martino6000
Chemical
- Apr 29, 2005
- 8
HALLOW EVERYONE!
I AM CONSTRUCTING A PIPELINE FOR COOLING TOWER .I NEEDED PUMP FOR PUMPING COOLLED WATER BACK TO HEAT EXCHANGER.BASED ON MY PIPELINE DESIGN AND VOLUME FLOW RATE;I HAVE CALCULATED OVERHEAD PRESSURE DROP.I HAVE BEEN SEACHING FOR A SUITABLE PUMP THAT COULD MACTH MY CALCULATED VALUES, I DID GET SOME BUT THEY ARE ALL SPECIFIED TO BE IN USE FOR OTHER PURPOSES e.g IN CHEMICAL INDUSTRIES:IS IT ADVISABLE TO USE THESE PUMPS FOR MY COOLING WATER SYSTEM:HERE ARE MY VALUES.
IS IT BETTER TO USE TWO PUMPS IN PARALLEL CONECTION SO THAT I CAN EASLY GET BETTER PUMP/BEST OPERATING POINT FOR MY SYSTEM.YOUR HELP WILL BE HIGHLY APPRECIATED.
Volume flow:900 cu meter/hr
pump head:98m
Static head:27m
kinetic viscosity:0,68cst
temperature:40°C
PumP power:299KW
Pumpen type:Coolling water pump
I AM CONSTRUCTING A PIPELINE FOR COOLING TOWER .I NEEDED PUMP FOR PUMPING COOLLED WATER BACK TO HEAT EXCHANGER.BASED ON MY PIPELINE DESIGN AND VOLUME FLOW RATE;I HAVE CALCULATED OVERHEAD PRESSURE DROP.I HAVE BEEN SEACHING FOR A SUITABLE PUMP THAT COULD MACTH MY CALCULATED VALUES, I DID GET SOME BUT THEY ARE ALL SPECIFIED TO BE IN USE FOR OTHER PURPOSES e.g IN CHEMICAL INDUSTRIES:IS IT ADVISABLE TO USE THESE PUMPS FOR MY COOLING WATER SYSTEM:HERE ARE MY VALUES.
IS IT BETTER TO USE TWO PUMPS IN PARALLEL CONECTION SO THAT I CAN EASLY GET BETTER PUMP/BEST OPERATING POINT FOR MY SYSTEM.YOUR HELP WILL BE HIGHLY APPRECIATED.
Volume flow:900 cu meter/hr
pump head:98m
Static head:27m
kinetic viscosity:0,68cst
temperature:40°C
PumP power:299KW
Pumpen type:Coolling water pump