has been made in view of the above circumstances, and solves the above problems and contains unburned matter in fine powder collected by classifying unburned matter residual coal ash (raw powder). An object of the present invention is to provide a method and an apparatus for reducing unburned content of coal ash, which is capable of reducing the overall rate.
【0010】[0010]
【課題を解決するための手段】上記目的を達成するため
に本発明は、粒径が概略数μm〜百数十μmの範囲に分
布している未燃分残留石炭灰(原粉)を分級することに
より捕集した微粉中の未燃分含有率を総じて低減するよ
うにした石炭灰の未燃分低減方法であって、貯留した原
粉を分散器を介して分散粉体とし、これを含む空気流と
ともにルーバー分級装置に導入し、ルーバー翼を角度調
整して分級点を変更し、吸引側に分離される微粉をフィ
ルターに捕集することを特徴とするものである。In order to achieve the above object, the present invention classifies unburned residual coal ash (raw powder) having a particle size distribution in the range of several μm to hundreds of tens μm. It is a method of reducing unburned content of coal ash that reduces the unburned content content in the fine powder collected as a whole by using the stored raw powder as a dispersed powder through a disperser, and It is characterized in that it is introduced into a louver classifier together with the air flow containing it, the angle of the louver blade is adjusted to change the classification point, and the fine powder separated on the suction side is collected by a filter.
【0011】ここで、上記ルーバー翼の角度調整が50
度〜80度の範囲を有効とするものである。Here, the angle adjustment of the louver blade is 50
The range of degrees to 80 degrees is effective.
【0012】また、粒径が概略数μm〜百数十μmの範
囲に分布している未燃分残留石炭灰(原粉)を分級する
ことにより捕集した微粉中の未燃分含有率を総じて低減
するようにした石炭灰の未燃分低減装置であって、原粉
を貯留し供給するためのテーブルフィーダーと、押し込
みファンと配管連絡し原粉を分散粉体としてこれを含む
空気流とともに装置投入するための分散器と、ルーバー
分級装置と、ルーバー翼を介した吸引側に配管連絡し分
級された微粉を捕集するためのフィルターと、吸引装置
とを具備したことを特徴とするものである。[0012] Further, the content of unburned matter in the fine powder collected by classifying the unburned matter residual coal ash (raw powder) whose particle size is distributed in the range of several μm to hundreds of tens of μm It is a device for reducing unburned content of coal ash that is generally reduced.It is connected to a table feeder for storing and supplying raw powder, a pushing fan and piping, and the raw powder is dispersed powder together with an air flow containing it. A disperser for introducing the device, a louver classification device, a filter for collecting finely classified powder by connecting piping to the suction side via a louver blade, and a suction device Is.
【0013】[0013]
【作用】原粉の供給流量(又は微粉回収側の吸引流量)
とルーバー翼角度とを調整して分級点を変更することに
より、捕集した微粉中の未燃分を総じて低減し、その低
減率を変更・調整することができる。[Function] Raw powder supply flow rate (or suction flow rate on the fine powder recovery side)
By adjusting the louver blade angle and the louver blade angle to change the classification point, the unburned amount in the collected fine powder can be generally reduced, and the reduction rate can be changed / adjusted.
【0014】[0014]
【実施例】本発明の一実施例を添付図面を参照して以下
説明する。図1はフライアッシュ分級による未燃分低減
プロセスを説明する装置系統図である。なお、本発明構
成は実験的に確認された事実に基づき採用されたもので
ある。(規模の拡縮によって影響されるものではな
い。)DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is an apparatus system diagram for explaining an unburned-content reduction process by fly ash classification. The configuration of the present invention is adopted based on the fact confirmed experimentally. (Not affected by scaling.)
【0015】ここで、1がテーブルフィーダー、2が分
散器、3がルーバー分級装置、4がフィルター、5が吸
引装置、31がルーバー翼及びXが未燃分低減装置(本発
明装置)である。Here, 1 is a table feeder, 2 is a disperser, 3 is a louver classifying device, 4 is a filter, 5 is a suction device, 31 is a louver blade, and X is an unburned-content reducing device (device of the present invention). .
【0016】図示するように、本発明装置(X)は、原
粉を貯留し供給するためのテーブルフィーダー(1)
と、押し込みファン(図示省略)と配管連絡し原粉を分
散粉体としてこれを含む空気流とともに装置投入するた
めの分散器(2)と、ルーバー分級装置(3)と、ルー
バー翼(31)を介した吸引側に配管連絡し分級された微
粉を捕集するためのフィルター(4)と、吸引装置
(5)とを具備しており、貯留した原粉を分散器(2)
を介して分散粉体とし、これを含む空気流とともにルー
バー分級装置(3)に導入し、ルーバー翼(31)を角度
調整して分級点を変更し、吸引側に分離される微粉をフ
ィルター(4)に捕集し回収するようにしている。As shown in the figure, the device (X) of the present invention is a table feeder (1) for storing and supplying raw powder.
, A disperser (2) for communicating with a pushing fan (not shown) through a pipe and introducing the raw powder as a dispersed powder together with an air flow containing the powder, a louver classifier (3), and a louver blade (31). It is equipped with a filter (4) for connecting the classified fine powder by connecting it to the suction side through a suction device (5) and collecting the raw powder stored in the disperser (2).
The powder is introduced into the louver classifier (3) together with the air flow containing it, the angle of the louver blade (31) is adjusted to change the classification point, and the fine powder separated on the suction side is filtered ( They are collected in 4) and collected.
【0017】ここで、上記ルーバー翼(31)の角度調整
が50度〜80度の範囲を有効とするものである。Here, the angle adjustment of the louver blade (31) is effective within the range of 50 to 80 degrees.
【0018】図2は各ルーバー翼角度における部分分離
効率を示す部分分離効率 vs.粒子径のデータプロット
(部分分離効率曲線)である。FIG. 2 is a data plot (partial separation efficiency curve) of partial separation efficiency vs. particle diameter showing the partial separation efficiency at each louver blade angle.
【0019】図からみてとれるように、ルーバー翼角度
の大きい方が部分分離効率曲線が小径側にシフトしてお
り、かつ、立ち上がりがシャープである。このことは、
分級点(50%分離径)が小径側に移行し、分級性能が
向上することを示すものであり、ルーバー翼角度が大き
くなるにしたがって吸引角度がより重力に逆らった方向
になるため、未燃分粒子を含む粗大粒子がフィルター側
に移動し難くなり、微粉と粗粉がはっきりと分離できた
ものと考察される。As can be seen from the figure, the larger the louver blade angle, the more the partial separation efficiency curve shifts to the smaller diameter side and the sharper the rising edge. This is
It shows that the classification point (50% separation diameter) shifts to the smaller diameter side and the classification performance is improved. As the louver blade angle increases, the suction angle becomes a direction more counter to gravity, so unburned It is considered that the coarse particles including the separated particles became difficult to move to the filter side, and the fine powder and the coarse powder could be clearly separated.
【0020】捕集した微粉中の未燃分(未燃炭素分)と
その未燃分低減率を表1に示す。Table 1 shows the unburned content (unburned carbon content) in the collected fine powder and the unburned content reduction rate.
【0021】[0021]
【表1】 [Table 1]
【0022】表からわかるように、未燃分含有率3.5
0%の石炭灰(通常原粉)について、これを大きく下回
る改質された石炭灰(微粉)を回収できている。〔ルー
バー翼角度70度で未燃分含有率2.63%(低減率2
4.9%)〕As can be seen from the table, the unburned content rate is 3.5.
For 0% of coal ash (usually raw powder), it is possible to recover modified coal ash (fine powder), which is much lower than this. [Unburned matter content 2.63% (reduction rate 2
(4.9%)]
【0023】本発明方法及び装置は、粉体流速に対する
装置内通過時間のみを処理時間として考慮すれば十分で
あり、燃焼方式等の従来処理と比べて短時間で容易にか
つ連続的に実行処理可能である。なお、未燃分含有率が
5〜6%程度の原粉であれば、さらに容易に5%以下の
JIS規格灰に改質可能である。In the method and apparatus of the present invention, it is sufficient to consider only the passage time in the apparatus with respect to the powder flow rate as the processing time, and the processing can be easily and continuously executed in a shorter time than the conventional processing such as the combustion method. It is possible. In addition, if the raw powder has an unburned content of about 5 to 6%, it can be more easily reformed to JIS standard ash of 5% or less.
【0024】また、実験規模のモデル装置(図示省略)
について、分級性能に関する数値シミュレーションをお
こないルーバー内の気流の流れ(図示省略)と各粒子軌
跡(図示省略)を解析して部分分離効率(計算値)を求
め、実験値と比較している。An experimental scale model device (not shown)
For the above, a numerical simulation on the classification performance was performed, the flow of the air flow in the louver (not shown) and each particle trajectory (not shown) were analyzed to obtain the partial separation efficiency (calculated value), and the partial separation efficiency (calculated value) was compared with the experimental value.
【0025】図3はこの結果を示す部分分離効率の計算
値と実験値を比較した部分分離効率vs.粒子径のデータ
プロット(部分分離効率曲線)である。FIG. 3 is a data plot (partial separation efficiency curve) of partial separation efficiency vs. particle diameter, which compares the calculated partial separation efficiency and the experimental value showing this result.
【0026】図示のとおり、両者がほぼ一致しているこ
とから、本発明装置の実効性が確認されるとともに、数
値シミュレーションが装置運用上の指標となりうること
が結論される。As shown in the figure, since the two are almost the same, it is concluded that the effectiveness of the device of the present invention is confirmed and that the numerical simulation can be an index for operating the device.
【0027】[0027]
【発明の効果】本発明は以上の構成よりなるものであ
り、これによれば以下に示す有益な効果を奏する。The present invention is constituted as described above, and has the following beneficial effects.
【0028】(1)ルーバー翼の角度調整により、分級
点の変更を可能とし、捕集した微粉中の未燃分含有率を
総じて低減することができる。しかも、その低減率は変
更(制御)可能である。(1) By adjusting the angle of the louver blade, the classification point can be changed, and the content of unburned components in the collected fine powder can be reduced as a whole. Moreover, the reduction rate can be changed (controlled).
【0029】(2)本発明方法及び装置は、粉体流速に
対する装置内通過時間のみを処理時間として考慮すれば
十分であり、燃焼方式等の従来処理と比べて短時間で容
易にかつ連続的に実行処理可能である。(2) In the method and apparatus of the present invention, it is sufficient to consider only the passage time in the apparatus with respect to the powder flow velocity as the processing time, which is easier and more continuous than the conventional processing such as the combustion method in a short time. Can be processed.
【0030】(3)高未燃分石炭灰粒子を分級除去する
ための高価なセパレーターや燃焼性の良好な高価な石炭
の使用及び燃焼方式による燃焼炉等を必要としないの
で、設備コストの低減が図れる。(3) Since no expensive separator for classifying and removing high unburned coal ash particles or expensive coal having good combustibility and a combustion furnace by a combustion system are required, the equipment cost is reduced. Can be achieved.
【図面の簡単な説明】[Brief description of drawings]
【図1】本発明の一実施例である図1はフライアッシュ
分級による未燃分低減プロセスを説明する装置系統図で
ある。1 is an embodiment of the present invention, FIG. 1 is a system diagram for explaining an unburned content reduction process by fly ash classification.
【図2】各ルーバー翼角度における部分分離効率を示す
部分分離効率 vs.粒子径のデータプロット(部分分離効
率曲線)である。FIG. 2 is a data plot (partial separation efficiency curve) of partial separation efficiency vs. particle diameter showing partial separation efficiency at each louver blade angle.
【図3】部分分離効率の計算値と実験値の比較した部分
分離効率 vs.粒子径のデータプロット(部分分離効率曲
線)である。FIG. 3 is a data plot (partial separation efficiency curve) of partial separation efficiency vs. particle diameter in which calculated values of partial separation efficiency and experimental values are compared.
1 テーブルフィーダー 2 分散器 3 ルーバー分級装置 4 フィルター 5 吸引装置 31 ルーバー翼 X 未燃分低減装置(本発明装置) 1 table feeder 2 disperser 3 louver classifier 4 filter 5 suction device 31 louver blade X unburned matter reduction device (device of the present invention)
───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉田 英人 広島県東広島市高屋町小谷981−206 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hideto Yoshida 981-206 Otani, Takayacho, Higashihiroshima City, Hiroshima Prefecture
Claims (3)
される未燃分残留石炭灰の改質処理方法において、粒径
が概略数μm〜百数十μmの範囲に分布している未燃分
残留石炭灰(原粉)を分級することにより捕集した微粉
中の未燃分含有率を総じて低減するようにした石炭灰の
未燃分低減方法であって、貯留した原粉を分散器を介し
て分散粉体とし、これを含む空気流とともにルーバー分
級装置に導入し、ルーバー翼を角度調整して分級点を変
更し、吸引側に分離される微粉をフィルターに捕集する
ことを特徴とする石炭灰の未燃分低減方法。1. In a method for reforming unburned residual coal ash discharged as incinerated ash from a pulverized coal combustion boiler, an unburned component having a particle size distributed in a range of approximately several μm to hundreds of tens of μm. A method for reducing unburned content of coal ash, in which the content of unburned content in fine powder collected by classifying residual coal ash (raw powder) is reduced as a whole. Dispersed powder through the louver, introduced into the louver classification device together with the air flow containing it, the angle of the louver blade is adjusted to change the classification point, and the fine powder separated on the suction side is collected by the filter. A method for reducing unburned coal ash content.
の範囲である請求項1記載の石炭灰の未燃分低減方法。2. The method for reducing unburned coal ash according to claim 1, wherein the angle adjustment of the louver blade is in the range of 50 degrees to 80 degrees.
される未燃分残留石炭灰の改質処理装置において、粒径
が概略数μm〜百数十μmの範囲に分布している未燃分
残留石炭灰(原粉)を分級することにより捕集した微粉
中の未燃分含有率を総じて低減するようにした石炭灰の
未燃分低減装置であって、原粉を貯留し供給するための
テーブルフィーダーと、押し込みファンと配管連絡し原
粉を分散粉体としてこれを含む空気流とともに装置投入
するための分散器と、ルーバー分級装置と、ルーバー翼
を介した吸引側に配管連絡し分離された微粉を捕集する
ためのフィルターと、吸引装置とを具備したことを特徴
とする石炭灰の未燃分低減装置。3. In a reforming treatment apparatus of unburned residual coal ash discharged as incinerated ash from a pulverized coal combustion boiler, unburned components having a particle size distributed in a range of approximately several μm to hundreds of tens of μm. A coal ash unburnt content reduction device that reduces the unburned content of fine powder collected by classifying residual coal ash (raw powder), and stores and supplies the raw powder. The table feeder, the pushing fan, and the disperser for piping the raw powder as a dispersed powder and introducing the equipment together with the air flow containing it, the louver classifier, and the suction side via the louver blade are connected to the pipe for separation. An apparatus for reducing unburned content of coal ash, comprising: a filter for collecting the generated fine powder and a suction device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9786095A JP2787555B2 (en) | 1995-03-29 | 1995-03-29 | Method and apparatus for reducing unburned coal ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9786095A JP2787555B2 (en) | 1995-03-29 | 1995-03-29 | Method and apparatus for reducing unburned coal ash |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH08266830A true JPH08266830A (en) | 1996-10-15 |
| JP2787555B2 JP2787555B2 (en) | 1998-08-20 |
Family
ID=14203513
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9786095A Expired - Lifetime JP2787555B2 (en) | 1995-03-29 | 1995-03-29 | Method and apparatus for reducing unburned coal ash |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2787555B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002001222A (en) * | 2000-06-27 | 2002-01-08 | Takahashi Kikan:Kk | Fibrillation facilities |
| US7077887B2 (en) * | 2002-05-21 | 2006-07-18 | University Of Massachusetts | Low pressure impact separator for separation, classification and collection of ultra-fine particles |
| JP2016060673A (en) * | 2014-09-19 | 2016-04-25 | 株式会社Ihi | How to treat fly ash |
| JP2018015677A (en) * | 2016-07-25 | 2018-02-01 | 株式会社リュウクス | Fly ash classification device, fly ash classification method, and production method of spherical fly ash particles |
| JP2018505773A (en) * | 2014-12-23 | 2018-03-01 | ハルドール・トプサー・アクチエゼルスカベット | Particle separation catalytic chemical reactor and particle separator |
| CN113351480A (en) * | 2021-05-13 | 2021-09-07 | 天津水泥工业设计研究院有限公司 | Two-stage dynamic rotor powder concentrator capable of adjusting grain size grading of finished products |
-
1995
- 1995-03-29 JP JP9786095A patent/JP2787555B2/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002001222A (en) * | 2000-06-27 | 2002-01-08 | Takahashi Kikan:Kk | Fibrillation facilities |
| US7077887B2 (en) * | 2002-05-21 | 2006-07-18 | University Of Massachusetts | Low pressure impact separator for separation, classification and collection of ultra-fine particles |
| US7951217B2 (en) * | 2002-05-21 | 2011-05-31 | University Of Massachusetts | Low pressure impact separator for separation, classification and collection of ultra-fine particles |
| JP2016060673A (en) * | 2014-09-19 | 2016-04-25 | 株式会社Ihi | How to treat fly ash |
| JP2018505773A (en) * | 2014-12-23 | 2018-03-01 | ハルドール・トプサー・アクチエゼルスカベット | Particle separation catalytic chemical reactor and particle separator |
| JP2018015677A (en) * | 2016-07-25 | 2018-02-01 | 株式会社リュウクス | Fly ash classification device, fly ash classification method, and production method of spherical fly ash particles |
| CN113351480A (en) * | 2021-05-13 | 2021-09-07 | 天津水泥工业设计研究院有限公司 | Two-stage dynamic rotor powder concentrator capable of adjusting grain size grading of finished products |
| CN113351480B (en) * | 2021-05-13 | 2022-05-03 | 天津水泥工业设计研究院有限公司 | Two-stage dynamic rotor powder concentrator capable of adjusting grain size grading of finished products |
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| Publication number | Publication date |
|---|---|
| JP2787555B2 (en) | 1998-08-20 |
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