JPS58111893A - Viscosity depressant for highly concentrated coal/water slurry - Google Patents

Viscosity depressant for highly concentrated coal/water slurry

Info

Publication number
JPS58111893A
JPS58111893A JP21037481A JP21037481A JPS58111893A JP S58111893 A JPS58111893 A JP S58111893A JP 21037481 A JP21037481 A JP 21037481A JP 21037481 A JP21037481 A JP 21037481A JP S58111893 A JPS58111893 A JP S58111893A
Authority
JP
Japan
Prior art keywords
coal
water slurry
water
viscosity
thinner
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
JP21037481A
Other languages
Japanese (ja)
Inventor
Akihiro Naka
中 昭廣
Shuichi Honjo
本荘 秀一
Fukunobu Mayuzumi
黛 福信
Yasuji Tanakamaru
田中丸 八州治
Yoshihisa Nishida
善久 西田
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.)
DKS Co Ltd
Original Assignee
Dai Ichi Kogyo Seiyaku 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 Dai Ichi Kogyo Seiyaku Co Ltd filed Critical Dai Ichi Kogyo Seiyaku Co Ltd
Priority to JP21037481A priority Critical patent/JPS58111893A/en
Publication of JPS58111893A publication Critical patent/JPS58111893A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a viscosity depressant which lowers the viscosity of a coal/ water slurry and makes it possible to pump a highly concentrated coal/water slurry by adding it in a small amount, consisting of a polyether compd. (derivative) obtd. by adding an alkylene oxide to an active hydrogen-contg. amine (derivative). CONSTITUTION:An alkylene oxide such as ethylene oxide is added to an amine contg. at least one active hydrogen or its derivative, such as dimethylamine and the product is, if necessary, modified with an aicd to obtain a viscosity depressant consisting of a polyether (derivative) having an MW of 1,000-100,000. 0.01-5.0wt% said viscosity depressant is added to a coal/water slurry contg. coal at a concn. of 70wt% or above, whereby the viscosity of the slurry can be lowered to a level at which the slurry can be pumped. EFFECT:The viscosity depressant has an effect of stably dispersing coal in water.

Description

【発明の詳細な説明】 本発明は石炭−水スラリー用減粘剤に関する。[Detailed description of the invention] The present invention relates to a thinner for coal-water slurries.

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。
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.

近年石油資源の枯渇により、石炭の利用が再認識され、
その利用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ってくる。
In recent years, due to the depletion of oil resources, the use of coal has been reconsidered.
Various ways of using it 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 becomes difficult to pump as increasing the coal concentration significantly thickens the coal and loses its fluidity.

一方石炭一度を下げると輸送効率が低下し、さらGこ燃
焼111に脱水工程が必要となってきて、費用がかかる
ため実用的でない。
On the other hand, if the coal content is lowered, the transportation efficiency will decrease, and a dehydration step will become necessary for the combustion 111, which is expensive and impractical.

本発明者らは先に、ポリエーテル類を用いて石炭を油中
に安定分散させることに成功し特許出願中である。特開
昭54−52105.同54−52106、同54−5
3105.同54−’53106、同54−53107
.同54−53108゜同54−53109.同54−
65708.同54−65709.同54−11150
6.’同55−152789参照。しかしながらこれら
は石炭を油中に安定分散させるものであり、石炭−水ス
ラリーに用いるものでない。:”1′ 特開昭56−62538には微粉末を低濃度で水に安定
分散させる薬剤が記載されているが、高濃度石炭−水ス
ラリーの減粘剤とは目的を異にするものである。
The present inventors have previously succeeded in stably dispersing coal in oil using polyethers, and are currently applying for a patent. Japanese Patent Publication No. 54-52105. 54-52106, 54-5
3105. 54-'53106, 54-53107
.. 54-53108゜54-53109. Same 54-
65708. 54-65709. 54-11150
6. 'See 55-152789. However, these are for stably dispersing coal in oil and are not for use in coal-water slurries. :"1' JP-A-56-62538 describes an agent that stably disperses fine powder in water at a low concentration, but its purpose is different from that of a thinning agent for highly concentrated coal-water slurry. be.

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、雪のため高濃度の石炭縮度において
もポンプ輸送が可能な石炭−基スラリーを提供する減粘
剤の開光に成功した。
The present inventors fluidized a highly concentrated coal-water slurry,
We have conducted extensive research into a thinner for coal-water slurries that makes pumping possible. Adding a small amount can significantly reduce the viscosity of coal-water slurries, making pumping possible even when the coal condensation is high due to snow. We have successfully discovered a thinning agent that provides a coal-based slurry with high quality.

本発明の庫粘剤を用いると、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
\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。
By using the storage adhesive of the present invention, coal can be fluidized with a small amount of water, making it possible to not only transport it by pump, but also to burn it in a boiler as it is, and also eliminate the dehydration process before combustion. be able to. By using the thinning agent of the present invention, handling of coal becomes extremely simple, and its applications are greatly expanded.

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ってもよい。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っても
よいが、現在火力発電所で燃焼される微粉炭は200メ
ツシュア0%パス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
によっ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。
The coals used in the coal-water slurry include anthracite, bituminous coal,
Any type of coal may be used, such as sub-bituminous coal, lignite, or cleaned versions of these coals. In addition, 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 200 mesh 0% pass or higher, this particle size is fine. This is a guideline for the particle size of charcoal. However, the thinner of the present invention is not affected by particle size and exhibits excellent effects on coal powder of any particle size.

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。
Cleaned coal is coal from which inorganic substances such as ash and sulfur have been removed.

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 Agglaneration  法(以下O
A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。
Examples of methods for cleaning coal include heavy liquid separation method and oil aggregation method (hereinafter referred to as O
There are methods such as A method), flotation coal beneficiation method, etc. However, methods other than these may also be used and are not particularly limited.

OA法について記載すると、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、適駄の油を添加する
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、攪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
中に遊離するので、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重量
%である。
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 the coal is coated with oil in advance, a water slurry is prepared and 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 as a binder, which selectively wets the organic components of coal. On the other hand, since inorganic substances have a weak affinity with oil, they are liberated in water, so this method can simultaneously remove inorganic substances by separating water from coagulated coal. The coal concentration in the coal-water slurry of the OA method is usually 10 to 65% by weight.

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、3重泊、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一般に燃料として用いられる油や
、潤滑油、洗浄油などのt重油である。またベンゼン、
トルエン、キシレン、動植物油なと水に不溶の油も用い
ら1するが中でも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
般に30重量%以下の蓋で充分である。
The oil used in the OA method is crude oil or various fractions obtained from crude oil, such as kerosene, light oil, A heavy oil, triplex oil, C heavy oil, etc., tar or shale oil, ethylene cracked residual oil, or various blended oils, which are generally used as fuel. The oils used are heavy oils such as lubricating oils and cleaning oils. Also benzene,
Oils insoluble in water such as toluene, xylene, 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. It is generally sufficient to use this oil in an amount of 30% by weight or less based on the coal in the coal-water slurry to be treated for mineral removal.

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攪拌することにより泡立たせて、
70スを生成させる。本方法もOA法同様、石炭の有機
分が70ス油膜に付着するが、無機物は水中に遊離し、
石炭有機分と分離することができる方法である。
The flotation coal washing method is an existing coal washing method in which a very small amount of oil is added to the pulverized coal-water slurry and stirred to create foam.
Generate 70 spaces. Similar to the OA method, in this method, the organic components of the coal adhere to the 70% oil film, but the inorganic components are liberated in the water.
This is a method that can separate coal organic components.

浮遊選炭法において用いる油は、タービネオイル、ター
ル、へ重油、6重泊、軽油、灯油である。
The oils used in the flotation method are turbine oil, tar, heavy oil, hexagonal oil, light oil, and kerosene.

L配力法により数10重量%以上の無機物が石炭より除
去されるのが一般的である。
Generally, several tens of weight percent or more of inorganic substances are removed from coal by the L distribution method.

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減粘剤の効果は
著しく優れ、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
リットが非常に大きい。
If the coal cleaned in this manner is used, the effect of the thinner of the present invention will be significantly superior to that of uncleaned coal, 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.

本発明の石炭−水スラリー用減粘剤は、分子内に活性水
素を1個以上、好ましくは3個以上、さらに好ましくは
5個以上有するアミン、およびそれらの誘導体を出発物
質として、これにアルキレンオキシドを付加し、その分
子31ioooないし10万であるポリエーテル化合物
、または該ポリエーテル化合物の末端水酸基を各種反応
させた誘導体を含有することを特徴とする。
The thinner for coal-water slurry of the present invention uses as a starting material an amine having one or more active hydrogens, preferably three or more, more preferably five or more active hydrogens in the molecule, and derivatives thereof. It is characterized by containing a polyether compound to which an oxide has been added and the molecule thereof is 31iooo to 100,000, or a derivative in which the terminal hydroxyl group of the polyether compound is subjected to various reactions.

出発物質を例示すれば次のようなものがある。Examples of starting materials include the following.

活性水素1個を有するアミン類、例えばジメチルアミン
、N−メチルラウリルシアミン等、活性水素2個を有す
るアミン類、例えばメチルアミン、エチルアミン、プロ
ピルアミン、ブチルアミン、アリルアミン、アミルアミ
ン、オクチルアミン、デシルアミン、ラウリルアミン、
テトラデシルアミン、ペンタデシルアミン、オフタテシ
ルアミン、牛脂アルキルアミン、ヤシアルキルアミン、
アニリン、p−)ルイジン、m  )ルイジン、ニトロ
アニリン、ベンジルアミン、クロルアニリン、p−ドデ
シルベンジルアミン、シクロヘキシルアミン等、活性水
素を3個有するアミン、例えばアンモニア、牛脂プロピ
レンジアミン等、活性水素ヲ4個有するアミン、例えば
エチレンジアミン、テトラメチレンジアミン、ヘキサメ
チレンジアミン、フェニレンジアミン、ベンジジン、シ
クロヘキシルジアミン等、活性水素を5個以上有するア
ミン、た2個以上の活性水素を有するアミンの部分アミ
ド等の各種誘導体であっても、1個以上の活性水素が残
っていれば用いることができる。
Amines having one active hydrogen such as dimethylamine, N-methyllaurylcyamine, etc.; amines having two active hydrogen such as methylamine, ethylamine, propylamine, butylamine, allylamine, amylamine, octylamine, decylamine, laurylamine,
Tetradecylamine, pentadecylamine, ophtadecylamine, tallow alkylamine, coconut alkylamine,
Aniline, p-)luidine, m) Luidine, nitroaniline, benzylamine, chloroaniline, p-dodecylbenzylamine, cyclohexylamine, etc., amines having 3 active hydrogens, such as ammonia, tallow propylene diamine, etc., active hydrogen 4 Various derivatives such as amines having 5 or more active hydrogens, partial amides of amines having 2 or more active hydrogens, such as ethylenediamine, tetramethylenediamine, hexamethylenediamine, phenylenediamine, benzidine, cyclohexyldiamine, etc. However, it can be used as long as one or more active hydrogens remain.

本発明の減粘剤はこれらの出発物質にアルキレンオキシ
ドを付加し、その分子縁が1oooないしlO万である
ポリエーテル化合物または該ポリエーテル化合物の末端
水酸基を各梗反応させた誘導体であるが、とりわけ分子
(1tが10000ないし10万にしたものがより有効
である。
The thinner of the present invention is a polyether compound in which an alkylene oxide is added to these starting materials and the molecular edges thereof are 100 to 100,000, or a derivative in which the terminal hydroxyl groups of the polyether compound are reacted with each other. In particular, molecules (1t: 10,000 to 100,000) are more effective.

アルキレンオキシドとしては、エチレンオキシド、プロ
ピレンオキシド、ブチレンオキシドなどが使用され、こ
れらは単独であっても、2種以上であってもよく、2種
以上の場合その配列はブロック重合型またはランダム重
合型のいずれでもよいが、ブロック重合型が一般的であ
る。特にアルキレンオキシドとしてエチレンオキシドを
含み、その含有率が全アルキレンオキシドの10ないし
95重社%、好ましくは60ないし90重量%であるポ
リエーテル化合物、または該ポリエーテル化合物の末端
水酸基を各種反応させた誘導体が優れた効果を発揮する
Ethylene oxide, propylene oxide, butylene oxide, etc. are used as the alkylene oxide, and these may be used alone or in combination of two or more types. In the case of two or more types, the arrangement is block polymerization type or random polymerization type. Although any type may be used, block polymerization type is common. In particular, a polyether compound containing ethylene oxide as the alkylene oxide, the content of which is 10 to 95% by weight, preferably 60 to 90% by weight of the total alkylene oxide, or a derivative obtained by various reactions of the terminal hydroxyl group of the polyether compound. shows excellent effects.

また上記ポリエーテル化合物の末端水酸基を各種反応さ
せた゛誘導体も有効である。例えば下記のものを挙げる
ことができる。
Derivatives obtained by subjecting the terminal hydroxyl groups of the above polyether compounds to various reactions are also effective. For example, the following can be mentioned.

l)有機酸や無機酸と反応したエステル化物。l) Esterified products reacted with organic acids or inorganic acids.

2)ハロゲン化水素やハロゲン化リンとの反応で水酸基
がハロゲン置換されたもの。
2) Hydroxyl groups are replaced with halogens by reaction with hydrogen halide or phosphorus halide.

3)酸化反応により生成したアルデヒドやカルボン酸。3) Aldehydes and carboxylic acids produced by oxidation reactions.

4)水酸基、とモノイソシアネートとの反応生成物。4) A reaction product between a hydroxyl group and a monoisocyanate.

しかし本発明は上記例によって限定されるものではない 本発明の減粘剤が優れた効果を発揮する理由は、その特
殊構造により粒子表面に強固に吸着した後、多数のエー
テル結合が周囲の水を水和して、この水を潤滑油的作用
を有する構造にかえるため、石炭粒子は一次粒子として
安定し、流動性が向上するものと思われる。同時に著し
い粘度低下を起すのである。
However, the present invention is not limited to the above-mentioned examples. The reason why the present invention's thinning agent exhibits excellent effects is that after it is strongly adsorbed to the particle surface due to its special structure, many ether bonds are bonded to the surrounding water. It is thought that the coal particles are stabilized as primary particles and their fluidity is improved because the water is hydrated and the water is converted into a structure that acts like a lubricating oil. At the same time, a significant decrease in viscosity occurs.

また脱灰等のクリーン化した石炭を使用すればさらにそ
の効果が上昇するのは、脱灰することによって親水性が
大きく微粒子でその表面積が太きい灰が除去されること
により有機性が向上した石炭表面に、本発明の減粘剤が
効果的に作用するためであり、それによって石炭濃度の
上昇をはかることができる。
In addition, if you use clean coal that has been deashed, the effect will further increase because deashing removes ash, which is highly hydrophilic and has fine particles with a large surface area, improving its organic properties. This is because the thinner of the present invention effectively acts on the coal surface, thereby increasing the coal concentration.

か\る本発明の減粘剤は、石炭−水スラリーに対して0
.O1〜5.0重量%、好ましくは0.03〜2.0重
置%添加することによりすぐれた効果を発挿する。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っ
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重量%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6
1重量%以上、特に70重量%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〜l
Oポイント上昇する。
The thinner of the present invention has a zero viscosity for coal-water slurry.
.. Excellent effects can be obtained by adding 1 to 5.0% by weight, preferably 0.03 to 2.0% by weight of O. 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, the fluidity will be lost at a coal concentration of around 50% by weight, but with the addition of the thinner of the present invention. If this is done, the viscosity will drop significantly, so the coal concentration will be
It has fluidity even at 1% by weight or more, especially 70% by weight or more. If even cleaner coal is used, the coal concentration will be several points higher, generally 3 to 1
Increase by O points.

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。
The thinner of the present invention can also be used in combination with other surfactants.

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を
水溶液中に混合する方法や、石炭−水スラリーをつくっ
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。
Regarding the method for producing coal-water slurry and the method for adding a thinner, there are two methods: dry pulverizing the coal in advance and then mixing the thinner into an aqueous solution, or adding the thinner after making the coal-water slurry. A method of adding coal, water, and a thinner to a mill and mixing it while crushing the coal, and a method of mixing using cleaned coal instead of coal in each method. can be implemented.

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。
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.

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.O1〜5.0重量%、好ましくは0.03〜20
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、しかも高沸゛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。
As described above, the thinner of the present invention has a viscosity reduction of 0.0% for coal-water slurry. O1-5.0% by weight, preferably 0.03-20
By adding only % by weight, the viscosity of the coal-water slurry can be significantly reduced and a high-boiling coal-water slurry can be produced that can be pumped.

以下に実施例を示す。実施例中%は重量による。Examples are shown below. In the examples, percentages are by weight.

実施例1 所定量の第1表に示す減粘剤を溶解した水溶液に、20
0メツシュ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゛Cにて測定し、また流
動性を観察する。さら←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。
Example 1 Into an aqueous solution containing a predetermined amount of the thinner shown in Table 1,
Coal pulverized to 0 mesh 80% pass is added at room temperature with stirring to prepare a coal-water slurry of a predetermined concentration. The viscosity of this slurry is measured at 25°C and the fluidity is 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.

第2表に示すとおり、本発明の減粘剤を添加すると石炭
濃度72〜77%においても粘度は1100〜3000
 cp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20000 
cp以上になり、全く流動しない。
As shown in Table 2, when the thinner of the present invention is added, the viscosity is 1100 to 3000 even at a coal concentration of 72 to 77%.
cp and has extremely good fluidity. On the other hand, when a general anionic surfactant is added or no thinner is added, the viscosity is 20,000 at a coal concentration of 50%.
CP or more, and there is no flow at all.

本発明の減粘剤は石炭−水スラリーの粘度を著しく減少
せしめ、高濃度の石炭−水スラリーを可能にするととも
に、石炭−水スラリーの安定性をも著しく改良し、1ケ
月間以上静置しても、石炭沈降は生ぜず、また水の分離
も全く生じない。
The thinner of the present invention significantly reduces the viscosity of the coal-water slurry, making it possible to form a highly concentrated coal-water slurry, and also significantly improves the stability of the coal-water slurry, allowing it to stand still for more than one month. However, no coal settling occurs, and no water separation occurs at all.

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
濃度のクリーン化石炭−水スラリーを調整する。石炭粒
度は200メツシュ80%バスのものである。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。
Example 2 A cleaned 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 200 mesh 80% bath. The viscosity of this slurry is measured at 25° (゛), and the fluidity is also observed. After this slurry is allowed to stand for one month, the state of water separation is measured.

試験に用いた本発明の減粘°剤は第1表に示すとおりで
ある。試験結果を第3表に示す。
The viscosity reducing agents of the present invention used in the test are shown in Table 1. The test results are shown in Table 3.

第3表に示すとおり、クリーン化石炭−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1300〜2500cp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50%において粘度が20
000 cp以上になり、全く流動しない。
As shown in Table 3, when the thinner of the present invention is added to the cleaned coal-water slurry, the viscosity is 1300 to 2500 cp even at a coal concentration of 76 to 80%, and the fluidity is extremely good. On the other hand, when a thinner other than the present invention is added or no thinner is added, the viscosity is 20% at a coal concentration of 50%.
000 cp or more and does not flow at all.

(以下余白)(Margin below)

Claims (5)

【特許請求の範囲】[Claims] (1)石炭−水スラリーの粘度を低下させ、流動性を向
lさせるために用いる高濃度石炭−水スラリー用減粘剤
であって、分子内に活性水素を1個以上。 好ましくは3個以上、さらに好ましくは5個以−F有す
るアミンおよびそれらの誘導体を出発物質として、これ
にアルキレンオキシドを付加し、その分子[1000な
いし10万であるポリエーテル化合物または該ポリエー
テル化合物の末端水酸基を各種反応させた誘導体を必須
成分として含有することを特徴とする石炭−水スラリー
用減粘剤。
(1) A thinning agent for highly concentrated coal-water slurry used to reduce the viscosity of the coal-water slurry and improve its fluidity, and contains one or more active hydrogen atoms in the molecule. Preferably, an amine having 3 or more, more preferably 5 or more -F and a derivative thereof is used as a starting material, and an alkylene oxide is added thereto to form a polyether compound or the polyether compound whose molecule is [1,000 to 100,000]. A thinning agent for coal-water slurry, characterized in that it contains as an essential component a derivative obtained by variously reacting the terminal hydroxyl groups of.
(2)前記ポリエーテル化合物の分子量が10000な
いしlO万である特許請求の範囲第1項の石炭−水スラ
リー用減粘剤。
(2) The thinner for coal-water slurry according to claim 1, wherein the polyether compound has a molecular weight of 10,000 to 10,000.
(3)  アルキレンオキシドとしてエチレンオキシド
を含み、その含有率が全アルキレンオキシドの10ない
し95重量%、好ましくは60ないし90重量%である
特許請求の範囲第1項または第2項の石炭−水スラリー
用減粘剤。
(3) The coal-water slurry according to claim 1 or 2, which contains ethylene oxide as the alkylene oxide, and the content thereof is 10 to 95% by weight, preferably 60 to 90% by weight of the total alkylene oxide. Thinning agent.
(4)石炭濃度が61重量%以上、好ましくは70重量
%以上の石炭−水スラリーに用いるための特許請求の範
囲第1項ないし第3項のいずれかの石炭−水スラリー用
減粘剤。
(4) The thinning agent for coal-water slurry according to any one of claims 1 to 3, for use in a coal-water slurry having a coal concentration of 61% by weight or more, preferably 70% by weight or more.
(5)  石炭がクリーン化した石炭である特許請求の
範囲第1項ないし第4項のいずtlかの石炭−水スラリ
ー用減粘剤。
(5) The thinner for coal-water slurry according to any one of claims 1 to 4, wherein the coal is cleaned coal.
JP21037481A 1981-12-25 1981-12-25 Viscosity depressant for highly concentrated coal/water slurry Pending JPS58111893A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21037481A JPS58111893A (en) 1981-12-25 1981-12-25 Viscosity depressant for highly concentrated coal/water slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21037481A JPS58111893A (en) 1981-12-25 1981-12-25 Viscosity depressant for highly concentrated coal/water slurry

Publications (1)

Publication Number Publication Date
JPS58111893A true JPS58111893A (en) 1983-07-04

Family

ID=16588286

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21037481A Pending JPS58111893A (en) 1981-12-25 1981-12-25 Viscosity depressant for highly concentrated coal/water slurry

Country Status (1)

Country Link
JP (1) JPS58111893A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3621319A1 (en) * 1986-06-26 1988-01-14 Bayer Ag Coal/water slurries having improved behaviour under shear stress
US5082498A (en) * 1989-06-21 1992-01-21 Basf Aktiengesellschaft Highly concentrated solid pigment formulations
WO2000018825A1 (en) * 1998-09-28 2000-04-06 Crompton Corporation Organosiloxane containing modified groups in pesticidal compostions
DE212013000244U1 (en) 2012-12-05 2015-07-17 Panasonic Intellectual Property Management Co., Ltd. fridge

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3621319A1 (en) * 1986-06-26 1988-01-14 Bayer Ag Coal/water slurries having improved behaviour under shear stress
US5082498A (en) * 1989-06-21 1992-01-21 Basf Aktiengesellschaft Highly concentrated solid pigment formulations
WO2000018825A1 (en) * 1998-09-28 2000-04-06 Crompton Corporation Organosiloxane containing modified groups in pesticidal compostions
DE212013000244U1 (en) 2012-12-05 2015-07-17 Panasonic Intellectual Property Management Co., Ltd. fridge

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