METHOD AND DEVICE FOR MONITORING OF A GAS FLOW, IN PARTICULAR OF A NATURAL-GAS FLOW

Abstract: Method and device for monitoring of the composition of a flowing gas. An oscillation of sound frequency is applied to the gas flow pipe (10) downstream and upstream, and the travel times (t1, t2) of the monitoring sound over a certain measurement distance (L) downstream and upstream are detected. The sound speed (c) or a quantity representing same is determined on the basis of said travel times (t1, t2). This speed (c) is mainly dependent on the average molecular weight of the gas to be monitored. The temperature (T) of the flowing gas is measured, and on the basis of the measurement of temperature, the sound speed that has been reduced to a certain reference temperature T0 is determined from the formula c0 = c . 2ROOT (T0/T), which is applicable to an ideal gas and wherein T = absolute measured temperature of the gas, T0 = chosen absolute reference temperature, c = measured sound speed, and c0 = sound speed reduced to the reference temperature, or by using a corresponding more realistic formula. When the reduced temperature (c0) differs from its range of expected values (c1...c2), an alarm signal or control signal is given. Alternatively, the limits (C1, C2) of the range of expected values can be reduced to temperature.

Description: Method and device for monitoring of a gas flow, in particular of a natural-gas flow The invention concerns a method for monitoring of the composition of a flowing gas, in which method acoustic oscillations are applied to the gas flow pipe downstream and upstream, and the travel times of the monitoring sound down¬ stream and upstream are detected, and the sound speed or a quantity represent- ing same is determined on the basis of said travel times, which speed or quantity is mainly dependent on the average molecular weight of the gas to be monitored. Further, the invention concerns a device for monitoring of the flow of a gas, in particular of natural gas. From the FI Patent No. 76,885 of the Technical Research Centre of Finland (Valtion tutkimuskeskus NTT), a method and a device of acoustic flow measure¬ ment are known for measurement of the flow velocities, volumetric flows, and/or mass flows of gases, liquids, and/or multi-phase suspensions in a pipe or in an equivalent wave tube by making use of acoustic waves passing downstream and upstream. In this prior-art method and device, the wide-band acoustic signal coming from the sound sources is made to pass in the measurement pipe or equivalent wave tube in the plane-wave mode both downstream and upstream, and the flow velocity is determined on the basis of the sound travel times obtained from the maxima and/or the minima of the correlation functions of the measured sound signals and on the basis of the mutual distance between the measurement points. In one technical solution described in said FI patent, the sound is fed into the measurement pipe in the form of frequency scanning, and the travel time of sound is determined from the signals of the microphones placed at the ends of the measurement distance by means of a polarity correlator. From the travel times measured downstream and upstream, it is possible to measure both the average flow velocity and the sound speed in a medium at rest with high accu¬ racy. Moreover, if necessary, from the flow velocity and from the cross-sectional area of the pipe, it is possible to calculate the volumetric flow rate. The gas flow velocity measured in accordance with said FI patent or in some other way is, as a rule, used as starting information, together with the temperature and the pressure of the gas, for calculation of the mass flow. Thus, as a rule, measure¬ ment of flow velocity is combined with measurement of gas temperature and pressure. Besides measurement of the flow velocity and of the mass flow, there is also a need for gas monitoring of other sorts, in particular for monitoring of the composition of the gas. Need for monitoring has occurred, e.g., in the case of natural gas, which is economically the most important source of energy in gas form. For example, natural gas may contain varying quantities of hydrogen, water vapour, or inert gases. As is known in prior art, the quality of natural gas is monitored by taking a sample from it and by examining the sample chromato- graphically, which requires expensive equipment, is laborious, and difficult to carry out automatically. Thus, there is a considerable need to provide such a method and device for monitoring of a gas, in particular of natural gas, as can give the alarm in the case of a significant change in the quality of the gas, in which case, if necessary, it would be possible to perform a closer analysis of the composition of the gas by means of chromatography. It is also necessary to monitor the composition of the gas to determine its combustion value for purposes of invoicing. It is known that the speed of sound in a gas depends mainly on the composition and temperature of the gas. The composition affects the speed of sound mainly by the intermediate of the average molecular weight, and to some extent also by the intermediate of the number of degrees of freedom in the molecules, i.e. of the number of atoms present in a molecule. The object of the present invention is to provide a novel advantageous method and device for monitoring of the flow of a gas, in particular of natural gas, and in particular for monitoring of the composition of the gas. . An object of the invention is to provide a method in which, besides on the flow velocity of the gas, information is also obtained on whether the composition of the gas remains homogeneous or whether variations occur in it, for example foreign gases, such as hydrogen, water vapour or atmospheric gases in natural gas. It is a particular object of the invention to provide a method that can be favour¬ ably connected to measurement of the flow velocity of a gas, in particular to an acoustic gas flow meter described in said FI Patent No. 76,885, wherein the sound travel times downstream and upstream are measured by means of the correlation technique, preferably by means of a polarity correlator. With respect to the prior art closely related to the present invention, reference is further made to the CH Patent No. 669,463 and to the US Patent No. 4,596,133, in which devices suitable for monitoring of a flowing gas are described, which devices are accomplished mainly by means of an ultrasonic technique and in which devices, however, it is an essential difference as compared with the present invention of ours that, in the cited patents, the acoustic energy has been arranged to pass across the flow pipe diagonally along a certain path, in which case the wave length of the sound must be substantially shorter than the diam- eter of the measurement pipe. It is a further difference in said cited patents, as compared with the devices of our invention, that, as is common in ultrasonic technology, the same detectors operate both as the transmitters and as the receivers of the monitoring sound. In view of achieving the objectives stated above and those that will come out later, the method of the invention is mainly characterized in that, in the method, the frequency of said acoustic oscillations is chosen below a certain limit fre- quency, so that the monitoring sound moves in the axial direction of the measur¬ ement pipe in the plane-wave mode, that the travel times of the monitoring sounds are detected over a measurement distance in the axial direction of the measurement pipe, which measurement distance is dimensioned substantially larger than the average diameter of the measurement pipe, and that, when said sound speed or the quantity representing same differs from its range of expected values, an alarm signal or some other control signal is given. On the other hand, the device in accordance with the invention is mainly characterized in that the device comprises a measurement pipe, in which the gas flow to be measured runs, and loudspeakers as the transmitters of the sound signals of audio frequency and microphones as the sound detectors, which microphones are placed in connection with the measurement pipe between said loudspeakers at a certain known distance, in the axial direction of the measure- ment pipe, from one another, which axial distance is substantially, preferably by one order, larger than the average diameter of the measurement pipe, that the device comprises units by whose means both the gas flow velocity and the speed of sound in the gas flow are determined, and that the device comprises an alarm unit, which is fitted to produce an alarm when the detected sound speed or the quantity representing same is above or below certain preset limit values. In the most advantageous embodiment of the invention, by means of the same devices, both the gas flow velocity and the speed of sound in the gas are measured acoustically. Moreover, it is also advantageous to measure the gas temperature and, in some cases, also the pressure. On the basis of the measure¬ ment of the temperature, the detected sound speed can be reduced to the preset reference temperature. On the basis of the monitoring of this reduced sound speed, alarm or any other control signal is given. In this way, the composition of the gas can be monitored, said composition affecting the sound speed mainly by the intermediate of the average molecular weight and, to some extent, also by the intermediate of the number of the degrees of freedom in the molecules. The permitted range of variation in the sound speed can be determined empirically and, if necessary, by means of reference measurements carried out chromato- graphically. The average value of the range of variation in sound speed per¬ mitted without alarm may illustrate, for example, an average or ideal quality of gas. In this connection, it should be ascertained that, above and in the following, gas is understood as also meaning a gas mixture consisting of different gases. In the following, the invention will be described in detail with reference to an exemplifying embodiment of the invention illustrated in the figure in the accom¬ panying drawing, the invention being in no way strictly confined to the details of said embodiment. The figure is a schematic illustration of a gas-flow monitoring device in accord- ance with the invention mainly as a block diagram. According to the figure, a gas flow that runs in the measurement pipe 10 is monitored acoustically. Typically, the gas to be monitored is natural gas. Into the measurement pipe 10, sound signals are transmitted by means of loudspeakers 13a and 13b downstream and upstream, which signals are received by means of microphones 14a and 14b placed between the loudspeakers 13a and 13b, the mutual distance L between the microphones being essential for the monitoring. The diameter D of the measurement pipe 10 and the measurement distance L are chosen, e.g., so that L « 10D. From the point of view of the measurement technology related to the invention, it is the most essential physical observation that in a pipe 10 with rigid walls, below a certain limit frequency which depends on the dimensions of the pipe 10, exclusively a so-called plane-wave mode or piston mode can proceed, whose speed of progress does not depend on local variations in the medium, in its temperature or flow velocity, but exclusively on the average values prevailing within the measurement distance (B. Robertson, "Effect of Arbitrary Tempera- ture and Flow Profiles on the Speed of Sound in a Pipe", J. Acoust. Soc. Am.. Vol 62, No.4, p.813...818, October 1977, and B. Robertson, "Flow and Tempera¬ ture Profile Independence of Flow Measurements Using Long Acoustic Waves", Transactions of the ASME. Vol. 106, p. 18...20, March 1984), which permits accurate flow measurement independent from the profile. For a pipe of circular section, said limit frequency f c can be calculated from the formula f c = c/(1.7 • D), (1) wherein c is the travel speed of sound in the medium that fills the pipe, and D is the diameter of the pipe 10. In the following, the most important formulae of calculation used in the flow monitoring in accordance with the invention will be given. Sound speed [m/s] c = 0.5 • L • t ~ + i£-) (2) Temperature-reduced sound speed [m/s] c 0 = c • J (T 0 /T) (3) How velocity [m/s] v = 0.5 * L • (t^ 1 - 1^ 1 ) (4) Volumetric flow [cu.m/s] Q = v • A (5) Mass flow [kg/s] M = Q • p (6) v = average flow velocity L = distance between microphones 14a and 14b t χ = travel time of sound downstream t 2 = travel time of sound upstream T 0 = reference temperature to which the sound speed c 0 has been reduced T = temperature of gas in the measurement pipe 10 Q = volumetric flow A = cross-sectional area of the pipe 10 M = mass flow p = density of gas According to the figure, the loudspeakers 13a and 13b are fed alternatingly with electric signals received from the scanning generator 12. The alternation of the feed of the loudspeakers 13a and 13b is controlled by means of a switch 18 controlled by the control unit 11 of frequency scanning. The receiving side of the acoustic measurement system comprises the above microphones 14a and 14b, placed at the measurement distance L from one another, the output signal of said microphones being fed, by the intermediate of the amplifiers 16a and 16b, to the scannable filters 17a and 17b, which are essential components in the present invention and whose scanning band is controlled by the control unit 11 of frequency scanning. Said scannable filters 17a and 17b are connected to the polarity correlator 15. According to the figure, a gas-temperature T measurement detector 19 and a gas-pressure p measurement detector 21 are placed in the measurement pipe 10. From the detectors 19 and 21, the measurement information is passed to the calculator unit 20, to which the data concerning the sound travel times t λ downstream and the sound travel times t 2 upstream are also transferred from the polarity correlator 15. In the unit 20, on the basis of the above formula (2), the sound speed c in the gas to be monitored is calculated and, on the basis of the formula (4), the flow velocity v of the gas is calculated. From the unit 20, the flow velocity v is transferred to the calculation and/or display unit 22, in which the flow velocity v is displayed and, if necessary, recorded, e.g., by means of a plotter and, if necessary, based on the above formulae (5) and (6), the volumet¬ ric flow Q and/or the mass flow M is/are calculated, and they may also be displayed and/or recorded in the unit 22. In the present invention, the monitor¬ ing of the composition of the gas flowing in the pipe 10 is connected with the monitoring, described above, of the flow velocity v and of the quantities Q and M that can be derived from said flow velocity. Since the sound speed in a gas is mainly dependent on the temperature and on the composition of the gas, which affects the sound speed mainly by the inter- mediate of the average molecular weight and to some extent also by the inter¬ mediate of the number of the degrees of freedom in the molecules, the sound speed in the gas also illustrates the composition of the gas and at least such considerable changes in the composition as are supposed to be monitored by means of the present invention. In the unit 20, based on the above formula (2), the sound speed c is calculated by making use of the travel times t χ and . Further, when the information on the temperature T of the flowing gas is brought to the unit 20 from the detector 19, on the basis of the above formula (3), c 0 = c ■ -/ T 0 /T) , it is possible to determine the sound speed c 0 that has been reduced to the reference tempera¬ ture T Q given to the system. From the unit 20, the reduced sound speed c 0 is passed to the unit 23. The unit 23 operates as a reference and alarm unit, which gives the alarm when the reduced sound speed c 0 is above or below the given limit values λ and c^ Said limit values c λ and c 2 can be arranged so that they can be set and fed to the unit 23. When the reduced sound speed c 0 remains within the given limits c x and o^ the system considers that the composition of the gas is sufficiently homogeneous. When the reduced sound speed c 0 detected by the monitoring system is above said upper limit C j or below said lower limit c^, the system gives a suitable alarm signal. Alternatively, said limits C ± and ^ can be arranged as dependent on temperature in a way corresponding to the reduc¬ tion described above. An alarm activates more precise determination of the gas composition, e.g., chromatographically. If the temperature of the gas remains sufficiently invariable, its measurement is not always necessary, so that the temperature-reduction of sound speed described above is not necessary. As a rule, however, measurement of the temperature and reduction of the sound speed on its basis are necessary in the invention. It should be emphasized that the above monitoring and mode of determination of the sound travel times t j and t 2 is just one exemplifying embodiment, to which the invention is not confined. In the invention, it is possible to apply the various details of acoustic flow measurement that are described in more detail in said FI Patent No. 76,885 and in the applicant's FI Patent Application No. 916102. Regarding the block diagram in the accompanying figure, it is stated further that the units illustrated as individual blocks may, in practical apparatuses, be placed physically as divided in different ways. An operational division of the blocks different from the figure is also possible. In the following, the patent claims will be given, and the various details of the invention may show variation within the scope of the inventive idea defined in said claims and differ from what has been stated above by way of example only.

Claims: Claims 1. Method for monitoring of the composition of a flowing gas, in which method acoustic oscillations are applied to the gas flow pipe (10) downstream and upstream, and the travel times (t l5 t 2 ) of the monitoring sound (L) downstream and upstream are detected, and the sound speed (c) or a quantity representing same is determined on the basis of said travel times (t^), which speed (c) or quantity is mainly dependent on the average molecular weight of the gas to be monitored, characterized-!-- that, in the method, the frequency of said acoustic oscillations is chosen below a certain limit frequency (f c ), so that the monitoring sound moves in the axial direction of the measurement pipe in the plane-wave mode, that the travel times (-^) of the monitoring sounds are detected over a measurement distance (L) in the axial direction of the measure¬ ment pipe, which measurement distance is dimensioned substantially larger than the average diameter (D) of the measurement pipe, and that, when said sound speed (c) or the quantity representing same differs from its range of expected values (c-^.c^), an alarm signal or some other control signal is given. 2. Method as claimed in claim 1, characterized in that, in the method, the measurement pipe that is used is a gas flow pipe (10) of substantially circular section, and that the upper limit frequency f c of the monitoring sound is chosen so that f c = c/(1.7 • D), wherein c is the sound travel speed in the medium that fills the gas flow pipe (10), and D is the diameter of said gas flow pipe (10). 3. Method as claimed in claim lor2, characterized in that the distance of measurement L of the travel times (t^) of the monitoring sounds downstream and upstream, in the axial direction of the gas flow pipe (10), is chosen so that L« 10D. 4. Method as claimed in any of the claims lto3, characterized in that, in the method, the temperature (T) of the flowing gas is measured, that, on the basis of said measurement of temperature, the sound speed that has been reduced to a certain reference temperature T 0 is determined from the formula c 0 = c • y ( ' l ' 0 /T) , which is applicable to an ideal gas and wherein T = absolute, measured temperature of the gas, T 0 = chosen absolute reference temperature, c = measured sound speed, and c 0 = sound speed reduced to the reference temperature, or by using a corresponding more realistic formula, and that, when said reduced temperature (c 0 ) differs from its expected range (c^..^), an alarm signal or control signal is given. 5. Method as claimed in any of the claims l to 4, c h a r a c t e r i z e d in that, in the method, based on said travel times (t 1 ,t 2 ), the velocity (v) of the flowing gas is calculated by means of a known formula (4) of calculation and/or, based on the above flow-velocity measurement, the volumetric flow (Q) and/or the mass flow (M) is/are calculated on the basis of known formulae (5),(6) of calculation. 6. Method as claimed in any of the claims l to 5, c h a r a c t e r i z e d in that, in the method, the pressure (p) of the flowing gas is also measured. 7. Method as claimed in any of the claims l to 6, c h a r a c t e r i z e d in that, in the method, substantially by means of the same apparatuses, both the homogeneity of the composition of the gas is monitored and its flow velocity (v) and/or quantities (Q,M) that can be derived from same is/are measured, that in the method long-wave sound is transmitted into the measurement pipe (10) and the sound signals passing in the gas flow downstream and upstream are detected by means of two sound detectors (14a, 14b) placed in connection with the measurement pipe (10) at a specified distance (L) from one another, both the flow velocity (v) of the gas that flows in the measurement pipe (10) and the sound speed (c) being determined by making use of polarity correlation (15;15 l5 15 2 ) of said signals by means of known formulae (2) and (4) of calculation, and that the frequency of the sound that is transmitted into the measurement pipe (10) is scanned between a certain minimum and maximum frequency (f m in---f max )- that the measurement signals (f-^t), f 2 (t)) arriving from the two sound detectors (14a,14b) are passed to a narrow-band filter (17a,17b) or system of filters, that the passband of said filters (17) is scanned synchronously with the frequency scanning of the sound transmission, and that the duration of the frequency scanning and the width of the passband of said filters (17) have been chosen so that, at the moment of the measurement sequence, the measurement signal detected by each sound detector (14a, 14b) has access through its filter (17) substantially without attenuation, as well as so that the interference frequencies substantially different from the mean frequency of the filters (17) are attenuated significantly. 8. Device for monitoring of the flow of a gas, in particular of natural gas, c h a r a c t e r i z e d in that the device comprises a measurement pipe (10), in which the gas flow to be measured runs, and loudspeakers (13a,13b) as the transmitters of the sound signals of audio frequency and microphones (14a,14b) as the sound detectors, which microphones are placed in connection with the measurement pipe (10) between said loudspeakers (13a,13b) at a certain known distance (L), in the axial direction of the measurement pipe, from one another, which axial distance is substantially, preferably by one order, larger than the average diameter D) of the measurement pipe (10), that the device comprises units (20,22,23) by whose means both the gas flow velocity (v) and the speed of sound (c) in the gas flow are determined, and that the device comprises an alarm unit (23), which is fitted to produce an alarm when the detected sound speed (c) or the quantity representing same is above or below certain preset limit values (c- -c^). 9. Device as claimed in claim 8, c h a r a c t e r i z e d in that the device com¬ prises a temperature detector (19) fitted in the measurement pipe (10), from which detector a temperature measurement signal (T) can be passed to the calculator unit (20) of the device, by means of which unit (20) the sound speed (c 0 ) that has been reduced to a certain preset reference temperature (T 0 ) can be determined by means of a known formula (3) of calculation, and that the device comprises a unit (23), which is fitted to give an alarm or control signal when said reduced sound speed (c 0 ) differs from its range of expected values (c j ...^). 10. Device as claimed in claim 8 or 9, characterized in that the device comprises a frequency-scanned signal generator (12) or generators (12a, 12b), by whose means frequency-scanned electric signals are fed to said loudspeakers (13a,13b), and which device comprises a polarity correlator C15;15 1 ,15 2 ), into which the signals received from said microphones (14a, 14b) are fed, that the device comprises two frequency-scanned filters (17a, 17b) or an equivalent system of filters, through which the signals coming from said microphones (14a, 14b) are fed to said polarity correlator (15), and that the device comprises a control (11) of the frequency scanning, by whose means the frequency of the frequency- scanning signal generator (12) and the frequency scanning of said narrow-band filters (17) are controlled synchronously with one another. 11. Device as claimed in any of the claims 8 to 10, characterized in that a pressure detector (21) for the flowing gas is placed in the measurement pipe, which detector gives a pressure measurement signal to the calculator unit (20) of the device. 12. Device as claimed in any of the claims 8 to 11 for monitoring of natural gas, characterized in that the device is fitted to give a starting impulse for more precise chromatographic determination of the composition of natural gas.

Inventors: HIISMAEKI PEKKA, KAALL LEIF, KNUUTTILA MATTI, KOUKKARI SAULI, MAEYRAENEN TARMO, TIITTA ANTERO, HIISMAEKI, PEKKA, KAALL, LEIF, KNUUTTILA, MATTI, KOUKKARI, SAULI, MAEYRAENEN, TARMO, TIITTA, ANTERO
Applicants: KYTOELAE INSTRUMENTTITEHDAS, INSTRUMENTTITEHDAS KYTOELAE OY
Application year: 1992
Main classification: G01F1
IPC codes: G01F1, G01H5, G01N29, G01P5