|
|
|
This is a continuation of the Process Intensifier - Optimization with CFD: Part 1 paper. Process Intensifiers with Dual Axial Impellers
Figures 3 and 4 show schematically the general concept of a Process Intensifier with axial flow impellers. The differences between the two models are:
The general flow pattern is from the left to right in these illustrations. A Z-divider plate with orifice does not exist in these tested models. That is not to say that the vendors would not offer this as an option (see Figures 3a and 4a).
Model LTA: The Lightnin Line Blender model (Figs. 3,5) has dual 3.5" (88.9 mm) axial 3-bladed PBT impellers with a blade width to impeller diameter ratio of w/D = 0.25. D/T is approximately 1/3. Although Lightnin would use hydrofoils, our model approximates the hydrofoil by using 3 blades at 30 degrees. Both impellers are down-pumpers. The distance of the centerline of each impeller to the top and bottom of the pipe is 2.5" (63.5 mm) and the spacing between the impellers is S = 5" (127 mm). There are two baffles. One baffle is shaped like a horseshoe and is on the wall of the pipe at the centerline of the shaft. It is continuous around the pipe except at the top, where it is open enough to allow insertion of the impellers. Another baffle runs the length of the pipe section to form a cross directly under the lower impeller. This is the pipe version of a standard crucifix baffle configuration. A secondary fluid to be mixed would enter the pipe 5 to 10 impeller diameters in front of the Line Blender through a T, depending on the flow rate. Model HGA: The Hayward Gordon In-Line Mixer model (Figs. 4,5) has dual 5" (127 mm) axial 3-bladed PBT impellers with w/D = 0.25. D/T is approximately 1/2. Although Hayward Gordon would use hydrofoils, our model approximates the hydrofoil by using a pitched bladed turbine with 3 blades at 30 degrees. The distance of the centerline of each impeller to the top and bottom of the pipe is 3" (76 mm) and the spacing between the impellers is S = 4" (102 mm). The top impeller is a down-pumper, while the bottom impeller is an up-pumper. One baffle is a horseshoe baffle on the wall of the pipe at the centerline of the shaft. It is interrupted on the bottom by a 10-degree gap and at the top, where it is open enough to allow insertion of the impellers. A criss-cross flow straightener also precedes the impellers. A secondary fluid to be mixed would enter through a vertical pipe half way between the flow straighteners and the impeller blade tips. Continue with Experimental Design subtopics... Dual Radial Process Intensifiers CFD Solid Shape Models Standard Geometries or skip the Experimental Section and Continue with Results or Go back to the Title Page
|
|
Send mail to webmaster@postmixing.com with questions or comments about this web site. |