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thread124-478941 Feel free to check this content on the this magazine. Hydrocarbon processing. "Preferential baffle reboiler"

In the floating head shell &tube exchanger. Floating chember will be pressurized with shell fluid? How? Is there gap b/w tubesheet and she'll?

Thermoshipon reboiler return line should have one one bend or more than that is acceptable? How many bend(elbow) and how much length of bend is acceptable?

What is size of demister pad in compressor suction KO drum. And which type of demister to be used?

Can anyone prove the mollier chart of binary mixture (Ethylene and methane) ? Kindly help me

Why distillation column have hole in bottom baffle . What is use of this

Why these two design have difference? What is the reason for that? Do not think twice

1. At the time of turbine trip why extraction valve closed immediately? if it is open what happen 2.At the time of turbine warm up(steam taken from extraction side to HP casing ) why balance line in turbine should be closed? 3.why lube oil pressure should be 2.5 bara while it return pressure is...

Deep and shallow temperature of steam turbine provided but 1.which one will be higher deep or shallow? 2.what is purpose of that ? Do not think twice

HOW i can improve my running compressor performance and efficiency and reduce power? centrifugal compressor do not think twice

Inlet gas temperature higher than normal . what are effects on compressor an power consumption?

thread124-280666 first open the ASV of high then ip then low pressure casing. i think that would be better because if you open first LP casing ASV then NEXT casing GO under surge if ASV will not fast responding

If inlet gas of compressor increase than design What would be effect on operating point and power of compressor? If we remove the insulation of 500m long line of compressor inlet gas it would be helpful?

thread124-457827 i have read all your conversation i just want to know a clarification that sir 5S ASV tapping from downstream of cooler so any time did you get sluggish flow through due to liquid accumulation during startup if discharge line valve after NRV is closed? there is chance that...

if Compressor inlet temp increased more than design effect of surging power and performance?

thread124-459944 MW Of process gas decreased then operating point of compressor going towards surge if speed is not changing and vice versa. right???

thread137-374850 at steady state just trip the compressor then ASV will fully open and same time see the trend of flow and P,T and Speed .you get whether compressor going into surge during coast down then it required HGBV. ty