content. This modified feedstock has an acceptable performance under catalytic cracking producing significant yields, compared to commercial FCC catalysts, of gasoline and low catalyst coking.
98/01107 Stabilization by mild catalytic hydrotreating of bio-oils produced by flash pyrolysis: Maggi, R. et al. Biomass Energy Environ., Proc. Eur. Bioenergy Conf., 9th, 1996, 1, 327–332. Edited by Chartier, P., Elsevier, Oxford, UK
- Publisher
- Elsevier Science
- Year
- 1998
- Weight
- 379 KB
- Volume
- 39
- Category
- Article
- ISSN
- 0140-6701
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✦ Synopsis
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
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