JPS6122154B2 - - Google Patents
Info
- Publication number
- JPS6122154B2 JPS6122154B2 JP11108681A JP11108681A JPS6122154B2 JP S6122154 B2 JPS6122154 B2 JP S6122154B2 JP 11108681 A JP11108681 A JP 11108681A JP 11108681 A JP11108681 A JP 11108681A JP S6122154 B2 JPS6122154 B2 JP S6122154B2
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- pump
- density
- transfer
- concentration
- 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
- 239000002002 slurry Substances 0.000 claims description 60
- 239000013505 freshwater Substances 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 7
- 239000003245 coal Substances 0.000 description 7
- 239000003250 coal slurry Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 2
- 230000001186 cumulative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/30—Conveying 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)
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
リー移送配管の途中に詰まつたり、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の濃度を監視するこ
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 slurry concentration is high, particles in the slurry may clog the slurry transfer piping, or the load on the pump motor may increase. Inconveniences such as excessive size may occur. For this reason, it is necessary to monitor the concentration of the slurry during transfer, but no method has been proposed that can easily measure the concentration of the slurry during transfer.
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、これによつて
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. , 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実施例を説明す
る。 Embodiments of the present invention will be described 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11の底部に、高圧水噴
射ノズル12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引管14が接続
されており、吸引管14の他端がスラリー溜めタ
ンク15の上部に配置されている。このタンク1
5の底部に、スラリー移送ポンプ16を備えたス
ラリー移送管17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16の吸込側および
吐出し側に圧力計18,19,20,21がそれ
ぞれ設けられ、これらのポンプ13,16の駆動
用モータ(図示略)に電流計22,23がそれぞ
れ設けられており、これらの圧力計18,19,
20,21および電流計22,23はコンピユー
タを備えた演算制御装置24に接続されている。
船倉11底部およびスラリー溜めタンク15上部
に清水供給管25,26がそれぞれ設けられ、演
算制御装置24に接続された操作弁27,28が
各清水供給管25,26に取付けられている。 The drawing shows a part of the slurry landing equipment of a coal slurry transport ship, in which a high-pressure water injection nozzle 12 is provided at the bottom of each hold 11, and a slurry suction pipe 14 equipped with a slurry suction pump 13 is connected. The other end of the suction pipe 14 is placed at the top of the slurry storage tank 15. This tank 1
5 is connected to one end of a slurry transfer pipe 17 equipped with a slurry transfer pump 16. Pressure gauges 18, 19, 20, 21 are provided on the suction side and discharge side of the suction pump 13 and the transfer pump 16, respectively, and ammeters 22, 23 are provided on the drive motors (not shown) of these pumps 13, 16. These pressure gauges 18, 19,
20, 21 and ammeters 22, 23 are connected to an arithmetic and control unit 24 including a computer.
Fresh water supply pipes 25 and 26 are provided at the bottom of the hold 11 and at the top of the slurry storage tank 15, respectively, and operating valves 27 and 28 connected to the arithmetic and control unit 24 are attached to each of the fresh water supply pipes 25 and 26.
上記の輸送船の船倉11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
れ、揚げ地において陸揚げを行なう場合、船倉1
1底部のノズル12よりこれ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れたスラリ
ーは、吸引ポンプ13により吸引管14に吸引さ
れてタンク15に集められ、さらに移送ポンプ1
6により移送管17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 11 of the above-mentioned transport ship is dehydrated to some extent during loading or during navigation, and when unloading at the unloading port, the coal slurry is loaded into the cargo hold 11.
High-pressure water is injected into this from a nozzle 12 at the bottom. The slurry to which an appropriate amount of water has been added in this manner is sucked into a suction pipe 14 by a suction pump 13 and collected in a tank 15, and then further pumped into a transfer pump 14.
6 and transferred to land through a transfer pipe 17.
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16の圧力計2
0,21および電流計23の出力信号が連続的に
演算制御装置24に送られ、演算制御装置24
は、次のように、これらの測定値からスラリー密
度ρを計算し、この結果に基いてタンク15の清
水供給管26の弁28の開閉を制御する。すなわ
ち、電流計23に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20,21により測定
されるポンプ16の吸込圧力をPs、同吐出し圧
力をPd、これらの差圧をP=Pd−Ps、ポンプ1
6の水頭をH=Pρ、ポンプ16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, the pressure gauge 2 of the transfer pump 16
0, 21 and the output signals of the ammeter 23 are continuously sent to the arithmetic and control unit 24.
calculates the slurry density ρ from these measured values as follows, and controls the opening and closing of the valve 28 of the fresh water supply pipe 26 of the tank 15 based on this result. That is, the current value of the pump drive motor measured by the ammeter 23 is A, the suction pressure of the pump 16 measured by the pressure gauges 20 and 21 is Ps, the discharge pressure is Pd, and the differential pressure between these is P= Pd−Ps, pump 1
The water head of 6 is H = Pρ, and the discharge amount of pump 16 is Q
Then, the current value A is expressed as a function of the discharge amount Q and the differential pressure P 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) ……(2)
これらの式(1)(2)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(1)(2)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には、弁28を開いてタンク
15に清水を供給し、これによつてスラリー密度
を小さくする。また、弁28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つ
たときには、弁28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17に石炭粒子が詰まつたり移
送ポンプ16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28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)...(2) In these equations (1) and (2), the unknowns are the slurry density ρ and the discharge amount Since the other values can be obtained directly from the above measured values, the slurry density ρ and the discharge amount Q can be calculated by solving equations (1) and (2). When the slurry density is higher than a certain reference value, the valve 28 is opened to supply fresh water to the tank 15, thereby reducing the slurry density. Further, when the slurry density becomes considerably smaller than the above reference value while the valve 28 is open, the valve 28 is closed and the supply of fresh water is stopped. 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, and the transfer pipe 17 is not clogged with coal particles. There is no risk of excessive load being applied to the motor of the transfer pump 16. 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 28 in the same manner as above.
また、演算制御装置24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
17内を単位時間に流れる石炭の重量(瞬間移送
量)を求めるとともに、この瞬間移送量を積算す
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。 Further, the arithmetic and control unit 24 calculates the weight of coal flowing in the transfer pipe 17 per unit time (instantaneous transfer amount) by multiplying the slurry density or the slurry concentration by the discharge amount, and integrates this instantaneous transfer amount. Calculate the cumulative amount of coal transferred and display these values as necessary.
また、スラリー移送中、吸引ポンプ13の圧力
計18,19および電流計22の出力信号も連続
的に演算制御装置24に送られており、上記と同
様に、演算制御装置24は船倉11底部の清水供
給管25の弁27を制御する。さらに、船倉11
底部または吸引管14に石炭粒子が詰まつた場合
には、スラリー密度の計算値が異常に小さくなつ
たり、圧力計18,19の測定値が異常になつた
りするので、演算制御装置24は、このような異
常現象を検知し、弁27を開いて船倉11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。 Also, during slurry transfer, the output signals of the pressure gauges 18, 19 and ammeter 22 of the suction pump 13 are continuously sent to the arithmetic and control unit 24, and similarly to the above, the arithmetic and control unit 24 is connected to the bottom of the hold 11. The valve 27 of the fresh water supply pipe 25 is controlled. In addition, hold 11
If the bottom or the suction pipe 14 is clogged with coal particles, the calculated value of the slurry density may become abnormally small or the measured values of the pressure gauges 18 and 19 may become abnormal. By detecting such an abnormal phenomenon and opening the valve 27 to supply fresh water to the bottom of the hold 11, clogging with 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は石炭スラ
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き
る。 The slurry transfer method according to the present invention can be applied to transfers other than unloading and loading of coal slurry, and can also be applied to slurries other than coal.
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や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。 As described above, according to the present invention, the concentration or density of the slurry can be suppressed to a certain value or less, and clogging of particulate matter in the slurry and overloading of the pump driving motor can be prevented. Furthermore, the concentration or density of the slurry can be easily and reliably measured using a pressure gauge and an ammeter.
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。
15……スラリー溜めタンク、16……スラリ
ー移送ポンプ、17……スラリー移送管、20,
21……圧力計、23……電流計、24……演算
制御装置、26……清水供給管、28……操作
弁。
The drawing is a schematic pipe diagram showing one example of an apparatus for carrying out the method of the present invention. 15...Slurry storage tank, 16...Slurry transfer pump, 17...Slurry transfer pipe, 20,
21... Pressure gauge, 23... Ammeter, 24... Arithmetic control device, 26... Fresh water supply pipe, 28... Operation valve.
Claims (1)
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。1 Measure the suction pressure and discharge pressure of the slurry transfer pump 16 and the current of the pump drive motor, calculate the slurry concentration or slurry density from these measured values, and determine if the slurry concentration or slurry density exceeds a certain reference value. A method of transferring slurry by means of a pump, sometimes characterized by supplying fresh water to the slurry.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11108681A JPS5813190A (en) | 1981-07-15 | 1981-07-15 | How to transfer slurry using a pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11108681A JPS5813190A (en) | 1981-07-15 | 1981-07-15 | How to transfer slurry using a pump |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5813190A JPS5813190A (en) | 1983-01-25 |
| JPS6122154B2 true 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 | How to transfer slurry using a pump |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5813190A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6033187A (en) * | 1997-10-17 | 2000-03-07 | Giw Industries, Inc. | Method for controlling slurry pump performance to increase system operational stability |
| US11976661B2 (en) | 2011-04-19 | 2024-05-07 | Flowserve Management Company | System and method for evaluating the performance of a pump |
| CN110642016B (en) * | 2019-09-20 | 2021-11-02 | 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 |
| CN114720326A (en) * | 2022-04-12 | 2022-07-08 | 中国人民解放军海军特色医学中心 | A device and method for measuring the density of an object by air pressure |
-
1981
- 1981-07-15 JP JP11108681A patent/JPS5813190A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5813190A (en) | 1983-01-25 |
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