[0001] Recent developments of environmental protections topics and the need to obtain fuels
with a minimized impact on the environmental have led to the formulation of fuels
apt to meet technical combustion requirements as well as the imposed emission quality
levels at the stack.
[0002] On this subject, attention is especially riveted on sulphurized compounds that endanger
plants and animal life (acid rains), on unburnt products (flue gases) on carbon monoxide
(blood poisoning) and on the production of carbon dioxide (greenhouse effect).
[0003] Definite limits for noxious emissions are now enforced by Law (the Italian Presidential
Degree 203/88 and the Law n° 349 enacted in 1986) and the utilization of fuels is
subject to special authorizations. However besides the use of fossil fuels, studies
are also under way on the utilization of other, not yet exactly typified fuels derived,
for example, from vegetable oils.
[0004] This invention has the aim to suggest a series of new fuels, the basic constituents
of which are properly proportioned and mixed; their composition and use feature innovative
characteristics especially with regard to residual combustion products that have a
very low impact on the environment.
[0005] As technological background regarding the present invention there are to mention
same documents as it follows.
[0006] In the GB-A-2 099 449 it is disclosed a synthetic liquid fuel and fuel mixtures comprising
fatty acid esters in which the alkyl presents from 1 to 12 carbon atoms. The invention
WO-A-9 220 761 treats a fuel mixture containing at least one vegetable and/or animal
oil at least one aliphatic alchool with 1-5 C-atoms and petrol.
[0007] The document FR-A-2 492 402 concerns a mixture of 0-90% in volume of at least a gas
oil and 100-10% in volume of at least a fatty acid ester.
[0008] Besides it is known GB-A-2 127 433 which treats of a fuel composition comprising
10-40% by volume of coconoot oil, 10-40% by volume of palm kernel oil and 20-80% by
volume of kerosene. According to DE-A-2 930 220 it is provided a mixture of 25-75%
in volume of beet oil and 75-25% in volume of diesel oil. The document DE-A-4 135
294 provides a mixture of at least a vegetal and/or animal oil and at least an aliphatic
grease.
[0009] Finally according to JP-A-58 198 590 the molasses are converted into fuel by adding
a combustile material.
[0010] According to this invention, the basic constituents are:
a) sweet oil (distillate fractions having a boiling point in the 180°-300°C range);
b) fuel oil with a low sulphur content (a complex hydrocarbon mixture with less than
85% in volume volatile matter and less than 1% in weight sulphur content);
c) refined and/or unrefined vegetable olein (a mixture of liquid triglycerides derived
frown the extraction of vegetable fats);
d) refined and/or unrefined vegetable oils derived from various oleiferous crops;
e) Vegetable oil based alkyl esters (a mixture of fatty acid esters obtained by esterification
of triglycerides);
f) petroleum spirit (a distillate fraction having its boiling point in the 150°-220°C
range).
[0011] By proper batching of there constituents, this invention will permit to obtain fuels
with a low impact on the environment and in particular:
- pure vegetable gas oil
- semi-vegetable gas oil
- semi-vegetable fuel oil
the approximate formulation and average characteristics of which will be described
hereinafter.
PURE VEGETABLE GAS OIL
[0012] This fuel is a proportionally variable mix of vegetable oil based alkyl esters (for
example and only as a guide:
60% in weight), refined and/or unrefined vegetable oils ( for example and only as
a guide ranging between 30 and 40% in weight) and refined and/or unrefined vegetable
oleins (for example and only as a guide ranging between 0 and 10% in weight).
[0013] The typical characteristics of the formulated product can he identified as follows:
- density at 15°C, |
= 0.860-0.900 kg/lt (ASTM 1298) |
- viscosity at 37.8°C, |
= 2 - 7.4 cSt (ASTM D 445) |
- sulphur % w |
= none (ASTM D 1552) |
- pp, |
= 0 - 10°C (ASTM D 97) |
- flash point |
= min 55°C (ASTM D 93) |
- Ash content |
= max 0.01% (ASTM D 482). |
[0014] This mixture of vegetable oil derived alkyl esters and/or vegetable oils or oleins
permits to lower the viscosity and freezing point of the vegetable constituent so
as to obtain a fuel having characteristics similar to those of heating oil but with
the advantage of a virtually zero sulphur content.
[0015] The formula may also include a multi-purpose additive to provide the product with
a better reaction against water separation, a stability reserve and compatibility
at a lower freezing point.
[0016] From emission viewpoint it should be observed thatthese fuels contain no sulphur
and will therefore not increase the SO2 content in the atmosphere, no hydrocarbons
(to be considered as a warning sign for the emission of particulate matter) and, being
of pure vegetable nature, they will not raise the carbon dioxide level in the atmosphere.
This may also be a considerable adavantage in view of the tax on CO2 emissions proposed
by EEC.
SEMI-VEGETABLE GAS OIL
[0017] This gas oil is a proportionally variable mix of sweet oil and/or petroleum spirit
(for example and as a guide max. 70% in weight), refined and/or unrefined vegetable
oils (for example and as a guide ranging between 20% and 30% in weight) and refined
and/or unrefined vegetable oleins in a percentage ranging between 0 and 10% in weight.
[0018] The typical characteristics of this formula are identified as follows:
- density at 15°C |
= 0.820-0.875 kg/lt (ASTM D 1298) |
- viscosity at 37.8°C |
= 2 - 7.4 cSt (ASTM D 445) |
- sulphur content |
= traces (ASTM D 1552) |
- pp |
= - 20°C (ASTM D 97) |
- flash point |
= min 55°C (ASTM D 93) |
- ash content |
= max 0.01% (ASTM D 482). |
[0019] The mixing ratio of sweet oil and olein and/or vegetable oil is such as to permit
the formulation of a fuel having the typical characteristics of heating oil.
[0020] The formula of this fuel may also include a multi-purpose additive to provide the
product with a better reaction against water separation, a stability reserve and compatibility
at a lower freezing point.
[0021] The mixture of sweet oil and oleins and/or vegetable oils permits to lower the viscosity
and freezing point of the vegetable constituent so as to obtain a fuel having characteristics
similar to those of domestic heating oil but with the advantage of having about the
same sulphur content as sweet oil which is usually less than 0.1% in weight.
[0022] The presence of sweet oil also guarantees a fair stability reserve and compatibility
with conventional gas oil and fuels.
[0023] As to fluxes released into the atmosphere, the consideration expressed above are
also valid for pure vegetable oils except for same slight differences due to the presence
of domestic kerosene.
SEMI-VEGETABLE FUEL OIL
[0024] This fuel oil is a proportionally variable mix of fossil fuel oil with a low sulfur
content (for example and as a guide 60% in weight), vegetable oil (for example and
as a guide ranging between 20% and 40% in weight) and refined and/or unrefined vegetable
oleins (for example and as a guide ranging between 0 and 10%) possible with the addition
of sweet oil and/or petroleum spirit (for example and as a guide ranging between 0-10%
in weight).
[0025] The typical characteristics of this formula are identified as follows:
- density at 15°C |
= 0.900-0.970 kg/lt (ASTM D 1298) |
- viscosity at 50°C |
= 2 - 7 °E (NOM 47) |
- sulphur content |
= max. 0.3% in weight (ASTM D 1552) |
- pp |
= - 9°C (ASTM D 92) |
- flash point |
= min 65°C (ASTM D 93) |
- Ash content |
= max. 0.05% in weight (ASTM D 482) |
- water and sediments |
= max 1% in volume (ASTM D 1796). |
[0026] The considerations expressed above are also valid for this semi-fluid fuel as to
its performance in terms of emissions at the stack with the additional advantage of
its having a lower sulphur and asphaltene content than conventional fluid fuels, (as
a guide: sulphur max 0.2 - 0.3% in weight, asphaltene max. 4% in weight for industrial
purposes and max. 1.5% in weight for domestic heating) besides the very important
advantage of having a very low metal content especially as regards Nickel and Vanadium.
[0027] The formula of this fuel may also include one or more multi-purpose additives to
provide the product with a better reaction against water separation, a stability reserve
and compatibility at a lower freezing point.
1. Fuels with a low impact on the environment
characterized by the fact that they are derived from the following basic constituents:
a) Sweet oil (distillate fraction having its indicatory boiling point ranging between
180° and 300°);
b) fuel oil with a low sulphur content (complex mixture of hydrocarbons with less
than 85% in volume volatile matter evaporating at 350°C and less than 1% in weight
sulphur content;
c) Refined and/or unrefined vegetable olein;
d) Refined and/or unrefined vegetable oil obtained from oil producing plants of any
kind whatsoever;
e) Alkyl esters derived from vegetable oil (a mixture of fatty acid esters obtained
by triglyceride esterification);
f) petroleum spirit (distillate fraction having its indicatory boiling point in the
150° - 200°C range), properly dosed and batched so as to obtain a fuel with low impact
on the environment and in particular:
- pure vegetable gas oil
- semi-vegetable gas oil
- semi-vegetable fuel oil
the combustion products of which have a low content of unburnt residues and carbon
dioxide as well as no or very little sulphur and metals (Nickel, Vanadium, etc.).
2. Fuels as described in Claim 1,
characterized by the fact that the pure vegetable gas oil is consisting of a mixture of alkyl esters
derived from vegetable oils (for example and as a guide 60% in weight), refined and/or
unrefined vegetable oils (for example and as a guide ranging between 0% and 40% in
weight) and refined and/or unrefined vegetable oleins (for example and as a guide
ranging between 0 and 10% in weight) featuring the following average characteristics:
- density at 15 °C |
= 0.860 - 0.900 kg/lt (ASTM D 1298) |
- viscosity at 37.8°C |
= 2 - 7.4 cSt (ASTM D 445) |
- sulphur % in weight |
= none (ASTM D 1552) |
- pp |
= - 10°C (ASTM D 97) |
- flash point |
= min 55°C (ASTM D 93) |
- Ash content |
= max 0.01% in weight (ASTM D 482) |
3. Fuels as described in Claim 1,
characterized by the fact that this semi-vegetable oil is consisting of a mixture of sweet oil
and/or petroleum spirit (for example and as a guide max 70% in weight), refined and/or
unrefined vegetable oil (for example and as a guide ranging between 20% and 30% in
weight) and refined and/or unrefined vegetable oleins (for example and as a guide
ranging between 0 and 10% in weight), having the following characteristics:
- Density at 15°C |
= 0.820 - 0.875 kg/lt (ASTM D 1298) |
- viscosity at 37.8°C |
= 2 - 7.4 cSt (ASTM MD 445) |
- sulphur content % in weight |
= traces (ASTM D 1552) |
- pp |
= - 20°C (ASTM D 97) |
- Flash point |
= min 55°C (ASTM D 93) |
- Ash content |
= max 0.011 % in weight (ASTM D 482) |
4. Fuels as described in Claim 1,
characterized by the fact that the semi-vegetable heavy fuel oil is consisting of a mixture of
fossil fuel oil having a low sulphur content (for example and as a guide 60% in weight),
vegetable oil (for example and as a guide ranging between 20% and 40% in weight),
refined and/or unrefined vegetable oleins (for example and as a guide ranging between
0 and 10% in weight), possibly with the addition of sweet oil and/or petroleum spirit
(for example and as a guide ranging between 0 and 10% in weight), having the following
characteristics:
- density at 15% |
= 0.900 - 0.970 kg/lt (ASTM D 1298) |
- viscosity at 50°C |
= 2 - 7 E (NOM 47) |
- sulphur content |
= max 0.3% in weight (ASTM D 1552) |
- pp |
= -9°C (ASTM D 97) |
- flash point |
= min 65°C (ASTM D 93) |
- Ash content |
= max 0.05% in weight (ASTM D 482) |
- Water and sediments |
= max 1% in volume (ASTM 1796) |
5. Fuels as described in claim 1, characterized by the fact that one or more additives may be added to the basic constituents to
prevent water separation, to improve their stability and compatibility and to lower
their freezing point.