JPS59501163A - Finely divided carbon water dispersion system - Google Patents

Finely divided carbon water dispersion system

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Publication number
JPS59501163A
JPS59501163A JP50129082A JP50129082A JPS59501163A JP S59501163 A JPS59501163 A JP S59501163A JP 50129082 A JP50129082 A JP 50129082A JP 50129082 A JP50129082 A JP 50129082A JP S59501163 A JPS59501163 A JP S59501163A
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coal
dispersion system
water
dispersion
polymers
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JPH0248036B2 (en
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ステイグソン・ラルス・レンナ−ト
リンドマン・ビヨ−ン
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フルイドカ−ボン インタ−ナシヨナル アクテイエボラ−ク
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Priority claimed from PCT/GB1982/000107 external-priority patent/WO1982003417A1/en
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Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 石炭−水分散系 本発明は保存に非常に適しかつ輸送およびエネルギー生成に適した石炭−水分散 系に係る。よシ詳しく述べると、本発明は水、微粉砕石炭および添加物を含み、 石炭含分が60〜80重量係である分散系に係る。[Detailed description of the invention] Coal-water dispersion system The present invention provides a coal-water dispersion that is highly suitable for storage and suitable for transportation and energy production. Related to the system. More particularly, the present invention comprises water, pulverized coal and additives; It concerns a dispersion in which the coal content is between 60 and 80% by weight.

石炭分散系はかなり汚染が少なく、かつ固体石炭より取扱いが各易であり、しか も輸送や保存にともなう危険も除かれる。又、このような分散系は経済性の設点 からも好ましい。Dispersed coal is considerably less polluting and easier to handle than solid coal; It also eliminates the risks associated with transportation and storage. In addition, such a distributed system is an economical point. It is also preferable.

石炭分散系を用いる理由は基本エネルギー源゛として大規模に又眠気や熱を生オ するために小工場で石炭使用の増加か見ろまれでいるからである。これに関連し て、固体石炭の取扱いはいくつかの理由で困唯であり、従って一般的に石炭の液 体状態への変換が好lしい方法と考えられる。石炭を化学的に液体製品に変換す る所謂液化法ばlた石油に対抗できず、れている。石炙ヲ化学的て気体製品に変 換する所謂気化法は石炭全利用する好ましい方法であるように思われる。しかし ながら、この方法もその技術開発にかなり大・そい財価がさかれたにもかかわら ずまたかなり技術的に困難を残している。The reason for using coal dispersion is that it can be used on a large scale as a basic energy source, and also because it can produce sleepiness and heat. This is because small factories are reluctant to increase their use of coal. related to this However, solid coal is difficult to handle for several reasons, and therefore liquid coal is generally Conversion to a physical state is considered to be the preferred method. Chemically converting coal into a liquid product The so-called liquefaction method is unable to compete with oil. The stone roast is chemically transformed into a gaseous product. The so-called vaporization method for coal exchange appears to be the preferred method for total utilization of coal. but However, even though this method cost a considerable amount of money to develop the technology, However, there are still considerable technical difficulties.

石炭を液体状態に変換するもう一つの方法は物理的変換であり、本発明!fiこ の方法に関する。それは加熱油、メタノール、などのようなある種Ω有磯燃料、 または水からなる液体に石炭全分散することによって行なわれる。Another method of converting coal to a liquid state is physical conversion, and the present invention! Fi-ko Regarding the method. It uses some kind of heating oil, methanol, etc. Ariiso fuel, Alternatively, it is carried out by completely dispersing the coal in a liquid consisting of water.

微粉砕石炭の水分散系における問題は、主として、分散系を低粘度において安定 にすることにある。石炭分散系の保存あるいは輸送中に石炭粒子が沈澱してはな らない。さらに、石炭分散系は任意に僅か知変形した慣用技法音用いて燃焼する のに適するようにレオロジー的特注ヲ有すべきでありかつ高いポンプ操作性を持 つへきである。The problem with aqueous dispersions of pulverized coal is primarily to stabilize the dispersion at low viscosities. It is to make it. Coal particles should not settle during storage or transportation of the coal dispersion. No. Additionally, coal dispersions are optionally burned using slightly modified conventional techniques. The pump should have a customized rheology to suit the pump and have high pump operability. It is Tsuheki.

石炭−水分散系を安定化する先行する提案の中に、ノ連邦の刊行物Khim、  Pereab、 Topl、 1975 、30(2)。Among the earlier proposals for stabilizing coal-water dispersions are the Federal publication Khim, Pereab, Topl, 1975, 30(2).

19〜29頁、に記載さ几、かつChemi cal Abstracts87 :555326に要約されてた提案がある。この場合にはポリカルボ゛キシル酸 の塩およびポリホスフェートその他が安定剤として用いられている。最適の混合 物の粘度は石炭含分57〜63優における約5Pであり、従ってこの分散系、は 需要に対し満足でない。さらに、沈澱の安定性は不十分である。Pages 19-29, and Chemi cal Abstracts 87 There is a proposal summarized in :555326. In this case, polycarboxylic acid salts and polyphosphates and others have been used as stabilizers. optimal mix The viscosity of the product is about 5P at a coal content of 57-63, so this dispersion is Not satisfied with demand. Furthermore, the stability of the precipitate is insufficient.

スウェーデン国出願公開第7805632−2号公報(で、沈澱に対する安定化 作用が耐用の高分子電解質とりわけポリホスフェートで(上記ソ連邦刊行物に記 載されたものと同じ原理に従って)達成される石炭−水分散系が開示されている 。この場合も沈澱に対する安定化が十分ではない。Swedish Publication No. 7805632-2 (Stabilization against precipitation) Polyelectrolytes with durable action, especially polyphosphates (as described in the above-mentioned Soviet publications) A coal-water dispersion system is disclosed which is achieved (according to the same principles as those described). . In this case as well, stabilization against precipitation is insufficient.

米国特許第4,242.098号明細書けいくつかの水溶性ポリマー(ポリエチ レンオキシド、ポリアクリルアミド、など)の添加で安定化を達成する石炭−水 分散系を記載している。この分散系、′d前述の分散系よりも改良されている。U.S. Pat. No. 4,242.098 describes several water-soluble polymers (polyethylene Coal-water stabilization achieved by the addition of (ren oxide, polyacrylamide, etc.) Describes a dispersed system. This dispersion is an improvement over the previously described dispersion.

分散系の安定性の理論は、最近、かなり洗練された。その理論はより羨厚な系を 含むように発展したが、とりわけ新しいタイプの相互作用が検証された。The theory of stability of dispersion systems has recently been considerably refined. The theory suggests a more enviable system. It has evolved to include, but among other things, new types of interactions have been validated.

表面活性剤および高分子電解質による静電気的安定化やポリマーによる立体的安 定化のような従来から既知の作用の他に、更に中心の作用、所謂水利力がある。Electrostatic stabilization by surfactants and polyelectrolytes and steric stabilization by polymers In addition to the conventionally known effects such as stabilization, there is a further central effect, the so-called irrigation power.

この水利力は最近検証され、理論的にも説明された。この水利力が任意に他のタ イプの相互作用と共に上記のタイプの長期間安定石炭−水分散系を提供する本発 明の主たる基焚ヲ成す。この石炭−水盆散早は入手可能な技術全任意に僅かに変 形して使用して直接燃焼されるのに良く適している。本発明に依れば、この分散 系は請求の範囲第1項の特徴を得た。This water availability has recently been verified and explained theoretically. This irrigation power is optionally used by other water sources. The present invention provides a long-term stable coal-water dispersion of the type described above with It will form the main foundation of the Ming Dynasty. This coal-water basin dispersion rate may vary slightly depending on available technology. It is well suited to be used in the form and directly combusted. According to the invention, this dispersion The system has the characteristics described in claim 1.

この分散系は、犬きく低減した摩擦力で?ンデ操作され、・eイブライン中を輸 送することを許容するレオロジー的特ヰを有し、又とりわけ、凝集ならびに沈澱 ・・て対するかなり改良された安定曲を有する。This dispersion system has significantly reduced frictional force? was manipulated, and e-brine was imported. It has rheological properties that allow it to transport and, inter alia, to prevent flocculation and It has a much improved stability score for...

当然熱力学的て不安定である石炭−水分散系が安定rヒされている場合には、沈 澱2よび凝集の速度は粒子の吸引に対抗して作用するバリヤーの創出によって低 下される。この反発作用(は3つO主要原理:静電気的安定化、立体的安定比、 そして水利力による安定化、によって達成される。安定化は粒子のエネルギーを 変え、そして/または粒子の吸引を防止するバリヤーを創出する。こね−らの原 理・に基つくと、高含有量の石炭粒子を少量の有機添万0物の添加によって7に @vN中に安定1ヒすることか可能であり0新しいコロイドX k mlJ出す るためjf(tt−:、種子量の吸引力を最小化し、凝集および続いて起きる沈 殿に対して反発するバリヤーを発達させるような特ヰを系に付与する必要がある 。親水キポリマーによるある種の形の立体的安定化1は石炭−水分散系の長期間 安定性に好ましい条件を与える。If the coal-water dispersion system, which is naturally thermodynamically unstable, is stabilized, The rate of sludge and flocculation is reduced by the creation of a barrier that acts against particle attraction. It will be lowered. This repulsive action has three main principles: electrostatic stabilization, steric stability ratio, This is achieved through stabilization through water use. Stabilization reduces the energy of particles change and/or create a barrier that prevents the inhalation of particles. Konera no Hara Based on the theory, high-content coal particles can be reduced to 7 by adding a small amount of organic additives. @It is possible to have a stable 1 h during vN and release 0 new colloid X k mlJ In order to It is necessary to give the system a special feature that develops a barrier that repels the tongue. . Certain forms of steric stabilization by hydrophilic polymers1 provide long-term stability in coal-water dispersions. Provide favorable conditions for stability.

イオン性表面活性剤の系におけるラメラ液晶相の研究からそれらの相が膨潤し、 大量の水を取り込み得ることがわかった。これは表面活性剤の近隣する層の間の 水の層における反発警でよって説明され、又静電気的二重層の力に関係しよう。Studies of lamellar liquid crystal phases in ionic surfactant systems have shown that these phases swell and It was found that large amounts of water can be taken up. This occurs between adjacent layers of surfactant. This may be explained by the repulsion force in the water layer and may also be related to the force of an electrostatic double layer.

ホスホリピド5 (リン脂質)レシチンのような双性イオン物質では膨潤は著しくはないがしかし 非常に明瞭である。これjr−4純粋な電荷が存在しない場合でもかなりの反発 が存在することを示す。この反発力即ち所謂水和力は2〜3久の偏差を持って距 離と共にほぼ指数関数的に変化する。この力は一般的な性質のものであり、アル キル鎖の長さとかアルキル鎖の物理的状態(液体とか固体)とかてよって変化せ ず、多量荷電の(quantity charged )表面活性剤を系に含め た場合にも存在する。水利力は相互に数オングストローム離れた表面の間に働く 力全直接に測定することによっても検証された。水利力の理論モデルが最近考案 さね1、それによって、水和力を有功誘電定数が変化している界面における所謂 ミラーチャ−ノの存在に結びつけることが可能になった。双性イオン基によるそ うしたミラーチャージはミクロ2よひマクロの不均質系て共通である。これは本 発明において低誘覗改拗買の懸濁液に所望の特叶全付与するために利用される。phospholipid 5 (Phospholipids) Zwitterionic substances such as lecithin do not cause significant swelling, but Very clear. This jr-4 has considerable repulsion even in the absence of pure charge indicates the existence of This repulsive force, or so-called hydration force, has a deviation of 2 to 3 years over the distance. It changes almost exponentially with distance. This force is of a general nature and It varies depending on the length of the kill chain and the physical state of the alkyl chain (liquid or solid). First, a quantity charged surfactant is included in the system. It also exists in cases where Irrigation forces act between surfaces several angstroms apart from each other It was also verified by directly measuring the total force. A theoretical model of water utilization has recently been devised. 1, thereby increasing the hydration force to the so-called at the interface where the effective dielectric constant is changing. It became possible to link it to the existence of Miracciano. Due to the zwitterionic group Such mirror charges are common in micro-2 and macro-heterogeneous systems. this is a book In the invention, it is used to impart a desired special effect to a low-intensity suspension.

そのとさ、レシチンのような双性イオン表面活性剤全固体粒子の表面に吸着し得 る。すると、粒子間の強い反発力か近距離に存在する。従ってこの原理i 71 1厚な分散系にとって特別に有用である。However, zwitterionic surfactants such as lecithin can be adsorbed onto the surface of all-solid particles. Ru. Then, there is a strong repulsive force between the particles or they exist at a short distance. Therefore, this principle i71 1 is particularly useful for thick dispersions.

以下例を参照して本発明を更に詳細に説明する。The invention will be explained in more detail with reference to the following examples.

例 ■ レシチンまた(rlアルキルベタインのようなミセル非形成双性イオン表面 活↑生剤(従って、これは比較的水に溶解しにくい)を最初に有廐溶剤に溶解す る。溶剤は例えばオクタツール、ヘキサデカンまたはメタノールからなり得、適 当な仕方で回収し得、あるいは僅かて分散剤全音み得る。example ■Lecithin or (non-micelle-forming zwitterionic surface such as rl alkyl betaine) The active agent (therefore it is relatively insoluble in water) is first dissolved in the aqueous solvent. Ru. The solvent may, for example, consist of octatool, hexadecane or methanol, and It can be recovered in a proper way, or even just a little bit of the dispersant can be removed.

2 微粉砕石炭および水の分散系に、調製した表面活性剤を添加する。石炭粉末 の適当な大きさは広い粒径分布を持って(多分散石炭粉末)1〜200μmであ る。粒径および粒径分布は所望な安定性テ応じて選択でさる。粒径が小さいほど 、安定イ:ハ大きいか石炭を超マイクロメートルの粒径に粉砕するとと:q高価 である。粒子濃度は広い範囲で変わり得る。2. Add the prepared surfactant to the dispersion of pulverized coal and water. coal powder The suitable size is 1-200 μm (polydisperse coal powder) with a wide particle size distribution. Ru. The particle size and particle size distribution are selected depending on the desired stability. The smaller the particle size , Stable: C: When large coal is crushed to ultra-micrometer particle size: Q: Expensive. It is. Particle concentration can vary over a wide range.

経、斉2よひ技術的側面を考えると粒子濃度は場合に応じて最適なものにすべさ である。乾燥物質含有量65〜75重量係の石炭−水分散系は(例えば・やイブ ラインで輸送するために)良好なレオロジー的特a7c有しているので特に有益 である。最大の石炭含有量(70〜80重量%)全達成するため(では粒径分布 を特に考慮に入れなければならない。普通の場合Kj4、これは、異なる粒径の 粒子を充填するときに最も自由空間が少なくなるようにする単純な幾何学的計算 に基づいて為し得る。Considering technical aspects, the particle concentration should be optimized depending on the situation. It is. Coal-water dispersions with a dry matter content of 65-75% by weight (e.g. Particularly useful as it has good rheological properties (for transport in lines) It is. In order to achieve the maximum coal content (70-80% by weight), the particle size distribution must be taken into particular consideration. In the normal case Kj4, which is A simple geometric calculation to ensure the least free space when packing particles It can be done based on.

吸着工程の後、ある種の形の立体バリヤーを与えるため:(、又粒子間の摩擦を 低減するために、2種また・ばそれ以上の親水性塩イ万ンおよび非イオンポリマ ーを分散系に・奈卯する。それは例えばポリエーテル、ポリサラ刀すド、ポリア ルコール、7f!lJアクリラートの中から選択することができる。本発明に依 り特(c、適しているのはポリエチレンオキシド、ポリエチレンオキシドーポリ プロピレンオキシドタイプの共重合体、カルボキンメチルセルロース、キサンタ ンがムがある。全重量基阜の重量部でポリマー濃度I′io、1〜5%であり得 るが経済的には約05係か最適である。After the adsorption step, to provide some form of steric barrier: (also to reduce friction between particles) In order to reduce the - into a distributed system. For example, polyether, polysaratosudo, polya Lecole, 7f! One can choose from lJ acrylates. Relying on the present invention (c) Suitable materials are polyethylene oxide and polyethylene oxide polyester. Propylene oxide type copolymer, carboquine methylcellulose, xantha I have a hard time. Polymer concentration I'io in parts by weight based on total weight, which can be from 1 to 5% However, from an economical point of view, the optimum value is about 05.

分散系を油の非汚染物質としてもつと魅力的なものにするため:(ある種のアル カリ塩またはアルカリ土類金属の塩を分散液に添加し得る。塩は水酸[ヒカルシ ウムまたはドロマイト粉末であることが好適である。塩ri然科の酸化で発生す る酸キガス成分全中和し、粒子分離機(particle percipita tor )で回収でさる。To make the dispersion attractive as a non-contaminant of oil: Potassium salts or alkaline earth metal salts may be added to the dispersion. Salt is hydroxy acid [Hikarushi] Dolomite powder is preferred. Generated by natural oxidation of salt The acid gas component is completely neutralized, and the particle separator (particle percipita Collect it with tor).

水が分散系から蒸発するのを防止するためにその界面に単分子膜を形成する助剤 を分散系に添加し得る。そのような助剤にはセチルアルコールやヘキサデカノー ルがある。Auxiliary agent that forms a monolayer at the interface to prevent water from evaporating from the dispersion. may be added to the dispersion. Such adjuvants include cetyl alcohol and hexadecano. There is a le.

本発明は水溶液中の石炭粒子を安定化する従来技術よりも実質的て有利である。The present invention has substantial advantages over prior art techniques for stabilizing coal particles in aqueous solutions.

ポンプ操作用に好適なレオコノ−的特性と結び付いた優れた沈澱安定件のためて 、得られる分散系な例えば化学工業で使用するためちるいは直接エネルギー生成 のため1(導管または・ξイブラインで適当な仕方にて輸送するのによく適して いる。Due to excellent sedimentation stability combined with rheoconotic properties suitable for pump operation The resulting dispersion can be used for example in the chemical industry for direct energy generation. 1 (well suited for transport in a suitable manner in conduits or lines) There is.

重油用に設計したボ゛イラーにおける燃焼試験は分散系が重油を全部または一部 分置き換えるのて非常に適していることを示した。Combustion tests in boilers designed for heavy oil are conducted when the dispersion system absorbs all or part of the heavy oil. It was shown that it is very suitable for replacing parts.

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Claims (1)

【特許請求の範囲】 1 石炭粒子の表面て吸着されかつ石炭粒子間に水利力による反発を与える少な くとも1種類O両親媒性物質と;該両親媒性物質と共働しかつ少なくとも1種類 の2リマーが疎水:生および親水性の性質を有するポリマーと;1含有すること を特徴とし、石炭含有分が60〜80重量係である水、微粉砕石炭および添加吻 を含む分散系。 2 前記両親媒性物質がレシチンまたはその他O双性イオン表面活性剤であるこ とを特徴とする請求の範囲第1項記載の分散系。 3 前記ポリマーのうち1種類が、ポリエチレンオキシドの方が支配的量である ポリエチレンオキノドとポリエチレンオキシドの共重合体であることを特徴とす る請求の範囲第1項記載の分散系。 4 前記共重合体の分子量が5000〜50,000であることを特徴とする請 求の範囲第3項記載の分散系。 5 前記共重合体が少なくとも70重量楚のポリエチレンオキノドを含有し、分 子量が8000〜15.000であることを特徴とする請求の範囲第4項記載の 分散系。 6 前記ポリマーのうち1種類がポリサツカリドであることを特徴とする請求の 範囲第1項記載の分7 前記ポリサツカリドがキサンタンガムまたはグアーコ゛ ムであることを特徴とする謂采の範囲第6項記載の分散系。 8 添加剤の合計量が2重量係未満であることを特徴とする請求の範i用、嶋1 項記載の分散系。[Claims] 1. A small amount of water that is adsorbed on the surface of coal particles and causes repulsion between the coal particles due to the water utilization force. at least one type of O amphipathic substance; cooperating with said amphipathic substance and at least one type 2 polymers with hydrophobic: polymers with hydrophilic and hydrophilic properties; characterized by water, pulverized coal and additives with a coal content of 60 to 80% by weight. A distributed system containing 2 The amphipathic substance is lecithin or other O zwitterionic surfactant. The dispersion system according to claim 1, characterized by: 3 One of the polymers has a predominant amount of polyethylene oxide Characterized by being a copolymer of polyethylene oxide and polyethylene oxide The dispersion system according to claim 1. 4. A claim characterized in that the molecular weight of the copolymer is 5000 to 50,000. The dispersion system according to item 3 of the desired scope. 5. The copolymer contains at least 70% by weight of polyethylene oxide; Claim 4, characterized in that the molecular weight is 8,000 to 15,000. Distributed system. 6. A claim characterized in that one of the polymers is polysaccharide. Item 7 as described in Range 1: The polysaccharide is xanthan gum or guarco. 6. The dispersion system according to item 6, characterized in that the dispersion system is 8 Shima 1 for claim i, characterized in that the total amount of additives is less than 2 parts by weight Dispersion system described in section.
JP50129082A 1981-08-03 1982-04-05 Finely divided carbon water dispersion system Granted JPS59501163A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8104645-0 1981-08-03
PCT/GB1982/000107 WO1982003417A1 (en) 1981-04-08 1982-04-08 Improvements in and relating to the lining of sewers,pipes,or the like

Publications (2)

Publication Number Publication Date
JPS59501163A true JPS59501163A (en) 1984-07-05
JPH0248036B2 JPH0248036B2 (en) 1990-10-23

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Application Number Title Priority Date Filing Date
JP50129082A Granted JPS59501163A (en) 1981-08-03 1982-04-05 Finely divided carbon water dispersion system

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JP (1) JPS59501163A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2393053A1 (en) * 1977-05-31 1978-12-29 Scaniainventor Ab AQUEOUS DISPERSION OF SPRAYED COAL USEFUL AS A LIQUID FUEL AND ITS PREPARATION PROCESS
US4242098A (en) * 1978-07-03 1980-12-30 Union Carbide Corporation Transport of aqueous coal slurries
JPS5643394A (en) * 1979-09-14 1981-04-22 Lion Corp Dispersant for mixed fuel
JPS5657888A (en) * 1979-10-17 1981-05-20 Lion Corp Dispersing agent for mixed fuel
JPS5657887A (en) * 1979-10-17 1981-05-20 Lion Corp Dispersing agent for mixed fuel

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2393053A1 (en) * 1977-05-31 1978-12-29 Scaniainventor Ab AQUEOUS DISPERSION OF SPRAYED COAL USEFUL AS A LIQUID FUEL AND ITS PREPARATION PROCESS
US4242098A (en) * 1978-07-03 1980-12-30 Union Carbide Corporation Transport of aqueous coal slurries
JPS5643394A (en) * 1979-09-14 1981-04-22 Lion Corp Dispersant for mixed fuel
JPS5657888A (en) * 1979-10-17 1981-05-20 Lion Corp Dispersing agent for mixed fuel
JPS5657887A (en) * 1979-10-17 1981-05-20 Lion Corp Dispersing agent for mixed fuel

Also Published As

Publication number Publication date
JPH0248036B2 (en) 1990-10-23

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