JPS58215492A - Preparation of concentrated coal/water slurry with good fluidity - Google Patents

Preparation of concentrated coal/water slurry with good fluidity

Info

Publication number
JPS58215492A
JPS58215492A JP9814082A JP9814082A JPS58215492A JP S58215492 A JPS58215492 A JP S58215492A JP 9814082 A JP9814082 A JP 9814082A JP 9814082 A JP9814082 A JP 9814082A JP S58215492 A JPS58215492 A JP S58215492A
Authority
JP
Japan
Prior art keywords
coal
water
slurry
particles
amount
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.)
Granted
Application number
JP9814082A
Other languages
Japanese (ja)
Other versions
JPS628478B2 (en
Inventor
Shigemi Tsukahara
塚原 重美
Makoto Imoo
誠 芋生
Yoshitake Hizuka
肥塚 嘉剛
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.)
Kajima Corp
Original Assignee
Kajima Corp
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 Kajima Corp filed Critical Kajima Corp
Priority to JP9814082A priority Critical patent/JPS58215492A/en
Publication of JPS58215492A publication Critical patent/JPS58215492A/en
Publication of JPS628478B2 publication Critical patent/JPS628478B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To prepare a concentrated coal/water slurry with excellent fluidity, by adding inert spherical fine particles with a specified diameter to an aqueous slurry of coal. CONSTITUTION:Fine powder consisting of spherical inert/particles with an average diameter of 0.5mm. or smaller (e.g. fly ash) is added in an amount of 5- 10wt% to a concentrated aqueous slurry of coal prepared by suspending pulverized coal in water. EFFECT:The fine particles are presumed to be positioned between coal particles together with water and act as a bearing material to facilitate move of coal particles leading to formation of a slurry with required fluidity even when water is present only in a small amount.

Description

【発明の詳細な説明】 本発明は流動性の良好な高濃度石炭−水スラリーの製法
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a highly concentrated coal-water slurry having good fluidity.

近年、エネルギー源として石炭を利用すべく、大規模な
石炭使用プロジェクトが数多く計画されているが、一般
に、石炭は石油に比べて単位重量当りの発熱量が50〜
80%と小さいのでその取扱い高が多くなると共に、固
体であり、炭塵の発生を伴い、かつ空気中で酸化が進行
するなどその搬送や取扱いがやっかいで、石油と同程度
のエネルギー量を石炭で得るには、わが国が過去におい
て経験したことのないような規模での、船舶、港湾、荷
役などの諸設備並びに環境・防災対策上の設備などにお
いて、高効率化とクリーン化及び安全化全達成する取扱
い技術の確立が望まれ、石炭入手の信頼性全確保し、か
つ燃料費に上乗せされる関連経費をできるだけ節減する
と共に、立地に際して地域社会に受は入れられる諸条件
を満たすことが大きな課題となっている。
In recent years, many large-scale coal projects have been planned to utilize coal as an energy source, but coal generally has a calorific value of 50 to
Since coal is small (80%), it has to be handled in a large amount, and since it is solid, it generates coal dust and oxidizes in the air, making it difficult to transport and handle. In order to achieve this goal, we will improve the efficiency, cleanliness, and safety of various facilities such as ships, ports, and cargo handling facilities, as well as facilities for environmental and disaster prevention measures, on a scale that Japan has never experienced in the past. It is desirable to establish handling technology to achieve this goal, and it is important to ensure the reliability of coal procurement, reduce the related expenses added to fuel costs as much as possible, and meet various conditions to be accepted by the local community at the time of location. It has become a challenge.

これに答えるものの一つとして、固体である石炭を破砕
し、これを流体と均一に混合してスラリー状となし、石
油に準じて流体物として取扱う提案がなされている。な
力)でも、石炭と水のスラリーは大量かつ確実な石炭搬
送方式として米国において実用例があるほか、これによ
る巨大計画が世界各地で立案されているなど、有望な手
段であると考えられている。
As one solution to this problem, a proposal has been made to crush solid coal, mix it uniformly with a fluid to form a slurry, and treat it as a fluid in the same way as petroleum. However, coal and water slurry is considered to be a promising method, with examples of practical use in the United States as a method for transporting large quantities of coal reliably, and large-scale projects using this slurry being planned around the world. There is.

しかし、この石炭−水スラ’J −1ce多量の原水の
確保と搬送終点もしくは燃焼前での大規模な脱水と排水
の処理が前提となる。このために、地域によってはその
計画路線の隘路となる場合が多い。
However, this coal-water slurry'J-1ce requires securing a large amount of raw water and large-scale dewatering and wastewater treatment at the end of transportation or before combustion. For this reason, some areas often become bottlenecks for planned routes.

したがって、混合水量をできるだけ少なくした高濃度ス
ラリーを作ることが望1れる。(混合水量全充分に少f
i<L、た高濃度スラリーは、石油に替わる流体燃料と
して直接炉内に吹込むことができるよう炉側からの研究
も進められている。)だが、混合水量を少なくすればス
ラリーの流動性が低下1〜、取扱い面でも、燃料として
もその機能を喪失する。
Therefore, it is desirable to make a highly concentrated slurry with as little amount of mixed water as possible. (The amount of mixed water is sufficiently small.
Research is also progressing from the furnace side so that highly concentrated slurry with i<L can be directly injected into the furnace as a fluid fuel in place of petroleum. ) However, if the amount of mixed water is reduced, the fluidity of the slurry decreases1~, and it loses its function both in terms of handling and as a fuel.

一般F1破砕された石炭粉に粒度分布全適正に調整した
場合においても、石炭/スラリー比を重量で約55%よ
り高くすると、スラリーは粘土状となって固形化し、管
路輸送は困難となる。これに、破砕された石炭は粒子形
状が角ばっていること、また石炭は疎水性であり、粒子
表向が水に対する濡れ性に欠けることなどの理由により
、所定の水量に満たないとその流動性が著しく低下する
ようlK−なると考えられている。;f:こて、界面活
性剤などの化学薬剤を添加して石炭粒子表面の水に対す
る性質全改善し、粒子間の相互移動ヲ答易にすることに
よって、少ない水量で流動性全良好にする方法などが既
に提案されている。しかし、このような化学薬剤を主体
とするものを燃料物質に添加することに、燃料設備や排
煙性状に影響を及ぼすおそれがあると共に、巨大量のス
ラリー量を取扱う関係上、その副次作用が累積すること
も覚悟せねばならず、またこのような化学薬剤は、一般
に高価であり大量消費には適さない。
Even when the particle size distribution of general F1 crushed coal powder is properly adjusted, if the coal/slurry ratio is higher than about 55% by weight, the slurry becomes clay-like and solidifies, making pipe transportation difficult. . In addition, crushed coal has an angular particle shape, and coal is hydrophobic, meaning that the surface of the particles lacks wettability with water. It is thought that the level of lK- significantly decreases the ;f: By adding chemical agents such as trowels and surfactants to completely improve the properties of the surface of coal particles against water, and by facilitating mutual movement between particles, good fluidity can be achieved with a small amount of water. Methods have already been proposed. However, adding such chemical-based substances to fuel materials may affect fuel equipment and smoke exhaust properties, and since a huge amount of slurry is handled, there are risks of side effects. One must also be prepared for the accumulation of chemicals, and such chemical agents are generally expensive and unsuitable for mass consumption.

本発明は、このような問題の付随する化学薬剤の使用に
よる石炭粒子の水に対する濡れ性改善処法によらずとも
、石炭−水スラリーの流動性全高め、ひいては添加水量
の低減全図ること全目的としてなされたものである。
The present invention aims to completely increase the fluidity of coal-water slurry and further reduce the amount of added water, without using chemical agents that are associated with such problems to improve the wettability of coal particles with water. It was done for a purpose.

この目的において本発明に、平均粒径が0.5 mrn
以下の実質的に球形な不活性微粒子からなる微粉末を、
石炭と水の合計量に対して10重量%以下の量で配合す
ることによって、流動性のよい高濃度石炭−水スラリー
ヲ得る方法を提供するものである。ここで、不活性な微
粒子とは、水に溶解したり石炭−水に反応したり、ある
いは変成したりすることのない物理的化学的に安定な微
粒子を意味し、このような意味から鉱物質、例えば二酸
化硅素を主体とする硝子状物質が好適である。そして、
このような不活性微粒子は、実質的に球形の形状を有し
ているものが好ましい。より具体的には、このような実
質上球形の不活性微粒子としては、微粉炭燃焼灰である
フライアッシュ・火山灰・人工硝子球粉末などがある。
For this purpose, the present invention has an average particle size of 0.5 mrn.
Fine powder consisting of the following substantially spherical inert fine particles,
The present invention provides a method for obtaining a highly concentrated coal-water slurry with good fluidity by blending coal and water in an amount of 10% by weight or less based on the total amount of coal and water. Here, inert fine particles mean physically and chemically stable fine particles that do not dissolve in water, react with coal and water, or undergo metamorphosis. For example, a vitreous material mainly composed of silicon dioxide is suitable. and,
Preferably, such inert fine particles have a substantially spherical shape. More specifically, such substantially spherical inert fine particles include fly ash, which is pulverized coal combustion ash, volcanic ash, and artificial glass bulb powder.

このフライアッシュは、微粉炭燃焼ボイラーの煙道ガス
から採取されるが、これは石炭中に含まれている灰分が
燃焼時に溶融し、これが燃焼ガスに同伴して煙道に達し
、温度降下時にその表面張力によって球形となって凝固
したものであり、極く微量の未燃焼炭素等の非球形粒子
を含むが、直径が0.1m71以下の実質上球形の微粒
子からなっている。−f:の成分は 5− SiO□が多く、通常は45重量%以上が5i02であ
る。(このフライアッシュに他の類似粉末に比べて、品
質・量ともに安定入手が可能で、かつ廉価でもある。) 一方においてこのフライアッシュは、石炭全石油代替エ
ネルギー源として活用する場合に不可避的に大量発生す
ることが予想され、その利用を少しでも多く図ることが
石炭使用プロジェクトの大きな課題とされており、した
がって本発明[,1:れば、この課題にも答え得るもの
であって、フライアッシュの新しい用途ヲ見い出した点
においても非常に有益である。加えて、このフライアッ
シュの新しい用途が石炭活用プロジェクトの中で見い出
されたことは、その回収と一部の再利用が一元的になさ
れ得ることになり、−石二鳥の効果がある。
This fly ash is extracted from the flue gas of a pulverized coal-fired boiler.The ash contained in the coal melts during combustion, and it reaches the flue along with the combustion gas, and when the temperature drops, It solidifies into a spherical shape due to its surface tension, and although it contains a very small amount of non-spherical particles such as unburned carbon, it is made up of substantially spherical fine particles with a diameter of 0.1 m or less. The component -f: has a large amount of 5-SiO□, and usually 45% by weight or more is 5i02. (Compared to other similar powders, this fly ash is stably available in terms of quality and quantity, and is also inexpensive.) On the other hand, this fly ash is unavoidably necessary when used as a coal-oil alternative energy source. It is predicted that a large amount of coal will be generated, and the major challenge of coal usage projects is to increase its utilization as much as possible. Therefore, the present invention [,1: It is also very useful in finding new uses for ash. In addition, the discovery of a new use for this fly ash in a coal utilization project means that its recovery and partial reuse can be done in an integrated manner, which has the effect of killing two birds.

このようにして本発明は、フライアッシュのような硝子
状の実質的に球形の微粒子群全主体としてなる化学的お
よび物理的に不活性な微粉宋音、石炭−水スラリーに添
加して少ない添加水量で良 6 − 好な流動性全得るものT:あるが、その添加量は石炭と
水の合計量に対して10重量%以下の量でよく、フライ
アソンユの場合、5重量φ程度の添加量でも、後記実施
例に示すように、無添加の場合と同等の流動特性が約1
0%程度水の添加量を少?<1.でも得ることができる
。このような化学的、物理的に安定な微粉末の添加によ
って、石炭−水スラリーの流動特性が改善される理由は
、この微粒子が石炭粒子間に水と共に介在してベアリン
グ材として作用し、これlc、l:つて石炭粒子の相互
移動が容易となり、少ない水量でも所要の流動性全有す
るスラリーとなるものと考えられる。この点、従来の化
学薬剤VCXるものが、石炭粒子の水に対する濡れ住改
善を行なうのとに、その流動性改善機構が基本的に異な
るものであると推察されると共に、本発明による添加剤
は、スラリー中もしくは大気中でその効果が変化するこ
とがなく、長期貯蔵や長期使用に耐えると同時に、使い
易さの点において化学薬剤では得られない利点を有し、
かつ価格的にも格段に有利である。また、石炭燃焼時に
も、硝子状粉の成分は、もともと石炭に含有される灰分
と同質のものであるので、ボイラー設備や排ガス設備に
別設の影響を与えることがない点でも有利であり、既存
の設備で対応が可能で、かつ特別な排煙対策も不要であ
るなど、非常に数多くの利益が享受できる。
In this way, the present invention provides chemically and physically inert fine particles such as fly ash, consisting entirely of glass-like, substantially spherical particles, which can be added to a coal-water slurry in a small amount. 6 - Good fluidity T: Yes, but the amount added should be 10% by weight or less based on the total amount of coal and water, and in the case of fryer sonyu, the amount added is about 5 weight φ However, as shown in the examples below, the flow characteristics are about 1
Reduce the amount of water added by about 0%? <1. But you can get it. The reason why the flow characteristics of the coal-water slurry are improved by adding such chemically and physically stable fine powder is that these fine particles interpose together with water between coal particles and act as a bearing material. lc, l: It is thought that mutual movement of coal particles becomes easier and a slurry having all the required fluidity can be obtained even with a small amount of water. In this respect, it is presumed that the fluidity improvement mechanism is fundamentally different from that of the conventional chemical agent VCX, which improves the wettability of coal particles to water. does not change its effectiveness in slurry or in the atmosphere, can withstand long-term storage and long-term use, and at the same time has advantages that chemical agents cannot obtain in terms of ease of use.
It is also extremely advantageous in terms of price. In addition, even during coal combustion, the components of the glassy powder are of the same quality as the ash originally contained in the coal, so it is advantageous in that it does not have any effect on boiler equipment or exhaust gas equipment. It can be used with existing equipment, and there are many benefits such as no special smoke exhaust measures required.

以下に本発明の実施例を挙げる。Examples of the present invention are listed below.

粒径3龍以下に破砕された微粉炭と、粒径20〜30μ
mのフライアソ7ユと、水と力)らなる混合物を、その
混合比率を適当に変えて第1図に示す容器1に入れ、そ
の流動特性を測定した。測定に、容器1内の混合物2を
攪拌するための攪拌翼3をモーター4で回転させるさい
に、その回転軸に取付けた反射板5と反射式回転数計測
機6とによって、その回転数を計測すると同時に、モー
ター4への電流量を電流計7VCよって測定し、次式に
よって攪拌必要トルク(Tl’i算出した。
Pulverized coal crushed to a particle size of 3 or less, and a particle size of 20 to 30μ
A mixture consisting of 7 ml of frying fluid, water, and water was placed in a container 1 shown in FIG. 1 with appropriate mixing ratios, and its flow characteristics were measured. For measurement, when a stirring blade 3 for stirring a mixture 2 in a container 1 is rotated by a motor 4, its rotational speed is measured by a reflector 5 attached to its rotating shaft and a reflective rotational speed measuring device 6. At the same time as the measurement, the amount of current to the motor 4 was measured using an ammeter 7VC, and the required stirring torque (Tl'i) was calculated using the following formula.

T=K・− ただし、T;トルク(kg −cx IK;撹拌機固有
係数 T;電流(A) n;回転数(rpm ) 第2図および第5図に測定結果の代表値を示す。
T=K.- However, T: Torque (kg - cx IK; Stirrer specific coefficient T; Current (A) n: Number of rotations (rpm) Representative values of the measurement results are shown in FIGS. 2 and 5.

両図における縦軸q1水のみの場合のトルクに対する混
合物のトルクの比(トルり比)で表わしである。−!た
、両図において破線(イ)に、フライアンシュ全添加し
ない場合の対照例、実線(ロ)にフライアッシュ全混合
物全量に対して5重量%添加したときの値である。第2
図は水量比(水量/全重量)とトルク比の関係を、また
第3図は石炭比(石炭量/全重量)との関係を整理した
ものであるが、これらから明らかなように、フライアノ
ツユ無添加のスラリー(破線)に対してフライアッシュ
添加スラIJ−H1同じレベルの流動特性が少量の水添
加量(約10%程度少ない)で得られ、また石炭量の増
加にも有効であることがわかる。したがって、本発明に
よると、流動性のよい高濃度の石炭−水スラリーが得ら
れ、輸送効率の向上と燃焼の前工程で脱水等の省力、省
設備が達成できるこ 9 − とが明らかである。
In both figures, the vertical axis q1 is expressed as the ratio of the torque of the mixture to the torque in the case of only water (torque ratio). -! Furthermore, in both figures, the broken line (a) shows the control example when no fly ash was added, and the solid line (b) shows the value when 5% by weight was added to the total amount of the fly ash mixture. Second
The figure shows the relationship between water volume ratio (water volume/total weight) and torque ratio, and Figure 3 summarizes the relationship between coal ratio (coal volume/total weight). The same level of fluidity as fly ash-added slurry IJ-H1 compared to additive-free slurry (dashed line) can be obtained with a small amount of water added (approximately 10% less), and it is also effective in increasing the amount of coal. I understand. Therefore, it is clear that according to the present invention, a highly concentrated coal-water slurry with good fluidity can be obtained, and it is possible to improve transportation efficiency and save labor and equipment such as dehydration in the pre-combustion process. .

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

第1図に石炭−水スラリーの流動特性測定法を説明する
ための機器配置図、第2図は水量比とトノVり比との関
係図、第6図は石炭比とトルク比との関係図である。 出願人  鹿島建設株式会社  10− 第1図 第2図 第3図
Figure 1 is an equipment layout diagram to explain the method for measuring flow characteristics of coal-water slurry, Figure 2 is a relationship diagram between water volume ratio and tonnage V ratio, and Figure 6 is a relationship diagram between coal ratio and torque ratio. It is a diagram. Applicant: Kajima Corporation 10- Figure 1 Figure 2 Figure 3

Claims (3)

【特許請求の範囲】[Claims] (1)粉砕された石炭を水に分散させた石炭−水スラリ
ーを得るにさいし、平均粒径が0.5i71以下の実質
的に球形な不活性微粒子全主体としてなる微粉末を石炭
と水の合計重量に対して10重重量板下の量で該スラリ
ーに配合することを特徴とする流動性のよい高濃度石炭
−水スラリーの製法。
(1) To obtain a coal-water slurry by dispersing pulverized coal in water, fine powder consisting entirely of substantially spherical inert fine particles with an average particle size of 0.5i71 or less is mixed with coal and water. A method for producing a highly concentrated coal-water slurry with good fluidity, characterized in that the slurry is blended in an amount of 10 weight plates or less based on the total weight.
(2)微粉末が平均粒径OAmm以下の硝子状球形粒子
群から実質的になる特許請求の範囲第1項記載の製法。
(2) The manufacturing method according to claim 1, wherein the fine powder consists essentially of vitreous spherical particles having an average particle diameter of OAmm or less.
(3)微粉末がフライアッシュである特許請求の範囲第
1項またに第2項記載の製法。
(3) The manufacturing method according to claim 1 or 2, wherein the fine powder is fly ash.
JP9814082A 1982-06-08 1982-06-08 Preparation of concentrated coal/water slurry with good fluidity Granted JPS58215492A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9814082A JPS58215492A (en) 1982-06-08 1982-06-08 Preparation of concentrated coal/water slurry with good fluidity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9814082A JPS58215492A (en) 1982-06-08 1982-06-08 Preparation of concentrated coal/water slurry with good fluidity

Publications (2)

Publication Number Publication Date
JPS58215492A true JPS58215492A (en) 1983-12-14
JPS628478B2 JPS628478B2 (en) 1987-02-23

Family

ID=14211913

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9814082A Granted JPS58215492A (en) 1982-06-08 1982-06-08 Preparation of concentrated coal/water slurry with good fluidity

Country Status (1)

Country Link
JP (1) JPS58215492A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02281306A (en) * 1989-04-24 1990-11-19 Matsushita Electric Ind Co Ltd Hot water supply device
JP2658876B2 (en) * 1994-06-20 1997-09-30 松下電器産業株式会社 Hot water mixing equipment
JPH0868543A (en) * 1995-09-25 1996-03-12 Matsushita Electric Ind Co Ltd Equipment for mixing hot water with water

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57174394A (en) * 1981-04-22 1982-10-27 Hitachi Ltd Coal slurry composition

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57174394A (en) * 1981-04-22 1982-10-27 Hitachi Ltd Coal slurry composition

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Publication number Publication date
JPS628478B2 (en) 1987-02-23

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