JPH0576518B2 - - Google Patents
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- Publication number
- JPH0576518B2 JPH0576518B2 JP60067236A JP6723685A JPH0576518B2 JP H0576518 B2 JPH0576518 B2 JP H0576518B2 JP 60067236 A JP60067236 A JP 60067236A JP 6723685 A JP6723685 A JP 6723685A JP H0576518 B2 JPH0576518 B2 JP H0576518B2
- Authority
- JP
- Japan
- Prior art keywords
- coal
- raw material
- pulverizer
- material coal
- pulverized
- 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 - Lifetime
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- Liquid Carbonaceous Fuels (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、石炭水スラリー製造法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for producing coal water slurry.
一般に石炭には、粉砕するのに砕きやすいもの
や砕き難いもの、あるいは、揮発成分の少ないも
のや多いものがあり、これに対して従来、一定の
品質の石炭水スラリーを安定して得るために、そ
れらの石炭の種類に応じて各種石炭ごとに湿式微
粉砕の処理方法や時間等を調整して処理した後
に、異種の石炭どうしを混合する方法や、異種の
石炭を混合した後同時に湿式微粉砕する方法が行
われていた。
In general, there are types of coal that are easy to crush and those that are difficult to crush, and those that have low or high volatile components. Depending on the type of coal, the wet pulverization method and time are adjusted for each type of coal, and then different types of coal are mixed together, or different types of coal are mixed and then wet pulverized at the same time. A method of crushing was used.
〔発明が解決しようとする問題点〕
しかし、前者の場合、異種の石炭ごとに調整さ
れた粉砕機を各別に設け、更に異種の粉砕済の石
炭を混合する混合機を設けなければならないため
に、設備費が高くつく欠点があり、後者の場合、
たとえば砕きやすい種類の石炭や揮発分が多いた
めに粒子が多少大でも良い石炭等が不必要に粉砕
処理されすぎて運転経費が高くつく虞があつた。[Problem to be solved by the invention] However, in the former case, it is necessary to install separate crushers for different types of coal, and also to install a mixer to mix different types of crushed coal. , the disadvantage is that the equipment cost is high, and in the latter case,
For example, types of coal that are easy to crush or coal that can have large particles due to its high volatile content may be unnecessarily pulverized, resulting in high operating costs.
本発明の目的は、原料石炭の粉砕特性及び燃焼
性に適した粉砕ができるようにする点にある。 An object of the present invention is to enable pulverization suitable for the pulverization characteristics and combustibility of raw coal.
本発明の石炭水スラリー製造法の特徴構成は、
第1原料石炭を第1粉砕機で微粉砕し、前記第1
原料石炭とは異種で前記第1原料石炭よりも必要
粉砕時間の短い第2原料石炭と、前記第1粉砕機
で処理した第1原料石炭を、第2粉砕機で混合す
ると共に湿式微粉砕することにあり、その作用効
果は、次の通りである。
The characteristic structure of the coal water slurry manufacturing method of the present invention is as follows:
The first raw material coal is finely pulverized by a first pulverizer, and the
A second raw material coal that is different from the raw material coal and requires a shorter grinding time than the first raw material coal, and the first raw material coal processed in the first pulverizer are mixed and wet-pulverized in a second pulverizer. In particular, its functions and effects are as follows.
つまり、第1原料石炭として砕き難い種類の石
炭や、燃焼に有利な揮発成分が少ないために細か
く粉砕しなければならない石炭を使用し、且つ、
第2原料石炭として砕き易い種類の石炭や、燃焼
に有利な揮発成分が多いために粒子が多少大きく
ても良い石炭を使用すれば、第2原料石炭が第2
粉砕機だけで湿式微粉砕されるのに比して、第1
原料石炭は第1粉砕機で微粉砕した後、更に第2
粉砕機で細かく湿式微粉砕されるために、第1、
第2粉砕機を適当に調整することによつて、各種
原料石炭の粉砕特性及び燃焼性に最適の粉砕処理
が不必要に動力をかけずとも行えると共に、第2
粉砕機が第1原料石炭と第2原料石炭とを混合す
る混合機に兼用されるために、第1、第2原料石
炭を各別に設けた粉砕機によつて粉砕処理した後
に、混合機によつて混合するのに比して動力及び
設備を少なくできる。
In other words, a type of coal that is difficult to crush or a coal that must be finely crushed because it has few volatile components that are advantageous for combustion is used as the first raw material coal, and
If you use a type of coal that is easy to crush as the second raw material coal, or a coal whose particles may be somewhat large because it has a lot of volatile components that are advantageous for combustion, the second raw material coal can be used as the second raw material coal.
Compared to wet pulverization using only a pulverizer,
After the raw coal is finely pulverized in the first pulverizer, it is further pulverized in the second pulverizer.
In order to be finely wet-pulverized by a crusher, first,
By appropriately adjusting the second pulverizer, it is possible to carry out the pulverization process that is optimal for the pulverizing characteristics and combustibility of various types of raw coal without applying unnecessary power.
Since the pulverizer is also used as a mixer for mixing the first raw material coal and the second raw material coal, the first and second raw material coals are pulverized by separate pulverizers and then put into the mixer. Therefore, compared to mixing, power and equipment can be reduced.
従つて、設備費及び運転経費を安価にでき、安
定した品質の石炭水スラリーを長期にわたつて供
給できるに至つた。
Therefore, equipment costs and operating costs can be reduced, and coal water slurry of stable quality can be supplied over a long period of time.
次に、本発明の実施例を図面に基づいて説明す
る。
Next, embodiments of the present invention will be described based on the drawings.
粉砕し難い石炭や揮発分が少ないために細かく
粉砕しなければ燃焼しにくい石炭から成る第1原
料石炭Aを、湿式の第1粉砕機1に投入しながら
水及び添加剤を加えて粉砕し、第1粉砕機1によ
つて粉砕処理された第1原料石炭Aは、更に湿式
の第2粉砕機2に投入する。そして、同時に、粉
砕し易い石炭や揮発分が多く含まれるために多少
粒子が大きくとも効果的に燃焼する石炭から成る
第2原料石炭Bを、第1原料石炭Aに対する混合
比率を一定にする状態で第2粉砕機2に投入す
る。 First raw material coal A consisting of coal that is difficult to crush or coal that is difficult to burn unless it is finely crushed due to its low volatile content is fed into a first wet crusher 1 and crushed by adding water and additives, The first raw material coal A that has been pulverized by the first pulverizer 1 is further fed into a second wet pulverizer 2 . At the same time, the mixing ratio of the second raw material coal B, which is made of coal that is easy to crush or coal that contains a large amount of volatile matter and therefore burns effectively even if the particles are somewhat large, to the first raw material coal A is kept constant. Then, it is charged into the second crusher 2.
前記第2粉砕機2では、第1原料石炭Aと第2
原料石炭Bとが一定比率で混ざり同時に水及び添
加剤を加えながら湿式粉砕処理され、異種の石炭
原料どうしが混ざり合つて品質の安定した高濃度
石炭水スラリーが製造される。 In the second crusher 2, the first raw material coal A and the second
Raw material coal B is mixed at a constant ratio and wet-pulverized while simultaneously adding water and additives, and different types of coal raw materials are mixed to produce a highly concentrated coal-water slurry with stable quality.
尚、第2粉砕機2による処理条件は、第2原料
石炭Bが最適な状態に粉砕される様に設定され、
第1粉砕機1による処理条件は、第1原料石炭A
が第1粉砕機1と第2粉砕機2との双方による処
理によつて、最適な条件に粉砕される様に設定し
てある。 In addition, the processing conditions by the second crusher 2 are set so that the second raw material coal B is crushed in an optimal state,
The processing conditions by the first crusher 1 are the first raw material coal A
is set so that it is pulverized under optimal conditions through processing by both the first pulverizer 1 and the second pulverizer 2.
前記第1粉砕機1は湿式以外に乾式のものであ
つても良く、この場合は水及び添加剤を第1粉砕
機1に加える必要はない。
The first pulverizer 1 may be of a dry type instead of a wet type, and in this case, it is not necessary to add water and additives to the first pulverizer 1.
前記第1粉砕機1で湿式粉砕処理する場合、そ
の第1粉砕機1で加える水及び添加剤量の調節状
況によつては、第2粉砕機2で水及び添加剤を加
えなくとも良い。 In the case of wet pulverization using the first pulverizer 1, depending on how the amounts of water and additives added in the first pulverizer 1 are adjusted, it is not necessary to add water and additives in the second pulverizer 2.
図面は本発明に係る石炭水スラリー製造法の実
施例を示すブロツク図である。
1……第1粉砕機、2……第2粉砕機、A……
第1原料石炭、B……第2原料石炭。
The drawing is a block diagram showing an embodiment of the method for producing coal-water slurry according to the present invention. 1...First crusher, 2...Second crusher, A...
First raw material coal, B... second raw material coal.
Claims (1)
前記第1原料石炭Aとは異種で前記第1原料石炭
Aよりも必要粉砕時間の短い第2原料石炭Bと、
前記第1粉砕機1で処理した第1原料石炭Aを、
第2粉砕機2で混合すると共に湿式微粉砕する石
炭水スラリー製造法。1 Finely pulverize the first raw material coal A with the first pulverizer 1,
a second raw material coal B that is different from the first raw material coal A and requires a shorter grinding time than the first raw material coal A;
The first raw material coal A treated with the first crusher 1,
A method for producing coal water slurry in which mixing is performed in a second pulverizer 2 and wet pulverization is performed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6723685A JPS61225292A (en) | 1985-03-29 | 1985-03-29 | Production of coal-water slurry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6723685A JPS61225292A (en) | 1985-03-29 | 1985-03-29 | Production of coal-water slurry |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61225292A JPS61225292A (en) | 1986-10-07 |
| JPH0576518B2 true JPH0576518B2 (en) | 1993-10-22 |
Family
ID=13339077
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6723685A Granted JPS61225292A (en) | 1985-03-29 | 1985-03-29 | Production of coal-water slurry |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61225292A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1477824A2 (en) | 2003-05-08 | 2004-11-17 | Kabushiki Kaisha Toshiba | Parallel MR imaging |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6013890A (en) * | 1983-07-05 | 1985-01-24 | Babcock Hitachi Kk | Production of coal-water slurry having high concentration and lowered viscosity |
-
1985
- 1985-03-29 JP JP6723685A patent/JPS61225292A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1477824A2 (en) | 2003-05-08 | 2004-11-17 | Kabushiki Kaisha Toshiba | Parallel MR imaging |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61225292A (en) | 1986-10-07 |
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