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ERDC TN-DOER-I5
August 2000
calculations it is assumed that the hop-
Table 2
per dredge is filled to volume (6,122 m3)
Sediment and Water Variables and
and that the load is at the maximum
Uncertainties
272,160 kg. The Case 1 calculation rep-
Variables
resents the "ideal" situation where the
ρm
ρi
ρw
instruments are all calibrated, and the
(g/cm3)
(g/cm3)
(g/cm3)
Values
density of the sediments (mineral and in
Nominal
2.65
1.80
1.00
situ) and associated water has been
High Uncertainty (U)
0.08
0.18
0.03
measured (low uncertainty). The Case
Low Uncertainty (U)
0.03
0.36
0.01
2 calculation is for instruments that are
all properly calibrated, but the sediment Table 3
and water properties are estimated and Hopper Dredge Variables and Uncertainties
therefore have a high degree of uncer-
Variables
ρh
tainty. Case 3 consists of a calculation
Vh
Wh
(g/cm3)
(m3)
(g/cm3)
where the instruments are out of calibra-
Values
tion (high uncertainty), and the sediment Nominal
1.20
6122.0
272160.0
and water densities are measured. The High Uncertainty (U) --
306.0
13608.0
final case (Case 4) represents the worst Low Uncertainty (U)
--
61.2
2721.6
case situation, where the instruments are
not calibrated, and the sediment and water densities are estimated (high uncertainty). The pipeline
dredge uncertainty calculations (volumetric flow rate and solids flow rate) are found in Table 4, and
the hopper dredge calculations (in situ volume content and solids content of the hopper) are found
in Table 5.
The pipeline uncertainty calculations reveal two important considerations. First, if the sediment
properties are well defined, and the instruments correctly calibrated (the ideal case), an acceptable
6 percent uncertainty in the production of the dredge can be realized. Secondly, the accuracy of the
sediment and water properties, primarily the in situ density, are the primary factors in influencing
the total accuracy of the calculation. Because of the inherent accuracy of the density and flow
velocity instrumentation, the in situ sediment density, with its wide range of uncertainty (conserva-
tively 2 to 10 percent) dominates the accuracy of the calculations. The in situ density can actually
vary up to 40 percent (1.2 to 2.0 g/cm3) depending on the sediment type and dredging environment.
The Case 3 calculation reveals that even when the instruments are out of calibration, the uncertainty
(8 percent) is reasonable with known sediment and water properties. The solids flow rate
calculations are more accurate because the mineral density of solids only varies to about a
maximum of 4 percent. The solids flow rate calculations indicate that the water density is the
dominant variable in affecting the production accuracy. The Case 4 calculation reveals an error
potential for volumetric production calculations as high as 25 percent if the instruments are not
properly calibrated and the sediment and water properties are not well defined.
The hopper production equations reveal the opposite trend. Because the measured density in the
hopper is dependent on the measurement of the draft of the vessel (pressure transducers), and the
volume in the hopper (ultrasonic water level transducers), the uncertainty in the production
calculation is sensitive to the calibration and proper operation of the instruments. For the volume
content calculations, the in situ density of the sediments has the greatest influence on the calculation
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