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JPH0354719B2 - - Google Patents
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JPH0354719B2 - - Google Patents

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Publication number
JPH0354719B2
JPH0354719B2 JP2288383A JP2288383A JPH0354719B2 JP H0354719 B2 JPH0354719 B2 JP H0354719B2 JP 2288383 A JP2288383 A JP 2288383A JP 2288383 A JP2288383 A JP 2288383A JP H0354719 B2 JPH0354719 B2 JP H0354719B2
Authority
JP
Japan
Prior art keywords
slurry
fuel
concentration
coal
slurry fuel
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.)
Expired
Application number
JP2288383A
Other languages
Japanese (ja)
Other versions
JPS59149990A (en
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 filed Critical
Priority to JP2288383A priority Critical patent/JPS59149990A/en
Publication of JPS59149990A publication Critical patent/JPS59149990A/en
Publication of JPH0354719B2 publication Critical patent/JPH0354719B2/ja
Granted legal-status Critical Current

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  • Liquid Carbonaceous Fuels (AREA)

Description

【発明の詳細な説明】 この発明は石炭等の固形の燃料を粉砕したもの
と水等の液体を混合することにより形成したスラ
リー燃料の取り扱い方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for handling slurry fuel formed by mixing pulverized solid fuel such as coal with a liquid such as water.

石炭等の固形燃料を微粉砕しかつこの微粉砕し
た固形燃料と水等の液体を混合して製造したスラ
リー燃料(以下単に「スラリー」と称する)は固
体燃料の管路輸送を可能とし、かつ燃焼の制御も
容易であるため最近大いに注目されている。しか
し次の如き問題点も指摘されており、その改善が
要望されている。以下問題点を、固形分を石炭、
液体を水としたスラリー燃料を例に説明すると、 (1) スラリーの貯蔵から燃焼までの間、石炭と水
の混合比率を一定にしていたため、スラリー貯
蔵時もしくは燃焼時の少くとも一方において問
題を生じていた。すなわち、 (a) 石炭の濃度が高い場合には粘性が高くな
り、貯蔵時の石炭の沈降は防止し得るが、配
管内での詰り、特に熱を受ける部分において
詰りを生じることになる。
Slurry fuel (hereinafter simply referred to as "slurry"), which is produced by pulverizing solid fuel such as coal and mixing this pulverized solid fuel with liquid such as water, allows solid fuel to be transported through pipes, and Recently, it has been attracting a lot of attention because it is easy to control combustion. However, the following problems have been pointed out, and improvements are desired. The following problems are explained, solid content is coal,
Taking slurry fuel with water as the liquid as an example, (1) Since the mixing ratio of coal and water was kept constant from the time the slurry was stored to the time it was combusted, there was no problem in at least one of the slurry storage or combustion stages. It was happening. That is, (a) When the concentration of coal is high, the viscosity becomes high, and although it is possible to prevent the coal from settling during storage, it causes clogging in the pipes, especially in the parts that receive heat.

(b) 反対に石炭の濃度が低い場合には粘性も低
くなり配管内での詰りを防止し得る反面貯蔵
時に石炭が沈降固化していわゆるハードパツ
クを生じてしまう。このため定期的に貯蔵タ
ンク底部からハードバツクを除去する必要が
ある。
(b) On the other hand, if the concentration of coal is low, the viscosity will be low and clogging in the pipes can be prevented, but on the other hand, the coal will settle and solidify during storage, resulting in so-called hard packs. For this reason, it is necessary to periodically remove the hard bag from the bottom of the storage tank.

(2) (1)の理由によりスラリーの濃度は配管内にお
いて固化を生じないように低濃度に保持し、か
つこの低濃度スラリーの貯蔵時に石炭が沈降す
るのを防止するためスラリー中に安定剤を混入
させる方法も提案されているが、この方法の場
合には次の点が問題となる。
(2) Due to the reason mentioned in (1), the concentration of the slurry is kept low to prevent solidification in the pipes, and a stabilizer is added to the slurry to prevent coal from settling during storage of this low concentration slurry. A method has also been proposed in which the compound is mixed in, but this method has the following problems.

(a) 安定剤が高価であるためスラリー自体の価
格が上昇する。
(a) The price of the slurry itself increases because the stabilizer is expensive.

(b) 安定剤としては酢酸、塩化カルシウム
(CaCl2)等を使用するが、安定剤中の成分
により燃焼装置を損傷させる虞れがあり、特
に塩化カルシウムを使用する場合にはCl分に
よる激しい腐食が生じる。
(b) Acetic acid, calcium chloride (CaCl 2 ), etc. are used as stabilizers, but the components in the stabilizers may damage the combustion equipment, and especially when calcium chloride is used, severe Corrosion occurs.

(c) また安定剤の混入はスラリーの霧化特性を
悪化させ、燃焼効率を低下させることにもな
る。
(c) Incorporation of stabilizers also worsens the atomization characteristics of the slurry and reduces combustion efficiency.

この発明の目的は、上述した従来技術の問題点
を除去し得るスラリー燃料取り扱い方法を提供す
ることにある。
An object of the present invention is to provide a slurry fuel handling method that can eliminate the problems of the prior art described above.

要するにこの発明は、石炭−水スラリー燃料を
貯蔵しかつ貯蔵した燃料を燃焼装置に給送する方
法において、スラリー燃料貯蔵時には粘度を
2000CP以上に保持し、スラリー燃料貯蔵部から
燃焼部にスラリー燃料を給送するに際し、このス
ラリー燃料に対して水を加え2000CP以下にする
ことを特徴とするスラリー燃料取り扱い方法であ
る。
In short, this invention provides a method for storing coal-water slurry fuel and delivering the stored fuel to a combustion device, in which the viscosity is reduced during storage of the slurry fuel.
This slurry fuel handling method is characterized by maintaining the slurry fuel at 2000 CP or more and adding water to the slurry fuel to reduce the slurry fuel to 2000 CP or less when feeding the slurry fuel from the slurry fuel storage section to the combustion section.

以下この発明の実施例を図面を参考に説明す
る。
Embodiments of the present invention will be described below with reference to the drawings.

第1図は微粉炭と水との混合燃料における石炭
濃度とスラリー燃料の粘度との関係を発明者等が
測定した結果を示す。図示の如く、石炭濃度の上
昇と共に粘度は急激に上昇し、例えば濃度が70%
の場合粘度は最高約1000CP(センチポアズ)であ
るが、濃度が74%となると粘度は最高約2000CP
と2倍に上昇することが確認された。発明者等は
粘度の異なるスラリーを用いてスラリーの輸送と
貯蔵についての試験を行つた。この結果、スラリ
ーの輸送に当つては2000CP以下の場合には殆ん
ど詰りが生じないことを、また2000CP以上の場
合には貯槽内でのハードパツクの発生は殆んど生
じないことを確認した。つまり、これを石炭濃度
をもつて示せば、濃度約74%以下であれば輸送に
適し、それ以上の濃度の場合には貯蔵に適するこ
とを意味する。
FIG. 1 shows the results of the inventors' measurements of the relationship between the coal concentration and the viscosity of slurry fuel in a mixed fuel of pulverized coal and water. As shown in the figure, the viscosity increases rapidly as the coal concentration increases, for example, when the concentration is 70%
In the case of
It was confirmed that the number increased by two times. The inventors conducted tests on slurry transportation and storage using slurries of different viscosities. As a result, it was confirmed that when transporting slurry, there is almost no clogging when the slurry is less than 2000 CP, and when the slurry is more than 2000 CP, there is almost no hard packing in the storage tank. . In other words, if we express this in terms of coal concentration, it means that if the concentration is below about 74%, it is suitable for transportation, and if the concentration is higher than that, it is suitable for storage.

第2図は上述の試験に基づいて構成したスラリ
ー燃料取り扱い方法の第1の実施例を示す。図に
おいて、石炭1及び水2はスラリー製造装置3に
おいて、高濃度のスラリー(例えば石炭濃度74%
以上のスラリー)4となり、貯蔵手段5内に貯蔵
される。この場合前述の如く高濃度スラリー4の
粘度は約2000CP以上に保持されているため、石
炭の沈降、固化によるハードパツクは生じない。
貯蔵手段5を出た高濃度スラリー4は輸送手段6
を経て貯蔵手段7に至る。ここにおいて、水8が
供給されてスラリーの濃度を低下させ、その粘度
を2000CP以下に低下させた低粘度スラリー9と
する。低粘度スラリー9はバーナ10において霧
化され、燃焼装置11内で燃焼する。バーナ10
に対しては低粘度のスラリーが供給されるので、
バーナにおけるスラリーの霧化特性は向上して燃
焼効率が高まると共に、流量の制御も良好となる
ので燃焼の制御性も向上する。
FIG. 2 shows a first embodiment of a slurry fuel handling method constructed based on the tests described above. In the figure, coal 1 and water 2 are produced in a slurry manufacturing device 3 to form a highly concentrated slurry (for example, a coal concentration of 74%).
The above slurry becomes 4) and is stored in the storage means 5. In this case, as described above, the viscosity of the highly concentrated slurry 4 is maintained at approximately 2000 CP or more, so that hard packs due to coal settling and solidification do not occur.
The highly concentrated slurry 4 leaving the storage means 5 is transferred to the transportation means 6
and then reaches the storage means 7. Here, water 8 is supplied to reduce the concentration of the slurry, resulting in a low viscosity slurry 9 whose viscosity is reduced to 2000 CP or less. The low viscosity slurry 9 is atomized in a burner 10 and combusted in a combustion device 11 . burner 10
Since a low viscosity slurry is supplied to
The atomization characteristics of the slurry in the burner are improved and the combustion efficiency is increased, and the controllability of combustion is also improved because the flow rate is better controlled.

第3図は第2の実施例を示す。この実施例の場
合には一時貯蔵手段7の下流において高濃度スラ
リー4と水8とを混合させるようにしたものであ
る。この実施例の場合には一時貯蔵手段7に対し
て混合撹拌装置を設ける必要がない。但しバーナ
10近傍においてはスラリーが固化する虞れがあ
るので、できる限り一時貯蔵手段7の近傍におい
て水8と混合させ、早めに低濃度スラリー9とす
ることが望ましい。
FIG. 3 shows a second embodiment. In this embodiment, the highly concentrated slurry 4 and water 8 are mixed downstream of the temporary storage means 7. In this embodiment, there is no need to provide a mixing and stirring device for the temporary storage means 7. However, since there is a risk of the slurry solidifying near the burner 10, it is desirable to mix it with water 8 as close to the temporary storage means 7 as possible to form a low-concentration slurry 9 as soon as possible.

第4図は第3の実施例を示す。この実施例の場
合には一時貯蔵手段とバーナ10との間に高濃度
スラリー4と水8との混合を専門に行なうサービ
スタンク13を配置してスラリーの低濃度化を実
施し、かつ一時貯蔵手段7は純然たる流量調整手
段として使用するようにしたものである。
FIG. 4 shows a third embodiment. In the case of this embodiment, a service tank 13 that specializes in mixing high concentration slurry 4 and water 8 is arranged between the temporary storage means and the burner 10 to reduce the concentration of the slurry and temporarily store it. The means 7 is intended to be used purely as a flow rate adjusting means.

なお、以上の実施例において、高濃度スラリー
に対して、燃焼時に霧化特性が悪化したり燃焼装
置に腐食が生じない範囲において安定剤を添加し
てもよい。
In the above embodiments, a stabilizer may be added to the high concentration slurry as long as it does not deteriorate the atomization characteristics during combustion or cause corrosion to the combustion device.

この発明を実施することにより安定剤を全く使
用しないか、もしくはごく僅かの使用によつて、
スラリー貯蔵時に石炭等の固形物の沈降、固化が
生じない。
By practicing this invention, no or only a small amount of stabilizers are used.
Solids such as coal do not settle or solidify during slurry storage.

またスラリー給送及び燃焼時にはスラリーの粘
度が低いので配管中の詰りが生ぜず、かつスラリ
ーの霧化特性も向上する等種々の効果を発揮す
る。
Furthermore, since the viscosity of the slurry is low during slurry feeding and combustion, clogging in the piping does not occur, and the atomization characteristics of the slurry are improved, among other effects.

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

第1図は石炭濃度とスラリー燃料の粘度との関
係を示す線図、第2図はこの発明の第1の実施例
を示すスラリー燃料取り扱いの系統図、第3図は
第2の実施例を示す系統図、第4図は第3の実施
例を示す系統図である。 4……高濃度スラリー、8……水、9……低濃
度スラリー。
Fig. 1 is a diagram showing the relationship between coal concentration and viscosity of slurry fuel, Fig. 2 is a system diagram of slurry fuel handling showing the first embodiment of this invention, and Fig. 3 is a diagram showing the second embodiment. FIG. 4 is a system diagram showing the third embodiment. 4...High concentration slurry, 8...Water, 9...Low concentration slurry.

Claims (1)

【特許請求の範囲】 1 石炭−水スラリー燃料を貯蔵しかつ貯蔵した
燃料を燃焼装置に給送する方法において、スラリ
ー燃料貯蔵時には粘度を2000CP以上に保持し、
スラリー燃料貯蔵部から燃焼部にスラリー燃料を
給送するに際し、このスラリー燃料に対して水を
加え2000CP以下にすることを特徴とするスラリ
ー燃料取り扱い方法。 2 貯蔵時のスラリー燃料の固形分濃度を約74%
以上、給送時の固形分濃度を約47%以下とするこ
とを特徴とする特許請求の範囲第1項記載のスラ
リー燃料取り扱い方法。
[Claims] 1. A method for storing coal-water slurry fuel and feeding the stored fuel to a combustion device, wherein the viscosity is maintained at 2000 CP or more during storage of the slurry fuel,
A method for handling slurry fuel, characterized in that when the slurry fuel is fed from the slurry fuel storage section to the combustion section, water is added to the slurry fuel to reduce the concentration to 2000 CP or less. 2. Reduce the solid content concentration of slurry fuel to approximately 74% during storage.
The method for handling slurry fuel according to claim 1, characterized in that the solid content concentration during feeding is approximately 47% or less.
JP2288383A 1983-02-16 1983-02-16 Handling method of slurry fuel Granted JPS59149990A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2288383A JPS59149990A (en) 1983-02-16 1983-02-16 Handling method of slurry fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2288383A JPS59149990A (en) 1983-02-16 1983-02-16 Handling method of slurry fuel

Publications (2)

Publication Number Publication Date
JPS59149990A JPS59149990A (en) 1984-08-28
JPH0354719B2 true JPH0354719B2 (en) 1991-08-21

Family

ID=12095074

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2288383A Granted JPS59149990A (en) 1983-02-16 1983-02-16 Handling method of slurry fuel

Country Status (1)

Country Link
JP (1) JPS59149990A (en)

Also Published As

Publication number Publication date
JPS59149990A (en) 1984-08-28

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