JPS62169890A - Production of highly concentrated coal slurry - Google Patents
Production of highly concentrated coal slurryInfo
- Publication number
- JPS62169890A JPS62169890A JP1074886A JP1074886A JPS62169890A JP S62169890 A JPS62169890 A JP S62169890A JP 1074886 A JP1074886 A JP 1074886A JP 1074886 A JP1074886 A JP 1074886A JP S62169890 A JPS62169890 A JP S62169890A
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- coal
- highly concentrated
- finely divided
- coarse particles
- 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
- 239000003250 coal slurry Substances 0.000 title claims abstract description 8
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000011362 coarse particle Substances 0.000 claims abstract description 23
- 239000002002 slurry Substances 0.000 claims abstract description 23
- 239000003245 coal Substances 0.000 claims abstract description 14
- 239000000843 powder Substances 0.000 claims abstract description 10
- 239000010419 fine particle Substances 0.000 claims description 10
- 238000007667 floating Methods 0.000 claims description 6
- 238000003756 stirring Methods 0.000 abstract description 12
- 239000002245 particle Substances 0.000 abstract description 8
- 239000000446 fuel Substances 0.000 abstract description 7
- 239000004094 surface-active agent Substances 0.000 abstract description 6
- 239000004088 foaming agent Substances 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 238000002485 combustion reaction Methods 0.000 abstract description 3
- 238000004898 kneading Methods 0.000 abstract description 3
- 239000000725 suspension Substances 0.000 abstract 2
- 208000005156 Dehydration Diseases 0.000 abstract 1
- 230000005587 bubbling Effects 0.000 abstract 1
- 230000018044 dehydration Effects 0.000 abstract 1
- 238000006297 dehydration reaction Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000010298 pulverizing process Methods 0.000 abstract 1
- 239000007787 solid Substances 0.000 description 3
- 238000007873 sieving Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
【発明の詳細な説明】
(1) 産業上の利用分野
この発明は火力発電などに用いられる石炭高濃度スラリ
ーの製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (1) Industrial Application Field This invention relates to a method for producing a highly concentrated coal slurry used in thermal power generation and the like.
(2)従来の技術
第3.4図に従来一般的な石炭高濃度スラリー(CWM
)の製造方法を示す。図面において1は粉砕機、2は振
動スクリーンやシーブベンドなどの機械式篩分機、3は
フィルタなどの脱水機、4は混線機である。粉砕機lに
おいて石炭aは水すを加えられ湿成により。(2) Conventional technology Figure 3.4 shows the conventionally common high concentration coal slurry (CWM).
). In the drawings, 1 is a crusher, 2 is a mechanical sieve such as a vibrating screen or sieve bend, 3 is a dehydrator such as a filter, and 4 is a mixer. In pulverizer L, coal A is added with water and subjected to wet conversion.
−200メツシユ、約80%以上に粉砕される。-200 mesh, crushed to about 80% or more.
この粉砕された石炭粉は篩分機2により粗粒が除去でき
るように分級されるが、篩分機2の網の目詰り、製作上
の制限、及び篩上べ一200メツシュが逃げる問題が生
じるため、網の目開きを200メツシユ以上としなけれ
ばならず、必らず網下へ不必要な+200メツシユの粗
粒(例えば0.5mm以上)が混入してしまう、そして
このような粗粒を含んだスラリーが下記設備へ供給され
る。そのため−200メツシユの微粒に+200メツシ
ユの粗粒が混入したスラリーが脱水機3に供給され、脱
水機3で脱水処理された後、混線Ja4へ送られ、ここ
で所定量の界面活性剤Cを加えられて固体濃度65〜7
0%位でCWM化する。そして、CWM化スラリーdは
ボイラー等の燃料に供される。This pulverized coal powder is classified by the sieve machine 2 to remove coarse particles, but this causes problems such as clogging of the mesh of the sieve machine 2, manufacturing limitations, and escaping of 200 mesh pieces on the sieve. , the opening of the mesh must be 200 meshes or more, and unnecessary coarse particles (for example, 0.5 mm or more) of +200 meshes will inevitably get mixed into the bottom of the screen, and such coarse particles should not be included. The slurry is supplied to the following equipment. Therefore, a slurry in which -200 mesh fine particles and +200 mesh coarse particles are mixed is supplied to dehydrator 3, dehydrated in dehydrator 3, and then sent to cross line Ja4, where a predetermined amount of surfactant C is added. Added solids concentration 65-7
Converts to CWM at around 0%. The CWM slurry d is then used as fuel for a boiler or the like.
(3) 発明が解決しようとする問題点ところで、前
記のようにCWM化されたスラリ−は、+200メツシ
ユの粗粒を含んでいるため、燃料として供給されるバー
ナによる燃焼時において、バーナのノズルを閉塞させた
り、ボイラー内等で未燃分として残り、燃焼効率を低下
させる原因となる等の悪影響を及ぼしている。このこと
は第4図に示すように、第3図の篩分機2、脱水機3.
混練機4に代え、濃度調整攪拌槽5と第2粉砕機6を設
置し、粉砕機1で粉砕されたスラリーを濃度調整攪拌槽
5に導入し、この攪拌槽5で攪拌処理したうえ、第2粉
砕機6に導入する前に界面活性剤Cを加え、第2粉砕機
6でさらに細かく粉砕する製造方法においても同様のこ
とがいえ、この場合でもスラリー中への+200メツシ
ユの粗粒の混入を防止することが不可能であった。(3) Problems to be Solved by the Invention By the way, since the CWM-formed slurry as described above contains coarse particles of +200 mesh, when it is burned by the burner supplied as fuel, the burner nozzle This has negative effects such as clogging the fuel and remaining unburned in the boiler, causing a reduction in combustion efficiency. As shown in FIG. 4, this can be explained by the sieving machine 2, dehydrator 3, etc. in FIG.
In place of the kneader 4, a concentration adjustment stirring tank 5 and a second pulverizer 6 are installed, and the slurry pulverized by the pulverizer 1 is introduced into the concentration adjustment stirring tank 5, stirred in the stirring tank 5, and then The same thing can be said for the manufacturing method in which surfactant C is added before introduction into the second pulverizer 6, and the second pulverizer 6 grinds the slurry even more finely, and even in this case, coarse particles of +200 mesh are mixed into the slurry. It was impossible to prevent this.
そこで、この発明は粉砕機で粉砕された粗粒を含む石炭
粉を下流設備に供給する前に該石炭粉中から粗粒を確実
に除去できるようにすることを技術的課題とする。Therefore, the technical object of the present invention is to ensure that the coarse particles can be removed from the coal powder that has been crushed by a pulverizer before being supplied to downstream equipment.
(4)問題点を解決するための手段
前記のような問題点を解決するため、この発明の石炭高
類度スラリーの製造方法は、粉砕機で粉砕された微粒に
粗粒が混入した石炭粉を浮遊分級器に導入し、この浮遊
分級器の分級により前記石炭粉から粗粒を除去したのち
、微粒のみの高濃度スラリーとして下流設備に供給する
ことを特徴とする。(4) Means for Solving the Problems In order to solve the above-mentioned problems, the method for producing high-grade coal slurry of the present invention uses coal powder in which coarse particles are mixed with fine particles crushed by a pulverizer. The coal powder is introduced into a floating classifier, coarse particles are removed from the coal powder by classification by the floating classifier, and then a highly concentrated slurry containing only fine particles is supplied to downstream equipment.
(5)実施例
以下に示す実施例において、従来のものと同一の部材に
は同一の符号を付して説明を省略する。(5) Embodiments In the embodiments shown below, the same members as those in the conventional system are given the same reference numerals, and the explanation thereof will be omitted.
第1図はこの発明の1実施例を示したものである。図面
において、7は粉砕機1と攪拌槽5の間に設置され、気
泡の浮力を利用する浮遊分級器であり、この分級器7の
タンク内には界面活性剤eと気泡剤fが回収すべき粒度
を浮遊させる量だけ添加され、攪拌により所望量の気泡
を発生させるようになっている。FIG. 1 shows one embodiment of the invention. In the drawing, 7 is a floating classifier that is installed between the crusher 1 and the stirring tank 5 and uses the buoyancy of air bubbles. It is added in an amount that suspends the desired particle size, and the desired amount of bubbles is generated by stirring.
そして、前記の回収すべき粒度を+200メツシユの粗
粒(0、5mm以上)が気泡に接触し浮上しないように
コントロールすることにより。Then, the particle size to be recovered is controlled so that coarse particles (0.5 mm or more) of +200 mesh do not come into contact with air bubbles and float.
スラリー中の粗粒は浮遊せず、微粒のみが浮遊するよう
にされる。Coarse particles in the slurry are not suspended, and only fine particles are suspended.
このことを更に詳しく説明する。界面活性剤e、及び気
泡剤fを収容した分級器lのタンク内で攪拌翼(ロータ
)を回転して攪拌すると、タンク内には空気及び前記気
泡剤f等により微細な泡が発生する。このようにして所
望量の気泡が発生したタンク内に、粉砕機lで粉砕され
た粗粒を含むスらり−を導入すると、スラリー中の粗粒
はタンク底に沈降してしまい、微粒のみが気泡に接触し
て浮上し、気泡水とともにオーバーフローして回収され
、攪拌槽6に導入される。粒度分級は、タンク内に導入
されるスラリーの固体濃度が15〜50%の範囲で十分
に可能である。また、タンク底に沈降した粗粒は適宜の
手段で除去される。This will be explained in more detail. When a stirring blade (rotor) is rotated to stir the surfactant e and the foaming agent f in the tank of the classifier l containing the surfactant e and the foaming agent f, fine bubbles are generated in the tank due to the air and the foaming agent f. When a slurry containing coarse particles crushed by a crusher 1 is introduced into a tank in which a desired amount of bubbles have been generated, the coarse particles in the slurry will settle to the bottom of the tank, leaving only fine particles. comes into contact with the bubbles and floats up, overflows and is collected together with the bubble water and introduced into the stirring tank 6. Particle size classification is fully possible when the solids concentration of the slurry introduced into the tank is in the range 15-50%. In addition, coarse particles that have settled to the bottom of the tank are removed by appropriate means.
このように、粉砕mlで粉砕された粗粒を含むスラリー
は、分級器7によって+200メツシユの粗粒が除去さ
れ、−200メツシユの微粒だけのスラリーとして下流
設備に供給される。そのため、下流設備としての攪拌槽
5゜脱水機3、混練機4を経てCWM化されたスラリー
は、従来と同様、固体濃度65〜70%位の高濃度状態
でボイラー等の燃料に供され、燃料として高品質のもの
となる。In this way, the slurry containing the coarse particles pulverized by the milliliter is supplied to the downstream equipment after the +200 mesh coarse particles are removed by the classifier 7, and a slurry containing only the -200 mesh fine particles is supplied to the downstream equipment. Therefore, the slurry that has been converted into CWM after passing through the stirring tank 5° dehydrator 3 and kneader 4 as downstream equipment is used as fuel for boilers etc. in a highly concentrated state with a solids concentration of about 65 to 70%, as in the past. It becomes a high quality fuel.
第2図は第1図の実施例の異なる使用態様を示したもの
で、第1図の混練機4に代え。FIG. 2 shows a different usage mode of the embodiment shown in FIG. 1, in which the kneading machine 4 in FIG. 1 is replaced.
第2粉砕機6を設置したものである。このような使用に
おいても浮遊分級器7で前記と同様の分級が行なわれ、
第2粉砕機6を経てCWM化されたスラリーの品質に変
わるところがない。A second crusher 6 is installed. Even in such use, the floating classifier 7 performs the same classification as described above,
There is no change in the quality of the CWM slurry that has passed through the second crusher 6.
(6)発明の効果
以上のようにこの発明によれば、粉砕機で粉砕された微
粒に粗粒が混入した石炭粉を下流設備に供給する前に、
該粗粒を1%遊分級器の分級により除去したのち、微粒
のみの高濃度スラリーとして供給するので、これにょっ
てCWM化したスラリーをボイラー等の燃料として供し
ても、バーナノズルの閉塞や燃焼効率の低下の原因とな
る等の従来の問題点を完全に解消することができるとい
う優れた効果を有する。(6) Effects of the Invention As described above, according to the present invention, before supplying coal powder in which coarse particles are mixed with fine particles crushed by a crusher to downstream equipment,
After the coarse particles are removed by classification using a 1% free classifier, it is supplied as a highly concentrated slurry containing only fine particles, so even if the CWM slurry is used as fuel for boilers, there will be no clogging of burner nozzles or combustion. It has an excellent effect in that it can completely eliminate the conventional problems such as causing a decrease in efficiency.
第1図はこの発明の1実施例を示すフローシート、第2
図は第1図の異なる使用態様を示すフローシート、第3
図は従来例を示すフローシート、第4図は第3図の異な
る使用態様を示すフローシートである。
l・・・粉砕機 2・・・篩分機
3・・脱水機 4・・・混練機
5・・濃度調整攪拌槽Figure 1 is a flow sheet showing one embodiment of this invention;
The figure is a flow sheet showing a different usage pattern from Figure 1.
The figure is a flow sheet showing a conventional example, and FIG. 4 is a flow sheet showing a different usage mode from FIG. l...Crusher 2...Sieving machine 3...Dehydrator 4...Kneading machine 5...Concentration adjustment stirring tank
Claims (1)
を浮遊分級器に導入し、この浮遊分級器の分級により前
記石炭粉から粗粒を除去したのち、微粒のみの高濃度ス
ラリーとして下流設備に供給することを特徴とする石炭
高濃度スラリーの製造方法。1. Coal powder, which has been crushed by a pulverizer and has coarse particles mixed with fine particles, is introduced into a floating classifier, and after the coarse particles are removed from the coal powder by the classification of this floating classifier, a highly concentrated slurry containing only fine particles is produced. A method for producing a highly concentrated coal slurry, characterized in that the slurry is supplied to downstream equipment as a slurry.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1074886A JPS62169890A (en) | 1986-01-21 | 1986-01-21 | Production of highly concentrated coal slurry |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1074886A JPS62169890A (en) | 1986-01-21 | 1986-01-21 | Production of highly concentrated coal slurry |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62169890A true JPS62169890A (en) | 1987-07-27 |
Family
ID=11758930
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1074886A Pending JPS62169890A (en) | 1986-01-21 | 1986-01-21 | Production of highly concentrated coal slurry |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62169890A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5717241A (en) * | 1993-12-09 | 1998-02-10 | Northern Telecom Limited | Gate controlled lateral bipolar junction transistor |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5949291A (en) * | 1982-09-14 | 1984-03-21 | Electric Power Dev Co Ltd | Preparation of concentrated coal slurry |
JPS60156795A (en) * | 1984-01-25 | 1985-08-16 | Mitsubishi Heavy Ind Ltd | Manufacture of highly concentrated coal-water slurry |
-
1986
- 1986-01-21 JP JP1074886A patent/JPS62169890A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5949291A (en) * | 1982-09-14 | 1984-03-21 | Electric Power Dev Co Ltd | Preparation of concentrated coal slurry |
JPS60156795A (en) * | 1984-01-25 | 1985-08-16 | Mitsubishi Heavy Ind Ltd | Manufacture of highly concentrated coal-water slurry |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5717241A (en) * | 1993-12-09 | 1998-02-10 | Northern Telecom Limited | Gate controlled lateral bipolar junction transistor |
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