HI ALL,
I KNOW WE HAVE BEEN DISCUSSING OUR PROBLEMS FOR LONG TIME ON THIS PLATFORM.
I AM SHASHANK SAXENA, HAVING EXP. OF 12 YRS. IN ROATATING EQUIPMENT DESIGNING FOR EPCM BUSINESS.
I HAVE NOT THINK OF ANY CERTIFICATION SO FAR IN MY CAREER. HOWEVER DURING THIS TIME OF WFH KINDA ENVIRONMENT, I...
[highlight #5C3566]HI ALL,
I KNOW WE HAVE BEEN DISCUSSING OUR PROBLEMS FOR LONG TIME ON THIS PLATFORM.
I AM SHASHANK SAXENA, HAVING EXP. OF 12 YRS. IN ROATATING EQUIPMENT DESIGNING FOR EPCM BUSINESS.
I HAVE NOT THINK OF ANY CERTIFICATION SO FAR IN MY CAREER. HOWEVER DURING THIS TIME OF WFH...
I think you might be better off asking or looking in the automobile engineers forums which look fairly busy. Or the fluid power forum which deals with hyraulics
This is a very specific use whereby you need to control pressure and generate pressure very quickly but only for short periods.
This...
Dear Mukesh
How can 53b be employed. First we want to know whether there is presence of H2s more than 200 ppm?
Why not suggest plan 2352.
A well phrased question has answers in itself!!!
For selecting a pump many parameters are required as input such as :
Flow
Head
Sp.gr.
Viscosity
NPSHa
Vapour pressure
Suction Pressure
and solid contents
In absence of above parameters no selection is possible.
Usually OH2 pump can work upto temperature of 450degC.
A well phrased question has...
System curve is graphical representation of resistance offered by the system.It
It shows that the pressure developed in the pump is high enough to overcome the resistance offered by the system.
It will start from 0 head and 0 flow if there is no static lift otherwise it will have some head...
Depends on your volume but you could just use some pipe and connections.
The HX I couldn't see enough data but looks ok on the surface. 80 bar will rule out a lot of things so check that first.
A well phrased question has answers in itself!!!
We all know that BLO is required in multistage between bearing pumps(BB2/3 and 5)
BLO is a line in which some flow is taken from discharge side(balance drum on BB5,throttle sleeve on BB2/3) and routed back to suction
This flow from final stage of pump has some undergone some heating beacuse of...
you don't know any basics.
NPSHA shall be greater by 1m than NPSHr as minimum.
The 3% head drop is method by which NPSHR is measured either by suction throttling or vacumm supression method.
Its not that it is not applicable for smaller pumps, you have again sum confusion.
NPSHA shall always be...
i have also came to know that use of inducer is actually not accurate as this will reduce NPSHr at a particular speed only and rest speed it will have high NPSHR.
Kindly thro some light on it.
A well phrased question has answers in itself!!!