JPS5813190A - Transfer of slurry by pump - Google Patents

Transfer of slurry by pump

Info

Publication number
JPS5813190A
JPS5813190A JP11108681A JP11108681A JPS5813190A JP S5813190 A JPS5813190 A JP S5813190A JP 11108681 A JP11108681 A JP 11108681A JP 11108681 A JP11108681 A JP 11108681A JP S5813190 A JPS5813190 A JP S5813190A
Authority
JP
Japan
Prior art keywords
slurry
pump
transfer
density
fresh water
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.)
Granted
Application number
JP11108681A
Other languages
Japanese (ja)
Other versions
JPS6122154B2 (en
Inventor
Yasuo Nakai
康雄 中井
Hidemasa Takahama
高浜 秀正
Masaaki Tachikawa
正明 立川
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP11108681A priority Critical patent/JPS5813190A/en
Publication of JPS5813190A publication Critical patent/JPS5813190A/en
Publication of JPS6122154B2 publication Critical patent/JPS6122154B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/30Conveying materials in bulk through pipes or tubes by liquid pressure

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Control Of Non-Positive-Displacement Pumps (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)

Abstract

PURPOSE:To prevent coal particles from clogging by measuring a suction pressure and a discharge pressure of a slurry transfer pump and a current of a pump driving motor, computing a concentration or a density of slurry on the basis of the measurements, and supplying fresh water if the computed value exceeds a reference. CONSTITUTION:Pressure gauges 18, 19 and 20, 21 are disposed at suction sides and discharge sides of a suction pump 13 and a transfer pump 16 respectively, and ammeters 22, 23 are mounted to motors (not illustrated) for driving those pumps 13, 16 respectively. Those pressure gauges 18, 19, 20, 21 and ammeters 22, 23 are connected to an arithmetic controller 24 comprising a computer. Fresh water supply pipes 25, 26 open at the bottom of a hold 11 and at the upper part of a slurry storage tank 15, respectively. During transfer of slurry, output signals of the pressure gauges 20, 21 of the transfer pump 16 and the ammeter 23 are sent to the arithmetic controller 24, which computes a density of slurry from the measurements thereof. Based on the result, the controller controls opening or closing of a valve 28 of the fresh water supply pipe 26 of the tank 15 so that coal particles may be prevented from clogging.

Description

【発明の詳細な説明】 この発明はポンプによるスラリーの移送方法に関する。[Detailed description of the invention] The present invention relates to a method for transferring slurry using a pump.

たとえばスラリー輸送船から石炭、砂鉄などのスラリー
をポンプで吸引して陸揚げする場合、スラリー濃度が高
いと、スラリー中の粉粒物がスラリ、−移送配管の途中
に詰まったり、ポンプのモータの負荷が過大になるなど
の不都合が生、じる。このため、スラリー移送中にそ9
濃度を監視することが必要になるが、移送中のスラリー
の濃度を簡単に計測できる方法は提案されていない。
For example, when pumping slurry such as coal or iron sand from a slurry transport ship and discharging it ashore, if the concentration of the slurry is high, particles in the slurry may clog the slurry or the transfer piping, or the pump motor may become overloaded. This may cause inconveniences such as an excessive amount of Therefore, during slurry transfer,
Although it is necessary to monitor the concentration, no method has been proposed that can easily measure the concentration of slurry during transport.

この発明の目的は、移送中のスラリーの濃度または密度
を簡単かつ確実に計測し、これによってスラリーの濃度
・または密度を一定値以下に抑えることができるスラリ
ーの移送方法を提供することにある。
An object of the present invention is to provide a method for transporting slurry that can easily and reliably measure the concentration or density of slurry being transported, thereby suppressing the concentration or density of slurry below a certain value.

この発明によるスラリーの移送方法は、上記の目的を達
成するため、スラリー移送ポンプの吸込圧力および吐出
し圧力ならびにポンプ駆動用モータの電流を測定し、こ
れらの測定値からスラリー濃度またはスラリー密度を計
算し、スラリー濃度またはスラリー密度が一定の基準値
を越えたときにスラリーに清水を供給することを特徴と
する。
In order to achieve the above object, the slurry transfer method according to the present invention measures the suction pressure and discharge pressure of the slurry transfer pump and the current of the pump drive motor, and calculates the slurry concentration or slurry density from these measured values. The method is characterized in that fresh water is supplied to the slurry when the slurry concentration or slurry density exceeds a certain reference value.

以下図面を参照してこの発明の詳細な説明する。The present invention will be described in detail below with reference to the drawings.

図面は石炭スラリー輸送船のスラリー陸揚げ設備の一部
を示し、各船倉αDの底部に、高圧水噴射ノズルa渇が
設けられるとともに、スラリー吸引ポンプ13を備えた
スラリー吸す1管a1が接続されており、吸引管圓の他
端がスラリー溜めタンクa9の上部に配置さ、れている
。このタンクa9の底部に、スラリー移送ポンプ+16
1を備えたスラ□ リー移送管αηの一端が接続されている。吸引ポンプ(
13および移送ポンプ(IQの吸込側および吐出し側に
圧力計αtoss’(社)がそれぞれ設けられ、これら
のポンプαJaeの駆動用モータ(図示路)に電流計@
のがそれぞれ設けられており、これらの圧力計α印α9
1□(21)および電流計@(至)はコンピュータを備
えた演算制御装置(財)に接続さ・れている。
The drawing shows a part of the slurry landing equipment of a coal slurry transport ship, in which a high-pressure water injection nozzle a is provided at the bottom of each hold αD, and a slurry suction pipe A1 equipped with a slurry suction pump 13 is connected. The other end of the suction tube circle is placed above the slurry storage tank a9. A slurry transfer pump +16 is installed at the bottom of this tank a9.
1 is connected to one end of a slurry transfer pipe αη. Suction pump (
13 and a transfer pump (IQ), pressure gauges αtoss' (Company) are installed on the suction side and discharge side, respectively, and an ammeter @
are provided respectively, and these pressure gauges α mark α9
1□ (21) and the ammeter @ (to) are connected to an arithmetic and control unit equipped with a computer.

船倉aD底部およびスラリー溜めタンクαS上部に清水
供給管(251(261がそれぞれ設けられ、演算制御
装置′(至)に接続された操作弁@弼が各清水供給管@
母に取付けられている。
Fresh water supply pipes (251 (261) are installed at the bottom of the hold aD and the top of the slurry storage tank αS, respectively, and the operating valves connected to the arithmetic and control unit' (to) are connected to each fresh water supply pipe
attached to the mother.

上記の輸送船の船倉α1)に搭載された石炭スラリーは
積込み時または航行中にある程度脱水さn、揚げ地にお
いて陸揚げを行なう場合、船倉aυ底部のノズルQ2+
よりこnに高圧水が噴射される。このようにして適量の
水が加えらnたスラリーは、吸引ポレプ0:1により吸
引管(刊に吸引さ    □nてタンクa9に集められ
、さらに移送ポンプQ6)により移送管αηを通して陸
上′に移送される。なお、石炭スラリーを脱水せずに輸
送して、そのまま陸揚げすることも可能である。
The coal slurry loaded in the cargo hold α1) of the above transport ship is dehydrated to some extent during loading or during navigation, and when unloading at the unloading port, the nozzle Q2+
High-pressure water is sprayed at the tip. The slurry to which an appropriate amount of water has been added in this way is sucked into a suction pipe (by a suction polep 0:1) and collected in tank a9, and then sent to land via a transfer pipe αη by a transfer pump Q6. be transported. Note that it is also possible to transport the coal slurry without dehydrating it and unload it as is.

スラリー移送中、移送ポンプQ61の圧力;it (2
01(211および電流計@の出力信号が連続的に演算
制御に、これらの測定値からスラリーゞρを計算し、こ
の結果に基いてタンク05)の清水供給管敵の弁(支)
の開閉を制御する。すなわち、電流計@5より測定され
るポンプ駆動用モータの電流値をA、圧力計(20(2
1)により測定されるポンプQB+の吸込圧力をP6、
同吐出し圧力をPd、これらの差圧ンをP=Pd−Ps
、ポンプQ61の水頭をH=P/ρ、ポンプOeの吐出
し量をQとすれば、電流値Aは吐出し量Qおよび差圧P
の関数として式(1)のように表わされ、吐出し量Qは
水頭Hの関数として式(2)のように表わされる。
During slurry transfer, pressure of transfer pump Q61; it (2
The output signals of 01 (211 and ammeter @) are continuously used for calculation control, the slurry ρ is calculated from these measured values, and based on this result, the valve (branch) of the fresh water supply pipe of tank 05 is
control opening and closing. That is, the current value of the pump drive motor measured by the ammeter @5 is A, the pressure gauge (20 (2
The suction pressure of pump QB+ measured by 1) is P6,
The same discharge pressure is Pd, and the differential pressure between them is P=Pd-Ps
, the water head of pump Q61 is H=P/ρ, and the discharge amount of pump Oe is Q, then the current value A is the discharge amount Q and the differential pressure P.
The discharge amount Q is expressed as a function of the water head H as shown in equation (1), and the discharge amount Q is expressed as a function of the water head H as shown in equation (2).

A=f(Q、P)   ・・・・・・・・・・・(1)
Q)=f (H) =f (P/ρ)+111−(2)
これらの式+11 +21において未知数はスラリー密
度ρおよび吐出し量Qの2個であり、他は上記測定値か
ら直接求められるので、式fil (21を解くことに
よりスラリー密度ρおよび吐出し量Qを計算することが
できる。そして、スラリー密度が一定の基準値より大き
いとき番こは、弁■を開いてタンクQ51に清水を供給
し、これによってスラリー密度を小さく、する。また、
弁■が開いている状態でスラリー密度が上記基準値より
かなり小さくなったときには、弁■を閉じて清水の供給
を停止する。このようにすれば、スラリー密度が一定値
以下に保たれ、スラリー密度とスラリー濃度とは一定の
関係にあるので、スラリー濃度も一定値以下に保たれ、
移送管aηに石炭粒子が詰まったり移送ポンプ(161
のモータに過大な負荷がかかるおそれがない。なお、上
述のようにスラリー密度とスラリー濃度とは一定の関係
にあるので、スラリー密度の代わりにスラリー濃度を計
算して上記と同様に弁(2)の開閉を制御することも可
能である。
A=f(Q,P) ・・・・・・・・・・・・(1)
Q)=f (H) =f (P/ρ)+111-(2)
In these equations +11 +21, the two unknowns are the slurry density ρ and the discharge amount Q, and the others can be found directly from the above measured values, so by solving the equation fil (21), the slurry density ρ and the discharge amount Q can be calculated. When the slurry density is greater than a certain reference value, the controller opens valve ① to supply fresh water to tank Q51, thereby reducing the slurry density.Also,
When the slurry density becomes considerably smaller than the above reference value while valve (2) is open, valve (2) is closed to stop the supply of fresh water. In this way, the slurry density is kept below a certain value, and since there is a certain relationship between the slurry density and the slurry concentration, the slurry concentration is also kept below a certain value,
If the transfer pipe aη is clogged with coal particles or the transfer pump (161
There is no risk of excessive load being applied to the motor. Note that, as described above, since the slurry density and the slurry concentration have a certain relationship, it is also possible to calculate the slurry concentration instead of the slurry density and control the opening and closing of the valve (2) in the same manner as above.

また、演算制御装置@は、スラリー密度またはスラリー
濃度と吐出し量との乗算により移送管aη内を単位時間
に流れる石炭の重量(瞬間臀送量)を求めるとともに、
この騎間移送量を積算することにより石炭の積算移送量
を求め、必要に応じてこれらの値を表示する。
In addition, the arithmetic and control unit @ calculates the weight of coal flowing in the transfer pipe aη per unit time (instantaneous feeding amount) by multiplying the slurry density or slurry concentration by the discharge amount, and
The cumulative amount of coal transferred is calculated by summing up the amount of transferred coal, and these values are displayed as necessary.

また、スラリー移送中、吸引ポンプa急の圧力計a秒α
優および電流計(支)の出力iも連続的に演算制御装置
(支)に送られており、上記と、同様に、演算制御装置
(財)は船倉0υ底部の清水供給管(ハ)の−弁(イ)
を制御する。さらに、船倉(11)底部または吸(15
) す1管に石炭粒子が詰まった場合には、スラリー密度の
計算値が異常゛に小さくなったり、圧力計叫α9の測定
値が異常になったりするのア、演算制御装置(支)は、
このような異常現象を検知し、弁筒を開いて船倉O1J
底部に清水を供給することによ“り石炭粒、子の詰まり
を防′止する。
In addition, during slurry transfer, the suction pump a sudden pressure gauge a seconds α
The output i of the main and ammeter (sub) is also continuously sent to the arithmetic and control unit (sub), and similarly to the above, the arithmetic and control unit (incorporated) is connected to the fresh water supply pipe (c) at the bottom of the hold 0υ. -Valve (a)
control. Furthermore, the bottom of the hold (11) or the suction (15)
) If the pipe is clogged with coal particles, the calculated value of slurry density may become abnormally small, or the measured value of pressure gauge α9 may become abnormal. ,
When such an abnormal phenomenon is detected, the valve cylinder is opened and the hold O1J is closed.
By supplying fresh water to the bottom, clogging of coal particles and coal particles is prevented.

なお、輸送船への石炭スラリー積込み設備にも上記と同
様の装置を設けて同様の制御を行なうことができる。
Incidentally, a device similar to the above can be installed in a facility for loading coal slurry onto a transport ship, and similar control can be performed.

この発明によるスラリーの移送方法(ま石炭スラリーの
陸揚げ、積込み以外の移送時にも適用でき、さらには石
炭以外のスラリーにも適用で1゜ きる。          ) ゛以上のように、この発明によれば、スラリーの濃度ま
たは密度を一定値以下に抑えて、スラリー中の粉粒物の
詰まりゃポンプ駆動用モータの過負荷などを防止するこ
とができる。また、圧力計と電流計を用いて、スラリー
の濃度または密度を簡単かつ確実に計測することができ
る。
Slurry transfer method according to the present invention (applicable to transfers other than unloading and loading of coal slurry, and can even be applied to slurries other than coal.) As described above, according to the present invention, By suppressing the concentration or density of the slurry to a certain value or less, it is possible to prevent clogging of particulate matter in the slurry and overloading of the pump driving motor. Furthermore, the concentration or density of the slurry can be easily and reliably measured using a pressure gauge and an ammeter.

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

図面はこの発明の方法を実施する装置の1例を示す概略
管系図である。 α5)・拳・スラリー溜めタンク、ao・・・スラリー
移送ポンプ、07)・・・スラリー移送管、(201(
211・・・圧力計、の・声・電流計、(至)・・・演
算制御装置、(26)・・・清水供給管、(ハ)・・・
操作弁。     ′以  上 外4名
The drawing is a schematic pipe diagram showing one example of an apparatus for carrying out the method of the present invention. α5)・Fist・Slurry storage tank, ao...Slurry transfer pump, 07)...Slurry transfer pipe, (201(
211...Pressure gauge, voice/ammeter, (to)...arithmetic control unit, (26)...fresh water supply pipe, (c)...
Operation valve. ' or more 4 people

Claims (1)

【特許請求の範囲】[Claims] スラリー移送ポンプαeの吸込圧力および吐出し圧力な
らびにポンプ駆動用モータの電流を測定し、これらの測
定値からスラリー濃度またはスラリー密度を計算し、ス
ラリー濃度またはスラリー密度が一定の基準値を越えた
ときにスラリーに清水を供給することを特徴とするポン
プによるスラリーの移送方法。
Measure the suction pressure and discharge pressure of the slurry transfer pump αe and the current of the pump drive motor, calculate the slurry concentration or slurry density from these measured values, and when the slurry concentration or slurry density exceeds a certain reference value A method for transferring slurry using a pump, characterized in that fresh water is supplied to the slurry.
JP11108681A 1981-07-15 1981-07-15 Transfer of slurry by pump Granted JPS5813190A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11108681A JPS5813190A (en) 1981-07-15 1981-07-15 Transfer of slurry by pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11108681A JPS5813190A (en) 1981-07-15 1981-07-15 Transfer of slurry by pump

Publications (2)

Publication Number Publication Date
JPS5813190A true JPS5813190A (en) 1983-01-25
JPS6122154B2 JPS6122154B2 (en) 1986-05-30

Family

ID=14552021

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11108681A Granted JPS5813190A (en) 1981-07-15 1981-07-15 Transfer of slurry by pump

Country Status (1)

Country Link
JP (1) JPS5813190A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1014048C2 (en) * 1997-10-17 2002-01-22 Giw Ind Method for controlling slurry pumps.
WO2012145222A1 (en) * 2011-04-19 2012-10-26 Flowserve Management Company System and method for evaluating the performance of a pump
CN110642016A (en) * 2019-09-20 2020-01-03 中煤科工集团武汉设计研究院有限公司 Coarse particle coal slurry pipeline feeding system and feeding method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1014048C2 (en) * 1997-10-17 2002-01-22 Giw Ind Method for controlling slurry pumps.
WO2012145222A1 (en) * 2011-04-19 2012-10-26 Flowserve Management Company System and method for evaluating the performance of a pump
RU2585994C2 (en) * 2011-04-19 2016-06-10 Флоусерв Менеджмент Компани System and method for evaluating pump performance
US11976661B2 (en) 2011-04-19 2024-05-07 Flowserve Management Company System and method for evaluating the performance of a pump
CN110642016A (en) * 2019-09-20 2020-01-03 中煤科工集团武汉设计研究院有限公司 Coarse particle coal slurry pipeline feeding system and feeding method thereof

Also Published As

Publication number Publication date
JPS6122154B2 (en) 1986-05-30

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