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EP 2 287 276 B1 |
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EUROPEAN PATENT SPECIFICATION |
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Mention of the grant of the patent: |
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04.06.2014 Bulletin 2014/23 |
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Date of filing: 20.10.2009 |
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Previously filed application: 28.07.2009 PL 38865709 |
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International Patent Classification (IPC):
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Modifier of combustion of liquid and gaseous fuels in combustion engines
Modifikator für die Verbrennung von flüssigen und gasförmigen Brennstoffen in Verbrennungsmotoren
Modificateur de combustion des combustibles liquides et gazeux dans des moteurs à
combustion
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Designated Contracting States: |
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AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO
PL PT RO SE SI SK SM TR |
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Priority: |
28.07.2009 PL 38865709
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Date of publication of application: |
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23.02.2011 Bulletin 2011/08 |
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Proprietor: DAGAS Sp. z o.o. |
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05-660 Warka (PL) |
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Inventor: |
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- Majcher, Marek
05-660 Warka (PL)
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Representative: Gizinska-Schohe, Malgorzata et al |
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European Patent Attorney
Helmpertstrasse 11a 80687 München 80687 München (DE) |
| (56) |
References cited: :
EP-A1- 1 990 397 WO-A1-95/02655 WO-A2-99/35215 CH-A5- 599 464 CN-A- 1 184 146 RU-C1- 2 314 334
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EP-A1- 2 226 377 WO-A1-95/06805 WO-A2-2008/072254 CN-A- 1 114 676 DE-A1- 19 824 452 US-A- 4 389 220
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| Note: Within nine months from the publication of the mention of the grant of the European
patent, any person may give notice to the European Patent Office of opposition to
the European patent
granted. Notice of opposition shall be filed in a written reasoned statement. It shall
not be deemed to
have been filed until the opposition fee has been paid. (Art. 99(1) European Patent
Convention).
|
[0001] Object of the invention is a modifier of combustion of liquid and gaseous fuels,
such as fuel for marine engines, diesel oil, petrol, light and heavy oil, mazout and
other hydrocarbons, in combustion engines, a method of modifying a process of combustion
of fuels and a use of the modifier of fuel combustion.
[0002] Processes of combustion of liquid and gaseous fuels in combustion engines are still
being improved. In particular, all methods that allow to increase a process yield
and limitation of emission of harmful substances to atmosphere are investigated. Additives
of various types that modify processes taking place during combustion of fuels are
known. In particular, preventing from carbon black and other sludge banks settling
in e.g. in exhaust systems of combustion engines, is desirable.
[0003] Ferrocene derivatives belong to a group of metal organic compounds from a group of
cyclopentadienyl complexes. Complexes with iron II constitute a sandwich system, in
which two ligands are bound with a metal cation located between them. Derivatives
of such type are known and are used as catalysts of chemical processes.
[0004] From Japanese patent specification
JP2000247990, a use of cyclopentadiene complexes in chemical synthesis, e.g. during preparation
of aromatic amines, is known.
[0005] From Swiss patent
CH 599464, a use of ferrocene as a catalyst of processes of combustion to be used as an additive
to fuels used in engines, e.g. motor car engines, is known.
[0007] Object of the invention is a modifier of combustion of liquid and gaseous fuels,
such as fuel for marine engines, diesel oil, petrol, light and heavy oil, mazout and
other hydrocarbons in combustion engines,
characterised in that it contains from 10 to 30 wt. % of carrier, preferably water or a hydrocarbon distillate
of a fraction of the 180 - 380°C range, from 20 to 80 wt. % of at least one aliphatic
alcohol, from 5 to 15 wt. % of carbamide or its derivatives and from 5 to 15 wt. %
of monoacetylferrocene.
[0008] The modifier contains from 10 to 30 wt. % of water or a hydrocarbon distillate of
a fraction of the 180 - 380°C range, from 20 to 40 wt. % of isopropanol, from 20 to
40 wt. % of n-butanol, from 5 to 15 wt. % of carbamide and from 5 to 15 wt. % of monoacetylferrocene.
[0009] The modifier contains 20 wt. % of water or hydrocarbon distillate of a fraction of
the 180 - 380°C range, 30 wt. % of isopropanol, 30 wt. % of n-butanol, 10 wt. % of
carbamide and 10 wt. % of monoacetylferrocene.
[0010] Object of the invention is also a method of modifying a process of combustion of
liquid and gaseous fuels, such as fuel for marine engines, diesel oil, petrol, light
and heavy oil, mazout and other hydrocarbons, in combustion engines,
characterised in that the modifier of combustion containing from 10 to 30 wt. % of carrier, preferably
water or hydrocarbon distillate of a fraction of the 180 - 380°C range, from 20 to
80 wt. % of at least one aliphatic alcohol, from 5 to 15 wt. % of carbamide or its
derivatives, and from 5 to 15 wt. % of monoacetylferrocene, is metered as optionally
additionally diluted, the diluent preferably being a carrier, either is metered as
liquid directly to the fuel or to the aeration system of combustion chamber of the
engine, preferably through pumping together with air to fuel mixture fed to the combustion
chamber of the engine, the modifier being metered as diluted with a carrier, preferably
at the ratio 2.5 - 3.8 mL modifier per 1 L water or the hydrocarbon fraction of the
180 - 380°C range.
[0011] The modifier contains from 10 to 30 wt. %, preferably 20 wt. % of carrier, from 20
to 40 wt. %, preferably 30 wt. % of isopropanol, from 20 to 40 wt.%, preferably 30
wt. % of n-butanol, from 5 to 15 wt. %, preferably 10 wt. % of carbamide and from
5 to 15 wt. %, preferably 10 wt. % of monoacetylferrocene.
[0012] In case of metering the modifier to the aeration system, it is metered by means of
spraying.
[0013] From 1.8 to 10 mL of the modifier per 100 L of fuel as diesel oil or from 5 to 47
mL of the modifier per 1000 kg of fuel for marine engines or from 10 to 100 mL of
the modifier per 1000 litres of liquid fuels, such as mazout and heavy oil, is metered
in the method, and the given amounts refer to the modifier composition prior to the
additional dilution.
[0014] Object of the invention is also a use of the modifier of combustion defined above
for increasing a yield of combustion of liquid and gaseous fuels, reducing their consumption
and as a catalyst in combustion process in engines, and for decreasing emission of
undesirable gases, in particular carbon monooxide, to atmosphere and also for after-burning
carbon black, exhaust gases and other impurities present in the combustion chamber,
for example dusts and coal tar-type substances, as well as for purifying the combustion
chamber and exhaust system from sludge banks.
[0015] Object of the invention is also an application of the modifier of combustion of liquid
and gaseous fuels, containing a carrier, preferably water or hydrocarbon distillate
of a fraction of the 180 - 380°C range, at least one aliphatic alcohol, carbamide
or its derivatives and monoacetylferrocene, for increasing a yield of combustion of
liquid and gaseous fuels, reducing its consumption and as a catalyst in combustion
process in engines, and for decreasing emission of undesirable gases, in particular
carbon monooxide, to atmosphere and also for after-burning carbon black, exhaust gases
and other impurities present in the combustion chamber, for example dusts and coal
tar-type substances, as well as for purifying the combustion chamber and exhaust system
from sludge banks.
[0016] The above-mentioned composition of the modifier can be adjusted to a type of fuel
used and a type of engine powered with that fuel. Accordingly, amounts of individual
components can be changed. In addition to the ratios mentioned-above, the modifier
can also contain 15 to 25 wt. % of carrier, 25 to 35 wt. % of isopropanol, 25 to 35
wt. % of n-butanol, 8 to 12 wt. % of carbamide and 8 to 12 wt. % of monoacetylferrocene.
[0017] The modifier of combustion according to the invention can in particular be used in
chambers of self igniting diesel-oil, low-speed and high-speed engines powered with
low-octane or high-octane (92, 95, 98) petrol, light and heavy diesel oil, mazout,
gas e.g. methane or propane-butane. The modifier can also be used together with fuels
of a different type, selection or composition modification of which will be familiar
for a skilled in the art. As fuels to which the modifier of the invention can be utilised,
suitable hydrocarbon fractions utilised for fuelling combustion engines, e.g. a fraction
derived from crude oil distillation within the fraction of the 180 - 360°C range,
e.g. diesel oil, can be used. It can also be a fraction of the 220 - 340°C range.
Hydrocarbon fractions can also be used as an additional diluent for combustion modifier
composition, when it is metered in the liquid state directly to the fuel. When the
modifier is metered in a sprayed form to an aeration system of the engine (to a carburettor),
it is water which is used as a carrier and a diluent for the modifier composition.
A use of a different type of carriers and diluents having similar properties i.e.
not interfering into chemical processes during fuel combustion when using a modifier,
is also possible.
[0018] Aim of the invention was to develop a universal modifier of combustion of all fuel
types in combustion engines having different construction, to act as a catalyst that
limits settling carbon black and coal tar type substances, ensures its after-burning
and reduces emission of undesirable substances, e.g. carbon monoxide, solids and hydrocarbons
to atmosphere and - at the same time - enhances a yield of combustion processes by
reducing consumption of the respective fuels.
[0019] Unexpectedly, it has been found that modifier components - as a result of its specific
quantitative and qualitative selection - make it possible to carry out the combustion
process in engines in a stable and safe way. A use of a specific ferrocene derivative
(monoacetylferrocene) in combination with alcohols and carbamide has made it possible
to fully control existing processes and ensured a universal character of the modifier,
suitable to be used with various fuels. What is more important, general operational
parameters of engines used in tests have not been deteriorated. On the other hand,
several advantages resulting from a use of the modifier of combustion according to
the invention, in particular limitation of emission of harmful exhaust gas components
to atmosphere, were observed.
[0020] One of the most prospective directions when utilising the modifier of combustion
of the invention is its application for modifying the process of fuel combustion in
marine engines, motor-cars of any type, construction equipment, diesel locomotives,
in engines that supply electric energy generators, mining machines and aircraft reaction
engines. The performed study has demonstrated that the reduction in relative consumption
during modified fuel combustion for methane-rich natural gas (GZ-50) is not less than
12 %, for diesel oil - 12 %, and for mazout and fuel for marine engines - 10 -15%.
A decrease in fuel consumption was also observed for other hydrocarbon fractions used
as a liquid and gaseous fuel.
[0021] Experiments concerning practical implementation of the modifier of the invention
i.e. a composition of the modifier (for example according to Example 1) have evidenced
that in some cases there is a possibility of fuel saving up to 12% and even up to
25%, a direct influence of the modifier on saving of fuel consumption necessary to
perform definite work amounting to 8-12 %, while the remaining contribution to saving
being an indirect factor, e.g. resulting from purifying the engine and systems of
feeding and exhausting. An extra effectiveness of processes was achieved through introducing
a slight modification of aeration system of the combustion chamber, not involving
any construction changes in the feeding system. A use of the modifier of the invention
results in good condition of exhaust system as a result of e.g. its purification without
necessity of introducing substantial changes in engine construction.
[0022] It is also crucial that the modifier acts in all engine sections i.e. in the area
of fuel feeding to the engine, in the engine itself, and in the exhaust system, where
it causes a decrease in contamination of oil with fuel combustion products, and also
in oil filtration system, thanks to which advantageous changes occur within the whole
mentioned area and then after-burning of exhaust gas, dust and sludge banks takes
place.
[0023] The modifier according to the invention can be successfully used in combustion engines
and in jet engines of any type, for various fuels such as aircraft fuel, petrol, light
and heavy diesel oils, marine engines fuel, mazout, hydrocarbons of various types,
and their compositions in a mixture with petroleum-based synthetic fuels, optionally
processed or not, and all low-grade fuels. The invention is also applicable for gaseous
and liquid fuels such as methane, propane - butane, synthesis gas, as well as for
various contaminated mixtures and fuels.
[0024] An application of the modifier according to present invention makes it possible to
use low-processed and wet raw materials as fuels.
[0025] The essential component of the modifier according to the invention is a complex being
an iron carrier - monoacetylferrocene i.e. cyclopenta-1,3-diene; 1-(1-cyclopenta-2,4-
dienylidene) etanolate of ferrum ion 2+. In processes during combustion, presence
of hydroxyl groups in a reaction medium is of crucial importance. The modifier contains
also carbamide or its derivatives, selected from alkylurea of R
1R
2N(CO)NR
1R
2 type, where R
1, R
2, R
3, R
4 are the same or different and are C
1-C
6 alkyl groups, e.g. methylene or ethylene groups.
[0026] Aliphatic alcohols used in the modifier according to the invention can have linear
or branched chains. The modifier of the invention should include at least one alcohol
(a carrier of OH groups). Preferably, the alcohol is selected from a group of C
2 - C
11 alcohols, more preferably C
3-C
8 alcohols, in particular C
3-C
6 alcohols. Examples of alcohols used are: ethanol, propanol, isopropanol, n-butanol,
pentanol, heptanol and octanol. By selecting the alcohol, a ratio of hydroxyl groups
to a number of carbon atoms in a chain is changed, thereby changing the ratio of hydroxyl
groups to a mass of other modifier components. Advantageous effects are obtained when
using alcohols of moderate chain length, e.g. isopropanol and n-butanol. Thus, a mixture
of the two alcohols in the modifier is preferably used. On the other hand, the modifier
can contain only one alcohol of the mentioned group or a mixture of three or four
alcohols.
[0027] A mixture of the modifier may also include additives, which do not influence its
properties. e.g. dyes, to make a distinction between various types of the modifier.
[0028] One can assume that during combustion processes, complex ligands based on an N-radical
having a complexing centre constituted by an iron ion with built-in hydroxyl groups
and hydrocarbon chains in a suitable position are formed in the reaction mixture.
[0029] Roughly speaking, one can define these compounds as derivatives of C
5H
5FeC
5H
4COC
mH
n.type, but it is only a pictorial formula and there is no possibility to isolate such
compounds from the reaction mixture.
[0030] In the method according to the invention, the modifier composition is optionally
diluted with water or a hydrocarbon fraction, and only then it is metered. The modifier
is either directly added to the fuel (e.g. to a fuel container) and does not contain
water, or it is fed through a metering system to an air suction system i.e. to a carburettor
premixing chamber (through a feeding channel), where the modifier is metered by spraying
as an aqueous solution.
[0031] In Figures (Figs. 1-4) results of comparison of testing of exhaust gas components
for the basic fuel (diesel oil) and for the modifier-added fuel of the composition
of Example 1 are shown. The tests were carried out with a use of SULZER 6A20/24 engine.
The modifier diluted at the ratio of 2.8 mL modifier : 1 L diluent (carrier) was used.
The modifier was metered directly to the fuel or to the engine aeration chamber at
the amount from 4.6 mL to 5mL of modifier per 100 L and per 1000 L of diesel oil feeding
the engine.
[0032] Fig. 1 presents comparison of values of emission of not-burnt hydrocarbons (THC)
in exhaust gas when feeding with the basic fuel and the fuel with the added modifier
of the invention, Fig. 2 - comparison of values of emission of carbon monooxide in
exhaust gas when feeding with the basic fuel and the fuel with the added modifier
of the invention, Fig.3 - comparison of values of emission of carbon black in exhaust
gas when feeding with the basic fuel and the fuel with the added modifier of the invention,
Fig. 4 - comparison of values of emission of solid particles in exhaust gas when feeding
with the basic fuel and the fuel with the added modifier of the invention.
Example 1
[0033] A modifier of the following composition: 20 wt. % of carrier, 30 wt. % of isopropanol,
30 wt. % of n-butanol, 10 wt. % of carbamide and 10 wt. % of monoacetyloferrocene
has been prepared. Sample I a was a modifier, in which water was used as a carrier,
sample 1b was a modifier with an added hydrocarbon distillate of a fraction of the
180 - 380°C range as a carrier.
Example 2
[0034] In an analogous way, samples 2a and 2b were prepared. The modifier composition was
the following: 30 wt. % of carrier (water or hydrocarbon distillate), 35 wt. % of
isopropanol, 25 wt. % of n-butanol, 5 wt. % of carbamide, 5 wt. % of monoacetyloferrocene.
Example 3
[0035] In an analogous way, samples 3a and 3b were prepared; the modifier was of the following
composition: 20 wt. % of carrier (water or hydrocarbon distillate), 50 wt. % of isopropanol,
15 wt. % of carbamide and 15 wt. % of monoacetyloferrocene.
Example 4
[0036] The modifier of Example 1 - sample 1a was diluted with water at the ratio of 3 mL
catalyst composition per 1 L water. The resulting solution was metered to the aeration
chamber of the engine. Sample 1b was diluted with hydrocarbon fraction 180÷360 at
the analogous ratio and was metered as liquid to a fuel container. Amounts of the
metered modifier amounted to 5 mL per 100 L diesel oil (recalculated to modifier before
being diluted). Diluting the modifier carrier only provided uniform metering and more
easy handling with liquids. Testing of modifier efficiency was carried out using test
engines PERKINS 1104C-44 and SULZER 6A20/24.
[0037] In Table I below comparison of testing of emission of engine SULZER 6A20/24 for the
basic fuel with the added modifier of Example I and for the basic fuel (standard diesel
oil) with no additives, is presented. Emission of hydrocarbons (HC) and carbon monooxide
(CO) was considerably lower in case of the modifier-added fuel. Results of comparison
for engine SULZER are presented also in Fig. 1-4, which show, what advantages as regards
emission of exhaust gas were achieved by using the modifier of Example 1.
[0038] In tests carried out for PERKINS 1104C-44-type engine, a presence of the modifier
additive in diesel oil (basic fuel) resulted in a decrease in power output of the
engine within the whole range of engine speed. The observed power output decrease
at 2200 rpm was 7% as compared to the conventionally used diesel oil. At the same
time, a decrease in fuel consumption from 4 to 12% depending on a modifier composition
was observed. Calculations of general efficiency of engine for the conventional fuel
and the fuel with added modifier did not exhibit any significant differences. This
results from modifier properties, which cause a slight decrease in engine power output,
but at the same time reduce fuel consumption. It was also observed that using the
fuel with the added modifier resulted in a reduced emission of carbon monooxide and
solid particles, in particular at low engine speeds. A decrease in carbon monooxide
emission was within the range of 70÷90%. A level of hydrocarbons emission decreased
about 30%.
[0039] In tests with a use of SULZER 6A20/24 engine, testing of exhaust gas and calibration
procedures and analytical equipment control conformed to Norm PN-EN ISO 8178 (01.1999).
Testing was carried out on a marine piston diesel engine of SULZER 6A20/24 type. A
spectrophotometric analyzer of exhaust gas was used. No influence of the fuel with
the added modifier of the invention on change in mechanical or energy performance
of engine was observed. At the same time, an advantageous influence of the combustion
modifier on levels of emission of harmful exhaust gas components was observed. A level
of reduction of emission of solid particles lies within the range of 53÷73%. Emission
of insoluble fraction of organic compounds was reduced by 35÷62%. Also a decrease
in emission of solid particles within the range of 40÷62% was observed. A decrease
in emission of not-burnt hydrocarbons amounted to 19÷40% Values of listed parameters
depended on the engine load. A decrease in emission of carbon monooxide was very considerable
at low engine load and amounted to 38.6% (for the remaining ranges it amounted to
1÷9%).
[0040] The fuel with the added modifier of the invention in figures (fig. 1-4) was denoted
with a trade name "Reduxco".
Table 1
| Component |
|
Basic fuel |
Modified fuel |
| NOx unit weighed emission |
g/kWh |
16.71 |
17.40 |
| CO unit weighed emission |
g/kWh |
1.30 |
1.06 |
| HC unit weighed emission |
g/kWh |
1.33 |
0.97 |
| SOx unit weighed emission |
g/kWh |
0.05 |
0.05 |
1. Modifier of combustion of liquid and gaseous fuels, such as fuel for marine engines,
diesel oil, petrol, light and heavy oil, mazout and other hydrocarbons, in combustion
engines, characterised in that it contains from 10 to 30 wt. % of carrier selected from hydrocarbon distillate of
a fraction of the 180 - 380°C range, from 20 to 80 wt. % of at least one aliphatic
alcohol, from 5 to 15 wt. % of carbamide or its derivatives selected from alkylurea
of R1R2N(CO)NR1R2 type, where R1, R2, R3, R4 are the same or different and are C1-C6 alkyl groups, and from 5 to 15 wt % of monoacetylferrocene.
2. Modifier according to Claim 1, characterised in that it contains from 10 to 30 wt. % of a hydrocarbon distillate of a fraction of the
180 - 380°C range, from 20 to 40 wt. % of isopropanol, from 20 to 40 wt. % of n-butanol,
from 5 to 15 wt. % of carbamide and from 5 to 15 wt. % of monoacetylferrocene.
3. Modifier according to Claim 1, characterised in that it contains 20 wt. % of a hydrocarbon distillate of a fraction of the 180 - 380°C
range, 30 wt. % of isopropanol, 30 wt. % of n-butanol, 10 wt. % of carbamide and 10
wt. % of monoacetylferrocene.
4. Method of modifying a process of combustion of liquid and gaseous fuels, such as fuel
for marine engines, diesel oil, petrol, light and heavy oil, mazout and other hydrocarbons,
in combustion engines, characterised in that the modifier of combustion containing from 10 to 30 wt. % of carrier, from 20 to
80 wt. % of at least one aliphatic alcohol, from 5 to 15 wt. % of carbamide or its
derivatives selected from alkylurea of R1R2N(CO)NR1R2 type, where R1, R2, R3, R4 are the same or different and are C1C6 alkyl groups, and from 5 to 15 wt. % of monoacetylferrocene, is metered as optionally
additionally diluted, a diluent preferably being a carrier, either in the liquid state,
directly to the fuel or to an aeration system of an engine combustion chamber, the
modifier being metered as diluted with the carrier, preferably at the ratio of 2.5
- 3.8 mL modifier per 1 L water or the hydrocarbon fraction of the range 180 - 380°C.
5. Method according to Claim 4, characterised in that the carrier is selected from water or a hydrocarbon distillate of a fraction of the
180 - 380°C range.
6. Method according to Claim 4, characterised in that the composition is metered directly to the fuel or to an aeration system of an engine
combustion chamber by pumping together with air to a fuel mixture fed to the engine
combustion chamber.
7. Method according to Claim 4, characterised in that the modifier of combustion contains from 10 to 30 wt. % of carrier, from 20 to 40
wt. % of isopropanol, from 20 to 40 wt. % of n-butanol, from 5 to 15 wt. % of carbamide
and from 5 to 15 wt. % of monoacetylferrocene.
8. Method according to Claim 7, characterised in that the modifier of combustion contains 20 wt. % of carrier, 30 wt. % of isopropanol,
30 wt. % of n-butanol, 10 wt. % of carbamide, and 10 wt. % of monoacetylferrocene.
9. Method according to Claim 4, characterised in that in case of metering of the modifier to the aeration system, it is metered by spraying.
10. Method according to Claim 4, characterised in that from 1.8 to 10 mL modifier per 100 L fuel, as diesel oil, or from 5 to 47 mL modifier
per 1000 kg fuel for marine engines, or from 10 to 100 mL modifier per 1000 L liquid
fuels, such as mazout and heavy oil, is metered, and the given amounts of the modifier
refer to its composition prior to the additional dilution.
11. Use of the modifier of combustion defined in Claim 1 for increasing a yield of combustion
of liquid and gaseous fuels, for reducing its consumption, as a catalyst in combustion
engines, and for reducing emission of undesirable gases, in particular carbon monooxide,
to atmosphere, as well as for after-burning carbon black, exhaust gases and other
impurities present in the combustion chamber, for example dusts and coal tar-type
substances, as well as for purifying the combustion chamber and exhaust system from
sludge banks.
1. Modifikator für die Verbrennung von flüssigen und gasförmigen Brennstoffen, wie Brennstoffe
für Schiffsmotoren, Dieselöl, Benzin, Leichtund Schweröl, Masut und andere Kohlenwasserstoffe,
in Verbrennungsmotoren, dadurch gekennzeichnet, dass er von 10 bis 30 Gew.-% Träger, ausgewählt aus Kohlenwasserstoffdestillat einer Fraktion
aus dem Bereich 180 -380°C, von 20 bis 80 Gew.-% zumindest eines aliphatischen Alkohols,
von 5 bis 15 Gew.-% Carbamid oder seiner Derivate ausgewählt aus Alkylharnstoff vom
Typ R1R2N(CO)NR1R2, wobei R1, R2, R3, R4 gleich oder unterschiedlich sind und C1-C6-Alkylgruppen sind, und von 5 bis 15 Gew.-% Monoacetylferrocen enthält.
2. Modifikator nach Anspruch 1, dadurch gekennzeichnet, dass er von 10 bis 30 Gew.-% eines Kohlenwasserstoffdestillats einer Fraktion aus dem
Bereich 180 - 380°C, von 20 bis 40 Gew.-% Isopropanol, von 20 bis 40 Gew.-% n-Butanol,
von 5 bis 15 Gew.-% Carbamid und von 5 bis 15 Gew.-% Monoacetylferrocen enthält.
3. Modifikator nach Anspruch 1, dadurch gekennzeichnet, dass er 20 Gew.-% eines Kohlenwasserstoffdestillats einer Fraktion aus dem Bereich 180
- 380°C, 30 Gew.-% Isopropanol, 30 Gew.-% n-Butanol, 10 Gew.-% Carbamid und 10 Gew.-%
Monoacetylferrocen enthält.
4. Verfahren zum Modifizieren des Verbrennungsprozesses von flüssigen und gasförmigen
Brennstoffen, wie Brennstoffe für Schiffsmotoren, Dieselöl, Benzin, Leicht- und Schweröl,
Masut und andere Kohlenwasserstoffe, in Verbrennungsmotoren, dadurch gekennzeichnet, dass der Verbrennungsmodifikator, enthaltend von 10 bis 30 Gew.-% Träger, von 20 bis 80
Gew.-% zumindest eines aliphatischen Alkohols, von 5 bis 15 Gew.-% Carbamid oder seiner
Derivate ausgewählt aus Alkylharnstoff vom Typ R1R2N(CO)NR1R2, wobei R1, R2, R3, R4 gleich oder unterschiedlich sind und C1-C6-Alkylgruppen sind, und von 5 bis 15 Gew.-% Monoacetylferrocen, optional zusätzlich
verdünnt, wobei das Verdünnungsmittel vorzugsweise ein Träger ist, entweder im flüssigen
Zustand, direkt in den Brennstoff oder ins Belüftungssystem der Motor-Verbrennungskammer
dosiert wird, wobei der Modifikator mit dem Träger verdünnt, vorzugsweise im Verhältnis
von 2,5 - 3,8 mL Modifikator pro 1 L Wasser oder Kohlenwasserstofffraktion aus dem
Bereich 180 - 380°C, dosiert wird.
5. Verfahren nach Anspruch 4, dadurch gekennzeichnet, dass der Träger aus Wasser oder einem Kohlenwasserstoffdestillat einer Fraktion aus dem
Bereich 180 -380°C ausgewählt ist.
6. Verfahren nach Anspruch 4, dadurch gekennzeichnet, dass die Zusammensetzung direkt in den Brennstoff oder ins Belüftungssystem der Motor-Verbrennungskammer
dosiert wird, indem sie zusammen mit der Luft in die Brennstoffmischung, die in die
Motor-Verbrennungskammer eingespeist wird, gepumpt wird.
7. Verfahren nach Anspruch 4, dadurch gekennzeichnet, dass der Verbrennungsmodifikator von 10 bis 30 Gew.-% Träger, von 20 bis 40 Gew.-% Isopropanol,
von 20 bis 40 Gew.-% n-Butanol, von 5 bis 15 Gew.-% Carbamid und von 5 bis 15 Gew.-%
Monoacetylferrocen enthält.
8. Verfahren nach Anspruch 7, dadurch gekennzeichnet, dass der Verbrennungsmodifikator 20 Gew.-% Träger, 30 Gew.% Isopropanol, 30 Gew.-% n-Butanol,
10 Gew.-% Carbamid, und 10 Gew.-% Monoacetylferrocen enthält.
9. Verfahren nach Anspruch 4, dadurch gekennzeichnet, dass im Falle der Dosierung des Modifikators ins Belüftungssystem, dieser durch Sprühen
dosiert wird.
10. Verfahren nach Anspruch 4, dadurch gekennzeichnet, dass von 1,8 bis 10 mL Modifikator pro 100 L Brennstoff, wie Dieselöl, oder von 5 bis
47 mL Modifikator pro 1000 kg Brennstoff für Schiffsmotoren, oder von 10 bis 100 mL
Modifikator pro 1000 L flüssiger Brennstoffe, wie Masut und Schweröl, dosiert werden,
und sich die angegebenen Mengen an Modifikator auf seine Zusammensetzung vor der zusätzlichen
Verdünnung beziehen.
11. Verwendung des im Anspruch 1 definierten Verbrennungsmodifikators zum Steigern des
Verbrennungsertrags von flüssigen und gasförmigen Brennstoffen, zum Reduzieren seines
Verbrauchs, als Katalysator in Verbrennungsmotoren, und zum Reduzieren von Emissionen
von unerwünschten Gasen, insbesondere Kohlenstoffmonoxid, in die Atmosphäre, sowie
zum Nachverbrennen von Ruß, Abgasen und anderen in der Verbrennungskammer vorliegenden
Verunreinigungen, zum Beispiel Stäuben und Substanzen vom Kohlenteer-Typ, sowie zum
Reinigen der Verbrennungskammer und des Abgassystems von Ablagerungen der Rückstände.
1. Modificateur de combustion des combustibles liquides et gazeux, tels que combustible
pour les moteurs marins, gazole, essence, huile légère et lourde, mazout et autres
hydrocarbures, dans des moteurs à combustion, caractérisé en ce qu'il contient de 10 à 30% en poids de porteur choisi parmi distillat d'hydrocarbure
d'une fraction de la gamme de 180 - 380°C, de 20 à 80% en poids d'au moins un alcool
aliphatique, de 5 à 15% en poids de carbamide ou de ses dérivés choisis parmi alkylurée
de type R1R2N(CO)NR1R2, où R1, R2, R3, R4 sont identiques ou différents et sont des groupes alkyles C1-C6, et de 5 à 15% en poids de monoacétylferrocène.
2. Modificateur selon la revendication 1, caractérisé en ce qu'il contient de 10 à 30% en poids de distillat d'hydrocarbure d'une fraction de la
gamme de 180 - 380°C, de 20 à 40% en poids d'isopropanol, de 20 à 40% en poids de
n-butanol, de 5 à 15% en poids de carbamide et de 5 à 15% en poids de monoacétylferrocène.
3. Modificateur selon la revendication 1, caractérisé en ce qu'il contient 20% en poids de distillat d'hydrocarbure d'une fraction de la gamme de
180 - 380°C, 30% en poids d'isopropanol, 30% en poids de n-butanol, 10% en poids de
carbamide et 10% en poids de monoacétylferrocène.
4. Procédé de modification d'un processus de combustion des combustibles liquides et
gazeux, tels que combustible pour les moteurs marins, gazole, essence, huile légère
et lourde, mazout et autres hydrocarbures, dans des moteurs à combustion, caractérisé en ce que le modificateur de combustion contenant de 10 à 30% en poids de porteur, de 20 à
80% en poids d'au moins un alcool aliphatique, de 5 à 15% en poids de carbamide ou
de ses dérivés choisis parmi alkylurée de type R1R2N(CO)NR1R2, où R1, R2, R3, R4 sont identiques ou différents et sont des groupes alkyles C1-C6, et de 5 à 15% en poids de monoacétylferrocène, est dosé comme en outre éventuellement
dilué, le diluant étant de préférence un porteur, soit à l'état liquide, directement
au combustible soit à un système d'aération d'une chambre de combustion du moteur,
le modificateur étant dosé comme dilué avec le porteur, de préférence dans un rapport
de 2,5 à 3,8 mL de modificateur par 1 L d'eau ou la fraction d'hydrocarbures de la
gamme de 180 - 380°C.
5. Procédé selon la revendication 4, caractérisé en ce que le porteur est choisi parmi l'eau ou un distillat d'hydrocarbure d'une fraction de
la gamme de 180 - 380°C.
6. Procédé selon la revendication 4, caractérisé en ce que la composition est dosée directement au combustible ou à un système d'aération d'une
chambre de combustion du moteur par pompage avec de l'air à un mélange combustible
fourni à la chambre de combustion du moteur.
7. Procédé selon la revendication 4, caractérisé en ce que le modificateur de combustion contient de 10 à 30% en poids de porteur, de 20 à 40%
en poids d'isopropanol, de 20 à 40% en poids de n-butanol, de 5 à 15% en poids de
carbamide et de 5 à 15% en poids de monoacétylferrocène.
8. Procédé selon la revendication 7, caractérisé en ce que le modificateur de combustion contient 20% en poids de porteur, 30% en poids d'isopropanol,
30% en poids de n-butanol, 10% en poids de carbamide et 10% en poids de monoacétylferrocène.
9. Procédé selon la revendication 4, caractérisé en ce qu'en cas de dosage du modificateur au système d'aération, il est dosé par pulvérisation.
10. Procédé selon la revendication 4, caractérisé en ce que de 1,8 à 10 mL de modificateur par 100 L de combustible, comme gazole, ou de 5 à
47 mL de modificateur par 1000 kg de combustible pour les moteurs marins, ou de 10
à 100 mL de modificateur par 1000 L des combustibles liquides, tels que mazout et
huile lourde, est dosé, et les quantités données du modificateur se rapportent à la
composition avant la dilution supplémentaire.
11. Utilisation du modificateur de combustion défini dans la revendication 1 pour augmenter
un rendement de combustion des combustibles liquides et gazeux, pour réduire sa consommation,
comme catalyseur dans des moteurs à combustion, et pour réduire l'émission de gaz
indésirables, en particulier monoxyde de carbone, dans l'atmosphère, ainsi que pour
la post-combustion du noir de carbone, des gaz d'échappement et des autres impuretés
présentes dans la chambre de combustion, par exemple des poussières et des substances
de type goudron de houille, ainsi que pour purifier la chambre de combustion et le
système d'échappement des banques de boue.


REFERENCES CITED IN THE DESCRIPTION
This list of references cited by the applicant is for the reader's convenience only.
It does not form part of the European patent document. Even though great care has
been taken in compiling the references, errors or omissions cannot be excluded and
the EPO disclaims all liability in this regard.
Patent documents cited in the description