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you need to review the numbers that the simulator is providing you. Besides plugging numbers, you need to review them and see if they are feasible or not Gabriel Castaneda, P.E. http://www.gabcheminc.com

Hey, could you provide more information about your process? Regards Gabriel Castaneda http://www.gabcheminc.com Gabriel Castaneda, P.E. http://www.gabcheminc.com

Hi Ekaphol, Do you have plant data? Could you provide more information, please? Gabriel Castaneda, PE http://www.gabcheminc.com Gabriel Castaneda, P.E. http://www.gabcheminc.com

Hey, what are the components in the distillation? could you describe the system more? could you send me your simulation? Regards Gabriel Castaneda, PE http://www.gabcheminc.com Gabriel Castaneda, P.E. http://www.gabcheminc.com

Hey Mohamed, which components are present in the distillation? Do you have any more information? Thanks Gabriel Castaneda, PE http://www.gabcheminc.com Gabriel Castaneda, P.E. http://www.gabcheminc.com

Hey David, I could review your design and give you some feedback Gabriel Castaneda, PE http://www.gabcheminc.com Gabriel Castaneda, P.E. http://www.gabcheminc.com

get a flow orifice meter...or if there's no pressure when there's no gas, then just a pressure meter Gabriel Castaneda, P.E. http://www.gabcheminc.com

A diagram would be helpful to understand your problem Gabriel Castaneda, P.E. http://www.gabcheminc.com

an important part is to estimate the amount of gas that will be pumped out. For instance there may be decomposition which will bring the gas flowrate up. Gabriel Castaneda, P.E. http://www.gabcheminc.com

please contact me and I'll see how I can help you. Gabriel Castaneda, P.E. http://www.gabcheminc.com

consider the residence time and flowrates :) Gabriel Castaneda, P.E. http://www.gabcheminc.com

change the refractory ;) Gabriel Castaneda, P.E. http://www.gabcheminc.com

the backpressure would be the friction at a certain flowrate... calulate from there... Gabriel Castaneda, P.E. http://www.gabcheminc.com

please send me your drawings to take a look at them. Gabriel Castaneda, P.E. http://www.gabcheminc.com

if you need to improve your pumping system and your Merox, you can always make a hydraulics study. I could help you on that. Gabriel Castaneda, P.E. http://www.gabcheminc.com

The bundle should be submerged entirely to use all of the tubes for heat transfer. Gabriel Castaneda, P.E. http://www.gabcheminc.com

If you want to do preliminary explosion modeling you can use the DNV PHAST software, I can help you on that. If you want to see a more detailed information such as how barriers affect gas expansions, you would need software like FLACS, and again, I understand GEXCON is quite good on this kind of...

you would need to supply a P&ID and equipment information to answer that question Gabriel Castaneda, P.E. http://www.gabcheminc.com

Talk to vendors, it may help Alpema has a good standard. Gabriel Castaneda, P.E. http://www.gabcheminc.com

Hi, you can have three stage compressors without one intercooler, depending on the compressor manufacturer and operating conditions. I'd advise to have a second full compressor, you can also go for aeroderivative compressors, which are relatively small in size. Gabriel Castaneda, P.E...