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Hi, We are planning to buy a retrieval tool, and we got an offer from RCSL, anyone familiar with this company tool, how good is it? Thanks.

Thanks a lot georgeverghese

What kind of solution to desuperheat the steam and achieve 363 F. Regards.

Gents, a heat exchanger is to be supplied with steam at 147 psig and (363F) from higher steam source @429 psig& 456 F through pressure control valve, my question what will be practically the temperature downstream the pressure control valve, since there's no heat exchange? is it as per the steam...

Ok thanks.

Thanks BhanuMurty, Is there a reference to this or it's a rule of thumb? Regards

"I posted this thread in chemical plant design & operation forum, but I think this is the right forum for it" Dear all, What should be the distance between the corrosion inhibitor injection point and corrosion coupon/probe? is there a guideline or standard on this subject. Best regards

Dear all, What should be the distance between the corrosion inhibitor injection point and corrosion coupon/probe? is there a guideline or standard on this subject. Best regards

Thank you for your help.

Thank you Littleinch for your valuable input, you had used 3mm strainer, based on what you had choose this size? is there a selection guideline because i believe that if we select a small size this will plug rapidly, and larger one will not protect downstream equipment Regards.

Hi, What are the selection criteria for a temporary strainer to use during the commissioning? I think this has to start by defining the particle size any suggestion on this? Second thing if the equipment is fitted with a operation strainer do I need to add a temporary one? And thanks in advance.