CN209470741U - Wet gas meter based on resonance and differential pressure measurement - Google Patents
Wet gas meter based on resonance and differential pressure measurement Download PDFInfo
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Abstract
The utility model relates to a kind of wet gas meter based on resonance and differential pressure measurement, including sequentially connected input pipeline section, vibration measurement pipe and output pipeline section, pressure tappings are provided on the input pipeline section and on output pipeline section, the pressure tappings are all connected to differential pressure pickup, the input pipeline section and/or the pressure tappings exported on pipeline section are also connected with pressure sensor, it is provided with energy converter, the vibration measurement pipe and/or vibration measurement pipe on the vibration measurement pipe and/or output pipeline section is equipped with temperature sensor.The utility model is based on resonance density measure and differential flow measures and passes through corresponding calculate and completes wet gas measurement, and real needs are more suitable for from performance cost.
Description
Technical field
The utility model relates to the technical field of wet gas meter, more particularly, to a kind of based on resonance and differential pressure measurement
Wet gas meter.
Background technique
Moisture is a kind of special gas liquid two-phase flow form, is widely present in oil-gas mining, oil-refining chemical, energy source and power
Etc. many industries.Moist steam and wet gas are two kinds of Typical Representatives of moisture, and moist steam is often accompanied by phase transformation, and diabatic process is to it
There is significant impact；Wet gas is then almost without phase transformation, and the variation of temperature is only limitted to the influence to Media density, in the world
Liang Jia research institution: NEL(United Kingdom National engineering experiment room is concentrated mainly on to the technical research of moisture metering) and CEESI(beauty
State, engineering experiment room, Colorado), they are owned by the wet gas meter calibration system of oneself, and NEL gas phase uses nitrogen, liquid phase
Using kerosene, CEESI gas phase then uses the natural gas of standard, and liquid phase uses water, phase transformation is not present in cold test.
China's oil Gas Industry generally by moisture be defined as under running conditions gaseous phase volume containing rate be greater than 90%, liquid
The mutually gas well output object with other volume components containing rate less than 10%.Wherein, liquid phase component is mainly by carry secretly, bottom surface production system
It unites alkanes component, saturated water and the note to prevent gas hydrate synthesis to be manually added that temperature, pressure reduction and condensation generate
Agent etc., it is clear that well head metering room in oil field, terminal, associated gas involved in multi-purpose station belong to the scope of moisture.
Moisture metering method can be divided into two classes: first is that measuring moisture using traditional single phase gas flowmeter.Due to gas
In contain a small amount of liquid, most gas flowmeter indicating values by generate measure virtual height phenomenon, need founding mathematical models carry out humidity
Amendment, and which has had accumulated some experiences in developed country, in the type selecting of flowmeter, test, standard, use, maintenance
And a large amount of experience accumulated in terms of the applicability of various operating conditions, wherein the reference using differential pressure flowmeter metering moisture is studied
Comparative maturity；Second is that using Modern New Technology wet gas meter measure moisture, including microwave, ultrasound, cross-correlation, tracer,
The technologies such as process tomographic imaging, it is most of at present to research and develop the improvement stage all in field test or laboratory due to starting late.
So existing conventional wet gas measurement mode is measured using differential pressure flowmeter, although existing differential pressure flowmeter measures moisture
More mathematical model is had been set up in the process, but these models have more stringent suitable environment, change to operating condition
Adaptability it is not strong.
Utility model content
The purpose of the utility model is to provide a kind of wet gas meter based on resonance and differential pressure measurement, can be based on resonance
Density measure and differential flow, which measure and pass through corresponding calculate, completes wet gas measurement.
The above-mentioned technical purpose of the utility model has the technical scheme that
A kind of wet gas meter based on resonance and differential pressure measurement, including sequentially connected input pipeline section, vibration measurement pipe
And pipeline section is exported, pressure tappings are provided on the input pipeline section and on output pipeline section, the pressure tappings are all connected to press
Gap sensor, the input pipeline section and/or the pressure tappings exported on pipeline section are also connected with pressure sensor, the vibration measurement pipe
On be provided with energy converter, the vibration measurement pipe and/or input pipeline section and/or output pipeline section are equipped with temperature sensor.
By using above-mentioned technical proposal, according to the differential pressure pickup being connected on input pipeline section and on output pipeline section with
Differential pressure flow measurement is formed, while being completed by vibration measurement pipe and energy converter to resonance density measure, that is, realizing will be humorous
Vibration tube formula densitometer and differential pressure flowmeter organically combine；Corresponding data detected by all related sensors is fed back into stream
Measure computer, result needed for COMPREHENSIVE CALCULATING obtains；Wherein, all media pass through vibration measurement pipe, guarantee that two-phase mixtures are situated between
Matter can be all measured, and avoid the problem typical of sampling type measurement；The position for measuring hybrid density is exactly flow measurement
Position, avoid not at one measurement due to pressure change bring air tightness inaccuracy, so as to cause phase fraction inaccuracy；
Existing mode is that multiple measuring devices are together in series, i.e., has concatenated two unit vibration measurement pipes with differential pressure flowmeter
Come, this just brings a problem, and the hybrid density of survey, the mixing that can not be represented at differential pressure flowmeter are close at vibration measurement pipe
Degree, because an inherent feature of differential pressure flowmeter is exactly pressure change, pressure change can bring the variation of air tightness, throttling
The hybrid density at place and the hybrid density at other positions are also different, although can be represented reluctantly by amendment or compensation,
But its correction-compensation is an amount by effect of multiple parameters, complicated and inaccurate, the brought inaccuracy to hybrid density, both
Total flow measurement is influenced, phase fraction measurement is also influenced；By the way that vibration measurement pipe and differential pressure flowmeter are integrated in the same equipment
In the problem of being detected, corresponding accuracy can be greatly improved.
The utility model is further arranged to: on the input pipeline section and being carried out undergauge with the junction of vibration measurement pipe and is set
It sets.
The utility model is further arranged to: being provided on the input pipeline section and at undergauge along media flow side
Outer first inclined surface tilted towards pipe Xiang Youguan.
The utility model is further arranged to: carrying out expanding set on the output pipeline section and with the junction of vibration measurement pipe
It sets.
The utility model is further arranged to: being provided on the output pipeline section and positioned at expanding place along media flow side
Towards the second inclined surface of pipe outer incline in Xiang Youguan.
By using above-mentioned technical proposal, inputs the setting of the undergauge of pipeline section and export the expanding setting of pipeline section, formed
Throttle part realizes the function that throttling accelerates, and combines differential pressure pick-up, constitutes throttling differential pressure flowmeter；Undergauge and expansion
The setting of diameter is to allow vibration measurement pipe that can combine resonance principle and survey density and throttling differential pressure principle measurement of discharge two
Function；In addition, undergauge is formed by the first inclined surface and expanding second inclined surface that is formed by can allow the pipe of throttling as far as possible
Section, which is reduced, generates interference vortex.
The utility model is further arranged to: the caliber of the input pipeline section and the caliber of output pipeline section are all larger than vibration and survey
The caliber of buret.
By using above-mentioned technical proposal, the medium for being input to input pipeline section is enabled to have a biggish influx,
And during entering vibration measurement pipe, undergauge position can be passed through, therefore convenient for forming the function that throttling accelerates, so that into
Medium to vibration measurement pipe has certain flow velocity, is convenient for subsequent measurement；Pass through expanding position, enters efferent duct
Section, and flow velocity can be reduced.
The utility model is further arranged to: the input pipeline section and wall of the wall thickness greater than vibration measurement pipe for exporting pipeline section
It is thick.
By using above-mentioned technical proposal, since vibration measurement pipe needs to form starting of oscillation by driving, thus complete to detect,
Therefore the wall thickness of vibration measurement pipe is less than input pipeline section and exports the wall thickness of pipeline section；Meanwhile it also can effectively avoid inputting
Pipeline section and output pipeline section also occur starting of oscillation and generate interference.
The utility model is further arranged to: it is described input pipeline section on pressure tappings be located at input pipeline section on carry out undergauge it
Preceding pipeline section part.
The utility model is further arranged to: it is described output pipeline section on pressure tappings be located at output pipeline section on carry out it is expanding it
Pipeline section part afterwards.
By using above-mentioned technical proposal, the setting of pressure tappings is to measure the pressure between input pipeline section and output channel
Difference, if being arranged after undergauge or before expanding, due to undergauge and the expanding effect that will form throttling and accelerate, so can not be quasi-
The true pressure difference got between input pipeline section and output channel, that is, will affect measurement accuracy.
The utility model is further arranged to: the differential pressure pickup passes through default pressure tube with pressure tappings and connects
It connects.
By using above-mentioned technical proposal, the pressure for inputting required detection on pipeline section and output pipeline section is passed through into pressure transmission
Pipe is transmitted to differential pressure pickup, to form input pipeline section and export the pressure differential detection between pipeline section.
The utility model is further arranged to: the energy converter is located at the medium position of vibration measurement pipe.
By using above-mentioned technical proposal, the medium position of vibration measurement pipe can avoid input pipeline section and output as far as possible
Pipeline section and the influence generated, i.e., in vibration measurement pipe in self-oscillating, it is micro- that input pipeline section and output pipeline section are also affected generation
Weak starting of oscillation and the detection for influencing energy converter.
In conclusion the advantageous effects of the utility model are as follows:
1. measure and pass through corresponding calculating completion wet gas measurement based on resonance density measure and differential flow, from performance at
It is more suitable for real needs on this.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the wet gas meter based on resonance and differential pressure measurement.
In figure: 1, inputting pipeline section；2, vibration measurement pipe；3, pipeline section is exported；4 first inclined surface；5, the second inclined surface；6, it takes
Press mouth；7, differential pressure pickup；8, pressure sensor；9, pressure tube；10, energy converter；11, temperature sensor.
Specific embodiment
The utility model is described in further detail below in conjunction with attached drawing.
It referring to Fig.1, is a kind of wet gas meter based on resonance and differential pressure measurement disclosed by the utility model, gas-liquid two-phase
Medium flows in the apparatus, and carries out detecting relevant parameter to gas-liquid two-phase medium, and one is total flow, secondly for phase point
Rate (void fraction+liquid holdup=1)；I.e. by obtaining the two parameters and can be calculated accurate wet gas measurement by relevant
Data.
The structure of wet gas meter in the application specifically include sequentially connected input pipeline section 1, vibration measurement pipe 2 and
Pipeline section 3 is exported, the connection of three pipeline sections can be integrated connection, can realize by the existing fixed form such as flange-interface
It is fixedly connected, while can add corresponding sealing ring etc. also to avoid leakage.
Wherein, density and throttling differential pressure principle measurement of discharge are surveyed in order to allow vibration measurement pipe 2 that can combine resonance principle
Two functions, therefore the caliber for the caliber and output pipeline section 3 for inputting pipeline section 1 is all larger than the caliber of vibration measurement pipe 2, in input pipeline section
Undergauge setting is carried out on 1 and with the junction of vibration measurement pipe 2, the mode of undergauge on input pipeline section 1 and is located at undergauge
It is provided with and the first tilted inclined surface 4 is managed by direction outside pipe along flow direction of medium；Export pipeline section 3 on and and vibration measurement
The junction of pipe 2 carries out expanding setting；Expanding mode is provided on output pipeline section 3 and positioned at expanding place along medium flow field
Dynamic direction by pipe towards the second inclined surface 5 of pipe outer incline.Undergauge is configured so that input pipeline section 1, vibration measurement with expanding
Pipe 2 and output pipeline section 3 form throttle part, realize the function that throttling accelerates, and undergauge is formed by the first inclined surface 4 and expands
Diameter is formed by the second inclined surface 5 can allow the pipeline section of throttling to reduce generation interference vortex as far as possible.
Wherein, input pipeline section 1 and export pipeline section 3 wall thickness be greater than vibration measurement pipe 2 wall thickness, and input pipeline section 1 with it is defeated
The wall thickness of pipeline section 3 is thicker out, and the wall thickness of vibration measurement pipe 2 is relatively thin and has certain elasticity, can be convenient for vibration measurement
Pipe 2 forms starting of oscillation, input pipeline section 1 and output pipeline section 3 since thicker wall thickness makes that starting of oscillation will not be formed by driving by driving.
Meanwhile inputting on pipeline section 1 and being located at undergauge and export on pipeline section 3 and be located at expanding place and being also disposed as thicker wall thickness,
It can avoid interfering as far as possible.
Pressure tappings 6 are provided on input pipeline section 1 and on output pipeline section 3, pressure tappings 6 are all connected to differential pressure pickup 7,
Differential pressure pickup 7 is connect by default pressure tube 9 with pressure tappings 6；Pressure tappings 6 on input pipeline section 1 are located at input pipe
The pipeline section part before undergauge is carried out in section 1；Output pipeline section 3 on pressure tappings 6 be located at output pipeline section 3 on carry out it is expanding after
Pipeline section part.
Input pipeline section 1 and/or the pressure tappings 6 exported on pipeline section 3 are also connected with pressure sensor 8, exhausted for measuring pipeline section
To pressure；Wherein, the pressure tappings 6 for connecting pressure sensor 8 can be the pressure tappings 6 of connection differential pressure pickup 7, be also possible to
Input pipeline section 1 and/or the pressure tappings 6 newly opened on pipeline section 3 are exported, preferably using in input pipeline section 1 and/or defeated in the present embodiment
The pressure tappings 6 newly opened on pipeline section 3 out；And in measurement process, the absolute pressure on input pipeline section 1 can be measured, it can also be with
Absolute pressure on measurement output pipeline section 3 can also be while measure input pipeline section 1 and exports the absolute pressure on pipeline section 3,
Preferably using the absolute pressure on measurement input pipeline section 1 in the present embodiment, therefore a pressure tappings 6 are newly opened on input pipeline section 1,
And pressure sensor 8 is connected to complete the detection of absolute pressure.
Energy converter 10 is provided on vibration measurement pipe 2, which is electromechanical energy energy converter 10, can be electricity
Magnetic coil, piezoelectrics etc., for motivating and receiving vibration.In one embodiment, energy converter 10 includes but is not limited to electromagnetism
Coil, which is mounted on corresponding fixed pedestal, is passed through electric current to it, so that electromagnetic coil generates magnetic field, with
The preset permanent magnetism being fixed on vibration measurement pipe 2 or soft magnetic part interaction, to drive vibration measurement pipe 2, completion electromechanical
The transducing process of energy；It is then that permanent magnetism is fixed in vibrating tube in receiving end, electromagnetic coil is fixed on fixed pedestal, vibrating tube
Permanent magnetism movement is driven after generating vibration, the magnetic field of permanent magnetism and electromagnetic coil have a relative motion at this time, electromagnetic coil cutting magnetic line,
Electric signal relevant to vibration signal is generated, the transducing of mechanical-electricity is completed.In one embodiment, piezoelectric transducer 10, benefit
The characteristics of with piezoelectric material, when being subject to voltage to it, the geometric dimension of material changes, it can completes electromechanical energy
Ring energy, and press to it, deformation is generated, then can generate corresponding electric signal, completes the transducing of mechanical-electricity.Energy converter 10
It should be a pair of, one is used to drive vibration measurement pipe 2, another receives the vibration of vibration measurement pipe 2.Working method are as follows: receive
Obtained signal is held, electronically circuit is amplified, and with the energy converter 10 of the same-phase driving other end, that is, can produce resonance.
Energy converter 10 is located at the medium position of vibration measurement pipe 2；I.e. in vibration measurement pipe 2 in self-oscillating, input pipe
Section 1 is also affected the detection for generating faint starting of oscillation and influencing energy converter 10 with output pipeline section 3, and in vibration measurement pipe 2
Portion position can avoid input pipeline section 1 as far as possible and export pipeline section 3 and the influence of generation.
Vibration measurement pipe 2 and/or input pipeline section 1 and/or output pipeline section 3 are equipped with temperature sensor 11, are situated between for measuring
Matter temperature.It is preferably used in the present embodiment and corresponding temperature sensor 11 is set on vibration measurement pipe 2.Temperature sensor 11 is adopted
With the device of miniature quality very little, model includes but is not limited to the thermistors such as PT100, PT1000, is attached to vibration measurement pipe
2 tube walls pick out signal by filament, and there are surpluses so that by flutter failure, temperature sensor 11 must not have, and be used for for filament
Calculate the call parameter of air tightness.
The implementation principle of the present embodiment are as follows:
Gas-liquid two-phase medium sequentially enters input pipeline section 1, vibration measurement pipe 2 and output pipeline section 3, inputs according to being connected to
On pipeline section 1 and output pipeline section 3 on differential pressure pickup 7 with formed differential pressure flow measurement, while by vibration measurement pipe 2 with
And energy converter 10 is completed to examine relevant parameter by temperature sensor 11 and pressure sensor 8 resonance density measure
It surveys；Corresponding data detected by all related sensors is fed back into flow computer, result needed for COMPREHENSIVE CALCULATING obtains.
For two phase flow total flow calculation formula are as follows:
In formula: qv is volume flow；C is efflux coefficient；For expansibility factor；For diameter ratio,, d
For throttling element opening diameter, D is internal diameter of the pipeline；For detected fluid density；For pressure difference.
By formula it is found that after the actual size of wet gas meter has been determined, the relevant parameter of flow formula is had determined that.
Inflatable coefficient is related to medium, and for biphase gas and liquid flow, the gas-liquid ingredient of medium is variation, may expand coefficient
Objectively and variation, can be obtained by the calculation of medium, due to liquid phase it is considered that incompressible, the coefficient of expansion is
1, it may expand coefficient=gas phase coefficient of expansion * (1- liquid holdup)+liquid holdup；The coefficient of expansion of gas phase is that the physics of gaseous substance is special
Property.And the total coefficient of expansion of two phase flow is simple algebraic operation, it is related to liquid holdup.
For gas-liquid two-phase medium, pass through density measure, so that it may determine the component of each phase of gas-liquid.After simplified, flow
It is required in formula to obtain two parameter difference hybrid densities and differential pressure；Wherein, hybrid density and differential pressure can pass through the application
Wet gas meter obtain.The total flow of moisture can measure as a result,；The respective flow of gas phase and liquid phase is by terms of the mode of lower section
It calculates: total liquid measure=total flow * liquid holdup；Total tolerance=total flow * (1- liquid holdup).
Based on measurement hybrid density and air tightness, which is associated with temperature, pressure, and mixes for liquid holdup measurement
The result of density both influences phase fraction measurement, also influences the measurement of total flow, hybrid density is utilized in relevant formula, flow
The hybrid density for measuring part is detected fluid density, the calculation about phase fraction part is as follows:
Firstly, it is necessary to obtain air tightness, by the equation of gas state: PV=ε nRT it is found that the density p and pressure P of gas at just
Than being inversely proportional with temperature T, in the density by one state point (pressure, temperature) of calibration, so that it may by measuring other situations
The gas density of (pressure of different conditions, density) is i.e.:
It can be seen that the measurement of pressure and temperature is to must have, it is the critical quantity for obtaining air tightness.Obtain first
Density under calibration state, then calculated by temperature value, pressure value and obtain gas density, humorous by measurement vibrating tube 2
The hybrid density of vibration frequency acquisition gas-liquid two-phase medium, by simple algebraic operation, phase fraction can be obtained, here such as
Fruit indicates that liquid is incompressible with volume liquid holdup η, and fluid density is, then have:
=(1- η) *+η*
It can be obtained after simplification:
When we are calculated using the volume flow formula in flow formula, under operating condition,
Total amount of liquid=qv* η
Total gas flow=qv* (1- η)
Thus two phase flow, which calculates, completes.
The embodiment of present embodiment is the preferred embodiment of the utility model, and not limitation is originally practical new according to this
The protection scope of type, therefore: the equivalence changes that all structures, shape, principle according to the utility model are done should all be covered by practical
Within novel protection scope.
Claims (10)
1. a kind of wet gas meter based on resonance and differential pressure measurement, it is characterized in that: include sequentially connected input pipeline section (1),
Vibration measurement pipe (2) and output pipeline section (3) on the input pipeline section (1) and export and are provided with pressure tappings on pipeline section (3)
(6), the pressure tappings (6) are all connected to differential pressure pickup (7), taking on input pipeline section (1) and/or output pipeline section (3)
Pressure mouth (6) is also connected with pressure sensor (8), is provided with energy converter (10), the vibration measurement on the vibration measurement pipe (2)
It manages (2) and/or input pipeline section (1) and/or output pipeline section (3) is equipped with temperature sensor (11).
2. the wet gas meter according to claim 1 based on resonance and differential pressure measurement, it is characterized in that: the input pipeline section
(1) undergauge setting is carried out on and with the junction of vibration measurement pipe (2).
3. the wet gas meter according to claim 2 based on resonance and differential pressure measurement, it is characterized in that: the input pipeline section
(1) it is provided on and at undergauge and tilted the first inclined surface (4) is managed by direction outside pipe along flow direction of medium.
4. the wet gas meter according to claim 1 based on resonance and differential pressure measurement, it is characterized in that: the output pipeline section
(3) expanding setting is carried out on and with the junction of vibration measurement pipe (2).
5. the wet gas meter according to claim 4 based on resonance and differential pressure measurement, it is characterized in that: the output pipeline section
(3) on and be located at expanding place be provided with along flow direction of medium by pipe towards the second inclined surface (5) of pipe outer incline.
6. the wet gas meter described according to claim 1 or 2 or 3 or 4 or 5 based on resonance and differential pressure measurement, it is characterized in that:
The caliber of input pipeline section (1) and the caliber of output pipeline section (3) are all larger than the caliber of vibration measurement pipe (2).
7. the wet gas meter described according to claim 1 or 2 or 3 or 4 or 5 based on resonance and differential pressure measurement, it is characterized in that:
Input pipeline section (1) and the wall thickness for exporting pipeline section (3) are greater than the wall thickness of vibration measurement pipe (2).
8. the wet gas meter described according to claim 1 or 2 or 3 or 4 or 5 based on resonance and differential pressure measurement, it is characterized in that:
Pressure tappings (6) on input pipeline section (1) are located at the pipeline section part carried out before undergauge in input pipeline section (1).
9. the wet gas meter described according to claim 1 or 2 or 3 or 4 or 5 based on resonance and differential pressure measurement, it is characterized in that:
It is described output pipeline section (3) on pressure tappings (6) be located at output pipeline section (3) on carry out it is expanding after pipeline section part.
10. the wet gas meter described according to claim 1 or 2 or 3 or 4 or 5 based on resonance and differential pressure measurement, feature
Be: the differential pressure pickup (7) is connect by default pressure tube (9) with pressure tappings (6).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201920492797.XU CN209470741U (en) | 2019-04-11 | 2019-04-11 | Wet gas meter based on resonance and differential pressure measurement |
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| CN201920492797.XU CN209470741U (en) | 2019-04-11 | 2019-04-11 | Wet gas meter based on resonance and differential pressure measurement |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109974800A (en) * | 2019-04-11 | 2019-07-05 | 无锡洋湃科技有限公司 | Wet gas meter based on resonance and differential pressure measurement |
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2019
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109974800A (en) * | 2019-04-11 | 2019-07-05 | 无锡洋湃科技有限公司 | Wet gas meter based on resonance and differential pressure measurement |
| WO2020206733A1 (en) * | 2019-04-11 | 2020-10-15 | 无锡洋湃科技有限公司 | Wet gas flow meter based on resonance and differential pressure measurement |
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