JPS596701B2 - Method for producing fine powder material from slurry - Google Patents

Method for producing fine powder material from slurry

Info

Publication number
JPS596701B2
JPS596701B2 JP51010460A JP1046076A JPS596701B2 JP S596701 B2 JPS596701 B2 JP S596701B2 JP 51010460 A JP51010460 A JP 51010460A JP 1046076 A JP1046076 A JP 1046076A JP S596701 B2 JPS596701 B2 JP S596701B2
Authority
JP
Japan
Prior art keywords
slurry
conduit
coal
grinding
pulverized
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
JP51010460A
Other languages
Japanese (ja)
Other versions
JPS51105668A (en
Inventor
エドウイン・チヤールズ・マツケンジイ
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.)
BABUKOTSUKU INTERN Ltd
Original Assignee
BABUKOTSUKU INTERN 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 BABUKOTSUKU INTERN Ltd filed Critical BABUKOTSUKU INTERN Ltd
Publication of JPS51105668A publication Critical patent/JPS51105668A/ja
Publication of JPS596701B2 publication Critical patent/JPS596701B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/02Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/10Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour carrying the materials or objects to be dried with it
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C15/00Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
    • B02C15/12Mills with at least two discs or rings and interposed balls or rollers mounted like ball or roller bearings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/30Conveying materials in bulk through pipes or tubes by liquid pressure

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Food Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • General Engineering & Computer Science (AREA)
  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)
  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】 この発明はスラリーから微粉材料を製造することに関す
る。
DETAILED DESCRIPTION OF THE INVENTION This invention relates to producing fine powder materials from slurries.

石炭燃焼火力発電所が炭鉱から離れた処に設置されてい
るような場合、水圧パイプラインで炭鉱から発電所まで
石炭をスラリーとして経済的に運ぷことができる。
When a coal-fired power plant is located far from a coal mine, hydraulic pipelines can economically transport the coal as a slurry from the mine to the power plant.

この発明はパイプラインでスラリーの形で運ばれた石炭
を火力発電所で燃焼させうる装置の検討から生じたもの
である。この発明においては、スラリーは加熱区域では
熱的に遮断されている導管を通じ加熱区域に排出され、
かつ乾燥の行なわれる加熱区域に位置するグラインダ(
微粉化装置)に供給することによりスラリーから微粉材
料を得る方法が提案されるものである。
The invention arose from the study of an apparatus by which coal transported in the form of a slurry by pipeline could be burned in a thermal power plant. In this invention, the slurry is discharged into the heating zone through a conduit that is thermally isolated in the heating zone;
and a grinder (
A method is proposed for obtaining a fine powder material from a slurry by supplying the slurry to a micronization device.

またこの発明は、複数個のグラインディングポールの組
は、一連となつた複数個のボールにより環状体を形成し
、かつ固定の上部グラインディングレースと回転する下
部グラインディングレースとの間に位置して各ボールは
回転しながら上部レースと下部レースに挾まれてレース
の溝部を移動し、スラリーに含まれる石炭粗粒を微粉と
し、スラリーの乾燥は前記ボールを含む加熱区域で行な
われ、スラリーは加熱区域内に位置し熱的に遮断された
導管の出口たる排出ノズルから前記環状体(リング)内
に位置するグラインディングボールに向けて排出される
というスラリーから微粉材料を製造する方法を提案する
ものである。
Further, in the present invention, the plurality of grinding pole sets form an annular body with a plurality of series of balls, and are located between a fixed upper grinding race and a rotating lower grinding race. While rotating, each ball is sandwiched between the upper race and the lower race and moves through the grooves of the race to pulverize the coarse coal particles contained in the slurry, and the slurry is dried in the heating area containing the balls. A method is proposed for producing a pulverulent material from a slurry which is discharged from a discharge nozzle, which is the outlet of a thermally isolated conduit located in a heating zone, towards a grinding ball located in said ring. It is something.

この方法の変形としては、微粉化はグラインディングリ
ング上で回転するロールでなされてもよく、またそのロ
ールは軸上で回転するものでもよく上下レース間で回転
するものであつてもよい。またこの発明においては、加
熱区域をもつグラインディングミル(微粉化装置)装置
が提案されている。
In a variation of this method, the atomization may be done with rolls rotating on a grinding ring, and the rolls may rotate on an axis or between upper and lower races. The present invention also proposes a grinding mill device having a heating section.

このグラインディングミル装置内には、グラインディン
グ装置が設けられ、かつグラインディング装置内で処理
される材料をその装置に供給する入口導管が設けられ、
またその導管はスラリー供給源から加熱区域まで伸びる
もので、前記加熱区域においては前記導管は熱的に遮断
されるものである。この発明の一実施例を示すと、複数
個のクラインディングポール1a(以下単にボールと称
す)の組よりなる環状体1は固定上部クラインディング
レース2と回転下部レース3との間に位置する。
A grinding device is provided within the grinding mill device and an inlet conduit is provided for supplying the material to be processed within the grinding device;
The conduit also extends from the slurry source to the heating zone, where the conduit is thermally isolated. In one embodiment of the present invention, an annular body 1 consisting of a set of a plurality of climbing poles 1a (hereinafter simply referred to as balls) is located between a fixed upper climbing race 2 and a rotating lower race 3.

導管4の垂直部4aは前記クラインディングポールの環
状体1の回転軸心方向に伸び、またその下端からは一の
ノズル部を形成することになる一の枝導管4bがボール
1aの中心を含む平面5内で前記ボールの環状体1の内
側ぎりぎりに近い処まで、換言すればボール外面に近く
枝導管4(ノズル部)の端部を展出させて近接位置させ
る。前記導管4の垂直部4aと枝導管4bは熱的に遮断
され、その垂直部4aの上端は粘性をもつ石炭スラリー
の供給源に接続している。前記装置の稼動時においては
ボール1aを回転させるために下部レース3は回転する
The vertical portion 4a of the conduit 4 extends in the direction of the rotation axis of the annular body 1 of the climbing pole, and from its lower end, a branch conduit 4b forming one nozzle portion includes the center of the ball 1a. The end of the branch conduit 4 (nozzle part) is extended and positioned close to the inside of the annular body 1 of the ball within the plane 5, in other words close to the outer surface of the ball. The vertical portion 4a of the conduit 4 and the branch conduit 4b are thermally isolated, and the upper end of the vertical portion 4a is connected to a source of viscous coal slurry. When the device is in operation, the lower race 3 rotates in order to rotate the ball 1a.

スラリーは導管4からボール1aに向けて排出され、そ
のボールの外面にまつわり通過しながら微粉化される。
これらボール1aはスラリーにおける石炭/水比率が濃
厚ペーストを形成するような値を有する状態にあつても
充分にスラリーをすくい取るものである。熱風はボール
1aの外側から入り環状体のボール間を通過し、方向を
変換して前記した装置の上方へと向い、かつ導管4の垂
直部4aのまわりをまわりながら出口6に向つて微粉化
した石炭を随伴して上方へと進むものである。この微粉
炭随伴空気はこの装置の粉砕部材の作動により発生する
熱で更に加熱され、かつこの粉砕工程は、バーナーに直
接に前記微粉炭随伴空気を供給しうる状態がえられるま
でスラリーの乾燥作業を伴うものである。スラリーが排
出される区域は加熱されており、また加熱区域内にある
導管はスラリーが導管内で乾燥しスラリー流れを阻害す
ることのないように断熱処置がされるものである。前述
した装置を使用することにより石炭は遠隔の地域たる炭
鉱からスラリーとして直接火力発電所に運ばれ、そこで
燃焼に適した最終微粉粒度にまで粉砕微粉化乾燥するこ
とができ、また脱水装置の設置及び運転の費用を必要と
することなく、これに加えてスラリー乾燥により生ずる
水蒸気は燃焼用として使用される加熱された一次空気と
ともにバーナに供給され微粉炭搬送に際しての爆発防止
の安全性を高め、更には燃焼ガス温度を下げかつ不活性
ガスとしても働きNOx(窒素酸化物)の発生を抑制し
てスラリーの燃焼を行うことができる。
The slurry is discharged from the conduit 4 towards the ball 1a and is pulverized as it passes around the outer surface of the ball.
These balls 1a sufficiently scoop out the slurry even when the coal/water ratio in the slurry is such that a thick paste is formed. The hot air enters from the outside of the ball 1a, passes between the balls of the annular body, changes direction and heads upwards of the above-mentioned device, and then goes around the vertical part 4a of the conduit 4 toward the outlet 6 where it is pulverized. It moves upwards, accompanied by coal. This pulverized coal entrained air is further heated by the heat generated by the operation of the crushing member of this device, and this pulverization process is continued until the drying of the slurry is achieved until a condition is established in which the pulverized coal entrained air can be directly supplied to the burner. It is accompanied by The area from which the slurry is discharged is heated and the conduits within the heated area are insulated to prevent the slurry from drying within the conduits and interfering with slurry flow. By using the above-mentioned equipment, coal can be transported directly from a coal mine in a remote area as a slurry to a thermal power plant, where it can be crushed, pulverized and dried to a final fine particle size suitable for combustion, and a dewatering device can be installed. In addition, the water vapor produced by slurry drying is supplied to the burner together with the heated primary air used for combustion, increasing the safety of preventing explosions when transporting pulverized coal. Furthermore, it lowers the combustion gas temperature and also acts as an inert gas, suppressing the generation of NOx (nitrogen oxides), allowing the slurry to be combusted.

前記の一実施例にかかる装置の構造を添附図面に示す。The structure of the device according to the above embodiment is shown in the attached drawings.

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

第1図はこの発明の実施に使用する装置の縦断面図であ
る。 1・・・・・・クラインディングポールの組よりなる環
状体、1a・・・・・・クラインディングポール、2・
・・・・・固定上部クラインディングレース、3・・・
・・・回転下部レース、4・・・・・・導管、4a・・
・・・・導管の垂直部、4b・・・・・・枝導管(ノズ
ル部)、5・・・・・・ボールの中心を含む平面、6・
・・・・・出口、7・・・・・・荷重シリンダー、8・
・・・・・スパイダガイド、9・・・・・・スロートプ
レート、10・・・・・・シールエア接続部、11・・
・・・・電動機、12・・・・・・(減速)歯車箱、1
3・・・・・・廃棄物シユート、14・・・・・・ラビ
リンスシール、15・・・・・・規定粒度超過炭の戻リ
ンエート、16・・・・・・調整分級ブレード、17・
・・・・・断熱材、18・・・・・・スラリポンプ。
FIG. 1 is a longitudinal cross-sectional view of an apparatus used to carry out the invention. 1...An annular body consisting of a set of climbing poles, 1a...Clinding poles, 2.
...Fixed upper clinding lace, 3...
... Rotating lower race, 4... Conduit, 4a...
...Vertical part of the conduit, 4b... Branch pipe (nozzle part), 5... Plane containing the center of the ball, 6.
...Outlet, 7...Load cylinder, 8.
... Spider guide, 9 ... Throat plate, 10 ... Seal air connection part, 11 ...
...Electric motor, 12 ... (reduction) gear box, 1
3...Waste chute, 14...Labyrinth seal, 15...Return phosphorate for coal exceeding specified particle size, 16...Adjustment classification blade, 17.
...Insulation material, 18...Slurry pump.

Claims (1)

【特許請求の範囲】[Claims] 1 環状に位置する複数個のグラインディングボールの
組である環状体を固定上部グラインディングレースと回
転下部レースとの間に位置させ石炭を微粉化する方法に
おいて、遠隔の送出地域より石炭スラリーを微粉化する
装置内の導管に供給し、この装置の加熱区域内に位置す
る導管部分は断熱構造とし、該導管終末部分をノズル部
とし、その軸心をグラインディングボールの中心を含む
面内に位置させ、かつこのノズル部の端部を排出するス
ラリーがグラインディングボール面に巻き付き可能に近
接して位置させ、スラリーの輸送と微粉化と乾燥をして
送出地域からバーナに直接微粉炭を供給することを特徴
とするスラリーから微粉材料を製造する方法。
1. A method of pulverizing coal by placing an annular body, which is a set of a plurality of grinding balls arranged in a ring, between a fixed upper grinding race and a rotating lower race, in which coal slurry is pulverized from a remote delivery area. The conduit section that supplies the conduit in the equipment to be heated and is located in the heating area of this equipment has an insulated structure, and the end part of the conduit is used as the nozzle part, and its axis is located within the plane containing the center of the grinding ball. and the end of this nozzle part is located close to the surface of the grinding ball so that the slurry to be discharged can be wrapped around the surface of the grinding ball, and the slurry is transported, pulverized, and dried to supply pulverized coal directly from the delivery area to the burner. A method for producing a fine powder material from a slurry, characterized in that:
JP51010460A 1975-02-07 1976-02-04 Method for producing fine powder material from slurry Expired JPS596701B2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB5422/75A GB1483012A (en) 1975-02-07 1975-02-07 Slurry treatment apparatus

Publications (2)

Publication Number Publication Date
JPS51105668A JPS51105668A (en) 1976-09-18
JPS596701B2 true JPS596701B2 (en) 1984-02-14

Family

ID=9795893

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51010460A Expired JPS596701B2 (en) 1975-02-07 1976-02-04 Method for producing fine powder material from slurry

Country Status (6)

Country Link
JP (1) JPS596701B2 (en)
AU (1) AU497912B2 (en)
FR (1) FR2299912A1 (en)
GB (1) GB1483012A (en)
IN (1) IN144642B (en)
ZA (1) ZA76672B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2479159A1 (en) * 1980-03-28 1981-10-02 Eyer Charles Fluidiser for lifting gravel - has pump with discharge in gravel hopper and venturi to suck return water to tank
DE9406144U1 (en) * 1994-04-13 1995-08-10 Claudius Peters Ag, 21614 Buxtehude Ball ring mill
CN106733088A (en) * 2016-12-26 2017-05-31 郑州游爱网络技术有限公司 A kind of crushed stalk drying device
CN110882817B (en) * 2019-12-23 2021-12-21 山西晋武能源有限公司 Coal milling equipment for gasifier

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB901228A (en) * 1959-06-05 1962-07-18 Harvey Fabrication Limited Improvements in pulverising mills

Also Published As

Publication number Publication date
AU1089776A (en) 1977-08-11
AU497912B2 (en) 1979-01-18
GB1483012A (en) 1977-08-17
ZA76672B (en) 1977-01-26
JPS51105668A (en) 1976-09-18
FR2299912A1 (en) 1976-09-03
IN144642B (en) 1978-05-27

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