lcms
Chemical
- Dec 7, 2003
- 44
Dear Sirs,
I am working in a project where we will have to transfer a liquified gas (Butadiene, 3 kgf/cm2g; 30C) from a vessel bellow the sucction pump to charge a reactor that requires at least 7 kgf/cm2g at pump discharge.
I am considering to use a rotary lob pump I have available at my WWTP (MBR permeate) that work well in a self prime mode, but I am concerned since I have never heard about this kind of pump in LPG transfer.
Could you please explain me why?
Thanks.
I am working in a project where we will have to transfer a liquified gas (Butadiene, 3 kgf/cm2g; 30C) from a vessel bellow the sucction pump to charge a reactor that requires at least 7 kgf/cm2g at pump discharge.
I am considering to use a rotary lob pump I have available at my WWTP (MBR permeate) that work well in a self prime mode, but I am concerned since I have never heard about this kind of pump in LPG transfer.
Could you please explain me why?
Thanks.