JPS59204690A - Stabilizer for mixed fuel - Google Patents

Stabilizer for mixed fuel

Info

Publication number
JPS59204690A
JPS59204690A JP7911283A JP7911283A JPS59204690A JP S59204690 A JPS59204690 A JP S59204690A JP 7911283 A JP7911283 A JP 7911283A JP 7911283 A JP7911283 A JP 7911283A JP S59204690 A JPS59204690 A JP S59204690A
Authority
JP
Japan
Prior art keywords
stabilizer
mixed fuel
coal
fuel
derivative
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
JP7911283A
Other languages
Japanese (ja)
Inventor
Shinichi Watanabe
伸一 渡辺
Taizo Igarashi
泰蔵 五十嵐
Yasuhiro Kiyonaga
清永 康博
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.)
Lion Corp
Kao Corp
NOF Corp
Original Assignee
Lion Corp
Kao Corp
NOF Corp
Nippon Oil and Fats Co 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 Lion Corp, Kao Corp, NOF Corp, Nippon Oil and Fats Co Ltd filed Critical Lion Corp
Priority to JP7911283A priority Critical patent/JPS59204690A/en
Publication of JPS59204690A publication Critical patent/JPS59204690A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:A stabilizer for mixed fuel that contains, as an active ingredient, a polyether derivative of a specific alkylene oxide adduct, thus giving the fuel high stability in long-term standing, mechanical stability, fluidity and storage stability at high temperatures. CONSTITUTION:The objective stabilizer contains, as an active ingredient, a polyether derivative resulting from reaction between (A) a polyether of an adduct of an alkylene oxides containing ethylene oxide as an essential component to an N6-300 polyalkylenimine or its derivative and (B) a 7-23C fatty acid. The stabilizer is added to a mixed fuel generally in an amount of 0.01-0.15wt%, preferably 0.05-0.125wt%.

Description

【発明の詳細な説明】 本発明は石炭微粉末と燃料油との混合燃料用安定剤、%
に長期間にわたる静的安矩性に加えて、機械的な安定性
と流動性に後れ、更に高温での保存安定性にも優れた混
合燃料を装造1−るために使用される安定剤に関1゛る
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a stabilizer for mixed fuel of fine coal powder and fuel oil,
In addition to long-term static stability, it is a stable fuel used to create mixed fuels that have good mechanical stability and fluidity, and also have excellent storage stability at high temperatures. Regarding drugs.

近年、エネルギー源として最も重要な位Ikヲ占める石
油燃料が高騰するとともに、石油埋蔵蓋の限界が強く認
識されてぎたことから、長期にわたるエネルギー源確保
かエネルギー政策上の重要問題になってきた。このよう
なことから、エネルギー源として石油と並んでfiff
ikの太きい石炭か再び注目されるようになった。
In recent years, the price of petroleum fuel, which is the most important energy source, has soared, and the limits of oil reserves have become acutely recognized, so securing a long-term energy source has become an important issue in energy policy. For this reason, fif is used as an energy source along with oil.
IK's thick coal is once again attracting attention.

しかしながら、石炭の場合は、液状の石油とは異なり、
塊状物であるため、輸送や貯蔵のコストが高(、しかも
取扱いが著しく不便であるという欠点かある。このよう
な取扱い上の欠点を改善するためr(、石戻乞微粉末化
し、水や燃料油に分散させてスラリー状の燃料として使
用する方法か極々検討されている。微粉戻ン燃料油中に
分散させた石炭/油混合燃料は、水に分散させたものよ
りも、単位童画りの発熱量か大きく、工不ルキー源とし
てはより好ましいか、実用に供するためr(は種々の問
題かある。
However, in the case of coal, unlike liquid petroleum,
Since it is a lump, it has the drawbacks of high transportation and storage costs (and also extremely inconvenience in handling). A method of dispersing it in fuel oil and using it as a slurry fuel is being studied extensively.Coal/oil mixed fuel dispersed in finely recycled fuel oil has a higher unit density than one dispersed in water. Since the calorific value of R is large, there are various problems such as whether it is preferable as a source of industrial energy or whether it is suitable for practical use.

火力発゛亀などr(おいては多量の燃料か必要とされる
が、このような多量の燃料の輸送及び貯蔵は、タンカー
による輸送や、大型陸上タンクによる貯蔵が普辿である
。ところか、石炭/油混合燃料は製造されてから燃焼さ
れるまでのノくイブ移送、タンク貯蔵、輸送等のそれぞ
れの工程で種々の外力、例えは遠心ポンプやスクリュー
ポンプ等の移送ポンプによる剪断力、貯蔵タンクのサイ
ド攪拌やタンクからの燃料排出〜・の再流動化攪拌、船
舶輸送における振動、発熱量を一定に保持するための燃
焼前の均質化撹仔等の機械力を受ける。かかる銀械的履
歴を経ると、混合燃料中の石炭が分離して沈降圧密現象
を生じやすいという問題があり、沈降圧密した混合燃料
は流動性を失い、実際上その取扱いは小川能に近い。従
って、石炭/油混合燃料を実用に供するには、貯蔵時の
静的安定性は勿論のこと、かかる機械的安定性と流動性
を改良し7より゛れはンよらない。
Thermal power plants, such as turtles, require large amounts of fuel, and such large amounts of fuel are commonly transported and stored by tankers or by large land tanks. Coal/oil mixed fuel is subjected to various external forces during each process from production to combustion, such as fuel transfer, tank storage, and transportation, such as shearing force caused by transfer pumps such as centrifugal pumps and screw pumps, Such silver machines are subjected to mechanical forces such as side agitation of storage tanks, refluidization agitation of fuel discharged from tanks, vibration during ship transportation, and homogenization agitation before combustion to maintain a constant calorific value. There is a problem that the coal in the mixed fuel separates and tends to cause sedimentation consolidation phenomenon after a long history, and the mixed fuel that has undergone sedimentation and consolidation loses fluidity, and in practice its handling is similar to that of Ogawa Noh.Therefore, coal In order to put a /oil mixed fuel into practical use, it is necessary to improve not only the static stability during storage but also the mechanical stability and fluidity.

特開昭53−55305、同54−52105、同54
−52105、同54−53107、同57−1654
90号谷公報には混合燃料用安定剤としてポリフルキレ
ンオキシド基な含むポリエーテル化合物等が開示されて
いる。しかしこのような化合物の性能は効果を発現させ
るための添加量が多かったり、混合燃料の保存温度は7
0℃以下、保存条件は靜籠状愈が必要であるという大き
な欠点があった。支にへ体的には、添加量か多い場合は
に済的に不利であり混合燃料の経済メリットが失われる
。又、保存温度を高温(’70℃以上)Kできないため
に粘度が高(石炭龜#を上昇させることが望めずこれも
同a K q;経済である。又、静置状態が心安である
ということは、加昇からのタンカーによる輸送(ローリ
ング、ピッチング等の振動が長期にわたって与えられる
)が困難であるということである。このような現象は混
合燃料の実用化の上で大きな障害となっていた。
JP-A No. 53-55305, No. 54-52105, No. 54
-52105, 54-53107, 57-1654
Patent No. 90 discloses polyether compounds containing polyfulkylene oxide groups as stabilizers for mixed fuels. However, the performance of such compounds requires a large amount of addition to achieve the effect, and the storage temperature of the mixed fuel is 7.
A major drawback was that it required storage conditions of 0° C. or lower and a cage-like condition. In terms of support, if the amount added is too large, it is economically disadvantageous and the economic benefits of the mixed fuel are lost. In addition, since the storage temperature cannot be kept at a high temperature (above 70°C), the viscosity is high (it is not possible to increase the coal porosity, which is also economical. Also, it is safe to leave it standing still). This means that it is difficult to transport the mixed fuel by tanker (which is subject to long-term vibrations such as rolling and pitching).Such phenomena pose a major obstacle to the practical application of mixed fuel. was.

本発明者等は、このような欠点を改良すべく鋭意研究し
た結呆、ポリフルキレンイミンマタはその14体にフル
キレンオキシドを付加したポリエーテル化合物を脂肪酸
によりエステル化することで比較的少ない添加量で優れ
た効果を発揮し、又粒度分布や調整条件等に左右されな
い画期的な性能を示すことを見い出し本発明に到達した
The inventors of the present invention have conducted intensive research to improve these drawbacks, and the polyfulkylene imine mata has been developed by esterifying a polyether compound in which fullkylene oxide is added to 14 of the polyether compounds with fatty acids, thereby reducing the addition of relatively small amounts of polyfulkylene imine. The present invention was achieved by discovering that it exhibits excellent effects regardless of the amount and exhibits revolutionary performance that is independent of particle size distribution, adjustment conditions, etc.

これは分子末端に疎水基であるフルキル基をエステル結
合により尋人することにより石炭表面の疎水部との親和
性が良好となり、石炭表面への吸着が飛躍的に改良され
るためであろうと考えられる。
This is thought to be because the addition of a hydrophobic furkyl group to the end of the molecule through an ester bond improves affinity with the hydrophobic part of the coal surface, dramatically improving adsorption onto the coal surface. It will be done.

本発明の分散安定剤は屋素原子6〜300個を含むポリ
フルキレンイミン又はその誘導体にエチレンオキシドを
必須として含むフルキレンオキシドを付加し、かつポリ
オキシエチレン鎖の部分の合計の重量が全分子量の4〜
50に童%であり、さらに分子量がi o、o o o
〜600,000であるポリエーテル化合物に脂肪酸を
反応させて得られるポリエーテル化合物訪導体ン有効成
分とし【含むこと1f!:%徴とするものである。
The dispersion stabilizer of the present invention is obtained by adding a fullylene oxide containing ethylene oxide as an essential component to a polyfulkylene imine containing 6 to 300 yatom atoms or a derivative thereof, and in which the total weight of the polyoxyethylene chain portion is the total molecular weight. 4~
50%, and the molecular weight is i o, o o o
~600,000 polyether compound obtained by reacting a fatty acid with a polyether compound as an active ingredient [Contains 1f! : It is expressed as a percentage.

ポリエーテル化合物はポリアルキレンイミン又はその誘
導体に通常の方法によりエチレンオキサイドを必須とし
て含むフルキレンオキシドを付加することにより容易に
得ることができる。
A polyether compound can be easily obtained by adding fullkylene oxide, which essentially contains ethylene oxide, to a polyalkylene imine or a derivative thereof by a conventional method.

そのウチ特にエチレンオキシドとグロビレンオキシドと
のプルツク又は一部ブロック状の付加物が好ましくその
付加の順序はいずれが先でもよいが、プルピレンオキシ
ド(以後poと略記′3−る。)を先Kt9加させた後
エチレンオキシド(以後Eoと略記する。)ン付加させ
た場合が良好な分散安定性?示す。
In particular, a pull or partially block adduct of ethylene oxide and globylene oxide is preferred, and the order of addition may be in any order, but propylene oxide (hereinafter abbreviated as po) is added first. Is dispersion stability better when ethylene oxide (hereinafter abbreviated as Eo) is added? show.

次にこれらのポリエーテル化合物に脂肪酸を通常の方法
により反応させてポリエーテル化合物誘導体が得られる
が、その除梗われる脂肪酸は、炭系数7〜26個である
ことが好ましいが二重結合の数、枝分かれ尋は性能上影
譬はない。
Next, a polyether compound derivative is obtained by reacting these polyether compounds with a fatty acid by a conventional method. The fatty acid to be destemmed preferably has a carbon number of 7 to 26, but the number of double bonds is , there is no effect on the performance of branching.

ポリエーテル化合物の分子量は10,000〜600、
OD Oであり好ましくは15,000〜400.00
0である。またポリオキシエチレン鎖の部分の合計の!
M蓋は全分子量の4〜50i童%である。
The molecular weight of the polyether compound is 10,000 to 600,
OD O, preferably 15,000 to 400.00
It is 0. Also of the sum of the parts of the polyoxyethylene chain!
The M lid is 4-50 i% of the total molecular weight.

本発明り安定剤は混合燃料に対して0.01〜0.15
皇蚕%、好筐しくは0.05〜0.125重世%添加す
ることにより、燃料油中に石炭粒子乞安定に分散させる
ことができる。
The stabilizer of the present invention is 0.01 to 0.15 for mixed fuel.
By adding 0.05% to 0.125% of Japanese silkworms, preferably 0.05 to 0.125% of Japanese silkworms, coal particles can be stably dispersed in fuel oil.

又、本発明の安定剤を添加した混合燃料は保存温L70
〜150℃のl’iJでも3ケ月以上安定性が良好であ
り、罎製直後にプロペラ撹拌等の悪条件下でも極めて安
定性か良好であった。
Furthermore, the mixed fuel to which the stabilizer of the present invention has been added has a storage temperature of L70.
Even at l'iJ of ~150°C, the stability was good for more than 3 months, and the stability was extremely good even under adverse conditions such as propeller stirring immediately after the can production.

本発明の安定剤は前記有効数5分の他に、心太に応じ℃
他の昇面活性剤ン逸鉦加えることかできる。
In addition to the above-mentioned effective number of 5 minutes, the stabilizer of the present invention can be used depending on the thickness of the core.
Other surfactants can be added.

本発明の安定剤を用いて石炭欠油中VC分散させるには
、例えば前記安定剤を燃料油に溶解させたのち微粉炭と
混合しても、安定剤を微粉炭と燃料油との混合物に添加
して混合してもよい。
In order to disperse VC in coal-depleted coal using the stabilizer of the present invention, for example, the stabilizer may be dissolved in fuel oil and then mixed with pulverized coal, or the stabilizer may be added to a mixture of pulverized coal and fuel oil. It may be added and mixed.

本発明の安定剤を疾加混合づる渦fは任意であり、例え
は50〜150℃で混合され7)。温合圧力は常圧でも
よいが、混合燃料の脱気欠″′3−るために減圧にして
もよい。
The vortex f for rapidly mixing the stabilizer of the present invention is optional, for example, at 50 to 150°C 7). The heating pressure may be normal pressure, but it may be reduced pressure to avoid deaeration of the mixed fuel.

混合燃料成分としての石炭とじてを工、無煙炭、歴青炭
、褐炭など種々の炭他のものか使用され、その平均粒径
は、2m常100ミクロン以下であり、好ましくは20
0メツシュ篩通過Mb’a%以上がよい。重油としては
原油、重油、軽油、カンリンなどの任意の灰化水素油か
通用されるが、経済的には、原油や重油の使用か1駒で
ある。
As a mixed fuel component, various coals such as coal, anthracite, bituminous coal, lignite, etc. are used, and the average particle size is usually less than 100 microns, preferably 200 μm.
0 mesh sieve passing Mb'a% or more is preferable. As the heavy oil, any hydrogen ash oil such as crude oil, heavy oil, light oil, or kanlin can be used, but from an economic point of view, it is best to use crude oil or heavy oil.

混合燃料中の石炭と油の混合割合は必要とされる流動性
、安定性及び保存温度に依存する。
The mixing ratio of coal and oil in the blended fuel depends on the required fluidity, stability and storage temperature.

これまで開示された安定剤では保存温度か70℃前後に
限定されるため石炭濃度は50〜60wt%か限界であ
った。つまり60wt%以上になると粘度が急激に増大
し流動性を失う。ところが本発明の安定剤は70℃〜1
50℃の高温保存安定性に侵れるため石炭濃度を60〜
zowt%まで上昇させることが可能となった。
In the stabilizers disclosed so far, the storage temperature is limited to around 70°C, so the coal concentration has been limited to 50 to 60 wt%. In other words, when it exceeds 60 wt%, the viscosity increases rapidly and fluidity is lost. However, the stabilizer of the present invention has a temperature of 70°C to 1
The coal concentration should be set at 60~ because the high temperature storage stability of 50℃ is affected.
It became possible to increase it to zowt%.

本発明の安定剤を用いて、微粉炭、燃料油及び安定剤か
らなる石炭/油混合燃料を製造する場合、それらの各成
分の添加方法やtilt序あるいは混合を行なうための
撹拌機及び攪拌条件は、前記安定剤の作用が特に阻害さ
れない限り、制約されない。
When producing a coal/oil mixed fuel consisting of pulverized coal, fuel oil, and stabilizer using the stabilizer of the present invention, the addition method of each component, the tilt order, the stirrer and stirring conditions for mixing, etc. is not restricted as long as the action of the stabilizer is not particularly inhibited.

次に本発明を実施例により更VC詳細に説明する。尚、
実施例に示した「部」及びU%」は、いずれも取量基準
である。
Next, the present invention will be explained in further detail with reference to examples. still,
Both "part" and "U%" shown in the examples are based on the amount taken.

実施例 中東重油*’  iso、4y(油中に含まれ、ろ水分
は除いて〕を500 mlの容器中に入れ、史に表1−
1及び1−2に示す各柚女定A(jの所定蓋を夫々加え
、100℃のオイルバス中に浸す。200メツシユの篩
Yi(80%パスするように粉砕したベルモントtf2
 aooJ!(石炭中に名まれろ水分は除いて)を上記
の中東重油中に加える。中東重油中K O,03%、ベ
ルモント炭中K 3.25%の水が含まれているので、
石炭(乾燥分)/(中東重油士水) = 6o/4o 
(KM比)と7よる。
Example Middle East heavy oil*' iso, 4y (contained in the oil, excluding filtration water) was placed in a 500 ml container and poured into a container according to Table 1-
1 and 1-2, add the prescribed lids of each yuzumei A (j) and immerse them in an oil bath at 100°C.
aooJ! (excluding the moisture in the coal) is added to the above Middle East heavy oil. Middle East heavy oil contains K O, 03%, and Belmont coal contains K 3.25% water.
Coal (dry)/(Middle East heavy oil tanker water) = 6o/4o
(KM ratio) and 7.

即ち油と石炭中に含まれ℃いた水の鳳の合計は19.5
5.9である。安定剤を含む油と石R+入れた容器を1
00℃のオイルバス中に1時間没すと一定温度になる。
In other words, the total value of water contained in oil and coal is 19.5
It is 5.9. 1 container containing oil containing stabilizer and stone R+
When immersed in an oil bath at 00°C for 1 hour, the temperature becomes constant.

ラボミキサー(特殊機化工[)を用い、一定温度に1よ
った石炭と藺の混合物’t’ 6000 rpmで60
分間撹拌した。続いて攪拌機をプロペラ羽根に交換し、
90 rpmで72F#Pl!1PIt拌し、機械的履
歴を与えた混合燃料を―製し、安定性試験に供し7C。
Using a lab mixer (Tokushu Kikako), mix the coal and straw mixture at a constant temperature of 600 rpm at 6000 rpm.
Stir for a minute. Next, replace the agitator with a propeller blade,
72F#Pl at 90 rpm! A mixed fuel that had been stirred for 1 PIt and given a mechanical history was prepared and subjected to a stability test at 7C.

安定性試鹸 試験装置として、内径5.3鋤、尚さ24薗のステンレ
ス製シリンダーで、その底部から6 J12礪、18o
IILの各位置に流体の止栓句取出口を有するものを用
いる。このシリンダーに底部から18薗の尚さまで上記
の様にして調製した各種混合燃料の一定量を入れ、10
0℃の恒温槽に入れて90日間静匝1−る。90日経過
後、このシリンダーの底部から12−の位置の止栓をは
ずしそれより上の混合燃料(即ち底部から高さ12〜1
B−の個9rのシリンダー内の混合燃料)を取り出して
上層試料とし、その石炭嫉度を御」定した。eKK底部
から6薗の位置の止栓をは′J’ Lこの位置より上に
ある混合燃料を取り出し、中層試料としてその石炭論度
を測魔した。
The stability test soap test device is a stainless steel cylinder with an inner diameter of 5.3 mm and a diameter of 24 mm.
An IIL having a stopper outlet for fluid at each position is used. Pour a certain amount of the various mixed fuels prepared as above into this cylinder from the bottom up to 18 mm, and
Place in a constant temperature bath at 0°C and stand still for 90 days. After 90 days have elapsed, remove the stopper at the 12- position from the bottom of the cylinder and remove the mixed fuel above it (i.e., at a height of 12-1 from the bottom).
The mixed fuel in the cylinder of B-9r was taken out and used as an upper layer sample, and its coal jealousy was determined. The stopcock located 6 meters from the bottom of the eKK was 'J' L. The mixed fuel above this position was taken out and its coal density was measured as a middle layer sample.

最後に残存混合燃料な壜り出し、下層試料として石炭製
置をdll」定した。石炭銭度の測定は、混合燃料K 
1,1.1− ) !Jジクロロタンを加えて本油分y
=f&牌、を過して除去し、残置の石灰分の最初の混合
燃料Vζ対する比率乞嵐量パーセントで永めた。これら
の精米な表−2に示す。各層での右脚濃度の差が小さい
程機械的安矩、性の良い混合燃料であることを示す。
Finally, the remaining mixed fuel was removed from the bottle, and the coal was used as a sample of the lower layer. The measurement of coal density is based on mixed fuel K.
1,1.1-)! Add J dichlorothane and add real oil y
= f & tiles, and the remaining lime content was increased by the ratio of the remaining lime content to the initial mixed fuel Vζ. These polished rice varieties are shown in Table 2. The smaller the difference in right leg concentration in each layer, the better the mechanical stability and performance of the mixed fuel.

*1: 中東重油(中東産):*1: Middle East heavy oil (produced in the Middle East):

Claims (1)

【特許請求の範囲】 1、 窒素原子6〜600個を含むポリフルキレンイミ
ンまたはその誘導体にエチレンオキシドを必須として含
むアルキレンオキシドを付加し、かつポリオキシエチレ
ン鎖の部分の合計の重置か全分子量の4〜50東童%で
あり、さらに分子量か10,000〜600,000で
あるポリエーテル化合物に脂肪酸を反紀、させて惰たポ
リエーテル化合物誘導体を有効成分として含むことを%
徴とする混合燃料用安定剤。 2、 ポリアルキレンイミンまたはその誘導体がポリエ
チレンポリアミンとエチレンイミンとの反応物、及び/
又はエチレンイミンの重合物であるポリエチレンイミン
である特許請求の範囲第1項記載の安定剤。 3、 ポリエーテル化合物誘導体か、エチレンオキシド
とエチレンオキシド以外のアルキレンオキシドとのブロ
ック状又は一部ブロック状の付加物である特許請求の範
囲第1項配賊の混合燃料用安定剤。 4、ポリエーテル化合物中のフルキレンオキシドがエチ
レンオキシドとプロピレンオキシドである特許請求の範
囲第1項、第2項又は第3項記載の混合燃料用安定剤。
[Claims] 1. An alkylene oxide containing ethylene oxide as an essential component is added to a polyfulkylene imine containing 6 to 600 nitrogen atoms or a derivative thereof, and the total weight of the polyoxyethylene chain portions or the total molecular weight is The active ingredient is a polyether compound derivative obtained by adding a fatty acid to a polyether compound having a molecular weight of 10,000 to 600,000.
Stabilizer for mixed fuel with special characteristics. 2. Polyalkyleneimine or its derivative is a reaction product of polyethylene polyamine and ethyleneimine, and/
The stabilizer according to claim 1, which is polyethyleneimine, which is a polymer of ethyleneimine. 3. The stabilizer for mixed fuel according to claim 1, which is a polyether compound derivative or a block-like or partially block-like adduct of ethylene oxide and an alkylene oxide other than ethylene oxide. 4. The stabilizer for mixed fuel according to claim 1, 2 or 3, wherein the fullkylene oxide in the polyether compound is ethylene oxide and propylene oxide.
JP7911283A 1983-05-06 1983-05-06 Stabilizer for mixed fuel Pending JPS59204690A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7911283A JPS59204690A (en) 1983-05-06 1983-05-06 Stabilizer for mixed fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7911283A JPS59204690A (en) 1983-05-06 1983-05-06 Stabilizer for mixed fuel

Publications (1)

Publication Number Publication Date
JPS59204690A true JPS59204690A (en) 1984-11-20

Family

ID=13680819

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7911283A Pending JPS59204690A (en) 1983-05-06 1983-05-06 Stabilizer for mixed fuel

Country Status (1)

Country Link
JP (1) JPS59204690A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108203608A (en) * 2017-12-21 2018-06-26 北京三聚环保新材料股份有限公司 A kind of method for improving coal solid content

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108203608A (en) * 2017-12-21 2018-06-26 北京三聚环保新材料股份有限公司 A kind of method for improving coal solid content

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