JPS6128588A - Production of coal/water slurry - Google Patents
Production of coal/water slurryInfo
- Publication number
- JPS6128588A JPS6128588A JP15073084A JP15073084A JPS6128588A JP S6128588 A JPS6128588 A JP S6128588A JP 15073084 A JP15073084 A JP 15073084A JP 15073084 A JP15073084 A JP 15073084A JP S6128588 A JPS6128588 A JP S6128588A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- ball mill
- water slurry
- viscosity
- water
- 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
Abstract
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は石炭水スラリーの製造方法の改良に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to improvements in a method for producing coal water slurry.
(従来の技術)
近年1石炭の微粉末と水、更に界面活性剤等の添加剤と
を混合する石炭水スラリーが石油に代る燃料として開発
さねている。(Prior Art) In recent years, coal-water slurry, which is a mixture of fine coal powder, water, and additives such as surfactants, has been developed as a fuel to replace petroleum.
石炭水スラリーはそのま\貯蔵あるいは輸送され、液体
燃料と同様に取扱うことができる利点はあるが9反面輸
送及び燃焼のための噴霧に最も重要な性状である粘度及
び微粉末粒度が一定のものを得るだめの製造条件の固定
がなかなか難かしい。これは9石炭水スラリーとしては
出来るだけ石炭が高濃度でしかも微粉(200メソシュ
80%以上)の方がよく更には低粘度(2000cp以
下)であることが望まれるためである。Coal-water slurry has the advantage of being stored or transported as is and can be handled in the same way as liquid fuel.9 On the other hand, it has constant viscosity and fine powder particle size, which are the most important properties for transportation and atomization for combustion. It is quite difficult to fix the manufacturing conditions to obtain the desired results. This is because it is desired that the 9-coal-water slurry has as high a concentration of coal as possible, and that it is finely powdered (80% or more of 200 Mesosh) and furthermore, that it has a low viscosity (2000 cp or less).
粘度の増加に影響する因子としては一石炭濃度、添加剤
である界面活性剤の種類とその量。Factors that affect the increase in viscosity include coal concentration, type and amount of additive surfactant.
石炭の粒度と粒径分布9石炭の種類(銘柄)等が主とし
てあげられる。ここで石炭水スラリーめ粘度増加の現象
を表わすために、第2図に湿式ミルによる粉砕時間と石
炭水スラリーの粘度との関係の実験例を、また第8図に
は粉砕時間と石炭水スラリーの粒度との関係の実験例を
示す。Coal particle size and particle size distribution 9 Coal type (brand) etc. are mainly mentioned. In order to express the phenomenon of viscosity increase in coal water slurry, Fig. 2 shows an experimental example of the relationship between grinding time in a wet mill and viscosity of coal water slurry, and Fig. 8 shows an example of the relationship between grinding time and viscosity of coal water slurry. An experimental example of the relationship between particle size and grain size is shown.
これらの実験例から明らかなように、粉砕時間が不足す
ると粘度が小さいが粗粒の石炭水スラリーとなり、−刃
長すぎると粒度が小さいものの粘度が高い石炭水スラリ
ーとなるため、従来法では石炭の粒度が小さくてかつ粘
度の小さいしかも一定した性状を有する石炭水スラリー
を製造することが困難であった。As is clear from these experimental examples, if the grinding time is insufficient, the resulting coal-water slurry will have a low viscosity but coarse grains, and if the blade is too long, the resulting coal-water slurry will have a small particle size but a high viscosity. It has been difficult to produce a coal-water slurry that has a small particle size, low viscosity, and consistent properties.
(発明が解決しようとする問題点)
本発明は上述の石炭水スラリーの特質を考慮し、常に一
定のスラリー性状を有する石炭水スラリーが得らね、か
つその製造装置の制御が容易な石炭水スラリーの製造方
法を提案することを目的としたものである。(Problems to be Solved by the Invention) The present invention takes into account the above-mentioned characteristics of the coal-water slurry, and provides a coal-water slurry that does not always have constant slurry properties and that is easy to control the production equipment. The purpose of this study is to propose a method for producing slurry.
(問題点を解決するための手段)
本発明は石炭と水と添加剤(通常は界面活性剤2重量%
以下)とからなる常に一定のスラリー性状を有する石炭
水スラリーを湿式ボールミルにより製造するために、湿
式ボールミルへの石炭、水及び添加剤の供給量を制御す
るだけでなく、湿式ホ:−ルミルの出口から排出される
石炭水スラリーの粘度を計測し、その計測信号により、
湿式ボールミルの回転数を変化させることを特徴とする
石炭水スラリーの製造方法である。(Means for solving the problem) The present invention consists of coal, water, additives (usually 2% by weight of surfactant)
In order to produce a coal-water slurry with always constant slurry properties consisting of The viscosity of the coal water slurry discharged from the outlet is measured, and based on the measurement signal,
This is a method for producing a coal-water slurry characterized by changing the rotation speed of a wet ball mill.
(作用)
湿式ボールミルに石炭と水と添加剤とを供給し2回転さ
せて石炭を粉砕しながら石炭水スラリーを製造し7.湿
式ボールミル出口から排出される石炭水スラリーの粘度
を粘度計により計測し、その計測信号を制御盤に入力し
計測した粘度が設定値より低ければ湿式謔ケミルの回転
数を上げ、粘度が設定値より高ければ回転数を下ける。(Function) Coal, water, and additives are supplied to a wet ball mill, and the coal is pulverized by rotating twice to produce a coal-water slurry.7. The viscosity of the coal-water slurry discharged from the wet ball mill outlet is measured using a viscometer, and the measurement signal is input to the control panel. If the measured viscosity is lower than the set value, the rotation speed of the wet ball mill is increased and the viscosity is adjusted to the set value. If it's higher, lower the rpm.
ボールミルは9回転による周速度での漣心カと重力によ
りボールが落下する速度がつり合っている速度以下の回
転条件下では、高速である程粉砕力は強い。つまり粉砕
能力を低下するにはボールミルを低速にすればよいわけ
である。In a ball mill, under rotational conditions where the rotational force at the circumferential speed due to nine rotations and the speed at which the balls fall due to gravity are balanced, the higher the speed, the stronger the crushing force is. In other words, in order to reduce the grinding capacity, the speed of the ball mill should be lowered.
このことを示す実験例として第4図に試験に用いた磁製
ボールミルの回転数と粉砕粒度との関係を示す。As an experimental example showing this, FIG. 4 shows the relationship between the rotation speed of the porcelain ball mill used in the test and the pulverized particle size.
第4図から明らかなように回転数を上けると石炭の粒度
が小さくなる。石炭の粒度が小さくなると石炭水スラリ
ーの粘度が増大する。−刃口転数を下けるとこれとは逆
の現象が生じ石炭水スラリーの粘度が低下する。As is clear from FIG. 4, as the rotation speed increases, the particle size of the coal becomes smaller. As the particle size of coal decreases, the viscosity of the coal-water slurry increases. - When the cutting edge rotation speed is lowered, the opposite phenomenon occurs and the viscosity of the coal-water slurry decreases.
(実施例) 第1図に本発明の方法の1実施例の例示図を示す。(Example) FIG. 1 shows an illustrative diagram of one embodiment of the method of the invention.
第1図において、1は石炭供給ラインで粗粉原料石炭が
供給される。2は水供給ラインであり、水は3の界面活
性剤ラインから供給される界面活性剤と共に湿式ボール
ミル4内に一定量供給される。5は湿式ボールミル4を
駆動しているモーターであり2通常は一定速度である。In FIG. 1, numeral 1 denotes a coal supply line through which coarse raw material coal is supplied. 2 is a water supply line, and a fixed amount of water is supplied into the wet ball mill 4 together with the surfactant supplied from the surfactant line 3. Reference numeral 5 denotes a motor that drives the wet ball mill 4, and the motor 2 normally operates at a constant speed.
湿式ボールミル4で粉砕された石炭水スラリーは、粘度
計6を通って排出ライン7を経由して製品受タンク8へ
移送される。このとき粘度計6の計測信号は、制御盤9
に入力され、設定値との差に応じてモータ5の回転数を
変化させてそれにより湿式ボールミルの回転数を増減さ
せ一定粘度の石炭水スラリー製品を得ることができる。The coal-water slurry pulverized in the wet ball mill 4 passes through a viscometer 6 and is transferred to a product receiving tank 8 via a discharge line 7. At this time, the measurement signal of the viscometer 6 is
The number of revolutions of the motor 5 is changed according to the difference from the set value, thereby increasing or decreasing the number of revolutions of the wet ball mill, thereby making it possible to obtain a coal-water slurry product with a constant viscosity.
なお、得られる粘度の計測信号の度合いによっては1石
炭、水、界面活性剤の原料の供給系の供給量に対してそ
の計測信号を入力し制御することも可能であり、このこ
とは本発明実施の効果を妨げない。Note that depending on the degree of the obtained viscosity measurement signal, it is also possible to input and control the supply amount of the raw material supply system of 1 coal, water, and surfactant, and this is possible in the present invention. Do not hinder the effectiveness of implementation.
(効果)
本発明の方法により石炭水スラリーの製造を実施し、制
御することにより、一定の性状を有する石炭水スラリー
の製品を得ることができると・ともに、異常増粘による
石炭水スラリーの湿式ボールミルからの排出不能等のト
ラブルを防止できるだけでなく、原料供給系の不調時の
対策にもなり、かつ、装置の制御も容易である。(Effects) By carrying out and controlling the production of coal-water slurry according to the method of the present invention, it is possible to obtain a product of coal-water slurry having certain properties. This not only prevents troubles such as the inability to discharge from the ball mill, but also serves as a countermeasure against malfunctions in the raw material supply system, and the equipment is easy to control.
なお本発明の方法は石炭水スラリーの製造のみならず液
体一固体′混合スラリーで粉砕により粘度が増加するス
ラリーの製造時の管理にも応用できる。The method of the present invention can be applied not only to the production of coal-water slurry, but also to the management during production of slurry, which is a liquid-solid mixed slurry whose viscosity increases through pulverization.
第1図は本発明の実施例の例示図、第2図は粉砕時間と
石炭水スラリー粘度との関係を示すグラフ、第3図は粉
砕時間と石炭水スラリー粒度との関係を示すグラフ、第
4図はボールミル回転数と石炭水スラリー粒度との関係
を示すグラフである。
4・・・湿式ボールミル、5・モータ、6・・・粘度計
、9・・制御盤。FIG. 1 is an illustration of an embodiment of the present invention, FIG. 2 is a graph showing the relationship between grinding time and coal-water slurry viscosity, FIG. 3 is a graph showing the relationship between grinding time and coal-water slurry particle size, and FIG. FIG. 4 is a graph showing the relationship between the ball mill rotation speed and the coal water slurry particle size. 4... Wet ball mill, 5... Motor, 6... Viscometer, 9... Control panel.
Claims (1)
ルミルにより製造する方法において、湿式ボールミル出
口における石炭水スラリーの粘度を計測し、その信号に
より湿式ボールミルの回転数を制御して一定性状の石炭
水スラリーを得ることを特徴とする石炭水スラリーの製
造方法。In a method of manufacturing a coal-water slurry consisting of coal, water, and additives using a wet ball mill, the viscosity of the coal-water slurry at the outlet of the wet ball mill is measured, and the rotational speed of the wet ball mill is controlled based on the signal to produce coal with constant properties. A method for producing a coal-water slurry, characterized in that a water slurry is obtained.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15073084A JPS6128588A (en) | 1984-07-20 | 1984-07-20 | Production of coal/water slurry |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15073084A JPS6128588A (en) | 1984-07-20 | 1984-07-20 | Production of coal/water slurry |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6128588A true JPS6128588A (en) | 1986-02-08 |
Family
ID=15503155
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15073084A Pending JPS6128588A (en) | 1984-07-20 | 1984-07-20 | Production of coal/water slurry |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6128588A (en) |
-
1984
- 1984-07-20 JP JP15073084A patent/JPS6128588A/en active Pending
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