guerky
Chemical
- Feb 10, 2015
- 33
I'm designing a new pumping system for a relatively high melting point (72°C) and viscosity (6.600 cP) through a 90m, 2 in SS316L line, with ambient temperatures that can get to -5° on some nights in the winter.
The fluid can be heated up to 100°C without any degradation. I intend to heat the fluid up to 93°C, to allow a higher temperature in the steam traces (3 kgf/cm² saturated steam) without risking an overheating in the line during the transfer.
This kind of fluid was tradiotionally handled in my company through a "tank-pump" (the product is melted in a hot bath, sucked with vacuum through a short hose to a pressure vessel and pumped through nitrogen pressure (3 kgf/cm², tipically)), in lines insulated and heated with spiral steam tracing.
I know from the operating personal that this kind of operation became a sort of paradigm due to failed experiences with pumps in the past in similar aplications. Despite being an inexperienced Process Engineer i refuse to just acept that a jacketed internal gear pump + a well insulated line (even with the simple spiral steam traces) couldnt handle it if some precautions to avoid fluid stagnation in the lines between batches are taken.
I've done my insulation calculations. There isnt any aparent problem.
The internal gear pump seems like an apropriated choice for pumping this viscous fluid, as high flow rates are not crucial.
So, i ask you for some experienced advices and, if possible, tips about some cost effective line heating and pumping technology.
Best Regards
In God we trust. All the others must bring data.
The fluid can be heated up to 100°C without any degradation. I intend to heat the fluid up to 93°C, to allow a higher temperature in the steam traces (3 kgf/cm² saturated steam) without risking an overheating in the line during the transfer.
This kind of fluid was tradiotionally handled in my company through a "tank-pump" (the product is melted in a hot bath, sucked with vacuum through a short hose to a pressure vessel and pumped through nitrogen pressure (3 kgf/cm², tipically)), in lines insulated and heated with spiral steam tracing.
I know from the operating personal that this kind of operation became a sort of paradigm due to failed experiences with pumps in the past in similar aplications. Despite being an inexperienced Process Engineer i refuse to just acept that a jacketed internal gear pump + a well insulated line (even with the simple spiral steam traces) couldnt handle it if some precautions to avoid fluid stagnation in the lines between batches are taken.
I've done my insulation calculations. There isnt any aparent problem.
The internal gear pump seems like an apropriated choice for pumping this viscous fluid, as high flow rates are not crucial.
So, i ask you for some experienced advices and, if possible, tips about some cost effective line heating and pumping technology.
Best Regards
In God we trust. All the others must bring data.