CN1731105A - Fluid flow rate detector - Google Patents

Fluid flow rate detector Download PDF

Info

Publication number
CN1731105A
CN1731105A CN 200510044397 CN200510044397A CN1731105A CN 1731105 A CN1731105 A CN 1731105A CN 200510044397 CN200510044397 CN 200510044397 CN 200510044397 A CN200510044397 A CN 200510044397A CN 1731105 A CN1731105 A CN 1731105A
Authority
CN
China
Prior art keywords
phase fraction
flow
detector
fluid
detecting device
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
CN 200510044397
Other languages
Chinese (zh)
Other versions
CN1332183C (en
Inventor
陈宇
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CNB2005100443975A priority Critical patent/CN1332183C/en
Publication of CN1731105A publication Critical patent/CN1731105A/en
Priority to PCT/CN2006/001977 priority patent/WO2007016865A1/en
Application granted granted Critical
Publication of CN1332183C publication Critical patent/CN1332183C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • G01F1/363—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 with electrical or electro-mechanical indication
    • 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
    • G01F1/66—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 measuring frequency, phase shift or propagation time of electromagnetic or other waves, e.g. using ultrasonic flowmeters
    • 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
    • G01F1/66—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 measuring frequency, phase shift or propagation time of electromagnetic or other waves, e.g. using ultrasonic flowmeters
    • G01F1/666—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 measuring frequency, phase shift or propagation time of electromagnetic or other waves, e.g. using ultrasonic flowmeters by detecting noise and sounds generated by the flowing fluid
    • 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
    • G01F1/74—Devices for measuring flow of a fluid or flow of a fluent solid material in suspension in another fluid

Landscapes

  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • General Physics & Mathematics (AREA)
  • Electromagnetism (AREA)
  • Measuring Volume Flow (AREA)

Abstract

The invention relates to a flow measuring device of a stream, which fixes at least two dynamic pressure sensors on the measuring path of the changing cross-sectional area used to measure the undulating quantity value of restricting differential pressure which can measure the stream flow. The device overcomes the traditional shortages and can measure multiply two-phase flow. When adding a phase measuring device on the invention, it can measure two-phase flow with much accuracy and can be used to measure oil, gas and water three-phase flow.

Description

The flow detector of fluid
Technical field
The present invention relates to a kind of flow detector based on pressure detection, further say, the invention belongs to the device that carries out flow detection by the detection pressure surge value that restriction device produced, and when described fluid was various two-phase flows or three-phase stream, described device was especially suitable.
Background technology
In reality production and life, fluid is ubiquitous.Traditional throttling differential pressure flowmeter utilizes the throttling differential pressure feature that fluid flows to carry out the detection of its traffic characteristic, successfully be applied to industry and exceeded a century, its global marketing quantity is occupied the first place in all kinds of flow instrument midium or long term, reaches more than 50% of instrument total amount.
The throttling differential pressure flowmeter is based on Bernoulli equation and mobile continuity equation.Be full of the fluid of pipeline, during restriction device in it flows through pipeline, fluid will form local contraction at the throttling element place, thereby flow velocity increases, static pressure reduces, so just produced pressure reduction before and after the restriction device, this pressure reduction and flow square be approximated to direct ratio, can weigh the size of flow like this according to pressure reduction.This ultimate principle all has introduction in great majority relate to the books and periodicals of flow metering technology, for example " flow measurement technology and instrument " book (ISBN7-111-10147-2) chapter 3 second joint published of China Machine Press is the 43rd page.
But along with improving constantly of the automatization level of industrial processes, higher flow detection requires also constantly to occur, below the requirement of two aspects be exactly very urgent:
On the one hand, the throttling differential pressure flowmeter no doubt has many good qualities, but its following shortcoming is that urgent need is improved:
The one, rangeability is narrow.Because the throttling differential pressure signal and the fluid flow that detect are quadratic relationship, guarantee certain flow detection precision, rangeability is difficult to usually greater than 3: 1-4: 1.
The 2nd, throttling differential pressure impulse pipeline breaks down easily.This section pipeline is connected between restriction device and the differential pressure transmitter, is its weak link, is easy to generate faults such as obstruction, leakage, burn into are freezed, distorted signals.According to statistics, in all kinds of faults of throttling differential pressure flowmeter, the fault that the impulse pipeline causes accounts for more than 70% of sum.
On the other hand, increasingly sophisticated along with industrial processes often needs each component in some polycomponent fluid-mixings is carried out the flow detection that need not separate.Common heterogeneous fluid-mixing has following five classes:
The first kind is the gas-liquid mixed two-phase flow, and as water vapor, cold-producing medium in the air-conditioning and other liquid that is easy to vaporize of band water and the gas that is easy to liquefy etc., the rock gas that has a small amount of white oil or aqueous water that the oil gas well is produced also belongs to this type of fluid.Corresponding flow detection patent such as U.S. Pat-5031466.
Second class is a gas-solid mixing two-phase flow, as coal dust, grain and the industrial chemicals particle etc. that adopt strength to carry.Corresponding flow detection patent such as U.S. Pat-4726235.
The 3rd class is a liquid liquid mixing two-phase flow, oil-water mixture of producing as oil well etc.Corresponding flow detection patent such as U.S. Pat-6755086.
The 4th class is a solid-liquid mixing two-phase flow, as paper pulp, the coal water mixture that adopts the fluid power conveying and industrial chemicals pulpous state liquid etc.Corresponding flow detection patent such as U.S. Pat-4484478.
The 5th class is an oil-gas-water three-phase flow, i.e. the fluid-mixing of crude oil, associated gas and the mineralized water produced of oil gas well.Corresponding flow detection patent such as U.S. Pat-6655221, and publication number is that 1492216A, open date are the Chinese patent on April 28th, 2004.
From above-mentioned document as seen, the flow detection of not separating of above-mentioned each class heterogeneous fluid all is to perplex the technical barrier of industry member time decades.
Traditional throttling differential pressure flowmeter is under the testing environment of polyphasic flow, and aforementioned two shortcomings are especially serious.Reason is, on the one hand, often difference is bigger for the viscosity of each phase material, density in the heterogeneous fluid, when the interface of two kinds of materials can produce very big throttling differential pressure fluctuation during by restriction device.In this case, must select the bigger differential pressure pick-up of range just can bear the impact of this throttling differential pressure and be unlikely to cause permanent damage, and the excessive accuracy of detection that just can't guarantee under the less normal condition of throttling differential pressure ratio of range.On the other hand, usually be mixed with gas or solid in the polyphasic flow, these bubbles or solid particle have constituted unavoidable serious threat to the pressure propagation function of impulse pipeline again.As a result, the traditional throttling differential pressure flowmeter and the flowmeter of other kind are same, all can't be effective to solve polyphasic flow and detect this technical barrier.
At above-mentioned deficiency, mainly contain the development efforts of following several respects in recent years at the throttling differential pressure flowmeter:
The one, adopt wide-range differential pressure transmitter or many differential pressure transmitters and usefulness, widen rangeability.As the described technical scheme of U.S. Pat-6860325.
The 2nd, develop linear orifice plate, widen rangeability.Linear orifice plate claims elasticity to load variable area variable head orifice plate again, the conical stopper of its curved surface moves around under the effect of differential pressure and spring force, interstitial surface area is changed automatically with the flow size, the variation of this hole causes differential pressure output signal or output signal of displacement and flow linear, and then has enlarged rangeability.
The 3rd, shorten the impulse pipeline, restriction device and differential pressure transmitter are made of one, form integrated throttling differential pressure flowmeter, reduce the potential leakage point of pipeline, improve global reliability, improve dynamic perfromance, conveniently install and use.As U.S. Pat-6776054, and the described technical scheme of Chinese invention patent ublic specification of application (application number is 98239368.7, and the open date is on November 10th, 1999).
Chinese invention patent ublic specification of application (application number is 88105217.5, and the open date is on September 6th, 1989) once disclosed a kind of and the similar detection scheme of the present invention, was exclusively used in the flow detection of biphase gas and liquid flow.In this detection scheme, adopt traditional differential pressure pick-up that the throttling differential pressure on the restriction device is detected, after testing result is handled as calculated, obtain the throttling differential pressure mean value within a period of time and the root-mean-square value of throttling differential pressure fluctuation value respectively, the void fraction of biphase gas and liquid flow in determining during this period of time according to the ratio of these two values again, last total mass flow rate of trying to achieve biphase gas and liquid flow again.
Another part order laid-open U.S. Patents US-5031466 July 16 in 1991 also discloses the detection scheme of a biphase gas and liquid flow, the technical scheme everyway of this technical scheme and above-mentioned Chinese patent is quite similar, and difference between the two only is that the computing formula of flow is slightly different.
Above-mentioned two existing problems of existing patent are: its technical scheme is a structure of having indiscriminately imitated the conventional throttle differential pressure flowmeter fully, do not carry out improved wish for the variety of problems that this flowmeter is used for existing originally under the single-phase flow situation, just be directly used in two-phase flow and detect; Do not recognize that employed differential pressure pick-up and impulse pipeline all have very big harmful effect for the detection effect of throttling differential pressure fluctuation value.
Form above-mentioned dysgenic reason two aspects are arranged.On the one hand, the reaction velocity of any pressure transducer all has a limit, and when the velocity of wave motion of pressure signal during near some degree, bigger deviation will appear in testing result, can't correctly reflect its true fluctuation value.This limit just is called the frequency response of sensor.With present technical merit, traditional differential pressure pick-up just has been difficult to realize detecting accurately for the pressure signal of frequency greater than 5KHz.On the other hand, traditional impulse Methods for pipeline installation also is difficult to the accurate detection of assurance for the high-frequency pressure signal, because the impulse pipeline itself has constituted a bigger chamber, when its inner existence can compressed medium, just there was the elastic effect of spring-like in itself, is difficult to transmit effectively the high-frequency pressure signal, and excessive impurity and the bubble etc. of then entering easily of this chamber, too small then resistance increases, even causes local obstruction, all is unfavorable for the accurate detection of throttling differential pressure.Even adopt oil-filled kapillary as the impulse pipeline, this problem still is difficult to solve fully.
For above-mentioned reasons, the detection error of throttling differential pressure fluctuation value is bigger always, and this also to be the accurate relation of throttling differential pressure fluctuation value and flow never have found one of the main reasons.Though aforementioned two accurate relations that throttling differential pressure fluctuation value and flow are sought in existing patents trial are because the detection error of throttling differential pressure fluctuation value causes this relation smudgy.The result is that most experts think the ultimate principle that this relation is inaccurate, unreliable, can not become flowmeter of new generation, and this prejudice has further been aggravated ignoring this relation conversely.In the last hundred years, the invention of similar this case fails to occur always, and all so far experts all hold the suspicious attitude to this and do not reattempt, and reason just is this.(application number is 88105217.5 to the Chinese invention patent ublic specification of application, the open date is on September 6th, 1989) one of inventor (publication number is CN 1477375A at its second part of Chinese invention patent ublic specification of application, the open date is on February 25th, 2004) the technical background part estimate as follows once more for the technical scheme of its first part of patent of invention: " this method and instrument are owing to be subjected to down-hole impulse pipeline oversize; the restriction of test conditions such as the pipeline internal diameter is too little again; the pulsations signal of differential pressure is difficult to measure through overdamping and ", yet but fail to provide solution targetedly, just proposed the another one solution again.
With above-mentioned existing patent contrast, the present invention can look for another way on the detection principle, abandon the Bei Nuli equation, transfer direct relation based on throttling differential pressure fluctuation value and flow, reason just is, use by dynamic pressure transducer, found the method for accurate detection throttling differential pressure fluctuation value, and then found the accurate relation of throttling differential pressure fluctuation value and flow, proposed to detect its flow effectively according to the throttling differential pressure fluctuation value of single-phase flow, and it is extremely faint to have overcome in the single-phase flow throttling differential pressure fluctuation value, accurately detect a very difficult technologies difficult problem, the present invention successfully is applied to the field of flow detection of single-phase flow the most at last, and has produced unforeseeable technique effects such as ten times of flow detection rangeability enlarged proximal.Adopt dynamic pressure transducer also to eliminate the impulse pipeline simultaneously, thereby thoroughly eliminated the various faults that aforementioned impulse pipeline may cause.
From the surface, character of the present invention belongs to key element and substitutes invention, because compare with traditional throttling differential pressure flowmeter, on physical construction, difference of the present invention only is to adopt two dynamic pressure transducers to substitute a traditional differential pressure pick-up.It should be noted that, this is simple equal a replacement anything but, reason is: the testing goal of these two kinds of pressure detection methods has been diverse, adopt the impossible high fdrequency component that accurately detects in the throttling differential pressure fluctuation value of traditional differential pressure pick-up, and adopt the selected dynamic pressure transducer of the present invention also may not detect the stable state value that obtains the throttling differential pressure.Since American He Xieer in 1886 has just made the utility unit of measuring discharge with Venturi tube, so far throttling differential pressure flowmeter use total amount worldwide is at least millions of, in reaching the use in more than 100 year so far, its shortcoming is known by the technician already and is thirsted for solving always.But, the scheme that the present invention proposes never occurred, employed throttling differential pressure flowmeter all is based upon on the Bei Nuli equations based in the industrial process, that is to say, have only the flow information that is comprised in the throttling differential pressure mean value to be used effectively, and the flow information that is comprised in the throttling differential pressure fluctuation value is identified as detection noise and filtering always.The present invention has overcome this prejudice just, and has obtained unforeseeable technique effects such as ten times of rangeability enlarged proximal.
Summary of the invention
One of purpose of the present invention provides a kind of flow detector, and this pick-up unit is the throttling differential pressure fluctuation value of test fluid accurately, and further detects the flow of fluid on this basis.
Two of purpose of the present invention provides a class flow detector, when detected fluid common gas-liquid in, gas solid, liquid liquid, solid-liquid two-phase flow and oil-gas-water three-phase flow by aforementioned various industrial processs, can be according to using on-the-spot performance and price request, from such flow detector, select configuration targetedly, thereby adapt to different field requirement, the online detection that do not separate economic, that realize each phase flow rate of polyphasic flow effectively.
Technical scheme of the present invention is based on following principle: detect for any physical quantity of occurring in nature, testing result within a period of time in fact all comprises two parts, one of them is the average value, another is the fluctuation value, and testing result should be the stack result of these two values usually.Under opposite extreme situations, have only one to be of practical significance among these two values, for example the weight to object is carried out repeated detection continuously in a period of time, because all can there be a small amount of error in each detection inevitably, thereby causes testing result to present a kind of fluctuation of approximate random near certain average value.But the fluctuation value of this testing result can neglect, and has only the average value meaningful, and is because the fluctuation value mainly is each error of being introduced that detects, nonsensical.For example the voltage of alternating current is carried out detection in a period of time again, the average value of testing result is zero substantially, and is nonsensical, has only the frequency of fluctuation value and amplitude just meaningful.It should be noted that, these two examples are two kinds of opposite extreme situations, in the actual life for most of physical quantitys, testing result is normally between above-mentioned two extreme detection examples, that is to say, average value in the testing result and fluctuation value all have practical significance simultaneously, and in other words, average value in the testing result and fluctuation value all comprise Useful Information simultaneously.
Be that example is made a concrete analysis of with the throttling differential pressure below.Suppose that in a period of time two check point places on restriction device are detected the pressure that obtains and are respectively P1 (t) and P2 (t), the throttling differential pressure between these 2 is Y (t).According to the analysis of the preceding paragraph, the pressure of each check point and throttling differential pressure all are by the stack of average value and two parts of fluctuation value, promptly have:
P1(t)＝PA1+PD1(t)； (1)
P2(t)＝PA2+PD2(t)； (2)
Y(t)＝YA+YD(t)； (3)
PA1 and PA2 are respectively the average value of two check point place pressure in the following formula, because they all are the mean value in a period of time, thereby during this period of time are time-independent values; And PD1 (t) and PD2 (t) are respectively the fluctuation value of two check point place pressure, and they all are time dependent values, and their mean value during this period of time all is zero; YA is the average value of throttling differential pressure, because it also is a mean value during this period of time, thereby during this period of time is time-independent value; YD (t) is the fluctuation value of throttling differential pressure, and it is time dependent value, and its mean value during this period of time also is zero.
On the other hand, because throttling differential pressure Y (t) should be the difference of the pressure at two check point places according to definition, that is:
Y(t)＝P1(t)-P2(t)； (4)
Formula (1), formula (2) substitution formula (4) can be got:
Y(t)＝(PA1+PD1(t))-(PA2+PD2(t))
＝(PA1-PA2)+(PD1(t)-PD2(t))； (5)
Because the mean value of PD1 and PD2 all is zero, comparison expression (3) can get with formula (5),
YA＝PA1-PA2； (6)
YD(t)＝PD1(t)-PD2(t)； (7)
By formula (6) as can be known, throttling differential pressure mean value equals average value poor of two check point place pressure.By formula (7) as can be known, throttling differential pressure fluctuation value equals fluctuation value poor of two check point place pressure.In view of the above as can be known, it is feasible adopting dynamic pressure transducer to detect throttling differential pressure fluctuation value, and reason is as follows:
Dynamic pressure transducer is to design for the fluctuation situation of detected pressures accurately and efficiently, thereby is difficult to the stable state numerical value of detected pressures accurately and effectively.Be characterized in very responsive to the fluctuation value of pressure, and insensitive to the average value of pressure.In other words, dynamic pressure transducer is by the detection effect of sacrifice to pressure average value, and has got the better detection effect to the pressure surge value in return.Dynamic pressure transducer at present commonly used mainly is based on the dynamic pressure transducer that crystal piezoelectric principle, piezoelectric ceramics principle, coil add permanent magnet principle or optical fiber measurement principle.When adopting two dynamic pressure transducers to carry out the detection of pressure P 1 (t), P2 (t), pressure average value PA1, PA2 can not get effective detection usually, and pressure surge value PD1 (t), PD2 (t) can obtain very accurate detection fast.Like this, according to formula (6) as can be known, differential pressure mean value YA will can not get effective detection, thereby can't come the size of accurate calculated flow rate according to Bernoulli equation.And according to formula (7) as can be known, differential pressure fluctuation value YD (t) still can be detected accurately, and can not be subjected to differential pressure mean value YA and detect inaccurate influence.These characteristics are very favourable to the flow rate testing methods based on differential pressure fluctuation value YD (t).
Based on above-mentioned analysis, technical conceive of the present invention is as follows: at first, having proposed the mobile flow information of fluid not only is present among the average value of throttling differential pressure, and be present in equally among the fluctuation value of throttling differential pressure, will not detect throttling differential pressure mean value, only detect the target that throttling differential pressure fluctuation value can be realized flow detection equally.Secondly, pointed out under the identical situation of overall flow rate, because the difference of aspects such as density, viscosity between the different component, cause the formed throttling differential pressure fluctuation of heterogeneous fluid value often a lot of greatly than the formed throttling differential pressure fluctuation of monophasic fluid value, thus above-mentioned be that the flow rate testing methods of foundation has bigger advantage and potentiality when being used to detect polyphasic flow with throttling differential pressure fluctuation value.The 3rd, adopt two dynamic pressure transducers to carry out the detection of throttling differential pressure fluctuation value, the basic ideas of this detection method are: by sacrificing the detection effect for throttling differential pressure mean value, improve the detection effect for throttling differential pressure fluctuation value.The resulting result of this detection method is more accurate than traditional differential pressure pick-up, bandwidth is bigger, and has thoroughly eliminated the various faults that the impulse pipeline may cause.The 4th, on the basis of the above, main difference part at the physical property of each phase component of detected fluid, from various phase fraction detecting devices, make targetedly and selecting based on the different operating principle, and the phase fraction detecting device centralized arrangement that will select like this to obtain is near the position of the cross-sectional area minimum of fluid flowing passage on the restriction device, make each section fluid in the flow channel flow through when having arranged the position of phase fraction detecting device, can obtain the detection of most phase fraction detecting devices at synchronization, perhaps make each section fluid in the flow channel flow through when having arranged the position of phase fraction detecting device, can in the shortest time, obtain the detection of most phase fraction detecting devices successively, accuracy and reliability in the time of can further improving described flow detector like this and be used for two-phase flow and detect, and can realize online being regardless of to three-phase stream from flow detection.
Below be the basic technical scheme of the present invention that forms according to above-mentioned technical conceive:
Described flow detector has the airtight passage that fluid flows to constitute sense channel by an intersegmental part, on this sense channel, arrange 1 sensor combinations, this sensor combinations is made up of 2 sensors at least, at least 2 signal of sensor in this sensor combinations are introduced in 1 electronic installation, realize asking for of fluid flow by this electronic installation, the feature of described flow detector is: comprise 2 dynamic pressure transducers in the described sensor combinations at least, this dynamic pressure transducer is to design for the fluctuation situation of detected pressures accurately and efficiently, thereby is difficult to the stable state numerical value of detected pressures accurately and effectively; Have at least 2 dynamic pressure transducers to be spaced a distance and to arrange along fluid flow direction; Between 2 dynamic pressure transducers arranging being spaced a distance along fluid flow direction, there is variation in the cross-sectional area of sense channel, and therefore corresponding change has also taken place flow rate of fluid.
First kind of improvement of the present invention, be to increase by 1 phase fraction detecting device on the described flow detector of above-mentioned basic technical scheme, this phase fraction detecting device can be any one among following 8 kinds of phase fraction detecting devices: ultrasonic detector, capacitance detector, electrical impedance detecting device, microwave detector, infrared detector, laser detector, X-ray detector, gamma ray detector.And this phase fraction detector arrangement is near the position of the cross-sectional area minimum of fluid flowing passage on the restriction device.
Second kind of improvement of the present invention, be to increase at least 2 phase fraction detecting devices on the described flow detector of above-mentioned basic technical scheme, these phase fraction detecting devices can be selected for use arbitrarily from the detector set that following 8 kinds of phase fraction detecting devices are formed: ultrasonic detector, capacitance detector, electrical impedance detecting device, microwave detector, infrared detector, laser detector, X-ray detector, gamma ray detector; Selected detecting device has same or different principle of work, and has same or different operation wavelength; Selected phase fraction detecting device centralized arrangement is near the position of the cross-sectional area minimum of fluid flowing passage on the restriction device; Described phase fraction detecting device can the phase mutual interference and the precondition that allows of locus under, the center line of effective surveyed area of at least 2 phase fraction detecting devices is intersected at a point at the center of sense channel, and reduce the angle between these two center lines as far as possible, make the overlapped covering of effective surveyed area of 2 phase fraction detecting devices, make each section fluid in the sense channel when flowing through this position, can obtain the detection of these phase fraction detecting devices at synchronization; Perhaps, described phase fraction detecting device can the phase mutual interference and the precondition that allows of locus under, the effective surveyed area that makes at least 2 selected phase fraction detecting devices as far as possible closely is adjacent to be arranged in parallel in side by side in the same axial cross section along the flow direction of fluid, and reduce the spacing between the center line of these two effective surveyed areas as far as possible, make each section fluid in the sense channel when flowing through this position, can in the shortest time, obtain the detection of these phase fraction detecting devices successively.
The third improvement of the present invention, be on the restriction device of the described flow detector of above-mentioned basic technical scheme, to increase by 1 differential pressure pick-up again, and two pressure ports that this differential pressure pick-up connected are arranged in the xsect that dynamic pressure transducer is installed.
Electronic installation described in the technical scheme of the present invention can be an analogue means, it also can be digital means, its function is the output signal that receives dynamic pressure transducer and phase fraction detecting device, and handle accordingly, finally form the result of each phase flow rate in the flow results of single-phase flow or the polyphasic flow.Be used to calculate circuit arrangement with the delivery rate result in the present various flowmeter and all can be used for realizing this function, such as various flow computers, microcontroller circuit and hardware programmable logical circuit or the like.If select digital circuit for use, generally include the display device of analog to digital conversion circuit, data processing circuit, output signal interface and necessity etc. so.
The present invention proposes a kind of flow detector of novelty, because the narrow root of conventional throttle differential pressure flowmeter range ability is that both are quadratic relationship along with the stable state grow in magnitude of the increase throttling differential pressure of fluid flow is very fast based on restriction device; And the growth of amplitudes of the fluctuation value of throttling differential pressure is slow, frequency increases very fast, therefore, after the present invention adopted dynamic pressure transducer to replace original differential pressure pick-up, dynamic pressure transducer just made that up to the frequency response of hundreds of thousands hertz the range ability of flow detector of the present invention can significantly be enlarged like a cork very much at present.Simultaneously, owing to eliminated original impulse pipeline, this flow detector has kept traditional throttling differential pressure flowmeter firm, stable and reliable for performance, advantage that serviceable life is long simple in structure, overcome shortcomings such as conventional throttle differential pressure flowmeter rangeability is narrow, impulse pipeline easy break-down simultaneously, can also cancel necessary antifreezing type isolator and condenser etc. under some situation.
Simultaneously, when detected fluid in by aforementioned various industrial processs when common gas-liquid, gas-solid, solid-liquid two-phase flow, because this flow detector has been abandoned traditional throttling differential pressure flowmeter excavates flow information from throttling differential pressure mean value thinking, then from throttling differential pressure fluctuation value, excavate flow information, and owing to compare with the flow information that comprised in the throttling differential pressure mean value, the flow information that is comprised in the throttling differential pressure fluctuation value is more reliable and abundant, thus can realize each phase flow rate of two-phase flow reliable, economical onlinely do not separate detection.
In addition, because the employed flow information method for digging of this flow detector is asked for problem with the extreme value that the flow rate calculation problem is converted into an objective function, when needs further improve the detection effect of two-phase flow, perhaps need to detect some three-phases stream, during as oil-gas-water three-phase flow, just can be at the Main physical nature difference of each component in the detected fluid, select corresponding phase fraction detecting device, and be installed on this flow detector, and then in objective function, add and corresponding of newly-increased phase fraction detecting device.After improving like this, not only described pick-up unit can be further improved for the detection effect of two-phase flow, but also can realize oil-gas-water three-phase flow onlinely do not separate detection.
Description of drawings
The present invention is described in further detail below in conjunction with the drawings and specific embodiments.
Fig. 1 is the structural representation of embodiments of the present invention 1;
Fig. 2 is the structural representation of embodiments of the present invention 2;
Fig. 3 is a transversal section cut-open view of embodiments of the present invention 2, and this transversal section is to get along A-A hatching line shown in Figure 2;
Fig. 4 is the structural representation of embodiments of the present invention 3;
Fig. 5 is the structural representation of embodiments of the present invention 4;
Fig. 6 is a transversal section cut-open view of embodiments of the present invention 4, and this transversal section is to get along B-B hatching line shown in Figure 5;
Fig. 7 is the structural representation of embodiments of the present invention 5;
Fig. 8 is the structural representation of embodiments of the present invention 6;
Fig. 9 is a transversal section cut-open view of embodiments of the present invention 6, and this transversal section is to get along C-C hatching line shown in Figure 8;
Figure 10 is the structural representation of embodiments of the present invention 7;
Embodiment
Provide 7 indefiniteness embodiments below in conjunction with accompanying drawing, and make further detailed description.
Fig. 1 is the structural representation of embodiments of the present invention 1, and 1 is the fluid intake end among the figure, and 7 is fluid outlet, and sense channel is made of preceding straight length 2, orifice plate 16 and back straight length 6 successively.Two piezoelectric type dynamic pressure transducers 8,9 are spaced a distance along flow direction, straight length 2 and back straight length 6 before being arranged in, and its presser sensor end face flushes with the inside surface of fluid flowing passage as far as possible, and is mobile to avoid interference fluid.Piezoelectric type dynamic pressure transducer 8,9 is connected to electronic installation 36 by cable, this electronic installation provides working power and two voltage output signals is gathered preservation for dynamic pressure transducer 8,9, and then these two voltage output signals are carried out Filtering Processing and compare, obtain the fluctuation value of throttling differential pressure, at last this is fluctuateed value as the foundation of asking for fluid flow.
This configuration of embodiment 1 can be used for the flow detection of various monophasic fluids, the process of this detection is: the first step is carried out the calibration experiment of described flow detector, selected several flow numbers carry out reality and fail to be sold at auction calmly in its range ability, under each flow operating mode, the output signal of two dynamic pressure transducers is carried out the continuous recording in 10 seconds respectively.Second stepping rower devise a stratagem calculation work, the spectral density numerical value of this difference is calculated and stored to the difference of following two signal records of each flow operating mode of calculating more earlier.Because spectral density is the dull trend that increases along with the increase of flow presents, thereby can obtain between the two relation by non-linear interpolation.The 3rd step was to carry out on-the-spot flow detection.At this moment resulting relation in online spectral density of trying to achieve in scene and the calibration process directly need only be compared, can try to achieve the net result of flow.
Embodiment 1 this configuration can also detect various biphase gas and liquid flows, as: condensation air-flow, the gas stream that is easy to liquefy, flow of liquid of being easy to vaporize etc.Be that example is specifically described with the flow of band water water vapour and the detection of mass dryness fraction below.Water vapour is as a kind of thermal source, uses very extensively in modern industry, and its mass dryness fraction is an important indicator that relates to safety in production and various technological effects.Such as, the history of the thermal recovery technology existing decades by in oil reservoir, injecting high-temperature steam, the detection of the mass dryness fraction value of its employed high-temperature steam is very important, directly influences the safe operation of crude production rate, energy resource consumption, operation cost and injection boiler.Detect when therefore, cost-effectively water vapour being carried out flow and mass dryness fraction and have very important significance.But this detection up to now substantially all is by artificial realization, and low precision efficient is low, is badly in need of automatic detection device.
Embodiment 1 this configuration is used to detect is with the process of water water vapour as follows:
The first step, the exemplary parameter of definition polyphasic flow.For band water water vapour, following two parameter: total volumetric flow rate Q and gas volume fraction G are arranged.The reality that the composite condition of selected a plurality of different Q and G carries out described flow detector in the range ability of total volumetric flow rate Q is failed to be sold at auction and is decided experiment, under each composite condition, these two digital quantities of output signal S1, S2 of two dynamic pressure transducers 8,9 are carried out the continuous acquisition and the record deposit in 10 seconds respectively; In second step, design bandpass filter FA, FB, the FC that three frequency bands are respectively 10Hz to 100Hz, 100Hz to 1000Hz, 1000Hz to 10000Hz with the firl function in the MATLAB software package; The 3rd step, filter function in the first usefulness MATLAB software package is to two dynamic pressure transducer output signal S1, S2 carries out suitable filtering, the purpose of this filtering is the undesired signal of eliminating on 50Hz power frequency and some other Frequency point, calculate the difference D=S2-S1 of following two the dynamic pressure transducer output signals record of each composite condition then, use designed wave filter FA in second step more respectively, FB, FC carries out filtering to this difference DS and calculates three filtering DA as a result, DB, DC calculates and stores three filtering DA as a result respectively with the periodogram function in the MATLAB software package at last, DB, the spectral density numerical value PA of DC, PB, PC.The 4th stepping line function interpolation, adopt non-linear interpolation method try to achieve funtcional relationship between PA, PB, PC and total volumetric flow rate Q and the gas volume fraction G: PA=f1 (Q, G); PB=f2 (Q, G), PC=f3 (Q, G); Here we select for use the interpn function in the MATLAB software package can reach this purpose; The 5th step was to carry out on-the-spot flow detection.At this moment need only bring spectral density RA, RB, the RC that tried to achieve to the 3rd step in real time by second step at the scene into following objective function:
M＝(f1(Q，G)/RA-1) 2+(f2(Q，G)/RB-1) 2+(f3(Q，G)/RC-1) 2； (8)
And then objective function M is minimized optimizing calculate the net result to try to achieve total volumetric flow rate Q and gas volume fraction G.So far, this detection problem has been converted into the problem of the extreme value of finding the solution objective function M, and this ancient mathematical problem has had a large amount of very ripe mathematical algorithm and software program package at present, can select for use easily.Here we select for use fminimax function in the MATLAB software package can try to achieve the net result of total volumetric flow rate Q and gas volume fraction G.
Fig. 2 is the structural representation of embodiments of the present invention 2, among the figure as seen, sense channel is made of the restriction device of a similar Venturi tube, this restriction device is made of preceding straight length 2, preceding speed change pipeline section 3, throat 4 and back speed change pipeline section 5 successively, 1 is the fluid intake end, 7 is fluid outlet, adopts the insulating material manufacturing.The position of the cross-sectional area minimum of fluid flowing passage is a throat 4 on this restriction device.The sensor that is disposed on this restriction device also has following characteristics:
At first, two piezoelectric type dynamic pressure transducers 8,9 are spaced a distance along flow direction, the preceding straight length 2 and the throat 4 of speed change pipeline section 3 upstreams before being arranged in, and its presser sensor end face flushes with the inside surface of fluid flowing passage as far as possible, mobile to avoid interference fluid.Piezoelectric type dynamic pressure transducer 8,9 is connected to electronic installation 36 by cable, this electronic installation provides working power and two voltage output signals is gathered preservation for dynamic pressure transducer 8,9, and then these two voltage output signals are carried out Filtering Processing and compare, obtain the fluctuation value of throttling differential pressure, at last this is fluctuateed value as the foundation of asking for fluid flow.
Secondly, two electric capacity phase fraction detecting devices near the inside surface of throat 4, have been set up.By electrode 23,24 pair of electrodes that constituted with all embed the inside surface of throat 4 by electrode 25,26 pair of electrodes that constituted.Two pairs of arrangement of electrodes are on the same xsect of throat 4, this xsect is positioned near the position of cross-sectional area minimum of fluid flowing passage on the restriction device, and each all is arranged symmetrically in the axial line both sides of fluid flowing passage to electrode, and two lines of centres of two pairs of electrodes are vertically intersected on a bit.Electrode is set up insulation course after embedding the inside surface of throat 4 on the surface of electrode contacting with fluid, and the shape of the inside surface that as far as possible guarantees throat 4 still keep intercalation electrode after embedding four electrodes before, and can not influence fluid flowing through throat 4.Four electrodes are connected to electronic installation 36 by cable, in this electronic installation inside, these two pairs of electrodes are connected to the AD7745 chip of two ANALOG DEVICES companies respectively, this chip is special-purpose electric capacity-digital quantity conversion chip, only be required to be this chip 5V is provided power supply, the capacitance that gets final product between the electrode that will be connected two pin directly is converted to digital quantity, and this digital quantity offered the data processing circuit of electronic installation inside by the I2C interface, preserve and computing so that this digital quantity gathered.
Electric capacity phase fraction detecting device is to utilize the difference in dielectric constant of material to detect.Import the high frequency pumping voltage of 30KHz to 300MHz in the pipeline both sides of heterogeneous fluid by electrode, come the size of electric capacity between the detecting electrode, and the size of this electric capacity depends on the specific inductive capacity of fluid between the electrode fully, when the specific inductive capacity difference of each phase component in the heterogeneous fluid is big, just can obtain the corresponding information of phase fraction in view of the above.The frequency of present embodiment medium-high frequency driving voltage is elected 30KHz as.
Fig. 3 is a transversal section cut-open view of embodiments of the present invention 2, and this transversal section is to get along A-A hatching line shown in Figure 2; Can be clear that the relative position of electrode pair 23,24 and electrode pair 25,26 among the figure.
The 3rd, two ultrasonic transducers 11,12 near the inside surface of throat 4, have been set up, both just in time are positioned on the straight line of tiltedly wearing throat 4, this straight line is positioned at the fluid flowing passage axial cross section at electrode 23,24 places, and this straight line passes the intersection point of two lines of centres of aforementioned two pairs of electrodes.The sensitive surface of two ultrasonic transducers 11,12 is parallel to each other and stands opposite each other at a distance, so that ultrasonic transducer 12 can receive 11 ultrasonic waves transmitted of ultrasonic transducer effectively.Ultrasonic transducer 11,12 also is connected to electronic installation 36 by cable, this electronic installation inside comprises the 5072PR ultrasonic pulse transceiver of a Panametrics company, can be the ultrasonic pulse of 2MHz for ultrasonic transducer 11 provides the pulse excitation voltage of 0-40V to make its transmission frequency, can carry out corresponding processing and amplifying to the ultrasound wave voltage signal that ultrasonic transducer 12 is received simultaneously.And then will gather preservation in this signal input electronic installation 36, and compare by the pulse signal of being launched with ultrasonic transducer 11, Strength Changes result and hyperacoustic flight time result after ultrasound wave passes heterogeneous fluid obtained.
Here ultrasonic transducer 11,12 all is based on the part of hyperacoustic phase fraction detecting device.This phase fraction detecting device is that Strength Changes and the speed difference when utilizing ultrasound wave to propagate in material detects.Velocity of propagation and the density of medium of ultrasound wave in medium is approximated to direct ratio, so the flight time of ultrasound wave between two transducers is relevant with passing density of medium.In addition, ultrasound wave is when penetrating complicated dielectric structure such as bubble or liquid piece, and its intensity can and reflect because of reflection and significantly weaken, and the degree that weakens is relevant with the granularity of its medium that is passed.According to this character as can be known, the phase fraction of ultrasound wave fluid media (medium) between the flight time between two transducers and these two variablees of Strength Changes and transducer is directly relevant, when the density of each phase component in the detected fluid or granularity difference are big, these two variablees are detected the detection that just can realize phase fraction.
When being used for phase fraction and detecting, when in the detected fluid during air inclusion, hyperacoustic frequency of operation is selected between the 0.5MHz to 5MHz, and when in the detected fluid not during air inclusion, hyperacoustic frequency of operation is selected between the 2.0MHz to 20MHz.The concrete selection of its frequency need be compromised and be considered following factor: the one, and detect the position and often exist and the irrelevant low-frequency flow moving noise of phase fraction, the power of selecting lower frequency must improve signal just can obtain satisfactory SN ratio; The 2nd, phase fraction detects and must to wait for that last phase fraction detects institute's ultrasonic waves transmitted signal and fully decays each time, if adopt the lower ultrasound wave of frequency, because slow many of its attenuation ratio high-frequency ultrasonic, the frequency of phase fraction detection will be difficult to raising; The 3rd, the signal attenuation effect that frequency is high when having gas in the fluid is very strong, and the signal of reception will be difficult to guarantee precision because of very faint; The 4th, the size of common phase fraction depends primarily on and detects the existing thick mixed structure in position, as larger-size liquid piece or bubble, but they are often with trickle mixed structures such as very little bubble of some diameters or drops and deposit, the too high signal of frequency causes bigger phase fraction to detect error because too responsive to these trickle mixed structures easily.
Among Fig. 2 as seen, comprise the electric capacity phase fraction detecting device of electrode pair 23,24 and comprise the ultrasound wave phase fraction detector arrangement of ultrasonic transducer 11,12 in same axial cross section, and for the overlapped as far as possible covering of the effective surveyed area that makes these two phase fraction detecting devices, can not the phase mutual interference and the precondition that allows of locus under, effective surveyed area center line of these two phase fraction detecting devices intersects at a point at the center of sense channel, and the angle between these two center lines is reduced as far as possible.Such structural design makes each section fluid in the flow channel when flowing through this position, can obtain the detection of these two phase fraction detecting devices at synchronization.
Embodiment 2 this configurations can be used for the flow detection of multiple three-phase stream.Such as the ubiquitous oil-gas-water three-phase flow of oil and gas industry.Because the product that goes out of most oil gas wells tends to comprise these three kinds of compositions of crude oil, rock gas and mineralized water, therefore, onlinely do not separate detection and have very important significance what the oil gas well went out that product carries out each phase flow rate cost-effectively for reservoir management, production practice optimization and production process monitoring etc.But this detection up to now substantially all is to realize that by separation vessel low precision efficient is low, is badly in need of the pick-up unit that need not separate automatically.The process that embodiment 2 this configurations are used to detect oil-gas-water three-phase flow is as follows:
The first step, the exemplary parameter of definition polyphasic flow.Following three parameter: total volumetric flow rate Q, gas volume fraction G and liquid phase volume water percentage W are arranged for oil-gas-water three-phase flow.The reality that the composite condition of selected a plurality of different Q, G and W carries out described flow detector in the range ability of total volumetric flow rate Q is failed to be sold at auction and is decided experiment, under each composite condition, to output signal S1, the S2 of two dynamic pressure transducers 8,9, the output signal U 1 of capacitor C 1, C2 and ultrasonic transducer 12 between the two pairs of electrodes amounts to continuous acquisition and the record deposit that five digital quantities carried out for 10 seconds respectively; In second step, design bandpass filter FA, FB, the FC that three frequency bands are respectively 10Hz to 100Hz, 100Hz to 1000Hz, 1000Hz to 10000Hz with the firl function in the MATLAB software package; The 3rd step, filter function in the first usefulness MATLAB software package is to two dynamic pressure transducer output signal S1, S2 carries out suitable filtering, the purpose of this filtering is the undesired signal of eliminating on 50Hz power frequency and some other Frequency point, calculate the difference D=S2-S1 of following two the dynamic pressure transducer output signals record of each composite condition then, use designed wave filter FA in second step more respectively, FB, FC carries out filtering to this difference DS and calculates three filtering DA as a result, DB, DC calculates and stores three filtering DA as a result respectively with the periodogram function in the MATLAB software package at last, DB, the spectral density numerical value PA of DC, PB, PC.The 4th step was calculated the average value P 3 of average value P 1, P2 and the ultrasonic transducer output signal strength of capacitor C 1, C2 testing result under each composite condition.The 5th stepping line function interpolation, adopt interpolation method try to achieve funtcional relationship between PA, PB, PC, P1, P2, P3 and total volumetric flow rate Q, gas volume fraction G and the liquid phase volume water percentage W: PA=f1 (Q, G, W); PB=f2 (Q, G, W), PC=f3 (Q, G, W), P1=g1 (Q, G, W), P2=g2 (Q, G, W), P3=g3 (Q, G, W); Here we select for use the interpn function in the MATLAB software package can reach this purpose; The 6th step was to carry out on-the-spot flow detection.At this moment need only bring spectral density RA, RB, RC, condenser paper average R1, R2 and the ultrasonic intensity mean value R3 that is tried to achieve to the 4th step according to second step under the condition at the scene into following objective function M:
M＝(f1(Q，G，W)/RA-1) 2+(f2(Q，G，W)/RB-1) 2+(f3(Q，G，W)/RC-1) 2
+(g1(Q，G，W)/R1-1) 2+(g2(Q，G，W)/R2-1) 2+(g3(Q，G，W)/R3-1) 2； (9)
And then objective function M is minimized optimizing calculate the net result to try to achieve total volumetric flow rate Q, gas volume fraction G and liquid phase volume water percentage W.So far, this detection problem has been converted into the problem of the extreme value of finding the solution objective function M, and this ancient mathematical problem has had a large amount of very ripe mathematical algorithm and software program package at present, can select for use easily.Here we select for use fminimax function in the MATLAB software package can try to achieve the net result of total volumetric flow rate Q, gas volume fraction G and liquid phase volume water percentage W.
It is pointed out that the heterogeneous fluid of being made up of the bigger one-tenth branch of specific inductive capacity difference for other, this configuration of embodiment 2 also can realize each phase flow rate does not onlinely separate detection.And, at performance requirements such as precision is not very high, perhaps under the ability to bear condition of limited of price, embodiment 2 can also further be simplified, cancel ultrasound wave phase fraction detecting device and an electric capacity phase fraction detecting device of being adopted in its technical scheme, only keep another electric capacity phase fraction detecting device, can realize that equally each phase flow rate of above-mentioned polyphasic flow detects.Difference in the testing process only is, also is cancelled corresponding to the every of phase fraction detecting device who is cancelled among the objective function M.
Fig. 4 is the structural representation of embodiments of the present invention 3, and as seen, the part-structure of this embodiment and embodiment 2 is identical among the figure, and this part identical structure no longer repeats at this, describes the difference of these two embodiments below in detail:
At first, cancelled ultrasound wave phase fraction detecting device and electric capacity phase fraction detecting device in the embodiment 2, and restriction device can be without the insulating material manufacturing.
Secondly, throat 4 has set up two infrared ray phase fraction detecting devices.Infrared ray phase fraction detecting device is usually based on following principle work: when irradiation infrared light on material, photographed object can absorb the light of specific wavelength according to its constituent.With water is example, at the absorption band of infrared band 1.2 microns, 1.45 microns, 1.94 microns, 2.6 microns and 6 microns five wavelength is just arranged, and hydrone has obvious absorption for the infrared radiation of these wavelength.This absorption is to produce by the resonance effect that the combination that hydrone stretching vibration and angle vibrate causes.Therefore, in case with these rayed on moisture material, will produce the light absorption corresponding with water cut.In the infrared absorption wavelength of water, the absorptivity of water is little because of with 1.2 microns wavelength the time, so now adopt 1.45 microns or 1.94 micron wave lengths more.In the actual detection process, the interface of general fluid is irregular, and its reflectivity will change, thereby passes the luminous energy that arrives sensor behind the fluid and also will change.If only adopt the absorbing wavelength of water to measure, above-mentioned variation has just formed external disturbance, is difficult to measure accurately.Disturb for eliminating,, also will use this wavelength neighbouring difficult by the wavelength of moisture absorption, wavelength as a comparison except that using by the wavelength of moisture absorption.These two kinds of light are projected on the measured object, and the light that passes fluid is converted to electric signal, obtain ratio separately with sensor.Because external disturbance is usually with these two kinds of light of same scale effect, so after the testing result of two kinds of light asked for ratio, just can eliminate the influence of external disturbance.With 1.94 microns be example because water is that 1.81 microns infrared rays absorb hardly for its contiguous wavelength, this wavelength just can be used as desirable comparison wavelength, in order to eliminate the influence of external disturbance.
Among Fig. 4 as seen, can not the phase mutual interference and the precondition that allows of locus under, effective surveyed area of these two infrared ray phase fraction detecting devices is that the flow direction along fluid closely is adjacent to be arranged in parallel in the same axial cross section, and the spacing between effective surveyed area center line of two phase fraction detecting devices is reduced as far as possible.Such structural design makes each section fluid in the flow channel when flowing through this position, can obtain the detection of these two phase fraction detecting devices in the shortest time successively.In these two infrared ray phase fraction detecting devices, the operation wavelength of a pair of infrared emission tube 17, infrared receiver tube 19 is elected 1.94 microns as, and another operation wavelength to infrared emission tube 18, infrared receiver tube 20 is elected 1.81 microns as.As previously mentioned, wavelength be 1.94 microns infrared ray easily by moisture absorption, wavelength be 1.81 microns infrared ray then as a comparison wavelength use.Under the certain situation of the emissive power of infrared emission tube 17,18, ask for the ratio P between the output signal of infrared receiver tube 19,20, this ratio P is the testing result of water cut.Compare with the scheme of using a pair of infrared emission tube and receiving tube, such scheme can improve the accuracy that water cut detects.In addition, throat 4 also needs to set up infrared absorber as liner, is used to eliminate the influence of infrared external reflection ripple.
This configuration of embodiment 3 can be used to detect with water-setting gassing and other flow and water cut that contains the two-phase flow of moisture.Its testing process is similar to embodiment 2.
Fig. 5 is the structural representation of embodiments of the present invention 4, and as seen, the part-structure of this embodiment and embodiment 2 is identical among the figure, and this part identical structure no longer repeats at this, describes the difference of these two embodiments below in detail:
At first, restriction device can be without the insulating material manufacturing, near the inside surface of throat 4 ultrasonic transducer 11,12 has changed the locus, and set up a ultrasonic transducer 13 again, this ultrasonic transducer and ultrasonic transducer 11 directly are coupled by tube wall, perhaps directly be coupled by other coupling materials, so that the ultrasonic signal that does not pass fluid from ultrasonic transducer 11 is directly received, and compare with the signal that passes behind the fluid that ultrasonic transducer 12 is received, ask for Strength Changes and flight time.In electronic installation inside, this relatively is to realize by the AD8302 chip that adopts ANALOG DEVICES company.Ultrasonic transducer 12 is received passes two input ends that the signal that does not pass fluid that signal behind the fluid and ultrasonic transducer 13 received is connected to the AD8302 chip of ANALOG DEVICES company respectively, this chip is special-purpose high-frequency signal strength and phase place comparable chip, only be required to be this chip 5V is provided power supply, can carry out the comparison of intensity and phase place to the high frequency electrical signal that is connected two pin, and comparative result is converted to the voltage signal of two 0.03V to 1.8Vd, offer the analog to digital conversion circuit of electronic installation inside again, so that this analog quantity is gathered preservation and computing.According to the frequency of ultrasonic and the phase signal that obtains that detects, can calculate hyperacoustic flight time result.
Secondly, original two electric capacity phase fraction detecting devices are replaced by a microwave phase fraction detecting device.Microwave phase fraction detecting device is worked based on following principle: when electromagnetic wave was propagated in medium, its intensity can change because of the influence of the medium that it passed usually, and the dielectric property of this change and electromagnetic frequency and medium has direct relation.At present employed phase fraction detecting device great majority all utilize this class relation and design in the industrial process.The range of choice of microwave wavelength is 1 millimeter to 1 meter.Further say, among the set of wavelengths that its operation wavelength can be made up of following 4 wavelength optional one: 33cm, 16.7cm, 15.8cm, 12cm, reason is that these several wavelength are used very general in the microwave communication industry, microwaves corresponding hardware device and signal processing chip have very high cost performance owing to consumption is huge, corresponding data processing algorithm and software are abundant unusually especially, as long as on device, carry out shielding work for the external microwave signal, prevent external interference, great potential has been given play in these hardware and softwares this field of flow detection of just can migrating easily rapidly.Another preferred version of wavelength is 3cm, and reason is that the salinity of water when being lower than this frequency range is bigger to testing result influence, be higher than this frequency range then the aforementioned mixed structure in the fluid reflex of signal is strengthened the accuracy that influence detects.In the present embodiment, microwave wavelength is elected 15.8cm as.
As seen, this microwave phase fraction detecting device comprises two microwave antennas 14,15 among Fig. 5.The microwave signal that microwave signal source 31 is produced exports electronic installation 36 and microwave antenna 14 respectively to, microwave antenna 14 is used for the launched microwave signal, microwave antenna 15 is used to receive microwave signal and outputs it to electronic installation 36, in this electronic installation inside, two microwave signals are connected to two input ends of the AD8302 chip of ANALOG DEVICES company respectively, this chip is special-purpose high-frequency signal strength and phase place comparable chip, only be required to be this chip 5V is provided power supply, can carry out the comparison of intensity and phase place to the high frequency electrical signal that is connected two pin, and comparative result is converted to the voltage signal of two 0.03V to 1.8V, offer the analog to digital conversion circuit of electronic installation inside again, so that this analog quantity is gathered preservation and computing.
The 3rd, to compare with embodiment 2, change has taken place in the locus of ultrasound wave phase fraction detecting device.A transversal section cut-open view of embodiment 4 as shown in Figure 6, among the figure as seen, this ultrasound wave phase fraction detecting device and aforementioned microwave phase fraction detector arrangement are in same xsect, and can not the phase mutual interference and the precondition that allows of locus under, effective surveyed area of these two phase fraction detecting devices is positioned to overlapped as far as possible covering, that is effective surveyed area center line of these two phase fraction detecting devices intersects at a point at the center of sense channel, and the angle between these two center lines is reduced as far as possible.Such structural design makes each section fluid in the flow channel when flowing through this position, can obtain the detection of these two phase fraction detecting devices at synchronization.
This configuration of embodiment 4 can be used to detect oil-gas-water three-phase flow; Its testing process is similar to embodiment 2.
It is pointed out that the heterogeneous fluid of being made up of specific inductive capacity or the bigger one-tenth branch of density difference for other, this configuration of embodiment 4 also can realize each phase flow rate does not onlinely separate detection.And, at performance requirements such as precision is not very high, perhaps under the ability to bear condition of limited of price, embodiment 4 can also further be simplified, cancel the ultrasound wave phase fraction detecting device or the microwave phase fraction detecting device that are adopted in its technical scheme, only keep among both, can realize the flow detection of above-mentioned polyphasic flow equally.Difference in the testing process only is, also is cancelled corresponding to the every of phase fraction detecting device who is cancelled among the objective function M.
Fig. 7 is the structural representation of embodiments of the present invention 5, and as seen, the part-structure of this embodiment and embodiment 2 is identical among the figure, and this part identical structure no longer repeats at this, describes the difference of these two embodiments below in detail:
At first, increased back straight length 6, and back straight length 6 is changed into by preceding straight length 2 in the position of piezoelectric type dynamic pressure transducer 8 in the downstream of the back speed change pipeline section 5 of sense channel.Original two electric capacity phase fraction detecting devices and ultrasound wave phase fraction detecting device have been cancelled.And restriction device can be without the insulating material manufacturing.
Secondly, set up a laser phase fraction detecting device near the inside surface of back speed change pipeline section 5.Laser phase fraction detecting device is worked based on following principle: because laser has fabulous directivity, monochromaticity and coherence, the particle size analyzer that detects the molecule diameter adopts Principles of Laser usually.Under the situation of polyphasic flow, if the phase particle among the polyphasic flow is tiny and in flow process mixing ratio more even, use laser to carry out phase fraction so and detect and can reach reasonable effect equally.The ultimate principle of laser phase fraction detecting device is to produce the tested heterogeneous fluid of laser beam irradiation, because molecule has scattering process for laser, particle is many more on the path that laser passed, then final detected laser intensity is more little, and this intensity has promptly reflected the size of granule density that is phase fraction.
The 3rd, also set up an X ray phase fraction detecting device near the inside surface of throat 4, comprise x-ray source 27 and X-ray detector 28.X ray be meant wavelength at 30nm to the electromagnetic wave between the 0.01nm.Obtained immediately after short wavelength and extremely strong penetration capacity make it be found to use widely, become the strong instrument of medical diagnosis.Similar to gamma rays, its intensity can weaken equally when X ray passed medium.Detect by intensity, just can obtain the average density information on the X ray path, and then draw phase fraction information the X ray that passes heterogeneous fluid.
Among Fig. 7 as seen, can not the phase mutual interference and the precondition that allows of locus under, effective surveyed area of X ray phase fraction detecting device and laser phase fraction detecting device is that the flow direction along fluid closely is adjacent to be arranged in parallel in the same axial cross section, and the spacing between effective surveyed area center line of two phase fraction detecting devices is reduced as far as possible.Such structural design makes each section fluid in the flow channel when flowing through this position, can obtain the detection of these two phase fraction detecting devices in the shortest time successively.
This configuration of embodiment 5 can be used for the detection of coal dust gas stream, grain gas stream and chemical industry powder gas stream.Its testing process with
Embodiment 2 is similar.
It is pointed out that for other by the heterogeneous fluid that density or the bigger one-tenth branch of granularity difference are formed, this configuration of embodiment 5 also can detect.And, at performance requirements such as precision is not very high, perhaps under the ability to bear condition of limited of price, embodiment 5 can also further be simplified, cancel the laser phase fraction detecting device or the X ray phase fraction detecting device that are adopted in its technical scheme, only keep among both, can realize the flow detection of above-mentioned polyphasic flow equally.Difference in the testing process only is, also is cancelled corresponding to the every of phase fraction detecting device who is cancelled among the objective function M.
Fig. 8 is the structural representation of embodiments of the present invention 6, and as seen, the part-structure of this embodiment and embodiment 2 is identical among the figure, and this part identical structure no longer repeats at this, describes the difference of these two embodiments below in detail:
At first, original ultrasound wave phase fraction detecting device is replaced by a gamma rays phase fraction detecting device near the inside surface of throat 4.To be the density of utilizing material detect for the influence of gamma rays gamma rays phase fraction detecting device.Gamma rays has very strong penetration capacity as a kind of electromagnetic wave that gives off in the atomic nucleus, is easy to realize non-cpntact measurement.When gamma rays passed material, owing to photoelectric effect and scattering effect cause weakening of transmitted intensity, it weakens between the density of degree and material followed law of exponent.Gamma-ray densitometer utilizes this principle that the materials flow concentration in the various technological processes is measured, it is made up of following unit usually: gamma-ray source, photoelectric commutator, prime amplifier, signal processor etc., bore one timing when pipeline, materials flow concentration is big more, and the final intensity of gamma rays is just more little.This gamma-ray densitometer is widely applied in industry member already, has obtained good effect.In the present embodiment, after the gamma rays that gamma-ray source 29 is produced passes fluid, its intensity will change, and this Strength Changes can be detected by gamma detector 30 and obtain.The size of this intensity directly reflects the hybrid density size of heterogeneous fluid, and the size of the size of hybrid density and heterogeneous fluid phase fraction is directly related.
Secondly, cancelled near original two the electric capacity phase fraction detecting devices of throat's 4 inside surfaces, and near the inside surface of preceding speed change pipeline section 3, set up an electrical impedance phase fraction detecting device.Phase fraction detecting device based on electrical impedance is to utilize the specific inductive capacity of material and resistivity contrasts to detect.Import the high frequency pumping voltage of 30KHz to 300MHz in the pipeline both sides of heterogeneous fluid by electrode, electric current between the detecting electrode can obtain the situation of change of specific inductive capacity and resistivity, if the specific inductive capacity of each phase or resistivity difference are bigger in the heterogeneous fluid, can obtain phase fraction for information about so in view of the above.To the phase fraction detecting device based on electrical impedance or electric capacity, the range of choice of driving voltage frequency is generally 30KHz to 300MHz.In the present embodiment, the frequency of driving voltage is elected 30KHz as.The pair of electrodes that is made of electrode 23,24 embeds the inside surface of throat 4, and two electrodes are arranged symmetrically in the axial line both sides of fluid flowing passage.
After electrode embedded, the inside surface of speed change pipeline section 3 still kept previous shape before should guaranteeing after embedding two electrodes as far as possible, and can not influence fluid flowing through preceding speed change pipeline section 3.Two electrodes are connected to electronic installation 36 by cable, in this electronic installation inside, these two electrodes are connected to the AD5933 chip of an ANALOG DEVICES company, this chip is special-purpose electrical impedance-digital quantity conversion chip, only be required to be this chip 5V is provided power supply, the impedance value that gets final product between the electrode that will be connected two pin directly is converted to real part and two digital quantities of imaginary part, and these two digital quantities are offered the data processing circuit of electronic installation inside by the I2C interface, preserve and computing so that gather.
Among Fig. 8 as seen, can not the phase mutual interference and the precondition that allows of locus under, effective surveyed area of gamma rays phase fraction detecting device and electrical impedance phase fraction detecting device is that the flow direction along fluid closely is adjacent to be arranged in parallel in the same axial cross section, and the spacing between effective surveyed area center line of two phase fraction detecting devices is reduced as far as possible.Such structural design makes each section fluid in the flow channel when flowing through this position, can obtain the detection of these two phase fraction detecting devices in the shortest time successively.
Fig. 9 is a transversal section cut-open view of embodiments of the present invention 6, and this transversal section is to get along C-C hatching line shown in Figure 8; Can be clear that the relative position of electrode pair 23,24 among the figure.
This configuration of embodiment 6 can be used for the detection of coal water mixture and paper pulp.Its testing process is similar to embodiment 2.
It is pointed out that the heterogeneous fluid of being made up of specific inductive capacity or the bigger one-tenth branch of density difference for other, this configuration of embodiment 6 also can realize each phase flow rate does not onlinely separate detection.And, at performance requirements such as precision is not very high, perhaps under the ability to bear condition of limited of price, embodiment 6 can also further be simplified, cancel the gamma rays phase fraction detecting device or the electrical impedance phase fraction detecting device that are adopted in its technical scheme, only keep among both, can realize the flow detection of above-mentioned polyphasic flow equally.Difference in the testing process only is, also is cancelled corresponding to the every of phase fraction detecting device who is cancelled among the objective function M.
Figure 10 is the structural representation of embodiments of the present invention 7, among the figure as seen, the part-structure of this embodiment and embodiment 1 is identical, this part identical structure no longer repeats at this, the difference of these two embodiments is, on the tube wall of restriction device, at dynamic pressure transducer 8,9 separately in the xsect at place, opened a tracting pressuring hole respectively, and between these two tracting pressuring holes, connect a differential pressure pick-up 35 by impulse pipeline 32, be used for the detection of throttling differential pressure.The output signal of this differential pressure pick-up is connected to electronic installation 36 through cable.This electronic installation can as to the output signal of dynamic pressure transducer 8,9 to the output signal of differential pressure pick-up 35 gather, storage and computing.
This configuration of embodiment 7 can be used for the occasion that any needs accurately detect the full detail of throttling differential pressure, and said here full detail comprises throttling differential pressure fluctuation value and throttling differential pressure mean value.Though having analyzed, the front illustrated that traditional differential pressure pick-up can carry out highly effective detection to throttling differential pressure mean value, but because the restriction of frequency response can't effectively detect the HFS of throttling differential pressure fluctuation value medium frequency above 5KHz usually.Yet because dynamic pressure transducer 8,9 has been arranged, throttling differential pressure fluctuation value and throttling differential pressure mean value can effectively be detected simultaneously in the present embodiment.
Suppose that differential pressure pick-up 35 is selected for use and can effectively detect the differential pressure pick-up of frequency that for differential pressure pick-up commonly used, under the duty of low resistance, the overwhelming majority can both satisfy this requirement at the following differential pressure signal of 100Hz; Dynamic pressure transducer 8,9 is selected for use and can effectively be detected the piezoelectric type dynamic pressure transducer of frequency at 100Hz to 50KHz dynamic pressure signal.In electronic installation 36, the low-pass filter that is 100Hz with a cutoff frequency carries out filtering to the testing result of differential pressure pick-up 35, the Hi-pass filter that is 100Hz with a cutoff frequency carries out filtering to the difference of the testing result of dynamic pressure transducer 8,9 simultaneously, then with above-mentioned two filtering results added, like this, just obtained a bandwidth and be 0 to 50KHz throttling differential pressure testing result.This result compares with the testing result of independent use differential pressure pick-up 35, and its effective band has expanded to 0 to 50KHz from 0 to 100Hz, this be at present other detection means can't realize.The throttling differential pressure fluctuation information that this result comprised is horn of plenty more obviously, and can carry out flow rate calculation according to throttling differential pressure mean value and throttling differential pressure fluctuation value respectively, more resulting two result of calculations be checked mutually so that realize the fault self-diagnosis function of flow detector.If orifice plate stops up, very big difference will appear at this moment above-mentioned two result of calculations.Therefore, when appearring in flow detector, similar problem just can find in time that final flow detection result also just more accurately and reliably.
This configuration of embodiment 7 can be used to water water vapour, easily liquid gas stream and the easily detection of gasifying liquid stream.Its testing process with
Embodiment 2 is similar.
Because Fig. 3 has selected the phase fraction detecting device for use to embodiment shown in Figure 9, further introduce the scope of application of various phase fraction detecting devices commonly used in the present industrial process below.Table 1 has been listed the expection result of use of aforementioned 8 kinds of phase fraction detecting devices at common heterogeneous fluid in following 10 kinds of industrial processs: band water vapour stream, band water-setting gassing stream, the gas stream that is easy to liquefy, the flow of liquid that is easy to vaporize, oil-gas-water three-phase flow, coal dust gas stream, grain gas stream, chemical industry powder gas stream, coal water mixture, paper pulp.A kind of heterogeneous fluid of each row representative in the form, a kind of phase fraction detecting device of each row representative, "+" expression in the form is suitable fully, and " zero " expression part is suitable for, and "-" expression is difficult to be suitable for.
By in the table 1 as seen, because band water vapour stream, band water-setting gassing stream, the gas stream that is easy to liquefy, these 5 kinds of heterogeneous fluids of flow of liquid that is easy to vaporize and chemical industry powder gas stream comprise the different forms that exist of material of the same race usually, often difference is bigger and material exists specific inductive capacity under the form and resistivity in difference, and fluid ratio is purer, dirty impurity content is little, therefore 8 kinds of phase fraction detecting devices can be suitable for basically, just, cause ultrasound wave phase fraction detecting device can not be used for the detection of high-temperature water vapor because ultrasonic transducer still is difficult to tolerate the above high temperature of 200 degree at present.
The Expected Results of the various phase fraction detector applies of table 1. when different polyphasic flow
Band water vapor stream Band water-setting gassing stream Easy liquefied gas fluid Easily gasifying liquid flows Oil-gas-water three-phase flow The coal dust gas stream The grain gas stream Chemical industry powder air-flow Coal water mixture Paper pulp
Electric capacity + + + + ○ ○ ○ + - -
Electrical impedance - - - ○ ○ - - - ○ ○
Ultrasound wave - - ○ + + ○ ○ + + +
Microwave + + ○ ○ + ○ ○ + - -
Infrared ray + + - - ○ - - - - -
Laser + ○ + - - + ○ + - -
X ray ○ ○ ○ ○ + ○ ○ ○ ○ ○
Gamma rays ○ ○ ○ ○ + ○ ○ ○ ○ ○
For the oil gas water three phase fluid, what situation was slightly different is that often content is bigger owing to the dirty medium in the fluid, causes infrared ray and laser phase fraction detecting device to be difficult to be suitable for, and X ray and gamma rays phase fraction detecting device are especially suitable simultaneously; In addition, because the salinity of water might change and may become external phase, this brings difficulty can for again the use of electrical impedance and electric capacity phase fraction detecting device.
Coming and go of moisture limited being suitable for of electrical impedance, electric capacity, microwave and infrared ray phase fraction detecting device greatly in coal dust gas stream and the grain gas stream, and for coal water mixture and paper pulp, similar restriction has been played in the existence of a large amount of aqueous waters and partial impurities.
It should be noted that, see that from table 1 as if X ray and gamma rays phase fraction detecting device are blanket selections, but in actual production environment, because the existence of problems such as its higher cost and radioactivity, safety, energy consumption, environmental protection, the popularization of its application has been subjected to very big restriction.By contrast, the more worth user of electric capacity and ultrasound wave phase fraction detecting device considers to select for use.
In addition, it must be noted that, when accuracy of detection requires to contain gas in the very high or detected fluid, need measure static pressure and temperature simultaneously, and calculate and make corresponding pressure, temperature correction, so just can obtain the flow number under the standard state at this.This is the known basic general knowledge of technician in the field of flow detection.Specific to flow detector of the present invention, if other link of whole tubing can not provide this static pressure and temperature information, so just need on described flow detector, set up corresponding static pressure transducer and temperature sensor, static pressure and temperature are detected and be used for corrected Calculation.Because this feature belongs to the known basic general knowledge of technician in the field of flow detection, thus in technical scheme of the present invention and the claims all less than technical characterictic that this feature be can be regarded as described flow detector.
The present invention is not limited to above-mentioned several embodiments.Should be pointed out that ultimate principle of the present invention is to adopt two or more dynamic pressure transducers to detect for throttling differential pressure fluctuation value, and realize the detection of fluid flow as main foundation with this.For the person of ordinary skill of the art, under the prerequisite that does not break away from above-mentioned ultimate principle, can also make some modification and improvement, for example: restriction device is except the restriction device of used orifice plate and similar Venturi tube in the embodiment, also can select nozzle, inner conical throttling element and other non-standard restriction device, as long as reach the purpose that changes rate of flow of fluid; Because each embodiment finally all is converted to extreme value with the flow detection problem and finds the solution problem, near so another additional restriction device of the upstream and downstream of described flow detector, also can connecting again, resulting various additional detected results introduce in the electronic installation of described flow detector on the restriction device that this is additional, and in objective function, add and comprise these additional detected result's corresponding entry, so that improve the detection effect of described flow detector; The piezoelectric transducer of dynamic pressure transducer except using in the present embodiment, also can select other to detect the sensor of principle based on acoustic vibration, for example inner for coil adds the acoustic vibration sensor of permanent magnet structure and fibre optic compression sensor etc., as long as reach the purpose of accurate detection high-frequency pressure undulate quantity value; The various phase fraction detecting devices of phase fraction pick-up unit except using in the present embodiment also can be selected other forms of phase fraction detecting device, as long as signal of sensor changes along with the variation of a certain phase concentration in the heterogeneous fluid.Because above-mentioned these modification all are based upon on the identical ultimate principle with improving, and therefore all should drop within protection scope of the present invention.

Claims (12)

1. the flow detector of a fluid, the sense channel of this flow detector is the airtight passage that an intersegmental part has fluid to flow, on this sense channel, arrange 1 sensor combinations, this sensor combinations is made up of 2 sensors at least, at least 2 signal of sensor in this sensor combinations are introduced in 1 electronic installation, realize asking for of fluid flow by this electronic installation rice, the feature of described flow detector is:
1) comprise 2 dynamic pressure transducers in the described sensor combinations at least, this dynamic pressure transducer is to design for the fluctuation situation of detected pressures accurately and efficiently, thereby is difficult to the stable state numerical value of detected pressures accurately and effectively;
2) have at least 2 dynamic pressure transducers to be spaced a distance and to arrange along fluid flow direction;
3) between 2 dynamic pressure transducers arranging being spaced a distance along fluid flow direction, there is variation in the cross-sectional area of sense channel, and therefore corresponding change has also taken place flow rate of fluid.
2. flow detector as claimed in claim 1, it is characterized in that: described flow detector also comprises 1 differential pressure pick-up, and on sense channel, two pressure ports that this differential pressure pick-up connected are arranged in the xsect that dynamic pressure transducer is installed.
3. flow detector as claimed in claim 1, it is characterized in that: near the position of the cross-sectional area minimum of sense channel, also be furnished with 1 phase fraction detecting device, this phase fraction detecting device is by applying the way of driving voltage or exciting current, detect for existing electric capacity or electrical impedance between two electrodes that are arranged in the sense channel both sides, reaching the purpose that detects phase fraction, and the frequency of operation of used driving voltage of this detection or exciting current is selected between the 30KHz to 300MHz.
4. flow detector as claimed in claim 1, it is characterized in that: near the position of the cross-sectional area minimum of sense channel, also be furnished with 1 phase fraction detecting device, Strength Changes when this phase fraction detecting device passes fluid to ultrasound wave or flight time change to be detected, to reach the purpose that detects phase fraction, and when in the detected fluid during air inclusion, hyperacoustic frequency of operation is selected between the 0.5MHz to 5MHz, when in the detected fluid not during air inclusion, hyperacoustic frequency of operation is selected between the 2.0MHz to 20MHz.
5. flow detector as claimed in claim 1, it is characterized in that: near the position of the cross-sectional area minimum of sense channel, also be furnished with 1 phase fraction detecting device, Strength Changes when this phase fraction detecting device passes fluid to electromagnetic wave detects, reaching the purpose that detects phase fraction, described electromagnetic wave is any one among the electromagnetic wave group formed of following 5 kinds of electromagnetic waves: microwave, infrared ray, laser, X ray, gamma rays.
6. flow detector as claimed in claim 5, it is characterized in that: described electromagnetic wave belongs to microwave frequency band, among the set of wavelengths that its operation wavelength is made up of following 5 wavelength any one: 33cm, 16.7cm, 15.8cm, 12cm, 3cm, and the phase change when described phase fraction detecting device also passes fluid to described electromagnetic wave detects, to reach the purpose that detects phase fraction.
7. flow detector as claimed in claim 5, it is characterized in that: described electromagnetic wave belongs to the infrared ray frequency range, and among the set of wavelengths be made up of following 5 wavelength of its operation wavelength any one: 1.2 microns, 1.45 microns, 1.94 microns, 2.8 microns, 6 microns.
8. flow detector as claimed in claim 1, it is characterized in that: comprise 2 phase fraction detecting devices at least, these phase fraction detecting devices are to select for use arbitrarily from the detector set that following 8 kinds of phase fraction detecting devices are formed: ultrasonic detector, capacitance detector, electrical impedance detecting device, microwave detector, infrared detector, laser detector, X-ray detector, gamma ray detector; Selected detecting device has same or different principle of work, and has same or different operation wavelength; Selected phase fraction detecting device centralized arrangement is near the position of the cross-sectional area minimum of sense channel; Simultaneously, described phase fraction detecting device can the phase mutual interference and the precondition that allows of locus under, the center line of effective surveyed area of at least 2 phase fraction detecting devices is intersected at a point at the center of sense channel, and reduce the angle between these two center lines as far as possible.Like this, the overlapped covering of effective surveyed area of these phase fraction detecting devices makes each section fluid in the sense channel when flowing through this position, can obtain the detection of these phase fraction detecting devices at synchronization.
9. flow detector as claimed in claim 1, it is characterized in that: comprise 2 phase fraction detecting devices at least, these phase fraction detecting devices are to select for use arbitrarily from the detector set that following 8 kinds of phase fraction detecting devices are formed: ultrasonic detector, capacitance detector, electrical impedance detecting device, microwave detector, infrared detector, laser detector, X-ray detector, gamma ray detector; Selected detecting device has same or different principle of work, and has same or different operation wavelength; Selected phase fraction detecting device centralized arrangement is near the position of the cross-sectional area minimum of sense channel; Simultaneously, described phase fraction detecting device can the phase mutual interference and the precondition that allows of locus under, as far as possible effective surveyed area of at least 2 selected phase fraction detecting devices flow direction along fluid closely is adjacent to be arranged in parallel in side by side in the same axial cross section, and reduces spacing between the center line of these two effective surveyed areas as far as possible.Like this, section fluid of each in the sense channel just can obtain the detection of these phase fraction detecting devices successively in the shortest time when flowing through this position.
10. as each described flow detector in the claim 1 to 9, it is characterized in that: the long-pending constant throat of flow channel cross that described sense channel comprises at least 1 speed change pipeline section and is adjacent, moving cross-sectional area has taken place to change and has caused rate of flow of fluid to increase or reduce at this speed change pipeline section upper reaches, and this velocity variation tube section is positioned between the installation position of described 2 dynamic pressure transducers.
11. as each described flow detector in the claim 1 to 9, it is characterized in that: described dynamic pressure transducer is based on the dynamic pressure transducer that crystal piezoelectric principle, piezoelectric ceramics principle, coil add permanent magnet principle or optical fiber measurement principle.
12. flow detector as claimed in claim 10 is characterized in that: described dynamic pressure transducer is based on the dynamic pressure transducer that crystal piezoelectric principle, piezoelectric ceramics principle, coil add permanent magnet principle or optical fiber measurement principle.
CNB2005100443975A 2005-08-10 2005-08-10 Fluid flow rate detector Expired - Fee Related CN1332183C (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CNB2005100443975A CN1332183C (en) 2005-08-10 2005-08-10 Fluid flow rate detector
PCT/CN2006/001977 WO2007016865A1 (en) 2005-08-10 2006-08-04 A flow measuring device of a stream

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2005100443975A CN1332183C (en) 2005-08-10 2005-08-10 Fluid flow rate detector

Publications (2)

Publication Number Publication Date
CN1731105A true CN1731105A (en) 2006-02-08
CN1332183C CN1332183C (en) 2007-08-15

Family

ID=35963502

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2005100443975A Expired - Fee Related CN1332183C (en) 2005-08-10 2005-08-10 Fluid flow rate detector

Country Status (2)

Country Link
CN (1) CN1332183C (en)
WO (1) WO2007016865A1 (en)

Cited By (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102305645A (en) * 2011-07-26 2012-01-04 河北大学 Gas-liquid phase flow measurement device
CN102749111A (en) * 2012-07-24 2012-10-24 兰州海默科技股份有限公司 Wet gas flow measuring method and device
CN103175578A (en) * 2013-03-06 2013-06-26 中国计量学院 Device based on measurement of capacitance pore plate flow and measurement of electromagnetic flow
CN103292849A (en) * 2013-03-25 2013-09-11 兰州海默科技股份有限公司 Device and method for online measurement of gas-phase flux and liquid-phase flux of moisture in horizontal pipe
CN103453947A (en) * 2012-05-29 2013-12-18 罗斯蒙德公司 Differential pressure transmitter with redundant sensors
CN103808379A (en) * 2012-11-14 2014-05-21 丹尼尔测量和控制公司 System and method for ultrasonic metering using an orifice meter fitting
CN104089985A (en) * 2014-07-10 2014-10-08 天津大学 Visual multiphase flow test method based on electric and ultrasonic sensing principle
CN104121955A (en) * 2014-07-24 2014-10-29 西安交通大学 Liquid-liquid two-phase fluid flow measurement device and method based on phase separation and ultrasonic technologies
CN104198328A (en) * 2014-09-09 2014-12-10 深圳市奥电高压电气有限公司 Equipment and method for measuring volume occupancy of steam bubbles in two-phase fluid
CN104567986A (en) * 2013-10-11 2015-04-29 中国人民解放军第二炮兵工程大学 FBG (fiber bragg grating)-based multifunctional flow sensor provided with embedded standard nozzle
CN104952323A (en) * 2015-06-12 2015-09-30 浙江大学 Self-circulation Bernoulli experimental device with teaching effect flow digital display function
CN105181040A (en) * 2015-09-25 2015-12-23 辽宁聚焦科技有限公司 Method for digitized calibration and optimization of difference pressure flow meter
CN106422016A (en) * 2016-11-30 2017-02-22 四川大学 Mouse non-invasive trachea intubation instrument
CN106813758A (en) * 2017-02-22 2017-06-09 苏州市计量测试研究所 A kind of flow measurement device for borne bacteria sampler
CN106841669A (en) * 2015-12-04 2017-06-13 无锡乐华自动化科技有限公司 A kind of elastic strain formula pipe flow speed sensor and application method
CN107219239A (en) * 2017-06-12 2017-09-29 默斯测控技术（长沙）有限公司 Microwave measurement for moisture content method, device, equipment and storage medium
CN107469207A (en) * 2017-03-23 2017-12-15 北京怡和嘉业医疗科技股份有限公司 Device for storing liquid and lung ventilator
CN108412481A (en) * 2018-03-05 2018-08-17 中国石油天然气股份有限公司 Supersonic Doppler multiphase flow separate phase flow rate interpretation of logging data method and apparatus
CN108693379A (en) * 2018-07-10 2018-10-23 湖北文索光电科技有限公司 fiber grating ocean current detection sensor and ocean current detection system
CN108955787A (en) * 2017-05-17 2018-12-07 比尔克特韦尔克有限及两合公司 measuring device
CN109141553A (en) * 2017-06-19 2019-01-04 克洛纳有限公司 For determining flow sensor, method and the flowrate measuring tool of the speed of the phase of multiphase medium
CN110006544A (en) * 2019-04-11 2019-07-12 西安培华学院 A kind of telescopic temperature sensor
CN110662946A (en) * 2018-03-28 2020-01-07 株式会社木幡计器制作所 Flow rate measuring device and flow rate measuring method
CN110706835A (en) * 2019-10-16 2020-01-17 中广核工程有限公司 Detection device and method for analyzing non-contact flow based on stress difference
CN111505024A (en) * 2020-06-08 2020-08-07 中国电子科技集团公司第四十八研究所 Moisture content composite detection device and detection method based on microwave technology
CN111595395A (en) * 2020-05-08 2020-08-28 中国矿业大学 Accurate tunnel air volume monitoring system and method
CN112179592A (en) * 2020-09-02 2021-01-05 四川虹美智能科技有限公司 Refrigeration system detection method, device and readable medium
CN112218727A (en) * 2018-03-14 2021-01-12 卡莱尔液体科技(英国)公司 Flow balance in coating circulation systems
CN112452565A (en) * 2020-11-02 2021-03-09 海默新宸水下技术(上海)有限公司 Cyclone for multiphase flow measurement and measurement system
CN113029259A (en) * 2021-02-02 2021-06-25 辽宁工程技术大学 Gas-liquid two-phase flow measuring device based on microwave and rectangular flowmeter, internal transmission line arrangement method and flow measuring method

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8099476B2 (en) 2008-12-31 2012-01-17 Apple Inc. Updatable real-time or near real-time streaming
DE102014205040A1 (en) * 2014-03-19 2015-10-29 Robert Bosch Gmbh Flow meter and method for a flow meter
WO2017005268A1 (en) * 2015-07-03 2017-01-12 Kamstrup A/S Turbidity sensor based on ultrasound measurements
EP3948104A4 (en) * 2019-04-04 2023-04-26 Services Pétroliers Schlumberger Geothermal production monitoring systems and related methods
CN110595551A (en) * 2019-10-11 2019-12-20 无锡洋湃科技有限公司 Photon detection system, calculation method thereof and photon multiphase bidirectional flowmeter adopting system
US11506556B2 (en) 2020-09-30 2022-11-22 Rosenmount Inc. Single-use plastic pressure sensor

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1023952C (en) * 1988-02-15 1994-03-09 胜利油田采油工艺研究院 Method for measuring flow and aridity of double-phase fluid containing steam (gas) and liquid
CN1021083C (en) * 1989-01-03 1993-06-02 浙江大学 Gas-liquid fixed double phase flow measuring method
CN1018385B (en) * 1990-02-27 1992-09-23 机械电子工业部重庆工业自动化仪表研究所 Differential pressure type mass flowmeter for vortex street
US5031466A (en) * 1990-05-29 1991-07-16 Texaco Inc. Method and apparatus for determining steam quality and mass flow rate
TW283763B (en) * 1992-10-06 1996-08-21 Caldon Inc
JP3800691B2 (en) * 1996-10-03 2006-07-26 一平 鳥越 Source mass flow meter
CN1240930A (en) * 1998-06-25 2000-01-12 安德雷斯和霍瑟·弗罗泰克有限公司 Vortex flow sensor
CN2325762Y (en) * 1998-06-29 1999-06-23 中国核动力研究设计院 Device for measuring small amount of flow
CN2349553Y (en) * 1998-07-28 1999-11-17 窦剑文 Gas-liquid polyphase flow flowmeter
JP2000283810A (en) * 1999-03-31 2000-10-13 Miura Co Ltd Differential pressure type flowmeter
CN2606882Y (en) * 2003-03-25 2004-03-17 天津凯斯通能源技术有限公司 Flow and dryness measurer for vapour/liquid or gas/liquid double phase fluid
CN1268901C (en) * 2004-06-29 2006-08-09 浙江大学 Vertex mass and flow measuring method

Cited By (48)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102305645A (en) * 2011-07-26 2012-01-04 河北大学 Gas-liquid phase flow measurement device
CN102305645B (en) * 2011-07-26 2013-09-11 河北大学 Gas-liquid phase flow measurement device
US9200932B2 (en) 2012-05-29 2015-12-01 Rosemount Inc. Differential pressure transmitter with redundant sensors
CN103453947B (en) * 2012-05-29 2016-12-07 罗斯蒙特公司 There is the pressure difference transmitter of redundant sensor
CN103453947A (en) * 2012-05-29 2013-12-18 罗斯蒙德公司 Differential pressure transmitter with redundant sensors
CN102749111A (en) * 2012-07-24 2012-10-24 兰州海默科技股份有限公司 Wet gas flow measuring method and device
CN103808379A (en) * 2012-11-14 2014-05-21 丹尼尔测量和控制公司 System and method for ultrasonic metering using an orifice meter fitting
US9366556B2 (en) 2012-11-14 2016-06-14 Daniel Measurement And Control, Inc. Method for ultrasonic metering using an orifice meter fitting
CN103175578A (en) * 2013-03-06 2013-06-26 中国计量学院 Device based on measurement of capacitance pore plate flow and measurement of electromagnetic flow
US10126156B2 (en) 2013-03-25 2018-11-13 Haimo Technologies Group Corp. Device and method for online measurement of gas flowrate and liquid flowrate of wet gas in horizontal pipe
WO2014194729A1 (en) * 2013-03-25 2014-12-11 兰州海默科技股份有限公司 Device and method for online measurement of gas-phase flux and liquid-phase flux of moisture in horizontal pipe
CN103292849A (en) * 2013-03-25 2013-09-11 兰州海默科技股份有限公司 Device and method for online measurement of gas-phase flux and liquid-phase flux of moisture in horizontal pipe
CN103292849B (en) * 2013-03-25 2015-12-23 兰州海默科技股份有限公司 The gas phase flow rate of moisture and the device and method of liquid phase flow in a kind of on-line measurement horizontal tube
CN104567986A (en) * 2013-10-11 2015-04-29 中国人民解放军第二炮兵工程大学 FBG (fiber bragg grating)-based multifunctional flow sensor provided with embedded standard nozzle
CN104089985A (en) * 2014-07-10 2014-10-08 天津大学 Visual multiphase flow test method based on electric and ultrasonic sensing principle
CN104121955B (en) * 2014-07-24 2017-02-15 西安交通大学 Liquid-liquid two-phase fluid flow measurement device and method based on phase separation and ultrasonic technologies
CN104121955A (en) * 2014-07-24 2014-10-29 西安交通大学 Liquid-liquid two-phase fluid flow measurement device and method based on phase separation and ultrasonic technologies
CN104198328A (en) * 2014-09-09 2014-12-10 深圳市奥电高压电气有限公司 Equipment and method for measuring volume occupancy of steam bubbles in two-phase fluid
CN104952323A (en) * 2015-06-12 2015-09-30 浙江大学 Self-circulation Bernoulli experimental device with teaching effect flow digital display function
CN104952323B (en) * 2015-06-12 2017-08-08 浙江大学 Possesses self-loopa Bernoulli Jacob's experimental provision of teaching efficiency flow digital display
CN105181040A (en) * 2015-09-25 2015-12-23 辽宁聚焦科技有限公司 Method for digitized calibration and optimization of difference pressure flow meter
CN105181040B (en) * 2015-09-25 2018-10-23 辽宁聚焦科技有限公司 A kind of digitalized calibration and optimization method of differential pressure flowmeter
CN106841669A (en) * 2015-12-04 2017-06-13 无锡乐华自动化科技有限公司 A kind of elastic strain formula pipe flow speed sensor and application method
CN106422016A (en) * 2016-11-30 2017-02-22 四川大学 Mouse non-invasive trachea intubation instrument
CN106813758A (en) * 2017-02-22 2017-06-09 苏州市计量测试研究所 A kind of flow measurement device for borne bacteria sampler
CN107469207A (en) * 2017-03-23 2017-12-15 北京怡和嘉业医疗科技股份有限公司 Device for storing liquid and lung ventilator
CN108955787A (en) * 2017-05-17 2018-12-07 比尔克特韦尔克有限及两合公司 measuring device
CN108955787B (en) * 2017-05-17 2021-01-08 比尔克特韦尔克有限及两合公司 Measuring device
CN107219239B (en) * 2017-06-12 2019-12-31 默斯测控技术（长沙）有限公司 Microwave moisture measuring method, device, equipment and storage medium
CN107219239A (en) * 2017-06-12 2017-09-29 默斯测控技术（长沙）有限公司 Microwave measurement for moisture content method, device, equipment and storage medium
CN109141553A (en) * 2017-06-19 2019-01-04 克洛纳有限公司 For determining flow sensor, method and the flowrate measuring tool of the speed of the phase of multiphase medium
CN109141553B (en) * 2017-06-19 2022-08-12 克洛纳有限公司 Flow sensor, method and flow measuring device for determining the speed of phases of a multi-phase medium
CN108412481A (en) * 2018-03-05 2018-08-17 中国石油天然气股份有限公司 Supersonic Doppler multiphase flow separate phase flow rate interpretation of logging data method and apparatus
CN112218727B (en) * 2018-03-14 2023-02-17 卡莱尔液体科技(英国)公司 Flow balance in a coating circulation system
CN112218727A (en) * 2018-03-14 2021-01-12 卡莱尔液体科技(英国)公司 Flow balance in coating circulation systems
CN110662946A (en) * 2018-03-28 2020-01-07 株式会社木幡计器制作所 Flow rate measuring device and flow rate measuring method
CN108693379A (en) * 2018-07-10 2018-10-23 湖北文索光电科技有限公司 fiber grating ocean current detection sensor and ocean current detection system
CN110006544A (en) * 2019-04-11 2019-07-12 西安培华学院 A kind of telescopic temperature sensor
CN110706835B (en) * 2019-10-16 2021-02-05 中广核工程有限公司 Detection device and method for analyzing non-contact flow based on stress difference
CN110706835A (en) * 2019-10-16 2020-01-17 中广核工程有限公司 Detection device and method for analyzing non-contact flow based on stress difference
CN111595395A (en) * 2020-05-08 2020-08-28 中国矿业大学 Accurate tunnel air volume monitoring system and method
CN111505024A (en) * 2020-06-08 2020-08-07 中国电子科技集团公司第四十八研究所 Moisture content composite detection device and detection method based on microwave technology
CN111505024B (en) * 2020-06-08 2023-07-04 中国电子科技集团公司第四十八研究所 Composite detection device and detection method for water content based on microwave technology
CN112179592B (en) * 2020-09-02 2022-05-24 四川虹美智能科技有限公司 Refrigeration system detection method, device and readable medium
CN112179592A (en) * 2020-09-02 2021-01-05 四川虹美智能科技有限公司 Refrigeration system detection method, device and readable medium
CN112452565A (en) * 2020-11-02 2021-03-09 海默新宸水下技术(上海)有限公司 Cyclone for multiphase flow measurement and measurement system
CN113029259A (en) * 2021-02-02 2021-06-25 辽宁工程技术大学 Gas-liquid two-phase flow measuring device based on microwave and rectangular flowmeter, internal transmission line arrangement method and flow measuring method
CN113029259B (en) * 2021-02-02 2023-06-16 辽宁工程技术大学 Gas-liquid two-phase flow measuring device based on microwaves and rectangular flowmeter, internal transmission line arrangement method and flow measuring method

Also Published As

Publication number Publication date
WO2007016865A1 (en) 2007-02-15
CN1332183C (en) 2007-08-15

Similar Documents

Publication Publication Date Title
CN1731105A (en) Fluid flow rate detector
CN102803908B (en) Do not stop fluid and flow through the transducer frequency adjustment measuring instrument
US7311143B2 (en) Method and apparatus for generation of acoustic shear waves through casing using physical coupling of vibrating magnets
US7607358B2 (en) Flow rate determination of a gas-liquid fluid mixture
US9050628B2 (en) Pulse-echo acoustic transducer
CN102667419B (en) Flowmeter and method
CN103994796B (en) The system for detecting the liquid in both acoustic flowmeters
CN101076709A (en) Device for determining and/or monitoring the volume and/or mass flow rate of a medium
CN1662793A (en) Method for determining rheological parameters of a fluid
CN102985816A (en) Ultrasonic particle measuring system
US20180328163A1 (en) Flexural Wave Measurement For Thick Casings
NO345791B1 (en) A Method of identifying a material and/or condition of a material in a borehole
CN110159253A (en) A kind of ultrasonic imaging logging method
US20170167253A1 (en) Apodization of Piezo-Composite Acoustic Elements
WO2016033534A1 (en) Acoustic interface device
CN102330551B (en) Method and system for rectifying sound wave pressure in sound wave amplitude well logging
CN1847801A (en) Acoustic Doppler well flowmeter
CN110196284A (en) A kind of multifrequency array probe device for large forgings detection
CN108917866A (en) A kind of ultrasonic sensor and its installation method for compound pipeline complex pipeline flow detection
GB2399411A (en) Cased borehole investigation apparatus deviates parasitic echoes away from receiver
CN1054484A (en) Differential pressure type mass flowmeter for vortex street
KR101135213B1 (en) Ultrasonic wave detector for ultrasonic flowmeter
CN102312670B (en) Method and system for correcting sound wave emitting voltage in sound wave amplitude logging
Sun et al. Design of multi-functional ultrasonic imaging logging tool
Nabipour et al. Methods for measurement of solid particles in hydrocarbon flow streams

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
DD01 Delivery of document by public notice

Addressee: Chen Yu

Document name: Notification to Pay the Fees

DD01 Delivery of document by public notice
DD01 Delivery of document by public notice

Addressee: Chen Yu

Document name: Notification to Pay the Fees

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070815

Termination date: 20160810