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FRONT END CD HYDRO- RAW GAS HYDROGENATION ACHIEVED

机译:达到前端CD水力加氢氢化

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Front End CDHydro applies catalytic distillation hydrogenation to the ethylene flowsheet to successfully accomplish raw, cracked gas hydrogenation. The Front End CDHydrosystem features a depentanizer tower with a hydrogenation catalyst zone in the rectifying zone of the tower to convert the C_2 to C_5 acetylenes and dienes to olefins.By combining the numerous fixed bed reactors into a single integrated step, investment costs are lower and plant reliability is improved. In addition, 30% to 35% of the pyrolysis hydrogen is removed by chemical reaction rather than by cryogenic separation. This reduces compressor power requirements by 10%. Furthermore, by using the butenes produced by the Front End CDHydro system as feed to a metathesis unit, the process chemistry downstream of the cracking heaters is further changed by producing up to one third of the propylene by energy-neutral metathesis rather than by energy-intensive thermal cracking.
机译:前端CDHYDRO将催化蒸馏氢化施加到乙烯流动切片上,以成功完成原料裂纹的气体氢化。前端Cdhydroosystem具有在塔柱的整流区中具有氢化催化剂区的浮雕催化剂区,以将C_2转化为C_5乙炔和二烯。通过将许多固定床反应器组合成单一综合步骤,投资成本较低植物可靠性得到改善。此外,通过化学反应而不是冷冻分离除去30%至35%的热解氢。这将压缩机电源要求降低10%。此外,通过使用由前端Cdhydro系统产生的丁烯作为进料到复分解单元,通过通过能量中性复分解而不是通过能量产生高达三分之一的丙烯,进一步改变裂化加热器下游的过程化学。强烈的热裂解。

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