dP-Cell Level Measurement
3D. Differential
Pressure Level Measurement
1.
Calculate the required differential
pressure range for a given dp level measurement application.
2.
Select and describe applications for wet
and dry legs, chemical seals and purge or bubbler systems.
3.
Explain problems that may be encountered
due to change in ambient temperature and some solutions.
4.
Sketch a typical installation for a dp cell
and give reasons for the method used.
THEORY
Liquid
level can be measured by measuring the pressure it exerts due to its
gravitational attraction to the earth.
P
= rog h ro-
density of the fluid
g -
gravity
h -
height of liquid column
P -
pressure exerted
If
the density of the fluid is constant then the pressure exerted by a column of
liquid will be directly proportional to the fluids height or level. In other words, differential pressure level
measurement measures the pressure due to a column of liquid and infers the
level from this.
Example:
Note: The fluid level is directly related to the pressure measured by
the dp cell.
The
pressure measured by the dp cell needs to be related to the fluids height for
proper operation. This is accomplished
by determining the P that the dp cell would see when the fluid level is at the
Lower Range Valve (LRV) and determining the P
that the dp cell would see when the fluid level is at the Upper Range Valve (URV). This gives the necessary calibration range (DP @ the LRV to DP
@ the URV) for the dp cell so that its output will be proportional to the
fluids level.
Setting up a differential pressure transmitter for level measurement
There
are many different methods used to measure level using a differential pressure
transmitter (dp cell). Selecting the
appropriate method for a given application will be covered later in this
module. However, the basic steps
required to properly set up the dp cell to measure level are similar and
presented here.
1. The calibration range required for a
particular application must be determined.
The transmitters installed location must be know to be able to perform
this calculation.
2. The dp cell must be properly calibrated
using an appropriate pressure standard.
3. The transmitter is installed in its proper
location and the connection lines are “bleed” to ensure that there is no air
pockets in the line that may effect the pressure being measured. (Air pocket will cause measurement errors due
to surface tension especially when measuring low pressures)
Following
these steps will result in proper level measurement.
Atmospheric vessels using a
standard dp cell
For
vessels operated at atmospheric pressure, the high side of the dp
cell is connected to the bottom of the vessel and the low side is vented
to atmosphere.
Example:
Process
fluid RD = .750 Assume
g =
9.81 m/s2
Calculating
the required calibration range:
P seen by the dp cell when fluid is at its LRV
PH = (.750)(1000 kg/m3)(9.81 m/s2)(.2m)
+ Patm
PH = 1.4715 kPag + Patm
PL = Patm
P
= PH - PL
= (1.4715 kPag + Patm) - Patm = 1.4715 kPag
Calculation (continued)
P seen by the dp cell when fluid is at its URV
PH = (.750)(1000 kg/m3)(9.81 m/s2)(1.2m)
+ Patm
PH = 8.829 kPag + Patm
PL = Patm
P
= PH - PL
= (8.829 kPag + Patm) - Patm = 8.829 kPag
Therefore,
the calibration range is 1.4715 to 8.829
kPag
Calibration
procedure:
This
transmitter would now be calibrated for this P
range by using the appropriate pressure standards.
Installation:
The
dp cell is generally connected to the process with ½ inch tubing or ½ inch
pipe. A block valve should be installed
between the vessel and the dp cell to allow for isolation and maintenance of
the dp cell without having to shut down the process and drain the vessel. The preferred location for the transmitter is
below the connection point.
Differential
pressure transmitters come with two connection points to each of the high side
and low side. This allows the
installation to be “bleed” to ensure no air pocket exist in the connection line
and that the line is not plugged. The
connection point not connected to the vessel is opened allowing the process
fluid to “bleed” through the connecting line.
Note,
this type of installation would only be practical on those applications where
the connection line will not plug and the process fluid will not freeze or
congeal in the lines.
Operation:
If
the output of the transmitter was 12.000 mA this means that the level in the
tank from the LRV is
or
by calculation
PH = (.75)(1000 kg/m3)(9.81 m/s2)(0.7
m) + 0 kPag=5.150 kPag
PL = 0 kPag
P
= (5.150 kPag) - (0 kPag) = 5.150 kPag
With
proper calibration and installation the
output of the transmitter is directly related to the level in the vessel.
Notes:
1. If the inlet connection was 0.1 m from the
bottom of the tank then the level in the vessel from the bottom of the tank
would be .7 + .1 = 0.8 m or
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