JPH0431496A - Additive for pulverized coal/oil mixture - Google Patents
Additive for pulverized coal/oil mixtureInfo
- Publication number
- JPH0431496A JPH0431496A JP13661090A JP13661090A JPH0431496A JP H0431496 A JPH0431496 A JP H0431496A JP 13661090 A JP13661090 A JP 13661090A JP 13661090 A JP13661090 A JP 13661090A JP H0431496 A JPH0431496 A JP H0431496A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- oil
- additive
- coal
- molecule
- 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.)
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- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
本発明は安定性を改良し、石炭灰の各種機器への付着を
防止するための微粉炭−油混合物(以下COMと称す)
用添加剤に関するものである。The present invention is a pulverized coal-oil mixture (hereinafter referred to as COM) for improving stability and preventing coal ash from adhering to various equipment.
It is related to additives for use.
従来のCOM用添加剤としては、例えば特開昭53−4
7405号や53−82809号に示すアニオン系化合
物がある。As a conventional additive for COM, for example, JP-A-53-4
There are anionic compounds shown in No. 7405 and No. 53-82809.
しかしながら、これらは石炭の沈降を防止する効果はあ
る程度あったが、粗大石炭粒子、例えば300μ以上の
粒子の沈降を防止するには性能が不足しており、加える
に、特に、C0M中に含まれる灰分が遊離して撹拌機等
の金属部分に付着する問題を有している。このためCO
Mの安定性をさらに改良し、灰付着を防止する添加剤の
開発が切望されてきた。However, although these had the effect of preventing coal sedimentation to some extent, their performance was insufficient to prevent the sedimentation of coarse coal particles, such as particles larger than 300μ, and in addition, especially those contained in C0M. There is a problem that ash is released and adheres to metal parts such as the stirrer. For this reason, CO
It has been desired to develop an additive that further improves the stability of M and prevents ash adhesion.
この発明は、このような従来の問題点に着目してなされ
たものである。長期間安定性を保持し、灰付着を防止す
る添加剤について鋭意研究を重ねた結果、(A)分子内
にスルホン酸基をもつ化合物またはその塩、及び(B)
一般式R,−NH−(Rz −N H−) n −Rs
(式中R+、Rsは炭素数1〜30のアルキル基、アシ
ル基又は水素原子を示し、R2は炭素数2〜6のアルキ
レン基を示し、nは1〜20の整数を示す)で示される
ポリアミンを必須成分として含有する添加剤が非常に優
れた効果を有することを見い出した。
(手段を構成する要件)
本発明に使用する添加剤の(A)成分は、分子内にスル
ホン酸基をもつ化合物、またはその塩である。
具体的に用いられる化合物としては、有機物質を硫酸、
発煙硫酸、無水硫酸、クロルスルホン酸、酸性亜硫酸ソ
ーダ等のスルホン化剤で反応し、分子内にスルホン基を
1個又は2個以上導入した化合物である。大別すると、
■芳香環を有する物質の核にスルホン基が結合したもの
。
■脂肪族系の鎖状結合にスルホン基が結合したもの。
であり、これらを次に詳述する。
■芳香環を有する物質の核にスルホン基が結合したもの
とは、ベンゼン環、ナフタレン環、アントラセン環、フ
ェノール環にスルホン基を導入したもので、たとえばベ
ンゼン、トルエン、キシレン、アルキル(C,以上)ベ
ンゼン、ナフタレン、アルキルナフタレン、アントラセ
ン、フェノール、アルキルフェノール、アニリン、ニト
ロアニリン、スチレン等のスルホン酸又はその塩であり
、特にアルキルナフタレン、アルキル(C。
以上)ベンゼン、アルキルフェノールのスルホン酸が好
ましい。
次に芳香環を各種反応で2個以上結合させたもののスル
ホン化物、たとえばジフェニル、ジスチレン化フェノー
ル、スチレン重合体、スチレン共重合体のスルホン酸又
はその塩も好ましい。
さらには上記スルホン酸をホルマリン等のアルデヒドで
縮合させたり、重合等の各種反応を利用して、更に反応
したもの、例えばナフタレンスルホン酸のホルマリン縮
合物、ナフタレンスルホン酸とアルキルフェノールのナ
フタレンスルホン酸のホルマリン縮合物やアルキルフェ
ノールとナフタレンスルホン酸のホルマリン縮合物又は
スチレンスルホン酸と酢酸ビニル共重合体等が挙げられ
る。また、石油精製時に副生ずる石油スルホネートも有
効である。
■脂肪族系の鎖状結合にスルホン基が結合したものとは
、アルキルスルホン酸、アルカンスルホン酸、α−オレ
フィンスルホン酸、スルホン化高級脂肪酸、高級脂肪酸
エステルのスルホン酸、脂肪酸アミドのアルキルスルホ
ン酸、アルキルスルホコハク酸エステル等である。たと
えばスルホン化高級脂肪酸とは、α−スルホラウリン酸
塩やα−スルホ牛脂脂肪酸塩、α−スルホステアリン酸
塩があり、高級脂肪酸エステルのスルホン酸とは、高級
脂肪酸とオキシスルホン酸とでエステル化したもので、
オレイン酸とオキシエタンスルホン酸のエステル等が挙
げられる。また、脂肪酸アミドのアルキルスルホン酸は
、ラウリン酸メチルタウライド、ステアリン酸N−フェ
ニルタウライドである。アルキルスルホン酸り酸エステ
ルとはジー2−エチルへキシルスルホコハク酸エステル
や、ジノニルフェノールスルホコハク酸エステル等があ
る。
次に、■■のスルホン酸塩の場合、塩の対イオンとして
はNa、に、Ca、Mg等のアルカリ金属やアルカリ土
類金属およびアンモニアやエチルアミン、エタノールア
ミン、インプロパツールアミン、ラウリルアミンやポリ
アミン等のアミン類が用いられる。
次に、(B)成分に示されるポリアミンとは。
エチレンジアミン、牛脂プロピレンジアミン、トリエチ
レンテトラミン、テトラエチレンペンタミン、ペンタエ
チレンへキサミン等のポリアミン単独あるいはその誘導
体である。誘導体とは、アルキルハライドとの反応生成
物、例えばドデシルプロピレンジアミン、ドデシルトリ
エチレンテトラミン、牛脂ジプロピレントリアミン等で
ある。また、ポリアミンと脂肪酸、例えばオクチル酸、
ステアリン酸、オレイン酸、特にやし油脂肪酸、牛脂脂
肪酸とのアミド化合物が有効である。
本発明のスルホン酸(A)とポリアミン(B)の配合比
は、A/B=9515〜5/95.好ましくは90/1
0〜20/80である。
COMに用いる石炭としては、例えば無煙炭、瀝青炭、
亜瀝青炭、褐炭等の各種石炭が利用でき、種類や産地に
かかわりなく、または化学組成や水分含有量にもかかわ
りなく、いかなるものも利用できる。
かかる石炭をそのまま、あるいは粗砕して油中にいれ、
各種湿式粉砕機により油中で直接微粉炭とするか、また
は通常の乾式粉砕機により微粉炭としてもよい。ただし
、湿式の粉砕法の方が、COMの安定性が向上し、かつ
粉砕時の自然発火や粉じんが防止できるためさらによい
。
石炭中の水分は乾式粉砕時に除いても、あるいは湿式粉
砕中や粉砕後に砕いてもよ(、含有水分の少ないものは
除かなくても支障がない。
微粉炭の粒度は、燃焼性より判断して通常平均粒子径2
00ミクロン以下のものが好ましく、更に粒度の小さい
100ミクロン以下が好適であるが、COMの安定性等
の物性に関する限り、さらに粒度の大きいものでも問題
はない。
この微粉体の含有量は、最終混合物に対して20〜70
重量%であり、70重量%を越える微粉炭を含有した場
合は粘度が著しく高(なり、流動性を失うため好ましく
なく、20重量%未滴の場合は微粉炭含有に伴う経済面
の利点が減少するため好ましくない、したがって、20
〜70重量%含有できるが、30〜60重量%がさらに
好ましい。
また、COMに用いる油とは、石油原油、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
重油等やエチレン分解残油、クレオソート油、アントラ
セン油、各種配合油等の一般に燃料として用いられる油
や廃油、例えば、ガソリンスタンド廃油(自動車潤滑油
、洗浄油)、鉄工所廃油(機械油、切削油、洗浄油やそ
れらの混合油)、石油タンカーやその他船舶の廃油、般
化学工場廃油等をいい、それらの相互の混合物も含む。
中でも石油原油およびB重油、C重油の利用が好ましい
。単独油のみ、またはあらかじめ配合した油を用いてC
OMを調製しても、単独油(好ましくは石油原油、重油
)でCOMを作った復信の油を混合したり混焼してもよ
い。
水は、石炭中に含まれる水分がC0M中に混入したり、
製造者または使用者が加える場合等があるが、水の体積
分だけ輸送費、貯蔵費、その他−般管理費が高くなり、
さらに燃焼時蒸発熱をうばい、熱損失が大きくなるため
好ましくなく、少ない方がよい。一方、水COMの安定
性を良好にする性質と、燃焼時排ガス中にNOxとバイ
ジンを少なくする効果を有するため、少量の混入は許さ
れる。したがって、全水分量は15重量%以下、好まし
くは6重量%以下がよく、全く含有しなくてもよい。
本発明の添加剤を用いてCOMを安定化し、灰付着防止
効果を発揮させるには、乾式粉砕した微粉炭を油中に混
合後添加剤を加えるが、あらかじめ油中に添加剤を溶解
後転式粉砕した微粉炭を加えるか、または微粉炭、油お
よび添加剤の三者を一括して混合すればよ(、各々に水
添加を実施してもよい。また湿式粉砕の場合は、粉砕前
、粉砕中、または粉砕後のいずれの時期に添加してもよ
い。この場合も水添加を行なってもよい。
混合燃料系に対する本発明添加剤の添加量は、炭種、石
炭粒度分布および油種によって若干異なるが、一般に混
合燃料中0.O1〜5重量%、好ましくは0.04〜0
.8重量%であり、上限は単に経済理由によるものであ
る。
本発明により、添加物、微粉炭、油および必要により水
からなる分散系を形成する場合、任意の温度が採用され
、例えば50〜120℃で混合され、混合圧は加圧、常
圧、減圧脱気時でもよ(、撹拌機および攪拌条件は、制
約を受けない。This invention was made by focusing on such conventional problems. As a result of extensive research into additives that maintain long-term stability and prevent ash adhesion, we have found that (A) a compound or its salt that has a sulfonic acid group in the molecule, and (B)
General formula R, -NH-(Rz -NH-) n -Rs (In the formula, R+ and Rs represent an alkyl group, an acyl group, or a hydrogen atom having 1 to 30 carbon atoms, and R2 represents an alkylene group having 2 to 6 carbon atoms. It has been found that an additive containing as an essential component a polyamine represented by the following formula (n is an integer of 1 to 20) has very excellent effects. (Requirements constituting means) Component (A) of the additive used in the present invention is a compound having a sulfonic acid group in the molecule, or a salt thereof. Specifically used compounds include organic substances such as sulfuric acid,
It is a compound that reacts with a sulfonating agent such as fuming sulfuric acid, sulfuric anhydride, chlorosulfonic acid, and acidic sodium sulfite to introduce one or more sulfone groups into the molecule. Broadly divided, they are: ① Substances with an aromatic ring and a sulfone group bonded to the core. ■A sulfone group is bonded to an aliphatic chain bond. These are detailed below. ■ Substances with an aromatic ring in which a sulfone group is bonded to the core are those in which a sulfone group is introduced into a benzene ring, naphthalene ring, anthracene ring, or phenol ring, such as benzene, toluene, xylene, alkyl (C, or more). ) sulfonic acids such as benzene, naphthalene, alkylnaphthalene, anthracene, phenol, alkylphenol, aniline, nitroaniline, and styrene, or salts thereof; particularly preferred are sulfonic acids such as alkylnaphthalene, alkyl (C or higher) benzene, and alkylphenol. Also preferred are sulfonated products of two or more aromatic rings bonded together through various reactions, such as diphenyl, distyrenated phenol, styrene polymer, styrene copolymer sulfonic acids, or salts thereof. Furthermore, the above sulfonic acids are condensed with an aldehyde such as formalin, or are further reacted using various reactions such as polymerization, such as formalin condensates of naphthalenesulfonic acid, formalin of naphthalenesulfonic acids of naphthalenesulfonic acid and alkylphenol. Examples include a condensate, a formalin condensate of alkylphenol and naphthalene sulfonic acid, and a copolymer of styrene sulfonic acid and vinyl acetate. Petroleum sulfonate, which is produced as a by-product during petroleum refining, is also effective. ■Those in which a sulfonic group is bonded to an aliphatic chain bond include alkyl sulfonic acids, alkanesulfonic acids, α-olefin sulfonic acids, sulfonated higher fatty acids, sulfonic acids of higher fatty acid esters, and alkyl sulfonic acids of fatty acid amides. , alkyl sulfosuccinates, and the like. For example, sulfonated higher fatty acids include α-sulfolaurate, α-sulfo-tallow fatty acid salt, and α-sulfostearate, and higher fatty acid esters of sulfonic acid are esterified with higher fatty acids and oxysulfonic acid. I did it,
Examples include esters of oleic acid and oxyethanesulfonic acid. Further, the alkyl sulfonic acid of the fatty acid amide is methyl laurate and N-phenyl tauride stearate. Examples of alkylsulfonic acid esters include di-2-ethylhexylsulfosuccinate and dinonylphenol sulfosuccinate. Next, in the case of the sulfonate salt of ■■, the counter ions of the salt include alkali metals and alkaline earth metals such as Na, Ca, Mg, ammonia, ethylamine, ethanolamine, impropaturamine, laurylamine, etc. Amines such as polyamines are used. Next, what is the polyamine shown as component (B)? Polyamines such as ethylenediamine, tallow propylene diamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, etc., or their derivatives. Derivatives are reaction products with alkyl halides, such as dodecylpropylene diamine, dodecyltriethylenetetramine, tallow dipropylenetriamine, and the like. Also, polyamines and fatty acids, such as octyl acid,
Stearic acid, oleic acid, and especially amide compounds with coconut oil fatty acid and beef tallow fatty acid are effective. The blending ratio of sulfonic acid (A) and polyamine (B) of the present invention is A/B=9515 to 5/95. Preferably 90/1
0 to 20/80. Coal used for COM includes, for example, anthracite coal, bituminous coal,
Various types of coal such as sub-bituminous coal and lignite can be used, and any type of coal can be used, regardless of its type, origin, chemical composition, or moisture content. Such coal is put into oil as it is or after being crushed,
It may be made into pulverized coal directly in oil using various wet pulverizers, or it may be made into pulverized coal using a conventional dry pulverizer. However, a wet pulverization method is better because it improves the stability of COM and prevents spontaneous combustion and dust during pulverization. Moisture in coal can be removed during dry pulverization, or it can be crushed during wet pulverization or after pulverization (but there is no problem even if it is not removed if the coal has a low moisture content. The particle size of pulverized coal is determined based on combustibility. Normally the average particle size is 2
A particle size of 00 microns or less is preferable, and a smaller particle size of 100 microns or less is preferable, but as far as physical properties such as COM stability are concerned, even larger particle sizes are acceptable. The content of this fine powder is between 20 and 70% of the final mixture.
If the pulverized coal content exceeds 70% by weight, the viscosity will be extremely high (and fluidity will be lost, which is undesirable. If the pulverized coal content exceeds 70% by weight, the economical advantages associated with the pulverized coal content will be reduced). unfavorable because it decreases, therefore 20
Although it can be contained in an amount of up to 70% by weight, 30 to 60% by weight is more preferable. In addition, the oil used for COM refers to petroleum crude oil, various fractions obtained from crude oil, such as kerosene, light oil, A heavy oil, B heavy oil, C
Oils and waste oils commonly used as fuel such as heavy oil, ethylene decomposition residual oil, creosote oil, anthracene oil, and various blended oils, such as gas station waste oil (automobile lubricating oil, cleaning oil), ironworks waste oil (machine oil, (cutting oil, cleaning oil, and mixtures thereof), waste oil from oil tankers and other ships, waste oil from general chemical factories, etc., and also includes mixtures of these oils. Among them, it is preferable to use petroleum crude oil, B heavy oil, and C heavy oil. C using only oil alone or pre-blended oil
Even if OM is prepared, COM may be prepared from a single oil (preferably petroleum crude oil or heavy oil) and then mixed or co-fired with another oil. Water is caused by moisture contained in coal mixed into C0M,
There are cases where manufacturers or users add water, but transportation costs, storage costs, and other general and administrative costs will increase by the volume of water.
Furthermore, it steals the heat of vaporization during combustion and increases heat loss, which is undesirable, and the less the better. On the other hand, since it has the property of improving the stability of water COM and has the effect of reducing NOx and vizine in the exhaust gas during combustion, a small amount of water is allowed to be mixed in. Therefore, the total water content is preferably 15% by weight or less, preferably 6% by weight or less, and may not be contained at all. In order to stabilize COM and exhibit the ash adhesion prevention effect using the additive of the present invention, the additive is added after dry-pulverized pulverized coal is mixed into oil. Either add pulverized coal that has been pulverized, or mix the pulverized coal, oil, and additives all at once (water may be added to each separately. Also, in the case of wet pulverization, add pulverized coal before pulverization. The additive may be added at any time during the pulverization or after the pulverization.Water may also be added in this case.The amount of the additive of the present invention added to the mixed fuel system depends on the coal type, coal particle size distribution, and oil. Although it varies slightly depending on the species, generally 0.01 to 5% by weight in the mixed fuel, preferably 0.04 to 0.
.. 8% by weight, the upper limit being solely for economic reasons. According to the present invention, when forming a dispersion system consisting of additives, pulverized coal, oil, and optionally water, any temperature can be adopted, for example, mixing at 50 to 120°C, and the mixing pressure can be elevated pressure, normal pressure, or reduced pressure. Even during degassing (the stirrer and stirring conditions are not subject to any restrictions.
次に、本発明を実施例によりさらに詳細に説明するが、
例示は単に説明用のものであって、発明の思想を拘束す
るものではない。
C0M製造装置の撹拌部の小規模モデルとして、特殊機
化工業■の高度粘度用撹拌バネをつけたホモミキサーを
使用し、灰付着防止試験は次のように行なった。
70℃に加温したCOM (第1表に性状を示す)に添
加剤(第2表に示す)を0.25重量%(対COM)添
加し、スパチュラにて予備混合を行なった後、同じ温度
5000rprnで10分間撹拌する。つづいて、撹拌
機にイ」着したCOMを溶剤で洗浄した後、回転部まわ
りに固く付着した灰分量を測定した。この灰分量が少な
い程、灰分の付着防止性にすぐれているといえる。
また、C0M安定性試験は次により行なった。
COM (第1表に性状を示す)に添加剤を0.25重
量%(対COM)加え、ホモミキサー400Qrpmで
4分間撹拌する。攪拌したCOMを500mεのポリビ
ンに入れ、64℃の恒温器に10日間静置する。静置後
、ポリビンを逆さにしてCOMを払い出す。この時のポ
リビン底部に残ったCOMの重量、石炭濃度を測定し、
その結果を第3表に示す。
第3表の比較例に示すとおり、スルホン化物[(A)成
分]単独では、灰4−’r着が起こり、またC0M安定
性も十分でない。
本発明品のようにスルホン化物とポリアミン[(B)成
分]を配合すると灰付着が起きずかつ非常に安定なCO
Mが得られた。Next, the present invention will be explained in more detail with reference to Examples.
The examples are merely for illustrative purposes and are not intended to constrain the spirit of the invention. As a small-scale model of the stirring section of the C0M manufacturing equipment, a homomixer equipped with a stirring spring for high viscosity manufactured by Tokushu Kika Kogyo 2 was used, and the ash adhesion prevention test was conducted as follows. Add 0.25% by weight (based on COM) of additives (shown in Table 2) to COM (properties shown in Table 1) heated to 70°C, premix with a spatula, and then add the same Stir for 10 minutes at a temperature of 5000 rpm. Subsequently, after washing the COM that had landed on the stirrer with a solvent, the amount of ash firmly attached around the rotating part was measured. It can be said that the smaller the ash content, the better the ability to prevent ash adhesion. Further, the C0M stability test was conducted as follows. Add 0.25% by weight (relative to COM) of additives to COM (properties shown in Table 1) and stir for 4 minutes using a homomixer at 400 Qrpm. The stirred COM is placed in a 500 mε polybottle and left in a thermostatic chamber at 64° C. for 10 days. After allowing it to stand still, turn the polybin upside down and dispense the COM. At this time, the weight of COM remaining at the bottom of the polybin and the coal concentration were measured.
The results are shown in Table 3. As shown in the comparative example in Table 3, when the sulfonated product [component (A)] is used alone, ash 4-'r deposition occurs and the C0M stability is also insufficient. When a sulfonated product and a polyamine [component (B)] are blended as in the product of the present invention, ash adhesion does not occur and CO becomes very stable.
M was obtained.
本発明の添加剤の使用により、長期間安定でかつ灰付着
のないCOMが得られ、COMを長期間かけてタンク貯
蔵でき、又、C0Mポンプや制御弁等の各種機器への灰
付着がなく、大量製造及び燃焼が可能となった。
[第1表] COMの性状By using the additive of the present invention, COM that is stable for a long time and does not have ash adhesion can be obtained, COM can be stored in a tank for a long period of time, and there is no ash adhesion to various equipment such as COM pumps and control valves. , mass production and combustion became possible. [Table 1] Properties of COM
Claims (1)
塩、及び (B)一般式R_1−NH−(R_2NH)_n−R_
3(式中R_1、R_2は炭素数1〜30のアルキル基
、アシル基又は水素原子を示し、R_2は炭素数2〜6
のアルキレン基を示し、nは1〜20の整数を示す)で
示されるポリアミンを必須成分として含有することを特
徴とする微粉炭−油混合物用添加剤。[Claims] (A) A compound having a sulfonic acid group in the molecule or a salt thereof, and (B) General formula R_1-NH-(R_2NH)_n-R_
3 (in the formula, R_1 and R_2 represent an alkyl group having 1 to 30 carbon atoms, an acyl group, or a hydrogen atom, and R_2 has a carbon number of 2 to 6
An additive for pulverized coal-oil mixtures, characterized in that it contains as an essential component a polyamine represented by the following alkylene group (n is an integer of 1 to 20).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13661090A JPH0431496A (en) | 1990-05-25 | 1990-05-25 | Additive for pulverized coal/oil mixture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13661090A JPH0431496A (en) | 1990-05-25 | 1990-05-25 | Additive for pulverized coal/oil mixture |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0431496A true JPH0431496A (en) | 1992-02-03 |
Family
ID=15179325
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13661090A Pending JPH0431496A (en) | 1990-05-25 | 1990-05-25 | Additive for pulverized coal/oil mixture |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0431496A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105482859A (en) * | 2015-11-24 | 2016-04-13 | 宜兴市星光宝亿化工有限公司 | Environmentally-friendly treatment type coal water slurry additive suitable for coal chemical industry coal water slurry preparing and waste mixing technology, and preparation method and use thereof |
-
1990
- 1990-05-25 JP JP13661090A patent/JPH0431496A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105482859A (en) * | 2015-11-24 | 2016-04-13 | 宜兴市星光宝亿化工有限公司 | Environmentally-friendly treatment type coal water slurry additive suitable for coal chemical industry coal water slurry preparing and waste mixing technology, and preparation method and use thereof |
| CN105482859B (en) * | 2015-11-24 | 2017-04-26 | 宜兴市星光宝亿化工有限公司 | Environmentally-friendly treatment type coal water slurry additive suitable for coal chemical industry coal water slurry preparing and waste mixing technology, and preparation method and use thereof |
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