Pipe Sizing for Sand Transfer - SSL (Metric Units)

Pipe Sizing for Sand Transfer - SSL (English Units)

Summary

Sand is being transferred from a quarry sand pit and being transferred to receiving deposits in two different locations. There are two valves that control the flow to each of these deposits by changing their opening position (modeled as Cv). The ratio of the mixture velocity to the velocity at which the sand will settle out of the liquid and form a stationary bed on the bottom of the pipe (Vsm) must be kept above 1.2 to avoid potentially plugging the pipe. Determine if the pipe size and velocity ratio is acceptable during the transient where one valve starts to close while the other opens further.

Note: This example can only be run if you have a license of the SSL module.

Topics Covered

• Entering solids data

• Reviewing calculated slurry output

• Using Design Alerts

Required Knowledge

This example assumes the user has already worked through the Walk-Through Examples section, and has a level of knowledge consistent with the topics covered there. If this is not the case, please review the Walk-Through Examples, beginning with the Beginner - Valve Closure example. You can also watch the AFT Impulse Quick Start Video (Metric Units) on the AFT website, as it covers the majority of the topics discussed in the Valve Closure example.

Model File

This example uses the following file, which is installed in the Examples folder as part of the AFT Impulse installation:

• Metric - Pipe Sizing for Sand Transfer - SSL.imp

Step 1. Start AFT Impulse

From the Start Menu choose the AFT Impulse 10 folder and select AFT Impulse 10.

To ensure that your results are the same as those presented in this documentation, this example should be run using all default AFT Impulse settings, unless you are specifically instructed to do otherwise.

Step 2. Define the Modules Group

First the SSL Add-on Module needs to be activated for use in the model. To do this, open Analysis Setup from the Common Toolbar or Analysis menu. On the Modules panel, check the box next to Activate SSL. After the SSL module is activated, the Settling option should being selected by default.

Step 3. Define the Fluid Properties Group

1. Carrier Fluid panel (Figure 1)

   1. Carrier Fluid = Basic (Water)

   2. Temperature = 21 deg. C

2. Slurry Definition panel (Figure 2)

   1. Slurry Model = Settling Slurry - Wilson, Addie, Clift

   2. Slurry Calculation Method = Detailed

   3. Concentration Type = Volume Fraction

   4. Amount Solids Added = 20 Percent

3. Solids Definition panel (Figure 3)

   1. Solids Specifications = User Specified Solids Added

   2. M (Stratification Ratio Exponent) = Calculated

   3. Terminal Velocity Parameter, Vt / Vts (Xi) = 0.55

   4. Density = 2.65 S.G. water

   5. d50 = 0.07 cm

   6. d85 = 0.17 cm

   7. Bulk Modulus = 16000 MPa

Step 4. Define the Pipes and Junctions Group

At this point, the first two groups are completed in Analysis Setup. The next undefined group is the Pipes and Junctions group. To define this group, the model needs to be assembled with all pipes and junctions fully defined. Click OK to save and exit Analysis Setup then assemble the model as shown in the figure below.

Figure 4: Layout of pipe system for Sand Transfer to Two Locations example

Once the system is in place, enter the input data for the pipes and junctions. Double-click each pipe and junction and enter the following data in the properties window.

Pipe Properties

1. Pipe Model tab

   1. Pipe Material = Steel - ANSI

   2. Size = 10 inch

   3. Type = STD (schedule 40)

   4. Friction Model Data Set = Standard

   5. Length = Use table below

   6. Wavespeed = Calculated Wavespeed

Pipe	Length (meters)
1	3
2	122
3	1.5
4	26
5	122
13	1.5
14	30.5
15	213

Junction Properties

1. Reservoir J1

   1. Name = Sand Pit

   2. Tank Model = Infinite Reservoir

   3. Liquid Surface Elevation = 0 meters

   4. Liquid Surface Pressure = 0 barG

   5. Pipe Depth = 0 meters

2. Pump J2

   1. Name = Main Slurry Pump

   2. Inlet Elevation = 1.2 meters

   3. Pump Model = Centrifugal (Rotodynamic)

   4. Performance Curve Used in Simulation = Standard Pump Curve

   5. Enter Curve Data =

Volumetric	Head	Power
m3/hr	meters	kW
0	152	764
910	145	820
1595	122	894
2050	91	1006

6. Curve Fit Order = 2

7. Click Generate Curve Fit Now, then click OK

3. Branch J3

   1. Elevation = 1.2 meters

4. Valve J4

   1. Name = Valve to Deposit #1

   2. Inlet Elevation = 1.2 meters

   3. Loss Model tab

      1. Loss Source = User Specified

      2. Loss Model = Cv

      3. Cv = 500

   4. Transient tab

      1. Transient Special Condition = None

      2. Initiation of Transient = Time

      3. Transient Data = Absolute Values

Time (seconds)	Cv
0	500
1	500
6	300
10	300

5. Branch J5

   1. Elevation = 6 meters

6. Reservoir J6

   1. Name = Deposit #1

   2. Tank Model = Infinite Reservoir

   3. Liquid Surface Elevation = 6 meters

   4. Liquid Surface pressure = 0 barG

   5. Pipe Depth = 0 meters

7. Valve J7

   1. Name = Valve to Deposit #2

   2. Inlet Elevation = 1.2 meters

   3. Loss Model tab

      1. Loss Source = User Specified

      2. Loss Model = Cv

      3. Cv = 400

   4. Transient tab

      1. Transient Special Condition = None

      2. Initiation of Transient = Time

      3. Transient Data = Absolute Values

Time (seconds)	Cv
0	400
5	500
10	500

8. Branch J8

   1. Elevation = 9 meters

9. Reservoir J9

   1. Name = Deposit #2

   2. Tank Model = Infinite Reservoir

   3. Liquid Surface Elevation = 9 meters

   4. Liquid Surface pressure = 0 barG

   5. Pipe Depth = 0 meters

Design Alerts

In this system the Velocity Ratio (mixture to settling velocity ratio or Vm/Vsm) must remain greater than 1.2 in each of the pipes to avoid the potential of the sand falling out of the slurry and plugging the pipe. Use the Design Alert Manager to add a Design Alert to each pipe. This will give a warning message in the output if the velocity ratio is below the minimum value.

ØFrom the Tools menu, select Design Alerts to open the Design Alert Manager. Click the green plus icon to create a new Design Alert.

1. Name = Min Velocity Ratio (Vm/Vsm)

2. Alert Applies To = Pipes

3. Parameter Type = Velocity Ratio (Vm/Vsm)

4. Alert When Values Is = Less Than or Equal To (<=)

5. Value = 1.2

6. Click the All button under the Pipes in Design Alert list

7. The Design Alert Manager window should now appear as shown in Figure 5

8. Click OK to return to the Workspace

Open the Pipe Properties window of any pipe and click the Design Alerts tab. Check to confirm that the Design Alert you created has been applied (Figure 6).

ØTurn on the Show Object Status from the View menu to verify if all data is entered. If there are objects that are not defined, the uncompleted pipes or junctions will have their number shown in red on the workspace. If this happens, go back to the uncompleted pipes or junctions and enter the missing data. If all objects are defined, the Pipes and Junctions group in Analysis Setup will have a check mark.

Step 5. Define the Pipe Sectioning and Output Group

ØOpen Analysis Setup and open the Sectioning panel. When the panel is first opened it will automatically search for the best option for one to five sections in the controlling pipe. The results will be displayed in the table at the top. Select the row to use one section in the controlling pipe. 

Step 6. Define the Transient Control Group

ØOpen the Simulation Mode/Duration panel in the Transient Control group. Enter 10 seconds for the Stop Time.

All groups should now be complete and the model is ready to run. If all groups in Analysis Setup have a green checkmark then Click OK and proceed. Otherwise, enter the missing information.

Step 7. Run the Model

Click Run Model from the toolbar or from the Analysis menu. This will open the Solution Progress window. This window allows you to watch the progress of the Steady-State and Transient Solvers. When complete, click the Output button at the bottom of the Solution Progress window.

Step 8. Examine the Output

In the Output window, there is a warning that the Design Alert was violated for Pipe P4. The minimum value for the run was 1.134 in station 14 at 9.999 seconds as shown in the Transient Max/Min table.

There are several factors that may be contributing to this. Pipe P4 is sloped upward which increases the settling velocity and decreases the velocity ratio of concern. Also, all pipes in the model have a 10 inch diameter. However, the main pipes P1 and P2 are carrying much more flow than the others so the pressure drop in these is greater. This could be reduced by increasing the size. The size cannot be increased too much because this would reduce the velocity ratio below the 1.2 minimum.

Step 9. Increase the Pipe Diameter and Re-run the Model

Return to the Workspace and change pipes P1 and P2 to 14-inch diameter. Since the size of the pipes were changed they need to be re-sectioned by opening the Pipe Sectioning and Output group in Analysis Setup. Click OK to accept the results.

Re-run the model and view the output. There should not be any warnings now that the pipes were changed. The Graph Results window will be more useful in understanding the results.

Step 10. Graph the Results

1. Change to the Graph Results window by either clicking on the Graph Results tab, from the Window menu, or by pressing CTRL+G.

2. On the Profile tab in the Quick Access Panel, select Pipes P1 through P5 (Figure 8). These represent the flow path to Deposit #1.

3. Choose Velocity Ratio (Vm/Vsm) for the Parameter to graph.

4. Check the boxes for Mx, Mn, and DA in order to display the maximum, minimum, and Design Alert.

5. Click Generate.

The resulting graph is shown in Figure 9. This represents the flow path that had the velocity ratio Design Alert warning when 10-inch pipe was used. Now with 14-inch pipe the minimum is above the 1.2 limit along the entire path.

In the Graph Parameters section on the Quick Access Panel change the parameter to Pressure Static and the units to barG. Click show to view the new graph (Figure 10).

You can also check the same parameters for the flow path leading to Deposit #2.

A time comparison of the velocity ratio in the critical pipes along the two flow paths is important to consider.

1. On the Transient Pipe tab, select Pipes P4 Inlet and P7 Inlet and add them to the Graph These Pipes/Stations list (Figure 11). These are the two sloped pipes which have the lowest velocity ratio.

2. Choose Velocity Ratio (Vm/Vsm) as the Parameter to graph.

3. Check the DA box to display Design Alerts on the graph.

4. Click Generate.

The resulting graph is shown in Figure 12. This shows that as the valve J4 closes and valve J7 opens the velocity ratios in the pipe immediately downstream change but stay in the acceptable range.

SSL Analysis Summary

A slurry of sand and water flowing to two deposits was modeled. The velocity ratio (Vm/Vsm) was examined to ensure a minimum value was maintained throughout the transient to avoid the danger of the sand settling out of the slurry and plugging the pipe. The analysis showed that the initial pipe diameter selected was not adequate and the created Design Alert was violated. A larger size was selected to meet the system requirements over the simulation time.