Micro Motion 3000 9 wire Net Oil Computer Manual Manuals & Guides

ALTUS
Net Oil Computer Manual
May 2000
ALTUS
Net Oil Computer Manual
For technical assistance, phone the Micro Motion Customer Service Department:
• In the U.S.A., phone 1-800-522-6277, 24 hours
• In Europe, phone +31 (0) 318 549 443
• In Asia, phone (65) 770-8155
Copyright ©1998, Micro Motion, Inc. A l l rig h ts res erved.
Micro Motion, ELITE, and BASIS are registered trademarks, and ALTUS is a trademark of Micro Mo tion, Inc., Boulder, Colorado. Hastelloy is a registered trademark of Haynes International, Inc., Kokomo Indiana. Inconel is a re gi st er ed trademark of Inco Alloys International, Inc., Huntington, West Virginia. Teflon is a registered trademar k of E.I. DuPont de Nemours Co., Inc., Wilmington, Delaware.
Contents
1 Before You Begin
1.1 About this manual . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1
1.2 Application software described in this manual. . . . . . . 1
1.3 Introduction to the ALTUS
Replacing an older NOC and transmitter. . . . . . . . . . . 1
Water cut determination . . . . . . . . . . . . . . . . . . . . . . . 1
NOC capabilities . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2
2 Installation Considerations
2.1 Piping arrangement and ancillary equipment . . . . . . . 3
2.2 Sensor installation . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5
Sensor orientation . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5
Avoiding inaccurate flow counts . . . . . . . . . . . . . . . . . 6
2.3 Flow direction . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7
3 Using the Person-Process Interface
3.1 Person-Process Interface . . . . . . . . . . . . . . . . . . . . . . 9
3.2 Security button. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 10
3.3 Function buttons . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11
3.4 Cursor control buttons . . . . . . . . . . . . . . . . . . . . . . . . . 12
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
NOC . . . . . . . . . . . . . . . . 1
. . . . . . . . . . . . . . . . . . . . .
. . . . . . . . . .
1
3
9
ALTUS™ Net Oil Computer Manu al
4 Configuration
4.1 Recording the configuration. . . . . . . . . . . . . . . . . . . . . 15
4.2 Configuration sequence. . . . . . . . . . . . . . . . . . . . . . . . 15
Step 1 Configure well performance measurements . . . . . . . . 15
Mode of operation . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16
Units of measurement . . . . . . . . . . . . . . . . . . . . . . . . . 16
Well data-densities . . . . . . . . . . . . . . . . . . . . . . . . . . . 17
Compensations . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 21
Step 2 Configure system data. . . . . . . . . . . . . . . . . . . . . . . . . 24
Step 3 Configure inputs . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25
Flow variables . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25
Density inputs . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 26
Temperature . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 27
Sensor calibration data . . . . . . . . . . . . . . . . . . . . . . . . 28
Sensor information . . . . . . . . . . . . . . . . . . . . . . . . . . . 35
Step 4 Configure outputs . . . . . . . . . . . . . . . . . . . . . . . . . . . . 36
Discrete outputs. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 36
Milliamp outputs. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 37
Pulse output. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 40
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
15
i
Contents
continued
5 Using the View Menu
5.1 Accessing the view menu . . . . . . . . . . . . . . . . . . . . . . 43
5.2 Well performance measurements . . . . . . . . . . . . . . . . 44
Continuous mode. . . . . . . . . . . . . . . . . . . . . . . . . . . . . 44
Well test mode . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 44
5.3 Process totalizers. . . . . . . . . . . . . . . . . . . . . . . . . . . . . 45
5.4 Inventory totalizers. . . . . . . . . . . . . . . . . . . . . . . . . . . . 46
5.5 Active alarm log . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 47
5.6 LCD options . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 47
5.7 Diagnostic monitor. . . . . . . . . . . . . . . . . . . . . . . . . . . . 48
5.8 Applications list . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 48
5.9 Power outage. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 48
6 Continuous Mode
6.1 Continuous mode configuration . . . . . . . . . . . . . . . . . . 49
6.2 Startup and display test . . . . . . . . . . . . . . . . . . . . . . . . 49
6.3 Process monitor. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 49
6.4 Accessing continuous mode . . . . . . . . . . . . . . . . . . . . 49
6.5 Viewing production measurements . . . . . . . . . . . . . . . 50
6.6 Quick view . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 52
6.7 Pause and resume. . . . . . . . . . . . . . . . . . . . . . . . . . . . 52
6.8 Reset . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 54
. . . . . . . . . . . . . . . . . . . . . . . . . . .
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
43
49
7 Well Test Mode
7.1 Well test mode configuration . . . . . . . . . . . . . . . . . . . . 55
7.2 Startup and display test . . . . . . . . . . . . . . . . . . . . . . . . 55
7.3 Process monitor. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 55
7.4 Accessing well test mode. . . . . . . . . . . . . . . . . . . . . . . 55
7.5 Conducting a well test . . . . . . . . . . . . . . . . . . . . . . . . . 56
7.6 Stopping and continuing a well test . . . . . . . . . . . . . . . 58
7.7 Viewing performance measurements . . . . . . . . . . . . . 60
7.8 Viewing performance measurements for the
current test. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 61
7.9 Viewing previous well tests . . . . . . . . . . . . . . . . . . . . . 63
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
55
ii
ALTUS™ Net Oil Computer Manu al
Contents
continued
8 Maintenance
8.1 Alarm messages . . . . . . . . . . . . . . . . . . . . . . . . . . . . 67
Responding to alarms . . . . . . . . . . . . . . . . . . . . . . . . 67
NOC alarm messages . . . . . . . . . . . . . . . . . . . . . . . . 68
Transmitter alarm messages. . . . . . . . . . . . . . . . . . . 68
Alarms that do not generate fault outputs . . . . . . . . . 69
Fault outputs . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 73
Critical status fault alarms . . . . . . . . . . . . . . . . . . . . . 74
Transmitter failure fault alarms . . . . . . . . . . . . . . . . . 74
Fault alarms requiring troubleshooting . . . . . . . . . . . 75
Active alarm log. . . . . . . . . . . . . . . . . . . . . . . . . . . . . 78
8.2 Customer service. . . . . . . . . . . . . . . . . . . . . . . . . . . . 78
8.3 Setting outputs. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 78
Setting discrete outputs. . . . . . . . . . . . . . . . . . . . . . . 79
Setting milliamp outputs . . . . . . . . . . . . . . . . . . . . . . 79
Setting the frequency output . . . . . . . . . . . . . . . . . . . 80
8.4 Density calibration . . . . . . . . . . . . . . . . . . . . . . . . . . . 80
Density unit for calibration. . . . . . . . . . . . . . . . . . . . . 80
Duplicating the factory calibration . . . . . . . . . . . . . . . 81
Duplicating a previous calibration . . . . . . . . . . . . . . . 82
Two-point density calibration. . . . . . . . . . . . . . . . . . . 83
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
9 Laboratory Determination of Dry Oil and
67
Produced Water Densities
9.1 Reasons for using live oil density . . . . . . . . . . . . . . . 87
9.2 Laboratory density measurement . . . . . . . . . . . . . . . 87
Taking a sample from the flow line . . . . . . . . . . . . . . 88
Processing sample and measuring densities . . . . . . 91
. . . . . . . . . . . . . . . . .
10In-Line Determination of Live Oil and
Produced Water Densities
10.1 Reasons for using live oil density . . . . . . . . . . . . . . . 93
10.2 In-line density determination . . . . . . . . . . . . . . . . . . . 93
Density determination procedures. . . . . . . . . . . . . . . 93
Measuring and saving the water density . . . . . . . . . . 94
Manually entering the water density . . . . . . . . . . . . . 99
Measuring and saving the oil density . . . . . . . . . . . . 103
Entering the water cut . . . . . . . . . . . . . . . . . . . . . . . . 104
11Sensitivity Analysis
11.1 Error factors. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 107
11.2 Individual sensitivity. . . . . . . . . . . . . . . . . . . . . . . . . . 107
11.3 Overall uncertainty. . . . . . . . . . . . . . . . . . . . . . . . . . . 108
. . . . . . . . . . . . . . . . . . . . . . . . . . . .
. . . . . . . . . . . . . . . . .
87
93
107
ALTUS™ Net Oil Computer Manu al
iii
Contents
continued
12Software Diagrams
12.1 View menu in well test mode . . . . . . . . . . . . . . . . . . 111
12.2 View menu in continuous mode. . . . . . . . . . . . . . . . 112
12.3 Configuration menu . . . . . . . . . . . . . . . . . . . . . . . . . 113
12.4 Maintenance menu . . . . . . . . . . . . . . . . . . . . . . . . . 115
. . . . . . . . . . . . . . . . . . . . . . . . . . .
Appendixes
Appendix A ALTUS™ NOC Software Configuration
Record . . . . . . . . . . . . . . . . . . . . . . . . . . . . 117
Appendix B Return Policy . . . . . . . . . . . . . . . . . . . . . . . . . . . 121
Index
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
111
123
iv
ALTUS™ Net Oil Computer Manu al
Contents
continued
Figures
Figure 1-1 Water cut calculation. . . . . . . . . . . . . . . . . . . . . . . . 2
Figure 2-1 Typical installation, Micro Motion
NOC with 3-phase separator . . . . . . . . . . . . . . . 4
Figure 2-2 Typical installation, Micro Motion
NOC with 2-phase separator . . . . . . . . . . . . . . . 4
Figure 2-3 Sensor in horizontal pipe run,
tubes downward . . . . . . . . . . . . . . . . . . . . . . . . . 5
Figure 2-4 Sensor in vertical pipe run. . . . . . . . . . . . . . . . . . . . 5
Figure 3-1 Person-Process Interface . . . . . . . . . . . . . . . . . . . . 9
Figure 3-2 Pressing security button, security disabled. . . . . . . 10
Figure 3-3 Pressing security button, security enabled . . . . . . . 10
Figure 3-4 Function buttons . . . . . . . . . . . . . . . . . . . . . . . . . . . 11
Figure 3-5 Cursor control buttons. . . . . . . . . . . . . . . . . . . . . . . 13
Figure 4-1 Effect of transient bubbles on density . . . . . . . . . . . 22
Figure 4-2 Holding at last measured density . . . . . . . . . . . . . . 22
Figure 4-3 Correction of density readings . . . . . . . . . . . . . . . . 22
Figure 4-4 Flow calibration values on sensor serial
number tag . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 29
Figure 4-5 D1 and D2 on sensor serial number tag . . . . . . . . . 30
Figure 4-6 K1 and K2 on sensor serial number tag . . . . . . . . . 31
Figure 4-7 K1 and K2 values from comments section . . . . . . . 32
Figure 4-8 K1 and K2 values from second page . . . . . . . . . . . 32
Figure 4-9 FD and dens temp coeff on sensor serial
number tag . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 33
Figure 5-1 Using buttons in the view menu . . . . . . . . . . . . . . . 43
Figure 6-1 Process monitor mode . . . . . . . . . . . . . . . . . . . . . . 49
Figure 7-1 Process monitor mode . . . . . . . . . . . . . . . . . . . . . . 55
Figure 8-1 Model 3500 sensor wiring terminals . . . . . . . . . . . . 76
Figure 8-2 Model 3700 sensor wiring terminals . . . . . . . . . . . . 76
Figure 9-1 Sample port for laboratory density
measurement . . . . . . . . . . . . . . . . . . . . . . . . . . . 88
Figure 9-2 Laboratory sampling procedure using
water-filled cylinder . . . . . . . . . . . . . . . . . . . . . . . 89
Figure 9-3 Laboratory sampling procedure using
empty cylinder. . . . . . . . . . . . . . . . . . . . . . . . . . . 90
Figure 9-4 Laboratory density measurement system,
low pressure . . . . . . . . . . . . . . . . . . . . . . . . . . . . 92
Figure 9-5 Laboratory density measurement system,
high pressure . . . . . . . . . . . . . . . . . . . . . . . . . . . 92
Figure 10-1 Stratification with no flow. . . . . . . . . . . . . . . . . . . . . 96
Figure 10-2 Diameter and length of cylindrical vessel . . . . . . . . 97
Figure 10-3 Taking a water sample from the separator . . . . . . . 101
Figure 10-4 Using a hygrometer to measure water density . . . . 101
Figure 10-5 Taking an oil sample . . . . . . . . . . . . . . . . . . . . . . . . 103
®
sensor and
®
sensor and
ALTUS™ Net Oil Computer Manu al
v
Contents
continued
Tables
Table 4-1 Densities and deviations for continuous mode . . . . 18
Table 4-2 Well data for well test mode. . . . . . . . . . . . . . . . . . . 21
Table 4-3 Transient bubble remediation parameters. . . . . . . . 23
Table 4-4 System parameters . . . . . . . . . . . . . . . . . . . . . . . . . 24
Table 4-5 Flow variables . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25
Table 4-6 Density inputs . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 26
Table 4-7 Temperature inputs . . . . . . . . . . . . . . . . . . . . . . . . . 27
Table 4-8 Flow calibration values . . . . . . . . . . . . . . . . . . . . . . 29
Table 4-9 D1 and D2 density values . . . . . . . . . . . . . . . . . . . . 30
Table 4-10 K1 and K2 tube period values . . . . . . . . . . . . . . . . . 31
Table 4-11 FD and dens temp coeff values. . . . . . . . . . . . . . . . 33
Table 4-12 Nominal FD values for sensors . . . . . . . . . . . . . . . . 34
Table 4-13 Temperature calibration values . . . . . . . . . . . . . . . . 35
Table 4-14 Sensor information variables. . . . . . . . . . . . . . . . . . 35
Table 4-15 Discrete output 1 power sources. . . . . . . . . . . . . . . 36
Table 4-16 Discrete output assignment variables . . . . . . . . . . . 36
Table 4-17 Fault conditions and settings for
milliamp outputs . . . . . . . . . . . . . . . . . . . . . . . . . 37
Table 4-18 Process variables for milliamp outputs . . . . . . . . . . 38
Table 4-19 Calibration span variables . . . . . . . . . . . . . . . . . . . . 39
Table 4-20 Pulse output variables . . . . . . . . . . . . . . . . . . . . . . . 40
Table 6-1 Continuous production measurements . . . . . . . . . . 51
Table 7-1 Performance measurements for
current well test . . . . . . . . . . . . . . . . . . . . . . . . . . 62
Table 7-2 Performance measurements for
previous well tests. . . . . . . . . . . . . . . . . . . . . . . . 65
Table 8-1 Using NOC alarms. . . . . . . . . . . . . . . . . . . . . . . . . . 68
Table 8-2 Using slug flow alarms. . . . . . . . . . . . . . . . . . . . . . . 69
Table 8-3 Using output saturation alarms . . . . . . . . . . . . . . . . 70
Table 8-4 Using totalizer alarms . . . . . . . . . . . . . . . . . . . . . . . 70
Table 8-5 Using calibration and trim alarms . . . . . . . . . . . . . . 71
Table 8-6 Using conditional status alarms. . . . . . . . . . . . . . . . 72
Table 8-7 Fault output levels . . . . . . . . . . . . . . . . . . . . . . . . . . 73
Table 8-8 Configurations for fault outputs . . . . . . . . . . . . . . . . 73
Table 8-9 Using critical status fault alarms . . . . . . . . . . . . . . . 74
Table 8-10 Using transmitter failure fault alarms. . . . . . . . . . . . 74
Table 8-11 Troubleshooting excessive drive gain . . . . . . . . . . . 75
Table 8-12 Nominal resistance ranges for
flowmeter circuits. . . . . . . . . . . . . . . . . . . . . . . . . 77
Table 8-13 Troubleshooting sensor error fault alarms. . . . . . . . 77
Table 8-14 Density of air in grams per cubic centimeter . . . . . . 84
Table 8-15 Maximum flow rates for high-density
calibration . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 85
Table 8-16 Density of water. . . . . . . . . . . . . . . . . . . . . . . . . . . 86
Table 9-1 Laboratory equipment for determining live oil
and produced water densities . . . . . . . . . . . . . . 87
Table 10-1 Approximate capacity of cylindrical vessels. . . . . . 97
Table 10-2 Approximate capacity of spherical ends . . . . . . . . 97
Table 11-1 Uncertainty factors for percent water cut and
percent net oil . . . . . . . . . . . . . . . . . . . . . . . . . . 107
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ALTUS™ Net Oil Computer Manu al
1 Before You Begin
Water cut
D
eDo
DwD
o
-------------------- -=
1.1 About this manual
1.2 Application software described in this manual
1.3 Introduction to the ALTUS™ NOC
Replacing an older NOC and transmitter
This manual explains how to configure, operate, and maintain the ALTUS
Net Oil Computer (NOC). This manual does not explain
installation or wiring. For information about installation and wiring, see
ALTUS Installation Manual
the
.
This manual pertains to software menus that enable operation, configuration, and maintenance of the NOC.
The ALTUS applications platform has software functions that do not pertain to the NOC.
For information about software functions that are not described in this manual, refer to the installation and detailed setup manuals for the applications platform.
The ALTUS NOC works with a Micro Motion® sensor to produce real­time measurements of water cut, net oil volume flow, and net water volume flow. The NOC measures full-stream mass flow and volumetric flow at rates from a few barrels to more than 100,000 barrels per day.
If an AL TUS NOC is installed as a replacement for an older Micro Motion Net Oil Computer and RFT9739 or RFT9712 transmitter, power-supply and output wiring does not need to be replaced. Because transmitter software is included with the ALTUS NOC, a transmitter is not required.
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
Water cut determination
ALTUS™ Net Oil Computer Manu al
The NOC calculates water cut from the following equation:
Where
:
D
= Emulsion density
e
D
= Oil density
o
D
= Water density
w
Figure 1-1
, page 2, shows how water cut is calculated by the NOC. The operator enters the oil and water densities at the reference temperature (60°F in temperature (100°F in
Figure 1-1
). The Micro Motion sensor measures the fluid
Figure 1-1
). The NOC extrapolates the densities to the operating temperature, using an API equation for oil and a Chevron Research equation for produced water. The water cut equation is solved at operating temperature, then referenced back to 60°F. Using water cut, mass flow rate, and net oil and water densities, the NOC calculates net oil, net water, and gross flow at reference temperature.
1
continued
Before You Begin
Figure 1-1. Water cut calculation
1.05
1.00
0.95
0.90
0.85
0.80
Density (g/cc)
0.75
0.70
Produced water density enter ed in NOC
Crude oil density ent er ed i n N O C
60° 90°
NOC capabilities
Produced water density
D
Water cut
100°
Temperature (°F)
eDo
-------------------- -=
DwD
o
120° 150°
Crude oil density
The NOC can operate in continuous mode or well test mode:
In continuous mode, the NOC can continuously monitor a well, separator, or pipeline.
In well test mode, the NOC can perform a well test on any of up to 48 different wells. Well performance data for the test that is in progress or for previous tests can be viewed during the test.
The NOC nonvolatile memory archives data acquired during the last three well tests. The NOC resumes testing if a power failure or shutoff interrupts the test that is in progress. The last three power outages are recorded with power-on and power-off time/date stamps.
The NOC has three discrete outputs, two milliamp outputs, and a pulse output:
Discrete output 1 can be an alarm for transient bubble remediation.
Discrete output 2 indicates net oil. It produces 10 output pulses per barrel or 10 output pulses per cubic meter of net oil.
Discrete output 3 indicates net water. It produces 10 output pulses per barrel or 10 output pulses per cubic meter of net water.
Milliamp output 1 can indicate any measured variable.
Milliamp output 2 can indicate any measured variable.
The pulse output can represent a flow variable.
The NOC can remediate density readings to compensate for the presence of transient bubbles in the sensor. If erratic density resulting from transient bubbles causes sensor drive gain to exceed the programmed value, the NOC can be programmed to respond in one of three ways:
The NOC can hold the density value that was measured at a specified time before transient bubbles were detected.
The NOC can produce an alarm indicating the presence of transient bubbles. The alarm can be assigned to discrete output 1.
The NOC can stop the well test that is in progress.
2
ALTUS™ Net Oil Computer Manu al
2 Installation Considerations
2.1 Piping arrangement and ancillary equipment
Figure 2-1
when a 3-phase test separator is used.
Figure 2-2
when a 2-phase test separator is used. Adhere to the following general guidelines:
Design and size the test separator to ensure complete separation of the entrained gas from the liquid phase.
Size the Coriolis sensor so that at maximum liquid flow, pressure drop is less than 3 psi.
Install the sensor as far below the test separator as possible.
Install the sensor upstream from the dump valve
Balance any sensor pressure drop with hydrostatic head, measured from the lowest level in the separator down to the sensor inlet. Rule of thumb: pressure drop should be about 0.4 psi per foot.
If the liquid temperature is significantly different from the ambient temperature, thermally insulate or heat trace the sensor and upstream pipe to minimize paraffin coating and transient temperature at the start of dumping periods.
Install a meter proving loop, if required.
Install a static mixer and sampling port for calibration and verification purposes. Locate the static mixer and sampling port downstream from the sensor and the proving loop connections.
Make sure the dump valve is capable of regulating back pressure and controlling the liquid flow rate.
, page 4, shows a typical installation of a sensor and an NOC
, page 4, shows a typical installation of a sensor and an NOC
.
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
3
continued
Installation Considerations
Figure 2-1. Typical installation, Micro Motion® sensor and NOC with 3-phase separator
Figure 2-2. Typical installation, Micro Motion
®
sensor and NOC with 2-phase separator
4
ALTUS™ Net Oil Computer Manu al
Installation Considerations
continued
2.2 Sensor installation
Sensor orientation
Install the sensor according to the appropriate sensor instruction manual.
If possible, mount the sensor with its flow tubes downward in a horizontal pipe run, as shown in
Figure 2-3
.
If necessary to prevent sand or other solid particles from accumulating in the flow tubes, or to accommodate existing vertical piping, mount the sensor in a vertical pipe run, as shown in
Figure 2-4
. The oil/water
interface should flow upward through the pipeline.
Figure 2-3. Sensor in horizontal pipe run, tubes downward
Flow direction
Using the Person-Process
Interface
Figure 2-4. Sensor in vertical pipe run
Flow direction
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
5
Installation Considerations
PgPpP
m
+
>
Avoiding inaccurate flow counts
continued
CAUTION
Settling of the oil/water interface in a sensor can cause the flowmeter to indicate flow when there is no flow.
• To avoid inaccurate flow counts, program a low flow cutoff. To program a low flow cutoff, see page 25.
• Settling of the oil/water interface is more likely to occur if the sensor is mounted in a vertical pipe run than if the sensor is mounted in a horizontal pipe run.
Because the crude oil in the separator is at an equilibrium condition, any pressure reduction can cause the solution gas (i.e., the light end components) to break out from the saturated crude oil.
Even a seemingly small amount of free gas in the liquid phase can result in substantial measurement errors in water cut and net oil. (See pages 107-109 to estimate the effect of free gas).
The amount of gas that is produced varies, and depends on the properties of the crude oil and the operating conditions.
To prevent formation of solution gas in the flowmeter, the following criterio n shou ld be followed:
Where:
Pg= Static head pressure of liquid, measured from liquid level at
separator to sensor inlet
P
= Frictional pressure loss of flow line, from test separator to
p
sensor inlet
P
= Pressure drop across sensor
m
Detailed pressure drop calculations are strongly recommended during design and installation of the piping system.
6
ALTUS™ Net Oil Computer Manu al
Installation Considerations
continued
The following general guidelines are suggested:
To maximize the static head gain (P
), install the sensor as far below
g
the test separator as possible.
Note that 1 psi (6.9 kPa) of static head gain results from 28 inches of water column.
To minimize the frictional head loss (P
), install the sensor as near as
p
possible to the test separator, and use larger-diameter connecting pipes. Minimize use of piping elements such as tees, elbows, and reducing unions.
Install sampling ports, static mixer , proving connections, dump valve , back pressure regulator, or other flow-restricting devices downstream from the sensor. A full-port valve should be considered if a cutoff valve must be installed between the separator and the sensor.
Whenever possible, frictional pressure loss should be less than 3 psi (20.7 kPa) at the maximum anticipated flow rate.
To minimize pressure drop across the sensor (P
), install a larger
m
sensor. Pressure drop across the sensor should be less than 3 psi (20.7 kPa) at the maximum anticipated flow rate.
In some environments, extremely tight emulsion occurs. Extremely tight emulsion can make removal of entrained gas difficult, even with a large separator. Using a suitable demulsifier chemical to break down the emulsion is a possible method of alleviating this problem.
Using the Person-Process
Interface
2.3 Flow direction
If the sensor is installed directly at the wellhead, (i.e., if a test separator is not used), the line pressure at the sensor should be maintained above the crude oil bubble point pressure.
The sensor measures accurately regardless of flow direction. The arrow on the sensor housing indicates normal forward flow direction. Refe r to
ALTUS Detailed Setup Manual
the
for directions about setting the NOC
to indicate forward flow, reverse flow, or forward and reverse flow.
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
7
8
ALTUS™ Net Oil Computer Manu al
3 Using the Person-Process
Interface
3.1 Person-Process Interface
Figure 3-1. Person-Process Interface
Volume Flow
Backlit
display
Volume Total
NEXT PRINT VIEW
Figure 3-1
Configure the NOC
Monitor and control the application
Perform maintenance and diagnostic tasks
DEVICE 1
shows the Person-Process Interface. Use the interface to:
4,352.33
bpd
56,485.88
bbl
Using the Person-Process
Interface
Cursor control buttons
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
Function buttons
ALTUS™ Net Oil Computer Manu al
Security button
9
Using the Person-Process Interface
continued
3.2 Security button
The security button is in the lower right of the interface, marked by an icon of a padlock.
If security is disabled, press the security button to access the main menu. See
If security has been enabled, you will be prompted to enter a password. See
To enable security, see the
You can use the security button to return to the main menu or password entry screen. Press the security button once to return to:
The main menu, shown in
The password entry screen, shown in enabled
At the main menu or password entry screen, press EXIT to return to the operation screen.
Figure 3-2
Figure 3-2. Pressing security button, security disabled
DEVICE 1
Volume Flow
4,532.33
bpd
Mass Total
56,485.88 bbl
NEXT PRINT VIEW
.
Figure 3-3
.
ALTUS Detailed Setup Manual
Figure 3-2
DEVICE 1
Configuration
Maintenance Security Language
SEL HELP EXIT
, if security is disabled
Figure 3-3
, if security is
.
Figure 3-3. Pressing security button, security enabled
DEVICE 1
Volume Flow
4,532.33
bpd
Mass Total
56,485.88 bbl
NEXT PRINT VIEW
10
Enter Password
SEL HELP EXIT
ALTUS™ Net Oil Computer Manu al
Using the Person-Process Interface
continued
3.3 Function buttons
Figure 3-4. Function buttons
The pushbuttons below the display are the function buttons. The action each button performs appears on the display just above the button.
Figure 3-4
reviews the functions that are assigned to each button.
DEVICE 1
Configuration
Maintenance Security
SEL HELP EXIT
Using the Person-Process
Interface
START • Start well test
• Start averaging oil or water densities
STOP • Stop well test
• S t op averaging oil or water densities CLEAR Clear all displayed values RESET Reset total PAUSE • Pause counting of all displayed totals
• Pause performance measurements RESUME • R esume counting of all displ ayed totals
• R esume production meas ur em ents SEL Select the highlighted option CHG Make a change to the highlighted option SAVE Save a change ENTER Enter a password YES Proceed with action OK Proceed with action NEXT • Scroll to next screen
• At the last screen, scroll to the first screen
• Test the next well in the sequence RETURN Retu rn to well test screen PGDN Page down to next help screen
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
VIEW Access the view menu ACK Acknowledge an alarm message EXIT Return to the previous screen NO Cancel action
HELP Show a help screen RESET Reset total START Start a new well test VIEW View performance meas urements for a
well that is being tested PRINT Send a ticket to a printer PGUP Page up to previous help screen
ALTUS™ Net Oil Computer Manu al
11
Using the Person-Process Interface
continued
3.4 Cursor control buttons
Actions performed by the function buttons apply to the item at the cursor.
Figure 3-5
, page 13, shows a typical configuration sequence involving both a menu item and a variable edit item. Pressing HELP produces a screen that has help for the item at the cursor.
Menus
Each menu includes a list of items.
The cursor is a reverse-video highlight bar.
Use the up or down arrow buttons to locate the cursor at the menu
item you want to select or change.
After locating the cursor at the desired menu item, press CHG or the
right cursor button to select the item.
Items
After a menu item has been selected, the cursor enables you to enter or change the selected item:
The cursor is an underscore character, which is located under a
character.
If the item has a value of Yes or No, all arrows toggle between the
two choices. Otherwise, press the up and down arrow buttons to increase or decrease the value of the character at the cursor.
If the item has more than one digit or character (like the oil density in
the example), press the left and right arrow buttons to move the cursor to the next or previous character.
When the value is correct, press SAVE.
If y ou wish to cancel the change, press EXIT. The interface returns to
the previous screen without saving the changes.
12
ALTUS™ Net Oil Computer Manu al
Using the Person-Process Interface
Figure 3-5. Cursor control buttons
continued
Menu
Indicates items
available to scroll
Cursor is a
highlight bar
Item
Cursor is an
underscore
Well Data-Densities
Oil Density
Water Density
Oil Deviation
Water Deviation
CHG HELP EXIT
Well Data-Densities
Oil Density
Water Density
Oil Deviation
Water Deviation
SAVE EXIT
0.9000 g/cc
1.1000 g/cc
0.0005 g/cc
0.0005 g/cc
0.9000
g/cc
1.1000 g/cc
0.0005 g/cc
0.0005 g/cc
EXIT
Move cursor to left or toggle YES/NO
Move cursor up/Scroll up
SELECT
Move cursor down/Scroll down
Increase value at cursor or toggle YES/NO
Move cursor to right or toggle YES/NO
Decrease value at cursor or toggle YES/NO
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
13
14
ALTUS™ Net Oil Computer Manu al
4 Configuration
4.1 Recording the configuration
4.2 Configuration sequence
While you are configuring the NOC, record configuration parameters in the NOC configuration record (
Failure to perform configuration tasks in the proper sequence could result in an incomplete or flawed configuration. Perform configuration tasks in the following sequence:
1. Configure well performance measurements.
2. Configure system data.
3. Configure inputs.
4. Configure outputs.
Appendix A
).
CAUTION
Selecting configuration will interrupt measurement and control functions. All outputs will go to their configured fault settings.
Set control devices for manual operation before accessing configuration menus.
Step 1
Configure well performance measurements
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
Well performance measurements include the following parameters:
Mode of operation
Units of measurement
Well data – densities
Compensations
15
Configuration
Mode of operation
Configuration
Well performance meas
continued
Mode of operation
CAUTION
Changing the mode of operation will erase all stored test data.
Mode of Operation
Continuous Mode
Well Test Mode
SAVE EXIT
Units of measurement
To avoid erasing test data, d o not chan ge the mo de of operation during a well test.
To set the mode of operation: a. Press the security button on the display face. b. Select Configuration. c. Select Well Performance Meas. d. Select Mode of Operation. e. Select Continuous Mode or Well Test mode, then
press SAVE.
The units of measurement menu allows you to select a reference temperature for measuring net oil and net water.
To select a unit of temperature, see page 27. To select a unit of volume flow, see page 25.
CAUTION
Changing reference temperature changes the indicated standard volumes and reference densities.
If the reference temperature is changed, change oil and water reference density values.
16
ALTUS™ Net Oil Computer Manu al
Configuration
Configuration
Well performance meas
Units of Measurement
60 degF
15 degC 20 degC
continued
Units of measurement
To select the reference temperature: a. Press the security button on the display face. b. Select Configuration. c. Select Well Performance Meas. d. Select Units of Measurement. e. Select the desired refer ence temperature, then
press SAVE.
The reference temperature that is currently being used is always the one that is highlighted.
SAVE EXIT
Well data-densities
Configuration
Well performance meas
Well data-densities
Well Data-Densities
Oil Density
0.9000 g/cc
Water Density
1.1000 g/cc
Oil Deviation
0.0005 g/cc
Water Deviation
0.0005 g/cc
CHG HELP EXIT
Using the Person-Process
Interface
Continuous mode
To enter oil and water densities and deviations for continuous mode: a. Press the security button on the display face. b. Select Configuration. c. Select Well Performance Meas. d. Select Well Data-Densities.
e. Use the function buttons and the cursor control
buttons to configure the parameters that are listed
Table 4-1
in
, page 18.
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
17
Configuration
continued
Oil and water densities, deviations, and duration averages are described in the chapter that explains density determination (pages 93-104
).
Well Data-Densities
Oil Deviation
0.0005 g/cc
Water Deviation
0.0005 g/cc
Oil Duration Ave
Water Duration Ave
CHG HELP EXIT
5 sec
5 sec
Table 4-1. Densities and deviations for continuous mode
Variable Default Description
Oil density 0.9000 g/cc • I f oil density at reference temperature is known, enter the densi ty value
Water density 1.1000 g/cc • If water density at reference temperature is known , e nt e r the density value
Oil deviation 0.0005 g/cc • E nter the maximum oil density deviation that wi ll be allowed du ring density
Water deviation 0.0005 g/cc • Enter the maximum water density deviation that will be allowed during density
Oil density ave 5 sec Enter the amount of time during which oil density will be averaged during density
Water density ave 5 sec Enter the amount of time during which water density will be averaged during
• If oil density at reference tempe rature is unk nown, perform a density determina tio n (see pages 93-104)
• If water density at reference temperature is unknown, perform a density determina tio n (see pages 93-104)
determina tio n (see pages 93-104)
• I f t he dif ference bet wee n t wo co nsecutive density readings i s grea te r t han the programmed deviation, the densit y average is restarted. The averaging is completed when the deviation is not exceeded during the averaging period
determina tio n (see pages 93-104)
• I f t he dif ference bet wee n t wo co nsecutive density readings i s grea te r t han the programmed deviation, the densit y average is restarted. The averaging is completed when the deviation is not exceeded during the averaging period
determina tio n (see pages 93-104)
density determ i nation (see pages 93 -104)
18
ALTUS™ Net Oil Computer Manu al
Configuration
Configuration
Well performance meas
Well Data-Densities
Wells 1 to 12
Wells 13 to 24
Wells 25 to 36
Wells 37 to 48
continued
Well data-densities
Well test mode
To enter well names, oil and water densities, deviations, and purge times for well test mode: a. Press the security button on the display face. b. Select Configuration. c. Select Well Performance Meas. d. Select Well Data-Densities. e. Select the menu item for the number of the well
that will be configured, then press CHG.
CHG HELP EXIT
Wells 1 to 12
01: Tinsley 22-14b
02: N Cowden 24-17a 03: R Dutton 36-13c 04: B Olsen 23-15d 05: 13-24-44-5E6 06: 08-11-23-6E2 07: 18-44-04-3W5 08: 12-28-36-6W7
SAVE EXIT
Using the Person-Process
Interface
f. Select the well that will be configured, then press
SAVE.
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
19
Configuration
Well Name:
Oil Density
Water Density
Purge Time
CHG HELP EXIT
continued
Well #1
Tinsley 22-14b
0.8000 g/cc
1.0000 g/cc
30 minutes
g. To enter a well name:
Begin entering characters at the far left position
Enter up to 18 alphanumeric characters,
including spaces
h. Use the function buttons and the cursor control
buttons to configure the parameters that are listed
Table 4-2
in
.
Oil and water densities, deviations, and duration averages are described in the chapter that explains density determination (pages 93-104
).
Well #1
Oil Deviation
0.0005 g/cc
Water Deviation
0.0005 g/cc
Oil Duration Ave
5 sec
Water Duration Ave
5 sec
CHG HELP EXIT
20
ALTUS™ Net Oil Computer Manu al
continued
Configuration
Table 4-2. Well data for well test mode
Variable Default Description
Well name Not applicable
(none)
Oil density 0.8000 g/cc • I f oil density at reference temperature is known, enter the densi ty value
Water density 1.0000 g/cc • If water density at reference temperature is known , e nt e r the density value
Purge time 30 minutes Enter t he time during which, prior to a well test, measurements will not be recorded
Oil deviation 0.0005 g/cc • E nter the maximum oil density deviation that wi ll be allowed during density
Water deviation 0.0005 g/cc • Enter the maximum water density deviation that will be allowed during density
Oil density ave 5 sec Enter the amount of time during which oil density will be averaged during density
Water density ave 5 sec Enter the amount of time during which water density will be averaged during density
Beginning at the far left position , en te r up to 18 alphanumeri c ch aracters, including spaces, that will serve as the name for the selected well
• I f oil density at reference temperature is unknown, perform a density determina tio n (see pages 93-104)
• I f water density at reference temperature is unknown, perform a density determina tio n (see pages 93-104)
until separator conte nt s f ro m the previous tes t have been purg ed
determina tio n (see pages 93-104)
• I f t he dif ference bet wee n t wo co nsecutive density readings i s grea te r t han the programmed deviation, the densit y average is restarted. Th e averaging is completed when the deviation is not exceeded during the averaging period
determina tio n (see pages 93-104)
• I f t he dif ference bet wee n t wo co nsecutive density readings i s grea te r t han the programmed deviation, the densit y average is restarted. Th e averaging is completed when the deviation is not exceeded during the averaging period
determina tio n (see pages 93-104)
determina tio n (see pages 93-104)
Using the Person-Process
Interface
Compensations
The compensations menu allows you to configure the NOC to perform transient bubble remediation.
Transient bubble remediation (TBR) corrects density and water cut read ings during brief period s when gas bubbles are passing through the sensor.
Figure 4-1
, page 22, illustrates the effect of
transient bubbles on measured density.
Figure 4-2
, page 22, illustrates how the NOC holds the measured density at the time period before transient bubbles were detected, if hold last value is selected as the action taken.
Figure 4-3
, page 22, illustrates how transient bubble remediation corrects density readings.
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
21
continued
Configuration
Figure 4-1. Effect of transient bubbles on density
15.00 V
10.00 V
5.00 V
Drive gain (volts)
0.00 V
Figure 4-2. Holding at last measured density
15.00 V
10.00 V
5.00 V
Drive gain (volts)
0.00 V
Programmed drive gain level (see
Table 4-3
)
Programmed
time period
Table 4-3
(see
1.0 g/cc
Density (g/c c)
0.9 g/cc Drive gain (volts)
0.8 g/cc
Time
1.0 g/cc
Density (g/c c)
0.9 g/cc Drive gain (volts)
0.8 g/cc
Time
)
Figure 4-3. Correction of density readings
15.00 V
10.00 V
5.00 V
Drive gain (volts)
0.00 V
Programmed drive gain level (see
22
Table 4-3
)
1.0 g/cc
Density (g/c c)
0.9 g/cc Drive gain (volts)
0.8 g/cc
Time
ALTUS™ Net Oil Computer Manu al
continued
Configuration
Transient Bubble Remd
Drive Gain Level
Action Taken
Time Period
Configuration
Well performance meas
Hold Last Value
Compensations
Transient bubble remd
5.4 V
15 seconds
To set parameters for transient bubble remediation: a. Press the security button on the display face. b. Select Configuration. c. Select Well Performance Meas. d. Select Compensations. e. Select Transient Bubble Remd. f. Use the function buttons and the cursor control
buttons to configure the parameters that are listed
Table 4-3
in
.
CHG HELP EXIT
Table 4-3. Transient bubble remediation parameters
Variable Default Definition
Drive gain level 14.5 volts • Enter a value of 0.5 to 14.5 volts
Action taken Hold last value • Hold last value:
Time period 15 seconds If hold last value is selected as the action t aken, enter the amount of time before
• T he ent er ed value is the voltage above which the NOC will indicate transient bubbles
• To determine the appropria te value, view the average and maximum values in the view production measureme nt s m enu ( see 50-51), the view current test me nu (se e pages 61-62), or the view well tests me nu (se e pages 63-65)
• Entering a value of 14.5 will disable transient bubble remediation
-
The NOC will hold the measured density at the time period before transient bubb le s were detected
-
Transient bubbles can be indicated by discrete output 1 (see page 36)
-
This option requires configuration of a time period (s ee below)
• Stop well test:
-
The NOC will stop the well test if transient bubbles are detected
-
Transient bubbles can be indicated by discrete output 1 (see page 36)
• A larm only: Transient bubbles will be indicated by discrete output 1 (se e pa ge 36)
transient bubbles were detected that w ill be used to derive a density re ading
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
23
Configuration
continued
Step 2
Configure system data
To configure system data:
Configuration
System
a. Press the security button on the display face. b. Select Configuration. c. Select System. d. Use the function buttons and the cursor control
System
Tag
Time Date Master Reset
SEL HELP EXIT
buttons to configure the parameters that are listed
Table 4-4
in
.
Table 4-4. System parameters
Variable Default Description
Ta g Device 1 Enter up to 8 digits and/or characters that identify this NOC, well, or separator Time Current time Enter a value of 0 to 23 for hours, a value of 00 to 59 for minutes, and a value of 00
Date Cur rent date Enter 4 digits for the year, a character code for the month, and 2 digits for the day
to 59 for seconds
24
ALTUS™ Net Oil Computer Manu al
Configuration
continued
Flow variables
Configuration
Inputs
Coriolis
Config process var
Flow variables
Flow Variables
Flow Damping
0.8 sec
Meter Direction
Forward
Mass Units
g/s
Mass Low Flow Cutoff
0.00000 g/s
CHG HELP EXIT
Step 3
Configure inputs
To confi gur e flow variables: a. Press the security button on the display face. b. Select Configuration. c. Select Inputs. d. Select Coriolis. e. Select Config Process Var. f. Select Flow Variables. g. Use the function buttons and the cursor control
buttons to configure the parameters that are listed
Table 4-5
in
.
Using the Person-Process
Interface
Table 4-5. Flow variables
Variable Default Description
Flow damping 0.8 sec • The selected value is the time req ui re d for flow outputs and di s pl ays to
achieve 63% of their new value in response to a step change at the input
• D amping filters out nois e or th e ef fects of rapid changes in the flow rate without affecting measurem e n t acc uracy
Meter direction Forward • S el ect the direction in whi ch process fluid will flow thr ough the sensor
relative to the flow direction arrow on th e sensor
• T he sensor can measure forward or backward flow
Mass units g/s • Sel ect the desired unit of mass flow
• Mass flow outputs and displays will indicate flow in the selected unit
Mass low flow cutoff 0.00000 g/s • Enter the mass flow rate below which mass flow outputs and displays will
indicate zero flow
• T he recommended flow cut of f is 0.02% of the flow rate that is repre sented by the milliamp output at 20 mA. For example, if an output of 20 mA represents 100 lb/min, the flow cutoff should 0.02 lb/min
• To set the calibration span for milliamp outputs, see page 39
Volume units l/s • S elect the desired unit of volume flow
• Volume flow outputs and displays will indicate flow in the selected unit
V olume low flow cutoff 0.0000 0 l/s • Enter the volume flow rate belo w which v olu me flo w outputs and d ispla ys wil l
indicate zero flow
• T he recommended flow cut of f is 0.02% of the flow rate that is repre sented by the milliamp output at 20 mA. For example, if an output of 20 mA represents 100 l/min, t he f low cutof f sho ul d 0. 02 l/min
• To set the calibration span for milliamp outputs, see page 39
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
25
Configuration
continued
Density inputs
Configuration
Inputs
Coriolis
Config process var
Density
Density
Density Units
Density Damping
1.7 sec
Slug Low Limit
0.000000 g/cc
Slug High Limit
5.000000 g/cc
CHG HELP EXIT
Table 4-6. Density inputs
g/cc
To configure density inputs: a. Press the security button on the display face. b. Select Configuration. c. Select Inputs. d. Select Coriolis. e. Select Config Process Var. f. Select Density. g. Use the function buttons and the cursor control
buttons to configure the parameters that are listed
Table 4-6
in
.
Variable Default Description
Density units g/cc • Select the desired unit of density
Density damping 1.7 sec • The selected value is the time required for density outputs and displays to
Slug low limit 0.000000 g/ cc • E nter the desired low limit, in g/cc, for the fluid density. The recommended slug
Slug high limit 5.000000 g/cc • Enter the desire d hi gh limit, in g/cc, for the fluid density. The recommended slug
Slug time 1.0 sec • Enter the number of seconds for which flow outputs will hold their last measured
• D ensity outputs and displays will indicate density in the selected un it
achieve 63% of their new value in response to a step change at the input
• D am ping filters out noise or the effects of rapid cha nges in density without affecting measurement accurac y
low limit is 0.8 x the lowest density to be measured
• T he ent er ed value is the density below which a slug flow alarm will be generated
• T he ent er ed value should be lower than the density that will cau se drive gain to indicate the presenc e of tran sient bubbles in the sensor (see pages 21 -23)
• For more information about slug flow, see page 69
high limit is 1.4 g/cc
• T he ent er ed value is the density above which a slug flow alar m will be ge nerat ed
• The entered value should be higher than the density that will cause drive gain to indicate the presenc e of tran sient bubbles in the sensor (see pages 21 -23)
• For more information about slug flow, see page 69
flow r ate w hile d ens ity i s ou tside the r an ge sp ecif ied b y the s lug l ow limit and s lu g high limit
• If transient bubble remediation has been implemented, set slug time to 0.0 sec. If a value of 0.0 is entered, flow outputs will go to th e l evel that indicates zero flow as soon as slug flow is detected
• T he maximum slug time is 300 seconds
• For more information about slug time, see page 69
26
ALTUS™ Net Oil Computer Manu al
Configuration
continued
Temperature
Configuration
Inputs
Coriolis
Config process var
Temperature
Temperature
Temperature Units
degC
Temp. Damping
3.5 sec
CHG HELP EXIT
Table 4-7. Temperature inputs
To confi gure temperature inputs: a. Press the security button on the display face. b. Select Configuration. c. Select Inputs. d. Select Coriolis. e. Select Config Process Var. f. Select Temperature. g. Use the function buttons and the cursor control
buttons to configure the parameters that are listed
Table 4-7
in
.
Using the Person-Process
Interface
Variable Default Description
Temperature units degC • Select degrees Celsius, Fahrenheit, Rankine, or Kelvin
• Temperature outputs and displays will indicate temperature in the selected unit
Temperature damping 3.5 sec • The selected value is the time required for temperature outputs and displays to
achieve 63% of their new value in response to a step change at the input
• D am ping filters out noise or the effects of rapid cha nges in temperature without affecting measurement accurac y
• I f de nsi t y de te rmination will be per form ed, set temperature damping at 1.0 sec. To perform a density determinatio n, see pages 93-104
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
27
Configuration
continued
Sensor calibration data
Configuration
Inputs
Coriolis
Sensor cal data
Sensor Cal Data
Flow Factor
1.00000
Flocal Temp Coef
5.130
D1
0.000000
D2
1.000000
CHG HELP EXIT
Sensor calibration data describe the sensor’s sensitivity to flow, density, and temperature.
To configure sensor calibration data: a. Press the security button on the display face. b. Select Configuration. c. Select Inputs. d. Select Coriolis.
e. Select Sensor Cal Data. f. Use the function buttons and the cursor control
buttons to configure sensor calibration data.
Sensor cal data should be entered from the sensor serial number tag or factory calibration certificate.
Tags and certificates vary in appearance, depending on the sensor model number and manufacturing date.
Flow calibration values
include the flow factor and the flow calibration temperature coefficient. To configure flow calibration values, see page 29.
Density calibration values
include D1 and D2 density values, K1 and K2 tube periods, the flowing density correction factor, and the density calibration temperature coefficient. T o configure density calibration values, see pages 30-34.
Temperature calibration values
include the temperature slope and the temperature offset. To configure temperature calibration values, see page 35.
28
ALTUS™ Net Oil Computer Manu al
continued
Configuration
Flow calibration values
Flow calibration values include the flow factor and the flow calibration temperature coefficient. To configure flow calibration values, see
Table 4-8
and
Figure 4-4
.
Table 4-8. Flow calibration values
Variable Default Description
Flow factor 1.00000 g/sec • Enter the first 5 di gi ts of th e flow cal factor (see
Flowcal temp coef 5. 130 • Enter the last 3 digits of th e f low cal factor (see
• T he ent er ed value is the flow rate, in g/sec, that generates 1 between velocity signals from the sensor
• T he ent er ed value represents the percent change in the measured flow rate per 100°C change in tempe ratur e
Figure 4-4
Figure 4-4
)
sec of time shift
µ
)
Figure 4-4. Flow calibration values on sensor serial number tag
Flow factor
on
newer
tag
Flow factor
19.0005.13
Flocal temp coef
on
newer
tag
Flocal temp coef
19.0005.13
on
older
on
tag
19.0005.13
older
tag
19.0005.13
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
29
continued
Configuration
Density calibration values
Density calibration values include D1 and D2 density values, K1 and K2 tube periods, the flowing density correction factor (FD), and the density calibration temperature coefficient (dens temp coeff).
To configure D1 and D2, see
To configure K1 and K2, see
Table 4-9
Table 4-10
To configure FD and the dens temp coeff, see
Figure 4-9
, page 33.
and
and
Figure 4-5
Figure 4-6
Table 4-11
Table 4-9. D1 and D2 density values
Variable Default Description
D1 0.000000 g/cc • If the se ns or tag shows a D1 value, enter the D1 value (see
D2 1.000000 g/cc • If the se ns or tag shows a D2 value, enter the D2 value (see
• I f the sensor tag does not show a D1 value, enter the Dens A or D1 value from the calibration certificate
• The entered value is the density of the low-density calibration fluid (Micro Motion uses air)
• I f the sensor tag does not show a D2 value, enter the Dens B or D2 value from the calibration certificate
• The entered value is the density of the high-density calibration fluid (Micro Motion uses water)
, below.
, page 31.
Figure 4-5
Figure 4-5
and
)
)
Figure 4-5. D1 and D2 on sensor serial number tag
D1
newer
on
tag
0.0010
D2
on
newer
0.9980
tag
30
ALTUS™ Net Oil Computer Manu al
continued
Configuration
Table 4-10. K1 and K2 tube period values
Note
If K1 and K2 values are being entered from a factory calibration certificate:
• D O N OT enter values from the CO M MENTS section on the firs t pa ge ( see
• D O ent er values listed on the second page (see
Variable Default Description
K1 5000.000 • If the sensor tag shows a K1 value, enter the K1 value (see
• I f the sensor tag does not show a K1 value, enter the first 5 di gits of the den si ty calibration factor (see
• T he ent er ed value represents the sensor flow tube period in adjusted to 0°C
K2 50000.000 • If the sensor tag shows a K2 value, enter th e K2 value (see
• I f the sensor tag does not show a K2 value, enter the second 5 digits of the density calibration factor (see
• T he ent er ed value represents the sensor flow tube period in adjusted to 0°C
Figure 4-8
, page 32)
Figure 4-6
Figure 4-6
Figure 4-7
, older tag)
, older tag)
, page 32)
Figure 4-6
sec associated with D1,
µ
Figure 4-6
, newer tag)
, newer tag)
µsec associated with D2,
Using the Person-Process
Figure 4-6. K1 and K2 on sensor serial number tag
K1
newer
on
tag
12500142864.44
12502.000
K2
newer
on
tag
12500142864.44
14282.000
K1
K2
on
on
older
older
Interface
tag
12500142864.44
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
tag
12500142864.44
ALTUS™ Net Oil Computer Manu al
31
continued
Configuration
Figure 4-7. K1 and K2 values from comments section
not
Do
use these
K1 and K2 values
Figure 4-8. K1 and K2 values from second page
These K1 and K2 values can be used
32
ALTUS™ Net Oil Computer Manu al
continued
Configuration
Table 4-11. FD and dens temp coeff values
Variable Default Description
FD 0.000 • If the se ns or tag shows an FD value, enter the FD value (see
Dens temp coeff 4.440000 • If the se nsor tag shows a TC value, enter the TC value (see
• I f the sensor tag does not show an FD value, enter the ap pr opriate FD value from
Table 4-12
• The entered value adjusts density calculations for the effect of high flow rates on measured dens i ty
• If the sensor tag does not show a TC value, enter the last 3 digits of the density calibration factor (see
• T he ent er ed value represents the percent change in the measured density per 100°C change in temperature
, page 34
Figure 4-9
, older tag)
Figure 4-9. FD and dens temp coeff on sensor serial number tag
FD
newer
on
tag
Figure 4-9
Figure 4-9
)
, newer tag)
Using the Person-Process
Interface
Dens temp coeff
4.44000
newer
on
tag
12500142864.44
310
Dens temp coeff
on
older
tag
12500142864.44
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
33
continued
Configuration
Table 4-12. Nominal FD values for sensors
Nominal
ELITE
®
CMF010 standard pressure 316L stainless steel 140 CMF010 standard pressure Inconel
®
686 220
Sensor model Flow tube material
FD value
CMF010 high pressur e Inconel 686 760 CMF025 standard pressure 316L stainless steel or Hastelloy
®
C-22 450 CMF050 standard pressure 316L stainless steel or Hastelloy C-22 430 CMF100 standard pressure 316L stainless steel or Hastelloy C-22 230 CMF200 standard pressure 316L stainless steel or Hastelloy C-22 320 CMF300 standard pressure 316L stainless steel or Hastelloy C-22 280
®
BASIS
F025S 316L stainless steel 0 F050S 316L stainless steel 0 F100S 316L stainless steel 0 F200S 316L stainless steel 350
Model D DS006 standard pressure 316L stainless steel or Hastelloy C-22 450
DS012 stand ard pressure 316L stainless steel 900 DS012 standard pressure Hastelloy C-22 490 DS025 stand ard pressure 316L stainless steel 110 DS025 standard pressure Hastelloy C-22 330 DS040 stand ard pressure 316L stainless steel 220 DS040 standard pressure Hastelloy C-22 610 DS065 stand ard pressure 316L stainless steel 310 DS100 standard pressure 316L stainless steel or Hastelloy C-22 520 DS150 standard pressure 316L stainless steel or Hastelloy C-22 480 DS150 standard pressure 316L stainless steel with Tefzel
®
lining 640 DS300 standard pressure 316L stainless steel or Hastelloy C-22 200 DS300 standard pressure 316L stainless steel with Tefzel lining 260 DS600 standard pressure 316L stainless steel 50
Model DH DH006 high pressure 316L stainless steel 0
DH012 high pressure 316L stainless steel 0 DH025 high pressure 316L stainless steel 0 DH038 high pressure 316L stainless steel 0 DS100 high pressure 316L stainless steel 0 DH150 high pressure 316L stainless steel 0 DH300 high pressure 316L stainless steel 0
Model DL DL065 316L stainless steel 210
DL100 316L stainless steel 670 DL200 316L stainless steel 150
Model DT DT065 Hastelloy C-22 550
DT100 Hastelloy C-22 380 DT150 Hastelloy C-22 130
34
ALTUS™ Net Oil Computer Manu al
continued
Configuration
Temperature calibration values
Temperature calibration values include the temperature slope and the temperature offset. To configure temperature calibration values, see
Table 4-13
.
Table 4-13. Temperature calibration values
Variable Default Description
Temperature slope 1.000000 • Enter the temperature sl ope value provided by Micro Motion, or pe rfor m a
Temperature offset 0.000000 • Ente r th e t em perature offset value provided by Micro Mo tion, or perform a
temperature calibration
• To perform a temperature calibration, see the
temperature calibration
• To perform a temperature calibration, see the
ALTUS Detailed Setup Manual
ALTUS Detailed Setup Manual
Using the Person-Process
Sensor information
Configuration
Inputs
Coriolis
Sensor information
Sensor information includes variables that serve as references without affecting calibration parameters, totalizers, or outputs.
To configure sensor information: a. Press the security button on the display face. b. Select Configuration.
Sensor Information
Sensor Model No.
CMF025
Sensor Serial No.
000000
Sensor Material
304 SS
Sensor End Connection
ANSI 150
CHG HELP EXIT
c. Select Inputs. d. Select Coriolis. e. Select Sensor Information. f. Use the function buttons and the cursor control
buttons to configure the parameters that are listed
Table 4-14
in
.
Table 4-14. Sensor information variables
Variable Default Description
Sensor model no. Uninitialized Enter a description of the sensor model, such as "CMF30 0" Sensor serial no. 000000 Enter the serial number that is on the sensor serial number ta g Sensor material 304 SS Select the appropriate sensor flow tube material (304 SS, 316L SS, Hastelloy C,
Sensor end connection ANSI 150 Select the appropriate flange, union fitting, sanitary fitting, or wafer fitting Sensor liner None Select the appropriate liner mater i al for the sensor flow tubes (Tefzel or none)
Inconel, or Tantalum)
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
35
Configuration
continued
Discrete outputs
Configuration
Outputs
Discrete outputs
Discrete output 1 Discrete output 2 Discrete output 3
Discrete Output 1
Power Source
Internal
Assignment
None
CHG HELP EXIT
Step 4
Configure outputs
To configure discrete outputs: a. Press the security button on the display face. b. Select Configuration. c. Select Outputs. d. Select Discrete Outputs. e. Select Discrete Output 1, Discrete Output 2, or
Discrete Output 3.
f. Use the function buttons and the cursor control
buttons to configure the power source and assignment for the selected discrete output.
Power source
Discrete outputs can be connected to factory­supplied or user-supplied relays.
To select the appropriate power source for discrete output 1, see
Table 4-15
, below.
The power source for discrete output 2 and discrete output 3 cannot be configured.
For relay specifications and installation instructions, see the
ALTUS Installation Manual
Assignment
Discrete output 1 can be inactive or can indicate transient bubble remediation. See
Table 4-16
.
Discrete output 2 represents net oil.
Discrete output 3 represents net water.
.
Table 4-15. Discrete output 1 power sources
Note
For relay specifications and installation instructions, see the
Relay type
Factory-supplied relays Internal Select internal power User-supplied relays Internal • Select internal power if relays are internally powered
Default
Power source
• S el ect external power if relays are externall y powere d
ALTUS Installation Manual
Table 4-16. Discrete output assignment variables
Discrete output Variable
Discrete output 1 Transient bubble
remediation event None Discrete output 1 will be inactive
Discrete output 2 Net oil Cannot be
Discrete output 3 Net water Cannot be
36
Default
None Discrete output 1 will indicate high drive gain
re-assigned
re-assigned
Description
Discrete output 2 will produce 10 output pulses per barrel or 10 output pulses per cubic mete r of net oil
Discrete output 3 will produce 10 output pulses per barrel or 10 output pulses per cubic mete r of net water
ALTUS™ Net Oil Computer Manu al
Configuration
CAUTION
continued
Milliamp outputs
Configuration
Outputs
Milliamp outputs
Milliamp output 1
Fault indication
Milliamp output 2
Fault indication
Fault Indication
Condition
Downscale
Setting
3.60 mA
CHG HELP EXIT
Configuring milliamp outputs includes the following procedures:
Configuring fault indication
Assigning a process variable to the output
Configuring the calibration span
Fault indication
To configure fault indication for milliamp outputs: a. Press the security button on the display face. b. Select Configuration. c. Select Outputs. d. Select Milliamp Outputs. e. Select Milliamp Output 1 or Milliamp Output 2. f. Select Fault Indication. g. Use the function buttons and the cursor control
buttons to configure the condition and setting of fault indicators for the selected milliamp output.
Condition:
Milliamp outputs can produce downscale, upscale, last measured value, or internal zero fault indicators. See
Table 4-17
The default condition is downscale.
Setting:
If downscale or upscale is selected as the fault condition, the setting determines the amount of current that indicates a fault.
Table 4-17
See
.
Using the Person-Process
Interface
.
Using last measured value or internal zero may hamper identification of fault outputs.
To make sure fault outputs can be identified, select downscale or upscale.
Table 4-17. Fault conditions and settings for milliamp outputs
Note
The default condition for fault indication is downscale
Condition Description
Downscale Can be configured from 1. 0 to 3.6 m A 3.6 mA Upscale Can be configured from 21.0 to 24.0 mA 22.0 mA Last measured value • Holds at the mA value that represents the last measured value for the process
variable before the fault occurred
• A pp arent lack of variation in the process variable could i ndi cate a fault
Internal zero • Goes to the mA value that rep resents a value of 0.0 for the process variable
• An apparent value of 0.0 for the process variable could indicate a fault
Default setting
Not applicable
Not applicable
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
37
Configuration
None
Frequency Input Unc Oil Rate Unc Water Cut Unc Water Rate Net Oil Rate Water Cut Gross Flow Rate Net Water Rate Ave Unc Oil Rate
SAVE EXIT
continued
Configuration
Outputs
Milliamp outputs
Process Variable
Milliamp output 1
Variable assignment
Milliamp output 2
Variable assignment
Process variable
To configure process variables for milliamp outputs: a. Press the security button on the display face. b. Select Configuration. c. Select Outputs. d. Select Milliamp Outputs. e. Select Milliamp Output 1 or Milliamp Output 2. f. Select Variable Assignment. g. Press CHG to access the process variable menu. h. Use the function buttons and the cursor control
buttons to select one of the process variables listed in
Table 4-18
.
Table 4-18. Process variables for milliamp outputs
Variable
Frequency input Mass flow Process variable that is represented by the frequency input Unc oil rate Uncorrected flow rate of oil Unc water cut Uncorrected water cut Unc water rate Uncorrected flow rate of water Backflow rate Real-time reverse flow rate Net oil rate Real-time net flow rate of oil at reference temperature Water cut Real-time water cu t at re ference temperature Gross flow rate Real-time flow rate of oil and water Net water rate Real-time net flow rate of water at reference temperature Ave unc oil rate Average uncorrected flow rate of oil Ave unc water cut Average uncorrected water cut Ave unc gross flow Uncorrected average flow rate of oil and water Ave unc water rate Uncorrected average flow rate of water Ave net oil rate Average net flow rate of oil at reference temperature Ave water cut Average water cut at reference temperature Ave gross flow rate Average flow rate of oil and water Ave net water rate Average net flow rate of oil at reference temperature Temperature Temperature Mass flow rate Mass flow rate Mass flow live zero Flow rate when it drops below the mass low flow cutoff Density Density of oil and water Vol. flow rate Volume flow rate of oil and water Drive gain Drive gain voltage
Default
Description (what the output will represent)
38
ALTUS™ Net Oil Computer Manu al
Configuration
20.0mA
4.0mA
Low Flow Cutoff
Damping Seconds
CHG HE LP EXIT
continued
Configuration
Outputs
Milliamp outputs
Calibration Span
Milliamp output 1
Calibration span
Milliamp output 2
Calibration span
0.00 g/s
0.000 g/s
0.00 g/s
0
Calibration span
To configure the calibration span for milliamp outputs: a. Press the security button on the display face. b. Select Configuration. c. Select Outputs. d. Select Milliamp Outputs. e. Select Milliamp Output 1 or Milliamp Output 2. f. Select Calibration Span.
The calibration span menu item appears only after a process variable has been assigned to the output.
To assign process variables to milliamp outputs, see page 38.
g. Use the function buttons and the cursor control
buttons to configure the parameters that are listed
Table 4-19
in
.
Using the Person-Process
Interface
Table 4-19. Calibration span variables
Notes
• The calibration span menu item appears only after a process variable has been assigned to the output
• To assign process variables to milliamp outputs, see page 38
• S om e values are dependent on sensor calibration data. To configure sensor calibration d at a, see pages 18-26
Variable Default Description
20 mA Sensor upper limit • Enter the value the outp ut w ill represent at 20.0 mA
4 mA Sensor lower limit • Enter the value the output will represent at 4.0 mA
Low flow cutoff 0 for all variables If a flow variable is assigned to the output, the low flow cutoff is the flow rate below
Damping seconds 0 sec • Select the amount of added damping for the milliamp outpu t
4.0 mA minimum Not applicable
20.0 mA maximum The highest value that can be represented by the output Minimum span • The smallest allowable difference between the value re pr ese nt ed at 4.0 mA and
(read-only)
• T he ent er ed value must be greater than the 4.0 mA value
• T he ent er ed value must be less than the 20.0 mA value
which the output will indicate zero flow
• T he sel ected value is the amount of time that is added to damping on flow, density, or temperature
The lowest value that can be represented by the outpu t
the value represented at 20. 0 m A
• T he 20.0 mA value must be greater than th e 4. 0 mA value
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
39
Configuration
continued
Pulse output
Configuration
Outputs
Frequency output
To configure the pulse output:
1. Press the security button on the display face.
2. Select Configuration.
3. Select Outputs.
4. Select Frequency Output.
5. Use the function buttons and the cursor control
Frequency Output
Flow Source
None
Flow Units
kg/min
Scaling Method
Frequency = Flow
Frequency
1000.000 Hz
CHG HELP EXIT
buttons to configure the parameters that are listed
Table 4-20
in
.
CAUTION
Using last measured value or internal zero may hamper identification of fault outputs.
To make sure fault outputs can be identified, select downscale or upscale.
Table 4-20. Pulse output variables
Variable Default Description
Flow source Mass flow Select none, frequency inpu t, uncorrected oil volume, uncorrected water
Scaling method Frequency = flow • Select frequency = flow, pulses/unit, or units/pulse
Frequency 1000.000 Hz • I f fre quency = flow is selected as the scal ing m et hod, enter the
Flow 16,666 g/sec • If frequency = flow is selected as the scaling method, enter the flow rate
Pulses 60.00 pulses • If pulses/unit is selected as the scaling method, en te r t he num ber of
Units 16.667 g • I f un its/pulse is selected as t he scaling method, en te r t he num ber of
Maximum pulse width 511 ms • The pulse widt h can be configured for output frequencie s bel ow 500 Hz
Power Active Select active or passive operation for the frequency output
Fault indication Downscale • Downscale: Output goes to 0 Hz
volume, backflow volume, net oil volume, gross volume, net water volume, mass, or volume
• T he frequency output has a range of 0 to 12, 50 0 H z
frequency (or pulse rate), in Hz, that represents the configured flow rate
• To scale the pulse output, see the example on page 41
that is represented by the configured frequency
• To scale the pulse output, see the example on page 41
output pulses that re pr esent one mass or volume unit
• To scale the pulse output, see the example on page 41
mass or volume units that are represented by one output pulse
• To scale the pulse output, see the example on page 41
• Enter the desired pulse width in milliseconds
• Voltage is 24 VDC nominal for active operation, 20 VD C appli ed maximum fo r pa ssive operation
• S ourcing current is 10 mA at 3 VDC for active operation
• S i nking current is 500 mA for active or passive operation
• Upscale: Output goes to 15,000 Hz
• Last measured value:
- Output holds at the fre quency that represen t s t he la s t m easured flow
rate before the fault occurred
- Apparent lack of variation in the flow rate could indicate a fault
• I nt ernal zero:
- Output goes to 0 Hz
- An apparent no-flow condition could indicate a fault
40
ALTUS™ Net Oil Computer Manu al
Configuration
continued
Example:
Scale the pulse output so 10,000 pulses represent one barrel of actual liquid. This would be a common setting for a volumetric proving application.
a. Select volume as the flow source. Remember that gross volume is
temperature-corrected, and volume is actual volume at line conditions.
b. Select bbl/day as the flow unit.
c. Select pulses per unit as the scaling method.
Using the Person-Process
d. Change the frequency to 10,000 Hz.
Interface
The output pulses are now configured for 10,000 pulses per barrel.
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
41
42
ALTUS™ Net Oil Computer Manu al
5 Using the View Menu
5.1 Accessing the view menu
When you press VIEW at the operation screen, the view menu is displayed. buttons and cursor control buttons in the view menu.
Figure 5-1. Using buttons in the view menu
Well Performance Meas
Process Totalizers Active Alarm Log LCD Options Diagnostic Monitor Applications List Power Outage
SEL HELP EXIT
Figure 5-1
VIEW MENU
shows the functions performed by the function
EXIT If SEL has been pressed, move cursor toward left
Move cursor upward
SELECT If SEL has been pressed , move cursor toward right
Move cursor downward
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
START • Start well test
• S t art averaging oil or water densities
STOP • Stop well test
• Stop averaging oil or water densities CLEAR Clear all displayed values RESET Reset total PAUSE • Pause counting of all displayed totals
• Pause performance measurements RESUME • Resume counting of all displayed totals
• R esume production meas ur em ents SEL Select the highlighted option CHG Make a change to the highlighted option SAVE Save a change ENTER Enter a password YES Proceed with action OK Proceed with action NEXT • Scroll to next screen
• At the last screen, scroll to the first screen
• Test the next well in the sequence RETURN Return to well test screen PGDN Page down to next help screen
ALTUS™ Net Oil Computer Manu al
VIEW Access the view menu ACK Acknowledge an alarm message EXIT Retur n to t he pr evious sc reen NO Cancel action
HELP Show a help screen RESET Reset total START Start a new well test VIEW View performance meas urements for a
well that i s being tested PRINT Send a ticket to a printer PGUP Page up to previous help screen
43
Using the View Menu
continued
5.2 Well performance measurements
Continuous mode
View
Well performance meas
Well Performance Meas
View Production Meas
Quick View Pause / Resume Reset
SEL HELP EXIT
The tasks you can perform in the well performance measurements menu depend on the operation mode.
To set the NOC to operate in continuous mode, see page 16. To use the NOC in continuous mode, see pages 49-54.
In continuous mode, the well performance measurements menu includes the following items:
View Production Meas
•Quick View
Pause/Resume
Reset
Well test mode
View
Well performance meas
Well Performance Meas
Start Well Test
View Well Tests
SEL EXIT
To set the NOC to operate in well test mode, see page 16. To use the NOC in well test mode, see pages 55-65.
In well test mode, the items in the well performance measurements menu depend on whether or not a well test is in progress.
If a well test is not in progress
If a well test is not in progress, the well performance measurements menu includes the following items:
•Start Well Test
•View Well Tests
44
ALTUS™ Net Oil Computer Manu al
Using the View Menu
CAUTION
View
Well performance meas
Well Performance Meas
Return To Well Test View Well Tests
View Current Test
SEL EXIT
continued
If a well test is in progress
If a well test is in progress, the well performance measurements menu includes the following items:
Return to Well Test
•Start Well Test
View Current Test
Using the Person-Process
Interface
5.3 Process totalizers
View
Process totalizers
Process
Process
Mass
769.9 lb
Volume
56,485.88 bbl
Freq Input Rollover
9999999999.99 lb
Mass Rollover
9999999999.99 lb
PAUSE RESET EXIT
↓↑
In the view menu, you can monitor or reset process totals, and pause and resume counting of displayed totals.
The volume that is displayed in the process totalizers menu is the measured mass divided by the measured density. Temperature compensation and reference oil and water densities are not used in this calculation. The displayed total is the actual gross volume of fluid.
If counting has been paused, pressing RESET will cause the total to reset to a non-zero value.
To make sure the total resets to zero, press RESET before pressing PAUSE.
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
45
Using the View Menu
continued
To reset a process totalizer, or to pause and resume counting of the displayed totals:
1. At the operation screen, press VIEW.
2. Select Process Totalizers.
3. Select Process.
4. Select the desired process totalizer.
To reset the selected totalizer, press RESET. Pressing reset does not affect a well test that is in progress.
To pause counting of all displayed totals, press PAUSE.
To resume counting of all displayed totals, press RESUME.
5. Press EXIT repeatedly to return to the operation screen.
The value to which the process total resets depends on whether or not counting has been paused.
If you press RESET without pressing PAUSE, the total resets to zero.
If you press PAUSE, then press RESET, the total resets to the amount that accumulated from the time counting was paused to the time the total was reset. For example, if counting was paused at 500 barrels, then 25 barrels were counted before the total was reset, the total resets to 25 barrels.
5.4 Inventory totalizers
View
Process totalizers
Inventory
Inventory
Mass
769.9 lb
Volume
56,485.88 bbl
Freq Input Rollover
9999999999.99 lb
Mass Rollover
9999999999.99 lb
↓↑
EXIT
The display shows rollover values for each totalizer. The rollover value is the maximum total that can be achieved before the totalizer rolls over to zero .
To monitor inventory totalizers:
1. At the operation screen, press VIEW.
2. Select Process Totalizers.
3. Select Inventory.
4. Press EXIT repeatedly to return to the operation screen.
The volume that is displayed in the inventory totalizers menu is the measured mass divided by the measured density. Temperature compensation and reference oil and water densities are not used in this calculation. The displayed total is the actual gross volume of fluid.
The display shows rollover values for each totalizer. The rollover value is the maximum inventory that can be achieved before the inventory rolls over to zero.
46
ALTUS™ Net Oil Computer Manu al
Using the View Menu
continued
5.5 Active alarm log
View
Active alarm log
Active Alarm Log
Density Alarm
17-JUL-98 8:30
Temperature Alarm
10-JUL-98 9:04
Alarm-Meas Paused
10-JUL-98 5:10
HELP EXIT
5.6 LCD options
View
LCD options
LCD Options
Contrast
LCD Backlight
The NOC performs self-diagnostics during operation. If the NOC detects certain events or conditions, an alarm message appears in the highlight bar at the top of the screen.
If the condition that caused an alarm is present, the alarm is listed in the active alarm log.
Each alarm is time/date stamped.
The first alarm listed is the most recent. For information about responding to alarm
messages, see pages 67-78. The active alarm log is also accessible via the
maintenance menu (see page 78).
Using the Person-Process
Interface
Display contrast can be adjusted for operator preference. After selecting LCD Options from the View menu:
Select Contrast to adjust the screen contrast
Select LCD Backlight to turn screen backlighting on or off
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
SEL HELP EXIT
ALTUS™ Net Oil Computer Manu al
47
Using the View Menu
continued
5.7 Diagnostic monitor
View
Diagnostic monitor
Diagnostic Monitor
Drive Gain
2.580 V
Tube Frequency
89.23 Hz
Live Zero
0.01 lb/min
5.8 Applications list
The diagnostic monitor shows real-time values for drive gain, sensor flow tube frequency, and live zero.
Drive gain is useful for indicating transient bubbles in the sensor flow tubes. To configure the NOC for transient bubble remediation, see pages 21-23.
Tube frequency is useful for troubleshooting fault alarms. To troubleshoot fault alarms, see pages 75-77.
Live zero is useful for monitoring the indicated flow rate when it drops below the mass low flow cutoff, or when there is no flow. To configure the mass low flow cutoff, see page 25.
EXIT
The applications list shows all appli cat ion s that ar e installed and the software revision for each. Refer to this screen if you need to know the software revision number to report problems.
5.9 Power outage
View
Po wer outa ge
Power Outage
#3 Power Off At
06:00 28 OCT 1998
#3 Power On At
06:30 28 OCT 1998
#2 Power Off At
08:02 2 AUG 1998
#2 Power On At
08:05 2 AUG 1998
CLEAR EXIT
The power outage menu enables you to view the power off and power on times and dates for the last three power outa ges that lasted more than 30 seconds.
To clear times and dates, press CLEAR.
48
ALTUS™ Net Oil Computer Manu al
6 Continuous Mode
6.1 Continuous mode configuration
6.2 Startup and display test
6.3 Process monitor
6.4 Accessing continuous mode
Figure 6-1. Process monitor mode
To configure the NOC to operate in continuous mode, see page 16.
At startup, the transmitter automatically tests its display. During display testing, all pixels darken for approximately five seconds. After the display test is completed:
1. The Micro Motion
2. An application list appears.
3. The transmitter enters the operation mode, as shown in
The process monitor is the default operation mode. See
To access the continuous mode, press VIEW.
®
logo appears.
Figure 6-1
Figure 6-1
.
.
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
Volume Flow
Backlit
display
Volume Total
NEXT PRINT VIEW
Function buttons
ALTUS™ Net Oil Computer Manu al
DEVICE 1
4,352.33
bpd
56,485.88
bbl
Cursor control buttons
Security button
49
Continuous Mode
continued
6.5 Viewing production measurements
View
Well performance meas
Well Performance Meas
View Production Meas
Quick View Pause / Resume Reset
SEL HELP EXIT
View Production Meas
Net Oil
Water Cut Gross Flow Net Water Drive Gain Density Temperature Back Flow Mass Flow Uncorrected Flow
To view production measurements:
1. At the operation screen, press VIEW.
2. Select Well Performance Meas.
3. Select View Production Meas.
4. Select any of the production measurements that are listed in
Table 6-1
, page 51.
SEL EXIT
Net Oil
Actual Rate
13,110 bpd
Average Rate
13,050 bpd
Minimum Flow
12,111 bpd
Minimum Time/Date
08:23 28 SEPT 98
EXIT
For net oil, water cut, net water, density, temperature, mass flow, and uncorrected flow, the display indicates the actual value, the average value, the minimum and maximum values, the
time and date when minimum and maximum values were achieved, and the time and date of the last reset.
F or drive gain and back flow , the display indicates the actual value, the average value, the maximum value, the time and date when the maximum value was achieved, and the time and date of the last reset.
50
ALTUS™ Net Oil Computer Manu al
Continuous Mode
View
Well performance meas
View production meas
Temperature
Actual Temperature
Average Temperature
Minimum Temperature
Minimum Time/Date
08:23 28 SEPT 98
RESET EXIT
continued
Temperature
123.4 degF
122.7 degF
112.6 degF
Drive gain, density, temperature, and back flow menus have an individual RESET button for each, which enables resetting of these individual values in the menu.
Drive gain, density, temperature, and back flow are also reset when well performance measurements are reset (see page 54).
Using the Person-Process
Interface
Table 6-1. Continuous production measurements
Note
• For net oil, water cut, net water, density, temperature, mass flow, and uncorrected flow, the NOC indicates the actual value, the average value, the minimum and maximum values, the time and dat e w hen minimum and maximum values were achieved, and the time and date of the last res et
• For drive gain and back flow, the NOC indicates the act ual value, the average value, the maximum value, the time and date when the maximum value was achieved, and the time and date of t he l as t re set
Production measurement Definition
Net oil • Net oil, in barrels or cubic meters, at 60°F, 15°C, or 20°C
• N et oi l cannot be reset in this menu
Water cut • Water cut as 0% to 100% at 60°F, 15°C, or 20°C
• Water cut cann ot be reset in this menu
Gross flow • Flow rate of oil and water, in barrels or cubic meters, at 60°F, 15°C, or 20°C
• Gross flow cannot be reset in this menu
Net water • Net water, in barrels or cubic meters, at 60°F, 15°C, or 20°C
• N et water can not be r eset in this menu
Drive gain • Sensor drive gain in volts
• R ecorded drive gain can be reset individually
Density • Fluid density, in density unit selected during configuration
• D uring transient bubble remediation, the density at which the measure m ent is being held, if hold last value was selected as the action taken (see pag es 21-23)
• Density can be reset individually
Temperature • Fluid temperature, in temperature unit select ed during configuration
• Temperature can be reset individuall y
Back flow • Actual volume flow rate in reverse direction
• B ack flow can be r eset individually
Mass flow • Mass flow rate of all fluid
• Mass flow cannot be rese t in t hi s m enu
Uncorrected flow • Select any of these production measurements that are no t corrected for temperature:
- Uncorrecte d oil
- Uncorrecte d water
- Uncorrecte d water cut
- Uncorrecte d gross
• U ncorrected flow canno t be res et in the se menus
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
51
Continuous Mode
continued
6.6 Quick view
View
Well performance meas
Quick view
Quick View
Average Net Oil Rate
30,110.98 bpd
Net Oil Total
7,654,321.89 bbl
Average Water Cut
Average Gross Rate
The quick view menu allows you to view the following values:
Average net oil rate
Net oil total
Average water cut
Average gross rate
Gross total
Average/total since last reset
Test time elapsed
To access the quick view menu:
1. At the operation screen, press VIEW.
2. Select Well Performance Meas.
3. Select Quick View.
12.11 %
724.29 bpd
EXIT
6.7 Pause and resume
View
Well performance meas
Pause / resume
Well Performance Meas
View Production Meas Quick View
Pause / Resume
Reset
SEL HELP EXIT
52
To pause or resume the accumulation of production measurements:
1. At the operation screen, press VIEW.
2. Select Well Performance Meas.
3. Select Pause / Resume.
ALTUS™ Net Oil Computer Manu al
Continuous Mode
Pause / Resume
Production Meas
PAUSE EXIT
continued
Resumed
4. To pause accumulation of production measurements, press PAUSE.
Using the Person-Process
DEVICE 1 Production Measure­ments are on
Pause
Paused Time
0:08 hrs:min
RESUME EXIT
Alarm-Meas Paused
Net Oil
Actual Rate
13,110 bpd
Average Rate
13,050 bpd
Minimum Flow
12,111 bpd
Minimum Time/Date
08:23 28 SEPT 98
ACK
5. To resume accumulation of production measurements, press RESUME.
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
Fifteen minutes after measurements have been paused, the transmitter produces an alarm message that reads, "Meas Paused."
Press ACK to acknowledge the alarm.
The "Meas Paused" alarm will be produced every
15 minutes until measurements are resumed.
ALTUS™ Net Oil Computer Manu al
53
Continuous Mode
continued
6.8 Reset
View
Well performance meas
Reset
Well Performance Meas
View Production Meas Quick View Pause / Resume
Reset
SEL HELP EXIT
Reset
Last Reset All
19:07 28 SEPT 1998
Paused Time
Test Time Elapsed
22:52 hrs:min
To reset performance measurements:
1. At the operation screen, press VIEW.
2. Select Well Performance Meas.
3. Select Reset.
4. When the warning screen appears, select YES to continue to with the reset.
WARNING
Selecting reset will reset all of the performance measurement totals, averages, minimums, and maximums at once.
Set control devices for manual operation before selecting reset.
The display shows the time and date of the last reset, the total amount of time well performance measurements have been paused since the last reset, and the elapsed test time since the last reset.
0:00 hrs:min
RESET EXIT
54
ALTUS™ Net Oil Computer Manu al
7 Well Test Mode
7.1 Well test mode configuration
7.2 Startup and display test
7.3 Process monitor
7.4 Accessing well test mode
Figure 7-1. Process monitor mode
To configure the NOC to operate in the well test mode, see page 16.
At startup, the transmitter automatically tests its display. During display testing, all pixels darken for approximately five seconds. After the display test is completed:
1. The Micro Motion
2. An application list appears.
3. The transmitter enters the operation mode, as shown in
The process monitor is the default operation mode. See
To access the well test mode, press VIEW.
®
logo appears.
Figure 7-1
Figure 7-1
.
DEVICE 1
.
Determination
Determination
Laboratory Density
In-Line Density
Volume Flow
Backlit
display
Volume Total
NEXT PRINT VIEW
Function buttons
ALTUS™ Net Oil Computer Manu al
352.33
bpd
485.88
bbl
Cursor control buttons
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
Security button
55
Well Test Mode
continued
7.5 Conducting a well test
View
Well performance meas
Well Performance Meas
Start Well Test
View Well Tests
SEL EXIT
Start Well Test
Wells 1 to 12
Wells 13 to 24
Wells 25 to 36
Wells 37 to 48
To conduct a well test:
1. At the operation screen, press VIEW.
2. Select Well Performance Meas.
3. Select Start Well Test.
4. Select the menu item for the number of the well that will be tested, then press CHG.
CHG EXIT
Wells 1 to 12
01: Tinsley 22-14b
02: N Cowden 24-17a 03: R Dutton 36-13c 04: B Olsen 23-15d 05: 13-24-44-5E6 06: 08-11-23-6E2 07: 18-44-04-3W5 08: 12-28-36-6W7
SAVE EXIT
5. Select the well that will be tested, then press SAVE.
56
ALTUS™ Net Oil Computer Manu al
Well Test Mode
Well Name
Last Test
START EXIT
01: Tinsley
Well #1
Tinsley 22-14b
09:32 21 OCT 1998
DEVICE 1
On Test
Purge Time Remaining
STOP VIEW EXIT
continued
26:31
6. Press START to start the well test.
If purge time is zero, the NOC first indicates test time as zero, then begins counting.
If purge time is not zero, the NOC counts downward and indicates the purge time. When the purge is completed, the elapsed test time is displayed, and continues increasing throughout the test.
To monitor performance measurements while the test is in progress, press VIEW. For more information, see page 60.
To stop the test, press STOP. For more information, see pages 58-59.
Determination
Determination
Laboratory Density
In-Line Density
01: Tinsley
DEVICE 1
On Test
Test Started
14:33 28 OCT 1998
Test Time Elapsed
2:30:13
STOP VIEW EXIT
ALTUS™ Net Oil Computer Manu al
When the purge is complete, the NOC indicates the start time and elapsed time for the test. The Test Started time is the time when the purge was completed and the well test began.
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
57
Well Test Mode
continued
7.6 Stopping and continuing a well test
DEVICE 1
01: Tinsley
On Test
Test Started
14:33 28 OCT 1998
Test Time Elapsed
2:30:13
STOP VIEW EXIT
01: Tinsley
Stop Well Test?
To stop a well test, press STOP.
To stop the test, press YES.
To continue the test, press NO.
YES NO
DEVICE 1
01: Tinsley
Test Stop
Test Started
14:33 28 OCT 1998
Test Time Elapsed
2:30:13
NEXT START EXIT
To test the next well in the sequence, press NEXT.
To start a new test on the same well, press START.
58
ALTUS™ Net Oil Computer Manu al
Well Test Mode
Well Name
Last Test
START EXIT
Well #2
N. Cowden 24-17a
14:30 22 OCT 1998
Well #1
continued
If a well test has been stopped, then NEXT has been pressed as explained on page 58, the next well in the sequence can be tested.
Laboratory Density
Determination
To test the same well again after a test has been stopped as explained on page 58, press YES.
To return to the well selection screen that is illustrated at step 5 (page 56), press NO.
Test this well again?
YES NO
Well #1
Purge this well
again?
YES NO
To purge the well again, press YES.
To start a test without purging the well, press NO.
Determination
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
In-Line Density
ALTUS™ Net Oil Computer Manu al
59
Well Test Mode
continued
7.7 Viewing performance measurements
DEVICE 1
01: Tinsley
On Test
Test Started
14:33 28 OCT 1998
Test Time Elapsed
2:30:13
STOP VIEW EXIT
Well #1
Actual Net Oil Rate
14,223.88 bpd
Average Net Oil Rate
14,010.99 bpd
Actual Water Cut
12.01 %
Average Water Cut
11.89 %
RETURN HELP EXIT
During a well test, you can view on-line values of performance measurements by pressing VIEW.
The NOC indicates the following performance measurements:
Actual net oil flow rate
Average net oil flow rate
Actual water cut
Average water cut
Actual gross flow rate
Average gross flow rate
Actual fluid density. During transient bubble remediation, the density at which the measurement is being held, if hold last value was selected as the action taken (see pages 21-23)
Actual fluid temperature
60
To view detailed performance measurements for a well that is being tested, see pages 61-62.
ALTUS™ Net Oil Computer Manu al
Well Test Mode
continued
7.8 Viewing performance measurements for the current test
View
Well performance meas
Well Performance Meas
Return to Well Test View Well Tests
View Current Test
SEL EXIT
01: Tinsley
Net Oil
Water Cut Gross Flow Net Water Drive Gain Density Temperature Back Flow Mass Flow Uncorrected Flow Test Times
SEL EXIT
To view detailed performance measurements for the well that is being tested:
1. At the operation screen, press VI EW.
2. Select Well Performance Meas.
3. Select View Current Test. This menu item appears only while a well test is in progress.
4. Select any of the performance measurements that are listed in
Table 7-1
, page 62.
Determination
Determination
Laboratory Density
In-Line Density
ALTUS™ Net Oil Computer Manu al
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
61
continued
Well Test Mode
For each performance measure except test times, the NOC indicates the actual value, the average value, the minimum and maximum values, and the time and date when minimum and maximum values
Net Oil
Actual Rate
13,110.87 bpd
Average Rate
13,050.09 bpd
Minimum Flow
12.111.07 bpd
Minimum Time/Date
08:23 28 SEPT 1998
EXIT
were achieved.
Table 7-1. Performance measurements for current well test
Note
For each performance measurement except test times, the NOC indicates the actual value, the average value, the minimum and maximum values, and the time an d dat e w h en minimum and maximum values we re achieved
Performance measure D ef i ni ti on
Net oil Net oil, in barrels or cubic meters, at 60°F, 15°C, or 20°C Water cut Water cut as 0% to 100% at 60°F, 15°C, or 20°C Gross flow Volume flow of oil and water, in barrels or cubic meters, at 60°F, 15°C, or 20°C Net water Net water, in barrels or cubic meters, at 60°F, 15°C, or 20°C Drive gain Sensor drive gain in volts Density Fluid density, in density unit selected during configuration Temperature Flui d t em perature, in temperature unit selected during configuration Back flow Reverse flow rate of all fluid Mass flow Mass flow rate of all fluid Uncorrected flow Select any of these performa nce measurements that are not cor r ect ed for temperature:
Te st times View the following times:
• Uncorrected oil
• Uncorrected water
• Uncorrected water cut
• Uncorrected gross
•Test started
• Test time elapsed
• Transient bubble time
62
ALTUS™ Net Oil Computer Manu al
Well Test Mode
continued
7.9 Viewing previous well tests
View
Well performance meas
Well Performance Meas
Start Well Test
View Well Tests
SEL EXIT
Start Well Test
Wells 1 to 12
Wells 13 to 24
Wells 25 to 36
Wells 37 to 48
To view performan ce mea su re men ts for well tests that have been completed:
1. At the operation screen, press VI EW.
2. Select Well Performance Meas.
3. Select View Well Tests.
4. Select the menu item for the number of the well that has been tested, then press CHG.
Determination
Determination
Laboratory Density
In-Line Density
CHG EXIT
Wells 1 to 12
01: Tinsley 22-14b
02: N Cowden 24-17a 03: R Dutton 36-13c 04: B Olsen 23-15d 05: 13-24-44-5E6 06: 08-11-23-6E2 07: 18-44-04-3W5 08: 12-28-36-6W7
SAVE EXIT
5. Select a well that has already been tested, then press SAVE.
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
ALTUS™ Net Oil Computer Manu al
63
Well Test Mode
01:42 14 OCT 1998
10:12 13 SEP 1998 09:04 14 AUG 1998
SEL HELP EXIT
Net Oil
Water Cut Gross Flow Net Water Drive Gain Density Temperature Back Flow Mass Flow Uncorrected Flow Test Times
SEL EXIT
Well #1
01: Tinsley
continued
6. Select the time and date of the test for which performance measurements will be viewed. The listed time is the time when the purge was completed and the well test began.
7. Select any of the performance measurements that are listed in
Table 7-2
, page 65.
Average Rate
Minimum Flow
Minimum Time/Date
08:23 28 SEPT 1998
Maximum Flow
64
For each performance measure except test times, the NOC indicates the average value, the minimum and maximum values, and the time and date when minimum and maximum values were achieved.
01: Tinsley
13,050.09 bpd
12.111.07 bpd
14,097.45 bpd
EXIT
ALTUS™ Net Oil Computer Manu al
continued
Well Test Mode
Table 7-2. Performance measurements for previous well tests
Note
For each performance measu re m ent except test times, the NOC indi cat es th e average value, the minimum and m aximum values, and the time and date when minimum and maximum values were achieved
Performance measure Def inition
Net oil Net oil, in barrels or cubic meters, at 60°F, 15°C, or 20°C Water cut Water cut as 0% to 100% at 60°F, 15°C, or 20°C Gross flow Volume flow of oil and water, in barrels or cubic meters, at 60°F, 15°C, or 20°C Net water Net water, in barrels or cubic meters, at 60°F, 15°C, or 20°C Drive gain Sensor drive gain in volts Density Fluid density, in density unit selected during configuration Temperature Flui d t em perature, in temperature unit selected during configuration Back flow Reverse flow rate of all fluid Mass flow Mass flow rate of all fluid Uncorrected flow Select any of these performa nce measurements that are not cor r ect ed for temperature:
Te st times View the following times:
• Uncorrected oil
• Uncorrected water
• Uncorrected water cut
• Uncorrected gross
•Test started
• Test time elapsed
• Transient bubble time
Using the Person-Process
Interface
Configuration Using the View Menu Continuous ModeBefore You Begin Installation Considerations
ALTUS™ Net Oil Computer Manu al
65
66
ALTUS™ Net Oil Computer Manu al
8 Maintenance
Well Test Mode Maintenance
8.1 Alarm messages
Temperature Alarm
Net Oil
Actual Rate
13,110.87 bpd
Average Rate
13,050.09 bpd
Minimum Flow
12.111.07 bpd
Minimum Time/Date
08:23 28 SEPT 1998
HELP ACK
Responding to alarms
Temperature Alarm
Sensor temperature is outside the range of calculation accuracy for the NOC applica­tion. This range is 0 to 302 degF or -18 to 150 degC.
The NOC performs self-diagnostics during operation. If the NOC detects certain events or conditions, an alarm message appears in the highlight bar at the top of the screen.
If the alarm condition must be acknowledged, press ACK to acknowledge the alarm.
Laboratory Density
Determination
To respond to an alarm, press HELP, then follow the instructio ns on the scre en.
Determination
In-Line Density
The help screen explains what the alarm means.
The help screen will tell you what to do. You may be advised to perform an action, or to contact someone.
If the help occupies more than one screen, you can read all the help screens by pressing PGDN (page down) or PGUP (page up).
EXIT
ALTUS™ Net Oil Computer Manu al
Sensitivity Analysis Software Diagrams
67
Maintenance
continued
NOC alarm messages
The NOC produces alarm messages in the following situations:
Drive gain indicates transient bubbles in the Coriolis sensor.
Process temperature or density goes outside the acceptable range for the application.
Production measures have been paused for more than 15 minutes in the continuous operation mode.
Table 8-1
summarizes NOC alarms and lists corrective actions.
Table 8-1. Using NOC alarms
Notes
• To get help troubleshooting an alarm message, press HELP, then follow the instructions
• To acknowledge an alarm message, press ACK
Alarm message Cause
TBR Alarm Transient bubbles in Coriolis sensor • Check for cavitation, flashing, or bubble carry-under
Density Alarm D en si ty has gone below 0.6100 g/cc or
has gone above 1.1400 g/cc
Temperature Alarm Temperature has gone below 0°F
(–18°C) or above 302°F (150°C )
Pause Alarm Production measurements have been
paused for more than 15 minutes in continuous mode
Action
• Monitor density
• If desired, increase drive gain above which presence of transient bubbles will be indicated (see page 23)
• If desired, configure NOC to stop the well test if transient bubbles are detected (see page 23)
• I f desi r ed, configure NOC to hold las t value (see page 23)
• Check drive gain to see if gas has caused low density
• C heck drive gain to see if sediment has caused high density
• B ring temperature wit hi n ac ceptable limits
• Temperature is outside the specifie d accuracy range, but production is still being mea sur ed
• Acknowledge al arm
• Resume accumulation of production measurements
68
Transmitter alarm messages
The ALTUS transmitter produces several types of alarm messages. The following types of alarms do not drive outputs to fault levels:
Slug flow and output saturation alarms
Totalizer alarms
Calibration and trim alarms
Conditional status alarms The following types of alarms drive outputs to fault levels:
Critical status fault alarms
Transmitter failure fault alarms
Sensor error fault alarms
ALTUS™ Net Oil Computer Manu al
Maintenance
continued
Well Test Mode Maintenance
Alarms that do not generate fault outputs
Slug flow alarms
Conditions such as slug flow (large gas bubbles in a liquid flow stream) adversely affect sensor performance by causing erratic vibration of the flow tubes, which in turn causes the transmitter to produce inaccurate flow signals. If you program slug limits, a slug flow condition causes the transmitter to produce slug flow alarms.
The "Slug Flow" alarm indicates slug flow has occurred for less than the amount of time that is configured for the slug time. Outputs indicating the flow rate remain at the last measured flow rate before the slug flow condition occurred.
The "Slug Timeout" alarm indicates slug flow has occurred for more than the amount of time that is configured for the slug time. If the "Slug Timeout" alarm occurs, outputs indicating the flow rate go to the level that represents zero flow.
All outputs other than flow rate outputs continue to indicate the measured value for the process variable.
The flowmeter resumes normal operation when density stabilizes within the programmed slug flow limits.
Slug time can be up to 300 seconds.
If slug time is configured for 0.0 seconds, outputs indicating the flow rate will go to the level that represents zero flow as soon as slug flow is detected.
Laboratory Density
Determination
Table 8-2
summarizes slug flow alarms and lists corrective actions.
Table 8-2. Using slug flow alarms
Notes
• To get help troubleshooting an alarm message, press HELP, then follow the instructions
• To acknowledge an alarm message, press ACK
Alarm message Cause Action
Slug Flow • G as bubbles are causing density to go
below low slug flow limit
• S oli ds are causing process den sit y to exceed high slug flow limit
Slug Timeout Slug flow has occ ur re d for more th an
amount of time config ur ed for slug time
• Check process for cavitation, flashi ng, or leaks
• Monitor density
• If desired, enter new slug flow limits (see page 26)
• If desired, incre ase slug time (see page 26)
Determination
Sensitivity Analysis Software Diagrams
In-Line Density
ALTUS™ Net Oil Computer Manu al
69
Maintenance
continued
Output saturation alarms
If an output variable exceeds the upper range limit or goes below the lower range limit, the transmitter produces an output saturation alarm. The alarm can mean the output variable is outside appropriate limits for the process, or can mean measurement units need to be changed.
Table 8-3
summarizes output saturation alarms and lists corrective
actions.
Table 8-3. Using output saturation alarms
Notes
• To get help troubleshooting an alarm message, press HELP, then follow the instructions
• To acknowledge an alarm message, press ACK
Alarm message Caus e Action
Freq. Out Saturated Frequency output has exceeded 12,500 Hz • Alter fluid process
mA Out 1 High Sat Milliamp output 1 has exceeded 20.5 mA • Alter fluid process
mA Out 1 Low Sat Milliamp output 1 has gone below 3.8 mA • Alter fluid process
mA Out 2 High Sat Milliamp output 2 has exceeded 20.5 mA • Alter fluid process
mA Out 2 Low Sat Milliamp output 2 has gone below 3.8 mA • Alter fluid process
Drive Overrange • Severely erratic or complete cessation of
flow tube vibration
• Plugged flow tube
• C hange flow unit (see page 40)
• Change frequency and flow values, pulses per unit, or units per pulse (see pages 40-41)
• I ncr ease value of variable represented by milliamp output 1 at 20 mA ( see page 39)
• Decrease value of variable represented by milliamp output 1 at 4 m A (see page 39)
• I ncr ease value of variable represented by milliamp output 2 at 20 mA ( see page 39)
• Decrease value of variable represented by milliamp output 2 at 4 m A (see page 39)
• Fill sensor with process fluid
• Bring flow rate within sensor limit
• P ur ge flow tubes
Totalizer alarms
If the totalizers are operating, the transmitter produces totalizer alarms.
Table 8-4
summarizes totalizer alarms and lists corrective actions.
Table 8-4. Using totalizer alarms
Notes
• To get help troubleshooting an alarm message, press HELP, then follow the instructions
• To acknowledge an alarm message, press ACK
Alarm message Cause Action
Inventory 1 Rollover Inventory 2 Rollover Inventory 3 Rollover
Totalizer 1 Rollover Totalizer 2 Rollover Totalizer 3 Rollover
70
Inventory totalizer has exceeded rollover value and has rolled over to zero
Process totalizer has exceeded rollover value and has rolled over to zero
Press ACK to acknowledge alarm
ALTUS™ Net Oil Computer Manu al
Maintenance
continued
Well Test Mode Maintenance
Calibration and trim alarms
Calibration and trim alarms indicate the following conditions:
An output state or value has been set in the diagnostics menu
Calibration or output trim is in progress
Calibration was aborted by the operator
Calibration is complete
Table 8-5
summarizes calibration and trim alarms and lists corrective
actions.
Table 8-5. Using calibration and trim alarms
Notes
• To get help troubleshooting an alarm message, press HELP, then follow the instructions
• To acknowledge an alarm message, press ACK
Alarm message Cause Action
mA Out 1 Fixed Mil lia m p out put 1 trim or simulation in pro gres s Exit diagnostics menu mA Out 2 Fixed Milliamp output 2 trim or simulation in progress Freq. Out Fixed Frequency output trim or simulation in progress Cal In Progress • Sensor zero calibration in progress
• Density calibration in progress
• Temperature calibration in progress
Calibration Complete • Sensor zero calibration complete
• Density calibration complete
• Temperature calibration complete
Calibration Aborted • User aborted sensor zero calibration
• User aborted density calibration
• User aborted temperature calibration
• If "Calibration Complete" replaces "Cal In Progress", no action
• If "Calibration Failure" replaces "Cal In Progress" and sensor zero was perform ed, rezero after:
-
Eliminating mechanical noise, if possible
-
Completely shutting off flow
-
Ensuring interi or of sensor junction box is completely dry
• I f "Calibration Failure" replaces "Cal in Progress" and density or temperatu re cal ibrat ion was performed, recali b rat e for density or temperature
Press ACK to acknowledge alarm
• Re-initiate calibration procedure
• Existing calibration values will remain unchanged
Determination
Determination
Laboratory Density
In-Line Density
ALTUS™ Net Oil Computer Manu al
Sensitivity Analysis Software Diagrams
71
Maintenance
continued
Conditional status alarms
Conditio nal status a larms occur in the following situations:
During normal startup
During normal operation
After power to the transmitter has been cycled
After a master reset has been performed
Table 8-6
summarizes conditional status alarms and lists corrective
actions.
Table 8-6. Using conditional status alarms
Notes
• To get help troubleshooting an alarm message, press HELP, then follow the instructions
• To acknowledge an alarm message, press ACK
Alarm message Cause Action
Power Reset • Power failure
• Brownout
• Power cycle
Master Reset • Master reset has been performed
• Software configuration contains default values
EEPROM Initialized • EEPROM has been cleared and software
upgrade has been downloaded
• Software configuration contains default values
PPI Fault Person-Process Interface failed • Adj ust sc reen contrast (see page 47)
EEPROM Corrupt EEPROM has temporarily failed or been corrupted If problem persists, phone Micro Motion EEPROM Error
Check accuracy of totalizers
• Configure sensor calibration data (see pages 28-35)
• Do not operate transmi t te r until configuration has been verified
• If problem persists, phone Micro Motion Customer Service (see page 78 for phone numbers)
Customer Service (see page 78 for phone numbers)
72
ALTUS™ Net Oil Computer Manu al
Maintenance
continued
Well Test Mode Maintenance
Fault outputs
Outputs go to fault levels if a fault is detected. The transmitter also produces fault outputs when you perform configuration, calibration, or diagnostic tasks. See
Table 8-7
.
The transmitter can be configured to produce downscale, upscale, last measured value, or internal zero fault outputs. See
Table 8-8
.
To configure fault outputs, see page 37 and page 40.
The default configuration for fault outputs is downscale.
Table 8-7. Fault output levels
Software mode Output levels
Configuration Fault level Diagnostics Fault level Calibration Active (outputs indicate m eas ur ed values) Output simulation Active (outputs indicate values at which they are set)
CAUTION
Using last measured value or internal zero may hamper identification of fault outputs.
To make sure fault outputs can be identified, select downscale or upscale.
Laboratory Density
Determination
Table 8-8. Configurations for fault outputs
Fault limit Fault value
Downscale • Milliamp outputs can be configured from 1.0 to 3.6 mA;
default is 3.6 mA
• P ulse output goes to 0 Hz
Upscale • Milliamp outputs can be configured from 21.0 to
24.0 mA; default is 22.0 mA
• P ulse output goes to 15,000 H z
Last measured value Outputs hold at mA value or frequency that represents the
last measured value for the process variable before the fault occurred
Internal zero • Milliamp outputs go to mA value that represents 0.0 for
the process variable
• P ulse output goes to 0 Hz
Determination
Sensitivity Analysis Software Diagrams
In-Line Density
ALTUS™ Net Oil Computer Manu al
73
Maintenance
continued
Critical status fault alarms
Critical status fault alarms occur in the same situations in which conditional status alarms occur (see page 72); however, critical status fault alarms drive outputs to fault levels.
Table 8-9
summarizes critical fault alarms and lists corrective actions.
Table 8-9. Using critical status fault alarms
Notes
• To get help troubleshooting an alarm message, press HELP, then follow the instructions
• To acknowledge an alarm message, press ACK
Alarm message Cause Action
Warming Up • Transmitter is performing self-test
• O ut puts remain at fault levels until self-test is complete
Calibration Failure • Sensor zero calibration failed
• Density calibration failed
• Temperature calibration failed
• O ut puts remain at fault levels until calibration has been successfully completed
Charize Required • Master reset has been performed
• S of tware configuration contains default values
• O ut puts remain at fault levels until transmitter has been configured
Press ACK to acknowledge alarm
• If sensor zero calibration was performed, rezero after:
-
Eliminating mechanical noise, if possible
-
Completely shutting of f flow
-
Ensuring interior of sensor junction box is completely dry
• If density or temperatur e cal ibrat i on was performed, recalibrate for density or temperature
• Configure sensor calibration data (see pages 28-35)
• D o not operate transmitter until conf iguration has
been verified
Transmitter failure fault alarms
When a software or hardware failure occurs, the transmitter produces one of the fault alarms listed in
If any of the fault alarm messages listed in
Table 8-10
.
Table 8-10
appears on the screen, phone one of the Micro Motion Customer Service telephone numbers listed in
Customer service
, page 78.
CAUTION
Transmitter failure fault alarms are critical, and could result in measurement error.
The transmitter does not have any parts that are serviceable by the user. If a trans mitter f a ilure is in dicated, phone Micro Motion Customer Service (see page 78 for phone numbers).
Table 8-10. Using transmitter failure fault alarms
Alarm message Caus e Action
Hardware Failure Hardware has failed Phone Micro Motion Customer Service (see EEPROM Failure EEPROM has failed or been corrupted
page 78 for phone numbers)
74
ALTUS™ Net Oil Computer Manu al
Maintenance
CA UTION
continued
Fault alarms requiring troubleshooting
View
Diagnostic monitor
Diagnostic Monitor
Drive Gain
8.401 V
Tube Frequency
100.759 Hz
Live Zero
0.010 lb/min
EXIT
Some fault alarms require troubleshooting to isolate the problem that caused fault outputs to be produced. Fault alarms that require troubleshooting include:
Sensor Failure
Density Failure
Temperature Failure
Temperature Overrange
•RTD Failure
During troubleshooting the flowmeter could produce inaccurate output signals, resulting in measurement error.
Set control devices for manual operation before troubleshooting the flowmeter.
If the transmitter produces fault outputs and any of the alarm messages listed at the top of this page appears on the screen, follow these steps to troubleshoot the problem:
1. Press ACK, repeatedly if necessary, to clear all the messages.
2. Press VIEW to access the view menu.
3. Select Diagnostic Monitor.
4. Read the voltage for the drive gain: a. If drive gain exceeds 8.0 volts or is unstable,
Table 8-11
see
.
b. If drive gain is less than 8.0 volts, go to step 5,
page 76.
Determination
Determination
Laboratory Density
In-Line Density
Table 8-11. Troubleshooting excessive drive gain
Symptom Cause Corrective action
Drive gain exceeds 8.0 V or is unstable
ALTUS™ Net Oil Computer Manu al
Cavitation, flashing, or bubble carry-under • If possible, increa se inlet pressure and/or back pressure
Plugged flow tube Purge flow tubes
• D rive board failure
• S ensor imbalance
• S ensor failure See step 6, page 77
• I f pu mp is mounted upstre am fr om sensor, increase distance between pump and sensor
Phone Micro Motion Customer Service (see page 78 for phone numbers)
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
75
continued
Maintenance
5. Unplug sensor wiring terminal blocks at the transmitter.
Figure 8-1
Figure 8-2
Figure 8-1. Model 3500 sensor wiring terminals
illustrates Model 3500 sensor wiring terminals. illustrates Model 3700 sensor wiring terminals.
white
black (d r ains)
Connect outer braid
of shielded or
armored cable here
Model 3500 with I/O cable
(Terminal block attached to DIN rail)
Figure 8-2. Model 3700 sensor wiring terminals
brown red orange yellow green blue violet gray
yellow
violet
green
blue
brown
Model 3500 with screw-type or solder-tail
wiring connectors
(Middle term i nal block on back panel)
red brown yellow black (d r ains) violet orange green white blue gray
black (drains) orange white gray red
76
Model 3700 wiring terminals
(Blue terminal block)
ALTUS™ Net Oil Computer Manu al
continued
Maintenance
6. Measure ohms of resistance between the three wire pairs and wire triplet at the sensor junction box. a. If all measured resistance values are within the ranges listed in
Table 8-12
, the sensor cable is faulty or improperly connected.
Repair or replace the cable, or reconnect it according to the
9-Wire Cable Preparation and Installation Instruction Manual
.
b. If open or short circuits are found, the sensor case or junction box
contains moisture, or the sensor is damaged. See
Table 8-13
Table 8-12. Nominal resistance ranges for flowmeter circuits
Notes
• R esistance values increase 0. 38675 ohms per °C i ncrease in temperature
• Nominal resistance values will vary 40% per 100°C. However, confirming an open coil or shorted coil is more important than any slight deviation from the resist ance values presented below
• R esistance across blue and gray wires (ri ght pickoff circuit) should be within 1 0 % of res is t ance across green and whi t e w ires
(left pickoff circuit)
• A ct u al res ist ance values depend on the sensor model and date of manufacture
• R eadings across wire pair s should be stable. If they are unstable, see
Table 8-13
Well Test Mode Maintenance
.
Laboratory Density
Determination
Circuit Wire colors
Drive coil Brown to red 1 to 2 8 to 2650 Left pickoff Green to white 5 to 9 15.9 to 300 Right pickoff Blue to gray 6 to 8 15.9 to 300 Lead length compen sat or Orange to yellow 3 to 4 Ap proximat el y 0 t o 1 Temperature sensor Yellow to violet 4 to 7 100 Ω at 0°C + 0.38675 Ω per °C
Sensor junction box wiring terminals Nominal resi st ance range
Ω Ω
Table 8-13. Troubleshooting sensor error fault alarms
Notes
• To get help troubleshooting an alarm message, press HELP, then follow the instructions
• To acknowledge an alarm message, press ACK
Resistance at sensor junction box Cause Alarm message Action
All resistance values are within the ranges listed in
Open or short from green to white (termi nal 5 to terminal 9)
Open or short from blue to gray (terminal 6 to te rminal 8)
Open or short from red to brown (terminal 2 to terminal 1)
Open or short from orange to yellow (terminal 3 to terminal 4)
Open or short from yellow to violet (termi nal 4 to terminal 7)
Table 8-12
• Sensor cable is faulty
• Sensor cable is improperly connected
• M oisture in sensor case or junction box
• Open or short left pickoff
• M oisture in sensor case or junction box
• Open or short right pickoff
• M oisture in sensor case or junction box
• Open or short drive coil
• M oisture in sensor case or junction box
• Open or short lead length compensator
• M oisture in sensor case or junction box
• Open or short RTD
Sensor Failure Density Fail ure Temperature Failure RTD Failure Temperature Overrange
Sensor Failure Density Fail ure
Temperature Failure Temperature Overrange
RTD Failure Temperature Overrange
• Repair or replace cable
• Reconnect cable according to
9-Wire Cable Preparation
the
and Installation Instruction Manual
• If sensor case or junction box contains moisture, check for leaking junction box, conduit, or conduit seals
• If sensor case or junction box does not contain moistur e, return sensor to Micro Motion
Determination
Sensitivity Analysis Software Diagrams
In-Line Density
ALTUS™ Net Oil Computer Manu al
77
Maintenance
continued
Active alarm log
ALARMS
Active Alarm Log
Density Alarm
17-JUL-98 8:30
Temperature Alarm
10-JUL-98 9:04
Alarm-Meas Paused
10-JUL-98 5:10
HELP EXIT
8.2 Customer service
If the condition that caused an alarm is present, the alarm is listed in the active alarm log.
Each alarm is time/date stamped.
The first alarm listed is the most recent. The active alarm log can be accessed from the
maintenance menu or the view menu. To access the log from the maintenance menu:
1. At the operation screen, press the security button.
2. Select Maintenance.
3. Select Active Alarm Log. To access the log from the view menu:
1. At the operation screen, press VIEW.
2. Select Active Alarm Log.
For Customer Service, phone the Micro Motion Customer Service Department:
In the U.S.A., phone 1-800-522-6277, 24 hours.
Outside the U.S.A., phone 303-530-8400, 24 hours.
In Europe, phone +31 (0) 318 549 443.
In Asia, phone (65) 770-8155.
8.3 Setting outputs
The software allows you to set the states of discrete outputs or the values of milliamp outputs or the pulse output.
CAUTION
While diagnostic tasks are being performed outputs go to their configured settings, resulting in measurement error.
Set control devices for manual operation before accessing the diagnostics menu.
78
ALTUS™ Net Oil Computer Manu al
Maintenance
continued
Setting discrete outputs
Maintenance
Diagnostics
Simulate outputs
Discrete outputs
ALARMS
Discrete Outputs
Discrete Output 1
Discrete Output 2
Discrete Output 3
SAVE EXIT
YES
NO
NO
Setting milliamp outputs
Maintenance
Diagnostics
Simulate outputs
Milliamp outputs
ALARMS
Milliamp Outputs
Milliamp Output 1
Milliamp Output 2
12.578
8.994 mA
mA
To set the state of a discrete output:
1. Press the security button on the display face.
2. Select Maintenance.
3. Select Diagnostics.
4. Select Simulate Outputs.
5. Select Discrete Outputs.
6. Select the discrete output to be set.
7. Press CHG.
8. Use the cursor control buttons to toggle the output on or off.
• YES indicates the output is on.
• NO indicates the output is off.
9. Press SAVE to set the state of the output.
When you return to the operation mode, the states of the outputs are released and are again controlled by the application.
To set the value of a milliamp output:
1. Press the security button on the display face.
2. Select Maintenance.
3. Select Diagnostics.
4. Select Simulate Outputs.
5. Select Milliamp Outputs.
6. Select the milliamp output to be set.
7. Press CHG.
8. Use the cursor control buttons to change the output value.
9. Press SAVE to set the value.
When you exit to the simulate outputs screen, the output goes to its configured fault setting.
Determination
Determination
Laboratory Density
In-Line Density
SAVE EXIT
ALTUS™ Net Oil Computer Manu al
When you return to the operation mode, the values of the outputs are released and are again controlled by the application.
79
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
Maintenance
continued
Setting the frequency output
Maintenance
Diagnostics
Simulate outputs
Frequency output
ALARMS
Frequency Output
Frequency Output
5,258
SAVE EXIT
8.4 Density calibration
Hz
To set the value of the frequency output:
1. Press the security button on the display face.
2. Select Maintenance.
3. Select Diagnostics.
4. Select Simulate Outputs.
5. Select Frequency Output.
6. Press CHG.
7. Use the cursor control buttons to change the output value.
8. Press SAVE to set the value.
When you exit to the simulate outputs screen, the output goes to its configured fault setting.
When you return to the operation mode, the value of the output is released and is again controlled by the application.
At the factory, Micro Motion calibrates each NOC to work with a specific sensor. The NOC requires a field density calibration in the following situations:
The sensor flow tubes have become permanently coated.
The sensor flow tubes have eroded.
Density unit for calibration
If density calibration is necessary, use any of the following methods to calibrate the NOC:
Duplicate the factory calibration, as instructed on page 81.
Duplicate a previous field calibration, as instructed on page 82.
Use two fluids with known densities to perform a density calibration, as instructed on pages 83-86.
Density calibration requires reading and entering density values in grams per cubic centimeter.
CAUTION
Selecting configuration will interrupt measurement and control functions. All outputs will go to their configured fault settings.
Set control devices for manual operation before accessing configuration menus.
80
ALTUS™ Net Oil Computer Manu al
continued
Maintenance
CHG HELP EXIT
Configuration
Inputs
Coriolis
Density
Density Units
Density Damping
Slug Low Limit
0.000000 g/cc
Slug High Limit
1.000000 g/cc
Config process var
Density
g/cc
1.7 sec
To change the density unit:
1. Press the security button on the display face.
2. Select Configuration.
3. Select Inputs.
4. Select Coriolis.
5. Select Config Process Var.
6. Select Density.
7. At the density menu: a. Select Density Units. b. Press CHG. c. Select g/cc, then press SAVE.
Laboratory Density
Determination
Duplicating the factory calibration
Configuration
Inputs
Coriolis
Sensor cal data
Sensor Cal Data
↓↑
D1
0.000000
D2
1.000000
K1
5000.000
K2
50000.000
CHG HELP EXIT
To duplicate the factory calibration:
1. Press the security button on the display face.
2. Select Configuration.
3. Select Inputs.
4. Select Coriolis.
5. Select Sensor Cal Data.
6. Use the function buttons and the cursor control buttons to configure density calibration values.
Density calibration values include D1 and D2
density values, K1 and K2 tube periods, the flowing density correction factor, and the density calibration temperature coefficient.
To configure density calibration values, see
pages 30-34.
Density calibration values should be entered
from the sensor serial number tag or factory calibration certificate.
Tags and certificates vary in appearance,
depending on the sensor model number and manufacturing date. See pages 30-33.
Determination
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
In-Line Density
ALTUS™ Net Oil Computer Manu al
81
continued
Maintenance
Duplicating a previous calibration
Configuration
Inputs
Coriolis
Sensor Cal Data
D1
D2
K1
K2
CHG HELP EXIT
Sensor cal data
↓↑
0.000000
1.000000
5000.000
50000.000
CAUTION
Selecting configuration will interrupt measurement and control functions. All outputs will go to their configured fault settings.
Set control devices for manual operation before accessing configuration menus.
To dupli cat e a previous calibration, refer to the density factors that are recorded in the NOC configuration record ( steps:
1. Press the security button on the display face.
2. Select Configuration.
3. Select Inputs.
4. Select Coriolis.
5. Select Sensor Cal Data.
6. Use the function buttons and the cursor control buttons to enter D1, D2, K1, K2, FD, and dens temp coeff values from the worksheet.
Appendix A
), then follow these
82
ALTUS™ Net Oil Computer Manu al
Maintenance
continued
Well Test Mode Maintenance
Two-point density calibration
During 2-point density calibration, you command the transmitter to measure the sensor tube period when the flow tubes contain a fluid with a reference low density (usually air) and when the flow tubes contain a fluid with a reference high density (usually water).
Two-point density calibration is preferably performed under zero flow conditions. The calibration procedure includes a low-density calibration and a high-density calibration. If necessary, you can perform only the high-density calibration.
To prepare for the density calibration:
1. Use produced water to flush the flow line.
2. Remove the sensor from the flow line.
3. Drain the fluid from the sensor.
4. Rinse the sensor tubes with toluene at least twice, then rinse the tubes with acetone at least twice. Use another oil solvent if toluene or acetone is not available.
5. Use compressed air to blow the sensor dry until residual acetone or other solvent has been completely evaporated.
6. If sensor wiring was disconnected at step 2, reconnect the wiring and cycle power off, then on.
7. Wait approximately 5 minutes for the sensor flow tubes to achieve the ambient air temperature.
Laboratory Density
Determination
CAUTION
Selecting calibration will interrupt control functions. All control outputs will go to their configured idle settings.
Set control devices for manual operation before accessing calibration me n us.
Determination
Sensitivity Analysis Software Diagrams
In-Line Density
ALTUS™ Net Oil Computer Manu al
83
continued
Maintenance
CHG HELP EXIT
Maintenance
Calibration
ALARMS
Low Density
Density D1
0.000000 g/cc
Calibrate Density
Density
Low density
To perform the low-density calibration:
1. Prepare the sensor for density calibration as instructed on page 83.
2. Fill the sensor with a low-density fluid, such as air.
3. Use any established method to derive an accurate density, in grams per cubic centimeter, for the fluid at line conditions. If air is the low­density calibration fluid, a value from
Table 8-14
can be used for the density. (Specific gravity x
0.9991 = grams per cubic centimeter.)
4. Press the security button on the display face.
5. Select Maintenance.
6. Select Calibration.
7. Select Density.
8. Select Low Density .
9. At the low density menu:
10.Select Density D1, then press CHG.
11.Enter the line-condition density
cubic centimeter
, then press SAVE.
in grams per
12.Select Calibrate Density, then press CHG.
13.After calibration is complete, an alarm message appears at the top of the screen. Press ACK to acknowledge the alarm.
14.Press SAVE to save the calibration.
15.Perform the high-density calibration as instructed on pages 85-86.
Table 8-14. Density of air in grams per cubic centimeter
Pressure in millibar (inch es of mercury)
850 (25.14) .0010 .0010 .0010 .0010 .0010 .0010 .0009 .0009 .0009 900 (26.62) .0011 .0011 .0011 .0010 .0010 .0010 .0010 .0010 .0009 950 (28.10) .0012 .0011 .0011 .0011 .0011 .0011 .0010 .0010 .0010 1000 (29.57) .0 012 .0012 .0012 .0012 .0011 .0011 .0011 .0011 .0011 1050 (31.06) .0 013 .0013 .0012 .0012 .0012 .0012 .0012 .0011 .0011
If the actual atmospheric pressure is not known, use the following equation:
10°C 50°F
15°C 59°F
Air density in g/cc
20°C 68°F
=
Temperature in °C and °F
25°C 77°F
0.0012 1 0.000032
30°C 86°F
[]×
35°C 95°F
×()
Elevation in feet
40°C 104°F
45°C 113°F
50°C 122°F
84
ALTUS™ Net Oil Computer Manu al
Maintenance
continued
To perform the high-density calibration:
1. Perform the low-density calibration as instructed on page 84.
2. Press EXIT to return to the density menu.
3. Fill the sensor with a high-density fluid, such as tap water or distilled water.
4. If possible, shut off the flow. Otherwise, pump the fluid through the sensor at the lowest flow rate allowed by the process. The flow rate must be less than rate listed in
Table 8-15
, or the calibration will fail.
Table 8-15. Maximum flow rates for high-density calibration
Maximum flow rate
Sensor model lb/m in kg/h
®
ELITE
®
BASIS
Model D D6 0.5 13
Model DH DH6 0.5 13
Model DL DL65 62 1695
Model DT DT65 75 2040
CMF010 1 27 CMF025 20 545 CMF050 62 1700 CMF100 250 6800 CMF200 800 21,775 CMF300 2500 68,040 F025 10 272 F050 31 850 F100 125 3400 F200 400 10,887
D12 1 33 D25 6 170 D40 11 306 D65 75 2040 D100 200 5445 D150 700 19,050 D300 1750 47,625 D600 6250 170,100
DH12 1 33 DH25 6 170 DH38 12 340 DH100 200 5445 DH150 700 19,050 DH300 1750 47,625
DL100 200 5445 DL200 875 23,812
DT100 200 5445 DT150 350 9525
Well Test Mode Maintenance
Determination
Determination
Sensitivity Analysis Software Diagrams
Laboratory Density
In-Line Density
ALTUS™ Net Oil Computer Manu al
85
continued
Maintenance
CHG HELP EXIT
Maintenance
Calibration
ALARMS
High Density
Density D2
0.100000 g/cc
Calibrate Density
Density
High density
5. To ensure stable density, make sure the fluid in the flow tubes remains
completely
free of gas bubbles during the calibration. Using a rubber hammer, tap on the sensor case to dislodge any air bubbles that might be clinging to the flow tubes.
6. Wait approximately five minutes for the sensor tubes to achieve the same temperature as the high-density calibration fluid.
7. Use any established method to derive an accurate density, in grams per cubic centimeter, for the fluid at line conditions. If tap water is the high-density calibration fluid, a value from
Table 8-16
can be used for the density. (Specific
gravity x 0.9991 = grams per cubic centimeter.)
8. Select High Density.
9. At the high density menu:
10.Select Density D2, then press CHG.
11.Enter the line-condition density
cubic centimeter
, then press SAVE.
in grams per
12.Select Calibrate Density, then press CHG.
13.After calibration is complete, an alarm message appears at the top of the screen. Press ACK to acknowledge the alarm.
14.Press SAVE to save the calibration.
Table 8-16. Density of water
Temperature
32 33 34 35 36 37 38 39 40
41 42 43 44 45 46 47 48 49
50 51 52 53 54 55 56 57 58
0.0
0.6
1.1
1.7
2.2
2.8
3.3
3.9
4.4
5.0
5.6
6.1
6.7
7.2
7.8
8.3
8.9
9.4
10.0
10.6
11.1
11.7
12.2
12.8
13.3
13.9
14.4
Density
in g/cc
0.9998
0.9998
0.9999
0.9999
0.9999
0.9999
0.9999
1.0000
1.0000
0.9999
0.9999
0.9999
0.9999
0.9999
0.9999
0.9998
0.9998
0.9998
0.9997
0.9996
0.9996
0.9995
0.9995
0.9994
0.9994
0.9992
0.9992
Temperature
59 60 61 62 63 64 65 66 67
68 69 70 71 72 73 74 75 76
77 78 79 80 81 82 83 84 85 86
15.0
15.6
16.1
16.7
17.2
17.8
18.3
18.9
19.4
20.0
20.6
21.1
21.7
22.2
22.8
23.3
23.9
24.4
25.0
25.6
26.1
26.7
27.2
27.8
28.3
28.9
29.4
30.0
Density
in g/cc°F °C °F °C
0.9991
0.9991
0.9989
0.9989
0.9988
0.9987
0.9986
0.9984
0.9983
0.9982
0.9981
0.9980
0.9980
0.9979
0.9977
0.9975
0.9973
0.9972
0.9970
0.9969
0.9968
0.9966
0.9964
0.9963
0.9961
0.9960
0.9958
0.9956
86
ALTUS™ Net Oil Computer Manu al
9 Laboratory Determination of
Dry Oil and Produced Water Densities
9.1 Reasons for using live oil density
To enable the most accurate possible water cut and net oil measurements, "live oil" density rather than "dead oil" density should be programmed into the NOC. "Live oil" refers to the crude oil at line conditions. Reducing the operating pressure to atmospheric pressure causes the live oil to lose its solution gas or light-end components and become a dead oil at a greater density than when it was under pressure.
The difference between the density of live oil and the density of dead oil can be quite significant, depending on the gas-to-oil (GOR) ratio and the separator pressure and temperature. If dead oil density is used, water cut measurements will be too low, and net oil will be too high.
This chapter describes the laboratory method for measuring dry oil and produced water densities.
The method involves using a precision density meter to determine the density of a liquid sample taken from the flow line.
The method requires correcting measured densities of dry oil and produced water to 60°F.
To obtain an IBM-compatible software program for computing corrected crude oil and produced water densities, phone the Micro Motion Customer Service Department:
In the U.S.A., phone 1-800-522-6277, 24 hours.
Outside the U.S.A., phone 303-530-8400, 24 hours.
In Europe, phone +31 (0) 318 549 443.
In Asia, phone (65) 770-8155.
Determination
Determination
Laboratory Density
In-Line Density
9.2 Laboratory density
The laboratory method requires the equipment listed in
Table 9-1
measurement
Table 9-1. Laboratory equipment for determining live oil and produced water densities
Equipment Suggested supplier Mo del number
Precision lab density met er (0.0001 g/cc accuracy) Anton Paar DMA48* Pressure adaptor for density meter (80 psi g or lower) High-pressure density measuring cell (80 psig or higher) DMA512 Thermostati ng c irculating water bath Neslab RTE-1000 Stainless steel sample cy l in der s ( 500 ml capacity) Whitey 316L-HDF4-50 0 Stainless steel ¼-inch valve SS-33VM4-S4 Stainless steel ¼-inch tubi ng No specific supplier Nitrogen cylinder equipped with pressure regulator Pressure gauges * The standard Anton Paar density meter m easures liquid density at atmospheric pressur e. Wh en fitted with a pressure
adaptor, the meter can operate up to 80 psig. Wh en coupled with an external stainless steel measuri ng cell such as the Model DMA512, the DM A48 can measure liquid den si t y up to 5500 psig.
ALTUS™ Net Oil Computer Manu al
.
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
87
Laboratory Determination of Dry Oil and Produced Water Densities
continued
Taking a sample from the flow line
Locate the sample port downstream from the sensor, as shown in
Figure 9-1
probe opening situated near the center of the flow pipe. To ensure a representative sampling, install a static mixer immediately upstream from the sample port.
Use one of the following sampling procedures:
Method 1
• pressure is higher than 80 psig, or where flexible stainless steel tubing is not available.
Method 2
• pressure is less than 80 psig, or where flexible stainless steel tubing is available.
. The sampling port should protrude into the flow line, with the
involves using a water-filled sample cylinder if separator
involves using an empty sample cylinder if separator
Figure 9-1. Sample port for laboratory density measurement
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Laboratory Determination of Dry Oil and Produced Water Densities
Method 1
Use a water-filled sample cylinder if separator pressure is higher than 80 psig, or when flexible stainless steel tubing is not available.
1. Fill the clean sample cylinder with produced water, preferably the water from the well being tested or water with similar salinity. Pressurizing the sample cylinder is not necessary.
2. Connect the sample cylinder to the sampling port as shown in
Figure 9-2
3. Open V-1, then open V-4 to purge the connecting lines briefly . Close V-4 and open V-2 to equalize the pressure in the sample cylinder.
4. Slowly open V-3 to draw liquid into the sample cylinder and to displace the water in the sample cylinder.
5. Close V-3 when a trace of oil appears at the drain port.
6. Wait for a few minutes to allow the free water to settle in the sample cylinder. The wait time varies, depending on whether the oil and water are readily separable.
7. Slowly open V-3 to drain the free water from the bottom drain port and to allow additional liquid sample to flow into the sample cylinder. Close V -3 when a trace of oil appears at the drain port.
8. Repeat steps 6 and 7 several times until the amount of free water drained is less than 50 ml. This indicates that a sufficient amount of oil/water emulsion has been collected in the sample cylinder.
9. Close V-1, V-2, and V-3. Open V-4 to depressurize the sample line.
10. Remove the sample cylinder. Record well I.D., sample pressure, and sample temperature.
. Close V-1, V-2, V-3, and V-4.
continued
Laboratory Density
Determination
Figure 9-2. Laboratory sampling procedure using water-filled cylinder
Determination
Sensitivity Analysis Software DiagramsWell Test Mode Maintenance
In-Line Density
ALTUS™ Net Oil Computer Manu al
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Laboratory Determination of Dry Oil and Produced Water Densities
Method 2
Use an empty sample cylinder if separator pressure is less than 80 psig, or where flexible stainless steel tubing is available.
1. Connect an empty sample cylinder to the sampling port as shown in
Figure 9-3(A)
should point upward at about 75 degrees from horizontal.
2. Open V-1, then open V-2.
3. Slowly open V-3 to withdraw liquid sample into the sample cylinder and purge the air out of the sample cylinder. Close V-3 when a trace of liquid appears at the outlet port.
4. Secure the sample cylinder to a support base as shown in
Figure 9-3(B)
5. Wait for a few minutes to allow the free water to separate in the sample cylinder. The wait time varies, depending on whether oil and water are readily separable.
6. Slowly open V-3 slowly to drain the free water from V -3 and withdraw oil/water mixture into the sample cylinder. Close V-3 when a trace of oil appears at the outlet port.
7. Repeat steps 5 and 6 several times until the amount of free water drained is less than about 50 ml. This indicates that a sufficient amount of oil/water emulsion has been collected in the sample cylinder.
8. Close V-1, V-2, and V-3. Open V-4 to depressurize the sample lines.
9. Remove the sample cylinder. Record well I.D ., sample pressure, and temperature.
, with V-1, V-2, V-3 and V-4 closed. The outlet port
. Outlet V-3 should point downward.
continued
Figure 9-3. Laboratory sampling procedure using empty cylinder
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