Post by Inprocess Technology & Consulting Group, S.L.U

8,100 followers

๐—ข๐—ฝ๐˜๐—ถ๐—บ๐—ถ๐˜‡๐—ฒ๐—ฑ ๐—ฅ๐—ฒ๐—ณ๐—ถ๐—ป๐—ฒ๐—ฟ๐˜† ๐—™๐—น๐—ฎ๐—ฟ๐—ฒ ๐—ฆ๐˜†๐˜€๐˜๐—ฒ๐—บ ๐—ฅ๐—ฒ๐˜ƒ๐—ฎ๐—น๐—ถ๐—ฑ๐—ฎ๐˜๐—ถ๐—ผ๐—ป ๐—ฎ๐—ป๐—ฑ ๐—™๐—น๐—ฎ๐—ฟ๐—ฒ ๐—Ÿ๐—ผ๐—ฎ๐—ฑ ๐—”๐˜€๐˜€๐—ฒ๐˜€๐˜€๐—บ๐—ฒ๐—ป๐˜๐˜€ ๐Ÿ“Š Plant expansion projects, unit revamps or debottlenecking studies may lead to a re-evaluation of the capacity of an asset existing flare system. Usually, after a re-evaluation study, an increase in flare load is determined. If the capacity of the asset flare system is close to its limit, the only solution is a capital project to increase the original capacity. Nevertheless, ๐—ถ๐˜€ ๐˜๐—ต๐—ฒ๐—ฟ๐—ฒ ๐—ฎ๐—ป๐˜† ๐—ฝ๐—ผ๐˜€๐˜€๐—ถ๐—ฏ๐—ถ๐—น๐—ถ๐˜๐˜† ๐—ผ๐—ณ ๐—ฟ๐—ฒ๐—ฑ๐˜‚๐—ฐ๐—ถ๐—ป๐—ด ๐—–๐—”๐—ฃ๐—˜๐—ซ ๐—ฏ๐˜† ๐˜‚๐˜€๐—ถ๐—ป๐—ด ๐—ฎ ๐—บ๐—ผ๐—ฟ๐—ฒ ๐—ฎ๐—ฐ๐—ฐ๐˜‚๐—ฟ๐—ฎ๐˜๐—ฒ ๐˜„๐—ฎ๐˜† ๐—ผ๐—ณ ๐—ฒ๐˜€๐˜๐—ถ๐—บ๐—ฎ๐˜๐—ถ๐—ป๐—ด ๐˜๐—ต๐—ฒ ๐—ณ๐—น๐—ฎ๐—ฟ๐—ฒ ๐˜€๐˜†๐˜€๐˜๐—ฒ๐—บโ€™๐˜€ ๐—ฏ๐—ฒ๐—ต๐—ฎ๐˜ƒ๐—ถ๐—ผ๐—ฟ? It is a well-known fact that most existing flare systems were originally designed taking into account over-conservative assumptions which led to overly-sized relief and flare system designs. ๐—”๐—ฃ๐—œ ๐Ÿฑ๐Ÿฎ๐Ÿญ ๐—ป๐—ผ๐—ฟ๐—บ ๐—ฟ๐—ฒ๐—ฐ๐—ผ๐—บ๐—บ๐—ฒ๐—ป๐—ฑ๐˜€ ๐——๐˜†๐—ป๐—ฎ๐—บ๐—ถ๐—ฐ ๐—ฆ๐—ถ๐—บ๐˜‚๐—น๐—ฎ๐˜๐—ถ๐—ผ๐—ป as a valid alternative method for calculating transient pressure increases and determining relief loads in a more accurate way during unexpected contingencies during plant operation. ๐—œ๐—ป๐—ฝ๐—ฟ๐—ผ๐—ฐ๐—ฒ๐˜€๐˜€ ๐—ต๐—ฎ๐˜€ ๐—ฎ๐—ป ๐—ฒ๐˜…๐—ฐ๐—ฒ๐—น๐—น๐—ฒ๐—ป๐˜ ๐˜๐—ฟ๐—ฎ๐—ฐ๐—ธ ๐—ฟ๐—ฒ๐—ฐ๐—ผ๐—ฟ๐—ฑ ๐—ผ๐—ณ ๐—ฒ๐˜…๐—ฝ๐—ฒ๐—ฟ๐—ถ๐—ฒ๐—ป๐—ฐ๐—ฒ ๐—ถ๐—ป ๐—ฎ๐—ฝ๐—ฝ๐—น๐˜†๐—ถ๐—ป๐—ด ๐—ฑ๐˜†๐—ป๐—ฎ๐—บ๐—ถ๐—ฐ ๐˜€๐—ถ๐—บ๐˜‚๐—น๐—ฎ๐˜๐—ถ๐—ผ๐—ป ๐˜๐—ผ ๐˜๐—ต๐—ฒ ๐—ฎ๐—ป๐—ฎ๐—น๐˜†๐˜€๐—ถ๐˜€ ๐—ผ๐—ณ ๐—ณ๐—น๐—ฎ๐—ฟ๐—ฒ ๐—ป๐—ฒ๐˜๐˜„๐—ผ๐—ฟ๐—ธ๐˜€, ๐—ผ๐—ฝ๐˜๐—ถ๐—บ๐—ถ๐˜‡๐—ถ๐—ป๐—ด ๐—ฝ๐—ฟ๐—ผ๐—ท๐—ฒ๐—ฐ๐˜ ๐—ฐ๐—ผ๐˜€๐˜๐˜€ ๐—ฎ๐—ป๐—ฑ ๐˜€๐—ฐ๐—ต๐—ฒ๐—ฑ๐˜‚๐—น๐—ฒ๐˜€. โœ… Our experience in applying dynamic simulation to the analysis of existing flare networks helps operating companies to: โ€ข Reduce ๐—–๐—”๐—ฃ๐—˜๐—ซย requirements in flare system revamps, expansion, and debottlenecking projects. โ€ข Minimize ๐—ผ๐—ณ๐—ณ-๐—ฝ๐—ฟ๐—ผ๐—ฑ๐˜‚๐—ฐ๐˜๐—ถ๐—ผ๐—ป ๐˜๐—ถ๐—บ๐—ฒ due to flare system adequation. โ€ข Increase intrinsic ๐˜‚๐—ป๐—ถ๐˜ ๐˜€๐—ฎ๐—ณ๐—ฒ๐˜๐˜†. โ€ข Acquire ๐—ธ๐—ป๐—ผ๐˜„-๐—ต๐—ผ๐˜„ from Inprocessโ€™ project team (more than 30 successful flare projects). โ€ข Standardize to ๐—”๐—ฃ๐—œ ๐—ป๐—ผ๐—ฟ๐—บ๐˜€ while saving time and capital. ๐Ÿ”ธ Download our short ๐—•๐—ฟ๐—ผ๐—ฐ๐—ต๐˜‚๐—ฟ๐—ฒ ๐—ฎ๐—ฏ๐—ผ๐˜‚๐˜ ๐——๐˜†๐—ป๐—ฎ๐—บ๐—ถ๐—ฐ ๐—™๐—น๐—ฎ๐—ฟ๐—ฒ ๐—Ÿ๐—ผ๐—ฎ๐—ฑ ๐—”๐—ป๐—ฎ๐—น๐˜†๐˜€๐—ถ๐˜€ from here: https://lnkd.in/e2dysrdp ๐Ÿ”ธ Discover more ๐˜€๐—ฒ๐—ฟ๐˜ƒ๐—ถ๐—ฐ๐—ฒ ๐—ผ๐—ฝ๐˜๐—ถ๐—ผ๐—ป๐˜€ ๐˜๐—ต๐—ฎ๐˜ ๐—ต๐—ฎ๐˜ƒ๐—ฒ ๐—ต๐—ฒ๐—น๐—ฝ๐—ฒ๐—ฑ ๐—ฟ๐—ฒ๐—ณ๐—ถ๐—ป๐—ฒ๐—ฟ๐˜€ ๐˜๐—ผ ๐—ถ๐—บ๐—ฝ๐—ฟ๐—ผ๐˜ƒ๐—ฒ ๐˜๐—ต๐—ฒ ๐—ผ๐—ฝ๐—ฒ๐—ฟ๐—ฎ๐—ฏ๐—ถ๐—น๐—ถ๐˜๐˜† ๐—ผ๐—ณ ๐˜๐—ต๐—ฒ๐—ถ๐—ฟ ๐—ฎ๐˜€๐˜€๐—ฒ๐˜๐˜€: https://lnkd.in/ed4aC3PN #Inprocess #Refining #FlareSystems #DynamicSimulation #ProcessSimulation #EnergyTransition #ProcessEngineering #Decarbonization

Post content