JPS6147195B2 - - Google Patents

Info

Publication number
JPS6147195B2
JPS6147195B2 JP17917381A JP17917381A JPS6147195B2 JP S6147195 B2 JPS6147195 B2 JP S6147195B2 JP 17917381 A JP17917381 A JP 17917381A JP 17917381 A JP17917381 A JP 17917381A JP S6147195 B2 JPS6147195 B2 JP S6147195B2
Authority
JP
Japan
Prior art keywords
coal
water
slurry
ash
flotation machine
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.)
Expired
Application number
JP17917381A
Other languages
Japanese (ja)
Other versions
JPS5880389A (en
Inventor
Kazuhiko Nakaooji
Mitsugi Kamao
Kunizo Shinano
Toichiro Nagase
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.)
Electric Power Development Co Ltd
Sumitomo Heavy Industries Ltd
Original Assignee
Electric Power Development Co Ltd
Sumitomo 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 Electric Power Development Co Ltd, Sumitomo Heavy Industries Ltd filed Critical Electric Power Development Co Ltd
Priority to JP17917381A priority Critical patent/JPS5880389A/en
Publication of JPS5880389A publication Critical patent/JPS5880389A/en
Publication of JPS6147195B2 publication Critical patent/JPS6147195B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は石炭を流体燃料としてハンドリングし
かつボイラーをはじめ各種の目的にかなう炉へ直
接投入できるようにした高濃度石炭−水スラリー
を製造する方法に関する。 石炭は固体であり、通常2インチ以下に粉砕さ
れて貨車その他の手段でバルク輸送されている。
しかし、この輸送、さらにその前後の積込、積出
の荷役作業において、石炭の微粒粉(通常0.5mm
程度)が風などにより飛散し発塵の問題を起こ
す。さらに、石炭は本来地表下に存在するので、
それを採炭すると空気中の酸素と反応し、発熱さ
らには自然発火することもしばしば観測されてい
る。この自然発火特性は炭種にも依存するが、空
気中での放置時間との関係もあつて、貯炭場、輸
送または荷役中に着火する場合もある。 上述のように石炭のバルク輸送には、さまざま
な取扱い上の問題が提示され、その解決策もいろ
いろ研究されている。その中で最も注目されてい
るのが石炭を流体状態で扱う高濃度スラリーであ
る。これは石炭を微粉砕し、少量の水を媒質とし
て流体化状態にするものであり、石油と同様のハ
ンドリングが可能である。この場合、最終用途、
たとえば火力発電所等の燃焼工程においては、脱
水工程を経ずに経済的に燃焼できるよう石炭の固
体濃度をできるだけ高めるのが望ましい。 石炭はその細部にまで広く分布する不燃焼分
(灰分)を多かれ、少なかれ含んでいる。したが
つて、上述の高濃度スラリーにおいては、石炭中
の灰分を減少しておくことは、ハンドリング、輸
送の経済性を高めるのみならず、燃焼のような最
終用途においてボイラー壁の摩耗を減少させ、ま
た、ボイラー効率を高めることにもなる。また、
灰分以外に石炭中の硫黄の含有率を低下できれ
ば、燃焼排ガス等におけるSOXの濃度が減少し極
めて有意義となる。 石炭の脱灰、脱硫黄工程には通常浮選機が用い
られるが、浮選においてはスラリー中の石炭濃度
を10〜25%にする必要がある。本来、浮選による
脱灰は物理的現象、つまり石炭と灰分の比重の相
違によるこれらの分離を基本原理としているの
で、石炭と灰分との衝突頻度を少なくして自由運
動できるのが望ましく、そのため、低濃度で処理
するのである。脱灰処理後得られるスラリーは固
体濃度が高くなつて(15〜30%)いるが、所望の
高濃度スラリーを得るためには脱水工程が必要と
なる。高濃度石炭−水スラリーの固体濃度は60%
以上が好ましいため、脱水工程から多量の水が排
出されることになる。 本発明は、この排出される多量の水および浮選
機テール(灰分は除去する)処理水を再循環し、
高濃度スラリー製造の経済性を高めることを目的
としたものである。 すなわち、本発明の高濃度石炭−水スラリーの
製造方法は微粒に粉砕された石炭を浮選機に導入
して石炭中に含有する灰分を一部除去し、ついで
一部脱灰された石炭を含むスラリーを脱水処理し
て高濃度石炭−水スラリーを製造する方法におい
て、前記脱水処理で脱水された水および/又は浮
選機テールから灰分を除去した水を前記浮選機に
循環することを特徴とする。 第1図に示したのは本発明の一実施態様であ
る。 粒度200メツシユ以下の微粒子を多量に含む石
炭スラリー5は固体濃度10〜25%で浮選機1に投
入され脱灰、脱硫黄処理をする。脱灰された石
炭、つまり精炭を含むスラリーは固体濃度15〜30
%であり、ライン6を経て浮選フロス用シツクナ
ー2に投入する。ここでスラリーは幾分濃縮さ
れ、ライン7を経てフイルターなどの脱水機3に
導かれ固体濃度60%以上の高濃度石炭−水スラリ
ー8が得られる。脱水工程、すなわちフロス用シ
ツクナー2および脱水機3で脱水された水は、そ
れぞれライン9および10から14を経て浮選機
1に再循環される。また、浮選機テールはライン
11を経て浮選機テール、シツクナー4に供給さ
れ、清澄液(灰分を除いた水)は溢流堰からライ
ン12,14を経て再循環される。灰分を含む排
泥13は処理工程に供給される。本発明はこのよ
うに脱水工程および浮選機テールから回収した水
の全量を循環してもよいし、またその一部を循環
してもよい。脱水あるいは浮選機テールからの灰
分の除去が第1図に示した手段に限られないこと
は勿論であり、たとえば、シツクナーによる精炭
の沈降性が良くないとき、あるいは脱水機の性能
が良く低濃度から一挙に高濃度化が可能な場合は
第1図においてシツクナー2を使用せず、浮選フ
ロスを直接脱水機3に導くこともできる。 第1表は浮選による脱灰特性を示すものであ
り、スラリー濃度が低いと、高い石炭回収率で灰
分の除去ができるのが判る。
The present invention relates to a method for producing a highly concentrated coal-water slurry in which coal is handled as a fluid fuel and can be directly fed into boilers and other furnaces for various purposes. Coal is a solid and is usually crushed into pieces of less than 2 inches and transported in bulk by railcars or other means.
However, during this transportation, loading and unloading operations before and after the transportation, fine coal powder (usually 0.5mm
) may be blown away by wind, etc., causing problems with dust generation. Furthermore, since coal originally exists below the earth's surface,
When coal is mined, it reacts with oxygen in the air, causing heat generation and even spontaneous combustion, which is often observed. This spontaneous ignition characteristic depends on the type of coal, but it is also related to the time it is left in the air, and may ignite during coal storage, transportation, or cargo handling. As mentioned above, bulk transportation of coal presents various handling problems, and various solutions are being researched. Among these, highly concentrated slurry, which handles coal in a fluid state, is attracting the most attention. This involves pulverizing coal into a fluid state using a small amount of water as a medium, and it can be handled in the same way as petroleum. In this case, the end use
For example, in the combustion process of thermal power plants, etc., it is desirable to increase the solid concentration of coal as much as possible so that it can be burned economically without going through a dehydration process. Coal contains more or less unburned matter (ash) that is widely distributed even in its fine details. Therefore, in the highly concentrated slurries mentioned above, reducing the ash content in the coal not only improves the economics of handling and transportation, but also reduces wear on the boiler walls in end uses such as combustion. , it also increases boiler efficiency. Also,
If it were possible to reduce the content of sulfur in coal in addition to ash, it would be extremely meaningful as it would reduce the concentration of SOx in combustion exhaust gas. A flotation machine is usually used for coal deashing and desulfurization processes, but flotation requires a coal concentration of 10 to 25% in the slurry. Originally, deashing by flotation is based on a physical phenomenon, that is, the separation of coal and ash due to the difference in specific gravity, so it is desirable to reduce the frequency of collisions between coal and ash and allow free movement. , treated at low concentrations. Although the slurry obtained after deashing has a high solids concentration (15-30%), a dehydration step is required to obtain the desired high concentration slurry. Solids concentration of highly concentrated coal-water slurry is 60%
Since the above is preferable, a large amount of water will be discharged from the dehydration process. The present invention recirculates this large amount of discharged water and flotation machine tail (ash content is removed) treated water,
The purpose is to improve the economic efficiency of producing highly concentrated slurry. That is, the method for producing a highly concentrated coal-water slurry of the present invention introduces finely pulverized coal into a flotation machine to remove part of the ash contained in the coal, and then removes the partially deashed coal. In the method of producing a highly concentrated coal-water slurry by dehydrating a slurry containing the same, the water dehydrated in the dehydration treatment and/or the water from which ash has been removed from the flotation machine tail is circulated to the flotation machine. Features. Illustrated in FIG. 1 is one embodiment of the present invention. Coal slurry 5 containing a large amount of fine particles with a particle size of 200 mesh or less is fed into a flotation machine 1 at a solid concentration of 10 to 25%, where it is deashed and desulfurized. Slurry containing deashed coal, i.e. clean coal, has a solids concentration of 15 to 30
%, and is fed into the flotation floss thickener 2 via line 6. Here, the slurry is somewhat concentrated and led to a dehydrator 3 such as a filter via a line 7 to obtain a highly concentrated coal-water slurry 8 with a solids concentration of 60% or more. The water dewatered in the dewatering process, ie the floss thickener 2 and the dehydrator 3, is recycled to the flotation machine 1 via lines 9 and 10 to 14, respectively. Further, the flotation machine tail is supplied to the flotation machine tail and the thickener 4 via line 11, and the clarified liquid (water from which ash has been removed) is recirculated from the overflow weir via lines 12 and 14. The waste sludge 13 containing ash is supplied to a treatment process. The present invention may circulate the entire amount of water thus recovered from the dewatering process and the flotation machine tail, or may circulate a portion thereof. Of course, dehydration or removal of ash from the tail of the flotation machine is not limited to the means shown in Figure 1. If it is possible to increase the concentration from a low concentration to a high concentration all at once, the thickener 2 in FIG. 1 can be omitted and the flotation froth can be led directly to the dehydrator 3. Table 1 shows the characteristics of deashing by flotation, and it can be seen that when the slurry concentration is low, ash can be removed with a high coal recovery rate.

【表】 本発明によれば灰分を一部除去して高濃度石炭
−水スラリーを製造するに際し、多量の水を回収
循環することにより、水さらには浮選試薬を有効
に利用できる。
[Table] According to the present invention, when producing a highly concentrated coal-water slurry by partially removing the ash content, by collecting and circulating a large amount of water, it is possible to effectively utilize the water and the flotation reagent.

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

第1図は本発明の一実施例についてのフロー図
である。 1……浮選機、2,4……シツクナー、3……
脱水機。
FIG. 1 is a flow diagram for one embodiment of the present invention. 1...flotation machine, 2, 4...stickner, 3...
Dehydrator.

Claims (1)

【特許請求の範囲】[Claims] 1 微細に粉砕された石炭を浮選機に導入して石
炭中に含有する灰分を一部除去し、ついで一部脱
灰された石炭を含むスラリーを脱水処理して高濃
度石炭−水スラリーを製造する方法において、前
記脱水処理で脱水された水および/又は浮選機テ
ールから灰分を除去した水を前記浮選機に循環す
ることを特徴とする高濃度石炭−水スラリーの製
造方法。
1 Finely crushed coal is introduced into a flotation machine to remove part of the ash contained in the coal, and then the slurry containing the partially deashed coal is dehydrated to form a highly concentrated coal-water slurry. A method for producing a highly concentrated coal-water slurry, characterized in that water dehydrated in the dehydration treatment and/or water from which ash has been removed from the tail of the flotation machine is circulated to the flotation machine.
JP17917381A 1981-11-09 1981-11-09 Production of highly concentrated coal/water slurry Granted JPS5880389A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17917381A JPS5880389A (en) 1981-11-09 1981-11-09 Production of highly concentrated coal/water slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17917381A JPS5880389A (en) 1981-11-09 1981-11-09 Production of highly concentrated coal/water slurry

Publications (2)

Publication Number Publication Date
JPS5880389A JPS5880389A (en) 1983-05-14
JPS6147195B2 true JPS6147195B2 (en) 1986-10-17

Family

ID=16061210

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17917381A Granted JPS5880389A (en) 1981-11-09 1981-11-09 Production of highly concentrated coal/water slurry

Country Status (1)

Country Link
JP (1) JPS5880389A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU5717786A (en) * 1985-05-10 1986-11-13 Babcock & Wilcox Co., The Coal-water fuel
JPS62169891A (en) * 1986-01-21 1987-07-27 Sumitomo Heavy Ind Ltd Production of highly concentrated coal slurry

Also Published As

Publication number Publication date
JPS5880389A (en) 1983-05-14

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