plat heat ex is hard to clean chemicaly and it is not easy to clean it mechanicaly because of it's reassembly also amine system is have many contaminate because it contact with gas which always not clean
dear gus
why in LNG plants and other plant which use Amin solution to remove CO2 from gas, alwas the heat exchanger betwwen rich and lean amin is plat heat exchanger ?
we have almost the same incinerator D/S amine unit i think you dont need that demister. to prevent liquid carry over you can put HHL trip to trip incinerator
dear Atlek
you need to know if the amount of energy in the steam which heating water/glycol mixture will raise mixture Temp to its evapouration temp or not, because you need high energy (latent heat+sensible haet) to evapourat the mixture, if it is yes then you need to calculate the amount of...
dear gents
i would like to konw what is the range of absorber turndown ratio, it is trayed one 20 tray withe normal feed gas 700Knm3/h and amin circulation is 90 M3/h, our plant have proplem in startup with 125 Knm3/h always we have CO2 off-spec ( grater than 100 ppm ) what can we do ? lower or...
dear gents
i would like to konw what is the range of absorber turndown ratio, it is trayed one 20 tray withe normal feed gas 700Knm3/h and amin circulation is 90 M3/h, our plant have proplem in startup with 125 Knm3/h always we have CO2 off-spec ( grater than 100 ppm ) what can we do ? lower or...
dear gents
i would like to know what is the range of turndown ratio for absorber, because normal feed gas rate for liquefied gas plant is about 700KNm/h3 with amine circualation about 90 M3/h but on start up we have always off-spec co2 in the gas (grater than 100 ppm )that happens with 125...
dear gents
i would like to know what is the range of turndown ratio for absorber, because normal feed gas rate for a liquefied gas plant is about 700KNm/h3 with amine circualation about 90 M3/h but on start up we have always off-spec co2 in the gas (grater than 100 ppm )that happens with 125...
