CAJ | 학술논문

介绍了新配方 MIP 催化剂在中国石油呼和浩特石化公司2．8 Mt？a 催化裂化装置的工业应用情况。工业应用结果表明：使用新配方催化剂后，随着新配方催化剂在系统藏量中比例的增加，液化气产率呈下降趋势，轻油收率逐渐增加，油浆产率呈下降趋势，说明新配方催化剂的重油裂解能力强于原催化剂；生焦量逐渐降低，说明新配方催化剂的焦炭选择性优于原催化剂；同时新配方催化剂有助于多产丙烯。
개소료신배방 MIP 최화제재중국석유호화호특석화공사2．8 Mt？a 최화열화장치적공업응용정황。공업응용결과표명：사용신배방최화제후，수착신배방최화제재계통장량중비례적증가，액화기산솔정하강추세，경유수솔축점증가，유장산솔정하강추세，설명신배방최화제적중유렬해능력강우원최화제；생초량축점강저，설명신배방최화제적초탄선택성우우원최화제；동시신배방최화제유조우다산병희。
The commercial application of the new formula catalyst tailored for MIP process in the 2.8 Mt?a RFCC unit of PetroChina Huhhot Petrochemical Company was introduced. Compared with the original catalyst,the new catalyst has better heavy oil cracking ability,better coke selectivity,and high-er light oil yield. LPG and slurry yield show a downward trend as the new catalyst inventory increases. The new formulation catalyst is helpful to produce more propylene as well.