JPH0113517B2 - - Google Patents
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- Publication number
- JPH0113517B2 JPH0113517B2 JP56122166A JP12216681A JPH0113517B2 JP H0113517 B2 JPH0113517 B2 JP H0113517B2 JP 56122166 A JP56122166 A JP 56122166A JP 12216681 A JP12216681 A JP 12216681A JP H0113517 B2 JPH0113517 B2 JP H0113517B2
- Authority
- JP
- Japan
- Prior art keywords
- coal
- water
- water slurry
- thinner
- oil
- 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
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- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Liquid Carbonaceous Fuels (AREA)
Description
本発明は石炭−水スラリー用減粘剤に関する。
さらに詳しくは、微粉炭を水に分散させ、ポンプ
輸送が可能な高濃度石炭−水スラリーを提供する
ための減粘剤に関する。
近年石油資源の枯渇により、石炭の利用が再認
織され、その利用方法が種々検討されている。と
ころが石炭は石油と異なり、固体であるためポン
プ輸送ができない。そのため石炭を粉体化して水
中に分散し、水スラリーにする方法が種々検討さ
れている。しかしながらこの方法は現技術では、
石炭濃度を上げていくと著しく増粘し、流動性が
なくなるため、ポンプ輸送が困難になつてくる。
一方石炭濃度を下げると輸送効率が低下し、さら
に燃焼前に脱水工程が必要となつてきて、費用が
かゝるため実用的でない。
特開昭54−33803号には微粉鉱石スラリーに高
分子界面活性剤を加えることが記載されている
が、具体的にはポリアクリルアミド、ポリエチレ
ンイミンが例示されているだけであり、かつ低濃
度の微粉鉱石スラリーを対象としたものである。
本発明者らは、高濃度の石炭−水スラリーを流
動化し、ポンプ輸送を可能にする石炭−水スラリ
ー用減粘剤について鋭意研究し、少量の添加で、
石炭−水スラリーの粘度を著しく減少し、そのた
め高濃度の石炭濃度においてもポンプ輸送が可能
な石炭−水スラリーを提供する減粘剤の開発に成
功した。
本発明の減粘剤を用いると、少量の水で石炭を
流動化できるため、ポンプ輸送を可能にすること
は勿論、そのままの状態でボイラー燃焼ができ、
燃焼前の脱水工程をも省くことができる。本発明
の減粘剤の使用により、石炭の取り扱いは非常に
簡便になり、その利用用途は大きく広がる。
石炭−水スラリーに使用される石炭は無煙炭、
瀝青炭、亜瀝青炭、褐炭、またはそれらをクリー
ン化したものなど、どのような石炭であつてもよ
い。また水スラリー中の石炭粒度も粉末であれば
どのような粒度であつてもよいが、現在火力発電
所で燃焼される微粉炭は200メツシユパス70%以
上のものであるから、この粒度が微粉炭の粒度の
目安である。しかし本発明の減粘剤は粒度によつ
て影響されるものではなく、どのような粒径の石
炭粉末に対してもすぐれた効果を発揮する。
またクリーン化した石炭は石炭中より無機物、
例えば灰およびイオウなどを除去したものであ
る。石炭をクリーン化する方法としては、例えば
重液分離法、Oil Agglomeration法(以下OA法
という)、浮遊選炭法などがある。しかしながら
これら以外の方法でもよく特に限定するものでは
ない。
OA法について記すと、石炭を乾式あるいは湿
式で粉砕した後、水スラリーを調整し、適量の油
を添加するか、あらかじめ石炭に油をコートした
後、水スラリーを調整し、撹拌することにより石
炭の有機分と無機物との油および水に対する濡れ
の差を利用して、選択的に石炭の有機分を濡らす
油をバインダーにして石炭有機分の凝集を起させ
る。一方無機物は油との親和力が弱いため、水中
に浮離するので、凝集した石炭の水分離を行なえ
ば同時に無機物を除去することができる方法であ
る。OA法の石炭−水スラリー中の石炭濃度は通
常10〜65%である。
OA法において用いる油は原油あるいは原油か
ら得られる各種留分、例えば灯油、軽油、A重
油、B重油、C重油などや、タールまたは頁岩油
またはエチレン分解残油または各種配合油などが
一般に燃料として用いられる油や、潤滑油、洗浄
油などの鉱物油である。またベンゼン、トルエ
ン、キシレン、動植物油など水に不溶の油も用い
られるが中でもC重油、タール残渣油などの重質
油類は安価であるため特に好ましい。この油は無
機物除去処理をしようとする石炭−水スラリー中
の石炭に対して一般的に20%以下の量で充分であ
る。
また浮遊選炭法は既存の選炭法で微粉炭−水ス
ラリー中に極く少量の油を加え撹拌することによ
り泡立たせて、フロスを生成させる。本方法も
OA法同様、石炭の有機分がフロス油膜に付着す
るが、無機物は水中に浮離し、石炭有機分と分離
することができる方法である。
浮遊選炭法において用いる油は、ターピネオイ
ル、タール、A重油、C重油、軽油、灯油であ
る。
上記方法により数10%以上の無機物が石炭より
除去されるのが一般的である。
このようにしてクリーン化した石炭を使用すれ
ばクリーン化していない石炭にくらべて本発明の
添加剤の効果は著じるしく優れ、数ポイント高濃
度の石炭−水スラリーを得ることができる。さら
に、クリーン化した石炭を用いた場合、本効果以
外にも燃焼時のボイラー腐蝕が抑制され、灰の除
去設備、脱硫設備への負担が軽減される等のメリ
ツトが非常に大きい。
本発明の石炭−水スラリー用減粘剤は、2%水
溶液の粘度が25℃において10000cp以下、好まし
くは2000cp以下であるカルボキシメチルセルロ
ースまたはその塩を必須成分として含有するもの
である。
カルボキシメチルセルロースは、典型的なエー
テル化度1.0の場合を例にとれば以下の一般構造
式で示される。
式中Mは水素または塩を形成するカチオン、n
は重合度を意味する。
本発明に用いるカルボキシメチルセルロースま
たはその塩のエーテル化度は0.3〜3.0の範囲で、
水溶性ないし水分散性であればよい。塩として
は、ナトリウム、カリウムなどのアルカリ金属
塩、アンモニウム塩、アミン塩、およびこれらの
塩の一部がカルシウムなどのアルカリ土類金属で
置換されたものなどが使用できる。
よく知られているように、カルボキシメチルセ
ルロースおよびその塩は、反応媒体として水のみ
を用いる水媒法や、有機溶剤と水を用いる溶媒法
により、パルプを水酸化ナトリウムとモノクロル
酢酸またはそのアルカリ塩によりエーテル化して
得ることができる。
本発明の減粘剤は、2%水溶液の粘度が25℃に
おいて10000cp以下、好ましくは2000cp以下のカ
ルボキシメチルセルロースまたはその塩のみが有
効であり、これらの粘度を有するものを得るに
は、適切な原料パルプを選択するほか、製造過程
や製造後に、過酸化物、次亜ハロゲン酸塩、過ヨ
ウ素酸塩、二酸化窒素、その他酸化剤および紫外
線により酸化分解したり、酵素分解によつて容易
に粘度調整することができる。
水側に電荷をもつたカルボキシル基を向けて石
炭粒子表面に吸着され、その電荷の反撥作用によ
つて石炭粒子が分散し、流動性が向上するために
著しい粘度低下を起こすものと思われる。またカ
ルボキシメチルセルロースは鎖状に沿つて多くの
解離基を持つ高分子電解質であり、水溶液中では
解離して高分子イオンを生じるため、物理的特性
は平均重合度、つまり水溶液の粘度に強く影響を
受ける。2%水溶液の粘度が25℃で10000cp以
下、好ましくは2000cp以下のものだけが有効で
あり、10000cpより大きくなると凝集作用が生
じ、スラリーの粘度が著しく上昇し、流動性のあ
るスラリーを得ることができない。
かゝる本発明の減粘剤は、石炭−水スラリーに
対してカルボキシメチルセルロースまたはその塩
として、0.01〜5.0重量%、好ましくは0.03〜2.0
重量%添加することによりすぐれた効果を発揮す
る。石炭−水スラリーの流動性の限界は石炭の種
類や粒度によつて異なるが、一般に減粘剤を添加
しなければ石炭濃度が50%前後で流動性がなくな
るが、本発明の減粘剤を添加すれば著しく粘度が
低下するため、石炭濃度が61%以上、特に70%以
上においても流動性を有するものである。さらに
クリーン化した石炭を用いた場合は石炭濃度がさ
らに数ポイント、一般的には3〜10ポイント上昇
する。
本発明の減粘剤は、他の界面活性剤と併用して
使用することもできる。
石炭−水スラリーの製造方法および減粘剤の添
加方法に関しては、石炭をあらかじめ乾式で粉砕
した後減粘剤水溶液中に混合する方法や、石炭−
水スラリーをつくつた後減粘剤を添加する方法
や、ミル中へ石炭、水、減粘剤を加え、石炭を粉
砕しながら混合する方法や、それぞれの方法にお
いて、石炭の代わりにクリーン化した石炭を用い
て混合する方法等任意の方法が実施できる。
本発明の減粘剤は、石炭を水中に安定に分散す
る効果もすぐれており、長期間、例えば1ケ月間
静置しても水分離を生ぜず、均質な石炭−水スラ
リーを保持している。
このように本発明の減粘剤は、石炭−水スラリ
ーに対して0.01〜5.0重量%、好ましくは0.03〜
2.0重量%添加するだけで、石炭−水スラリーの
粘度を著しく減少せしめ、しかも高濃度でポンプ
輸送が可能な石炭−水スラリーをつくることがで
きる。
以下に実施例を示す。実施例中%は重量によ
る。
実施例 1
所定量の減粘剤を溶解した水溶液に、200メツ
シユ80%パスまで粉砕した石炭を室温にてかきま
ぜながら加え、所定濃度の石炭−水スラリーを調
整する。このスラリーの粘度を25℃にて測定し、
また流動性を観察する。さらにこのスラリーを1
ケ月間静置した後、水の分離状態を測定する。
試験結果を第1表に示す。第1表に示すとお
り、本発明の減粘剤を添加すると石炭粘度72〜77
%においても粘度は1000〜3000cpであり、極め
て流動性が良好である。これに対し一般のアニオ
ン界面活性剤や本発明以外のCMCを添加したり、
減粘剤無添加の場合は、石炭濃度50%において粘
度が20000cp以上になり、全く流動しない。
The present invention relates to a thinner for coal-water slurries.
More particularly, it relates to a thinning agent for dispersing pulverized coal in water to provide a highly concentrated coal-water slurry that can be pumped. In recent years, due to the depletion of petroleum resources, the use of coal has been reconsidered, and various methods of its use are being considered. However, unlike oil, coal is a solid and cannot be transported by pump. For this reason, various methods are being considered for pulverizing coal and dispersing it in water to form a water slurry. However, with current technology, this method
As the coal concentration increases, it becomes significantly thicker and loses its fluidity, making pumping difficult.
On the other hand, lowering the coal concentration reduces transportation efficiency and requires a dehydration process before combustion, which is not practical as it increases costs. JP-A No. 54-33803 describes adding a polymeric surfactant to a fine ore slurry, but it only specifically exemplifies polyacrylamide and polyethyleneimine, and It is intended for fine ore slurry. The present inventors have conducted intensive research on a thinning agent for coal-water slurry that can fluidize highly concentrated coal-water slurry and enable pumping.
A thinning agent has been successfully developed that significantly reduces the viscosity of a coal-water slurry and thus provides a coal-water slurry that is pumpable even at high coal concentrations. By using the thinner of the present invention, coal can be fluidized with a small amount of water, which not only makes it possible to transport it by pump, but also allows it to be burned in a boiler as it is.
The dehydration step before combustion can also be omitted. By using the thinning agent of the present invention, handling of coal becomes extremely simple, and its applications are greatly expanded. The coal used in the coal-water slurry is anthracite;
Any coal may be used, such as bituminous coal, sub-bituminous coal, brown coal, or cleaned versions thereof. Furthermore, the particle size of the coal in the water slurry may be any particle size as long as it is powder, but since the pulverized coal currently burned in thermal power plants is 70% or more of 200 mesh pass, this particle size is suitable for pulverized coal. This is a guideline for the particle size of However, the thinner of the present invention is not affected by particle size and exhibits excellent effects on coal powder of any particle size. In addition, the cleaned coal contains more inorganic substances than in the coal.
For example, ash and sulfur have been removed. Methods for cleaning coal include, for example, heavy liquid separation method, oil agglomeration method (hereinafter referred to as OA method), and coal flotation method. However, methods other than these may also be used and are not particularly limited. Regarding the OA method, coal is pulverized dry or wet, then a water slurry is prepared, and an appropriate amount of oil is added, or coal is coated with oil in advance, a water slurry is prepared, and the water slurry is stirred. Utilizing the difference in wettability of the organic and inorganic components of coal to oil and water, the organic components of coal are coagulated using oil that selectively wets the organic components of coal as a binder. On the other hand, since inorganic substances have a weak affinity with oil and float in water, this method can remove inorganic substances at the same time by separating the water from coagulated coal. The coal concentration in the coal-water slurry of the OA method is usually 10-65%. The oil used in the OA method is generally crude oil or various fractions obtained from crude oil, such as kerosene, light oil, A heavy oil, B heavy oil, C heavy oil, etc., tar or shale oil, ethylene cracked residual oil, or various blended oils. The oils used are mineral oils such as lubricating oils and cleaning oils. Water-insoluble oils such as benzene, toluene, xylene, and animal and vegetable oils may also be used, but heavy oils such as C heavy oil and tar residue oil are particularly preferred because they are inexpensive. This oil is generally sufficient in an amount of 20% or less of the coal in the coal-water slurry to be treated for mineral removal. The flotation coal washing method is an existing coal washing method in which a very small amount of oil is added to a pulverized coal-water slurry and stirred to create froth. This method also
Similar to the OA method, the organic components of the coal adhere to the froth oil film, but the inorganic components float in the water and can be separated from the organic components of the coal. The oils used in the flotation method are turpine oil, tar, A heavy oil, C heavy oil, light oil, and kerosene. Generally, several tens of percent or more of inorganic substances are removed from coal by the above method. If coal cleaned in this way is used, the effect of the additive of the present invention is significantly superior to coal that has not been cleaned, and a coal-water slurry with several points higher concentration can be obtained. Furthermore, when cleaned coal is used, in addition to this effect, boiler corrosion during combustion is suppressed, and the burden on ash removal equipment and desulfurization equipment is reduced, among other great benefits. The thinner for coal-water slurries of the present invention contains as an essential component carboxymethyl cellulose or a salt thereof, which has a viscosity of 2% aqueous solution at 25° C. of 10,000 cp or less, preferably 2,000 cp or less. Carboxymethylcellulose is represented by the general structural formula below, taking as an example a typical case with a degree of etherification of 1.0. In the formula, M is hydrogen or a salt-forming cation, n
means the degree of polymerization. The degree of etherification of carboxymethylcellulose or its salt used in the present invention is in the range of 0.3 to 3.0,
Any material may be used as long as it is water-soluble or water-dispersible. Examples of salts that can be used include alkali metal salts such as sodium and potassium salts, ammonium salts, amine salts, and salts in which a portion of these salts is substituted with an alkaline earth metal such as calcium. As is well known, carboxymethyl cellulose and its salts can be produced by a water-based method using only water as a reaction medium, a solvent method using an organic solvent and water, or a method in which pulp is mixed with sodium hydroxide and monochloroacetic acid or its alkali salt. It can be obtained by etherification. The thinning agent of the present invention is effective only with carboxymethyl cellulose or its salts whose viscosity in a 2% aqueous solution is 10,000 cp or less, preferably 2,000 cp or less at 25°C, and in order to obtain a product having these viscosities, suitable raw materials are required. In addition to selecting the pulp, viscosity can be easily adjusted by oxidative decomposition using peroxides, hypohalites, periodates, nitrogen dioxide, other oxidizing agents, and ultraviolet rays, or by enzymatic decomposition during or after the manufacturing process. can do. It is thought that coal particles are adsorbed on the surface of coal particles with their charged carboxyl groups facing the water side, and the coal particles are dispersed due to the repulsion of the charges, improving fluidity and causing a significant decrease in viscosity. Carboxymethyl cellulose is a polymer electrolyte with many dissociative groups along its chain, and because it dissociates in aqueous solution to produce polymer ions, its physical properties strongly affect the average degree of polymerization, that is, the viscosity of the aqueous solution. receive. Only 2% aqueous solutions with a viscosity of 10,000 cp or less, preferably 2,000 cp or less at 25°C are effective; if it exceeds 10,000 cp, flocculation occurs and the viscosity of the slurry increases significantly, making it difficult to obtain a fluid slurry. Can not. Such a thinner of the present invention is used in an amount of 0.01 to 5.0% by weight, preferably 0.03 to 2.0% by weight of carboxymethylcellulose or its salt based on the coal-water slurry.
Excellent effects can be achieved by adding % by weight. The fluidity limit of a coal-water slurry differs depending on the type and particle size of the coal, but generally, if a thinner is not added, fluidity will be lost at a coal concentration of around 50%, but with the thinner of the present invention, When added, the viscosity decreases significantly, so it has fluidity even when the coal concentration is 61% or more, especially 70% or more. If cleaner coal is used, the coal concentration will increase by several points, typically 3 to 10 points. The thinner of the present invention can also be used in combination with other surfactants. Regarding the method of producing a coal-water slurry and the method of adding a thinner, there are two methods: dry-pulverizing coal in advance and then mixing it into an aqueous solution of a thinner;
There are methods that add a thinner after making a water slurry, methods that add coal, water, and a thinner to a mill, and mix while grinding the coal. Any method can be used, such as a method of mixing using coal. The thinner of the present invention has an excellent effect of stably dispersing coal in water, and does not cause water separation even when left standing for a long period of time, for example, one month, and maintains a homogeneous coal-water slurry. There is. Thus, the thinner of the present invention can be used in an amount of 0.01 to 5.0% by weight, preferably 0.03 to 5.0% by weight, based on the coal-water slurry.
By adding only 2.0% by weight, the viscosity of the coal-water slurry can be significantly reduced and a highly concentrated coal-water slurry can be produced that can be pumped. Examples are shown below. In the examples, percentages are by weight. Example 1 Coal pulverized to 80% pass of 200 mesh is added to an aqueous solution containing a predetermined amount of a thinning agent while stirring at room temperature to prepare a coal-water slurry of a predetermined concentration. The viscosity of this slurry was measured at 25℃,
Also observe fluidity. Add this slurry to 1
After allowing it to stand for several months, measure the state of water separation. The test results are shown in Table 1. As shown in Table 1, when the thinner of the present invention is added, the viscosity of coal is 72 to 77.
%, the viscosity is 1000 to 3000 cp, and the fluidity is extremely good. To this, general anionic surfactants or CMC other than the present invention may be added,
If no thinner is added, the viscosity will be over 20,000 cp at a coal concentration of 50%, and it will not flow at all.
【表】【table】
【表】
実施例 2
クリーン化した石炭を使用して実施例1と同様
に、所定濃度の石炭−水スラリーを調整する。石
炭粒度は200メツシユ80%パスのものである。こ
のスラリーの粘度を25℃にて測定し、また流動性
をも観察する。このスラリーを1ケ月間静置した
後、水の分離状態を測定する。
試験結果を第2表に示す。
第2表に示すとおり石炭−水スラリーに本発明
の減粘剤を添加すると、石炭濃度76〜80%でも粘
度が1000〜3000cpであり極めて流動性が良好で
ある。一方、本発明以外の減粘剤を添加したり、
減粘剤無添加の場合は石炭濃度80%において粘度
が20000cp以上になり全く流動しない。[Table] Example 2 A coal-water slurry of a predetermined concentration is prepared in the same manner as in Example 1 using cleaned coal. The coal particle size is 80% pass of 200 mesh. The viscosity of this slurry is measured at 25°C and the fluidity is also observed. After this slurry was allowed to stand for one month, the state of water separation was measured. The test results are shown in Table 2. As shown in Table 2, when the thinner of the present invention is added to a coal-water slurry, the viscosity is 1000 to 3000 cp even at a coal concentration of 76 to 80%, resulting in extremely good fluidity. On the other hand, adding a thinner other than the present invention,
If no thinner is added, the viscosity will be over 20,000 cp at a coal concentration of 80%, and there will be no flow at all.
【表】【table】
Claims (1)
を向上させるため、2%水溶液の粘度が25℃にお
いて10000cp以下、好ましくは2000cp以下である
カルボキシメチルセルロースまたはその塩を必須
成分として添加することを特徴とする石炭−水ス
ラリー用減粘剤。 2 石炭濃度が61%以上、好ましくは70%より高
い石炭−水スラリーに用いるための特許請求の範
囲第1項記載の石炭−水スラリー用減粘剤。 3 石炭がクリーン化した石炭である特許請求の
範囲第1項または第2項記載の石炭−水スラリー
用減粘剤。[Claims] 1. In order to reduce the viscosity of the coal-water slurry and improve its fluidity, carboxymethyl cellulose or its salt, whose viscosity in a 2% aqueous solution is 10,000 cp or less, preferably 2,000 cp or less at 25°C, is an essential component. A thinning agent for coal-water slurry, characterized in that it is added as a thinner. 2. The thinning agent for coal-water slurry according to claim 1, for use in a coal-water slurry having a coal concentration of 61% or higher, preferably higher than 70%. 3. The thinner for coal-water slurry according to claim 1 or 2, wherein the coal is cleaned coal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56122166A JPS5823887A (en) | 1981-08-03 | 1981-08-03 | Viscosity reducing agent for coal-water slurry in high concentration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56122166A JPS5823887A (en) | 1981-08-03 | 1981-08-03 | Viscosity reducing agent for coal-water slurry in high concentration |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5823887A JPS5823887A (en) | 1983-02-12 |
| JPH0113517B2 true JPH0113517B2 (en) | 1989-03-07 |
Family
ID=14829209
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56122166A Granted JPS5823887A (en) | 1981-08-03 | 1981-08-03 | Viscosity reducing agent for coal-water slurry in high concentration |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5823887A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1997009399A1 (en) * | 1995-09-08 | 1997-03-13 | Central Research Institute Of Electric Power Industry | High-concentration coal/water mixture fuel and process for production thereof |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5880388A (en) * | 1981-11-09 | 1983-05-14 | Electric Power Dev Co Ltd | Production of highly concentrated pulverized coal slurry |
| JPS5958092A (en) * | 1982-09-29 | 1984-04-03 | Babcock Hitachi Kk | Preparation of coal slurry |
| JPS6243488A (en) * | 1985-08-21 | 1987-02-25 | Kawasaki Heavy Ind Ltd | Aqueous slurry composition of carbonaceous solid |
| JPS62149793A (en) * | 1985-12-24 | 1987-07-03 | Daicel Chem Ind Ltd | Solid fuel-water slurry composition |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5433803A (en) * | 1977-08-22 | 1979-03-12 | Hitachi Zosen Corp | Pulverized ore slurry composition |
| US4242098A (en) * | 1978-07-03 | 1980-12-30 | Union Carbide Corporation | Transport of aqueous coal slurries |
-
1981
- 1981-08-03 JP JP56122166A patent/JPS5823887A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1997009399A1 (en) * | 1995-09-08 | 1997-03-13 | Central Research Institute Of Electric Power Industry | High-concentration coal/water mixture fuel and process for production thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5823887A (en) | 1983-02-12 |
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