Recent content by AnhsirkT

https://www.hydrocarbonprocessing.com/magazine/2022/april-2022/heat-transfer/preferential-baffle-reboiler-part-1

Due to acid gas in the amine. MOC of the exchange is not suitable. Kindly check the compatibility.

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

Tema S type which you shown

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?

Thanks

What we use normal for elbow or one miter bend

Yes at this stage I have 4 bend in return line How we can reduce pressure drop

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?

Thank you For caustic service? Size in micron? Sock absorber?

Ok But it is thermoshipon reboiler . How we can fix the flow rate ? Due to pre flashing reboiler feed density may increase and chances of heavy accumulation in the reboiler and problem in thermo shiponing

Yes agree with your point t will increase the reboiler inlet temperature that's why effeciency decrease (we cannot assume reboiler is A therotical plate

Thank you georgeverghese But we are mixting cold liquid with hot liquid (reboiler inlet liquid is cold and product side liquid is hot) so it will not reduce mixing.i think it will promote

Liquid maintain above the hole

Yes downcomer is correct But if we mix both liquid then what is the use of baffle