Dear members,
Has anyone heard of or use the criteria RhoV2 (fluid density multiplied by fluid velocity squared- has SI unit of kg/m2s ) for line sizing of gas or two/multiphase lines. I understand the criteria is to limit vibration in pipes. Does anyone know any internationally recognised code...
hi fellow engineers,
I know this issue has been around for many years and I am aware of various pros and cons but I would like to hear opinions and reasons from engineers why they have chosen to design and install direct seawater cooling system in lieu of indirect system (use sw to cool fresh...
hi fellow engineers,
I know this issue has been around for many years and I am aware of various pros and cons but I would like to hear opinions and reasons from engineers why they have chosen to design and install direct seawater cooling system in lieu of indirect system (use sw to cool fresh...
hi folks,
My question is directed to people who have operating experience or feed back on the use of seawater cooling in the process exchangers (compressor or oil coolers) used on BP Andrew platform, i.e. what problems,if any, have been encountered, e,g corrosion, fouling etc
many thanks
ce
hi all,
I am looking for a flow meter to measure gas flow rate in flare stack. The meter must be largely non-intrusive (being in flare pipe to avoid blockage)and has good accuracy (within 2%) and good turndown (100:1). I was told that ultrasonic meters are not reliable when flow velocity exceeds...
hi folks,
I am looking for a pilot operated relief valve (set pressure @ 214 barg to flare b.p 10 barg max)that will pass full flow of gas (PSV full opened)with absolutely no overpressure, i.e. at full relief the pressure upstream PSV is 214 barg only. I understand that is one attribute of pilot...
