ISSN 1070-4272, Russian Journal of Applied Chemistry, 2010, Vol. 83, No. 5, pp. 918−920. Pleiades Publishing, Ltd., 2010.
Original Russian Text N.F. Akhmedov, S.E. Mamedov, R.A. Akhmedova, 2010, published in Zhurnal Prikladnoi Khimii, 2010, Vol. 83, No. 5, pp. 865−867.
BRIEF
COMMUNICATIONS
Cycloalkyldecalins as Components of Jet Fuels
N. F. Akhmedov, S. E. Mamedov, and R. A. Akhmedova
Baku State University, Baku, Azerbaijan
Received July 22, 2009
Abstract—The possibility of obtaining cycloalkyldecalins by the alkylation of 1- and 2-methylnaphthalenes
by cycloolefins with subsequent hydrogenation of methylcycloalkylnaphthalenes was studied. Physicochemical
parameters of reaction products were determined, and their structure was defined on the basis of IR and NMR
spectra.
DOI: 10.1134/S1070427210050307
As flight velocities in aviation increase the require-
ments to the quality of applied jet fuels raise. They should
have a high density, a maximal heat of combustion, and
a low solidification temperature. The most suitable com-
ponents of jet fuels are cycloalkylnaphtene hydrocarbons
possessing optimal properties for such fuels. However the
content of such hydrocarbons in commercial-grade fuel,
as a rule, is not sufficiently high, therefore the attempts
to find synthetic methods for obtaining fuels with high
contents of naphthene hydrocarbons are undertaken [1,
2]. From this point of view the hydrogenation of cyclo-
alkylnaphthalene hydrocarbons with the aim of obtaining
cycloalkyldecalins and their applications as components
of jet fuels seems promising.
The aim of the present work was to obtain cycloal-
kyldecalins promising as highly heat-producing stable
components of jet fuel.
EXPERIMENTAL
To synthesize cycloalkyldecalins, we used naphtha-
lene and 1- and 2-methylnaphthalenes as initial feed
stock, which were isolated by the fractionation and
crystallization methods from the fraction 200–250°С of
heavy pyrolysis resins (HPR). Cycloalkyldecalins were
synthesized in two stages.
(1) The alkylation of naphthalene and 1- and 2-meth-
ylnaphthalenes by cycloolefins (С5Н10, С6Н12, and
С6Н11СН3) was carried out onY-form zeolite catalysts in
a flowing system at 250°С. Physicochemical parameters
of the cycloalkylnaphthalenes are presented in Table 1.
It was found on the basis of IR and NMR spectra that
1- and 1,2-substituted naphthalenes are the main reac-
tion products.
In the pyrolysis of low-octane petrol and gas oils with
the purpose of obtaining low-molecular olefins a pyrolysis
resin is formed as a side product containing significant
amounts of naphthalene (~27%), methylnaphthalenes
(~20%), and other aromatic hydrocarbons, which do
not find a qualified application as yet, but can be a good
source for obtaining naphthene hydrocarbons. It is known
[3] that the fraction 200–350°Сobtained in the pyrolysis of
oil hydrocarbons during their hydrogenation on Raney
nickel gives a product meeting the requirements for jet
fuels by its quality. It was also offered [4] to hydroge-
nate the fraction 150–320°С of liquid pyrolysis products
on NiO/Al2O3 or on a tungsten-nickel sulfide catalyst at
temperatures of 150–350°С and pressures of 5–25 MPa
with the formation of naphthenes.
(2) Resulting cycloalkylnaphthalenes were subjected
to hydrogenation on a nickel-chromic catalyst. The
hydrogenation was carried out in a rotating (50 rpm)
stainless-steel autoclave of volume 1 l in the presence of
a nickel-chromic catalyst. Cycloalkylnaphthalene, 310 g,
and the catalyst, 10% the cycloalkylnaphthalene weight,
were loaded into the autoclave.After blowing through by
hydrogen, the autoclave was filled with hydrogen up to
the pressure of 9 MPa.At170–190°Сhydrogen absorption
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