Hi, What is (are) the book(s) most complete in subjects about fluids pumping, hydraulic calculations, with resolute problems and to solve? I want to review and learn about these subjects. Recommend me a web page. Thanks
Hi. If it is used flangeness wafer valves, i.e. butterfly or check, must be installed packing? Is it necessary? If it is true, what type of packing?
Thanks in advance.
In the wide range of PLC's, what are the most echonomical, applicables and singles trade marks for application in control of HVAC system.
Thanks in advance.
Hi. Anybody know what is the best shape of blade for a centrifugal fan that convey solids minuscle particles,less than 200 microns, specificly PVC resin. What shape has the best performance? In what web page I get information about it?
Thanks.
Hi. Anybody know a web page for information of bins and hoopers calculations, fundamentals, spreadsheet, technical articles? I'm new in these themes and need to calculate and design it. Its very important and urgent. Thanks.
ciralca
Hi. Anybody know a web page for information of bins and hoopers calculations, fundamentals, spreadsheet, technical articles? I'm new in these themes and need to calculate and design it. Its very important and urgent. Thanks.
Hi. Anybody know a web page for information of bins and hoopers calculations, fundamentals, spreadsheet, technical articles? I'm new in these themes and need to calculate and design it. Its very important and urgent. Thanks.
ciralca
Please, somebody know web pages about fundamentals, theory, design about heat transfer and Flow of hot gases in ducts and stacks. I am studying a practical problem about those areas. Thanks.
ciralca
TrevorP
Fluid B batche is 107000 bbl; Fluid A batche is 125000 bbl; the capacity of pipeline is 117500 bbl. Fluid B is pumped by screw pumps and fluid A by centrifugal pumps.
Could somebody help me about the hydraulic analisis for transportation in a pipeline of two liquids with differente viscosity. That liquids are transported in batches separated by pig. What viscosity must I consider? Pipeline is 200 miles lenght.
Its known that in a positive displacement pump suction line must be take in account the acceleration head (ha)and substract it for the NPSHA. But, what is the value of NPSHA for comparison with NPSHR.
NPSHA = Pa+Hs-Pv-hf-ha?
or NPSHA = Pa+Hs-Pv-hf?
Why?
Thanks
Ciro