1.  Processing of n-decane and n-octane
Table 1 shows the results processing of the n-decane. We observed isomerization of the hydrocarbon output with formation of volatile 2-, 3-, 4- methylene-nonane, n-nonane.  Table 2 shows the results of the processing of the n-octane. During processing of n-octane the isomerization reaction also takes place.  On the chromatograms we observed the separation of CH3 groups, formation of Benzyl and breaking off the Benzyl chain  The mechanism of reaction  differs from the classic hydrocarbon creaking separation of CH3 groups from molecular saturated hydrocarbons with carbon atom Number greater that 7.  Reactions of forming cyclical and aromatic hydrocarbons are similar with reactions of catalytic reforming.

2. Activation of the straight-run gasoline
Table 3 shows the results processing of the strain-run fraction of gasoline. 
The increase during of the treatment promotes the increase of number of destructed hydrocarbons.
The long-term process can increase Octane Number of gasoline up to 12 %.

3. Processing of the fuel and crude oil
The processed fuel oil was subject to the vacuum dispersion on a laboratory stand with the selection of fraction higher than 480 degree C.  The output of vacuum distillate under dispersion of the processed fuel oil was composed of 22.6% by weight.  After processing, the output of vacuum distillate under dispersion was composed of 32.7% by weight.  We observed an increase of the output of vacuum distillate to 10.1%.
Processing of the crude oil also permits to increase output of the gasoline-kerosene-diesel fractions up to 10 -15%.
4. Activation of the alkylation process
The application media in process alkylation permits to lower the use
of oxygen to 11 kg/m3 of alkylate. 
5. Supplying the reaction vessels
for preparation of the concentrates
of lubricant-coolant liquids allows increasing the output of the products
and improving its quality.