ISSN:
1573-8310
Source:
Springer Online Journal Archives 1860-2000
Topics:
Chemistry and Pharmacology
,
Process Engineering, Biotechnology, Nutrition Technology
Notes:
Conclusions Technical and economic calculations have shown: 1) The manufacturing cost of GTF from coking distillates is lower than from diesel fuel fractions by 20% (unfinished) or 50% (hydrofinished). 2) The manufacturing cost of GTF from thermal cracking distillates is the same as from the unfinished diesel fuel fraction and 1.3 times lower than from the hydrofinished diesel fuel fraction. 3) The manufacturing cost of GTF from residual products, because of the necessity of a separation stage, is 40–60% greater than the cost of fuels from coking distillates. 4) It is possible to reduce significantly the cost of GTF from residual products by obtaining them from petroleums subjected to intensive desalination.
Type of Medium:
Electronic Resource
URL:
http://dx.doi.org/10.1007/BF00718960
Permalink