JPS59179697A - Preparation of aqueous slurry of carbon-containing composition - Google Patents

Preparation of aqueous slurry of carbon-containing composition

Info

Publication number
JPS59179697A
JPS59179697A JP5727983A JP5727983A JPS59179697A JP S59179697 A JPS59179697 A JP S59179697A JP 5727983 A JP5727983 A JP 5727983A JP 5727983 A JP5727983 A JP 5727983A JP S59179697 A JPS59179697 A JP S59179697A
Authority
JP
Japan
Prior art keywords
carbon
containing composition
water
weight
slurry
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
JP5727983A
Other languages
Japanese (ja)
Inventor
Hayamizu Ito
伊東 速水
Shuhei Tatsumi
巽 修平
Shoichi Takao
彰一 高尾
Jintaro Suzuki
鈴木 仁太郎
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.)
Kawasaki Heavy Industries Ltd
Kawasaki Motors Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
Kawasaki Jukogyo KK
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 Kawasaki Heavy Industries Ltd, Kawasaki Jukogyo KK filed Critical Kawasaki Heavy Industries Ltd
Priority to JP5727983A priority Critical patent/JPS59179697A/en
Publication of JPS59179697A publication Critical patent/JPS59179697A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prepare the titled aqueous slurry causing no scattering or explosion of dust and having excellent fluidity, by adding water and an additive to a carbon-containing composition with special properties. CONSTITUTION:Water and when necessary, 0.01-5wt% additive (e.g. salt of fatty oil sulfate) are added to a carbon-containing composition consisting mainly of petroleum coke, coal, heavy oil, etc. and having a carbon content of 82- 98wt% (water and mineral oil-free basis), a hydrogen atom/carbon atom ratio of 0.001-0.10 (water and mineral oil-free basis), an adsorbed water content of 0.1- 6wt% and a specific surface area of 0.01-7g/m<2>. The mixture is crushed to obtain an aqueous slurry having such a particle size distribution that particles of 200 mesh or smaller accout for 40-90wt%, a carbon-containing composition concentration of 70wt% or highr and a viscosity of below 1,000cP (25 deg.C).

Description

【発明の詳細な説明】 未発明は特定の性状範囲に入る石油コークス、重質油、
脱れきアスファルト、石炭などの各種炭素含有組成物を
用いて水スラリーを製造する方法に関するものである。
[Detailed description of the invention] The uninvented invention is petroleum coke, heavy oil,
The present invention relates to a method for producing a water slurry using various carbon-containing compositions such as deasphalted asphalt and coal.

近年、石油供給の不安定化のため、石油コークス、重質
油、脱れきアスファルト、石炭などの各種炭素含有組成
物を有効利用する技術開発が進められている。たとえば
石油コークス、重質油、脱れきアスファルト、石炭など
の有効利用技術としては、熱分解、ガス化、燃焼あるい
は鉄鋼業における高炉吹込重油の代替燃料、セメントキ
ルンの重油の代替燃料など種々のものが考えられる。し
かしこのような各種利用技術において、炭素含有組成物
は常温で固体であるために、ハンドリングが困難である
上、粉塵飛散による公害発生や粉塵爆発の危険があるな
どの短所があり、利用が困難になっている。したがって
こうした炭素含有組成物の流体化を図り、ハンドリング
を容易にし公害発生や危険を防止することが望まれる。
In recent years, due to the instability of petroleum supply, technological development has been progressing to effectively utilize various carbon-containing compositions such as petroleum coke, heavy oil, deasphalted asphalt, and coal. For example, there are various technologies for effectively utilizing petroleum coke, heavy oil, deasphalted asphalt, coal, etc., such as pyrolysis, gasification, combustion, alternative fuels for blast furnace injection heavy oil in the steel industry, and alternative fuels for heavy oil in cement kilns. is possible. However, in these various utilization technologies, carbon-containing compositions are difficult to handle because they are solid at room temperature, and there are disadvantages such as the risk of pollution due to dust scattering and the risk of dust explosions, making it difficult to use carbon-containing compositions. It has become. Therefore, it is desirable to make such carbon-containing compositions into fluids to facilitate handling and prevent pollution and danger.

一方、炭素含有組成物の輸送コストを下げるためにも、
流体化して輸送するのが効果的である。
On the other hand, in order to reduce the transportation cost of carbon-containing compositions,
It is effective to transport it as a fluid.

以、にのよりな口(k+のために、炭素含有組成物を流
体化する方法として、スラリー化するのが効果的である
が、このスラリーを熱分解、ガス化−燃焼あるいは高炉
への吹込、セメントキルンの燃判などに利用するだめに
は濃度が高い方が望ましい。
In order to obtain a more suitable solution (k+), an effective method for fluidizing a carbon-containing composition is to form it into a slurry. A higher concentration is preferable for use as a fuel for cement kilns.

また輸送効率を高めるためにもやはり濃度が高い方が望
ましい。すなわち濃度が無水分基準で70重量%以上、
粘度が25℃で1000 cp程度以下の性状含有する
スラリーであることが要求され、こうした性状のスラリ
ーを製造しなければならない。
Furthermore, in order to increase transport efficiency, it is desirable that the concentration is high. That is, the concentration is 70% by weight or more on a moisture-free basis,
A slurry is required to have a viscosity of about 1000 cp or less at 25°C, and a slurry with such properties must be manufactured.

未発明者らは上記の諸点に鑑み、炭素含有組成物の流体
化の方法について鋭意研究を進めた結果、ある特定の性
状範囲に入る炭素含有組成物について、炭素含有組成物
の濃度が70重量%以上で流動性に富み、かつ粉塵飛散
、粉塵燥発の起こらない水スラリー組成物を製造する方
法を知見し、本発明を完成させるに至った。
In view of the above-mentioned points, the inventors conducted intensive research on a method of fluidizing carbon-containing compositions, and found that for carbon-containing compositions that fall within a certain property range, the concentration of the carbon-containing composition is 70% by weight. The present inventors have discovered a method for producing an aqueous slurry composition that is highly fluid and does not cause dust scattering or dust drying, and has completed the present invention.

すなわち炭素含有率が無水分、無鉱物基準で82〜98
重量%、無水分、無鉱物基準での酸素原子数/炭素原子
数の比が0001〜010であシ、吸着水分が0.01
〜6重量%、比表面積が0.0−1〜72イ/1の性状
の炭素含有組成物に、水と必要に応じて炭素含有組成物
に対し0.01〜5重爾%、望ましくは01〜1.5重
量%の添加剤を添加し、組成物の粒度を200メツシュ
以下40〜90重量%、望ましくは200メツシュ以下
50〜80重量%に調整し、炭素含有組成物濃度70重
量%以上で、粘度1000 cp(25℃)程度以下の
流動性に富むスラリーを製造するものである。なお炭素
含有組成物の性状の確認は、表1に記載した方法で行な
うのが望捷しいが、これ以外の方法でもよい。
In other words, the carbon content is 82 to 98 on a moisture-free and mineral-free basis.
The ratio of the number of oxygen atoms/the number of carbon atoms on a weight%, moisture-free, mineral-free basis is 0001 to 010, and the adsorbed moisture is 0.01.
~6% by weight of the carbon-containing composition having a specific surface area of 0.0-1 to 72 I/1, and optionally water and preferably 0.01 to 5% by weight of the carbon-containing composition. 01 to 1.5% by weight of additives are added, the particle size of the composition is adjusted to 40 to 90% by weight below 200 mesh, preferably 50 to 80% by weight below 200 mesh, and the carbon-containing composition concentration is 70% by weight. In the above manner, a highly fluid slurry having a viscosity of about 1000 cp (25° C.) or less is produced. It is preferable to check the properties of the carbon-containing composition by the method shown in Table 1, but other methods may be used.

(以下余白) 表     1 すなわち本発明の方法は、石油コークス、重質油、脱れ
きアスファルト、石炭などの炭素含有組成物に水、必要
に応じて添加剤を加えてスラIJ +を製造するに当た
9、無水分、無鉱物基準での炭素含有率が82〜98重
量%、無水分、無鉱物基準での酸素原子数/炭素原子数
の比が0001〜0、10、吸着水分が0.01〜6重
量%、比表面積が001〜7 mf / gの性状の炭
素含有組成物の粒度を200メツシユ以下が40〜90
重量%になるように調整し、水、必要に応じて添加剤を
添加して、炭素含有組成物濃度70重単形以上のスラリ
ーを製造することを特徴としている。
(The following is a blank space) Table 1 In other words, the method of the present invention involves adding water and additives as necessary to a carbon-containing composition such as petroleum coke, heavy oil, deasphalted asphalt, and coal to produce sludge IJ+. Hit 9, carbon content on moisture-free and mineral-free basis is 82 to 98% by weight, ratio of oxygen atoms / carbon atoms on moisture-free and mineral-free basis is 0001 to 0, 10, adsorbed moisture is 0 The particle size of the carbon-containing composition having the properties of .01 to 6% by weight and a specific surface area of 0.01 to 7 mf/g is 200 mesh or less, 40 to 90.
The slurry is characterized in that the carbon-containing composition concentration is adjusted to % by weight, and water and additives are added as necessary to produce a slurry having a carbon-containing composition concentration of 70 monomers or more.

図面は、太発明者らが実施した実験結果を示したもので
ある。表2にA−Jの10種類の各種炭素含有組成物の
性状を示した。これらのうち、A〜Fの6種類は本発明
で規定した性状の範囲に入る炭素含有組成物である。こ
れらの組成物を200メツシュ通過率70重世%の粒度
に粉砕した後、アニオン系添加剤を炭素含有組成物に対
し1重量%添加し、さらに水を加えて濃度調整した後、
充分混合しスラリー化した。調整スラリーの粘度をB型
粘度計によυ測定した結果は、図面に示したけ ように本発明の範囲に入る炭素含有組成物V、いずれも
濃度70重量%で粘度1000 cp(25℃)以下の
流動性のあるスラリーが得られた。逆に本発明の範囲か
らにずれる性状の炭素含有組成物を用いた場合には、い
ずれも濃度70重量%で粘度が1000cp(25℃)
よシも高いスラリーとなった。なお添加剤を用いなくて
も未発明の目的を達成することができるが、でき得れば
添加剤を添加するのが望ましい。
The drawings show the results of experiments conducted by the inventors. Table 2 shows the properties of 10 types of various carbon-containing compositions A-J. Among these, six types A to F are carbon-containing compositions that fall within the range of properties defined in the present invention. After pulverizing these compositions to a particle size with a 200 mesh pass rate of 70%, 1% by weight of an anionic additive was added to the carbon-containing composition, and water was further added to adjust the concentration.
The mixture was thoroughly mixed to form a slurry. The viscosity of the prepared slurry was measured using a B-type viscometer.As shown in the drawing, the carbon-containing composition V falls within the scope of the present invention, and both have a viscosity of 1000 cp (at 25°C) or less at a concentration of 70% by weight. A fluid slurry was obtained. Conversely, when a carbon-containing composition with properties that deviate from the scope of the present invention is used, the viscosity is 1000 cp (25°C) at a concentration of 70% by weight.
The result was a very high slurry. Although the uninvented object can be achieved without using additives, it is desirable to add additives if possible.

(以下余白) 表      2 本発明において用いられる添加剤としては、アニオン系
、カチオン系、/ニオン系の界面活性剤などを単独でま
たは組み合わせて用いられ、炭種によって適宜選択され
る。具体的には、アニオン系界面活性剤としては、脂肪
油硫酸エステル塩、高級アルコール硫酸エステル塩、非
イオンエーテル硫酸エステル塩、オレフィン硫酸エステ
ル塩、アルキルアリルスルホン酸塩、二塩基酸エステ、
ルスルホン酸塩−ジアルキルスルホこはく酸塩、アシル
ザルコシネート、アルキルベンゼンスルホン酸塩、アル
キルリ酸エステル塩、ポリオキシエチレンアルキル(ア
ルキルフェノール)硫酸エステル塩、アルキルリン酸エ
ステル塩、ジアルキルスルホコハク酸エステル塩、アク
リル酸もしくハ/および無水マレイン酸共重合体、多環
式芳香族スルホン化物もしくはホルマリン化合物などが
使用され、カチオン系界面活性剤としては、アlレキル
アミン塩、第4級アミン塩などが使用され、ノニオン系
界面活性剤としては、ポリオキシアルキルエーテル−ポ
リオキシエチレンアルキルフェノールエーテル、オキシ
エチレン・オキシプロピレンブロンクボリマー、ポリオ
キシエチレンアルキルアミン、ソルビクン脂肪酸エステ
ル、ポリオキシエチレンソルビクン脂肪酸エステル、ア
ルキルトリメチルアンモニクムクロライド、アルキルジ
〆チルベンジルアンモニクムクロライド、アルキルビi
)ジニクム塩、ポリオキシエチレン脂肪酸ニスデル−脂
肪族アルコールポリオキシエチレンエーテル、アルキル
フェノールポリオキシエチレンエーテル、多価アルコー
ル脂肪酸エステル、脂肪酸のエタノールアマイドなどが
用因られ、両性系界面活性剤としては、アルキルベクイ
ンなどが(1され、また1、2,3モノアミン、ジアミ
ンなどのアミン化合物、高級アルキルアミン酸などが用
いられる。
(The following is a blank space) Table 2 The additives used in the present invention include anionic, cationic, and/or ionic surfactants, used alone or in combination, and are appropriately selected depending on the type of coal. Specifically, the anionic surfactants include fatty oil sulfate ester salts, higher alcohol sulfate ester salts, nonionic ether sulfate ester salts, olefin sulfate ester salts, alkylaryl sulfonates, dibasic acid esters,
Rusulfonate - dialkyl sulfosuccinate, acyl sarcosinate, alkylbenzene sulfonate, alkyl phosphate ester salt, polyoxyethylene alkyl (alkylphenol) sulfate ester salt, alkyl phosphate ester salt, dialkyl sulfosuccinate ester salt, acrylic acid Alternatively, c/and a maleic anhydride copolymer, a polycyclic aromatic sulfonated product, or a formalin compound, etc. are used, and as the cationic surfactant, an allekylamine salt, a quaternary amine salt, etc. are used, Examples of nonionic surfactants include polyoxyalkyl ether-polyoxyethylene alkylphenol ether, oxyethylene/oxypropylene bronze polymer, polyoxyethylene alkylamine, sorbicun fatty acid ester, polyoxyethylene sorbicun fatty acid ester, and alkyltrimethyl ammonicum. Chloride, alkyldimethylbenzyl ammonicum chloride, alkylbi I
) dinicum salt, polyoxyethylene fatty acid Nisdel-aliphatic alcohol polyoxyethylene ether, alkylphenol polyoxyethylene ether, polyhydric alcohol fatty acid ester, fatty acid ethanolamide, etc. In addition, amine compounds such as 1, 2, 3 monoamines and diamines, higher alkyl amine acids, etc. are used.

つぎに本発明の実施例について説明する実施例1 表3に示す性状の石油コークスを、3 HIN以下に粗
砕した後、12kに!/hcドライベース)で湿式ボー
ルミルに導入し、同時にアニオン系添加剤を180 g
/h (有効1戊分40%)で加え、さらに石油コーク
ス濃度が72重僧形となるよう水を供給し、湿式ボール
ミルで石油コークスの粒度が200メツシュ以下75重
量%となるように粉砕し、出口から72重量%のスラ1
ノーを排出させた。製品スラリーの粘度をB型粘度計で
測定した結果−880cp(25℃)であシ流動性が良
く、通常の遠心ポンプあるいはプランジャーポンプによ
シ配管中を流送させることができた。
Next, Examples of the present invention will be described.Example 1 Petroleum coke having the properties shown in Table 3 was crushed to 3 HIN or less, and then to 12K! /hc dry base) into a wet ball mill, and at the same time 180 g of anionic additive
/h (effective 1 minute 40%), water was further supplied so that the petroleum coke concentration was 72 folds, and crushed in a wet ball mill so that the petroleum coke particle size was 200 mesh or less and 75% by weight. 72% by weight slurry 1 from the outlet
Exhausted the no. The viscosity of the product slurry was measured with a B-type viscometer and found to be -880 cp (at 25 DEG C.), which showed good fluidity and could be flowed through piping using a normal centrifugal pump or plunger pump.

表      3 実施例2 表4に示す脱れきアスファルトを200メツシュ以下6
0重量%に乾式粉砕した後、二軸ニーダーに20kQ/
h(ドライベース)で供給し、同時にアニオン系添加剤
を250 f/h (有効成分40%)で加え0、さら
に脱れきアスファルト濃度が71重自形となるように水
を供給し、二軸ニーダ−によシ毎分50回転でこれらの
原料を混練し71重量%スラリーを28kg/hで製造
した。製品スラリーの粘度をB型粘度計で測定した結果
、600cp(25℃)であり、流動性の良いスラリー
が得られた。
Table 3 Example 2 Degraded asphalt shown in Table 4 was prepared with a density of 200 mesh or less 6
After dry grinding to 0% by weight, 20kQ/
At the same time, anionic additives were added at 250 f/h (40% active ingredient) and water was supplied so that the deasphalt asphalt concentration became 71 euhedral. These raw materials were kneaded in a kneader at 50 revolutions per minute to produce a 71% by weight slurry at 28 kg/h. The viscosity of the product slurry was measured using a B-type viscometer and was found to be 600 cp (25° C.), indicating that a slurry with good fluidity was obtained.

以上説明したように、本発明の方法によれば、ある特定
の性状範囲に入る炭素含有組成物を選択して使用するこ
とにより、輸送、直接燃焼に適した高濃度スラリーを容
易に製造することができるという優れた効果を奏する。
As explained above, according to the method of the present invention, by selecting and using a carbon-containing composition that falls within a certain property range, it is possible to easily produce a highly concentrated slurry suitable for transportation and direct combustion. It has the excellent effect of being able to

【図面の簡単な説明】[Brief explanation of drawings]

図面は表2に示す各種炭素含有組成物をスラリー化した
場合におけるスラリー濃度と粘度との関係を示すグラフ
である。
The drawing is a graph showing the relationship between slurry concentration and viscosity when various carbon-containing compositions shown in Table 2 are slurried.

Claims (1)

【特許請求の範囲】[Claims] 1 炭素台゛有組成物に水、必要に応じて添加剤を加え
てスラリーを製造するに4〜、無水分、無鉱物基準での
炭素含有率が82〜98重量%−無水分、無鉱物基準で
の酸素原子数/炭素原子数の比が0.001〜0.10
、吸着水分が0.01〜6重量%、比表面積が0.01
〜777t′/ f/の性状の炭素含有組成物を用、い
−この炭素含有組成物の粒度を200メツシユ以下が4
0〜90重量%になるように調整し、水、必要に応じて
添加剤を添加して炭素含有組成物濃度70重量%以上の
スラリーを製造することを特徴とする炭素含有組成物の
水スラリーの製造方法。
1 To produce a slurry by adding water and optional additives to a composition containing a carbon base, the carbon content is 82 to 98% by weight on a moisture-free, mineral-free basis - moisture-free and mineral-free. The ratio of the number of oxygen atoms/number of carbon atoms in the standard is 0.001 to 0.10
, adsorbed moisture is 0.01-6% by weight, specific surface area is 0.01
A carbon-containing composition having a property of ~777 t'/f/ is used, and the particle size of this carbon-containing composition is 4.
An aqueous slurry of a carbon-containing composition, which is prepared by adjusting the carbon-containing composition concentration to 0 to 90% by weight, and adding water and, if necessary, additives to produce a slurry having a carbon-containing composition concentration of 70% by weight or more. manufacturing method.
JP5727983A 1983-03-31 1983-03-31 Preparation of aqueous slurry of carbon-containing composition Pending JPS59179697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5727983A JPS59179697A (en) 1983-03-31 1983-03-31 Preparation of aqueous slurry of carbon-containing composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5727983A JPS59179697A (en) 1983-03-31 1983-03-31 Preparation of aqueous slurry of carbon-containing composition

Publications (1)

Publication Number Publication Date
JPS59179697A true JPS59179697A (en) 1984-10-12

Family

ID=13051093

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5727983A Pending JPS59179697A (en) 1983-03-31 1983-03-31 Preparation of aqueous slurry of carbon-containing composition

Country Status (1)

Country Link
JP (1) JPS59179697A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6344928A (en) * 1987-07-22 1988-02-25 Babcock Hitachi Kk Slurry preparing apparatus

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5719024A (en) * 1980-07-04 1982-02-01 Kao Corp Dispersant for aqueous slurry of coal powder
JPS57174394A (en) * 1981-04-22 1982-10-27 Hitachi Ltd Coal slurry composition

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5719024A (en) * 1980-07-04 1982-02-01 Kao Corp Dispersant for aqueous slurry of coal powder
JPS57174394A (en) * 1981-04-22 1982-10-27 Hitachi Ltd Coal slurry composition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6344928A (en) * 1987-07-22 1988-02-25 Babcock Hitachi Kk Slurry preparing apparatus

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