Scope of Use
[0001] The invention relates to the technology for improved quality liquid hydrocarbon fuel
generation and can be used in various industrial processes, such as petrochemical
industry, as well as for the preparation of liquid hydrocarbon fuel for the combustion
process in a variety of power plants in order to increase efficiency and improve environmental
performance.
Prior Knowledge
[0002] There is a method of electrical processing of liquid fuel and a liquid fuel activator
(patent
RU No 2032107, cl. F02M 27/04, published on 27/03/1995).
[0003] According to this method, liquid fuel before dispersing is activated in the 250-300
Hz and 20-25 kV pulse current electric field and separated into flows of opposite
polarity.
[0004] Liquid fuel activator comprises of a housing with inlet and outlet pipes, electrodes
placed inside the activator and connected to a source of high voltage, and a semi-permeable
membrane to separate the charged currents.
[0005] The disadvantages of this method and the activator are as follows:
- separation of the processed fuel into two bipolar flows does not ensure a full processing
of the entire fuel flow, as after fractionation only a part of the processed fuel
is combusted;
- use of the 250-300 Hz and 20-25 kV pulse current electric field reduces operational
safety of the equipment used.
[0006] The closest to the claimed method in regards to the technical substance and the achieved
result is the method of fuel processing, which consists of passing the fuel flow through
the fuel pipe section with variable frequency AC voltage electrodes. A layer of dielectric
material is placed in the processing chamber between electrodes of different polarities.
The parameters of electromagnetic effect on fuel are set in accordance with the experimental
ratio and the numeric values (patent
RU No 20385506, cl. F02M 27/04, published on 27/06/1995 - prototype).
[0007] The disadvantages of this method are as follows. The fuel is further energised and
broken into small fractions by the electromagnetic field due to the additional energy
potential. Thus, due to the smaller fractions of fuel it is combusted more completely
without changing the molecular composition of the fuel and increasing its combustion
value.
[0008] The closest to the claimed device in regards to the technical substance is the device
for the fuel processing containing a chamber-shaped housing with input and output
ports and equipped with at least two electrodes of different polarities to use electrostatic
field in order to influence a fuel flow in the processing chamber, which are connected
to the power supply, thus, the housing serves as one of the electrodes, and the other
internal electrode placed in the processing chamber is located coaxially to the housing
(patent
RU No 2156879, cl. F02M 27/04, published on 27/09/2000 - prototype).
[0009] Disadvantages of this device are as follows:
- use of complex and expensive technology for the production of dielectric material
of 4x10-6 to 0.5x10-3 thickness;
- limited application due to the low melting temperature of the dielectric material;
- insufficient mechanical resistance to mechanical abrasion and impurities present in
the fuel;
- influencing a fuel flow by the electrostatic field and placing a dielectric material
between the electrodes of different polarities does not provide structural changes
of the molecular composition of the fuel and the increase of its combustion value.
Disclosure of the Invention
[0010] The technical object of the invention is to create the method of and device for changing
the molecular composition of the liquid hydrocarbon fuel in the electric field that
improve the chemical structure of fuel and increase its combustion value.
[0011] The object of the invention is achieved by providing the method of changing the molecular
composition of the liquid hydrocarbon fuel in the electric field, which involves placing
the fuel between the electrodes with electric potential, which, according to the invention,
includes parameters of the alternating electric field and the mass of fuel in the
processing zone determined in accordance with the following empirical relationship:

where:
f - oscillation frequency of the electric field - 1/s,
E - amplitude of the electric field intensity - V/m,
v - fuel viscosity - m2/s,
σ - electric conductivity of fuel - Ohm-1·m-1,
I - leakage current in the processing zone - A,
M - molecular mass of fissionable hydrocarbons in the processed fuel - amu
[0012] Regarding this method of changing the molecular composition of liquid hydrocarbon
fuel under the influence of an electric field, the following conditions are preferable:
- the fuel mass in the processing zone is determined in accordance with the following
ratio:

where:
m - fuel mass in the processing zone - kg,
Vc - volume of the processing zone - m3,
Ve - total volume of electrodes placed in the processing zone - m3,
ρ - fuel density - kg/m3;
- fuel processing is carried out in its stationary position relative to the electrodes;
- fuel processing is carried out in the course of its movement through the processing
zone.
[0013] The object of the invention is also achieved by creating a device for changing the
molecular composition of the liquid hydrocarbon fuel in the electric field, which
comprises of a housing with inlet and outlet ports equipped with electrodes to use
an electric field in order to influence a fuel flow in the processing chamber, which
are connected to the power supply, whereby the housing serves as one of the electrodes,
and the other internal electrode placed in the processing chamber is located coaxially
to the housing; according to the invention, the power supply is made in the form of
the AC generator, and the inner electrode is hollow where an additional electrode
electrically coupled to the housing is coaxially placed, whereby the length of the
inner electrode corresponds to the following formula:

Where:
L - length of the middle electrode - m,
Q - volume throughput of the processed fuel - m3/s,
v - fuel velocity in the processing chamber - m/s.
[0014] Regarding this device for changing the molecular composition of liquid hydrocarbon
fuel under the influence of an electric field, the following conditions are preferable:
- sectional area of the inlet port and sectional area of the processing chamber are
determined by the Sin≤Sc ratio, where Sin - sectional area of the inlet port, Sc - sectional area of the processing chamber;
- Inlet and outlet pipes are installed in the housing where inlet and outlet ports are
located respectively;
- insulating inserts are installed between the housing and the inner electrode.
- The claimed method and device allow for a change in the molecular composition of liquid
hydrocarbon fuels under the influence of an alternating electric field that provides
an improvement of the chemical structure of the fuel and increases its combustion
value.
Brief Description of Drawings
[0015]
Fig.1 shows a longitudinal section of the device that changes the molecular composition
of the liquid hydrocarbon fuel under the influence of an electric field.
Best Mode of Implementation of the Invention
[0016] The claimed method is implemented in the device for changing the molecular composition
of the liquid hydrocarbon fuel in the electric field, which contains the housing 1
with inlet and outlet ports 2 and 3, and is equipped with electrodes in order to use
an electric field to influence the fuel flow in the processing chamber 4, which are
connected to a power source (not shown in the drawing), the housing 1 is one of the
electrodes, and the other internal electrode 5 in the processing chamber 4 is located
coaxially to the housing 1, the power supply is made in the form of the AC generator,
and the inner electrode 5 is hollow where the additional electrode 6 electrically
coupled to the housing 1 is coaxially placed, whereby the length of the inner electrode
5 corresponds to the following formula:

[0017] Regarding this device for changing the molecular composition of liquid hydrocarbon
fuel under the influence of an electric field, the following conditions are preferable:
- sectional area of the inlet port 2 and sectional area of the processing chamber 4
are determined by the Sin≤Sc ratio;
- Inlet and outlet pipes 7 and 8 are installed in the housing where inlet and outlet
ports 2 and 3 are located respectively;
- insulating inserts 9 are installed between the housing 1 and the inner electrode 5.
[0018] The claimed method is implemented in the device for changing the molecular composition
of liquid hydrocarbon fuel under the influence of an electric field as follows.
[0019] Fuel is supplied through the inlet port 2 of the inlet pipe 7 to the processing chamber
4 and divided into two flows: first flow - between the housing 1 and the inner electrode
5, second flow - between the inner electrode 5 and the additional electrode 6. Change
of the molecular composition of the processed fuel occurs under the influence of an
alternating electric field produced on the internal electrode 5. In addition, the
molecules of heavy hydrocarbons, the carbon skeleton of which consists of 18 or more
carbons, are split into lighter molecules, the carbon skeleton of which consists of
5÷10 carbons. The resulting light molecules are mostly alkanes, which have a higher
combustion value than heavy molecules and are oxidised during combustion to CO
2 and H
2O. Restructured fuel leaves the processing chamber 4 through the outlet port 3 of
the outlet pipe 8. Insulating inserts 9 allow for the supply of AC electric potential
to the inner electrode 5, centering the inner electrode 5 on the longitudinal axis
of the processing chamber 4, and determination of the required distance between the
housing 1 and the inner electrode 5. Furthermore, the introduction of the additional
electrode 6 reduces the electric field intensity and the supply power.
[0020] Technical results of the claimed invention are confirmed by the chemical research
data, mass spectrometry and the internal combustion engine indicator diagrams, which
showed the decrease of heavy aromatic hydrocarbons and the increase of light alkanes
in the processed fuel. In particular, the concentration of decane (C
10H
22) increased by 3.5 times, the concentration of xylele (C
8H
10) increased by 8 times, and the concentration of heavy aromatics (C
18H
20 and C
18H
22) decreased to zero in the processed fuel. As a result, the combustion value increased
by at least 10%. Indicator diagrams of internal combustion engines, which worked on
the processed fuel, show a decrease in the time of combustion of fuel mixture in the
cylinders of the engine and an increase of the combustion value. Thermotechnical measurements
of the boilers showed an increase of the combustion value, an increase of efficiency
of the boilers, and a reduction of the toxicity of exhaust gases.
Industrial Applicability
[0021] The use of the claimed invention in various industrial processes, such as petrochemical
industry, as well as for preparation of liquid hydrocarbon fuel for the combustion
process in a variety of power plants in order to increase efficiency and improve environmental
performance, ensures its industrial applicability.
1. The method of changing the molecular composition of the liquid hydrocarbon fuel in
the electric field, which involves placing the fuel between the electrodes with electric
potential and differs in that the parameters of the alternating electric field and
the mass of fuel in the processing zone are determined in accordance with the following
empirical relationship:

where:
f - oscillation frequency of the electric field - 1/s,
E - amplitude of the electric field intensity - V/m,
v - fuel viscosity - m2/s,
σ - electric conductivity of fuel - Ohm-1·m-1,
I - leakage current in the processing zone - A,
M - molecular mass of fissionable hydrocarbons in the processed fuel - amu
2. The method of changing the molecular composition of the liquid hydrocarbon fuel in
the electric field according to paragraph 1, which differs in that the fuel mass in
the processing zone is determined in accordance with the following formula:

where
m - fuel mass in the processing zone - kg,
Vc - volume of the processing zone - m3,
Ve - total volume of electrodes placed in the processing zone - m3,
ρ - fuel density - kg/m3;
3. The method of changing the molecular composition of the liquid hydrocarbon fuel in
the electric field according to paragraph 1, which differs in that the fuel processing
is carried out in its stationary position relative to the electrodes.
4. The method of changing the molecular composition of the liquid hydrocarbon fuel in
the electric field according to paragraph 1, which differs in that the fuel processing
is carried out in the course of its movement through the processing zone.
5. The device for changing the molecular composition of the liquid hydrocarbon fuel in
the electric field, which comprises of a housing with inlet and outlet ports equipped
with electrodes connected to the power supply to use an electric field in order to
influence a fuel flow in the processing chamber, whereby the housing serves as one
of the electrodes, and the other internal electrode placed in the processing chamber
is located coaxially to the housing, which differs in that the power supply is made
in the form of the AC generator, and the inner electrode is hollow where an additional
electrode electrically coupled to the housing is coaxially placed, whereby the length
of the inner electrode corresponds to the following formula:

where
L - length of the middle electrode - m,
Q - volume throughput of fissionable hydrocarbons in the processed fuel m3/s,
v - fuel velocity in the processing chamber - m/s.
6. The device for changing the molecular composition of the liquid hydrocarbon fuel in
the electric field according to paragraph 5, which differs in that the sectional area
of the inlet port and the sectional area of the processing chamber are determined
by the Sin≤Sc ratio, where Sin - sectional area of the inlet port, Sc - sectional area of the processing chamber.
7. The device for changing the molecular composition of the liquid hydrocarbon fuel in
the electric field according to paragraph 5, which differs in that the inlet and outlet
pipes are installed in the housing where inlet and outlet ports are located respectively.
8. The device for changing the molecular composition of the liquid hydrocarbon fuel in
the electric field according to paragraph 5, which differs in that the insulating
inserts are installed between the housing and the inner electrode.