Recent content by mimentzos

Ι think that all your comments i have already mentioned with red line.

2)see the attachmenthttp://files.engineering.com/getfile.aspx?folder=68f70640-242c-4a08-b158-5d514eebbb95&file=Start_pump.jpg

According to your data the operation point is at the midle of the curve where the NPSHr is almost flat. The system curve is OK ?

and one more http://files.engineering.com/getfile.aspx?folder=7c9a6bea-41de-4414-9b79-90f11b458306&file=NPSH_2.jpg

graph... with the answers From Europump guide " NPSH FOR ROTODYNAMIC PUMPS"http://files.engineering.com/getfile.aspx?folder=abd3b836-dd07-4da6-8785-81f1947d3043&file=NPSH_1.jpg

Sorry for the above wrong reply The correct Thread is "Gear Pump" of a1981

Very useful http://www.michael-smith-engineers.co.uk/pdfs/engineeringdata/Why_Use_Relief_Valves%20with%20Liquiflo%20gear%20pumps.pdf

From API Standard 610 / ISO 13709 page 9, you can see the difference (see attachment file) I am not sure concerning the reply of nfinithttp://files.engineering.com/getfile.aspx?folder=d8fa7311-80cc-4280-8c77-e053f9ab4b52&file=BB4_-_BB5.jpg

Pennpiper first I want to thank you for your reply. Secondly I want to ask you if all this procedure included officialy in any Standard code like ASME, ISO etc. Thanks in advance

Pls can someone to inform me if there are some standards concerning the drawing of an isometric piping? The data that should have(Pressure, Temperature etc) and all the necessary related informations. Thanks in advance