JPS585394A - Submerged granulation of pulverized coal - Google Patents
Submerged granulation of pulverized coalInfo
- Publication number
- JPS585394A JPS585394A JP10245081A JP10245081A JPS585394A JP S585394 A JPS585394 A JP S585394A JP 10245081 A JP10245081 A JP 10245081A JP 10245081 A JP10245081 A JP 10245081A JP S585394 A JPS585394 A JP S585394A
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- coal
- pulverized coal
- granulated
- particle size
- 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
Links
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
【発明の詳細な説明】
微粉炭をノ々インダーの存在下に水中で攪拌して造粒し
、得られたスラリーを篩にかけて所望粒径の造粒炭を回
収する微粉炭の水中造粒法に於ては、I9インダー(普
通、重油その他の粘稠油が使用される)の使用量をでき
るだけ少なくすることが好ましいとされているOこれは
経済的理由もさることながら、バインダーの量が余り多
いと、スラリーを簡分けする際に造粒炭の水切れが極端
に悪化するからである。尤もバインダー量が余りに少な
すぎると、それに見合う量の微粉炭しか造粒できなに九
め、造粒炭の収量が低下する@従って、本来ならば原料
たる微粉炭の粒径や諸々の造粒条件を考慮して、バイン
ダーの量を過不足ない量に調節するのが理想である。し
かし、バインダー量を過不足なく調節することは、実際
問題として極めて困難であるので、実操業では/々イン
グー量を多少不足気味にして、造粒工程からのスラリー
を篩にかけて目標粒径の造粒炭を回収し、篩下スラリー
はこれを廃棄してしまう従来の水中造粒法で社、未造粒
の11の微粉炭や造粒されても目標粒径まで成長しなか
った造粒炭が、篩下スラリーに逃げてしまう不利を免れ
ない。[Detailed Description of the Invention] A method for underwater granulation of pulverized coal, in which pulverized coal is granulated by stirring in water in the presence of a Nono Inder, and the resulting slurry is sieved to recover granulated coal with a desired particle size. It is said that it is preferable to use as little amount of I9 binder (usually heavy oil or other viscous oil is used) as possible in the This is because if the amount is too large, drainage of the granulated coal becomes extremely difficult when dividing the slurry. Of course, if the amount of binder is too small, only a commensurate amount of pulverized coal will be granulated, and the yield of granulated coal will decrease. Ideally, the amount of binder should be adjusted to just the right amount, taking into account the conditions. However, it is extremely difficult in practice to adjust the amount of binder to just the right amount, so in actual operations, the amount of binder is slightly insufficient and the slurry from the granulation process is sieved to produce the target particle size. The conventional underwater granulation method collects the granulated coal and discards the slurry under the sieve. However, it cannot escape the disadvantage of escaping into the sieve slurry.
本発明は従来の水中造粒法に浮選工程を組込むことによ
り、従来法では篩下スラリーに逃げてしまう石炭粒子を
も造粒して造粒炭の収量増大を図る方法を提案する0す
なわち、本発明の方法は微粉炭を/セインダーの存在下
に水中造粒する工程と、この水中造粒工程からのスラリ
ーを簡にかけて所望粒径の造粒炭を篩上に回収する工程
を包含する微粉炭の水中造粒法に於て、前記の部分は工
程で得られる篩下スラリーに浮選処理を施してこのスラ
リーに含まれる微粉炭並びに所望粒径以下の造粒炭を分
離し、これらの石炭粒子を前記の水中造粒工程に循還す
ることを特徴とする0
以下図面にそって本発明の詳細な説明すると、原料たる
微粉炭のスラリーとバインダーとは水中造粒装置1の入
口に供給される0図示の例ではそれぞれ攪拌翼を具えて
直列に接続された3基の攪拌槽で水中造粒装f1が構成
されているO微粉炭は水中造111m置l内に於てバイ
ンダーの存在下に攪拌されることにより造粒され、造粒
装置1の出口からスラリー状でオーバーフローする。こ
のオーツセーフローは所望の目開き(例えば篩目0.5
m )の弧状篩2及び線動篩3に供給され、ここに於
て所望粒径(例えば0.5 m以上)の造粒炭は篩上に
、未造粒の微粉炭と所望粒径以下の造粒炭を含有するス
ラリーは篩下にそれぞれ分離される。そして篩上の造粒
炭はコンベアー4によって貯蔵場所に運搬される〇一方
、弧状@2及び振動篩3で得られる篩下スラリーは、従
来法−ζよれば、そのままシックナー6に供給されて固
液分離され、その固形分は廃棄されるが、本発明によれ
ば、上記の篩下スラリーは浮選機5に供給される0浮選
機5では起泡剤の存在下に篩下スラリー中の未造粒微粉
炭と所望粒径以下の造粒炭が浮選され、これらはフロス
として浮選機5から取シ出され1図示の通り水中造粒装
置lの入口に循環されるのである。篩下スラリー中の泥
分は浮選機5の底部からシックナー6に排出され、ここ
で濃縮された後廃棄される@
以上説明して来たところから明らかな通り、本発明の方
法によれば微粉炭及び所望粒径以下の造粒炭を繰返し造
粒工程に付すことができるので、Aイングー量を増加さ
せなくとも、換言すれば造粒炭の水切れ性を犠牲にしな
くても、所望粒径にある造粒炭の収量を増大させること
ができ、従ってまた微粉炭のaxを大幅に減少させるこ
とができる0The present invention proposes a method for increasing the yield of granulated coal by incorporating a flotation step into the conventional underwater granulation method, thereby granulating coal particles that escape into the slurry under the sieve in the conventional method. , the method of the present invention includes the steps of granulating pulverized coal underwater in the presence of a saunder, and briefly applying the slurry from this underwater granulation step to collect granulated coal of the desired particle size on a sieve. In the underwater granulation method of pulverized coal, the above-mentioned part is obtained by subjecting the under-sieve slurry obtained in the process to flotation treatment to separate the pulverized coal contained in this slurry and granulated coal with a particle size below the desired particle size. The invention is characterized in that the coal particles are recycled to the underwater granulation process described above. In the illustrated example, the underwater granulator f1 is made up of three stirring tanks connected in series, each equipped with a stirring blade. The slurry is granulated by stirring in the presence of the granulator 1, and overflows from the outlet of the granulator 1 in the form of a slurry. This oat safe flow has a desired mesh size (e.g. sieve mesh 0.5).
m) is supplied to an arcuate sieve 2 and a linear sieve 3, where granulated coal with a desired particle size (for example, 0.5 m or more) is placed on the sieve with ungranulated pulverized coal and pulverized coal with a particle size smaller than the desired particle size. The slurry containing granulated coal is separated under the sieve. Then, the granulated coal on the sieve is transported to the storage place by the conveyor 4. On the other hand, the slurry under the sieve obtained from the arc @ 2 and the vibrating sieve 3 is supplied as it is to the thickener 6 according to the conventional method-ζ. Solid-liquid separation is performed, and the solid content is discarded.According to the present invention, the above-mentioned under-sieve slurry is supplied to the flotation machine 5.In the flotation machine 5, the under-sieve slurry is separated in the presence of a foaming agent. The ungranulated pulverized coal and the granulated coal with a particle size smaller than the desired size are flotated, and these are taken out from the flotation machine 5 as froth and circulated to the inlet of the underwater granulation device 1 as shown in Figure 1. be. The mud in the undersieve slurry is discharged from the bottom of the flotation machine 5 to the thickener 6, where it is concentrated and then discarded. As is clear from the above explanation, according to the method of the present invention, Since pulverized coal and granulated coal having a particle size smaller than the desired particle size can be repeatedly subjected to the granulation process, the desired granule can be produced without increasing the amount of A-ing, or in other words, without sacrificing the drainage properties of the granulated coal. can increase the yield of granulated coal in diameter, and therefore can also significantly reduce the ax of pulverized coal.
図面は本発明の一実施例で採用されるフルーダイアグラ
ムであるOThe drawing is a full diagram adopted in one embodiment of the present invention.
Claims (1)
と、この水中造粒工程からのスラリーを簡にかけて所望
粒径の造粒炭を回収する工程、を包含する微粉炭の水中
造粒法に於て、前記の篩分は工程で得られる篩下スラリ
ーを浮選処理に付してこのスラリーに含まれる微粉炭と
所望粒径以下の造粒炭を分離し、これらを前記の水中造
粒工程に循環することを特徴とする微粉炭の水中造粒法
O1. An underwater granulation method for pulverized coal that includes the steps of granulating pulverized coal underwater in the presence of a binder, and simply applying slurry from this underwater granulation step to recover granulated coal of a desired particle size. In the above-mentioned sieving process, the under-sieve slurry obtained in the process is subjected to flotation treatment to separate the pulverized coal contained in this slurry and the granulated coal having a particle size below the desired particle size, and these are then subjected to the above-mentioned underwater granulation process. Underwater granulation method for pulverized coal characterized by circulation in the granulation process O
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10245081A JPS585394A (en) | 1981-07-01 | 1981-07-01 | Submerged granulation of pulverized coal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10245081A JPS585394A (en) | 1981-07-01 | 1981-07-01 | Submerged granulation of pulverized coal |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS585394A true JPS585394A (en) | 1983-01-12 |
Family
ID=14327803
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10245081A Pending JPS585394A (en) | 1981-07-01 | 1981-07-01 | Submerged granulation of pulverized coal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS585394A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61103992A (en) * | 1984-10-26 | 1986-05-22 | Tokyo Electric Power Co Inc:The | Deashing recovery of coal |
-
1981
- 1981-07-01 JP JP10245081A patent/JPS585394A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61103992A (en) * | 1984-10-26 | 1986-05-22 | Tokyo Electric Power Co Inc:The | Deashing recovery of coal |
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