JPS61283691A - Production of high-concentration coal-water slurry in short time - Google Patents

Production of high-concentration coal-water slurry in short time

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Publication number
JPS61283691A
JPS61283691A JP12545585A JP12545585A JPS61283691A JP S61283691 A JPS61283691 A JP S61283691A JP 12545585 A JP12545585 A JP 12545585A JP 12545585 A JP12545585 A JP 12545585A JP S61283691 A JPS61283691 A JP S61283691A
Authority
JP
Japan
Prior art keywords
water
coal
mixture
pulverized coal
dispersant
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
JP12545585A
Other languages
Japanese (ja)
Inventor
Isao Sekiguchi
勲 関口
Jintaro Suzuki
鈴木 仁太郎
Hironori Ozaki
尾崎 弘憲
Ken Yamaguchi
憲 山口
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP12545585A priority Critical patent/JPS61283691A/en
Publication of JPS61283691A publication Critical patent/JPS61283691A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain the title slurry in a short time using a simple device, by consolidating a specific mixture comprising a pulverized coal, water and a dispersant and applying a shear force to the consolidated mixture in a saturated state of water, to thereby liquefy the mixture. CONSTITUTION:A coal 1 is pulverized with a vertical roller mill 2 etc. while blowing a heated air which has been produced in an air heater 4 into the mill. The pulverized coal 3 is transferred to a mixing step 6 where the pulverized coal is mixed with water 7 of which the pH value has been adjusted, a dispersant 9 comprising a surfactant and optionally a stabilizer 13 such as CMC so as to have a coal content of 60wt% or higher, and the pulverized coal which is in a sufficiently dispersed state and water are formed into a mixture 10 which is in a packing state of a funicular region. A pressure is applied to the mixture from the outside to consolidate the mixture 11. When the degree of saturation of water approaches saturation point, a shearing force is applied to the end of the consolidation product to instantaneously liquefy the consolidation product, thereby obtaining the title slurry 12.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、高濃度石炭水スラリーの高速製造方法に関す
る。詳しくは乾式法により高濃度石炭水スラリーを高速
にて製造する方法である。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a high-speed method for producing highly concentrated coal-water slurry. Specifically, it is a method for producing high-concentration coal-water slurry at high speed using a dry method.

〔従来の技術〕[Conventional technology]

高濃度石炭水スラリーは、固体燃料である石炭を流体化
することにより、その輸送、貯蔵のみならず直接燃焼の
ために利用することができる。さらに灰分および硫黄分
を低減できるために有効な燃料である。
High-concentration coal-water slurry can be used not only for transportation and storage but also for direct combustion by fluidizing coal, which is a solid fuel. Furthermore, it is an effective fuel because it can reduce ash and sulfur content.

高濃度石炭水スラリーを製造する方法としては、湿式法
および乾式法などがある。
Methods for producing high-concentration coal-water slurry include wet methods and dry methods.

湿式法の場合には、ボールミルなどを用い、破砕された
石炭と水および界面活性剤からなる分散剤を供給して湿
式粉砕を行い、石炭濃度が約60重量%以上の高濃度石
炭水スラリーを製造する。
In the case of the wet method, wet pulverization is performed using a ball mill or the like by supplying crushed coal, a dispersant consisting of water and a surfactant, and a highly concentrated coal-water slurry with a coal concentration of about 60% by weight or more is produced. Manufacture.

このさい、必要に応じて安定化剤が附加的に添加される
At this time, a stabilizer is additionally added as required.

乾式法の場合には、従来は竪型ローラミルなどを用い、
破砕された石炭を微粉砕して微粉炭となし、微粉炭と水
および界面活性剤からなる分散剤を撹拌混合して石炭濃
度が約60重量%以上の高濃度石炭水スラリーを製造し
ていた。撹拌混合操作のために通常連続式混合装置など
が用いられるが、微粉炭と水とが充分に混合しかつスラ
リー状をしめすためには撹拌混合を繰返す回分式の多段
操作が行われ、比較的長い操作時間を必要としていた。
In the case of the dry method, conventionally a vertical roller mill etc. was used.
Crushed coal was pulverized into pulverized coal, and a highly concentrated coal-water slurry with a coal concentration of about 60% by weight or more was produced by stirring and mixing the pulverized coal with a dispersant consisting of water and a surfactant. . Continuous mixing equipment is usually used for the stirring and mixing operation, but in order to sufficiently mix the pulverized coal and water and form a slurry, a batch-type multi-stage operation that repeats stirring and mixing is performed, which is relatively slow. It required long operation time.

(例えば、E、す、 Knellら、MODERN p
OWEFLSYSTEMS、 September 1
984.pp63〜65参照)なお、水はpH調整剤に
より適当なPH調整が行われている。
(e.g., E. Knell et al., MODERN p.
OWEFLSYSTEMS, September 1
984. (See pp. 63-65) Note that the pH of the water is appropriately adjusted using a pH adjuster.

また、必要に応じて安定化剤が附加的に添加されること
は、湿式法の場合と同一である。
Further, as in the case of the wet method, a stabilizer may be additionally added as necessary.

〔発明が解決しようとする問題点3 以上述べた従来の方法では、微粉炭と水との撹拌混合の
ために長い操作時間を必要とし、さらに撹拌混合の過程
において造塊現象の発生、消費エネルギーの増大、混合
物の移動速度の不均一が発生するばかりでなく、さらに
、撹拌混合における微粉炭と水と分散剤との作用として
は、すでに微粉砕された微粉炭界面との相互作用に限定
されてしまうので、石炭粒子の粉砕による新生界面と分
散剤やpH調整剤との親和作用が充分でなく低粘度高濃
度石炭水スラリーを製造するにさいしての分散剤をはじ
めとする薬剤の効果の有効性を発揮しえないという問題
があった。
[Problem to be solved by the invention 3 The conventional method described above requires a long operation time to stir and mix the pulverized coal and water, and also causes agglomeration phenomenon and energy consumption in the stirring and mixing process. Not only does this cause an increase in the movement speed of the mixture, but also the interaction between the pulverized coal, water, and dispersant during stirring and mixing is limited to the interaction with the interface of the pulverized coal that has already been pulverized. As a result, the affinity between the new interface created by the pulverization of coal particles and the dispersant and pH adjuster is not sufficient, and the effectiveness of the dispersant and other chemicals when producing a low-viscosity, high-concentration coal-water slurry is reduced. There was a problem that it could not be effective.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は低粘度にして流動性が良好な高濃度石炭水スラ
リーを高速に製造するために、微粉炭と水と分散剤から
なり、必要に応じ安定化剤を添加してなる索状域の充て
んをなす混合物を圧密化し、これをほゞ水の飽和状態の
もとでせん断力により液状化することを特徴とするもの
である。
In order to rapidly produce a highly concentrated coal-water slurry with low viscosity and good fluidity, the present invention has developed a cord-like region consisting of pulverized coal, water, and a dispersant, with a stabilizer added as necessary. It is characterized by compacting the filling mixture and liquefying it by shearing force under substantially water-saturated conditions.

〔作 用〕[For production]

本発明においては、はじめに微粉炭と水と分散剤からな
り必要に応じ安定化剤を添加して索状域の充てんをなす
混合物とする。
In the present invention, a mixture is first made of pulverized coal, water, and a dispersant, and a stabilizer is added as necessary to form a mixture that fills the cord-like region.

微粉炭の充てん構造としては微粉炭粒子、水および空気
が連続して充てんしているかあるいは空気のみが不連続
に充てんしている索状域にあり、通俗的な表現を行うと
パサパサしている。この充てん構造にある混合物に圧力
を加えて圧密化するとその体積が減少して空気の放出が
行われる。かくして水の飽和度が増大して100%に近
付きはマ飽和状態に達したさいに、圧密層の端部にせん
断力を作用させることによって瞬間的に液状化を行い高
濃度石炭水スラリーを得るものである。
The filling structure of pulverized coal is either a continuous filling of pulverized coal particles, water, and air, or a cord-like region filled with only air discontinuously. . When pressure is applied to the mixture in this filling structure to compact it, its volume decreases and air is released. In this way, the water saturation increases and approaches 100%, and when the water saturation is reached, a shear force is applied to the end of the consolidation layer to instantaneously liquefy it and obtain a highly concentrated coal-water slurry. It is something.

このさい、微粉炭は摩擦力をうけて微細化が行われ、こ
れに伴い微粉炭の新生界面が生成されて、水や分散剤、
安定化剤との親和作用が促進せしめられる。さらに摩擦
力をうけることによりぜん断面において温度上昇がみら
れ、高濃度石炭水スラリーの粘度が低減せしめられる。
At this time, the pulverized coal is subjected to frictional force and becomes finer, and a new interface of the pulverized coal is generated, and water, dispersant, etc.
The affinity with the stabilizer is promoted. Furthermore, due to the frictional force, a temperature rise is observed at the fracture surface, and the viscosity of the highly concentrated coal-water slurry is reduced.

〔実施例〕〔Example〕

以下、本発明の一実施例を図面について詳述する。 Hereinafter, one embodiment of the present invention will be described in detail with reference to the drawings.

第1図は本発明の一実施例をしめず工程図である。FIG. 1 is a process diagram showing one embodiment of the present invention.

石炭1は竪型ローラミル2などにより微粉砕されて微粉
炭3が得られる。空気加熱器4においては微粉砕に必要
な加熱空気5を発生している。混合工程6においては、
微粉炭3.PH調整を行った水7および分散剤9をそれ
ぞれ供給して混合し、混合物10の石炭比率が60重量
%以上となるように配合する。
Coal 1 is pulverized by a vertical roller mill 2 or the like to obtain pulverized coal 3. The air heater 4 generates heated air 5 necessary for pulverization. In the mixing step 6,
Pulverized coal 3. PH-adjusted water 7 and dispersant 9 are respectively supplied and mixed so that the coal ratio of mixture 10 is 60% by weight or more.

分散剤9は界面活性剤からなり、微粉炭表面に吸着して
作用し、充分なポテンシャルエネルギーにより微粉炭相
互に凝集体を生ずることなく、充分に分散した微粉炭粒
子と水との充てん状態を得るために用いる。上記の充て
ん構造は索状域として存在している。
The dispersant 9 is made of a surfactant and acts by adsorbing on the surface of the pulverized coal, and with sufficient potential energy, it maintains a filling state of sufficiently dispersed pulverized coal particles and water without forming aggregates among the pulverized coal. used to obtain The above-mentioned filling structure exists as a funicular region.

また、必要に応じて安定化剤13を配合しているがキサ
ントンガムなどの天然の多糖類やCMC(Sodium
 Carboxymethyl (1:ellulos
a)などを用い、高分子分子鎖の相互作用により高濃度
石炭水スラリーにおいて弱い凝集体を形成させ、性状の
安定化をはかっている。
In addition, stabilizers 13 are blended as needed, but natural polysaccharides such as xanthone gum and CMC (sodium
Carboxymethyl (1: ellulos
a) etc. are used to form weak aggregates in a highly concentrated coal-water slurry through the interaction of polymer chains, thereby stabilizing the properties.

さらに、混合物10は圧密液状化工程11において、混
合物10に外部より圧力を加えて圧密化し、水の飽和度
がはマ飽和状態に達したさいに、水の湧出のもとで圧密
体の端部にせん断力を作用させることによって瞬間的に
液状化を行い、高濃度石炭水スラリー12を得ることが
できる。
Further, the mixture 10 is consolidated in a consolidation liquefaction step 11 by applying pressure from the outside to the mixture 10, and when the degree of water saturation reaches a saturated state, the end of the consolidated body is formed under water gushing out. By applying a shearing force to the portion, liquefaction is instantaneously performed, and a high concentration coal water slurry 12 can be obtained.

実施例にもちいた石炭の分析結果は下記のとうりであっ
た。
The analysis results of the coal used in the examples were as follows.

HGI50(−) また、微粉炭の粒度分析(マイクロトラック法による)
結果は、下記のとうりであった。
HGI50(-) Also, particle size analysis of pulverized coal (by Microtrack method)
The results were as follows.

106          95゜1 7580゜2 53          70.1 38          51.3 27          38.4 19          29.0 13          17.8 9.4         13.2 6・68.2 4.7         6.0 3.3         4.3 2.4         3.0 配合は、微粉炭70重量%、Ca(OH)、によりpH
=9に調整した水29.4重量%、アニオン系界面活性
剤よりなる分散剤006重量%の割合とし、撹拌混合に
よって得られた湿潤微粉炭からなる混合物を358Kg
/aJの圧縮力のもとで圧密化し、かさ密度(湿潤基準
) 1.01g/aJの圧密層を形成し、さらに圧密層
端部の自由表面に平均周速5m/sのもとて回転円板に
よりせん断力を作用させ粘度750CPをしめず充分な
流動性を有する高濃度石炭水スラリーを得た。
106 95゜1 7580゜2 53 70.1 38 51.3 27 38.4 19 29.0 13 17.8 9.4 13.2 6・68.2 4.7 6.0 3.3 4.3 2.4 3.0 The formulation consists of 70% by weight of pulverized coal, Ca(OH), and pH
358 kg of a mixture consisting of wet pulverized coal obtained by stirring and mixing with a ratio of 29.4% by weight of water adjusted to 9.0% by weight and 0.06% by weight of a dispersant made of an anionic surfactant.
Consolidation was performed under a compressive force of /aJ to form a consolidated layer with a bulk density (wet basis) of 1.01 g/aJ, and the free surface at the end of the consolidated layer was further rotated at an average circumferential speed of 5 m/s. A high concentration coal-water slurry having sufficient fluidity without reducing the viscosity to 750 CP was obtained by applying shearing force using a disk.

このさい圧密層の軸方向速度は約0.5am/Secで
、圧密層の表面温度は約47℃であり、かぎる過程のも
とで高速せん新作用を促進させている。
At this time, the axial velocity of the compacted layer is about 0.5 am/Sec, and the surface temperature of the compacted layer is about 47° C., promoting high-speed shearing action under these processes.

高濃度石炭水スラリーの石炭粒子の粒度分布は下記のと
うりであって、微粉炭に比して微細化が行われていた。
The particle size distribution of the coal particles in the high-concentration coal-water slurry was as shown below, and was finer than that of pulverized coal.

粒 径 μm    フルイ下 百分率%150   
       99.8 106          95.2 75          82.3 53          72.3 38          56.0 27          45.9 19          33.4 13          24.0 9・4         18.2 6.6         12.0 4.7         8.2 3.3         6,3 2.4         4.3 〔発明の効果〕 本発明によれば、*粉炭と水を主体とする索状域の充て
んをなす混合物を圧密化してせん断力により液状化する
ことにより、微粉炭粒子の微細化と圧密層の表面温度の
上昇がみられ、水や分散剤。
Particle size μm Under sieve Percentage% 150
99.8 106 95.2 75 82.3 53 72.3 38 56.0 27 45.9 19 33.4 13 24.0 9.4 18.2 6.6 12.0 4.7 8.2 3 .3 6, 3 2.4 4.3 [Effects of the Invention] According to the present invention, *by compacting the mixture that fills the cord-like region, mainly consisting of powdered coal and water, and liquefying it by shearing force. , the refinement of pulverized coal particles and the increase in the surface temperature of the consolidated layer were observed, as well as water and dispersant.

安定化剤などとの親和作用を促進させて、低粘度にして
流動性が良好な石炭濃度が約60重量%以上の高濃度石
炭水スラリーを高速にて製造することができ、従来の方
法に比して操作時間を短縮しろるので、装置の著しい簡
素化が可能である。
By promoting affinity with stabilizers, etc., it is possible to rapidly produce a highly concentrated coal-water slurry with a coal concentration of about 60% by weight or more, which has low viscosity and good fluidity, and is much easier to use than conventional methods. Since the operating time can be shortened in comparison, the device can be significantly simplified.

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

第1図は本発明の一実施例に係る工程図である。 3・・・微粉炭    7・・・水 9・・・分散剤    10・・・混合物12・・・高
濃度石炭水スラリー 手続補正書(カベ2 1.事件の表示 3、 補正をする者 事件との関係        特許出願人代表者  長
谷用  謙 浩・
FIG. 1 is a process diagram according to an embodiment of the present invention. 3...Pulverized coal 7...Water 9...Dispersant 10...Mixture 12...Highly concentrated coal-water slurry procedure amendment (wall 2) 1. Display of case 3, Amendment person case and Relationship between patent applicant representative Hiroshi Haseyo

Claims (1)

【特許請求の範囲】[Claims] 微粉炭と水と分散剤からなり、必要に応じ安定化剤を添
加してなる索状域の充てんをなす混合物を圧密化し、こ
れをほゞ水の飽和状態のもとでせん断力により液状化す
ることを特徴とする高濃度石炭水スラリーの高速製造方
法。
A mixture consisting of pulverized coal, water, and a dispersant, with a stabilizer added if necessary, that fills the cord-like region is compacted, and this is liquefied by shearing force under nearly water-saturated conditions. A high-speed production method for highly concentrated coal-water slurry.
JP12545585A 1985-06-10 1985-06-10 Production of high-concentration coal-water slurry in short time Pending JPS61283691A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12545585A JPS61283691A (en) 1985-06-10 1985-06-10 Production of high-concentration coal-water slurry in short time

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12545585A JPS61283691A (en) 1985-06-10 1985-06-10 Production of high-concentration coal-water slurry in short time

Publications (1)

Publication Number Publication Date
JPS61283691A true JPS61283691A (en) 1986-12-13

Family

ID=14910519

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12545585A Pending JPS61283691A (en) 1985-06-10 1985-06-10 Production of high-concentration coal-water slurry in short time

Country Status (1)

Country Link
JP (1) JPS61283691A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02158688A (en) * 1988-12-12 1990-06-19 Mitsubishi Heavy Ind Ltd Production of concentrated coal-water slurry

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02158688A (en) * 1988-12-12 1990-06-19 Mitsubishi Heavy Ind Ltd Production of concentrated coal-water slurry

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