I am working on a multitube exchangers which will be installed on the FPSO. Vendor has informed that tube side nozzles are not classical nozzles and will not provide nozzle load calculation because of its construction. That is there is a weld neck flange connected to the body flange where the body flange in turn is welded to a straight pipe. However, vendor has performed flange leak verification by converting the allowable loads into equivalent pressure(Enquiry case 5500/123). But client has rejected vendor's clarification stating that just flange design check is not sufficient and further said Vendor has to assess the loads(forces and moments) imposed on the nozzles.
Because of this the tube side design has to be completely modified. That is a flange will be now welded to a cone instead of directly welded to the body flange, which has big impact on us.
Vendor has supplied the exchangers for many clients and submitted equivalent pressure calculation for tube side nozzles instead of nozzle load calculation and were accepted. This is the first time client is not accepting to this kind of verification.
Can anyone who has experience in reviewing multitube exchangers suggest if the vendor clarification is acceptable? Please suggest.
Thanks.