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· Issue 8 · Issue 1


Oil & Gas Automation
Solutions
is a publication
of Unico, Inc.

Since 1967

Unico, Inc.
3725 Nicholson Rd.
P. O. Box 0505
Franksville, WI
53126-0505
262.886.5678
262.504.7396 fax
oilgas@unicous.com
unicous.com

Power Quality Test Summary

 
 
THD
Conventional three-phase (six-pulse)
1
118.4%
1.00
0.64
0.64
Line reactor three-phase (six-pulse)
2
29.1%
0.97
0.96
0.93
Link choke three-phase (six-pulse)
3
31.3%
1.00
0.96
0.96
Reactor/choke three-phase (six-pulse)
4
23.8%
0.97
0.97
0.94
Transformer/reactor six-phase (12-pulse)
5
11.0%
0.98
0.99
0.97
Dual-output transformer six-phase (12-pulse)
6
7.8%
0.94
1.00
0.94
Triple-output transformer nine-phase (18-pulse)
7
4.3%
0.97
1.00
0.97
Harmonic eliminator
8
6.3%
1.00
0.99
0.99

Summary
The amounts by which actual systems deviate from this ideal standard are summarized in the above table for drives of various types operating at full load and full speed. Figures 1 through 8 show harmonic test results for various types of 100 hp PWM drive configurations.

Do you have questions about this article? If so, please contact us.



On-Line Correlations Calculator Updated

In the last issue of Solutions, Unico debuted its Correlations Calculator, a convenient tool for predicting the fluid properties of a well from limited information. The calculator implements published statistical relationships that estimate gas content and viscosity based upon field measurements. We introduced the first two correlations, the Standing and Beal methods. In this issue, we'd like to present two new ones, the Lasater and Chew-Connally methods.

Lasater Correlation
In 1958, J. A. Lasater developed a correlation for assessing gas content based upon 158 samples having the following range:

Bubble-point pressures:
48 to 5,780 psia
Reservoir temperature:
82° to 272° F
Gas/oil ratio: 3 to 2,905 scf/STB
API: 17.9° to 51.1°
Gas gravity: 0.574 to 1.223

The method was originally presented graphically using two charts, but equations were later fit to extend its usefulness.

The Lasater correlation determines gas/oil ratio from the oil API gravity and investigated pressure and temperature. Bubble-point pressure is estimated based upon the API gravity, gas/oil ratio, and investigated temperature. The method does not determine the oil formation volume factor or oil density.

Lasater's method is slightly more accurate in predicting bubble-point pressure than Standing's when each is applied to its original data set. Lasaster's agreed within 3.8% as compared to 4.8% with the Standing method.

Chew-Connally Correlation
J. Chew and C. A. Connally introduced their correlation for determining the viscosity of gas-saturated crude oils in 1959. The effect of dissolved gas is to lighten the oil and decrease its viscosity. Their study data was taken from wells in North and South America.

The Chew-Connally correlation estimates dead oil viscosity using the oil API gravity, gas/oil ratio, and investigated temperature. Saturated oil viscosity is based upon the dead oil viscosity and adjusted for the gas content using the gas/oil ratio. Gas/oil ratio can be estimated using a correlation such as Standing's or Lasater's. The method does not determine the unsaturated oil viscosity.

Try these and other methods for yourself using the Correlations Calculator at www.unicous.com/oilgas/corrcalc.php. We will update the calculator as new methods are introduced in future issues of Solutions.

For more information, please contact us.

In Future Issues...

Look for the following articles in upcoming issues of Oil & Gas Automation Solutions:

Field tests of methods to eliminate rod pump gas locking and interference
Reducing power consumption and improving power factor of beam pumps
Using a torque economizer mode to improve efficiency and reduce gearbox stress
Detecting stick/slip oscillations that fatigue rod-string couplings and reduce energy efficiency of PCPs
Control options to ride through power disturbances

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