Note: Descriptions are shown in the official language in which they were submitted.
F~EB 2? '81 14:52 (613) 78?-3558 P.3
APPARATUS FOR MEASURING THE TEMPERATURE OF A FLUID FLOW
~'IEr.D ;?F ~,"HE INVENTION
The present invention relates in general to fl.owmeters.
More specifically, the present invention is related to flowmeters
using ultrasonic transducers for the noninvasive measurement of
attributes of a fluid, such as its flow, in a pipe.
BACKGRQUND OF ',~'~~',"" ;~~;~ENTTON
A convenient and conuuon7.y used means of measuring fluid
flow is by the use of ultrasonic flowmeters. This is typically
accomplished by a system in whioh two transducers, located at
angulaxly opposed upstream and downstream positions r~e3.ative to one
another are adapted to alternatively function as a transmitter and
a receiver thereby causing ultrasonic signals to travel
alternatively in upstream and downstream directions between the
transducers. The difference inn transit times between the upstream
signal and the downstream signal can be used to calculate the flow
rate of the fluid.
It is preferred that a second set of transducers be
disposed in a diametxica:L opposed relation. These "cross path"
transducers provide more ~.nformation about the flow field, allowing
for improvement in flow measurement accuracy and understanding of
the flow field.
sera disclosed is an apparatus =or determining the
Flow rate of a fluid in a pipe. The apparatus ~,ncludes means for
providing acoustic energy on a diagonal path through the fluid.
The diagonal providing means is in contact with the pipe. The
apparatus also includes means fox providing acoustic energy on a
r
CA 02271502 2001-02-19
-2-
diametrical path through the fluid. The diametrical providing
means is in contact with the pipe. The apparatus is also comprised
of means for determining the f low o:f f luid in the pipe based on the
acoustic energy of the diagonal providing means and the acoustic
energy of the diametrical providing means.
In one embodiment, the diagonal providing means is
fixedly disposed on the pipe. In another embodiment, the
diametrical providing means provides acoustic energy emitted in
both directions on the diametrical path. The diametrical providing
means preferably includes a first transducer and a second
transducer located at diametrically opposed positions about the
pipe. The first transducer and second transducer are preferably
adapted to alternatively function as transmitter and receiver so as
to cause ultrasonic signals to travel through the fluid
alternatively along the diametric path.
The diagonal providing means preferably includes a third
transducer and a fourth transducer located at diagonally opposed
upstream and downstream positions relative to one another. The
third transducer and the forth transducer are preferably adapted to
alternatively function as a transmitter and receiver so as to cause
ultrasonic signals to travel through the fluid in upstream and
downstream directions along the diagonal path between the third
transducer and the fourth transducer. The diametric path is
adjacent to the diagonal path so that the transducers are sampling
the same portion of fluid.
The determining means preferably comprises signal
processing means for determining the flow of fluid in the pipe
based on the transmission speed of ultrasonic signals transmitted
between the first and second transducers and the third and fourth
transducers.
CA 02271502 1999-OS-12
CA 02271502 2000-03-17
-3-
In accordance with the invention there is provided,
an apparatus for measuring temperature of a flowing fluid in a
pipe comprising:
An apparatus for measuring temperature of a flowing
fluid in a pipe comprising:
means for actively testing the flowing fluid with
acoustic energy and producing a test signal corresponding to
the temperature of the fluid, said testing means disposed on
the outside of the pipe and acoustic energy follows a path
through the pipe wall; and
signal processing means for determining the
temperature of the fluid based on the test signal and its time
of flight through the pipe, said testing means in communication
with said signal processing means.
-3a-
Embodiments of the invention will now be described with
reference to the accompanying drawings wherein:
Figure 1 is a schematic representation showing an
apparatus for determining fluid flow in a pipe.
Figure 2 is a schematic representation showing the
geometric parameters associated with the apparatus for determining
fluid flow in a pipe.
Figure 3 is a schematic representation showing the signal
processing means of the apparatus for determining fluid flow in a
pipe. '
Figure 4 is a schematic representation of the apparatus
for determining fluid flow in a pipe having a four ultrasound
paths.
Figure 5 is a schematic representation showing an
apparatus for determining fluid flow in a pipe using a bounce path.
Figure 6 is a schematic representation of an apparatus
for determining fluid flow using transducers disposed below the
pipe's surface.
Figure 7 is a schematic representation showing an
apparatus for determining the axial transverse velocity profile.
Figure 8 is a schematic representation of an apparatus
for determining fluid flow in a pipe using three transducers.
CA 02271502 1999-OS-12
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Figure 9 is an image of a transverse velocity profile of
a pipe.
DESCRIPTION OF THE PREFERRED EMBODIMETIrTS
Referring now to the drawings wherein like reference
numerals refer to similar or identical parts throughout the several
views, and more specifically to figures 1 and 2 thereof, there is
shown an apparatus 10 for determining the flow rate of a fluid 11
in a pipe 12. The apparatus 10 comprises means for providing
acoustic energy on a diagonal path 24 through the fluid 11. The
diagonal providing means is in acoustic contact with and preferably
disposed on the pipe 12. The apparatus 10 also comprises means for
providing acoustic energy on a diametrical path 18 through the
fluid 11. The diametrical providing means is in acoustic contact
with and preferably disposed on the pipe 12. The apparatus l0 is
also comprised of means for determining the flow of fluid 11 in the
pipe 12 based on the acoustic energy of the diagonal providing
means and the acoustic energy of the diametrical providing means.
In one embodiment, the diagonal providing means is f fixedly disposed
on the pipe 12. In another embodiment, the diametrical providing
means provides acoustic energy emitted in both directions on the
diametrical path 18.
Referring to figure 1, the diametrical providing means is
preferably comprised of a first transducer 14 and a second
transducer 16 located at diametrically opposed upstream and
downstream positions relative to one: another. The first transducer
14 and second transducer 16 are preferably adapted to alternatively
function as transmitter and receiver so as to cause ultrasonic
signals to travel through the fluid 11 alternatively in upstream
and downstream directions along a diametric path 18 between the
first transducer 14 and the second transducer 16.
CA 02271502 1999-OS-12
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The diagonal providing means is preferably a third
transducer 20 and a fourth transducer 22 located at diagonally
opposed positions about the pipe 12. The third transducer 20 and
the forth transducer 22 are preferably adapted to alternatively
function as a transmitter and receiver so as to cause ultrasonic
signals to travel through the fluid 11 along a diagonal path 24.
The diametric path 18 is adjacent to the diagonal path 24 so that
the transducers are essentially sampling the same portion of fluid
11.
The determining means preferably comprises signal
processing means 26 for determining the flow of fluid 11 in the
pipe 12 based on the transmission speed of ultrasonic signals
transmitted between the first and second transducers 14 , 16 and the
third and fourth transducers 20, 22, respectively.
Preferably, the transducers 14, 16, 20 and 22 are mounted
on the outside of the pipe 12 and thus do not disturb the fluid
flow therein. The coupling between the third and fourth
transducers 20, 22 and the pipe 12 is preferably accomplished by
mounting the third and fourth transducers 20, 22 onto a coupling
wedge 28 which can be comprised of vespal or lucite, for example.
The first and second transducers 14, 16 are mounted on a pad 30,
which can also be comprised of vespal or lucite. The coupling
between the wedges 28 and pads 30 and the pipe 12 can be enhanced
by providing a layer 32, such as silicon rubber. The layer 32
helps in preventing disruption or dispersion of the ultrasonic
signals as they travel from their respective wedge 28 or pad 30 to
the pipe 12. Preferably, the signal processing means 26 includes
means for measuring the transit time of ultrasonic signals
transmitted between the first and second transducers 14 , 16 and the
transit time between ultrasonic signal transmitted between the
third and fourth transducers 20, 22, respectively.
CA 02271502 1999-OS-12
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In a preferred embodiment, there is a plurality of
diagonal sets of transducers for transmitting ultrasonic signals
through the fluid 11 along a plura7.ity of diagonal paths 24 and an
equal number of diametrical sets of transducers for transmitting
ultrasonic signal through the fluid 11 along a plurality of
diametrical paths 18. Figure 4 shows a cross section through the
axis of the pipe 12 showing a four path system. Since figure 4 is
a cross sectional view, the transducers shown can be either
diagonal sets or diametrical sets. Likewise, the four paths shown
can be either diametrical paths 18 or diagonal paths 24.
It should be noted that in figure 2 and the
specification, the following nomenclature is used:
Q = total flow in pipe 12 (cubic inches/sec)
II = Pi = 3.141593
ID = Inside diameter of pipe 12 (inches)
PF = Hydraulic profile factor = ratio of average velocity over
whole pipe 12 to average velocity along diameter
cf = velocity of sound in fluid 11 (inches/sec)
= angle of acoustic path in fluid il
tdl = transit time along diametrical path 18 from transducer 14 to
transducer 16
t~ = transit time along diametrical path 18 from transducer 16 to
transducer 14
Otd = difference in time along diametrical path 18 (seconds)
that is Otd = tdl - t~
t~l is transit time along diagonal path 24 from transducer 20 to
transducer 22
CA 02271502 1999-OS-12
_7_.
t~2 is transit time along diagonal cross path 24 from transducer 22
to transducer 20
~t~ = difference in time along diagonal cross path 24 (seconds)
that is ~t~ = t~l - t~z
cw = velocity of sound in transducer wedge 28 and pad 30
(inches/sec)
Iowa = mechanical wedge 28 angle
aw = height of wedge (inches)
aw~ = height of pad 30
l0 aP = wall thickness of pipe 12 (inches)
= acoustic path angle in pipe 12
= acoustic path angle in wedge 28
cP~ = velocity o~f transverse wave in pipe 12 (inches/sec)
cP~ = velocity of longitudinal wave in pipe 12 (inches/sec)
td = average transit time along diametrical path 18 (seconds)
that is td = (tal + t~) /2
t~ = average transit time along diagonal path 24 (seconds)
that is t~ _ (t~t + t~2) /2
y is the distance between centers of transducers 14, 16
yo is the calculated value of y to be used in initial set up
temp = Temperature in degrees F
press = Pressure in psi absolute
press = pressure gauge + 14.7
tr, vt, dvdp, tc are parameters used in the calculation of velocity
of sound in water
CA 02271502 1999-OS-12
-g_
Acpl, Bcpl, Acpt, Bcpt are constants used in calculation of
velocity of sound in pipe (dependent on pipe material)
Acw, Bcw, Ccw are constants used in calculation of velocity of
sound in wedge (dependent on wedge material)
The flow rate Q of the fluid is calculated by:
Q = (~r ~ IDZ ~ PF/4) ~ v.
since,
v, = vd/Sin~pf - v~/Tan~Of
and,
wa = (cf2 ~ Cos~pf/2 ~ ID) ~ (ltd)
v~ _ (cf2/2 ~ ID) ~ (~lt~) (0)
Thus,
w, _ (cfz/2 ~ ID ~ Tan~pf) ~ (Otd - Ot~)
substituting into the original equation,
Q = (~r ~ ID ~ PF ~ Cf2/8 ~ tan~pf) ~ (Otd - Ot~) (1)
For acoustic path-to-transmitter length ratios less than
16:1, ~pf is calculated using Snells law relationship as follows:
f = S1I11 (CfSln~w/Cw)
CA 02271502 1999-OS-12
-9-
For acoustic path-to-transmitter length ratios greater
than 100:1, calculation of ~of is given by solution of the following
simultaneous equations:
td = 2 ~aw/COStpw~Cw + 2 ~aP/COS~pp~Cp~ + ID/COSSof~Cf (2)
Sincpf/cr = Sin~pP/cP~ (Spells law) (
Sin~pf/cf = Sin~pw/cw (Spells law)
Ideally, the acoustic path-to-transmitter length ratio
should be chosen to fall clearly into one of these regions.
Alternatively, if this cannot be achieved, then the fourth
transducer is moved axially along the pipe 12 until the position is
found at which the signal transferred from the third transducer 20
to the fourth transducer 22 is a maximum. At this point, either
set of the above equations can be used.
If y is known ~pf is given by solution of the following set
of equations
y = 2 ~ aw ~ Tan~pw+2 ~ aP ~ Tan~pP+ID ~ Tan~pf
Sin~pf/cf = Sin~pP/c~ Spells law
and
Sin~pf/cf = Sin~ow/cw Spells law
Calculation of y
Sin~of = cf~Sln~pwo/Cw Spells law
CA 02271502 1999-OS-12
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Sin~pp = cp~~Sln~p~,o/c~, Snells law
yo 2 ~ aw ~ Tan~pw+2 ~ ap ~ Tan~pp+I D ~ Tan~O f
Calculation of cf is given by solution of equation:
t~ = ID/cf + 2 ~ap/Cp~ + 2'aa,c/Cw (5)
The speed of sound values are dependent on temperature.
td is measured with the first transducer 14 and the second
transducer 16 through the diametric path 18 therebetween. Cps, Cp;
and Cw are determined by the following equations.
cp< = Acpt*(1+Bcpt*temp) (6)
cp, = Acpl*(1+Bcpl*temp) (7)
cw = Acw*(1+Bcw*temp+Ccw*temp~2) (8)
ID, ap and a~,~ are known (measured) from the specific
application of the apparatus.
With cf known by solution of Equation (5) , t~ measured
with the third transducer 20 and the fourth transducer 22 through
the diagonal path 24 therebetween, and aw, cw and ap, cp< and ID
known, solution of, for example, the three Equations (2)-(4)
determine the three unknowns how, ~p and ~pf in these equations.
Consequently, Q can then be determined since every variable in
Equation (1) is now known.
For instance, for carbon steel pipe 12
Acpl=2356000
Bcpl=.0000735
CA 02271502 1999-OS-12
-11-
Acpt=127700
Bcpt=.0000925
For vespal wedges 28
Acw=98299
Bcw=.0003960
Ccw=2.08E-7
To calculate cf in water temperatures>200°F
tr=temp-175.1 (9)
vt=5290.52-.15302*tr-.0138265*tr~2+3.326E-6 (10)
*tr~3+3.11042*tr~4-5.1131E-il*tr~5
dvdp=756.78/(725-temp)+6.3846-.034241*(725-temp) (il)
+7.4075-5*(725-temp)~2-5.666E-8*(725-temp)~3
vtp=vt-(4437-press)*dvdp*.02253 (12)
cf=vtp*12 (13)
To calculate cf at water temperatures<200°F
tc=(temp-32)/1.8 (14)
cf=100/2.54*(1402.49+5.0511*tc-.05693*tc~2+2.7633E-4*
tc~3-&.1558E-7tc~4)
The above equations assume that the wedges 28, pipe 12
2 0 and fluid 1l are al l at the same temperature . When the temperature
of the fluid 11 is different from that of ambient temperature, it
CA 02271502 1999-OS-12
-12--
is desirable to provide insulation or other means to insure that
the temperature is uniform or to modify the equations given above
to correct for these differences. For small crradients it
sufficient to assign different temperatures to the wedges and pipe
thus
temp (pipe) - temp (fluid) - ~tp
temp (wedge) - temp (fluid) - ~t~"
temp (cross wedge) - temp(fluid) - dtW~
where
Otw is the difference between the fluid temperature and the average
temperature of the wedge
~tw~ is the difference between the fluid temperature and the average
temperature of~the cross wedge or pad
Otp is the difference between the fluid temperature and the average
temperature of the pipe
For large gradients, it is desirable to have detailed knowledge of
the temperature distribution in the pipe and wedge and to use ray
tracing techniques as practiced in the design of optical
instruments to calculate the times spent in the wedge and pipe and
contribution of the pipe and wedge to the y displacement.
If the temperature of the fluid is not known, as shown in
the "REM Calculation of Fluid Temperature" section of the program
of the Appendix, cf as well as the temperature of the water can be
arrived at in an iterative loop technique that essentially picks a
temperature value of the water based on the known temperature
limits of the water, uses this temperature value to arrive at
CA 02271502 1999-OS-12
-13-
values of c~ cw~ and cP" and then uses the values of cf, cw~ and cP, in
equation (5) to arrive at a calculated value of t~. The actual
measured value of t~ is then compared with the calculated value of
t~.
If the calculated value of t~ does not match the measured
value of t~, different temperature values are sequentially picked
in the program and the loop is reiterated until the calculated
value of t~ matches the measured value of t~. The picked
temperature and the calculated value of cf during the last loop are
then known to be the actual values of temperature and cf.
In this manner, both the speed of sound in the fluid, c~,
and the temperature of the fluid 11 flowing in the pipe 12 can be
determined by ,mounting a pair of ultrasonic transducers in a
diametrical opposed relation on the pipe 12 and using signal
processing means to determine a measured value of t~.
In the operation of the inventive apparatus, the
transducers 14, 16, 20 and 22 are preferably strap-on types. The
strap-on transducer assembly contains a piezoelectric transducer, a
coupling wedge 28 or pad 30 and a protective cover. The transducer
converts the electrical energy to ultrasonic energy which the wedge
28 and pads 30 directs into the pipe 12 at the proper angle. The
protective cover provides a fitting for the transducer cable 36
conduit as well as protection of the 'transducer.
After precisely locating the transducer on the surface of
the pipe 12, the transducer wedge is coupled acoustically to the
pipe wall and then secured with strapping material, magnetic
holders, or welded brackets.
CA 02271502 1999-OS-12
-14-
The transducer signal cable is a twinax twisted pair with
a shield with an appropriate jacket for underwater or above ground
use as required. It is connected to the transducer at one end and
to the signal processing means 26 at the other, normally without
splices.
The signal processing means 26 is comprised of three
major functional units. These are the Acoustic Processing Unit 100
(APU), the Central Processing Unit 102 (CPU), and the Control and
Display Panel 104 (CDP) . Figure 3 provides a functional diagram of
these electronics.
The APU 100 controls the transmission and reception of
ultrasonic signals to and from the transducers. Electronic pulses
are generated and sent to the transducers, where the energy is
converted into'ultrasound and directed upstream or downstream in
directly into the pipe depending on which transducer is
transmitting, converted back into electronic pulses, and received.
Transmit times of pulses are measured with a 100 Mhz clock,
alternately upstream and downstream, every 4 ms to assure that data
is essentially simultaneous for upstream and downstream transit
times. These time measurements are stored and then sent to the
central processing unit 102 for mathematical manipulation.
The APU 100 typically is equipped with two
transmitter/receiver boards which control a total of four
ultrasonic diametrical paths 18. Additionally, there are two
transmitter/receiver boards to control four ultrasonic diagonal
paths 24.
The CPU 102 consists of a 286 microprocessor and I/O with
software suited specifically to the needs of the application. The
CPU 102 provides a number of important functions, including
CA 02271502 1999-OS-12
-15-
processing the transit time measurements from the APU 100. Flow
totalizers are also updated according to Euler's equation. At the
same time as high speed calculations are being processed, the
displays are updated, electronic checks are being made of the
entire APU 100 circuitry, user keypad commands are followed, and
outputs are updated.
The CDP 104 functions as the user interface. A full
screen display 106 provides readouts of flowrates, flow totals,
diagnostics, set-up parameters, and pertinent performance
characteristics. A numeric keypad 108 allows the operator to
select desired display screens without consulting a programmer's
handbook and without need of attaching a separate computer.
Listed below in Tables 1 through 3 are summaries of the
calculated parameters for two verification sites. These
verification sites were the Alden research Laboratories (ARL) and
the Tennessee Valley Authority (TVA) Sequoyah Nuclear Power Plant.
The ARL test used a l6in OD pipe with fluid temperature at
approximately 105° Fahrenheit. (The data presented below are
documented by ARL which is an NIST approved facility). The TVA
test used a 32in OD pipe with fluid temperature at approximately
435° Fahrenheit. Independent error analysis determined its
accuracy to be ~0.9% of measured flow.
CA 02271502 1999-OS-12
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Table 1: Flow Calculation at ARL 12/18/91
Conditions:
ID - 15.028in (Direct Measurement)
pressure - 50 psi
ap - .495in (Direct Measurement)
temp - 105.32 (ARL Reference)
Q - 18,390 gpm (ARL Reference)
cw - 92,170 in/sec (Direct Measurement)
~Pwo - 30.550
cPl - 233,774in/sec (Curve fit from
Published values)
awe - . 2 5 i n
- 125,454in/sec (Curve fit from
Published values)
aw - .586 in
LEFM Measured values:
tai - 291.86 ,sec
tai - 290.66 usec
tai - .241.45 ,sec
t~2 - 241.45 sec
Vita - :1218 ns
to - 241.45 ~CSec
~t~ - -4 ns
to - 291.26 ~tsec
CA 02271502 1999-OS-12
_17_.
LEFM Calculated values:
cf - 60,260in/sec
temp - 105°
Q - 18,488 gpm
~Pf - 19 . 4 °
SAw - 3 0 . 5 3
~Pp - 43.75°
Y - 6.92 in
y° (calculated) - 6.92 in
Table 2: Flow Calculation at ARL 12/18/91
Conditions:
ID - 15.028in (Direct Measurement)
ap - .495 in (Direct Measurement)
temp - 105.19° (ARL Reference)
Q - 13,430 gpm (ARL Reference)
cw - 92,170in/sec (Direct Measurement)
- 233,774in/sec (Curve fit from
Published values)
- 125,454in/sec (Curve fit from
published values)
LEFM Measured values:
to - 291.26 usec
t~ - 241.45 ,sec
CA 02271502 1999-OS-12
-18-
ltd - 890 ns
~t~ - -3 ns
LEFM Calculated values:
cf - 60,260 in/sec
temp - 105°
Q - 13,480 gpm
Sof - 19.4°
Table 3: Flow Calculation at TVA Sequoyah 2/6/92
Conditions:
ID ~ - 29.92 in (Indirect Measurement)
ap - 1.194in (Direct Measurement)
temp - 428 (TVA RTD measurement)
cw - 82,750in/sec (Direct Measurement
and Curve Fit)
cPi - 223,466in/sec (Curve fit from
Published values)
- 124,322in/sec (Curve fit from
Published values)
LEFM Measured values:
td - 670.32 sec
t~ - 612.22 ~CSec
Vita - 1413 ns
Ot~ - 1 ns
CA 02271502 1999-OS-12
-19-
LEFM Calculated values:
of - 50,386 in/sec
temp - 428.8°
Q - 13.518 Mlbs/hr
~Pf - 19 . 4 °
In an alternative embodiment, as shown in figure 5, the
third transducer 20 and the fourth transducer 22 are aligned with
each other such that acoustic energy transmitted by the third
transducer 20 follows a diagonal path to the fourth transducer 22
which is formed by reflection of the acoustic energy off of the pipe
12. This configuration of the apparatus 10, as shown in figure 5, is
otherwise known as the bounce path configuration. The first
transducer 14 and the second transducer 16 which create the
diametrical path 18, are disposed adjacent the diagonal path 24 that
forms the bounce path, either between the third transducer 20 and
fourth transducer 22 or outside the third transducer 20 or fourth
transducer 22. The equations described above are also applicable to
determine flow in the bounce path configuration of figure 5. An
example of such a configuration is the following:
Q = 472 gpm
ID = 27.25 inches
PF = 1.00
cf = 47,275.7 inches
18.35°
tdl = 385.180 sec
t~ = 385.000 sec
ltd = 180 nsec
t~l = 179.008 sec
t~2 = 179.000 ~CSec
3 0 Ot~ = 8 nsec
cw = 92,046.09 inches/sec
~Gwo = 38~52°
aw = 0.642 inches
CA 02271502 1999-OS-12
-2 0-
aw~ = 0.250 inches
aP = 0.360 inches
57.74°
~pw = 37.80°
c~ = 126,989.7 inches/sec
cP~ = 231, 992 . 8
td = 385.090 ~CSec
t~ = 179.004 sec
y = 7.5
y° = 7.423
temp = 74°F
pressure = 775 psi
Conditions
Pipe ID = 7.9529 inches
aP = 0.3605 inches
temp = 74°
cp, = 231,945.8 in/sec (from tables)
c~ = 126,956.3 in/sec (from tables)
cw = 91,987.1 (direct measurement)
LEFM Measurements
td = 386 ~CSec
t~ = 180 ~CSec
ltd = 177 nsec
~t~ = 8 nsec
LEFM Calculated Values
c~ = 47,001.3 in/sec. (~Ow = 37.18°)
Q = 468 gpm (~pP = 56.51°)
17.98°
In another alternative embodiment, as shown in figure 6,
the pipe 12 has an outside surface 27 and an interior 29 and the
first transducer 14 and second transducer 16 are disposed in the pipe
12 beneath the outside surface 27 such that acoustic energy
transmitted by the first transducer 14 is introduced into the
CA 02271502 1999-OS-12
-21-
interior 29 of the pipe 12, an acoustic energy is received by the
second transducer 16 directly from the interior 29 of the pipe 12 as
shown in figure 6. The diametrical path 18 is thus formed without
having acoustic energy, preferably ultrasonic energy, passing
directly through the pipe 12. Preferably, the third transducer 20
and fourth transducer 22 are disposed in the pipe 12 beneath the
outside surface 27 such that acoustic energy transmitted by the third
transducer 20 is introduced directly into the interior 29 of the
pipe, and acoustic energy is received by the fourth transducer 22
directly from the interior 29 of the pipe 12 after it has taken a
diagonal path 24 therethrough. Of course, the third transducer 20
and fourth transducer 22 can be mounted on the outside 27 of the pipe
12 as described above, or, the various transducers can be mounted on
or below the outside surface 27 depending on the design choice such
that only one transducer, three transducers, etc. can be on or below
the outside surface 27. The algorithm associated with calculation of
the flow and other relevant factors for the embodiment shown in
figure 6 can be found in Caldon technical report DS-112-991
(incorporated by reference) with respect to a single pair of
transducers forming a diagonal ultrasonic path. For the pair of
transducers forming the diametrical 'ultrasonic path B=90°, Cos B=1
yielding the transverse flow velocity v. For a 4-path configuration,
see Caldon technical report DS-116-392 (incorporated by reference).
The placement of the transducers beneath the outside surface 27 of
the pipe 12 is well known. See Caldon technical report installation
procedure SP1041 Rev. C, incorporated by reference.
The present invention is alsa embodied in an apparatus for
creating a transverse velocity profile of fluid flowing in a pipe 12.
The apparatus comprises means for obtaining a transverse velocity of
fluid in a plurality of different locations in the pipe 12 by
introducing energy into the pipe 12 and analyzing the energy.
Preferably, the obtaining means includes means for providing acoustic
CA 02271502 1999-OS-12
-22-
energy along a plurality of diametrical paths in the pipe 12, all of
which are in a common cross section of the pipe 12, and producing an
information signal corresponding to the transverse velocity of the
plurality of different locations. The providing means can be a
plurality of transducers which create a plurality of diametrical
paths 18 in the pipe 12 as shown in figure 4. Each diametrical path
18 identifies the transverse velocity component associated with a
corresponding location in the pipe 12. The transverse velocity
corresponding to each diametrical path 18 can be determined by
Equation (0).
The apparatus is also comprised of means for forming a
transverse velocity profile from the transverse velocities at the
plurality of different locations. The forming means is in
communication with the obtaining means. Preferably, the forming
means includes~signal processing means 26. The signal processing
means 26 receives the information signal and determines the
transverse velocity associated with each location. Each pair of
transducers which form a diametrical path 18 can be connected to
signal processing means 26 as described above to calculate the
transverse velocity for the corresponding diametrical path 18.
Preferably, the more diametrical paths 18 in a given cross section of
the pipe, the more accurate the transverse velocity flow profile will
be.
Preferably, the forming means includes a monitor in which
the transverse velocity of the locations are displayed together to
show the transverse velocity profile. An example of a display that
would appear on a monitor is shown in figure 9 which shows the
rotational component both in the clockwise and counterclockwise
direction cross section of the pipe 12. A ratio of V~:VD can be used
to deduce the flow profile characteristic (see Weske, J.
CA 02271502 1999-OS-12
-23-
"Experimental Investigation of Velocity Distributions Downstream of
Single Duct Bends," NACA-TN-1471, January 1948, incorporated by
reference). The flow profile characteristic can be used to choose
paths) with the lowest diametrical to diagonal velocity ratio.
. The present invention is also embodied in an apparatus for
determining transverse velocity of fluid in a pipe 12. The apparatus
is comprised of means for actively testing the flowing fluid with
energy and producing a test signal corresponding to the transverse
velocity of the fluid. The testing means is in contact with the pipe
l0 12. The apparatus 106 is also comprised of signal processing means
26 for determining the transverse velocity of the fluid based on the
test signal. The signal processing means 26 is in communication with
the transverse velocity testing means 106. As described above, the
testing means is preferably a first transducer 14 and a second
transducer 16 which are in contact with the pipe 12 such that they
form a diametrical path 18. From Equation (0), the transverse
velocity can be obtained with the signal processing means 108.
The present invention is also embodied in a method for
creating a velocity profile of fluid flowing through an axial length
110 of pipe 12 as shown in figure 7. The method comprises the steps
of (a) measuring transverse velocity flow of the fluid at a first
axial location 112 of the pipe 12 with energy introduced therein.
Then, there is the step of (b) measuring transverse velocity flow of
the fluid at a second axial location 114 of the pipe 12 with energy
introduced therein. Preferably, after step (b), there is the step
(c) of forming a profile of the transverse velocity of fluid flowing
in the pipe 12 over the axial length 110 of the pipe from the
transverse velocity measured at the first axial location 112 and
second axial location 114. Preferably, before step (c), there is the
step (d) of measuring the transverse velocity of fluid flowing in the
pipe 12 at a plurality of additional different axial locations, such
CA 02271502 1999-OS-12
-24-
as axial location 116 with energy introduced to the pipe 12. After
the step (d) , there can be the step (e) of fixing a flow meter in
contact with the pipe 12 at a desired axial location based on the
transverse velocity flow thereat.
Also as shown in figure 7, there is an apparatus 118 for
creating a velocity profile of fluid flowing through a pipe 12. The
apparatus 118 is comprised of means 120 for obtaining transverse
velocity flow information of fluid along an axial length 110 of the
pipe 12 with energy introduced therein. The apparatus 118 is also
comprised of means 122 for forming a transverse velocity profile
along the axial length 110 of the pipe 12 from the transverse flow
information. The forming means 122 is in communication with the
obtaining means 120. Preferably, the obtaining means 120 can be a
plurality of transducers 124 disposed in a removable housing, for
instance, connected with velcro. The transducers 124 are disposed in
the housing 126 such that each transducer 124 has a mate transducer
124, which together form a diametrical path. Individual sets of
transducers provide their diametrical path information to the
obtaining means 122, which is preferably signal processing means 26
as described above, to calculate the transverse flow. The forming
means 122 can also include a monitor 121 which is connected to signal
processing means 26 that displays the velocity profile along the
axial length 110. A flow meter, for instance, comprised of first
transducer 14, second transducer 16, third transducer 20 and fourth
transducer 22, as shown in figure 1, can then be fixedly attached to
the pipe 12 at a location where there is minimal transverse velocity
flow so that an accurate a reading as possible of the axial flow
through the pipe 12 can be obtained.
The present invention is also embodied in an apparatus
3o for measuring the temperature of a flowing fluid 11 in a pipe 12.
The apparatus is comprised of means far actively testing the flowing
CA 02271502 1999-OS-12
-25-
fluid energy and producing a test signal corresponding to the
temperature of the fluid 11. The testing means is in contact with
and preferably disposed on the outside of the pipe 12. The
apparatus is also comprised of signal processing means 26 for
determining the temperature of the fluid 11 based on the test signal.
Preferably, the testing means comprises a first transducer
14 for transmitting ultrasonic signals through the fluid 11 and a
second transducer 16 for receiving ultrasonic signals transmitted by
the first transducer 14. The second transducer 16 is disposed in an
opposing relation with the first transducer 14 such that the
ultrasonic signals transmitted by the first transducer 14 travel on
a diametric path 18 with respect to the pipe 12 to the second
transducer 16. Preferably, the testing means also includes means for
measuring pressure of the fluid in the pipe 12, such as a pressure
gauge or sensof. The pressure measuring means is in communication
with the signal processing means 26 and the pipe 12. The signal
processing means 53 preferably determines the temperature of the
fluid in the pipe 12 based on the transmission speed of ultrasonic
signals transmitted between the first and second transducers and the
pressure of the fluid. Preferably, the signal processing means 26
identifies the average temperature of the fluid across the pipe 12
corresponding to the diametric path 18 between the first transducer
14 and second transducer 16. Preferably, to calculate the
temperature, Equations 9-14 below can be used in the signal
processing means 20, such as a computer. By being disposed on the
outside of the pipe 12, the first and second transducers do not
interfere with the flow of fluid 11 with the pipe. The temperature
of the fluid il flowing in the pipe 12 can thus be determined without
the apparatus penetrating the envelope defined by the inside
diameter, ID, of the pipe 12.
CA 02271502 1999-OS-12
-26-
The present invention is also embodied in an apparatus
for measuring the speed of sound in a fluid 11 flowing in a pipe
12. The apparatus comprises means for testing the flowing fluid 11
and producing a test signal corresponding to the speed of sound of
the fluid in the pipe. The testing means is in contact with and
preferably disposed on the outside of the pipe 12. The apparatus
also includes signal processing means 26 for determining the speed
of sound of the fluid in the pipe based on the test signal.
Preferably, the testing means is disposed in a gaseous environment
l0 on the outside of the pipe 12. Preferably, the testing means
comprises a first transducer 14 for transmitting ultrasonic signals
through the fluid li and a second transducer 16 for receiving
ultrasonic signals transmitted by the first transducer 14. The
second transducer 16 is disposed in an opposing relation with the
first transducer 14 such that the ultrasonic signals transmitted by
the first transducer 14 travel on a diametric path 18 with respect
to the pipe 12 to the second transducer 16. The speed of sound can
be determined by the signal processing means 26, such as a computer,
with Equations (5), (7j and (8) and the necessary measured data.
The present invention is also embodied in an apparatus 10
for characterizing fluid properties in a pipe 12. The apparatus 10
comprises first means for measuring sound velocity in the fluid and
producing a first signal corresponding to the sound velocity. The
first measuring means is in communication with the fluid. The
apparatus 10 is also comprised of second means for measuring at least
one state variable of the fluid and providing a second signal
corresponding to the state variable measured. The second means is in
communication with the fluid in the pipe. Additionally, the
apparatus is comprised of signal processing means 26 in communication
with the first and second measuring means for determining fluid
properties. As shown in figure 1, the second measuring means
preferably includes means for measuring pressure of the fluid. The
CA 02271502 1999-OS-12
-27-
pressure measuring means is connected with the signal processing
means 26. The pressure measuring means can be a pressure sensor in
communication with the fluid. The first means can include a first
transducer 14 and a second transducer 16 in contact with the pipe
such that first transducer 14 transmits acoustic energy in a
diametric path 18 to the second transducer 16. Each transducer is in
communication with the signal processing means 26.
In this embodiment, preferably, the signal processing means
26 also determines specific volume of the fluid. The specific volume
can be determined from the "REM calculation" as specific volume cubic
feet/pound" in Appendix A. For this calculation, the pressure is
independently measured with a pressure gauge and the temperature is
calculated from the speed of sound, as described above.
Additionally, the signal processing means 24 can determine Reynolds
number for the fluid in the pipe from the specific volume and
viscosity and consequently PF. It does this in the following way.
The determination of the kinematic viscosity (kvis), the profile
factor PF and the Reynolds number can be obtained from "REM
calculation of meter factor" in Appendix A, where L represents log.
The profile correction factor, PF, relates to axial velocity averaged
along the acoustic path between the diagonal transducers, v, with the
axial velocity average across the cross sectional area of the flow, v.
This is expressed as:
V
- PF
The PF will vary depending on three factors. These are:
(1) Average fluid velocity, v.
(2) Fluid density and viscosity, p and ~c, respectively.
CA 02271502 1999-OS-12
-28-
(3) cross section dimensions (i.e. ID).
The Reynolds number combines the hydraulic effect of the
above 3 factors into one number. 7.'he Reynolds number, Re, can be
used to determine an expression for the velocity profile (Nikuradse,
J. "Laws of Turbulent Flow in Smoath Pipes," NASA TT F-10, 359,
October 1966; Reichardt, H., "Vollst~ndige Darstellung der
turbelenten Geskhwindigkeitsverteilung in glatten Leitungen" ZAI~I 31,
208-219 (1951), incorporated by reference) and thus the PF may be
determined from knowledge of the Reynolds number.
The LEFM first calculates the kinematic viscosity using the
curve fit of the published values fo:r water vs. temperature.
where:
a = Kinematic viscosity = ~/p = absolute viscosity/density
Then, the Reynolds number is calculated:
Re = Reynolds number = Dv/u
The PF is then calculated using published data (i.e.
Reichardt and Nikuradse) that express the velocity profile as a
function of Reynolds number.
In the apparatus 10, with temperature measuring means, the
signal processing means 24 preferably identifies when a boundary
between fluid of a first material and fluid of a second material
passes through the pipe at the diametrical path. The temperature
measuring means can be, for instance, a thermal couple in contact
with the pipe 12 or the fluid. Since there is independent
identification of temperature and pressure, and with an essentially
CA 02271502 1999-OS-12
-29-
constant temperature and pressure, a change in specific volume
determined by the first and second transducers and signal processing
means 26 indicates a change in material in the pipe 12. Knowledge of
the pressure, temperature and sound velocity can be used to
distinguish fluids which have sound velocities distinct from each
other. Typically, fluid with sound velocities that differ by .5% at
a given temperature and pressure are easily distinguished. Likewise,
with knowledge of the pressure and calculated temperature, the
specific heat content of water and water density can be determined
from a curve fit of published data vs. temperature and pressure.
Fluid enthalpy can be determined using the fluid density and specific
heat content.
Another embodiment requires only three transducers to form
a diagonal and a diametrical path, as shown in figure 8. Second
transducer 16 end fourth transducer 22 are the same as described
above. In place of first transducer 14 and third transducer 20 is
double transducer 23. On a first face 25 forming a 45° angle with
the surface 27 is disposed piezoelectric 37 which emits ultrasonic
energy. The ultrasonic energy is incident upon the double transducer
23-pipe 12 interface where a portion of the energy is refracted
therethrough ultimately to third transducer 22, and a portion of the
energy is reflected to free face 33. Free face 33 forms a 22.5°
angle with the outer surface 27 of the pipe 12. The reflected energy
from the double transducer 23-pipe 12 interface is again reflected by
free face 33 such that it forms a right angle with the outer surface
of the pipe 12 and is transmitted the:rethrough to second transducer
16.
Although the invention has been described in detail in the
foregoing embodiments for the purpose of illustration, it is to be
understood that such detail is solely for that purpose and that
variations can be made therein by those skilled in the art without
CA 02271502 1999-OS-12
-30-
departing from the spirit and scope of the invention except as it may
be described by the following claims.
CA 02271502 1999-OS-12
CA 02271502 2000-09-14
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APPENDIX A
REM High Temperature Strapon Flowmeter method 1
pi = 3.141593 'value of Pi
rad = 180 / pi 'conversion from radians to degrees
REM measured pipe and wedge dimensions
awc = .247 ' wedge height cross path, inches
aw = .7825 ' wedge height diagonal wedge , inches
Thetawo = 30.55 / rad
OD = 16.04 ' Pipe diameter inches
ap = .992 ' Pipe wall thickness, inches
ID = OD - 2 * ap' calculation of pipe inside diameter
tauEc = (2.64 + 1.075) * .000001'Tau electronics + Tau transducer + Tau
cable cross path, seconds
tauEd = (1.64 + 1.075) * .000001'Tau electronics + Tau transducer + Tau
cable diagonal path, seconds
pressg = 1100' measured fluid pressure
press = pressg + 14.7'conversion from press gauge to press absolute
REM measured values of times
td = .0003387' average transit time diagonal path, seconds
tc = .00029542#' average transit time cross path, seconds
dtd = 7. 59E-07'difference in transit time diagonal path, seconds
dtc = -lE-09'difference in transit time cross path, seconds
REM coefficients used in calculation of velocity of sound in pipe and wedge
Acw = 98299: bcw = -.000396054#: ccw = -2.08E-07'KKB Vespal corrected
Acpt = 127700: Bcpt = -.0000925
Acpl = 235600: Bcpl = -.0000735
CA 02271502 2000-09-14
-31 a-
REM coefficients for calculation of lkvis= natural log kvis
Akv = -5.507787: Bkv = -.01557479#: Ckv = 2. 87701 E-O5: Dkv
- -1.8516E-08
REM calculation of fluid temperature
Th = 660: Tl = 165: 'temperature limits
dto = .001 ' max error in calculation of temp
dt=Th-Tl
DO
i=i+1
dt=dt/2
temp=Tl+dt
cwc = Acw * (1 + bcw * tempwc + ccw * tempwc ~ 2) ' velocity in wedge,
inches/sec
cpl = Acpl * ( 1 + Bcpl * tempp)'longitudinal velocity in steel, inches/sec
tr = temp - 175.1
vt = 5290.52 - .15302 * tr - .0138265 * tr ~ 2 + 3.326E-06 * tr " 3 +
3.11042E -08 * tr ~ 4 - 5.1131E-11 * tr ~ 5
dvdp = 756.78/ (725 - temp) + 6.3846 - .034241 * (725 - temp) + 7.407E-OS*
(725 - temp) ~ 2 - 5.666E-08 * (725 - temp) ~ 3
vtp = vt - (4437 - press) * dvdp * .02253
cf-vtp * 12
taul = tauEc + 2 * awc / cwc + 2 * ap / cpl'Tau for cross path
F1=tc-taul-ID/cf
IF F 1 >= 0 THEN Tl = temp
LOOP UNTIL ABS(dt) < dto OR F1 = 0
CA 02271502 2000-09-14
-32-
REM calculation of Tangent phif
sphiw = SIN(Thetawo)' Sine of wedge angle
cw = Acw * ( 1 + bcw * temp + ccw * temp ~ 2) ' velocity of sound in
wedge, ins/sec
sphif = cf * sphiw / cw' Sine of angle on fluid
cphif = SQR( 1 - sphif ~ 2)' Cosine of angle in fluid
tphif = sphif / cphif Tangent of angle in fluid
REM calculation of meter factor
v=cf~2/2/ID/tphif*(dtd-dtc)
Lkvis = Akv + Bkv * temp + Ckv * temp " 2 + Dkv * temp " 3 'natural log
kinetic viscosity of water, square inches/sec
lre = LOG(ABS(v * ID)) - Lkvis 'Calculation of natural log Reynolds
number
PF = 1.0144 - .8442 / lre 'meter factor
REM calculation of flow
Q = pi * ID * PF * cf ~ 2 / (8 * tphif) * (dtd - dtc)' flow in cubic
inches/sec
PRINT Q
END
REM calculation of specific volume cubic feet/pound
svt = .01566 + 6.97E-06 * temp - 6.27E-08 * temp ~ 2 + 3.61 E-10 * temp
3-7.34E-13 *temp~4+OS.SE-16*temp~5
dsvdp = 70931 / (700 - temp) - 17.9 + .01621 * (700 - temp) + .000004
* (700 - temp) ~ 2
svtp = svt + (3000 - press) * dsvdp * lE-08
