JPH0412918B2 - - Google Patents
Info
- Publication number
- JPH0412918B2 JPH0412918B2 JP63090869A JP9086988A JPH0412918B2 JP H0412918 B2 JPH0412918 B2 JP H0412918B2 JP 63090869 A JP63090869 A JP 63090869A JP 9086988 A JP9086988 A JP 9086988A JP H0412918 B2 JPH0412918 B2 JP H0412918B2
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- coal
- water
- moisture
- amount
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/21—Measuring
- B01F35/2135—Humidity, e.g. moisture content
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/22—Control or regulation
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
- B01F35/2218—Weight of at least one component to be mixed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/82—Forming a predetermined ratio of the substances to be mixed by adding a material to be mixed to a mixture in response to a detected feature, e.g. density, radioactivity, consumed power or colour
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- 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、高濃度石炭水スラリー製造方法に係
り、とくにスラリー水分を制御するようにした石
炭水スラリー製造方法におけるスラリー水分制御
方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing a highly concentrated coal-water slurry, and more particularly to a method for controlling slurry moisture in a method for producing a coal-water slurry in which the slurry moisture is controlled.
従来の石炭水スラリー製造方法は、湿式ボール
ミルを用い、破砕された石炭を水及び界面活性剤
から成る分散剤と共に湿式粉砕し、スラリー化
し、石炭濃度が約60重量%以上の石炭水スラリー
を製造する。また、湿式粉砕にさいし粉砕熱によ
り温度上昇した石炭水スラリーを冷却するため、
石炭水スラリー中の粗大粒子を分離除去するさい
空気流との熱交換するようにすることが提案され
ている(例えば、特開昭60−8393号公報、特開昭
60−13887号公報、特願昭61−212011号明細書な
ど)。
The conventional coal-water slurry production method uses a wet ball mill to wet-pulverize crushed coal with a dispersant consisting of water and a surfactant to form a slurry, producing a coal-water slurry with a coal concentration of approximately 60% by weight or more. do. In addition, in order to cool the coal-water slurry whose temperature has increased due to the heat of grinding during wet grinding,
It has been proposed to perform heat exchange with an air stream when separating and removing coarse particles in a coal-water slurry (for example, Japanese Patent Laid-Open No. 60-8393,
60-13887, Japanese Patent Application No. 61-212011, etc.).
石炭水スラリー製造にさいし、石炭水スラリー
の性状のうち、水分すなわち石炭濃度が変動する
とプロセスに多くの影響を与える。すなわち、湿
式ミルにおける粉砕性をはじめ、流動性、安定性
などの流動特性、さらに、燃料特性として発熱量
ならびに熱効率、バーナにおける微粒化や燃焼特
性などへの著しい影響をあげることができる。 In the production of coal-water slurry, variations in water content, that is, coal concentration, among the properties of coal-water slurry, have a large effect on the process. That is, it can have a significant influence on the pulverization properties in a wet mill, flow properties such as fluidity and stability, as well as fuel properties such as calorific value and thermal efficiency, atomization in a burner, and combustion properties.
上記の影響を解消するため、従来の石炭水スラ
リー製造方法におけるスラリー水分制御方法とし
ては、所要のスラリー水分が得られるように湿式
ミルへの石炭および水の供給量を比率制御のもと
で調節してそれぞれの供給を行い、さらに、湿式
粉砕過程における石炭水スラリーの粉砕熱による
温度上昇にともなうスラリー水分の蒸発量に対す
る補正を手動により行うことによつて上記供給量
を調節するようにしていた。また、スラリー水分
を工業的に適用しうるスラリー濃度計などをもち
いて測定して上記の石炭および水の供給量を調節
することによりスラリー水分制御することも行わ
れていた。 To eliminate the above effects, the slurry moisture control method in the conventional coal-water slurry manufacturing method involves adjusting the amount of coal and water supplied to the wet mill under ratio control to obtain the required slurry moisture. In addition, the above-mentioned supply amounts were adjusted by manually making corrections for the amount of evaporation of slurry moisture caused by the temperature rise due to the heat of pulverization of the coal-water slurry during the wet pulverization process. . In addition, slurry water content has also been controlled by measuring the slurry water content using an industrially applicable slurry concentration meter and adjusting the above-mentioned supply amounts of coal and water.
しかしながら、上記従来の石炭水スラリー製造
方法におけるスラリー水分制御方法では、オフラ
インによりスラリー水分を測定し、スラリー水分
の蒸発量に対する補正を行つたが、スラリー水分
の蒸発量も多数の複雑な変動要因によつて影響を
受けるので、上記蒸発量の正確な検出が困難であ
るため、正確なスラリー水分を制御することが困
難であつた。また、スラリー濃度計などをもちい
てスラリー水分を検出しフイードバツク制御によ
り石炭および水の供給量を調節するとしても、複
雑な変動要因のもとでのプロセスに対して適切な
スラリー水分制御が困難であると言う問題があつ
た。
However, in the slurry moisture control method in the conventional coal water slurry manufacturing method described above, the slurry moisture is measured off-line and correction is made for the amount of evaporation of the slurry moisture, but the amount of evaporation of the slurry moisture is also subject to many complicated fluctuation factors. Therefore, it is difficult to accurately detect the amount of evaporation, and it is difficult to accurately control the slurry water content. In addition, even if slurry moisture is detected using a slurry concentration meter and the amount of coal and water supplied is adjusted through feedback control, it is difficult to control slurry moisture appropriately for processes under complex fluctuating factors. There was a problem.
本発明はこのような従来の問題を解決するもの
であり、スラリー水分の蒸発量を簡易な方法をも
ちいて確実に決定し、高い的中率をもつて正確な
スラリー水分制御をすることができる優れた石炭
水スラリー製造方法におけるスラリー水分制御を
提供することを目的とするものである。 The present invention solves these conventional problems by reliably determining the amount of evaporation of slurry water using a simple method, and making it possible to accurately control slurry water with a high accuracy rate. The purpose is to provide superior slurry moisture control in a coal-water slurry manufacturing method.
本発明は上記目的を達成するために、石炭を湿
式ミルにて水、分散剤と共に湿式粉砕してスラリ
ー化し、粉砕熱により温度上昇した前記スラリー
を空気流により冷却する石炭水スラリー製造方法
におけるスラリー水分制御方法であつて、スラリ
ーと空気流との接触前後における空気流の湿度変
化を検出して水分蒸発量を演算し、湿式ミルへの
水供給量を操作してスラリー水分を制御するよう
にしたものである。
In order to achieve the above object, the present invention provides a slurry in a method for producing a coal-water slurry in which coal is wet-pulverized with water and a dispersant in a wet mill to form a slurry, and the slurry whose temperature has increased due to the heat of crushing is cooled by an air flow. This is a moisture control method that detects the humidity change in the air flow before and after the slurry comes into contact with the air flow, calculates the amount of moisture evaporation, and controls the slurry moisture by controlling the amount of water supplied to the wet mill. This is what I did.
本発明は上記のような構成により次のような作
用を有する。すなわち、湿式粉砕にともない粉砕
熱により温度上昇したスラリーをその流路を包囲
する冷却室において空気流により冷却し、そのさ
い、スラリーと空気流との接触前後における空気
流の湿度変化を検出することによりスラリーの水
分蒸発量を演算することができるので、スラリー
製品の所要の水分が得られるように、上記水分蒸
発量による補正のもとで、湿式ミルへの水供給量
を操作することにより複雑な変動要因の影響を受
けても高い的中率をもつて正確なスラリー水分を
制御することが可能である。
The present invention has the following effects due to the above configuration. That is, the slurry whose temperature has increased due to the heat of grinding due to wet grinding is cooled by air flow in a cooling chamber surrounding the flow path, and at that time, the change in humidity of the air flow is detected before and after the slurry comes into contact with the air flow. Since the water evaporation amount of the slurry can be calculated using the above method, the amount of water supplied to the wet mill can be manipulated to obtain the required water content of the slurry product. It is possible to accurately control slurry moisture with high accuracy even under the influence of various fluctuation factors.
以下、本発明の一実施例を図面について詳細に
説明する。
Hereinafter, one embodiment of the present invention will be described in detail with reference to the drawings.
第1図は、本発明の実施例に係る構成をしめす
ものである。 FIG. 1 shows a configuration according to an embodiment of the present invention.
第1図において、1は破砕された石炭2を貯留
する石炭貯留槽、3は石炭2を計量給炭する計量
給炭機、4は石炭2を水、分散剤と共に湿式粉砕
する湿式ボールミルである。5はポンプ6を有す
る水供給管、8はポンプ9を有する分散剤供給管
で、給水流量調節弁7を介して湿式ボールミル4
の入口に連通されている。10は湿式ボールミル
4により製造されたスラリーをしめし、11はス
ラリー10に含まれている石炭の粗大粒子を分離
除去するための振動篩である。12は振動篩11
を通過したスラリーを空気流により冷却するため
の冷却室をしめし、冷却室12には空気取入口お
よび空気排出口とがそれぞれ設けられている。冷
却室12の空気取入口には入口空気管13が設け
られ、また、空気排出口には出口空気管26が設
けられている。送風機30によつて冷却室12内
に空気を流動させるようにしている。22はスラ
リー管をしめし、冷却室12により冷却されたス
ラリー20はポンプ21によつて次工程に給送さ
れる。 In Fig. 1, 1 is a coal storage tank that stores crushed coal 2, 3 is a metering coal feeder that feeds coal 2 by metering, and 4 is a wet ball mill that wet-pulverizes coal 2 together with water and a dispersant. . 5 is a water supply pipe with a pump 6; 8 is a dispersant supply pipe with a pump 9;
It is connected to the entrance. Reference numeral 10 indicates a slurry produced by the wet ball mill 4, and reference numeral 11 indicates a vibrating sieve for separating and removing coarse particles of coal contained in the slurry 10. 12 is a vibrating sieve 11
The cooling chamber 12 is provided with an air inlet and an air outlet, respectively, for cooling the slurry that has passed through the cooling chamber 12 with an air flow. An inlet air pipe 13 is provided at the air intake of the cooling chamber 12, and an outlet air pipe 26 is provided at the air outlet. He is trying to make air flow into the cooling chamber 12 by the blower 30. 22 indicates a slurry pipe, and the slurry 20 cooled in the cooling chamber 12 is fed to the next step by a pump 21.
振動篩11によつて分離された粗大粒子17は
輸送手段、例えば、ポンプ18によつて給送さ
れ、粗粒スラリー19として再び湿式ボールミル
4に戻されてスラリー製造に供せられる。入口空
気管13には湿度計14、流量計15および温度
計16がそれぞれ設けられ入口空気流の状態値を
検出するために用いられる。出口空気管26には
湿度計27、流量計28および温度計29がそれ
ぞれ設けられ出口空気流の状態値を検出するため
に用いられる。スラリー管22にはスラリー濃度
計23、流量計24および温度計25がそれぞれ
設けられスラリー製品の性状を検出するために用
いられる。 The coarse particles 17 separated by the vibrating sieve 11 are fed by a transport means, for example, a pump 18, and are returned to the wet ball mill 4 as a coarse particle slurry 19 to be used for slurry production. The inlet air pipe 13 is provided with a hygrometer 14, a flow meter 15, and a thermometer 16, respectively, and are used to detect the state value of the inlet air flow. The outlet air pipe 26 is provided with a hygrometer 27, a flow meter 28, and a thermometer 29, respectively, and are used to detect the state value of the outlet air flow. The slurry pipe 22 is provided with a slurry concentration meter 23, a flow meter 24, and a thermometer 25, which are used to detect the properties of the slurry product.
31は主制御器、32は設定指令をしめし、上
記入口空気流、出口空気流の状態値およびスラリ
ー製品の性状の測定値がそれぞれ入力される。主
制御器31においてはスラリー製品の水分をはじ
めとする設定指令値として、入口空気流および出
口空気流における湿度、流量、温度の測定値によ
つてそれぞれの空気流に含まれる水分量を演算
し、さらに、上記水分量の減算処理によつてスラ
リーから空気流に移動した水分量、すなわち、水
分蒸発量の演算が行われる。主制御器31からは
給水流量調節弁7に対する信号34が出力せら
れ、このさい、前記の水分蒸発量により補正した
水供給量となるように設定される。出力信号33
は計量供給機3に対する給炭量設定を行う。給水
流量調節弁7および計量供給機3においては上記
給水流量偏差および給炭量偏差に対応して給水流
量および給炭量の操作、制御が行われる。 Reference numeral 31 indicates a main controller, and 32 indicates a setting command, into which the state values of the inlet air flow and outlet air flow and the measured values of the properties of the slurry product are respectively input. The main controller 31 calculates the amount of moisture contained in each air stream based on the measured values of humidity, flow rate, and temperature in the inlet air stream and outlet air stream, as set command values including the moisture content of the slurry product. Furthermore, the amount of moisture transferred from the slurry to the air flow by the moisture amount subtraction process, that is, the amount of moisture evaporated is calculated. The main controller 31 outputs a signal 34 to the water supply flow rate control valve 7, and at this time, the water supply amount is set so as to be corrected based on the water evaporation amount. Output signal 33
sets the amount of coal to be fed to the metering feeder 3. In the water supply flow rate control valve 7 and the metering feeder 3, the water supply flow rate and the coal supply amount are operated and controlled in response to the above-mentioned water supply flow rate deviation and coal supply amount deviation.
次に上記実施例の動作について説明する。上記
実施例において、石炭貯留槽1に貯留された石炭
2は計量給炭機3により湿式ボールミル4に所定
給炭量をもつて給炭され、同時に水および分散剤
が水供給管5および分散剤供給管8より給水流量
調節弁7により所定水供給量をもつて湿式ボール
ミル4に給水される。そして石炭2は湿式ボール
ミル4の運転によつて湿式粉砕のもとで微粒化
し、スラリー10となつて振動篩11に導かれ
る。このさい、スラリー10は粉砕熱により温度
上昇をともなつている。スラリー10に含まれて
いる石炭の粗大粒子の分離除去したのち、冷却室
12において入口空気管13からの空気流との直
接接触による熱交換が行われ、スラリーの冷却が
行われると同時にスラリー中の水分が出口空気管
26の空気流側に移動する。かくして、スラリー
と空気流との接触前後において空気流の湿度変化
を発生させることになる。したがつて入口空気管
13および出口空気管26内の空気流の湿度を測
定し、主制御器31に入力されるとともに演算処
理されその湿度変化量に対し空気流量、温度を考
慮してスラリー中の水分変化量、換言すれば水分
蒸発量が演算によつて決められる。ついで、スラ
リー製品の所要の水分量に対してスラリーの水分
蒸発量により補正した水供給量となるように設定
した信号34が出力されて給水流量の操作、制御
を行い、同時に給炭量の操作、制御を行うことに
より、スラリー水分制御を高い的中率をもつて正
確にすることができる。 Next, the operation of the above embodiment will be explained. In the above embodiment, the coal 2 stored in the coal storage tank 1 is fed to the wet ball mill 4 with a predetermined coal feed amount by the metering coal feeder 3, and at the same time, water and dispersant are supplied to the water supply pipe 5 and the dispersant. Water is supplied from the supply pipe 8 to the wet ball mill 4 at a predetermined amount by the water supply flow rate control valve 7. Then, the coal 2 is atomized by wet pulverization by the operation of the wet ball mill 4, becomes a slurry 10, and is led to a vibrating sieve 11. At this time, the temperature of the slurry 10 increases due to the heat of crushing. After the coarse particles of coal contained in the slurry 10 are separated and removed, heat exchange is performed in the cooling chamber 12 by direct contact with the air flow from the inlet air pipe 13, and the slurry is cooled and at the same time moisture moves to the airflow side of the outlet air tube 26. This results in a humidity change in the air stream before and after the slurry contacts the air stream. Therefore, the humidity of the air flow in the inlet air pipe 13 and the outlet air pipe 26 is measured, and is input to the main controller 31 and processed, and the air flow rate and temperature are taken into consideration for the amount of humidity change. The amount of moisture change, in other words, the amount of moisture evaporation, is determined by calculation. Next, a signal 34 is output, which is set so that the water supply amount is corrected by the water evaporation amount of the slurry for the required water content of the slurry product, and the water supply flow rate is operated and controlled, and at the same time, the coal feed amount is operated. , control enables accurate slurry moisture control with high accuracy.
このように、上記実施例によれば、石炭水スラ
リーを湿式ミルにより製造するにあたり、スラリ
ー水分制御のため石炭および水の供給量を比率制
御のもとで調節して供給し、さらに、石炭水スラ
リーの粉砕熱による温度上昇にともなうスラリー
水分蒸発量による水供給量の補正が冷却室におけ
る石炭水スラリーと空気流との接触前後における
空気流の湿度変化の検出のもとで行われるので、
上記補正を確実に行うことができ、石炭水スラリ
ー製造過程において複雑な変動要因の影響を受け
る場合でも高い的中率をもつて正確なスラリー水
分制御を行うことができる。 In this way, according to the above embodiment, when producing coal water slurry using a wet mill, the amounts of coal and water supplied are adjusted under ratio control in order to control the slurry moisture content, and the coal and water slurry is The amount of water supplied is corrected based on the amount of slurry moisture evaporated as the temperature rises due to the heat of grinding the slurry, and the amount of water supplied is corrected based on the detection of the humidity change in the air flow before and after the contact between the coal water slurry and the air flow in the cooling chamber.
The above correction can be performed reliably, and even when the coal-water slurry production process is influenced by complex fluctuation factors, accurate slurry moisture control can be performed with a high accuracy rate.
本発明の実施態様は上記実施例のみに限定され
るものでなく、種々の態様が採用可能である。 The embodiments of the present invention are not limited to the above embodiments, and various embodiments can be adopted.
本発明は上記実施例により明らかなように、石
炭を湿式ミルにてスラリー化し、粉砕熱により温
度上昇したスラリーを空気流により冷却する石炭
水スラリー製造方法におけるスラリー水分制御の
ため、冷却室におけるスラリーと空気流との接触
前後における空気流の湿度変化の検出のもとでス
ラリー水分蒸発量を演算し湿式ミルへの水供給量
の補正が確実になされて操作されるので、石炭水
スラリー製造過程において複雑な変動要因の影響
を受ける場合でも高い的中率をもつて正確なスラ
リー水分制御を行うことができるという顕著な効
果を奏する。
As is clear from the above embodiments, the present invention is aimed at controlling the moisture content of the slurry in a coal-water slurry manufacturing method in which coal is slurried in a wet mill and the slurry whose temperature has risen due to the heat of grinding is cooled by an air flow. The amount of water evaporated in the slurry is calculated based on the detection of humidity changes in the air flow before and after contact with the air flow, and the amount of water supplied to the wet mill is reliably corrected and operated. This method has the remarkable effect of being able to accurately control slurry moisture with a high accuracy rate even when it is affected by complex fluctuation factors.
第1図は本発明の一実施例に係る概略フローシ
ートである。
2…石炭、4…湿式ミル、5…水供給管、7…
給水流量調節弁、12…冷却室、13…入口空気
管、14,27…湿度計、20…スラリー、26
…出口空気管、31…主制御器。
FIG. 1 is a schematic flow sheet according to an embodiment of the present invention. 2...Coal, 4...Wet mill, 5...Water supply pipe, 7...
Water supply flow rate control valve, 12...Cooling chamber, 13...Inlet air pipe, 14, 27...Hygrometer, 20...Slurry, 26
...Outlet air pipe, 31...Main controller.
Claims (1)
砕してスラリー化し、粉砕熱により温度上昇した
前記スラリーを空気流により冷却する石炭水スラ
リー製造方法におけるスラリー水分制御方法であ
つて、スラリーと空気流との接触前後における空
気流の湿度変化を検出して水分蒸発量を演算し、
湿式ミルへの水供給量を操作してスラリー水分を
制御することを特徴とする石炭水スラリー製造方
法におけるスラリー水分制御方法。1. A slurry moisture control method in a coal-water slurry manufacturing method in which coal is wet-pulverized with water and a dispersant in a wet mill to form a slurry, and the slurry, whose temperature has risen due to the heat of crushing, is cooled by air flow. The amount of moisture evaporated is calculated by detecting the humidity change in the air flow before and after contact with the air flow,
A method for controlling slurry moisture in a coal-water slurry manufacturing method, which comprises controlling slurry moisture by controlling the amount of water supplied to a wet mill.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63090869A JPH01261496A (en) | 1988-04-13 | 1988-04-13 | Method of regulating water content of slurry in production of coal-water slurry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63090869A JPH01261496A (en) | 1988-04-13 | 1988-04-13 | Method of regulating water content of slurry in production of coal-water slurry |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01261496A JPH01261496A (en) | 1989-10-18 |
| JPH0412918B2 true JPH0412918B2 (en) | 1992-03-06 |
Family
ID=14010527
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63090869A Granted JPH01261496A (en) | 1988-04-13 | 1988-04-13 | Method of regulating water content of slurry in production of coal-water slurry |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01261496A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105819231A (en) * | 2016-03-28 | 2016-08-03 | 徐州工业职业技术学院 | Pipeline conveying method and device for gas-making wet coal ash |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020052550A (en) * | 2000-12-26 | 2002-07-04 | 이구택 | Method and apparatus for milling semi-smokeless coal |
| CN105233731A (en) * | 2015-11-17 | 2016-01-13 | 重庆市渝派农产品开发有限公司 | Dried tofu stirring device with automatic feeding function |
| CN106311051A (en) * | 2016-08-31 | 2017-01-11 | 无锡东恒新能源科技有限公司 | System for premixing slurry with high solid content |
-
1988
- 1988-04-13 JP JP63090869A patent/JPH01261496A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105819231A (en) * | 2016-03-28 | 2016-08-03 | 徐州工业职业技术学院 | Pipeline conveying method and device for gas-making wet coal ash |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01261496A (en) | 1989-10-18 |
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