WO2010108380A1 - 一种长距离浆体管道输送压力检测系统及检测方法 - Google Patents

一种长距离浆体管道输送压力检测系统及检测方法 Download PDF

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Publication number
WO2010108380A1
WO2010108380A1 PCT/CN2010/000092 CN2010000092W WO2010108380A1 WO 2010108380 A1 WO2010108380 A1 WO 2010108380A1 CN 2010000092 W CN2010000092 W CN 2010000092W WO 2010108380 A1 WO2010108380 A1 WO 2010108380A1
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WO
WIPO (PCT)
Prior art keywords
differential pressure
detection
ring pipe
loop
slurry
Prior art date
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PCT/CN2010/000092
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English (en)
French (fr)
Inventor
安建
普光跃
黄朝兵
潘春雷
Original Assignee
云南大红山管道有限公司
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 云南大红山管道有限公司 filed Critical 云南大红山管道有限公司
Priority to BRPI1009374A priority Critical patent/BRPI1009374B1/pt
Priority to AU2010228003A priority patent/AU2010228003B2/en
Publication of WO2010108380A1 publication Critical patent/WO2010108380A1/zh

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Classifications

    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01L—MEASURING FORCE, STRESS, TORQUE, WORK, MECHANICAL POWER, MECHANICAL EFFICIENCY, OR FLUID PRESSURE
    • G01L13/00—Devices or apparatus for measuring differences of two or more fluid pressure values
    • E—FIXED CONSTRUCTIONS
    • E02—HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
    • E02F—DREDGING; SOIL-SHIFTING
    • E02F3/00—Dredgers; Soil-shifting machines
    • E02F3/04—Dredgers; Soil-shifting machines mechanically-driven
    • E02F3/88—Dredgers; Soil-shifting machines mechanically-driven with arrangements acting by a sucking or forcing effect, e.g. suction dredgers
    • E02F3/90—Component parts, e.g. arrangement or adaptation of pumps
    • E02F3/907—Measuring or control devices, e.g. control units, detection means or sensors
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow
    • G01F1/05—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects
    • G01F1/34—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects by measuring pressure or differential pressure
    • G01F1/36—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects by measuring pressure or differential pressure the pressure or differential pressure being created by the use of flow constriction
    • G01F1/37—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects by measuring pressure or differential pressure the pressure or differential pressure being created by the use of flow constriction the pressure or differential pressure being measured by means of communicating tubes or reservoirs with movable fluid levels, e.g. by U-tubes
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F5/00—Measuring a proportion of the volume flow
    • G01F5/005—Measuring a proportion of the volume flow by measuring pressure or differential pressure, created by the use of flow constriction

Definitions

  • the invention belongs to the field of long-distance slurry pipeline transportation, and particularly relates to a long-distance slurry pipeline conveying pressure detecting system and a detecting method.
  • the present invention discloses a long-distance slurry pipeline conveying pressure detecting system and a detecting method, and the specific technical solutions are as follows.
  • a long-distance paddle pipeline conveying pressure detecting system comprising a detecting loop pipe, a differential pressure transmitter and a mercury U-tube differential pressure gauge, the detecting loop pipe is completely identical to the main pipe, and is arranged in parallel with the main pipe, and the differential pressure is sent
  • the mercury and U-tube differential pressure gauges are installed at both ends of the detection ring tube, and a main pipe is installed in the main pipe, a ring pipe inlet valve is installed at the inlet end of the detection ring pipe, and a ring pipe outlet valve is installed at the outlet end.
  • the differential pressure transmitter converts the differential pressure across the loop detected by the field into an analog signal recognizable by the programmable logic controller, and transmits it to the programmable logic controller, and then to the pipeline operation expert system, the pipeline operation expert system.
  • the resistance along the unit length at the current flow rate and concentration is calculated in conjunction with the actual length of the test collar.
  • the length of the detection loop is approximately 200 meters.
  • a method for detecting slurry pressure in a long distance slurry pipeline includes the following steps: when performing slurry transportation, closing the main valve, opening the annular inlet valve and the annular outlet valve, so that the slurry flows before entering the main pump Detecting the loop tube;
  • the differential pressure transmitter detects the differential pressure across the loop and sends the detected differential pressure signal to the programmable logic controller;
  • the pipeline operation expert system takes the slurry differential pressure value from the programmable logic controller and calculates the resistance per unit length at the current flow rate and concentration in combination with the actual length of the detection loop.
  • each pressure detection point along the main pipeline According to the length and altitude elevation of each pressure detection point along the main pipeline, the theoretical pressure value of each inspection point is calculated, and compared with the actual detection value, the fluid movement state of the slurry in the pipeline is judged.
  • the accuracy of the differential pressure transmitter is calibrated with a mercury U-tube differential pressure gauge.
  • Figure 1 is a schematic view of the long-distance slurry pipeline delivery pressure detecting system of the present invention.
  • a detection loop 2 identical to the main pipe 1 is arranged in parallel with the main pipe 1, and the length is about 200.
  • Meter install differential pressure transmitter 4 and mercury U-tube differential pressure gauge 3 at both ends of the loop.
  • the main valve 7, the open loop inlet valve 5 and the loop outlet valve 6 are closed, so that the slurry flows through the detecting loop 2 before entering the main pump, and the concentration of the slurry in the loop 2 is detected.
  • the flow rate is the same as the slurry concentration and flow rate in the main pipe 1.
  • the accuracy of the differential pressure transmitter 4 is calibrated by the U-tube differential pressure gauge 3, and the calibrated differential pressure transmitter 4 detects
  • the differential pressure signal is sent to the PLC (Programmable Logic Controller). After the pipeline operation expert system obtains the value from the PLC, combined with the actual length of the detection loop 1 can accurately calculate the unit length at the flow rate and concentration. Resistance along the way.
  • the pressure value of each detection point can be accurately calculated. Compared with the actual detection value, the fluid movement condition of the slurry in the pipeline can be judged, reminding and guiding operation. The personnel perform the corresponding operations in time.

Description

一种长距离浆体管道输送压力检测系统及裣测方法 技术领域
本发明属于长距离浆体管道输送领域， 特别是涉及一种长距离浆 体管道输送压力检测系统及检测方法。
背景技术
利用水力学原理进行固体物料的长距离管道输送时， 因输送距离 少则几十公里， 多则近千公里， 因此在管线途中根据地形变化需增加 多个压力检测站以监视流体在管道中的运行状态， 在实际管道输送时 , 因为输送浓度、 流速等工艺参数均会发生一定的变化， 此时流体的流 变特性也会随之发生变化， 因此整条管线中流体的沿程阻力随之发生 变化， 各压力监测站的参数也随之发生变化。 那么， 如何检测管道中 流体的参数进而根据检测到的参数调整各压力站的参数是长距离管道 输送中需要解决的问题。 发明内容
为了解决浆体在不同浓度、 不同流速下的沿程阻力的精确计算， 本发明公开了一种长距离浆体管道输送压力检测系统及检测方法， 具 体技术方案如下。
一种长距离桨体管道输送压力检测系统， 包括检测环管、 微差压 变送器及水银 U形管差压计， 检测环管与主管完全相同， 与主管并联 设置， 微差压变送器及水银 U形管差压计安装在检测环管两端， 在主 管中安装有主管阀， 在检测环管入口端安装有环管入口阀， 在出口端 安装有环管出口阀。 微差压变送器将现场检测的环管两端的压差转换为可编程逻辑控 制器可识别的模拟信号， 传送给可编程逻辑控制器， 然后再传送到管 道运行专家系统， 管道运行专家系统结合检测环管的实际长度计算在 当前流速和浓度下的单位长度的沿程阻力。
检测环管的长度约为 200米。
一种长距离浆体管道输送浆体压力检测的方法， 包括如下步骤： 在进行浆体输送时， 关闭主管阀门、 开启环管入口阀和环管出口 阀， 使得浆体进入主泵前先流经检测环管；
微差压变送器检测环管两端的压差， 将检测的差压值信号送入可 编程逻辑控制器；
管道运行专家系统从可编程逻辑控制器中取得浆体差压值， 结合 检测环管的实际长度计算在当前流速和浓度下的单位长度的沿程阻 力。
根据主管道沿途各压力检测点的长度和海拔高程， 计算出各个检 测点的理论压力值， 与实际检测值比较， 判断浆体在管道内的流体运 动状况。
在微差压变送器检测环管两端压差前， 先用水银 U形管差压计对 微差压变送器的准确度进行校准。
采用本发明所公开的系统进行检测， 解决了两相流在紊流状态时 理论计算值与实际值误差很大的问题， 保障了长距离浆体管道安全、 稳定、 高效地运行。 附图说明
图 1 : 本发明长距离浆体管道输送压力检测系统示意图。
附图标记说明：
1-主管； 2 -检测环管； 3 -水银 U形管差压计；
4 -微差压变送器； 5 -环管入口阀； 6 -环管出口阀； 7 -主管阀； 8 -喂料泵； 9 -主泵入口。 具体实施方式
下面结合附图对本发明进行具体描述。
如图 1所示， 在起点泵站主泵入口 9前， 即喂料泵 8与主泵入口 9 之间， 与主管 1并联设置一条与主管 1完全相同的检测环管 2 , 长度约 为 200米， 在环管两端安装微差压变送器 4及水银 U形管差压计 3。
在进行浆体输送时， 关闭主管阀门 7、 开启环管入口阀 5和环管出 口阀 6, 使得浆体进入主泵前先流经检测环管 2， 则检测环管 2内浆体 浓度与流速都与主管 1中的浆体浓度与流速相同， 先用水银 U形管差 压计 3对微差压变送器 4的准确度进行校准， 经校准后的微差压变送 器 4检测的差压值信号送入 PLC (可编程逻辑控制器） ， 管道运行专家 系统从 PLC中取得该值后， 结合检测环管 1的实际长度可精确计算出 在该流速和浓度下的单位长度的沿程阻力。
根据主管道沿途各压力检测点的长度和海拔高程， 就可精确计算 出各个检测点的压力值， 与实际检测值比较， 就可判断出浆体在管道 内的流体运动状况， 提醒、 指导操作人员及时进行相应的操作。

Claims

权 利 要 求 书
1、 一种长距离浆体管道输送压力检测系统， 其特征在于： 包括检 测环管（2)、 微差压变送器（4)及水银 U形管差压计（3)， 检测环管（2) 与主管（1)完全相同， 与主管（1)并联设置， 微差压变送器（4)及水银 U 形管差压计（3)安装在检测环管（2)两端， 在主管（1)中安装有主管阀 (7)， 在检测环管（2)入口端安装有环管入口阀（5) , 在出口端安装有环 管出口阀（6) 。
2、 根据权利要求 1所述的长距离浆体管道输送压力检测系统， 其 特征在于： 微差压变送器（4)将现场检测的环管 （2 ) 两端的压差转换 为可编程逻辑控制器可识别的模拟信号， 传送给可编程逻辑控制器， 然后再传送到管道运行专家系统， 管道运行专家系统结合检测环管（2) 的实际长度计算在当前流速和浓度下的单位长度的沿程阻力。
3、根据权利要求 1或 2所述的长距离浆体管道输送压力检测系统， 其特征在于： 检测环管（2)的长度约为 200米。
4、 采用权利要求 1所述的长距离浆体管道输送压力检测系统进行 浆体压力检测的方法， 其特征在于包括如下步骤：
在进行桨体输送时， 关闭主管阀门（7)、 开启环管入口阀（5)和环 管出口阀（6)， 使得浆体进入主泵前先流经检测环管（2)；
微差压变送器（4)检测环管两端的压差， 将检测的差压值信号送入 可编程逻辑控制器；
管道运行专家系统从可编程逻辑控制器中取得浆体差压值， 结合 检测环管（2)的实际长度计算在当前流速和浓度下的单位长度的沿程 阻力。
5、 根据权利要求 4所述的方法， 其特征在于： 根据主管道沿途各 压力检测点的长度和海拔高程， 计算出各个检测点的理论压力值， 与 实际检测值比较， 判断浆体在管道内的流体运动状况。
6、 根据权利要求 4或 5所述的方法， 其特征在于： 在微差压变送 器（4)检测环管两端压差前， 先用水银 U形管差压计（3)对微差压变送 器（4)的准确度进行校准。
PCT/CN2010/000092 2009-03-26 2010-01-21 一种长距离浆体管道输送压力检测系统及检测方法 WO2010108380A1 (zh)

Priority Applications (2)

Application Number Priority Date Filing Date Title
BRPI1009374A BRPI1009374B1 (pt) 2009-03-26 2010-01-21 sistema de detecção de pressão de distribuição para uma tubulação de lama de longa distância e método para a realização de detecção de pressão de lama usando o mesmo
AU2010228003A AU2010228003B2 (en) 2009-03-26 2010-01-21 Delivery pressure detection system for long distance slurry pipeline and detection method thereof

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CN2009101197425A CN101532897B (zh) 2009-03-26 2009-03-26 一种长距离浆体管道输送压力检测系统及检测方法
CN200910119742.5 2009-03-26

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CN106555606A (zh) * 2016-11-30 2017-04-05 长沙矿山研究院有限责任公司 一种充填管道内冲洗水自动外排装置及方法

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CN101532897B (zh) * 2009-03-26 2010-11-24 云南大红山管道有限公司 一种长距离浆体管道输送压力检测系统及检测方法
WO2011153659A1 (zh) * 2010-06-09 2011-12-15 云南大红山管道有限公司 一种长距离浆体管道输送压力检测系统
CN102507078B (zh) * 2011-11-14 2014-06-18 北京宇航系统工程研究所 一种输送管流阻精确测量系统及测量方法
CN103808449A (zh) * 2012-11-13 2014-05-21 北京华德创业环保设备有限公司 一种测量压力发生系统微差压保护微差压取样测量仪的机构
CN104315343A (zh) * 2014-10-13 2015-01-28 云南大红山管道有限公司 一种控制加速流的浆体管道输送系统及加速流控制方法
CN106482890B (zh) * 2015-08-27 2018-12-14 北京环鼎科技有限责任公司 一种间接测量仪器在流体中所受推力的试验方法
CN109556993B (zh) * 2018-11-30 2023-08-18 中煤科工集团武汉设计研究院有限公司 长距离浆体管道安全检测环路系统
CN215004083U (zh) * 2021-04-24 2021-12-03 中国测试技术研究院流量研究所 差压变送器静压特性测试装置

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AU2010228003A1 (en) 2011-10-27
BRPI1009374B1 (pt) 2019-08-13
BRPI1009374A2 (pt) 2016-03-15
CN101532897A (zh) 2009-09-16
CN101532897B (zh) 2010-11-24
AU2010228003B2 (en) 2012-10-18

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