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IBJ Technology 
Ingenieurbüro Jäger 
IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 
1 
Experimental study 
Measurement of sonic speed of drilling muds under shear stress 
Short version 
Frank-Michael Jaeger, Dipl.-Ing.(FH),Dipl.-Ing.Öc., IBJ Technology 
Introduction 
Investigations for the speed of the sound of drilling muds was carried out so far under static conditions 
[1] and [2]. 
Major limitations of the results for the practical result from the used piezoceramic transducers and the 
vibration generation technology. 
In particular, the following points for the evaluation of the technical suitability are not optimal in above 
mentioned investigations: 
-adverse selection of the frequency 
-too small diameter of the piezo disk 
-low power of the transmitters 
-single pulse to excite 
-no shear stress of muds 
Apparatus 
The measurement of sound velocity and damping took place at IBJ technology with other acoustic and 
electric parameters and under realistic conditions with shear stress of the muds. Changing circular 
rotations of the muds were realized with a stirrer. 
Figure (1) shows the experimental setup with 
a PC-controlled processor that monitors the 
variable burst pulse generation. Is the transit 
time between the transmitter and receiver with 
a standard deviation (time measurement) of 
approximately 50 ns with a TDC is 
determined. 
The amplitude of the envelope at certain times 
of the multiple reflections between the 
transmitter and receiver with an ADC is 
calculated by determining the damping. In 
addition, even the length of multiple 
reflections is determined. These represent the 
penetration depth of the ultrasonic signals in 
the mud. 
Figure 1: Apparatus
IBJ Technology 
Ingenieurbüro Jäger 
As a criterion for the penetration depth, the reliably trigger enabled signal level is taken for determining 
maturity. Figure (2) shows the principle of measurement of the penetration depth. 
IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 
2 
This depth is greater than a multiple of the real distance between the transmitter and receiver can be 
assumed by a practical measurement. 
The penetration depth of process water (soapy 
water between the single muds) is in image 
(2). The distance of the transmission burst is 
28 ms. The amplification of the received 
pulses of ultrasound was chosen so that 
multiple echoes not per the new transmitter 
into range. The process water, a penetration 
depth is achieved by 17,19 ms, corresponds to 
about 25 m or 984 inch. 
Figure 2: depth of penetration in process water 
Implementation 
The first investigations for the time being confined to water-based muds. Similar behavior was found for 
the water-based and oil-based sludge in [1]. The absolute sound speeds are about 200 to 250 m/s lower. 
4 mud densities (11,3 lb/gal, 12 bl/gal, 15,6 bl/gal and 20,2 bl/gal) were produced for the experimental 
investigations. The blends consist of water, barite, bentonite, and methyl cellulose. 
Further additives like pot ash, salt, xanthan gum, starch, etc were not admitted. 
The mixture for the water-based mud with 12 bl/gal was, for example, as follows: 
Water 65,33 mass % 
Bentonite 3,73 mass % 
Barite 29,84 mass % 
Methyl cellulose 1,10 mass %
IBJ Technology 
Ingenieurbüro Jäger 
Mud Density Penetration 
50 rpm # 300 rpm # 500 rpm # 
11,3 lb/gal* 157 inch 
12,0 lb/gal 615 inch 587 inch 143 inch** 
15,6 lb/gal 320 inch 347 inch 333 inch 
20,2 lb/gal 198 inch 164 inch 119 inch 
IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 
3 
Results 
Of course the absolute sound speeds are also influenced by the salinity and temperature. Decides for the 
practicality, however, is the penetration depth in the mud and the behaviour under shear load through the 
rotating drill string. 
Table 1 shows the measurement results without shear load below. 
Mud Density Basis Sound Speed Penetration 
Time Length 
1,35 kg/l 11,3 lb/gal Bentonite 1505,93 m/s 3,09 ms 465 cm 181 inch 
1,44 kg/l 12,0 lb/gal Barite 1505,14 m/s 9,41 ms 1416 cm 552 inch 
1,87 kg/l 15,6 lb/gal Barite 1498,36 m/s 7,22 ms 1082 cm 422 inch 
2,42 kg/l 20,2 lb/gal Barite 1449,67 m/s 4,42 ms 641 cm 250 inch 
Table 1: Static penetration and sound speed 
The following tables show the measurement results with dynamic shear stress (strirrer rotation in rpm). 
#Rotation 
*Basis: Bentonite 
** Stirrer trompe, air trapped in the Sound path. The 
resulting  S of the speed of sound is the 
Path length in the air small. 
Table 2: Dynamic penetration 
Table 2 shows the dynamic penetration depth in different stirrer rotations per minute. The results for 
20.2 lb/gal are constant without averaging Very much, because the viscosity of the mud is the highest. 
Thus, the flow conditions are Very much constant and little turbulence. 
Please note this is for all studies with the same constant reinforcement work was. The signal-to noise 
ratio would have approved a 20 to 40 dB higher gain of the received signal.
IBJ Technology 
Ingenieurbüro Jäger 
Mud Density Ultrasound Speed 
50 rpm # 300 rpm # 500 rpm # 
18:22:30 18:27:30 18:32:30 18:37:30 18:42:30 18:47:30 18:52:30 
IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 
4 
#Rotation 
*Basis: Bentonite 
** Stirrer trompe, air trapped in the Sound path. The 
resulting  S of the speed of sound is the 
Path length in the air small. 
Table 3: ultrasound speed under shear stress 
Table 3 are shown in dynamic ultrasonic speeds. For mud densities up to 15, lb/gal minor changes of the 
speed detected these amounted to less the maximum up to 1 m/s. 
At a density of the mud of 20, lb/gal, signified a proportional monotonically increasing velocity was 
measured. This increase amounted to around 2, m/s at 500 rpm. 
Figure 3 shows the significant increase in the speed of sound by 
shear stress. 
The slight increase of the curve is based on the influence of 
temperature. 
The influence of the shear stress on the speed moves in the 0,1 
% area and is for the kick detection without meaning. A change of 
in temperature of 1° Celsius has even greater influence on the 
change of speed. 
Figure 3: Boost the speed 
11,3 lb/gal * 1505,42 m/s 
12,0 lb/gal 1505,13 m/s 1505,15 m/s 1433.65 m/s** 
15,6 lb/gal 1499,88 m/s 1499.05 m/s 1498.97 m/s 
20,2 lb/gal 1451,54 m/s 1452,12 m/s 1452,60 m/s 
h:min:s 
1470 
1465 
1460 
1455 
1450 
1445 
1440 
Schreiber 0
IBJ Technology 
Ingenieurbüro Jäger 
16:50:00 16:55:00 17:00:00 17:05:00 17:10:00 17:15:00 17:20:00 
IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 
5 
Penetration depth and Non-Newtonian behavior 
The penetration rises at first monotonous after a standstill of the stirrer. The example of 12 bl/gal it was 
ms after 10 min over 10 ms. 
Then with a low rotation speed of about 50 rpm shear forces applied rpm, the penetration depth remains 
essentially at this size (9.96 ms). 
At about 500 rpm, the depth of half breaks together 4,8 ms with a variation of +-2 ms. The speed of 
sound drops further, it formed a stirring trompe between the sensors. Thus, the results are affected 
significantly. Too small values for the speed and depth are determined. 
With increasing time the penetration depth on 3 +-1ms (without averaging, real-time sampling). The 
speed remains relatively constant with the error by the trompe 1419 m/s. 
The mud 15.6 lb/gal starts at 1506,17 m/s and 0,83 ms penetration depth after a rest period of 24 hours 
without moving. More recently turning over 300 rpm monotonically in the subsequent peace on 5,16 ms 
penetration depth and the speed drops to 1501,63 m/s. 
The depth of penetration into the drilling mud under shear stress increases from 49 inch to 302 inch. 
Thus, the drilling mud shows the behavior of a Bingham fluid. 
The envelopes of the multiple echoes were recorded 
with the ADC. In the time range of the first multiple 
echoes until about 2 ms a decrease of the absorption 
of ultrasonic waves in the drilling mud witnessed as 
the drilling mud with the density of 20.2 lb/gal. She 
reflected in increase in the amplitude, so the following 
display (Figure 4) shows the dependence of the 
measured amplitudes at different speeds. This was 
reduced from 300 rpm 50 rpm (from 17: 00), and then 
click zero rpm (from 17:12). 
A higher speed causes a higher amplitude, or smaller 
absorption of ultrasonic waves. 
Figure 4: ultrasonic amplitude as a function of Speed 
h:min:s 
4500 
4000 
3500 
3000 
2500 
2000 
1500 
1000 
500 
3500 
3250 
3000 
2750 
2500 
2250 
2000 
1750 
1500 
1250 
1000 
750 
Schreiber 0 Schreiber 1
IBJ Technology 
Ingenieurbüro Jäger 
1750 
1500 
1250 
1000 
750 
500 
250 
12:50:00 12:55:00 13:00:00 13:05:00 13:10:00 13:15:00 13:20:00 
h:min:s 
Schreiber 0 Schreiber 1 
400 
375 
350 
325 
300 
12:47:30 12:52:30 12:57:30 13:02:30 13:07:30 13:12:30 13:17:30 
h:min:s 
Schreiber 0 
IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 
6 
Measurement without fluid 
The ultrasonic transducers are designed so the they in fluid and gas can measure (Fig. 5). With the used 
open experiment measurement can be 
demonstrated with gas only with air. The speed of 
sound drops when draining on 357 m/s. Due to the 
high resolution of 1 cm/s, even small changes in 
speed can be measured by dissolved gases. At a 
rate of 28 ms, a Very much fast display of real 
values is achieved even with a moving average 
from a variety of values. 
Figure 5 Change of the mud 
Figure 6 change the speed air-mud Figure 7 zoom speed in air 
Figure 6 shows the speed of sound in the phase of emptying and new filling with drilling mud. Figure 7 
shows the zoom ultra sound velocity in air. 
The measurement of the velocity of gaseous and liquid hydrocarbons inflows cannot be determined with 
this open experiment. 
In the literature, there are about A few calculations and practical studies. 
The solubility of methane in diesel oil is in [3] consider. 
The effect of gas solubility is considered in [4]. 
The sound velocity of fluid-fluid mixtures and fluid-gas mixtures under pressure is investigated in [5]. 
Reflections on the sound speed in liquid-gas mixtures' water-air and water-steam are to find in [6].
IBJ Technology 
Ingenieurbüro Jäger 
IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 
7 
Conclusions 
The measurement of the speed of sound is practical with the concept of the Ultrasonic sensors. 
Interference by rotating drill strands are not to be expected. The depth and range of the sensors safely 
exceeds the damping of the mud. Even in the most absorbing mud (20.2 lb/gal), the penetration depth is 
10 x the distance of the sensor. 
With an AGC (automatic gain control), the penetration depth in the drilling mud 20.2 can lb/gal on the 2 
or 3 be lifted times. Thus one is 30 to 50 times security across the entire range. The absorption of 
ultrasound has no disturbing effect on a measurement of velocity or velocity high mud densities and 
viscosities at the selected frequencies of ultrasound and the transmission burst. 
The measurement of the flow of drilling mud is possible also with all commonly used drilling sludge 
and diameters of pipelines. 
It is measurable not disturbing increase of noise during the operation of the stirrer. 
References 
[1] Molz, E.; Canny, D.; Evans, E.; Baker Hughes INTEQ, Houston, Texas 
” Ultrasonic Velocity and Attenuation Measurements 
in High Density Drilling Muds” 
SPWLA-1998-F,SPWLA 39th Annual Logging Symposium, 26-28 May, Keystone, Colorado, 1998 
[2] Raeymaekers, B.; Pantea, C.; N. Sinha, D. N. 
“Creating a collimated ultrasound beam in highly attenuating fluids” 
Elsevier, Ultrasonics 52 (2012) 564–570 
11 December 2011 
[3] Atolini, T. M.; Ribeiro, P. R. 
“VAPOR-LIQUID MIXTURE BEHAVIOR AT HIGH TEMPERATURES AND 
PRESSURES : A REVIEW DIRECTED TO DRILLING ENGINEERING” 
Brazilian Journal of Petroleum and Gas. v. 1, n. 2, p. 123-130, 2007. 
ISSN 1982-0593 
[4] Galves, L. V., Federal University of Rio de Janeiro; Gandelman, R. A.; Martins, A. L., Petrobras 
” Impact of Gas Solubility on Kick Detection in N-Paraffin Based Drilling Fluids” 
Leandro Victalino Galves, Federal University of Rio de Janeiro; Roni Abensur Gandelman; André Leibsohn Martins, 
Petrobras 
2014 AADE Fluids Technical Conference and Exhibition held at the Hilton Houston North Hotel, Houston, Texas, April 15- 
16, 2014. 
[5] Liu, Y. 
” ACOUSTIC PROPERTIES OF RESERVOIR FLUIDS” 
Dissertation, Stanford University, June, 1998 
[6] Kiefer, S. W. 
”Sound Speed in Liquid-Gas Mixtures' Water-Air and Water-Steam” 
VOL. 82, NO. 20 JOURNAL OF GEOPHYSICAL RESEARCH, JULY 10, 1977 
Markkleeberg, September 2014

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Experimentalstudy measurement of sonic speed of drilling muds under shear stress

  • 1. IBJ Technology Ingenieurbüro Jäger IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 1 Experimental study Measurement of sonic speed of drilling muds under shear stress Short version Frank-Michael Jaeger, Dipl.-Ing.(FH),Dipl.-Ing.Öc., IBJ Technology Introduction Investigations for the speed of the sound of drilling muds was carried out so far under static conditions [1] and [2]. Major limitations of the results for the practical result from the used piezoceramic transducers and the vibration generation technology. In particular, the following points for the evaluation of the technical suitability are not optimal in above mentioned investigations: -adverse selection of the frequency -too small diameter of the piezo disk -low power of the transmitters -single pulse to excite -no shear stress of muds Apparatus The measurement of sound velocity and damping took place at IBJ technology with other acoustic and electric parameters and under realistic conditions with shear stress of the muds. Changing circular rotations of the muds were realized with a stirrer. Figure (1) shows the experimental setup with a PC-controlled processor that monitors the variable burst pulse generation. Is the transit time between the transmitter and receiver with a standard deviation (time measurement) of approximately 50 ns with a TDC is determined. The amplitude of the envelope at certain times of the multiple reflections between the transmitter and receiver with an ADC is calculated by determining the damping. In addition, even the length of multiple reflections is determined. These represent the penetration depth of the ultrasonic signals in the mud. Figure 1: Apparatus
  • 2. IBJ Technology Ingenieurbüro Jäger As a criterion for the penetration depth, the reliably trigger enabled signal level is taken for determining maturity. Figure (2) shows the principle of measurement of the penetration depth. IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 2 This depth is greater than a multiple of the real distance between the transmitter and receiver can be assumed by a practical measurement. The penetration depth of process water (soapy water between the single muds) is in image (2). The distance of the transmission burst is 28 ms. The amplification of the received pulses of ultrasound was chosen so that multiple echoes not per the new transmitter into range. The process water, a penetration depth is achieved by 17,19 ms, corresponds to about 25 m or 984 inch. Figure 2: depth of penetration in process water Implementation The first investigations for the time being confined to water-based muds. Similar behavior was found for the water-based and oil-based sludge in [1]. The absolute sound speeds are about 200 to 250 m/s lower. 4 mud densities (11,3 lb/gal, 12 bl/gal, 15,6 bl/gal and 20,2 bl/gal) were produced for the experimental investigations. The blends consist of water, barite, bentonite, and methyl cellulose. Further additives like pot ash, salt, xanthan gum, starch, etc were not admitted. The mixture for the water-based mud with 12 bl/gal was, for example, as follows: Water 65,33 mass % Bentonite 3,73 mass % Barite 29,84 mass % Methyl cellulose 1,10 mass %
  • 3. IBJ Technology Ingenieurbüro Jäger Mud Density Penetration 50 rpm # 300 rpm # 500 rpm # 11,3 lb/gal* 157 inch 12,0 lb/gal 615 inch 587 inch 143 inch** 15,6 lb/gal 320 inch 347 inch 333 inch 20,2 lb/gal 198 inch 164 inch 119 inch IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 3 Results Of course the absolute sound speeds are also influenced by the salinity and temperature. Decides for the practicality, however, is the penetration depth in the mud and the behaviour under shear load through the rotating drill string. Table 1 shows the measurement results without shear load below. Mud Density Basis Sound Speed Penetration Time Length 1,35 kg/l 11,3 lb/gal Bentonite 1505,93 m/s 3,09 ms 465 cm 181 inch 1,44 kg/l 12,0 lb/gal Barite 1505,14 m/s 9,41 ms 1416 cm 552 inch 1,87 kg/l 15,6 lb/gal Barite 1498,36 m/s 7,22 ms 1082 cm 422 inch 2,42 kg/l 20,2 lb/gal Barite 1449,67 m/s 4,42 ms 641 cm 250 inch Table 1: Static penetration and sound speed The following tables show the measurement results with dynamic shear stress (strirrer rotation in rpm). #Rotation *Basis: Bentonite ** Stirrer trompe, air trapped in the Sound path. The resulting S of the speed of sound is the Path length in the air small. Table 2: Dynamic penetration Table 2 shows the dynamic penetration depth in different stirrer rotations per minute. The results for 20.2 lb/gal are constant without averaging Very much, because the viscosity of the mud is the highest. Thus, the flow conditions are Very much constant and little turbulence. Please note this is for all studies with the same constant reinforcement work was. The signal-to noise ratio would have approved a 20 to 40 dB higher gain of the received signal.
  • 4. IBJ Technology Ingenieurbüro Jäger Mud Density Ultrasound Speed 50 rpm # 300 rpm # 500 rpm # 18:22:30 18:27:30 18:32:30 18:37:30 18:42:30 18:47:30 18:52:30 IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 4 #Rotation *Basis: Bentonite ** Stirrer trompe, air trapped in the Sound path. The resulting S of the speed of sound is the Path length in the air small. Table 3: ultrasound speed under shear stress Table 3 are shown in dynamic ultrasonic speeds. For mud densities up to 15, lb/gal minor changes of the speed detected these amounted to less the maximum up to 1 m/s. At a density of the mud of 20, lb/gal, signified a proportional monotonically increasing velocity was measured. This increase amounted to around 2, m/s at 500 rpm. Figure 3 shows the significant increase in the speed of sound by shear stress. The slight increase of the curve is based on the influence of temperature. The influence of the shear stress on the speed moves in the 0,1 % area and is for the kick detection without meaning. A change of in temperature of 1° Celsius has even greater influence on the change of speed. Figure 3: Boost the speed 11,3 lb/gal * 1505,42 m/s 12,0 lb/gal 1505,13 m/s 1505,15 m/s 1433.65 m/s** 15,6 lb/gal 1499,88 m/s 1499.05 m/s 1498.97 m/s 20,2 lb/gal 1451,54 m/s 1452,12 m/s 1452,60 m/s h:min:s 1470 1465 1460 1455 1450 1445 1440 Schreiber 0
  • 5. IBJ Technology Ingenieurbüro Jäger 16:50:00 16:55:00 17:00:00 17:05:00 17:10:00 17:15:00 17:20:00 IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 5 Penetration depth and Non-Newtonian behavior The penetration rises at first monotonous after a standstill of the stirrer. The example of 12 bl/gal it was ms after 10 min over 10 ms. Then with a low rotation speed of about 50 rpm shear forces applied rpm, the penetration depth remains essentially at this size (9.96 ms). At about 500 rpm, the depth of half breaks together 4,8 ms with a variation of +-2 ms. The speed of sound drops further, it formed a stirring trompe between the sensors. Thus, the results are affected significantly. Too small values for the speed and depth are determined. With increasing time the penetration depth on 3 +-1ms (without averaging, real-time sampling). The speed remains relatively constant with the error by the trompe 1419 m/s. The mud 15.6 lb/gal starts at 1506,17 m/s and 0,83 ms penetration depth after a rest period of 24 hours without moving. More recently turning over 300 rpm monotonically in the subsequent peace on 5,16 ms penetration depth and the speed drops to 1501,63 m/s. The depth of penetration into the drilling mud under shear stress increases from 49 inch to 302 inch. Thus, the drilling mud shows the behavior of a Bingham fluid. The envelopes of the multiple echoes were recorded with the ADC. In the time range of the first multiple echoes until about 2 ms a decrease of the absorption of ultrasonic waves in the drilling mud witnessed as the drilling mud with the density of 20.2 lb/gal. She reflected in increase in the amplitude, so the following display (Figure 4) shows the dependence of the measured amplitudes at different speeds. This was reduced from 300 rpm 50 rpm (from 17: 00), and then click zero rpm (from 17:12). A higher speed causes a higher amplitude, or smaller absorption of ultrasonic waves. Figure 4: ultrasonic amplitude as a function of Speed h:min:s 4500 4000 3500 3000 2500 2000 1500 1000 500 3500 3250 3000 2750 2500 2250 2000 1750 1500 1250 1000 750 Schreiber 0 Schreiber 1
  • 6. IBJ Technology Ingenieurbüro Jäger 1750 1500 1250 1000 750 500 250 12:50:00 12:55:00 13:00:00 13:05:00 13:10:00 13:15:00 13:20:00 h:min:s Schreiber 0 Schreiber 1 400 375 350 325 300 12:47:30 12:52:30 12:57:30 13:02:30 13:07:30 13:12:30 13:17:30 h:min:s Schreiber 0 IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 6 Measurement without fluid The ultrasonic transducers are designed so the they in fluid and gas can measure (Fig. 5). With the used open experiment measurement can be demonstrated with gas only with air. The speed of sound drops when draining on 357 m/s. Due to the high resolution of 1 cm/s, even small changes in speed can be measured by dissolved gases. At a rate of 28 ms, a Very much fast display of real values is achieved even with a moving average from a variety of values. Figure 5 Change of the mud Figure 6 change the speed air-mud Figure 7 zoom speed in air Figure 6 shows the speed of sound in the phase of emptying and new filling with drilling mud. Figure 7 shows the zoom ultra sound velocity in air. The measurement of the velocity of gaseous and liquid hydrocarbons inflows cannot be determined with this open experiment. In the literature, there are about A few calculations and practical studies. The solubility of methane in diesel oil is in [3] consider. The effect of gas solubility is considered in [4]. The sound velocity of fluid-fluid mixtures and fluid-gas mixtures under pressure is investigated in [5]. Reflections on the sound speed in liquid-gas mixtures' water-air and water-steam are to find in [6].
  • 7. IBJ Technology Ingenieurbüro Jäger IBJ Technology, Colkwitzer Weg 7, 04416 Markkleeberg, GERMANY fmj@ibj-technology.com http:// www.ibj-technology.com 7 Conclusions The measurement of the speed of sound is practical with the concept of the Ultrasonic sensors. Interference by rotating drill strands are not to be expected. The depth and range of the sensors safely exceeds the damping of the mud. Even in the most absorbing mud (20.2 lb/gal), the penetration depth is 10 x the distance of the sensor. With an AGC (automatic gain control), the penetration depth in the drilling mud 20.2 can lb/gal on the 2 or 3 be lifted times. Thus one is 30 to 50 times security across the entire range. The absorption of ultrasound has no disturbing effect on a measurement of velocity or velocity high mud densities and viscosities at the selected frequencies of ultrasound and the transmission burst. The measurement of the flow of drilling mud is possible also with all commonly used drilling sludge and diameters of pipelines. It is measurable not disturbing increase of noise during the operation of the stirrer. References [1] Molz, E.; Canny, D.; Evans, E.; Baker Hughes INTEQ, Houston, Texas ” Ultrasonic Velocity and Attenuation Measurements in High Density Drilling Muds” SPWLA-1998-F,SPWLA 39th Annual Logging Symposium, 26-28 May, Keystone, Colorado, 1998 [2] Raeymaekers, B.; Pantea, C.; N. Sinha, D. N. “Creating a collimated ultrasound beam in highly attenuating fluids” Elsevier, Ultrasonics 52 (2012) 564–570 11 December 2011 [3] Atolini, T. M.; Ribeiro, P. R. “VAPOR-LIQUID MIXTURE BEHAVIOR AT HIGH TEMPERATURES AND PRESSURES : A REVIEW DIRECTED TO DRILLING ENGINEERING” Brazilian Journal of Petroleum and Gas. v. 1, n. 2, p. 123-130, 2007. ISSN 1982-0593 [4] Galves, L. V., Federal University of Rio de Janeiro; Gandelman, R. A.; Martins, A. L., Petrobras ” Impact of Gas Solubility on Kick Detection in N-Paraffin Based Drilling Fluids” Leandro Victalino Galves, Federal University of Rio de Janeiro; Roni Abensur Gandelman; André Leibsohn Martins, Petrobras 2014 AADE Fluids Technical Conference and Exhibition held at the Hilton Houston North Hotel, Houston, Texas, April 15- 16, 2014. [5] Liu, Y. ” ACOUSTIC PROPERTIES OF RESERVOIR FLUIDS” Dissertation, Stanford University, June, 1998 [6] Kiefer, S. W. ”Sound Speed in Liquid-Gas Mixtures' Water-Air and Water-Steam” VOL. 82, NO. 20 JOURNAL OF GEOPHYSICAL RESEARCH, JULY 10, 1977 Markkleeberg, September 2014