CN1139787C - Combined sensor assembly for measuring several parameters of gas and liquid fluid inside pipe - Google Patents

Combined sensor assembly for measuring several parameters of gas and liquid fluid inside pipe Download PDF

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Publication number
CN1139787C
CN1139787C CNB00111249XA CN00111249A CN1139787C CN 1139787 C CN1139787 C CN 1139787C CN B00111249X A CNB00111249X A CN B00111249XA CN 00111249 A CN00111249 A CN 00111249A CN 1139787 C CN1139787 C CN 1139787C
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initiator
low pressure
fluid
sensor
lumen pore
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CNB00111249XA
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CN1336536A (en
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邹德蕴
崔建明
谭允祯
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Resource & Environment Engineering College Shandong Science & Technology Univ
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Resource & Environment Engineering College Shandong Science & Technology Univ
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Abstract

The present invention relates to a gas and liquid fluid parameter signal initiator for a pipeline and a sensor package thereof, which is characterized in that an initiator has an upper cavity hole and a lower cavity hole which are arranged in a rhombic cylinder, the initiator communicates with a plurality of signal acquisition holes on an acute angle smooth surface; a sensor package on the casing is provided with three cavities and a high and low pressure sensing nozzle, a temperature sensor, a differential pressure sensor and an absolute static pressure sensor; the initiator is inserted into a fluid pipeline after tight connection to output a fluid physical signal to a measuring instrument.

Description

Combined pipeline gas, liquid fluid multiparameter integrated transducer assembly
The invention belongs to the fluid parameter monitoring device.
All adopt the distributing instrument measurement for the measurement of important parameters such as the parameter of gas, liquid fluid in the pipeline such as flow Q, pressure P, temperature T for many years, because condition restriction, measurement point even also disperse.The monitoring of fluid parameter (Q, P, T) is three important parameters of pipeline fluid monitoring, in engineering, all has relatively independent important practical usage separately, influential mutually again, especially absolute static pressure P, the temperature T of prolonging flow process when fluid is random variation; The constancy of the density p value of fluid is stressed again, temperature effect is significant, promptly ρ=f (P, T), thereby then need by measure absolute static pressure P, temperature T carry out density conversion when realizing the compensation correction of flow measurement precision ( Q v = C ΔP × T / P m 3/ s, Q v---fluid volume flow, C---comprehensive constant value), just bring difficulty and trouble to measurement.For this reason, in many cases, just abandoned density measuring and calculating link, given up flow measurement accuracy correction process, as the gas flow monitoring of mine gas drainage pipe network system.The orifice flowmeter that always adopts the different process form for many years is the classical measuring instrument of the throttle type of representative.The disadvantage of using this quasi-instrument is the energy loss that increases the system dynamic source, is not easy to installing/dismounting on the pipeline of operation, and the long-time running expense is big, and measuring accuracy is poor, can't realize online dynamic automatic monitoring and control.Occur vortex street principle, ultrasonic principle and pressure measurement in recent years and asked the flow instrumentation of fast principle etc., the instrument of these principles has solved the problem of automatic monitoring, but the specific aim of instrument development is too strong, exist the limited many fatal shortcoming of service condition (as fluid media (medium) density correction etc.), general and poor stability.
The objective of the invention is to design a kind of installing/dismounting that is easy to, the power source loss is few, and the measuring accuracy height can be realized the integrated apparatus of on-line automaticization of multiparameter dynamic monitoring.
Main-body structure of the present invention comprises signal initiator and sensor module.The structure of signal initiator is that xsect is the column of prismatic, and the corner angle of this cylinder are handled through slyness, is processed with the lumen pore of two same specifications in this column on the axial direction, and one of them lumen pore is the fluid high-pressure lumen pore, and another is the low pressure lumen pore.The diameter of phi in hole 1Mm is more suitable in=(5~8).4~6 signals collecting holes of vertical brill on two rhombus acute angle round slip surfaces, and be communicated with the high and low pressure lumen pore respectively.The diameter of phi in signals collecting hole 2=(0.4~0.6) Φ 1, the signals collecting hole number is relevant with the fluid line internal diameter, and concrete quantity is calculated by Chebyshev's formula and is calculated (or homalographic circule method).The structure of combined type trans assembly is that three cavitys and the high and low pressure sensing hole that are processed with perforation in a housing are chewed.The high voltage induction hole is equipped with temperature sensor in chewing, and draws signal wire from the left side accent; Middle chamber is installed differential pressure pick-up, and draws signal wire from this accent; The right side cavity is installed absolute static pressure sensor, and draws signal wire from this accent.The high pressure lumen pore of signal initiator and low pressure lumen pore are tightly connected with high and low high and low pressure sensing hole mouth of combined type trans assembly respectively and are in the same place during assembling.When measuring fluid parameter, the signal wire (or signal plug) of sensor is inserted the digital signal receiving processing circuit of being made up of A/D processor, cpu data disposal system, data display circuit and communication interface etc.; The fluid parameter signal initiator is inserted in the fluid line by the fluid pipeline wall opening, and fix and seals, during insertion with on high-tension side signals collecting hole aligning fluid flow direction.Gather three sensors, sensor output signal that the fluid physics parameter signal gathered in the hole passes to the combined type trans assembly through high pressure lumen pore and low pressure lumen pore from signal initiator and receive to digital signal and handle electrical equipment, after testing with data processing, demonstrate flow, pressure, temperature value.
Advantage of the present invention is: be fluid physics amount signal initiator owing to having adopted the rhombus cylinder of slick and sly processing corner angle 1,, in gathering naturally, two obtuse angles of initiator play the effect of a fixedly separated point of symmetry (along on the caliber cross-wise direction) to the fluid flow line of flowing through, and have guaranteed that there is not the boundary layer fluid layer in initiator surface (after the fixedly separated point) and is in the border disturbed flow condition all the time; The coefficient of shock resistance of the interference in initiator convection cell flow field and generation was not only stable but also can ignore like this, neglected to the power source loss of pipe network system is also little that it is little; Coefficient of flow is stable, and irrelevant with the pipeline Reynolds number; 2, the initiator simple installation is easily gone, and is particularly suitable for the absolute static pressure of pipeline inner fluid less than the pipeline with absolute altitude place barometric absolute pressure, promptly extracts the pipe network system of exhaust fluid mode out, as the mine gas drainage system; 3, be convenient to realize robotization dynamic monitoring and control by digital signal processing circuit.4, measuring accuracy height when especially causing that when hydrodynamic pressure, temperature random variation fluid density is non-stable constant value, needs to measure absolute static pressure of the fluid power P and temperature T compensates correction, reaches the more measurement purpose of high-precision requirement.
The accompanying drawings embodiments of the invention.
Embodiment such as Fig. 1, Fig. 2, Fig. 3, the embodiment of the invention shown in Figure 4 belong to the measuring instrument that has than high automation and intelligent degree, are the devices that is used for demonstration of combined fluid multiparameter on-line monitoring and remote data communication.Fig. 1 is the structure and the use-pattern key diagram of combined fluid multi-parameter monitoring devices; Fig. 2 is the main pseudosection of compound temperature, pressure flow sensor assembly; Fig. 3 is the main pseudosection of rhombus fluid physics amount signal initiator; Fig. 4 is that the K of Fig. 3 is to figure.Marginal data: 1-display; The 2-I/O communication interface; 3-combined type trans assembly; The 4-seal; 5-fluid parameter signal initiator; The 6-pipeline; 7-combined type trans housing; 8-four-core sensor signal socket; The 9-differential pressure pick-up; The absolute static pressure transducer of 10-; 11-sensor low pressure sensing hole mouth; The 12-Pt100 temperature sensor; 13-sensor high voltage induction hole mouth; The 14-high-pressure chamber; 15-low pressure cavity; 16-fluid parameter signals collecting hole; The 17-plug silk hole of removing contamination; 18-initiator housing; 19-high-pressure chamber pressure P 1The tracting pressuring hole mouth.As can be seen from Figure 2: the housing (7) of combined type trans assembly (3) is upper body and the lower body that connects together with bolt, three cavitys and the high and low sensing hole mouth (11) (13) that are interconnected are arranged in the housing (7), high voltage induction hole mouth (13) is built-in with temperature sensor (12), the signal wire of sensor (12) is drawn from left cavity, and is connected on the four-core socket (8) of left cavity mouth; Middle chamber is built-in with differential pressure pick-up (9), and its signal wire is connected on the four-core socket of middle accent; Right cavity is built-in with absolute static pressure transducer (10), and its signal wire is connected on the four-core socket of right accent.Find out from Fig. 3, Fig. 4, signal initiator (5) is at two diameter 6mm through holes of brill in slyness is handled the rhombus cylinder (18) of 65 ° of acute angles of corner angle, be respectively high-pressure chamber (14) and low pressure cavity (15), via bottoms is mantle fiber respectively, silk hole, bottom (17) is the plug silk hole of removing contamination, and high pressure tracting pressuring hole mouth (19) and low pressure tracting pressuring hole mouth (20) are arranged at the top; The signals collecting hole (16) of boring four diameter 3mm on two acute angle rib round slip surfaces respectively also is communicated with the high and low pressure cavity respectively.Install and use state as shown in Figure 1.During use, two hole mouths (19), (20) of signal initiator (5) are inserted high and low pressure sensing hole mouth (11), (13) of sensor module (3) respectively, and sealed with seal (4), three four-core sockets of sensor module (3) pick out signal wire and connect communication interface (2) and display (1), are inserted in the pipeline (6) and can use behind the fixing seal.Its principle of work is: the high-pressure chamber internal pressure P of initiator 1Be transferred to the high voltage induction hole mouth (13) of differential pressure pick-up, simultaneously the temperature T of fluid imported into the temperature sensor (12) in the high voltage induction hole mouth of sensor module.The low pressure cavity internal pressure P of initiator 2Be transferred to the low pressure sensing hole mouth (11) of differential pressure pick-up, measure P by differential pressure pick-up (9) 1Subtract P 2Difference DELTA P.The while pressure P 2Act on equivalence relation in the sensing hole of absolute pressure sensor (10), measure absolute static pressure of the fluid power P by absolute pressure sensor (10).The volumetric flow rate calculating formula of this embodiment adopts the compensation correction formula.
The embodiment of the invention belongs to the measuring instrument that has than high automation and intelligent degree, is the device that is used for demonstration of combined fluid multiparameter on-line monitoring and remote data communication.

Claims (1)

1, a kind of pipeline gas, liquid fluid multiparameter integrated transducer assembly is characterized in that it comprises signal initiator and sensor module; Signal initiator is that xsect is the column of prismatic, the corner angle of this prismatic are handled through slyness, in this column, be processed with high pressure lumen pore and low pressure lumen pore in the axial direction, 4~6 signals collecting holes of vertical brill on two rhombus acute angle round slip surfaces, and be communicated with the high and low pressure lumen pore respectively; Sensor module is three cavitys and the high and low pressure sensing hole mouth that is processed with perforation in a housing, temperature sensor is installed in the mouth of high voltage induction hole and draws signal wire from the accent of left side cavity, middle chamber is installed differential pressure pick-up and is drawn signal wire from this accent, and the right side cavity is installed absolute static pressure sensor and drawn signal wire from this accent; The high pressure lumen pore of signal initiator and low pressure lumen pore are tightly connected with the high and low pressure sensing hole mouth of sensor module respectively and are in the same place then.
CNB00111249XA 2000-07-28 2000-07-28 Combined sensor assembly for measuring several parameters of gas and liquid fluid inside pipe Expired - Fee Related CN1139787C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB00111249XA CN1139787C (en) 2000-07-28 2000-07-28 Combined sensor assembly for measuring several parameters of gas and liquid fluid inside pipe

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Application Number Priority Date Filing Date Title
CNB00111249XA CN1139787C (en) 2000-07-28 2000-07-28 Combined sensor assembly for measuring several parameters of gas and liquid fluid inside pipe

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CN1336536A CN1336536A (en) 2002-02-20
CN1139787C true CN1139787C (en) 2004-02-25

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EP3446737B8 (en) 2012-04-05 2021-12-22 Fisher & Paykel Healthcare Limited Respiratory assistance apparatus
JP6522624B2 (en) * 2013-09-06 2019-05-29 イリノイ トゥール ワークス インコーポレイティド Absolute pressure differential pressure transducer
JP2017517319A (en) 2014-05-27 2017-06-29 フィッシャー アンド ペイケル ヘルスケア リミテッド Gas mixing and measurement for medical devices
GB2598024B (en) 2015-12-02 2022-05-04 Fisher & Paykel Healthcare Ltd Flow path sensing for flow therapy apparatus

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