𝔖 Bobbio Scriptorium
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98/01105 The SELOP-processes: BASF-technology for hydrogenations in the steam cracker downstream treatment: Mueller, H.-J. et al. Pet. Coal, 1995, 37, (4), 34–44


Publisher
Elsevier Science
Year
1998
Weight
204 KB
Volume
39
Category
Article
ISSN
0140-6701

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✦ Synopsis


02 Liquid fuels (transport refining, quality, storage) ASPEN process simulation models were developed. Based on a typical PADD II refinery, a linear programming model was developed to assess the values of the oroduced F-T oroducts. The results then were used in a discounted caih flow spreadiheet model to examine the effect of key process variables on the overall F-T economics. Cracking of F-T waxes produced products rich in C-r-reactive olefins which are especially suitable for production of ethers for gasoline blending. The fluid catalytic cracking process produces -34% more gasoline blending components than mild hydrocracking, which is produced at the expense of distillate production.

96/01094

Emulsified fuel and one methodffor preparing same