JPH0768529B2 - Method for producing high-concentration coal / water slurry - Google Patents
Method for producing high-concentration coal / water slurryInfo
- Publication number
- JPH0768529B2 JPH0768529B2 JP18922787A JP18922787A JPH0768529B2 JP H0768529 B2 JPH0768529 B2 JP H0768529B2 JP 18922787 A JP18922787 A JP 18922787A JP 18922787 A JP18922787 A JP 18922787A JP H0768529 B2 JPH0768529 B2 JP H0768529B2
- Authority
- JP
- Japan
- Prior art keywords
- wet
- water slurry
- coal
- concentration coal
- coarse
- 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
Links
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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〕 本発明は原料石炭を湿式粗粉砕機で粗粉砕処理して、高
濃度石炭・水スラリーを造り、この湿式粗粉砕機で造っ
た高濃度石炭・水スラリーを湿式ミルで微粉砕処理する
高濃度石炭・水スラリーの製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is to pulverize raw coal with a wet coarse pulverizer to produce a high-concentration coal / water slurry. The present invention relates to a method for producing a high-concentration coal / water slurry by finely pulverizing a coal / water slurry with a wet mill.
従来、第2図に示すように、湿式粗粉砕機(4)に原料
石炭、水、添加剤からなる原料だけを供給し、この湿式
粗粉砕機(4)での粗粉砕処理により造った高濃度石炭
・水スラリーを、管路(8)により、かつ、必要に応じ
て一旦タンク(9)に貯留した上で、湿式ミル(5)に
供給して微粉砕処理し、そして、この湿式ミル(5)で
微粉砕処理した高濃度石炭・水スラリーを、石炭粗粒子
を分離するためのスクリーン(6)に送り、スクリーン
(6)で石炭粗粒子を分離した高濃度石炭・水スラリー
を製品として貯留タンク(7)に送っていた(例えば、
特開昭61−283363号公報参照)。Conventionally, as shown in FIG. 2, only a raw material consisting of raw coal, water, and an additive is supplied to a wet coarse crusher (4), and a high crushing process is performed by the coarse crushing process in the wet coarse crusher (4). The concentrated coal / water slurry is temporarily stored in the tank (9) through the pipe line (8) and, if necessary, supplied to the wet mill (5) for fine pulverization treatment, and this wet mill The high-concentration coal / water slurry finely pulverized in (5) is sent to the screen (6) for separating coarse coal particles, and the high-concentration coal / water slurry obtained by separating coarse coal particles in the screen (6) is manufactured. Was sent to the storage tank (7) as
See JP-A-61-283363).
しかし、湿式粗粉砕機(4)での粗粉砕処理により造っ
た高濃度石炭スラリーは、石炭の平均的粒度が粗いため
石炭が沈降し易く、また、石炭の粒度分布の巾が狭いた
め流動性が悪く、これらのことから、湿式粗粉砕機
(4)と湿式ミル(5)との間で管路(8)やタンク
(9)の閉塞を生じ易い、また、搬送動力が嵩むといっ
た問題があった。However, the high-concentration coal slurry produced by the coarse crushing process in the wet coarse crusher (4) has a coarse average particle size of the coal, so that the coal tends to settle, and the width of the particle size distribution of the coal is narrow, so that the fluidity is low. Therefore, there is a problem that the pipeline (8) and the tank (9) are likely to be blocked between the wet coarse pulverizer (4) and the wet mill (5) and the transport power is increased. there were.
本発明の目的は、極めて簡単かつ経済的な手段をもっ
て、湿式粗粉砕機から湿式ミルに送る高濃度石炭・水ス
ラリーを沈降し難く流動性の高いものに改質する点にあ
る。An object of the present invention is to reform highly concentrated coal / water slurry sent from a wet coarse pulverizer to a wet mill into a highly fluid one which is difficult to settle and has a high fluidity by an extremely simple and economical means.
本発明による高濃度石炭・水スラリーの製造方法の特徴
構成は、 原料石炭を湿式粗粉砕機で粗粉砕処理して、高濃度石炭
・水スラリーを造り、この湿式粗粉砕機で造った高濃度
石炭・水スラリーを湿式ミルで微粉砕処理する基本構成
において、 前記湿式ミルで微粉砕処理した後の高濃度石炭・水スラ
リーを、前記湿式粗粉砕機への原料供給量の5重量%以
上の割合で、 前記湿式粗粉砕機への供給原料に混入、又は、前記湿式
粗粉砕機に投入、又は、前記湿式粗粉砕機で造った高濃
度石炭・水スラリーに混入することにある。The characteristic configuration of the method for producing a high-concentration coal / water slurry according to the present invention is that raw coal is coarsely pulverized by a wet coarse pulverizer to produce a high-concentration coal / water slurry, and the high-concentration coal produced by this wet coarse pulverizer is used. In the basic configuration of finely pulverizing the coal / water slurry by the wet mill, the high-concentration coal / water slurry finely pulverized by the wet mill is used in an amount of 5% by weight or more of the raw material supply amount to the wet coarse pulverizer. It is mixed in the feed material to the wet coarse pulverizer in a ratio, or is charged into the wet coarse pulverizer or mixed in the high-concentration coal / water slurry produced by the wet coarse pulverizer.
つまり、各種実験の結果、湿式ミルで微粉砕処理した後
の高濃度石炭・水スラリーを湿式粗粉砕機への原料供給
量の5重量%以上の割合で、また、この好ましくは、50
重量%以下の割合で、湿式粗粉砕機への供給原料に混
入、又は、前記湿式粗粉砕機に投入、又は、前記湿式粗
粉砕機で造った高濃度石炭・水スラリーに混入すると、
湿式粗粉砕機から湿式ミルに送る高濃度石炭・水スラリ
ーの沈降性を効果的に低減でき、かつ、流動性を効果的
に高め得ることを確認できた。That is, as a result of various experiments, the high-concentration coal / water slurry after being finely pulverized by the wet mill was used at a ratio of 5% by weight or more of the amount of the raw material supplied to the wet coarse pulverizer, and preferably 50%.
In a proportion of less than or equal to wt%, mixed in the feed material to the wet coarse crusher, or charged into the wet coarse crusher, or mixed in the high-concentration coal-water slurry produced by the wet coarse crusher,
It was confirmed that the settling property of the high-concentration coal / water slurry sent from the wet coarse crusher to the wet mill can be effectively reduced and the fluidity can be effectively improved.
本発明によれば、湿式粗粉砕機から湿式ミルに送る高濃
度石炭・水スラリーの沈降性を効果的に低減でき、か
つ、流動性を効果的に高め得ることから、湿式粗粉砕機
と湿式ミルとの間における管路やタンクでの閉塞といっ
た搬送面や貯留面でのトラブルを回避できて、高濃度石
炭・水スラリーの生産性を向上でき、また、必要搬送動
力を低減できて生産コストの低減も可能にし得るに至っ
た。According to the present invention, it is possible to effectively reduce the sedimentation property of the high-concentration coal / water slurry sent from the wet coarse pulverizer to the wet mill and to effectively enhance the fluidity, and therefore, the wet coarse pulverizer and the wet coarse pulverizer are used. It is possible to avoid troubles on the transport surface and storage surface such as blockages in the pipelines and tanks with the mill, improve the productivity of high-concentration coal / water slurry, and reduce the required transport power to reduce production costs. It has become possible to reduce the above.
しかも、湿式湿式ミルで微粉砕処理した後の高濃度石炭
・水スラリーの一部を上流側に戻すだけの簡単な改良方
法であるから、設備コスト面での負担も少なく有利であ
る。Moreover, since this is a simple improvement method in which a part of the high-concentration coal / water slurry after finely pulverized by a wet-type wet mill is returned to the upstream side, the burden on the facility cost is small and advantageous.
次に第1図に基づき実施例を説明する。 Next, an embodiment will be described with reference to FIG.
ホッパー(1)から供給する原料石炭、第1タンク
(2)から供給する水、及び、第2タンク(3)から供
給する添加剤を適当な配合比で湿式粗粉砕機(4)に供
給し、そして、これら原料を湿式粗粉砕機(4)で粗粉
砕処理して高濃度石炭・水スラリーを造る。The raw material coal supplied from the hopper (1), the water supplied from the first tank (2), and the additive supplied from the second tank (3) were supplied to the wet coarse crusher (4) at an appropriate mixing ratio. Then, these raw materials are roughly pulverized by a wet coarse pulverizer (4) to produce a high-concentration coal / water slurry.
原料石炭は一般に粒径が50〜60mm以下のものを用い、石
炭と水との配合比は一般に石炭重量濃度で60〜75%程度
とする。また、添加剤としては、例えばナフタレンスル
ホン酸塩ホルマリン縮合物、ポリスチレンスルホン酸
塩、リグニンスルホン酸塩、ポリカルボン酸塩を0.3〜
1.0%(対石炭)で使用したり、ポリスチレンオキサイ
ドを0.5〜1.5%(対石炭)で使用する。Raw coal generally has a particle size of 50 to 60 mm or less, and the mixing ratio of coal and water is generally about 60 to 75% in terms of coal weight concentration. Further, as the additive, for example, naphthalene sulfonate formalin condensate, polystyrene sulfonate, lignin sulfonate, polycarboxylate 0.3 ~
Use at 1.0% (vs coal) or polystyrene oxide at 0.5-1.5% (vs coal).
湿式粗粉砕機(4)での粗粉砕処理により造った高濃度
石炭・水スラリーは湿式ミル(5)に供給して微粉砕処
理し、また、この湿式ミル(5)で微粉砕処理した高濃
度石炭・水スラリーの大部分はスクリーン(6)に送っ
て石炭粗粒子を分離し、そして、スクリーン(6)を通
った高品質の高濃度石炭・水スラリーは製品として貯留
タンク(7)に回収貯留し、一方、スクリーン(6)で
分離された石炭粗粒子は湿式ミル(5)に戻して再度微
粉砕処理する。The high-concentration coal / water slurry produced by the coarse pulverization process in the wet coarse pulverizer (4) is supplied to the wet mill (5) to be finely pulverized, and the high-concentration coal finely pulverized in the wet mill (5). Most of the concentrated coal / water slurry is sent to the screen (6) to separate the coarse particles of coal, and the high quality concentrated coal / water slurry that passed through the screen (6) is stored in the storage tank (7). On the other hand, the coarse coal particles separated and collected by the screen (6) are returned to the wet mill (5) and finely pulverized again.
湿式ミル(5)で微粉砕処理した高濃度石炭・水スラリ
ーのうち一部は、湿式粗粉砕機(4)への原料供給量の
5重量%以上の割合で、また、望ましくは製造効率の向
上面から50%以下の割合で、上流側に戻して湿式粗粉砕
機(4)に投入し、これにより、湿式粗粉砕機(4)か
ら湿式ミル(5)へ送る高濃度石炭・水スラリーの沈降
性を低減するとともに流動性を高めてスラリー搬送を円
滑にする。A part of the high-concentration coal / water slurry finely pulverized by the wet mill (5) accounts for 5% by weight or more of the amount of the raw material supplied to the wet coarse pulverizer (4), and preferably the production efficiency. From the aspect of improvement, at a rate of 50% or less, it is returned to the upstream side and charged into the wet coarse crusher (4), whereby the high-concentration coal / water slurry sent from the wet coarse crusher (4) to the wet mill (5). It reduces the sedimentation property and enhances the fluidity to facilitate the slurry transportation.
前述の実施例では、湿式ミル(5)で微粉砕処理した後
の高濃度石炭・水スラリーを、湿式粗粉砕機(4)への
原料供給量の5重量%以上の割合で、湿式粗粉砕機
(4)に投入する形態を採ったが、同様に搬送性の向上
を目的として、湿式ミル(5)で微粉砕処理した後の高
濃度石炭・水スラリーを、湿式粗粉砕機(4)への原料
供給量の5重量%以上の割合で、湿式粗粉砕機(4)へ
の供給原料に混入する形態、あるいは、湿式粗粉砕機
(4)で造った高濃度石炭・水スラリーに混入する形態
を採用してもよい。In the above-described embodiment, the high-concentration coal / water slurry that has been finely pulverized by the wet mill (5) is wet coarsely pulverized at a rate of 5% by weight or more of the amount of the raw material supplied to the wet coarse pulverizer (4). Although it was introduced into the machine (4), similarly, for the purpose of improving the transportability, the high-concentration coal / water slurry after finely pulverized by the wet mill (5) was wet coarse pulverizer (4). 5% by weight or more of the amount of raw material supplied to the wet coarse pulverizer (4), or a high concentration coal / water slurry produced by the wet coarse pulverizer (4) The form may be adopted.
湿式粗粉砕機(4)の具体構成は、例えばロッドミルな
ど適当に選定でき、また、湿式ミル(5)の具体構成
は、例えば一段又は複数段でタワーミルにより微粉砕す
るものなど適当に選定できる。The specific configuration of the wet coarse pulverizer (4) can be appropriately selected, for example, a rod mill, and the specific configuration of the wet mill (5) can be appropriately selected, for example, one in which one stage or a plurality of stages are used for fine pulverization by a tower mill.
【図面の簡単な説明】 第1図は本発明の実施例を示すフローシート、第2図は
従来例をフローシートである。 (4)……湿式粗粉砕機、(5)……湿式ミル。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a flow sheet showing an embodiment of the present invention, and FIG. 2 is a flow sheet showing a conventional example. (4) …… Wet coarse crusher, (5) …… Wet mill.
Claims (2)
理して、高濃度石炭・水スラリーを造り、この湿式粗粉
砕機(4)で造った高濃度石炭・水スラリーを湿式ミル
(5)で微粉砕処理する高濃度石炭・水スラリーの製造
方法であって、前記湿式ミル(5)で微粉砕処理した後
の高濃度石炭・水スラリーを、前記湿式粗粉砕機(4)
への原料供給量の5重量%以上の割合で、 前記湿式粗粉砕機(4)への供給原料に混入、又は、前
記湿式粗粉砕機(4)に投入、又は、前記湿式粗粉砕機
(4)で造った高濃度石炭・水スラリーに混入する高濃
度石炭・水スラリーの製造方法。1. A high-concentration coal / water slurry is produced by roughly pulverizing raw material coal with a wet coarse pulverizer (4), and the high-concentration coal / water slurry produced by this wet coarse pulverizer (4) is wet. A method for producing a high-concentration coal / water slurry finely pulverized by a mill (5), wherein the high-concentration coal / water slurry finely pulverized by the wet mill (5) is treated by the wet coarse crusher (4). )
5% by weight or more of the amount of raw material supplied to the wet coarse crusher (4), or mixed into the raw material supplied to the wet coarse crusher (4), or the wet coarse crusher ( A method for producing a high-concentration coal / water slurry mixed with the high-concentration coal / water slurry produced in 4).
高濃度石炭・水スラリーを、前記湿式粗粉砕機(4)へ
の原料供給量の50重量%以下の割合で、 前記湿式粗粉砕機(4)への供給原料に混入、又は、前
記湿式粗粉砕機(4)に投入、又は、前記湿式粗粉砕機
(4)で造った高濃度石炭・水スラリーに混入する特許
請求の範囲第1項に記載の高濃度石炭・水スラリーの製
造方法。2. The high-concentration coal / water slurry after being finely pulverized by the wet mill (5) at a ratio of 50% by weight or less of the amount of raw material supplied to the wet coarse pulverizer (4), Claims to be mixed in the feed material to the coarse crusher (4), or charged in the wet coarse crusher (4), or mixed in the high-concentration coal / water slurry produced by the wet coarse crusher (4) The method for producing a high-concentration coal / water slurry according to item 1 of the above.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18922787A JPH0768529B2 (en) | 1987-07-29 | 1987-07-29 | Method for producing high-concentration coal / water slurry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18922787A JPH0768529B2 (en) | 1987-07-29 | 1987-07-29 | Method for producing high-concentration coal / water slurry |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6433190A JPS6433190A (en) | 1989-02-03 |
| JPH0768529B2 true JPH0768529B2 (en) | 1995-07-26 |
Family
ID=16237711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18922787A Expired - Lifetime JPH0768529B2 (en) | 1987-07-29 | 1987-07-29 | Method for producing high-concentration coal / water slurry |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0768529B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012180481A (en) * | 2011-03-02 | 2012-09-20 | Tokyo Electric Power Co Inc:The | Method of manufacturing high density coal/water slurry |
| CN103965981B (en) | 2013-01-31 | 2016-05-25 | 通用电气公司 | The apparatus and method of preparation water-coal-slurry |
| CN115058267A (en) * | 2022-07-27 | 2022-09-16 | 神华准能资源综合开发有限公司 | Coal water slurry concentration method and coal water slurry concentration device |
-
1987
- 1987-07-29 JP JP18922787A patent/JPH0768529B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6433190A (en) | 1989-02-03 |
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