The production and the features of water-residual fuel emulsion.
Moroianu, Corneliu ; Samoilescu, Gheorghe ; Patrichi, Ilie 等
1. INTRODUCTION
This paper presents a possibility of producing the water-heavy fuel
emulsions by means of ultrasounds. The emulsion (Clayton, 1981), is a
heterogeneous system consisted of, at least, an immiscible liquid
intimately dispersed in another one under the form of some drops with a
diameter over 0.1mm. These systems have a minimum stability which can be
increased by additives like surface-active agents, finely powdered solid
particles, etc. The reference to the particle dimensions of dispersed
phase makes a distinction between the emulsify phenomenon and the
solubilization one. The emulsions are considered heterogeneous systems
which belong to the pseudo-colloid category. In the analysis of
emulsions it is necessary to differentiate the emulsion phases. The
phase that is under the form of some fine drops is named the disperse
phase or the internal phase. The phase that forms the matrix, in which
these drops are suspended, is called the continuous phase or the
external phase. Also, the internal phase is named the discontinuous
phase while the external phase is called the non-disperse phase.
Classically, there are two types of emulsions, starting from the known
case of water-oil emulsions (Travis, 2007). When the disperse phase is
oil, then it is the oil-water emulsion and it is noted with the symbol
O/W. When the disperse phase is water, it is the water-oil emulsion
noted with the symbol W/O. This paper presents a possibility of
producing the water-heavy fuel emulsions by the naval combustion
engines.
2. THE ULTRASOUND ACTION IN LIQUID MEDIA
The ultrasonic activation process of the liquids is based on the
cavitation phenomenon (Popa & Iscrulescu, 1983). When an acoustic
pressure changing from positive values to negative values acts on a
liquid, the liquid volume is put to compression and dilatation, at the
same time. When a maximum pressure is reached, in the points where the
cohesion is weak, a liquid breakage is produced. This breakage is
followed by an overpressure in the point where it has occurred, finding
the presence of some cavities. In these hollows, the liquid-dissolved
gases, under the form of bubbles which blow up after a short time,
generate local pressures of tens of bars. As on the surface and inside
the bubbles there are contrary electric charges, with the explosion, the
lightning discharges are generated. These produce an ionization of
surrounding particles and an emission of ultraviolet rays. The
cavitation process is influenced by the frequency and the intensity of
ultrasounds. The appearance of cavitation in a liquid depends, to a
great extent, on the existence of liquid-suspended undissolved gases
(Dragan, 1983). The cavitation can be obtained with acoustic pressures
lower than 20 [bar] and in this case, the well-differentiated points
appear in the liquid, named nuclear centers. These inhomogenities
localized in a liquid form the place of cavitation process. If in a
liquid there are introduced particles from another liquid which is
inmiscible with the first one, the liquid resistance is reduced, being
possible that the included gas molecules to separate the liquid from the
particles introduced on their surface. The presence of gas seems to play
the role of a real catalytic agent of cavitation formation. The cavity
bubble is developed up to a certain extent which, at a certain pressure,
depends on the developing time and the ultrasound frequency. The time,
t, necessary for the development of spherical cavity bubble from the
initial radius R0 to R is given by the relation:
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (1)
where:
[rho]--the liquid density [kg/[m.sup.3]]; P--the hydrostatic
pressure [daN/[mm.sup.2]]; [tau]--the surface liquid pressure [N/m].
In the following phase, after the relative slow dilatation of the
cavity bubble, its sudden compression and its quick destruction are
produced. The compression time of the bubble from a radius [R.sub.m] to
a radius R can be calculated by the relation:
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (2)
As a result of the cavity bubble destruction, the gas or the
existing vapors inside it are adiabatically compressed, the temperature
can reach 1000[degrees]C and a shock wave is generated of which
intensity increases with the increase of acoustic pressure. The
generation of acoustic cavitation in a liquid causes a series of
mechanical, acoustical, optical and chemical effects.
3. THE HYDRODYNAMIC WHISTLE FOR LIQUIDS
The generation of high intensity ultrasounds in liquids was
performed by means of hydrodynamic whistle for liquids. The hydrodynamic
whistle for liquids, Figure 1, is formed of a tapered nozzle (1)
provided with a nipple which has in front of it, at a distance of 0,3 -
1 mm, a vibrator segment (2) fixed in one or two nodal points.
[FIGURE 1 OMITTED]
4. THE EXPERIMENTAL RESEARCHES
In the experimental researches we have determined the fundamental
characteristics of water/fuel emulsion (Moroianu, 2001). For stating the
quality and durability (endurance) of emulsions produced by the
ultrasound generator we shall present the properties of such emulsion in
comparison with the non-emulsified fuel. The characteristics of
emulsified and non-emulsified fuels are shown in Table 1 for a naval RMC 15 fuel.
5. CONCLUSIONS
The water/fuel emulsion has been stored for a long time, 45 days
for a naval RMC 15 fuel. The determinations performed after 45 days have
showed that it has a good stability in time without the danger of
separating the two liquid components. At the same time, we performed
tests related to the behavior of water/fuel emulsion stored in
heat-proof vessels at different temperatures (50, 60, 80[degrees]C) for
60 and 150 days. The analysis of dimensions of water drops contained in
fuel and that of its percentage distribution showed changes of quality,
namely, an increase of average diameter of water drops and a reduction
of proportion of water drops with a diameter smaller than 4.8
([micro]m); though, these indicators are kept at high values. The test
results are presented in Table 2 (for 3 months) and Table 3 (for 4
months). It can be found that the quality indicators of water/fuel
emulsion (the average diameter of water drops and the proportion of
water drops with a diameter smaller than 4.8 ([micro]m) in RMC 10 fuel)
vary with the storage temperature, respectively, with the emulsion
viscosity and from this point of view it is recommended that for a long
storage the temperature should be below 50[degrees]C. Taking into
account the naval use of this emulsion, it can be chosen an average time
of storage up to 15-20 days as the consumption value at different cargo
ships is relatively low and the production possibilities of emulsion are
sure because the changes of preparation fuel plant for boilers are
minimum. During the experiments it was observed the behavior of
water/fuel emulsion under transport conditions and on the circuits of
fuel supply plant of boilers. It has been found that the preparation,
pre-heating and transport operations along the pipes didn't
influence the quality of emulsion.
6. REFERENCES
Clayton, R.,(1981). The Theory of Emulsion and Their Tehnical
Treatment, J.A.Churcill Ltd., London
Dragan, O., (1983). Ultrasunetele de mari energii (The high power
ultrasounds), Ed. Academiei, Bucharest
Moroianu, C. (2001). Arderea combustibililor lichizi in sistemele
de propulsie navale (The liquid fuel burning in the naval propulsion
systems), Editura Academiei Navale "Mircea cel Batran" ISBN 973-8303-04-4, Constanta
Popa, B.; Iscrulescu, V. (1983). Procese de ardere in camp sonor
(The combustion process in sound field), Ed.Academiei, Bucharest
Travis P.M., (2007), The Theory of Emulsion and Emulsification,
ISSN 003-021X, Springer Berlin/Heidelberg
Tab. 1. The characteristics of emulsified and non-emulsified
fuels for a naval RMC 15 fuel
Fuel characteristics Non-emulsified Water/fuel
fuel emulsion
Lower thermal
power 38650 [+ or -] 845 36920 [+ or -] 845
(kJ/kg).
Water content 0-1 7,5-10,5
(%).
Sulphur content 2,5-3,5 2,2-3,3
(%).
Conradson coke 12-20 11,5-19
content (%).
Density 960-980 960-985
(kg/[m.sup.3]).
Viscosity at 14-26 14-25,5
80[degrees]C
([degrees]E).
Average diameter -- 3-4,4
of water drops
([micro]m)
Proportion of 80-90,6
water drops with a
diameter smaller
than 4.8 ([micro]m).
Viscosity at 2,5-3 3,2-5,8
injection nozzles
([degrees]E).
Tab. 2 The test results in storage for 3 months
Water/fuel Initial Storage for 3 months
emulsion state
characteristics
Temperature -- 50/20,8 60/43,3 80/13,9
([degrees]C)/
Viscosity
([degrees]E)
Average 3,1 3,5 3,8 3,9
diameter of
water drops
([micro]m)
Proportion of 93,7 88,2 82,6 81,2
water drops
with a diameter
smaller than
4.8 ([micro]m)
Tab. 3. The test results in storage for 4 months
Water/fuel Initial Storage for 4 months
emulsion state
characteristics
Temperature -- 50/20,4 60/41,3 80/14
([degrees]C)/
Viscosity ([degrees]E)
Average
diameter of 3,6 3,8 3,9 4,1
water drops
([micro]m)
Proportion of
water drops
with a diameter 87,1 84,2 82,5 80,2
smaller than
4.8 ([micro]m)