Artisi.... I did a preselection of pump Flowserve Titan TKL model. As you know, they are manufacturer of mechanical seals. In this moment, the problem is estimated consumption of flushing service, that must be added to normal pump capacity.
Sorry, basic data is the following:
Titan Slurry Heavy-duty, Radially Split-case Lined Pump
The pump will hand 1269 gpm of product with viscosity 3.91 cP. Head: ft H2O. Temperature: 567 F. 1.5 to 3% solids.
any of you have the drawing of pump indicated in subject? pump is for slurry service and I need dimensional drawing in order to verify size against available area.
Regards
I would like to know if it exists a rule for estimation of volume of flushing (gpm) to seal A centrifugal pump or in my particular case, which is flushing requirement (gpm) for seal with a product at 567 F.? The pump will hand 1269 gpm of product with viscosity 3.91 cP
