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Hi all Can anyone provide me the tutorial to use HTRI software

Can anyone provide me HEI Standard for gasketed plate frame heat exchanger

Hi all Hope u all are well. Can appendix 1-10 be applied for the Self reinforced nozzle? For my case inputs are like this: vessel ID -94" nozzle dia -32" Hence this is a case of large access opening. As per client specification appendix 1-10 to be used in case of large opening. But other client...

Hi all As per client specification "since the zero crossing periods of the cyclic load are less than 25 seconds for most equipment on this FPSO, the total cycles in 25 years exceeds 30X10^6, therefore fatigue analysis is required"??? Can any one please provide me the procedure to calculate the...

Hi all while designing a tall pressure column I came across a situation to use stiffener rings. As a cost optimization approach I was trying to use the internal rings provided for placing packing trays as my internal stiffener ring. Is there anything wrong with my approach? Thanks in advance

Hi all while going through a client specification I found that for sour service requirement vessel plate shall have to be Z quality with 35% s. 1.As per nace MR0175 What is the criteria for a service to be declared as Sour? 2.What is this Z quality plate? 3.Vendor is providing me material as SA...

Dear all Can we design a flat head cylindrical tank through Pv-Elite? Because for atmospheric tank design pressure will be one bara while in Pv-Elite min pressure to be entered is 1 Barg.

Can any one please share the design calculation for rectangular tank with stiffeners . I need it urgently. Please help me to carry out the calculations

dear XL83NL Thanks for your reply but it didn't short out my problem. I understand your concern but this is client requirement. They wont accept our design if we follow some other specification or engineering . Finally u need to take deviation costing more time and money. So if u have solution...

Thanks for the replies gentle man But my concern is still the same. Actually I have to design a long horizontal pressure vessel(18000mm) where thickness due to internal pressure is coming out to be 7 mm but in case of external pressure it is coming out to be 17 mm for which I need stiffeners...

I have a doubt regarding the pipe schedule for LWN nozzles. As per BP specification for pressure vessel "it states that all connection 2" and below shall be LWN" and other clause is that all the connection below 2" shall have a minimum schedule of 160.As per my understanding all the LWN nozzles...

while calculating the thickness in case of external pressure we use graph from sec II part D for calculating the allowable stress. In any case suppose if we require to calculate the allowable pressure in case of compression how can we take the allowable stress value for carbon steel in case of...