JPS59105810A - Coal flotation machine - Google Patents

Coal flotation machine

Info

Publication number
JPS59105810A
JPS59105810A JP57216682A JP21668282A JPS59105810A JP S59105810 A JPS59105810 A JP S59105810A JP 57216682 A JP57216682 A JP 57216682A JP 21668282 A JP21668282 A JP 21668282A JP S59105810 A JPS59105810 A JP S59105810A
Authority
JP
Japan
Prior art keywords
coal
air bubbles
shearing force
ash content
tray
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP57216682A
Other languages
Japanese (ja)
Inventor
Akira Osawa
大澤 旭
Yukitaka Sawada
沢田 幸隆
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
RYONICHI ENG KK
Mitsubishi Heavy Industries Ltd
Original Assignee
RYONICHI ENG KK
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by RYONICHI ENG KK, Mitsubishi Heavy Industries Ltd filed Critical RYONICHI ENG KK
Priority to JP57216682A priority Critical patent/JPS59105810A/en
Publication of JPS59105810A publication Critical patent/JPS59105810A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To make it possible to reduce the amount of shower water used in a toilet, by mounting a mechanical apparatus for imparting shearing force to air bubbles collected in the toilet and reducing the sizes of air bubbles or crushing the same in the toilet. CONSTITUTION:A rotary cylinder 100 is mounted to a toilet 30 while bars 101 are spirally attached to the surface of said rotary cylinder 100 in a direction sending coal with low ash content and imparts shearing force to air bubbles to be capable of crushing the same or making the same fine. The shape of each bar 101 is formed into a shape for easily imparting shearing force to air bubbles. In addition, the rotary number of the rotary cylinder 100 is adjusted to high speed rotation of 300-1,000rpm and shearing force is effectively imparted to air bubbles.

Description

【発明の詳細な説明】 本発明は石炭高濃度水スラリの脱灰プロセスに使用さイ
する浮選機に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a flotation machine used in the deashing process of highly concentrated coal water slurry.

石炭高濃度水スラリとは、石炭濃度60〜85重量係、
界面活性剤0.O1〜5゜0 重量%(対石炭粉末)、
水分残りのチで構成されるスラリ燃料である。石炭濃度
、界面活性剤添加率は、石炭の種類によって異なってく
る。普通石炭には灰分が含まれているが、石炭高濃度水
スラリをボイラで燃焼させる際、灰分があるとボイラ効
率の低下が発生ずるため、出来るだけ灰分を燃焼前に除
去しておくことが好ましい。
Coal high concentration water slurry means coal concentration 60-85 weight ratio,
Surfactant 0. O1~5゜0 weight% (based on coal powder),
It is a slurry fuel consisting of water with residual water. Coal concentration and surfactant addition rate vary depending on the type of coal. Ordinary coal contains ash, but when combusting a highly concentrated water slurry of coal in a boiler, the presence of ash will reduce boiler efficiency, so it is best to remove as much ash as possible before combustion. preferable.

また石炭中の残灰分を各炭種毎に値を揃えるということ
は、炭種による発熱量、燃焼効率のQj、らつきを最小
に出来るという効果がある。このような背景のもaこ、
従来°も浮選機を使った石炭高濃度水スラリの脱灰プロ
セスが知られている。
In addition, adjusting the residual ash content in the coal to the same value for each coal type has the effect of minimizing the calorific value, combustion efficiency Qj, and fluctuations depending on the coal type. With a background like this,
A deashing process for high-concentration coal water slurry using a flotation machine has been known in the past.

石炭高濃度水スラリの脱灰プロセスに使われる従来の浮
選機について第1図及び第2図により説明すると、第2
図で200メツシュバス65係〜90%の如く微粉砕さ
れた石炭(5υが起泡剤、補集剤の混合物(200)と
よく攪拌された状態で、石炭濃度10〜80重量係の水
スラリ状でセル1に供給される。セルI、 n、 Il
l、IYは各々第1図に示す断面の構造をしている。
The conventional flotation machine used in the deashing process of highly concentrated coal water slurry is explained using Figs. 1 and 2.
In the figure, finely pulverized coal (5υ) is well stirred with a mixture of foaming agent and scavenger (200), and the coal concentration is 10 to 80% by weight. are supplied to cell 1. Cells I, n, Il
1 and IY each have a cross-sectional structure shown in FIG.

さて第2図において水スラリ状でセルIに送られた石炭
00、起泡剤、補集剤の混合物(200)は、第1図に
示す攪拌翼(4)により充分攪拌される。
Now, in FIG. 2, the mixture (200) of coal 00, foaming agent, and scavenger sent to cell I in the form of a water slurry is sufficiently stirred by the stirring blade (4) shown in FIG.

攪拌翼(4)と駆動プーリα0)を連結している中空軸
(5)lこは、攪拌翼(4)の吸込力lこより空気Q〃
が自動的Iこ入り込み、攪拌翼(4)により泡状となっ
て水中へと吹き出される。また整流板(1) (2) 
(3)は空気泡α6)が全空間へ効率よく拡がるのを助
ける役目をもっている。
The hollow shaft (5) that connects the stirring blade (4) and the drive pulley α0) has air Q due to the suction force of the stirring blade (4).
The water enters the water automatically and is blown out into the water in the form of foam by the stirring blade (4). Also rectifier plate (1) (2)
(3) has the role of helping the air bubble α6) to spread efficiently throughout the entire space.

空気泡αωの気液の境界には、起泡剤、補集剤の混合物
(200)が膜状についていて、石炭θυ中のより炭分
の多い石炭粒子(17)が付着し、空気泡(1匂の浮力
によりセルの上部へ上昇していく。このように上昇した
石炭粒子αηが付着した空気泡(161は、電動機u5
)、駆動チェーン(141により駆動される補集板(1
31により、トレイa功にかき出される。そしてトレイ
(12)に集められた空気泡をつぶすために、ジャワパ
イプ(2υにより水をかける。空気泡α0に付着しない
灰分の多い石炭粒子及び灰分翰は、水と共にセルαυ中
の液レベルを調整するためのゲートα樽を越え、モール
ボックス(6)に流れ込む。
A mixture of foaming agent and scavenger (200) is attached to the gas-liquid boundary of the air bubble αω in the form of a film, and coal particles (17) with a higher carbon content in the coal θυ adhere to the air bubble ( Due to the buoyancy of 1 smell, the coal particles αη rise to the top of the cell.The air bubbles (161 are the electric motor u5
), a collector plate (1) driven by a drive chain (141),
31, it is scraped out by the tray a gong. Then, in order to crush the air bubbles collected in the tray (12), water is applied using a Java pipe (2υ).The ash-rich coal particles and ash particles that do not adhere to the air bubbles α0 together with water reduce the liquid level in the cell αυ. It passes through the adjustment gate α barrel and flows into the mall box (6).

テールボックスに流れ込んだ灰分の多い石炭粒子及び灰
分(11と水は、送流口(力を通って下流のセルへと流
れ込み、再び同じ操作が繰り返えされる。
The ash-rich coal particles and ash (11) and water that have flowed into the tail box flow into the downstream cells through the flow inlet (force), and the same operation is repeated again.

ここで再び第2図に戻って説明をつづける。Here, we return to FIG. 2 again to continue the explanation.

さて第2図において、第1図で説明した作用をセルIで
石炭粒子がうけ、灰分の少ない石炭粒子Hは空気泡と共
にトレイ(至)へ回収され、灰分の多い石炭粒子及び灰
分−はテールボックスへと流れ、パイプ0→を通ってセ
ル■へ流れ込み、再びセルIき同じ作用をうける。そし
て再度灰分の少ない石炭粒子に)は空気泡と共にトレイ
(叫へ回収され、灰分の多い石炭粒子及び灰分0呻はテ
ールボックスへと流れ、パイプHを通ってセル■へ流れ
込み、再びセルIと同じ作用をうける。
Now, in Fig. 2, the coal particles undergo the action explained in Fig. 1 in cell I, and the coal particles H with low ash content are collected into the tray (toward) along with air bubbles, and the coal particles with high ash content and ash content are collected in the tray. It flows into the box, passes through pipe 0 → and flows into cell ■, where it is again subjected to the same effect on cell I. Then, the coal particles with low ash content (coal particles with low ash content) are collected together with air bubbles into the tray (coal particles with low ash content), and the coal particles with high ash content and low ash content flow into the tail box, flow through pipe H to cell ■, and return to cell I. have the same effect.

輪は灰分の少ない石炭粒子、輪は灰分の多い石炭粒子及
び灰分を示していて、同粒子及び灰分に)はテールボッ
クス、パイプ−を通って排水処理の如き灰処理装置へと
送られる0またトレイ(ト)に補集された灰分の少ない
石炭粒子−0時輪は、空気泡と共にあるため容量が大き
くなっているが、ジャワ水により空気泡をできるだけつ
ぶして処理容量を小さくシ、パイグーを通ってセル■で
再び浮選操作を繰り返えす0また灰分が少ない石炭粒チ
ーυは空気泡♂共にトレイ0υに補集され、ジャワ水に
より処理容量を小さくシ、製品として石炭濃度40〜5
0重量%となって脱灰処理は完了する。セル1vで灰分
の多い石炭粒子及び灰分−はテールボックスに集められ
、パイプf3′4を通って再びセル■に送液される。
Rings indicate coal particles with low ash content, rings indicate coal particles with high ash content and ash content, and the particles and ash content are sent to ash treatment equipment such as wastewater treatment through tail boxes and pipes. The coal particles with low ash content collected in the tray (T) have a large capacity because they are together with air bubbles, but the processing capacity is reduced by crushing the air bubbles as much as possible with Java water. Coal grains with low ash content are collected in tray 0υ with air bubbles ♂, and the processing capacity is reduced with Java water, resulting in a product with a coal concentration of 40 to 5.
The deashing process is completed when the amount becomes 0% by weight. Coal particles with a high ash content and ash content in cell 1v are collected in a tail box and sent to cell 2 again through pipe f3'4.

石炭高濃度水スラリ用の脱灰プロセスに浮選機を使った
場合のフロー構造は以上の通りであるが、石炭高濃度水
スラリに適用した場合には、次の如き欠点があった。
The flow structure when a flotation machine is used in the deashing process for a highly concentrated coal water slurry is as described above, but when it is applied to a highly concentrated coal water slurry, it has the following drawbacks.

(1)石炭高濃度水スラリの石炭粒度は200メツシュ
パス65〜90%の如く微粒子のため、浮選のための起
泡剤、補集剤の混合物試薬の量が大量に必要となり、ト
レイ(至)Ovに補集された灰分の少ない石炭粒子をつ
けている空気泡が強固で、ジャワ水のみで消すのは困難
であった。 − (II)  石炭高濃度水スラリの脱灰処理ということ
でトレイに回収する炭分が多く、セル■、■、■1より
トレイに回収した粗選の空気泡が大量になり、消泡のた
めのジャワ水が多量となる。しかし加えたジャワ水はセ
ル■(精選区)に流れ込み、セル■中の石炭濃度、起泡
剤、補集剤の混合物試薬濃度が下り、セルiv中の浮選
速度が早くなり、セル1■よりトレイGυに回収される
灰分の少ない石炭elυの歩留(精選歩留)が悪化する
欠点があった。
(1) Since the coal particle size of the highly concentrated coal water slurry is as fine as 65% to 90% of the 200 mesh pass, a large amount of a mixture reagent of foaming agent and scavenger is required for flotation. ) The air bubbles that attached the low ash coal particles collected in Ov were strong and difficult to eliminate with Java water alone. - (II) Due to the deashing treatment of highly concentrated coal water slurry, there is a large amount of coal collected in the tray, and a large amount of roughly selected air bubbles collected in the tray from cells ■, ■, and ■1 becomes difficult to defoamer. There is a large amount of Java water for this purpose. However, the added Java water flows into cell ■ (selected area), the concentration of coal in cell ■, the concentration of the mixture of foaming agent and scavenger reagent decreases, the flotation rate in cell IV increases, and cell 1■ There was a drawback that the yield (refined yield) of coal elυ with a lower ash content recovered in the tray Gυ deteriorated.

(1)  セル■よりトレイ(31Jに回収される灰分
の少ない石炭@0(精成)の空気泡をつぶすためのジャ
ワ水が多いと、パイプに)より後工程にある排水処理工
程の容量が大きくなり、建設費が大きくなる欠点があっ
た。   ゛本発明は前記従来の欠点を解消するために
提案されたもので、トレイCご用いるジャワ水を減少さ
せることを目的とし、トレイに用いるジャワ水を減少さ
せるため、トレイに補集された空気泡に剪断力を与え、
空気泡を小さくしたり、つぶしたりする機械装置を前記
トレイ中に具備せしめた浮選機を提供せんとするもので
、第8図〜第6図にその実施例を示す。
(1) The capacity of the wastewater treatment process that is downstream from the tray (if there is a lot of Java water to collapse the air bubbles in the low-ash coal @ 0 (refined) recovered in 31J, the capacity is increased from the cell ■ to the pipe) The drawback was that it was larger and the construction costs were higher.゛The present invention was proposed in order to eliminate the above-mentioned conventional drawbacks, and aims to reduce the amount of Java water used in Tray C. Applying shear force to the bubbles,
The present invention aims to provide a flotation machine in which the tray is equipped with a mechanical device for reducing or crushing air bubbles, and an embodiment thereof is shown in FIGS. 8 to 6.

以下本発明を第8図〜第6図に示す実施例について説明
すると、第8図ではトレイ(至)に回転円筒−が備えら
れ、同回転円筒−の表面に第4図(イ)(0)(ハ)に
いくつかの例を示したバー(101)又は(102)(
108)を、灰分の少ない石炭が送られる方向C呻に螺
旋状に取り付けていて、空気泡に剪断力を与えて同空気
泡をつぶしたり、小さくしたりできるようになっている
。バーの形は第4図(イ)に示すバー(101) 、(
C1)に示すバー(102)、(ハ)に示すバー(10
8)の如く、空気泡に剪断力を与え易い形が考えられる
The present invention will be described below with reference to the embodiments shown in FIGS. 8 to 6. In FIG. ) (c) shows some examples of bar (101) or (102) (
108) are spirally attached in the direction C in which coal with a low ash content is sent, and it is possible to crush or reduce the size of air bubbles by applying shearing force to the air bubbles. The shape of the bar is the bar (101) shown in Figure 4 (a), (
The bar (102) shown in C1), the bar (102) shown in (C)
8), a shape that can easily apply shearing force to the air bubbles can be considered.

また回転体−の回転数は800〜1000 rpmの如
く高速回転とし、剪断力を空気泡に有効に与えるように
している。
The rotating body is rotated at a high speed of 800 to 1000 rpm to effectively apply shearing force to the air bubbles.

第5図は本発明の別の実施例を示す。第5図において、
トレイ(至)内に設けられた2本のチェノ(118)に
攪拌板fl12)が取り付けられ、駆動軸(110)に
取り付けられている鎖車(111)により、空気泡に剪
断力が与えられるよう回転する。また従動軸(115)
にも鎖車(114)がついていて従動させられる。(1
16) (117)は軸受で、トレイ(至)に固定され
ている。
FIG. 5 shows another embodiment of the invention. In Figure 5,
A stirring plate fl12) is attached to two chinos (118) provided in the tray (to), and a shearing force is applied to the air bubbles by a chain wheel (111) attached to a drive shaft (110). Rotate like this. Also, the driven shaft (115)
The chain wheel (114) is also attached to it and is driven. (1
16) (117) is a bearing, which is fixed to the tray (to).

第6図は第5図のA−A断面図で、(118)は灰分の
少ない石炭の排出口である。また攪拌板(112)の移
□動速度は、灰分の少ない石炭の送られる方向ケリへの
移動速度の少なくとも2倍以上とし、空気泡に剪断力を
与えるのが゛良い。
FIG. 6 is a sectional view taken along the line A-A in FIG. 5, and (118) is an outlet for coal with a low ash content. Further, the moving speed of the stirring plate (112) is preferably at least twice the moving speed in the direction in which coal with a low ash content is sent, so as to apply shearing force to the air bubbles.

以上詳細に説明した如く本発明は構成されているので、
トレイに回収された空気泡に剪断力を与えて同空気泡を
小さくしたり、つぶしたりすることができる。従ってト
レイ内でジャワ水で処理される容量を小さくでき、ジャ
ワ水の量を減少させることができる。
Since the present invention is configured as explained in detail above,
By applying a shearing force to the air bubbles collected in the tray, the air bubbles can be made smaller or crushed. Therefore, the capacity to be treated with Java water in the tray can be reduced, and the amount of Java water can be reduced.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の石炭浮選機を示す側断面図、舗2図は第
1図の浮選機を設置されたセルを並設してなる脱灰プロ
セスを示す平面図、第8図は本発明の実施例を示す浮選
機におけるトレイの平面図、第4図(イ)(0)(ハ)
は夫々異なる実施例の、第8図の回転円筒に取付けるバ
ーの斜視図、第5図は第8図と異なる実施例を示すトレ
イの平面図、第6図は第8図のA−A断面図である。 図の主要部分の説明 80・・・トレイ     100・・・回転円筒10
1、102.108 ・・・バー 112・・・撹拌板
特許出願人 三菱重工業株式会社 同        菱日エンジニアリング株式会社7 
第3図 帛4図 (イ)          1口)(/\)第5図 π
Figure 1 is a side sectional view showing a conventional coal flotation machine, Figure 2 is a plan view showing a deashing process in which cells equipped with the flotation machine of Figure 1 are arranged side by side, and Figure 8 is a side sectional view showing a conventional coal flotation machine. A plan view of a tray in a flotation machine showing an embodiment of the present invention, FIG. 4 (A) (0) (C)
8 is a perspective view of a bar attached to the rotating cylinder of FIG. 8, each showing a different embodiment, FIG. 5 is a plan view of a tray showing an embodiment different from that of FIG. 8, and FIG. 6 is a cross section taken along line A-A in FIG. 8. It is a diagram. Description of main parts of the figure 80...Tray 100...Rotating cylinder 10
1, 102.108... Bar 112... Stirring plate Patent applicant Mitsubishi Heavy Industries, Ltd. Ryonichi Engineering Co., Ltd. 7
Figure 3 Figure 4 (a) 1 bite) (/\) Figure 5 π

Claims (1)

【特許請求の範囲】[Claims] 200メツシュパス65〜90%の如き微粉炭を脱灰処
理する石炭浮選機において、灰分の少ない石炭粒子が空
気泡と共に回収されるトレイを有する石炭浮選機におい
て、同トレイ内に、前記回収された空気泡に機械的に剪
断力を与える40mを配設したことを特徴とする石炭浮
選機。
In a coal flotation machine that deashes pulverized coal such as 200 mesh pass 65 to 90%, in a coal flotation machine that has a tray in which coal particles with a low ash content are collected together with air bubbles, the collected coal particles are A coal flotation machine characterized by being equipped with a 40m length that mechanically applies shearing force to air bubbles.
JP57216682A 1982-12-10 1982-12-10 Coal flotation machine Pending JPS59105810A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57216682A JPS59105810A (en) 1982-12-10 1982-12-10 Coal flotation machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57216682A JPS59105810A (en) 1982-12-10 1982-12-10 Coal flotation machine

Publications (1)

Publication Number Publication Date
JPS59105810A true JPS59105810A (en) 1984-06-19

Family

ID=16692269

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57216682A Pending JPS59105810A (en) 1982-12-10 1982-12-10 Coal flotation machine

Country Status (1)

Country Link
JP (1) JPS59105810A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001093978A1 (en) * 2000-06-05 2001-12-13 M.I.M. Holdings Limited Method and apparatus for froth deaeration

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001093978A1 (en) * 2000-06-05 2001-12-13 M.I.M. Holdings Limited Method and apparatus for froth deaeration

Similar Documents

Publication Publication Date Title
JP4917309B2 (en) How to remove unburned carbon in fly ash
KR101287486B1 (en) Apparatus for removing of unburned carbon from fly ash and relevant removing method
CN100455357C (en) Method of removing unburned carbon from fly ash
EP0787107B1 (en) Equipment for the purification of a liquid
US10040104B2 (en) Soil remediation facility and soil remediation method using the same
KR20090109529A (en) Method of removing unburned carbon from coal ash
US4659458A (en) Apparatus and method for froth flotation employing rotatably mounted spraying and skimming means
JPH0711268A (en) Production of deashed high-concentration coal-water slurry
KR101047166B1 (en) A flotation apparatus for treating high-concentrated organic waste water
PL166219B1 (en) Chaser mill
JP4346299B2 (en) Pulverized coal flotation method, pulverized coal surface reformer, and pulverized coal flotation system
JPS59105810A (en) Coal flotation machine
JP4751139B2 (en) Equipment for removing unburned carbon in fly ash
GB2058737A (en) Concentrating sludge
JP4969764B2 (en) Method and apparatus for collecting pulverized coal
GB2162196A (en) Sewage treatment process
RU2223828C2 (en) Method of concentration of coal sludge
JPS6228705B2 (en)
JPS60122065A (en) Method for recovering fine granulated coal by floatation
Gürsu et al. Beneficiation of fine bituminous coal by column flotation
SU839572A1 (en) Pneumomechanic flotation machine
JPS5773082A (en) Granulating method of coal
JPS5773083A (en) Granulating method of coal and apparatus thereof
JPS5939332A (en) Granulator
JPS59142289A (en) Deashing of coal