کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
146165 456363 2015 10 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Feedstock and catalyst effects in fluid catalytic cracking – Comparative yields in bench scale and pilot plant reactors
ترجمه فارسی عنوان
اثر مواد اولیه و کاتالیزور در ترک خوردگی کاتالیزوری مایع تطبیق مقادیر در مقیاس نیمکت و راکتورهای خلبان کارخانه
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


• FCC reaction performance between a riser and a confined fluid bed reactor (CFBR).
• Performance of the CFBR at constant catalyst residence time and constant space time.
• CFBR correctly ranks feeds and catalysts but exaggerates relative differences.
• CFBR working at constant catalyst residence time simulates better the riser operation.
• Riser is the most reliable reactor to rank catalysts for commercial projections.

Laboratory testing of fluid catalytic cracking (FCC) for feeds and catalysts in a confined fluid bed reactor (CFBR) is widely applied in industry as a standard evaluation tool. In this paper, comparative yields are presented from a circulating riser reactor (CRR) in an FCC pilot plant and in a standard CFBR unit. It is shown that, although a good agreement is obtained for comparative ranking of feedstock quality and catalyst activity, there are significant differences on the absolute yields obtained at constant conversion. These results are explained by differences in reactor operating parameters and their effect on catalyst performance and product selectivity.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Journal - Volume 278, 15 October 2015, Pages 140–149
نویسندگان
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