DEAR MECH ENGINEERS
CAN I ASK YOU
whats the rank of catia between other softwares
such as solid works and solid edge and pro eng and inventor
and if its possible tell me
is catia the most effieicnt between them and is it enough for any mechanical engineer or its like other software has...
dear friends i have an application for pumping system
it consists of 3 parallel pumps having a max head of 8 bars
i have a stainless steel pipe has 8" diameter and sch 10
will this be suitable to be used under this pressure ?
boneh3ad i know the NSE can be applied to all systems on the earth but here how can we apply it ?? in cartisian co-ord. or we will use the polar co-ord. and in the redius direction or in the angel direction i think its complicated , i have studied this case and get an equation for flow using the...
i am very sorry for unclear description but the original pump in the manual was
2.2 kw has q=12m3/hr and H = 20 m
the new pump they put is 10hp q=20m3/hr and H= 40 m and while its operatin on the machine it gives 25 meter head only not 40
the sitiuation now is that i have searched for these...
accordin to my last to posts here i found this special pump which has materials designed to carry a high press but the problem now
i found a pump on the machine is bigger than the one in the manual
so shall i buy the pump from manual or as the existing pump ?
yes ur very right
u know the pump has high Hms and Hmd but normal Hm and the pump will give speed to water yes correct
i think its an ordinary pump not special pump
because these 10 bars after operating the pump it will reduced by the value of vacum created by pump impeller
do u faced...
tell me guys whats the relation between Hms and Hmd and the pump selection for example
i have Hms =10bar , Hmd =12 bars so Hm =2 bars
so the Head of the pump is only 2 bars or its said that
pump has a head of 2 bars and can withstand 12bars ???
how are u ??
i ve a problem with selecting a centrifugal pump for circulating water in a closed system this system consists of tank , pipes up to 60 meters with 2 inch dia , then these pipes deliver water to a tube contains pressurized nitrogen @ 10 bars then return back to tank and...
the majority of piping systems specially in liquids using round pipe to make the flow is smoother and reducing eddy losses also because of the hydralic diameter and also case of pipes fittings it will be easier to work on a circle than a rectang
Hm = Hst + losses
losses is defined as constant * Q^2
and u have Q = 12 L/S
AND d = 3/7 " so sub in this
o.8 * f * L * Q2/gD^5 you will find it a very small term because Q is small
so finally u can consider that H pump = H st + 3 or 4 meters
but H static should be taken into...
hello everyone i am a maintenance engineer in old factory so while we were working on an old machine yesterday we found a very strange gear box like the harmonic drives but it transmitts the motion from the motor shaft by a key to bearings those bearings transmitts motion to a elliptic shaped...
i have a system consists of a shell an tube exchanger and a centrifugal blower the blower suction is at the exit of the exchanger
i want to replace the shell and tube with a multi plates heat exchanger
whats my conditions for this process
max press 16 bar
mechanical engineer :D or :S
well i am a mechanical engineer in a factory my job is maintenance of different machines so i am dealing with many mechanical systems
also dealing with air compressors pneumatic circuits , hydraulic circuits and air chillers i deal with many things may be...
hello guyz i have some questions about shell and tube exchangers
1- whats the difference between shell and tube exchanger over the plate exchanger ??
2- whats the data required for selecting heat exchanger ??
3- if i will replace the shell and tube with a plate exchanger whats the...