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Hi Dan, The key to find your answer is follow Appendix O and determine Sbsel following Joint Component Approach O-4.2. Integrity of a flange joint is dependent on integrity of all the assembly components - the flange, gasket and bolt. Para O-4.2 is a stress check for all the components both at...

PED 2014-68-EU is for stationary pressure equipment. PED had recognized and accepted ASME B31.3 - process piping code indirectly through two supporting documents: ISO 15649: Petroleum and Natural Gas Industries - Piping. EEMUA Publication No. 202: Guide to the use of ISO 15649. These...

The Code will not tell you if you can tie-in to a flanged connection or not. Many Owners will have their own specification not allowing flanged connections to a flare header - the reason being - to avoid ingress of air/oxygen to form a combustible mixture with the vented/flared gas. Of course...

Dan, The key to keeping the appropriate bolt preload at both ambient (installation) and operating condition (500C) is to determine the bolt stress (Sbsel) is as per Appendix-O. O-4.2 will take you through all the checks at both ambient and operating conditions for the flange assembly - bolt...

You should revisit your design. The top part of 310S you said will be operating at creep (650-675C) and 100,000 hrs. (say 12 operating years ). One of the things designers overlook is the design life when taking stress values from BPVC Sec II Part D. For vessel that predominantly operates in the...

That's the direction I would go in absence of any dimensions not found in a standard (example ASME B16.47) acceptable to the construction Code - qualify by Sec VIII Div1 Appendix 2.

You should treat B31.8 831.4.2(c) and 831.4.2(j)(3) separately for understanding. Whereas 831.4.2(c) talks about a complete encirclement reinforcement type that we encounter in daily life, 831.4.2(j)(3) talks about hot tapping/plugging fittings, where the reinforcing sleeve is pressurised and is...

I will be a bit skeptical on the 1200C. What is that process that uses 1200C? Furnace heater tubes goes upto 900C and the high temperature nuclear reactor cores made of graphite materials. Typically Ni-Fe-Cr alloys can see the max temperature. If you are talking about Pyrolysis process, users...

Sorry, I am not used to EN standard. I am an ASME guy. I can’t therefore validate your strength numbers. As for creep, it is when the material time-dependent properties kicks-in. Examples are heater tubes where the tubes has to be designed for both elastic and rupture (creep). If you haven’t...

Why do you even have to do the time-dependent evaluation? CS @204 C will never cross to the creep regime. Temperature limit to define the creep range for EN 10217-2 Gr P235GH material will be 343C-371C depending on the reported tensile strength.

There is no standard available. You have to make one for your company or the project. Process vent should be a proper vent assembly with valves that will be used for the life cycle of the plant during start up, shutdown, maintenance etc. It should be based on the piping class. Different vent...

If I am reading/interpreting B16.5 P8.2.2 correctly, CL150 reads 20 bar (290 PSI) at 38C X1.5 =30 bar (435PSI) max flange pressure. Or would it be 21 bar? The test pressure would be 450 psig rounding off to next higher 25 psig. It's the max test pressure. However, note that you won't be only...

You don't have to break your head. Instead you need to read ASME B16.5 Para 8. Flange test pressure is 1.5x the pressure rating (MAWP) at 38C given in Tables 2-1.1 or Table II-2-1.1 rounded off to next higher 1 bar or 25 psi.

What's your pump make and model?

You are right. For t<D/6, the Lame's equation for thickness calculation becomes overly conservative. The stress across the wall thickness is no more assumed as membrane (equal) and varies across the wall. That's where the base code and high pressure fluid system Chapter IX kicks in. If you...

Grid option is preferable for both because if the PTR produces COV >10%, grid is required anyway.

Why do you say the nozzle has to be from a pipe? As long as it meets the acceptable material by the Code, it can be fabricated by other methods too.

How about the possibility of a clamp over the coupling, injecting with sealant, with tapping to a surface vault to monitor the joint pressure and inject with fresh sealant when required.

Looks like 110 psi discharge pressure meets your system requirement. Look for a pump with TDH 114 psi (as Katmar had said) and 200 GPM near to the Best Efficiency Point (BEP) on the pump Characteristics curve (H-Q Curve). if you are little skeptical, you can increase to say 120 psi (you can...

The Safety valve is set at 290 Barg which is equal to the MAWP or Design Pressure of the Pump. Pump manufacturer has set it based on the design of the pump. For the piping, you need to first determine what should be the design pressure. This will be based on the MOP you need. If the PRV had...