JPS62232493A - High-concentration coal/water slurry composition - Google Patents
High-concentration coal/water slurry compositionInfo
- Publication number
- JPS62232493A JPS62232493A JP61075499A JP7549986A JPS62232493A JP S62232493 A JPS62232493 A JP S62232493A JP 61075499 A JP61075499 A JP 61075499A JP 7549986 A JP7549986 A JP 7549986A JP S62232493 A JPS62232493 A JP S62232493A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- compound
- compd
- weight
- water
- 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.)
- Granted
Links
- 239000003245 coal Substances 0.000 title claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 239000002002 slurry Substances 0.000 title claims abstract description 30
- 239000000203 mixture Substances 0.000 title claims description 18
- -1 polyoxyethylene group Polymers 0.000 claims abstract description 16
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract description 12
- 125000002947 alkylene group Chemical group 0.000 claims abstract description 9
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000005062 Polybutadiene Substances 0.000 claims abstract description 6
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229920002857 polybutadiene Polymers 0.000 claims abstract description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229940126062 Compound A Drugs 0.000 claims description 9
- NLDMNSXOCDLTTB-UHFFFAOYSA-N Heterophylliin A Natural products O1C2COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC2C(OC(=O)C=2C=C(O)C(O)=C(O)C=2)C(O)C1OC(=O)C1=CC(O)=C(O)C(O)=C1 NLDMNSXOCDLTTB-UHFFFAOYSA-N 0.000 claims description 9
- 150000001875 compounds Chemical class 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 7
- 229910019142 PO4 Inorganic materials 0.000 claims description 2
- 239000012736 aqueous medium Substances 0.000 claims description 2
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 239000010452 phosphate Substances 0.000 claims description 2
- 230000000379 polymerizing effect Effects 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 abstract description 5
- 230000032050 esterification Effects 0.000 abstract description 3
- 238000005886 esterification reaction Methods 0.000 abstract description 3
- 238000006386 neutralization reaction Methods 0.000 abstract description 2
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 abstract 1
- 239000010763 heavy fuel oil Substances 0.000 abstract 1
- 239000000654 additive Substances 0.000 description 16
- 125000001165 hydrophobic group Chemical group 0.000 description 6
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 4
- 230000000996 additive effect Effects 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000012644 addition polymerization Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000002202 Polyethylene glycol Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920001223 polyethylene glycol Polymers 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229920001732 Lignosulfonate Polymers 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- AWMVMTVKBNGEAK-UHFFFAOYSA-N Styrene oxide Chemical compound C1OC1C1=CC=CC=C1 AWMVMTVKBNGEAK-UHFFFAOYSA-N 0.000 description 1
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000002528 anti-freeze Effects 0.000 description 1
- 230000002421 anti-septic effect Effects 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 238000012661 block copolymerization Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- YDEXUEFDPVHGHE-GGMCWBHBSA-L disodium;(2r)-3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Na+].[Na+].COC1=CC=CC(C[C@H](CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O YDEXUEFDPVHGHE-GGMCWBHBSA-L 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 125000003367 polycyclic group Chemical group 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
Landscapes
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、石炭濃度が高いにもかかわらず、低粘度で流
動性に優れた石炭/水スラリー組成物に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a coal/water slurry composition that has low viscosity and excellent fluidity despite having a high coal concentration.
近年の石油代替エネルギーとしての石炭用途開発は、エ
ネルギー源としての石油が長期的供給安定性に不安があ
ること、ハンドリングコストを含めても石油よシ経済的
であると考えられることから、世界的に推進されている
。石炭のハンドリングの主たる問題点は、固体である為
パイプライン輸送やタンク貯蔵が困難であること、灰分
な有すること等であるが、これらの点を考慮したハンド
リング技術として、石炭/重油スラリー(COM)、石
炭/水スラリー(CWMあるいはcws ) 、石炭/
メタノールスラリー(Methacoal)等のスラリ
ー組成物が検討されている。そして、これらスラリー組
成物の媒体としては、安価かつ供給の容易な水を利用す
る方法が実用的であり、研究の中心となっている。In recent years, the development of the use of coal as an energy alternative to petroleum has become a global trend, as oil as an energy source is uncertain about its long-term supply stability and is considered to be more economical than petroleum, even when handling costs are included. is being promoted. The main problems in handling coal are that it is solid, making it difficult to transport by pipeline or storing in tanks, and that it has a high ash content. ), coal/water slurry (CWM or cws), coal/
Slurry compositions such as methanol slurry (Methacoal) are being considered. As a medium for these slurry compositions, it is practical to use water, which is inexpensive and easy to supply, and is the focus of research.
石炭は、分子中に水酸基やカル辻rン酸基等の親水性の
基を有してはいるものの、全体としては疎水性であり、
多量の石炭微粉末を水と混合した場合、水に良く湿潤し
ないために均一な分布状態とはならず、流動性が著しく
悪いスラリーとなシ、現状においては最大でも60チ程
度の石炭濃度のスラリーが得られるにすぎない。石炭/
水スラリーが燃料として有効に働らく為には、水の蒸発
潜熱を考慮に入れ、少なくとも石炭濃度として7oチ以
上のものが一般に要望されている。これを達成する為に
、適証な石炭の微粒分布状態と、石炭と水の間に介在し
、石炭の分散を保持し、かつ流動性を向上することので
きる界面活性剤であるところの添加剤の検討がなされて
いる。Although coal has hydrophilic groups such as hydroxyl groups and carboxylic acid groups in its molecules, it is hydrophobic as a whole.
When a large amount of fine coal powder is mixed with water, it does not wet well with water and is not evenly distributed, resulting in a slurry with extremely poor fluidity. All you get is a slurry. coal/
In order for water slurry to work effectively as a fuel, a coal concentration of at least 70% is generally required, taking into consideration the latent heat of vaporization of water. In order to achieve this, we need to ensure that the coal particles are properly distributed and that a surfactant is added between the coal and water that can maintain the dispersion of the coal and improve its fluidity. Agents are being considered.
従来、高濃度石炭/水スラリーを得る目的で使用検討さ
れた添加剤としては、リグニンスルホン酸塩(特開昭5
7−96090など)、多環系芳香族スルホン酸塩ホル
マリン縮金物(特開昭57−145193など)、ある
いは本発明で用いる化合物に類似のポリエーテル化合物
(特開昭57−147595など)等がある。これらは
、それぞれに特徴ある添加剤ではあるが、7oチの石炭
濃度のスラリーにするには、比較的多量の添加を要する
とか、流動性の面で不十分であるといつた問題点がある
。Conventionally, lignin sulfonate (Japanese Unexamined Patent Application Publication No. 1989-1999
7-96090, etc.), polycyclic aromatic sulfonate formalin condensates (Japanese Patent Publication No. 57-145193, etc.), or polyether compounds similar to the compounds used in the present invention (Japanese Patent Application Publication No. 57-147595, etc.). be. Each of these additives has its own characteristics, but they have problems such as requiring a relatively large amount to be added in order to make a slurry with a coal concentration of 70%, and their fluidity being insufficient. .
添加剤による高濃度石炭/水スラリーの作製は、添加剤
コストがスラリとしてのトータルコストを上昇せしめ、
石油代替としてのコストメリットを無くする様では意味
が無く、したがって添加剤が安価であるか、あるいは少
量の添加で目的のスラリーを与えるものである事が要求
される。When creating a highly concentrated coal/water slurry using additives, the cost of the additives increases the total cost of the slurry.
There is no point in eliminating the cost advantage as a petroleum substitute, so it is required that the additive be inexpensive or that it can provide the desired slurry by adding a small amount.
本発明の目的は、即ち、この要求に合致し、重油並みの
輸送と燃焼が可能な石炭/水スラリー組成物を提供する
ことにある。The object of the present invention is to provide a coal/water slurry composition that meets this requirement and is transportable and combustible on a par with heavy oil.
本発明によれば、下記化合物Aおよび/またはBの存在
下に、水性媒体中に、少なくとも60重量%の石炭を低
粘度で微粒懸濁させたことを特徴とする、高濃度石炭/
水スラリー組成物が提供される。According to the present invention, high concentration coal/
A water slurry composition is provided.
化合物A:ポリブタジェングリコールを、エチレンオキ
サイドと炭素数3以上のア
ルキレンオギサイドを付加重合して
得られる、ポリアルキルエーテル化
合物。Compound A: A polyalkyl ether compound obtained by addition polymerizing polybutadiene glycol with ethylene oxide and alkylene oxide having 3 or more carbon atoms.
化合物B:化合物Aの硫醗エステル塩あるいはリン酸エ
ステル塩。Compound B: Compound A sulfur ester salt or phosphate ester salt.
本発明においては、好ましくは、水性媒体中に、添加剤
として前記化合物Aおよび/またはBを、石炭に対し0
.1〜10重量%存在させ、全量中60重量%以上の石
炭を、200メツシュ(74μm)パス約70%以上の
粒径で、低粘度に懸濁した石炭/水スラリー組成物が提
供される。In the present invention, preferably, the compound A and/or B is added to the aqueous medium as an additive to the coal.
.. A coal/water slurry composition is provided in which 1 to 10% by weight of coal is present, and 60% by weight or more of the total amount of coal is suspended in a low viscosity with a particle size of about 70% or more in a 200 mesh (74 μm) pass.
本発明において添加剤として使用する化合物は、付加さ
れたアルキレンオキサイド全体に対してポリオキシエチ
レン基を40〜100重量%、好ましくは70〜100
重量%含有し、末端に必らずポリオキンエチレン基を有
する、ポリブタジェングリコールのポリアルキルエーテ
ル−化合物(化合物A)と、その硫酸エステル塩あるい
はリン酸エステル塩(化合物B)であシ、分子量が5,
000〜10’0.000の化合物である。The compound used as an additive in the present invention contains 40 to 100% by weight of polyoxyethylene groups, preferably 70 to 100% by weight, based on the total added alkylene oxide.
A polyalkyl ether compound of polybutadiene glycol (compound A) containing % by weight and always having a polyoxine ethylene group at the end, and its sulfuric acid ester salt or phosphoric acid ester salt (compound B), molecular weight is 5,
000 to 10'0.000.
添加剤は、そのイオン性、親水基の種類、疎水基の種類
、親水基と疎水基の結合構造、親水基と疎水基の量比や
分子量によってその性能が大きく左右されるけれども、
本発明に有用な化合物は、特に、疎水基の種類、親水基
と疎水基の量比、および分子量のバランスによって、目
的とする性能を達成するものである。The performance of additives is greatly influenced by their ionicity, the type of hydrophilic group, the type of hydrophobic group, the bond structure between hydrophilic and hydrophobic groups, the ratio of amounts of hydrophilic and hydrophobic groups, and the molecular weight.
Compounds useful in the present invention are those that achieve the desired performance, particularly by controlling the type of hydrophobic group, the ratio of amounts of hydrophilic groups to hydrophobic groups, and the balance of molecular weight.
化合物Aの合成は、分子量1,000〜4,000のポ
リブタジェングリコールに、通常の条件でエチレンオキ
サイド、ノロピレンオキサイド、ブチレンオキサイド、
スチレンオキサイド等を付加重合する。付加重合は、こ
れらアルキレンオキサイドをブロック重合してもよいし
、ランダム重合してもよいが、好ましくはブロック共重
合が採用される。エチレンオキサイドは、アルキレンオ
キサイド中親水基を形成するものであって、その一部又
は全量を末端基形成する様に付加重合するのがよい。ポ
リブタジェングリコールは疎水基であシ、エチレンオキ
サイドのみを付加重合して化合物Aを形成してもかまわ
ない。これら重合に際し、微量に存在する水によってポ
リエチレングリコール等が副生ずると、充分な性能を発
揮し得ないことはあきらかであシ、かかる副生がない様
合成を行うO
化合物Bは、化合物Aを通常の条件で硫酸エステル化あ
るいはリン酸エステル化し、次いで有機系、無機系のア
ルカリで中和して得られる。Compound A was synthesized by adding ethylene oxide, nolopyrene oxide, butylene oxide,
Addition polymerization of styrene oxide, etc. The addition polymerization may be performed by block polymerization or random polymerization of these alkylene oxides, but block copolymerization is preferably employed. Ethylene oxide forms a hydrophilic group in alkylene oxide, and it is preferable to add-polymerize part or all of it to form a terminal group. Since polybutadiene glycol is a hydrophobic group, compound A may be formed by addition polymerization of only ethylene oxide. During these polymerizations, it is clear that if polyethylene glycol or the like is produced as a by-product due to the presence of a trace amount of water, sufficient performance cannot be achieved. It is obtained by sulfuric acid esterification or phosphoric acid esterification under normal conditions, and then neutralization with an organic or inorganic alkali.
石炭は、脱灰した石炭あるいは脱灰してない石炭で、し
かもいずれの炭種のものでも使用することができる。ま
た、石炭は、粗粉砕した後、添加剤を含む水を加え、湿
式粉砕機にて微粉砕スラリーとするか、あらかじめ乾式
粉砕機にて微粉砕した後、添加剤を含む水と混合ス/F
IJ−とするいずれの方法をとってもよい。スラリー
中の石炭粒径は、200メツシー(74μm)フルイ通
過量として約70チ以上、好ましくは約80チ以上にす
ることが望ましい。一般には、石炭粒径は微粒である程
燃焼の際に着火性が向上するが、スラリー性状としては
、表面積が増加することによ)、添加剤量を増さないと
高粘度になるかあるいは凝集をおこす等、負の面も出て
くる。しかし、本発明組成物においてはこの様な問題は
少ない。使用する石炭の濃度は、石炭/水スラリー中約
60%以上、好ましくは70〜75チである。水は、流
動化の媒体として一番安価なものであるが、燃焼の際蒸
発潜熱を奪いカロリーロスとなる。更に、その量が増せ
ば滅火の原因ともな9うるため、できる限9少い水量が
望ましい。この点から、一般的に70%以上の石炭濃度
が指向されておシ、本発明ではこの濃度が達成され、し
かも低粘度のスラリーを与える。低粘度であることは、
輸送が容易であるばかシでなく、通常の燃焼装置で噴霧
燃焼が可能となることを意味し、極めて有利である。The coal may be deashed coal or non-deashed coal, and any type of coal can be used. In addition, after coarsely pulverizing the coal, water containing additives is added to form a finely pulverized slurry in a wet pulverizer, or the coal is first pulverized in a dry pulverizer and then mixed with water containing additives. F
Any method of setting IJ- may be used. The coal particle size in the slurry is desirably about 70 inches or more, preferably about 80 inches or more, as the amount passing through a 200 mesh (74 μm) sieve. In general, the finer the coal particle size, the better the ignitability during combustion, but the slurry properties (due to an increase in surface area) may become highly viscous or viscous if the amount of additive is not increased. There are also negative aspects such as agglomeration. However, such problems are rare in the composition of the present invention. The concentration of coal used is about 60% or more in the coal/water slurry, preferably 70-75%. Water is the cheapest fluidizing medium, but it absorbs latent heat of vaporization during combustion, resulting in calorie loss. Furthermore, if the amount increases, it may cause the fire to go out, so it is desirable to reduce the amount of water as much as possible. From this point of view, a coal concentration of 70% or more is generally desired, and the present invention achieves this concentration while still providing a slurry of low viscosity. Low viscosity means
This is extremely advantageous as it means that spray combustion can be carried out in a normal combustion device rather than in a bulky container that is easy to transport.
なお、本発明の石炭/水スラリー組成物中には、脱気、
防錆、防腐、凍結防止や安定性改良を目的とする薬剤の
添加も可能である。Note that the coal/water slurry composition of the present invention includes deaeration,
It is also possible to add chemicals for the purpose of rust prevention, antiseptic, antifreeze, and stability improvement.
次に、本発明を実施例により更に説明する。なお、実施
例中の部及びチは、特記しない限り、重量を基準とする
。Next, the present invention will be further explained by examples. In addition, unless otherwise specified, parts and parts in the examples are based on weight.
実施例1
太平洋炭(揮発分42.3%、灰分14.9%、全80
.19%)を、ハンマーミルで2,300 r、p、m
。Example 1 Pacific coal (volatile content 42.3%, ash content 14.9%, total 80
.. 19%) in a hammer mill for 2,300 r, p, m
.
の回転数で粉砕し、200メツシュパス50%、平均粒
子径70μmのものを得た。The powder was crushed at a rotational speed of 200 mesh passes 50% and an average particle size of 70 μm.
次に、本発明の添加剤を表1に示す配合にて、総量で0
.7部を水60部に溶解後、140部の上記石炭粗粒を
加え、ニーダ−にて充分混線後、ボールミルにて6 O
r、p、m、で2時間湿式粉砕し、流動性良好な石炭/
水スラIJ−200部を得た。Next, the additives of the present invention were added in the formulation shown in Table 1 in a total amount of 0.
.. After dissolving 7 parts in 60 parts of water, 140 parts of the above coarse coal particles were added, and after thorough mixing in a kneader, the mixture was heated to 6 O in a ball mill.
Coal with good fluidity was wet-pulverized for 2 hours at r, p, m.
200 parts of water slurry IJ was obtained.
添加剤の比較例として、リグニンスルホン醗ナトリウム
、ナフタリノスルホン酸ナトリウムホルマリン縮金物、
またはポリエチレングリコール(分子量20,000)
を、それぞれ、4部加えtll製した結果を表1に示す
。Comparative examples of additives include sodium lignin sulfonate, sodium naphthalinosulfonate formalin condensate,
or polyethylene glycol (molecular weight 20,000)
The results are shown in Table 1.
なお、表中の記号については、表2の後に記す。Note that the symbols in the table are described after Table 2.
表中の物性値は、それぞれ下記の方法にて測定した。The physical property values in the table were measured using the methods described below.
200メツシュパスチ
作製した石炭/水スラ!J −3,9を、水にて50倍
に希釈し、最低200メツシュのふるい上に流し込み、
振とり開始後llの水で洗い、ふるい上の石炭を乾燥秤
量し、算出する(振とう時間10分)。Coal/water slurry made with 200 mesh pasties! J-3,9 was diluted 50 times with water and poured onto a sieve of at least 200 mesh.
After starting shaking, wash with 1 liter of water, dry and weigh the coal on the sieve, and calculate (shaking time 10 minutes).
測定機:ふるい振とう機VSS−50(筒井理化学器械
製)
粘度
作製した石炭/水スラリー3−を、カップに入れ、EL
D−8T型ローターにて3分後の粘度を測定した。回転
数2 Or、p、m、 (7sec””’ ) 、測定
温度30℃。Measuring device: Sieve shaker VSS-50 (manufactured by Tsutsui Rikagaku Kikai) Put the prepared coal/water slurry 3- into a cup and EL
The viscosity was measured after 3 minutes using a D-8T type rotor. Rotation speed: 2 Or, p, m, (7 sec""'), measurement temperature: 30°C.
測定機:E凰回転粘度計(東京計器製)静置安定性
作製した石炭/水スラリー約200−を、メスシリンダ
ーに入れて静置し、1週間後の状態を棒貫入し、観察し
た。Measuring device: E-o rotational viscometer (manufactured by Tokyo Keiki) Static stability Approximately 200 mm of the prepared coal/water slurry was placed in a graduated cylinder and allowed to stand, and the state after one week was observed by penetrating the cylinder with a rod.
以下余白
実施例2
南アフリカ炭(揮発分33.3%、灰分9.6%、全5
O66%)を、微粉砕盤ハンマーミルで粉砕し、200
メツシュパス78チのものを得た。Below is the margin Example 2 South African coal (volatile content 33.3%, ash content 9.6%, total 5
066%) was pulverized with a fine grinding machine hammer mill, and 200%
I got a mesh pass of 78 inches.
次に本発明の添加剤を、表2に示す配合にて総量で0.
7部を水60部に溶解後、140部の上記石炭微粉を加
え、オートホモミキサー(特殊機化製)にて4.00
Or、p、m、で5分間混合し、流動性良好な石炭/水
スラリー200部を得た。Next, the additives of the present invention were added in the formulation shown in Table 2 in a total amount of 0.
After dissolving 7 parts in 60 parts of water, add 140 parts of the above fine coal powder, and mix with an autohomogen mixer (manufactured by Tokushu Kika) to 4.00 parts.
Mixing was carried out for 5 minutes using Or, p, m, to obtain 200 parts of coal/water slurry with good fluidity.
物性値を、実施例1に示す方法にて測定した。Physical property values were measured by the method shown in Example 1.
同様に、添加剤の総量で0.75部あるいは1,05部
を水50部に溶解後、150部の上記石炭微粉を加えて
調製した場合も、流動性良好なスラリーが得られた。Similarly, slurries with good fluidity were also obtained when 0.75 parts or 1.05 parts of the total amount of additives were dissolved in 50 parts of water and then 150 parts of the above fine coal powder was added.
添加剤の比較例として、表1に例示のものを、それぞれ
、4部加えて調製した結果を示した。As a comparative example of additives, the results were shown by adding 4 parts of each of the additives shown in Table 1.
以下余白 尚、表1及び表2において各記号は下記を意味する。Margin below In addition, each symbol in Table 1 and Table 2 means the following.
PBG :ポリブタジエングリコール RO:アルキレンオキサイド PO:fロビレンオキサイド EO:エチレンオキサイドPBG: Polybutadiene glycol RO: alkylene oxide PO: f Robylene oxide EO: Ethylene oxide
Claims (1)
体中に、少なくとも60重量%の石炭を低粘度で微粒懸
濁させたことを特徴とする、高濃度石炭/水スラリー組
成物。 化合物A:ポリブタジエングリコールに、エチレンオキ
サイドと炭素数3以上のアルキレンオキサイドを付加重
合して得られる、ポリアルキルエーテル化合物。 化合物B:化合物Aの硫酸エステル塩あるいはリン酸エ
ステル塩。 2、化合物AまたはBが、分子中に付加されたアルキレ
ンオキサイド全体に対してポリオキシエチレン基を40
〜100重量%好ましくは70〜100重量%含有し、
末端に必らずポリオキシエチレン基を有し、かつ、5,
000〜100,000の分子量を有する特許請求の範
囲第1項記載の組成物。 3、組成物を構成する石炭の粒径が、200メッシュ(
74μm)パス約70%以上である特許請求の範囲第1
項又は第2項記載の組成物。 4、石炭に対し、0.1〜1.0重量%の化合物Aおよ
び/またはBを含む特許請求の範囲第1〜3項のいずれ
かに記載の組成物。[Claims] 1. Highly concentrated coal/, characterized in that at least 60% by weight of coal is finely suspended with low viscosity in an aqueous medium in the presence of the following compounds A and/or B: Water slurry composition. Compound A: A polyalkyl ether compound obtained by addition polymerizing ethylene oxide and alkylene oxide having 3 or more carbon atoms to polybutadiene glycol. Compound B: Compound A sulfate ester salt or phosphate ester salt. 2. Compound A or B has 40 polyoxyethylene groups on the entire alkylene oxide added to the molecule.
-100% by weight, preferably 70-100% by weight,
necessarily have a polyoxyethylene group at the end, and 5,
A composition according to claim 1 having a molecular weight of 000 to 100,000. 3. The particle size of the coal constituting the composition is 200 mesh (
74 μm) pass approximately 70% or more
The composition according to item 1 or 2. 4. The composition according to any one of claims 1 to 3, which contains 0.1 to 1.0% by weight of compounds A and/or B based on coal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61075499A JPS62232493A (en) | 1986-04-03 | 1986-04-03 | High-concentration coal/water slurry composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61075499A JPS62232493A (en) | 1986-04-03 | 1986-04-03 | High-concentration coal/water slurry composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62232493A true JPS62232493A (en) | 1987-10-12 |
JPH0579277B2 JPH0579277B2 (en) | 1993-11-01 |
Family
ID=13578016
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61075499A Granted JPS62232493A (en) | 1986-04-03 | 1986-04-03 | High-concentration coal/water slurry composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62232493A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0982337A2 (en) * | 1998-08-28 | 2000-03-01 | Basf Corporation | Compound and coating compositions for adhesion to olefinic substrates |
NL1012561C2 (en) * | 1999-07-09 | 2001-01-10 | Dsm Nv | Thermoplastic block copolyester elastomer. |
US6939916B2 (en) * | 2000-11-07 | 2005-09-06 | Basf Corporation | Adhesion promoter, coating compositions for adhesion to olefinic substrates and methods therefor |
-
1986
- 1986-04-03 JP JP61075499A patent/JPS62232493A/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0982337A2 (en) * | 1998-08-28 | 2000-03-01 | Basf Corporation | Compound and coating compositions for adhesion to olefinic substrates |
EP0982337A3 (en) * | 1998-08-28 | 2000-04-26 | Basf Corporation | Compound and coating compositions for adhesion to olefinic substrates |
US6300414B1 (en) | 1998-08-28 | 2001-10-09 | Basf Corporation | Additive for coating compositions for adhesion to TPO substrates |
NL1012561C2 (en) * | 1999-07-09 | 2001-01-10 | Dsm Nv | Thermoplastic block copolyester elastomer. |
WO2001004174A1 (en) * | 1999-07-09 | 2001-01-18 | Dsm N.V. | Thermoplastic block copolyester elastomer |
US6939916B2 (en) * | 2000-11-07 | 2005-09-06 | Basf Corporation | Adhesion promoter, coating compositions for adhesion to olefinic substrates and methods therefor |
Also Published As
Publication number | Publication date |
---|---|
JPH0579277B2 (en) | 1993-11-01 |
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