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65 
ISSN 1516-8913 Printed in Brazil BRAZILIAN ARCHIVES OF 
Vol.49, Special : pp. 65-71, January 2006 
BIOLOGY AND TECHNOLOGY 
AN I N T E R N A T I O N A L J O U R N A L 
Influence of the Temperature, Pressure and Viscosity on the 
oil Measurement with Turbine Type Measurers 
Magalí Araújo Damasceno1*, Janaina Karla de Medeiros Penha1, Nivaldo Ferreira da Silva 
Junior1, Raimundo Nonato B. Felipe1, Renata Carla Tavares dos Santos Felipe1 and Gilson 
Gomes de Medeiros1,2 
1Centro Federal de Educação Tecnológica do Rio Grande do Norte - CEFET-RN; Av. Sen. Salgado Filho, 1559; 
Tirol; Natal - RN - Brasil. 2Universidade Federal do Rio Grande do Norte - UFRN/DEQ;Campus Universitário; 
Natal - RN - Brasil 
ABSTRACT 
The flow measurement of liquids and gases is a necessity in many industrial applications. There is a great amount of 
measurers for such purpose, as, for example, the coriolis, positive displacement and type turbine measurers. A 
measurer sufficiently used for the oil flow measurement is the turbine type, because it uses the proper extracted 
energy of the measured flow for its functioning, moreover is also used as standard for the calibration of other 
measurers. For this reason, it is important to study the parameters that influence the measurement process for 
turbine measurers. In Brazil, to measure the volume of oil, regardless the type of measurer, it is necessary to 
observe “Portaria Conjunta Nº. 1”, of June 19, 2000, that approved the Technical Regulation of Measurement of 
Oil and Natural Gas, establishing the minimum conditions and requirements for the systems of oil and natural gas 
measurement, in order to get a measurement standard. As such, the present work has the objective of determining 
parameters that influence in the measurement of oil volumes using turbine measurers. 
Key words: Oil, measurement, turbine 
The oil is the main worldwide energy source and 
the basic element for the modern industrial 
society. From its extraction, the fluid is measured 
to know the amount that each well and each field 
produces. 
The Brazilian norm “Portaria Conjunta Nº 1” 
(ANP/INMETRO, 2000) approved the use of 
several fluid measurers, such as the measurers type 
positive displacement, coriolis and measurers type 
turbines. Other types of measurers can be used, 
since its use is duly authorized by the National 
Agency of Oil - ANP. 
Brazilian Archives of Biology and Technology 
INTRODUCTION 
* Author for correspondence 
Each one of these tools has its proper principle of 
functioning and fields of application, determined 
by the work conditions , which include: type of 
fluid, temperature and other important factors. 
Therefore, to get a true value of a measurement of 
oil, it is necessary to know the involved 
parameters in the process. The result of a 
measurement can be evaluated by statistics 
methods or through variation of the factors of 
which this result depends on, with the objective to 
guarantee the certainty in the measurement of the 
produced and transferred volumes. 
The turbine types of the industrial series are used 
as the instrument of measurement for oil and its
Damasceno, M. A. et al. 
Brazilian Archives of Biology and Technology 
66 
derivatives and gases. There are several types of 
turbines, depending on the positioning of axle of 
the rotor in relation to the flow, as well as the 
methods of measuring their rotations. 
Some turbine types are purely mechanical and 
others are equipped with sophisticated electronic 
secondary elements. The measurer turbine is also 
used as standard for the calibration of other 
measurers. 
In this type of measurer, the exit of pulses is 
convenient for the direct totaling of the flow. The 
linear relation between the frequency and the flow 
results in great range of measuring (Ribeiro, 
1997). 
The conventional measurer is a type of turbine that 
is sufficiently used because the rotor is made with 
longitudinal axle to the flow, integral bifool and 
has approximately equal diameter to the one of the 
tubing, as seen in the figure 1. It shows a great 
performance and the highest precision, linearity 
and repeatability, and is very much used for the 
calibration of other measurers (Ribeiro, 1997). 
The measurer consists basically of a rotor with 
vanes that are put inside the perpendicular tubing 
the flow. The fluid to be measured stimulates the 
rotor and it makes it turn in a definite angular 
speed. The rotational speed of the vanes is directly 
proportional to the flow and can be detected by a 
mechanical or electric sensor, which can get the 
value of the flow from the passage of the blades of 
the rotor of the turbine. 
Figure 1 - Constituent parts of the conventional measurer 
turbine type. From Ribeiro (1997). 
The exit signal is practically linear, therefore each 
pulse corresponds to one certain volume. The 
number of pulses for unit of flow is called factor K 
of the turbine. This factor varies according to the 
flow intensity, the pressure and the operating 
temperature. 
This work aims to analyze the parameters that 
come to influence in the measurement of oil. 
Three basic parameters of the measurers type 
turbine were evaluated: firstly, the influence of the 
temperature, which provides an error in case the 
density is not corrected in the measurement 
process and in case of bad distribution of the 
temperature in the fluid; the second factor is the 
influence of the viscosity, whose increase 
provokes a reduction of factor K of the measurer; 
and, finally, the influence of the pressure. 
METHODOLOGY 
The methodology used in this work consisted in 
the accomplishment of a bibliographical research 
on the oil measurer turbine, the norms that 
establish the measurement and correction, as well 
as a simulation of data, in order to evaluate the 
parameters that influence in the process of 
measurement of oil. 
The study was developed on the basis of the 
standards established by the norms “Portaria 
Conjunta Nº 1” (ANP/INMETRO, 2000), ISO 
4267 (1988) and the “Resolução nº 06/70” (CNP, 
1970), which aims to establish the reliability of 
the procedures of flow measurement of the Oil by 
turbine type measurers.. 
Influence of the temperature on the 
correction of the measured volume of oil 
The temperature of the measured liquid affects the 
performance of the turbine, due to a mechanical 
effect caused by the expansion or thermal 
contraction of the box and the turbine, when the 
operating temperature is different from the 
temperature of calibration. The variation of the 
temperature affects the physical properties of the 
measured fluid, such as its vapor pressure, density 
and viscosity. 
The right measurement of the temperature is one 
of the most important factors in the operations, in 
view of that small variations can present great 
errors because of bad distribution of the 
temperature of the fluid, intervening the
Influence of the Temperature, Pressure and Viscosity on the oil Measurement 
Brazilian Archives of Biology and Technology 
67 
conversion of the volumes of the products for the 
temperature standard of 20 ºC, adopted as 
temperature of reference for the measurement of 
derivatives of the oil, in accordance with “Portaria 
nº 27” (MIC, 1959). 
Therefore, it is also necessary to measure the 
temperature of the product and to correct the 
volume at room temperature for the standard 
temperature, as mentioned in the previous 
paragraph. This correction uses a factor which is 
obtained from the collecting of a representative 
sample of the product, in view of the correction of 
the thermal expansion among the temperature 
reference and the temperature of measurement, 
through the correction of the density of the oil 
measured in the conditions of work to 20 ºC, 
according the norm of the National Council of 
Petroleum, “Resolução nº 06/70” (CNP, 1970). 
The absence of correction of the density generates 
an error in function of the temperature of the oil. 
Therefore, the need for this correction for the 
attainment of more accurate measured volumes is 
evident. 
For the simulation, a sample of oil with estimated 
density of 0.7852 g/m3 (representative average 
value) in the work condition was used, for the 
volumes established in table 1. On the other hand, 
for the determination of the influence of the 
temperature in the correction of the measured 
volume of oil, the temperatures of work were 
considered in accordance with table 2. 
Table 1 - Dimensions of the analyzed measurers. 
Measurer specifications 
Identification of the 
measurer Nominal diameter of the tubing 
(mm) 
Maximum flow 
(m3/h) 
M1 25 2 
M2 250 1200 
M3 500 6000 
Tabela 2 - Operation temperatures. 
Temperatures (ºC) 
Temperature 1 26 
Temperature 2 28 
Temperature 3 30 
Temperature 4 32 
Temperature 5 34 
Temperature 6 36 
Influence of viscosity on the correction of 
the measured volume of oil 
The value of a measurement made for a measurer 
turbine is affected by changes in the viscosity of 
the fluid to be measured. The viscosity of the 
liquid is dependent on the temperature. Therefore, 
with the increase of the temperature a reduction of 
viscosity occurs and, consequently, the 
performance of the turbine is modified. 
The measurement of kinematics viscosity is 
desirable when the operation occurs at a great 
range of temperature or at very low flows, and 
mainly when a great precision is desired. 
The linear range of the measurer is one of the 
more affected parameters by the variation of 
viscosity, specially if the turbine presents parallel 
blades. This variation depends on the type of the 
rotor. For a kinematics viscosity above of 100 cSt, 
the turbine does not present the linear region 
(Ribeiro, 1997). 
For the same pressure, the flow diminishes when 
the fluid viscosity increases. For a given flow, an 
increase of viscosity can present a reduction in the 
factor K of the measurer. 
Influence of the pressure on the correction 
of the measured volume of oil 
When the compressibility has a considerable 
value, it is important to measure the pressure to 
allow the correction of the measured flow. 
The variation of the pressure causes changes in the 
physical dimensions of the measurer due to 
pressure made by the liquid, leading to an
Damasceno, M. A. et al. 
18.00 
16.00 
14.00 
12.00 
10.00 
8.00 
6.00 
Brazilian Archives of Biology and Technology 
68 
expansion or contraction of the box measurer, as 
established by the norm ISO 2715 (1980). 
According to Ribeiro (1997), if the pressure of the 
liquid approaches to its vapor pressure, the local 
vaporization can happen soon behind the vanes of 
the rotor. This provokes an artificial increase in the 
speed of the fluid, which can drastically affect the 
factor K. 
The variation of the pressure in meter is 
proportional to the square of the flow. To have a 
constant entrance, a maximum flow is necessary, 
in which the measuring turbine can be operated 
with an acceptable margin of error. This happens 
due to the effect caused by the cavitation in the 
measurer, that is the boiling of the liquid 
originated for the reduction in the pressure, instead 
of the temperature rise. 
It is important to remember that, for any 
installation, the downstream turbine flow needs to 
be kept to a minimum pressure to prevent a 
variation in the calibration factor due the 
cavitation. The minimum pressure after the turbine 
is function of the vapor pressure of the liquid and 
the presence of dissolved gases. 
M1 
0.040 
0.030 
0.020 
0.010 
0.000 
26 28 30 32 34 36 
Temperature (ºC) 
• V (m 3 ) 
Figure 2 - Variation of the measured volume by the M1 measurer due to the correction of the 
density for the reference temperature, after one hour operation. 
M2 
4.00 
26 28 30 32 34 36 
Temperature (ºC) 
• V (m3) 
Figure 3 - Variation of the measured volume by the M2 measurer due to the correction of the 
density for the reference temperature, after one hour operation.
Influence of the Temperature, Pressure and Viscosity on the oil Measurement 
100.00 
80.00 
60.00 
40.00 
Brazilian Archives of Biology and Technology 
69 
M3 
20.00 
26 28 30 32 34 36 
Temperature (ºC) 
• V (m 3) 
Figure 4 - Variation of the measured volume by the M3 measurer due to the correction of the 
density for the reference temperature, after one hour operation. 
Figure 5 - Influence of viscosity on the meter factor of the turbine (Faure Herman, 2004). 
RESULTS AND DISCUSSION 
Influence of the temperature 
The obtained results from the simulation of the 
measured volumes of oil, according to the norm 
“Portaria Conjunta Nº 01” (ANP/INMETRO, 
2000), must be corrected to the reference 
temperature (20 ºC). 
Taking an oil sample with density of 0.7852 g/m3 
(representative average value), it is observed that 
the variation of volume, due to the correction in 
function of the operation temperature, is linear, as 
shown in Figures 2, 3 and 4, when the 
measurement system is evaluated in the range 
from 26 ºC to 36 ºC. 
It can be stated that, if the density is not corrected 
from the actual oil temperature to the reference 
temperature, an error is generated, thus influencing 
in the measurement of the oil volume. So, it can be 
concluded that this correction is necessary to 
obtain more accurate measured volumes.
Damasceno, M. A. et al. 
Brazilian Archives of Biology and Technology 
70 
Influence of the oil viscosity 
Figure 5 shows the variation of the meter factor 
(correction factor of the measurer) in function of 
the flow, for different oil viscosities, when a 8” 
diameter measurer is used (Faure Herman, 2004). 
It can observed that, for a viscosity of 108 cSt 
(blue curve), an substancial reduction in the meter 
factor occurs reaching the flow of 2500 Bbl/h, and 
that above this value the factor remains steady. 
For an intermediate viscosity, as 49.2 cSt (green 
curve), we can say that its result is not different 
from the blue curve. The meter factor, even lower 
than 108 cSt, also decreases up to 2000 Bbl/h, 
remaining steady to higher flow values. For a 
viscosity of 0.62 cSt (gray curve), the meter factor 
practically remains steady. 
Figure 6 shows the influence of viscosity in the 
pressure drop (loss of load) of the turbine 
measurer type. It can be observed that this drop 
varies not linearly with viscosity. For the range of 
viscosity from 0 to 100 cSt, the drop varied from 
0.2 to 0.5 bar. 
0.6 
0.5 
0.4 
0.3 
0.2 
0.1 
0 
0 10 20 30 40 50 60 70 80 90 100 
Viscosity (cSt) 
Loss of Load (bar) 
Figure 6 - Pressure drop as function of viscosity. Adapted from Faure Herman (2004). 
CONCLUSION 
O estudo dos parâmetros, variabilidades e a forma 
de apresentação dos resultados, proporcionaram 
uma visão geral do desempenho do medidor 
turbina, assim como a simulação de dados 
contribuiu para a quantificação destes resultados 
observados. Caracterizando-se as variabilidades 
quanto ao desempenho do medidor, bem como 
suas faixas de influências, é possível concretizar as 
aplicações de medidores turbinas na indústria de 
petróleo. A forma de apresentação dos resultados 
irá permitir a comparação de desempenho de 
medidores turbinas com outros medidores de 
vazão. 
The study of the influence of the analyzed 
parameters provided a general view about the 
performance of the turbine measurer type. The 
data simulation contributed for the quantification 
of the results. The characterization of the 
performance of the measurers in the face of the 
variations in those parameters, as well as its ranges 
of influence, made the applications of measurer 
turbines in the oil industry possible.The 
presentation of the results will allow the 
comparison between the performance of turbine 
and other flow measurers. 
ACKNOWLEDGEMENTS 
This work was undertaken as part of the research 
project "Uncertainty of Measurement of Oil and 
Natural Gas", included in the Rede de 
Instrumentação e Controle (Rede 10/05). The 
authors are grateful to the Finep, CNPq e 
CENPES-Petrobras, for the financial support, 
which was essential for its accomplishment.
Influence of the Temperature, Pressure and Viscosity on the oil Measurement 
Brazilian Archives of Biology and Technology 
71 
RESUMO 
A medição de fluxo em líquidos e gases é uma 
necessidade em muitas aplicações industriais. 
Existe uma grande quantidade de medidores para 
tal finalidade, como, por exemplo, os medidores 
de velocidade tipo turbina, deslocamento positivo 
e coriolis. Um medidor bastante utilizado para a 
medição de vazão de petróleo é o tipo turbina, 
porque utiliza a própria energia extraída da vazão 
medida para seu funcionamento. Além disso, é 
também usado como padrão para a calibração de 
outros medidores. Daí a importância de se estudar 
os parâmetros que influenciam o processo de 
medição por medidores tipo turbina. Para se medir 
o volume de petróleo, independentemente do tipo 
de medidor, é necessário observar o que determina 
a Portaria Conjunta Nº. 1, de 19 de junho de 2000, 
que aprovou o Regulamento Técnico de Medição 
de Petróleo e Gás Natural, estabelecendo as 
condições e requisitos mínimos para os sistemas 
de medição de petróleo e gás natural, a fim de se 
obter um padrão de medição. Com isso, este 
trabalho visa determinar os parâmetros que 
influenciam na medição de volumes de petróleo 
utilizando medidores do tipo turbina. 
REFERENCES 
ANP/INMETRO (2000), Portaria Conjunta n. 01. 
Regulamento técnico da medição de petróleo e gás 
natural. 
CNP (1970), Resolução n. 06/70. Tabelas de correção 
de volume do petróleo e derivados. 
Delmée. G. J. (1982), Manual de medição de vazão. 
São Paulo: Edgard Blücher. 
Faure Herman (2004), HELIFLUTM TZN, the dedicated 
turbine flowmeter for custody transfer measurement. 
Disp. in: http://www.faureherman.com/download/ 
tzn.pdf. 
ISO 2715 (1980), Liquid Hydrocarbons - Volumetric 
Measurement by Turbine Meter Systems. 
ISO 4267 (1988), Petroleum and liquid petroleum 
products - Calculation of oil quantities - Part 2: 
Dynamic measurement. 
Ministério da Indústria e Comércio (1959), Portaria 
n. 27/59. 
Ribeiro, M. A. (1997), Medição de vazão - 
fundamentos e aplicações. Salvador: Tek 
Treinamento & Consultoria. 
Received: July 29, 2005; 
Revised: September 05, 2005; 
Accepted: November 22, 2005.
FOLHA 
EM 
BRANCO

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  • 1. 65 ISSN 1516-8913 Printed in Brazil BRAZILIAN ARCHIVES OF Vol.49, Special : pp. 65-71, January 2006 BIOLOGY AND TECHNOLOGY AN I N T E R N A T I O N A L J O U R N A L Influence of the Temperature, Pressure and Viscosity on the oil Measurement with Turbine Type Measurers Magalí Araújo Damasceno1*, Janaina Karla de Medeiros Penha1, Nivaldo Ferreira da Silva Junior1, Raimundo Nonato B. Felipe1, Renata Carla Tavares dos Santos Felipe1 and Gilson Gomes de Medeiros1,2 1Centro Federal de Educação Tecnológica do Rio Grande do Norte - CEFET-RN; Av. Sen. Salgado Filho, 1559; Tirol; Natal - RN - Brasil. 2Universidade Federal do Rio Grande do Norte - UFRN/DEQ;Campus Universitário; Natal - RN - Brasil ABSTRACT The flow measurement of liquids and gases is a necessity in many industrial applications. There is a great amount of measurers for such purpose, as, for example, the coriolis, positive displacement and type turbine measurers. A measurer sufficiently used for the oil flow measurement is the turbine type, because it uses the proper extracted energy of the measured flow for its functioning, moreover is also used as standard for the calibration of other measurers. For this reason, it is important to study the parameters that influence the measurement process for turbine measurers. In Brazil, to measure the volume of oil, regardless the type of measurer, it is necessary to observe “Portaria Conjunta Nº. 1”, of June 19, 2000, that approved the Technical Regulation of Measurement of Oil and Natural Gas, establishing the minimum conditions and requirements for the systems of oil and natural gas measurement, in order to get a measurement standard. As such, the present work has the objective of determining parameters that influence in the measurement of oil volumes using turbine measurers. Key words: Oil, measurement, turbine The oil is the main worldwide energy source and the basic element for the modern industrial society. From its extraction, the fluid is measured to know the amount that each well and each field produces. The Brazilian norm “Portaria Conjunta Nº 1” (ANP/INMETRO, 2000) approved the use of several fluid measurers, such as the measurers type positive displacement, coriolis and measurers type turbines. Other types of measurers can be used, since its use is duly authorized by the National Agency of Oil - ANP. Brazilian Archives of Biology and Technology INTRODUCTION * Author for correspondence Each one of these tools has its proper principle of functioning and fields of application, determined by the work conditions , which include: type of fluid, temperature and other important factors. Therefore, to get a true value of a measurement of oil, it is necessary to know the involved parameters in the process. The result of a measurement can be evaluated by statistics methods or through variation of the factors of which this result depends on, with the objective to guarantee the certainty in the measurement of the produced and transferred volumes. The turbine types of the industrial series are used as the instrument of measurement for oil and its
  • 2. Damasceno, M. A. et al. Brazilian Archives of Biology and Technology 66 derivatives and gases. There are several types of turbines, depending on the positioning of axle of the rotor in relation to the flow, as well as the methods of measuring their rotations. Some turbine types are purely mechanical and others are equipped with sophisticated electronic secondary elements. The measurer turbine is also used as standard for the calibration of other measurers. In this type of measurer, the exit of pulses is convenient for the direct totaling of the flow. The linear relation between the frequency and the flow results in great range of measuring (Ribeiro, 1997). The conventional measurer is a type of turbine that is sufficiently used because the rotor is made with longitudinal axle to the flow, integral bifool and has approximately equal diameter to the one of the tubing, as seen in the figure 1. It shows a great performance and the highest precision, linearity and repeatability, and is very much used for the calibration of other measurers (Ribeiro, 1997). The measurer consists basically of a rotor with vanes that are put inside the perpendicular tubing the flow. The fluid to be measured stimulates the rotor and it makes it turn in a definite angular speed. The rotational speed of the vanes is directly proportional to the flow and can be detected by a mechanical or electric sensor, which can get the value of the flow from the passage of the blades of the rotor of the turbine. Figure 1 - Constituent parts of the conventional measurer turbine type. From Ribeiro (1997). The exit signal is practically linear, therefore each pulse corresponds to one certain volume. The number of pulses for unit of flow is called factor K of the turbine. This factor varies according to the flow intensity, the pressure and the operating temperature. This work aims to analyze the parameters that come to influence in the measurement of oil. Three basic parameters of the measurers type turbine were evaluated: firstly, the influence of the temperature, which provides an error in case the density is not corrected in the measurement process and in case of bad distribution of the temperature in the fluid; the second factor is the influence of the viscosity, whose increase provokes a reduction of factor K of the measurer; and, finally, the influence of the pressure. METHODOLOGY The methodology used in this work consisted in the accomplishment of a bibliographical research on the oil measurer turbine, the norms that establish the measurement and correction, as well as a simulation of data, in order to evaluate the parameters that influence in the process of measurement of oil. The study was developed on the basis of the standards established by the norms “Portaria Conjunta Nº 1” (ANP/INMETRO, 2000), ISO 4267 (1988) and the “Resolução nº 06/70” (CNP, 1970), which aims to establish the reliability of the procedures of flow measurement of the Oil by turbine type measurers.. Influence of the temperature on the correction of the measured volume of oil The temperature of the measured liquid affects the performance of the turbine, due to a mechanical effect caused by the expansion or thermal contraction of the box and the turbine, when the operating temperature is different from the temperature of calibration. The variation of the temperature affects the physical properties of the measured fluid, such as its vapor pressure, density and viscosity. The right measurement of the temperature is one of the most important factors in the operations, in view of that small variations can present great errors because of bad distribution of the temperature of the fluid, intervening the
  • 3. Influence of the Temperature, Pressure and Viscosity on the oil Measurement Brazilian Archives of Biology and Technology 67 conversion of the volumes of the products for the temperature standard of 20 ºC, adopted as temperature of reference for the measurement of derivatives of the oil, in accordance with “Portaria nº 27” (MIC, 1959). Therefore, it is also necessary to measure the temperature of the product and to correct the volume at room temperature for the standard temperature, as mentioned in the previous paragraph. This correction uses a factor which is obtained from the collecting of a representative sample of the product, in view of the correction of the thermal expansion among the temperature reference and the temperature of measurement, through the correction of the density of the oil measured in the conditions of work to 20 ºC, according the norm of the National Council of Petroleum, “Resolução nº 06/70” (CNP, 1970). The absence of correction of the density generates an error in function of the temperature of the oil. Therefore, the need for this correction for the attainment of more accurate measured volumes is evident. For the simulation, a sample of oil with estimated density of 0.7852 g/m3 (representative average value) in the work condition was used, for the volumes established in table 1. On the other hand, for the determination of the influence of the temperature in the correction of the measured volume of oil, the temperatures of work were considered in accordance with table 2. Table 1 - Dimensions of the analyzed measurers. Measurer specifications Identification of the measurer Nominal diameter of the tubing (mm) Maximum flow (m3/h) M1 25 2 M2 250 1200 M3 500 6000 Tabela 2 - Operation temperatures. Temperatures (ºC) Temperature 1 26 Temperature 2 28 Temperature 3 30 Temperature 4 32 Temperature 5 34 Temperature 6 36 Influence of viscosity on the correction of the measured volume of oil The value of a measurement made for a measurer turbine is affected by changes in the viscosity of the fluid to be measured. The viscosity of the liquid is dependent on the temperature. Therefore, with the increase of the temperature a reduction of viscosity occurs and, consequently, the performance of the turbine is modified. The measurement of kinematics viscosity is desirable when the operation occurs at a great range of temperature or at very low flows, and mainly when a great precision is desired. The linear range of the measurer is one of the more affected parameters by the variation of viscosity, specially if the turbine presents parallel blades. This variation depends on the type of the rotor. For a kinematics viscosity above of 100 cSt, the turbine does not present the linear region (Ribeiro, 1997). For the same pressure, the flow diminishes when the fluid viscosity increases. For a given flow, an increase of viscosity can present a reduction in the factor K of the measurer. Influence of the pressure on the correction of the measured volume of oil When the compressibility has a considerable value, it is important to measure the pressure to allow the correction of the measured flow. The variation of the pressure causes changes in the physical dimensions of the measurer due to pressure made by the liquid, leading to an
  • 4. Damasceno, M. A. et al. 18.00 16.00 14.00 12.00 10.00 8.00 6.00 Brazilian Archives of Biology and Technology 68 expansion or contraction of the box measurer, as established by the norm ISO 2715 (1980). According to Ribeiro (1997), if the pressure of the liquid approaches to its vapor pressure, the local vaporization can happen soon behind the vanes of the rotor. This provokes an artificial increase in the speed of the fluid, which can drastically affect the factor K. The variation of the pressure in meter is proportional to the square of the flow. To have a constant entrance, a maximum flow is necessary, in which the measuring turbine can be operated with an acceptable margin of error. This happens due to the effect caused by the cavitation in the measurer, that is the boiling of the liquid originated for the reduction in the pressure, instead of the temperature rise. It is important to remember that, for any installation, the downstream turbine flow needs to be kept to a minimum pressure to prevent a variation in the calibration factor due the cavitation. The minimum pressure after the turbine is function of the vapor pressure of the liquid and the presence of dissolved gases. M1 0.040 0.030 0.020 0.010 0.000 26 28 30 32 34 36 Temperature (ºC) • V (m 3 ) Figure 2 - Variation of the measured volume by the M1 measurer due to the correction of the density for the reference temperature, after one hour operation. M2 4.00 26 28 30 32 34 36 Temperature (ºC) • V (m3) Figure 3 - Variation of the measured volume by the M2 measurer due to the correction of the density for the reference temperature, after one hour operation.
  • 5. Influence of the Temperature, Pressure and Viscosity on the oil Measurement 100.00 80.00 60.00 40.00 Brazilian Archives of Biology and Technology 69 M3 20.00 26 28 30 32 34 36 Temperature (ºC) • V (m 3) Figure 4 - Variation of the measured volume by the M3 measurer due to the correction of the density for the reference temperature, after one hour operation. Figure 5 - Influence of viscosity on the meter factor of the turbine (Faure Herman, 2004). RESULTS AND DISCUSSION Influence of the temperature The obtained results from the simulation of the measured volumes of oil, according to the norm “Portaria Conjunta Nº 01” (ANP/INMETRO, 2000), must be corrected to the reference temperature (20 ºC). Taking an oil sample with density of 0.7852 g/m3 (representative average value), it is observed that the variation of volume, due to the correction in function of the operation temperature, is linear, as shown in Figures 2, 3 and 4, when the measurement system is evaluated in the range from 26 ºC to 36 ºC. It can be stated that, if the density is not corrected from the actual oil temperature to the reference temperature, an error is generated, thus influencing in the measurement of the oil volume. So, it can be concluded that this correction is necessary to obtain more accurate measured volumes.
  • 6. Damasceno, M. A. et al. Brazilian Archives of Biology and Technology 70 Influence of the oil viscosity Figure 5 shows the variation of the meter factor (correction factor of the measurer) in function of the flow, for different oil viscosities, when a 8” diameter measurer is used (Faure Herman, 2004). It can observed that, for a viscosity of 108 cSt (blue curve), an substancial reduction in the meter factor occurs reaching the flow of 2500 Bbl/h, and that above this value the factor remains steady. For an intermediate viscosity, as 49.2 cSt (green curve), we can say that its result is not different from the blue curve. The meter factor, even lower than 108 cSt, also decreases up to 2000 Bbl/h, remaining steady to higher flow values. For a viscosity of 0.62 cSt (gray curve), the meter factor practically remains steady. Figure 6 shows the influence of viscosity in the pressure drop (loss of load) of the turbine measurer type. It can be observed that this drop varies not linearly with viscosity. For the range of viscosity from 0 to 100 cSt, the drop varied from 0.2 to 0.5 bar. 0.6 0.5 0.4 0.3 0.2 0.1 0 0 10 20 30 40 50 60 70 80 90 100 Viscosity (cSt) Loss of Load (bar) Figure 6 - Pressure drop as function of viscosity. Adapted from Faure Herman (2004). CONCLUSION O estudo dos parâmetros, variabilidades e a forma de apresentação dos resultados, proporcionaram uma visão geral do desempenho do medidor turbina, assim como a simulação de dados contribuiu para a quantificação destes resultados observados. Caracterizando-se as variabilidades quanto ao desempenho do medidor, bem como suas faixas de influências, é possível concretizar as aplicações de medidores turbinas na indústria de petróleo. A forma de apresentação dos resultados irá permitir a comparação de desempenho de medidores turbinas com outros medidores de vazão. The study of the influence of the analyzed parameters provided a general view about the performance of the turbine measurer type. The data simulation contributed for the quantification of the results. The characterization of the performance of the measurers in the face of the variations in those parameters, as well as its ranges of influence, made the applications of measurer turbines in the oil industry possible.The presentation of the results will allow the comparison between the performance of turbine and other flow measurers. ACKNOWLEDGEMENTS This work was undertaken as part of the research project "Uncertainty of Measurement of Oil and Natural Gas", included in the Rede de Instrumentação e Controle (Rede 10/05). The authors are grateful to the Finep, CNPq e CENPES-Petrobras, for the financial support, which was essential for its accomplishment.
  • 7. Influence of the Temperature, Pressure and Viscosity on the oil Measurement Brazilian Archives of Biology and Technology 71 RESUMO A medição de fluxo em líquidos e gases é uma necessidade em muitas aplicações industriais. Existe uma grande quantidade de medidores para tal finalidade, como, por exemplo, os medidores de velocidade tipo turbina, deslocamento positivo e coriolis. Um medidor bastante utilizado para a medição de vazão de petróleo é o tipo turbina, porque utiliza a própria energia extraída da vazão medida para seu funcionamento. Além disso, é também usado como padrão para a calibração de outros medidores. Daí a importância de se estudar os parâmetros que influenciam o processo de medição por medidores tipo turbina. Para se medir o volume de petróleo, independentemente do tipo de medidor, é necessário observar o que determina a Portaria Conjunta Nº. 1, de 19 de junho de 2000, que aprovou o Regulamento Técnico de Medição de Petróleo e Gás Natural, estabelecendo as condições e requisitos mínimos para os sistemas de medição de petróleo e gás natural, a fim de se obter um padrão de medição. Com isso, este trabalho visa determinar os parâmetros que influenciam na medição de volumes de petróleo utilizando medidores do tipo turbina. REFERENCES ANP/INMETRO (2000), Portaria Conjunta n. 01. Regulamento técnico da medição de petróleo e gás natural. CNP (1970), Resolução n. 06/70. Tabelas de correção de volume do petróleo e derivados. Delmée. G. J. (1982), Manual de medição de vazão. São Paulo: Edgard Blücher. Faure Herman (2004), HELIFLUTM TZN, the dedicated turbine flowmeter for custody transfer measurement. Disp. in: http://www.faureherman.com/download/ tzn.pdf. ISO 2715 (1980), Liquid Hydrocarbons - Volumetric Measurement by Turbine Meter Systems. ISO 4267 (1988), Petroleum and liquid petroleum products - Calculation of oil quantities - Part 2: Dynamic measurement. Ministério da Indústria e Comércio (1959), Portaria n. 27/59. Ribeiro, M. A. (1997), Medição de vazão - fundamentos e aplicações. Salvador: Tek Treinamento & Consultoria. Received: July 29, 2005; Revised: September 05, 2005; Accepted: November 22, 2005.