Bench-scale co-processing. Quarterly report No. 13, April 1, 1991--September 31, 1991

The objective of this contract is to extend and optimize UOP`s single-stage, slurry-catalyzed co-processing scheme. The current task is to complete a long-term operability run using a 0.05 wt-% Mo-based catalyst at approximately 460{degrees}C. The objectives of this run are to demonstrate that high-...

وصف كامل

التفاصيل البيبلوغرافية

المؤلفون الرئيسيون:	C.A. Piasecki, USDOE, Washington, DC (United States), J Gatsis
التنسيق:	Report
اللغة:	الإنجليزية
منشور في:	1992
الموضوعات:	Catalysis and Hydrodesulfurization Studies Petroleum Processing and Analysis Zeolite Catalysis and Synthesis co-processing molybdenum catalysts naphtha distillates vacuum gas oil product upgrading UOP
الوصول للمادة أونلاين:	https://www.osti.gov/servlets/purl/10138544 https://doi.org/10.2172/10138544
الوسوم:	إضافة وسم لا توجد وسوم, كن أول من يضع وسما على هذه التسجيلة!