US2012233911A1PendingUtilityA1
Fuel composition for a diesel engine
Est. expirySep 6, 2022(expired)· nominal 20-yr term from priority
C10L 1/08Y02P30/20C10L 1/32C10G 3/50
60
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Claims
Abstract
The invention is directed to a fuel composition for diesel engines. The fuel composition comprises 0.1-99% by weight of a component or a mixture of components produced from biological raw material originating from plants and/or animals and/or fish. The fuel composition comprises 0-20% of components containing oxygen. Both components are mixed with diesel components based on crude oil and/or fractions from Fischer-Tropsch process.
Claims
exact text as granted — not AI-modified1 - 7 . (canceled)
8 . A method for reducing nitrogen oxide emissions of a diesel engine, comprising:
(a) preparing a diesel fuel of biological origin consisting of at least one component produced by a process comprising:
(1) providing a feed stream of fatty acids, fatty acid esters, or both, derived from at least one biological raw material originating from animals or from animals in combination with plants and/or fish;
(2) hydrodeoxygenating the feed stream to form n-paraffins; and
(3) isomerizing the n-paraffins to form isoparaffins, in which the diesel fuel of biological origin is free of aromatics and has a cetane number higher than 60; and
(b) using the diesel fuel of biological origin in a diesel engine,
in which the nitrogen oxide emissions of the diesel engine are less than the nitrogen oxide emissions of the same engine using a diesel fuel derived from crude oil.
9 . The method of claim 8 , further comprising combining the diesel fuel of biological origin with a diesel fuel derived from crude oil before using the diesel fuel of biological origin in the diesel engine.
10 . The method of claim 8 , in which the biological raw material is selected from animal-based fats, fats contained in milk, recycled fats of the food industry, or mixtures thereof.
11 . The method of claim 8 , in which the fatty acid esters are triglycerides.
12 . The method of claim 8 , in which the diesel fuel of biological origin has a turbidity point lower than −30° C.
13 . A method for reducing nitrogen oxide emissions of a diesel engine, comprising:
(a) selecting a diesel fuel of biological origin consisting of at least one component produced by a process comprising:
(1) providing a feed stream of fatty acids, fatty acid esters, or both, derived from at least one biological raw material originating from animals or from animals in combination with plants and/or fish;
(2) hydrodeoxygenating the feed stream to form n-paraffins; and
(3) isomerizing the n-paraffins to form isoparaffins, in which the diesel fuel of biological origin is free of aromatics and has a cetane number higher than 60; and
(b) using the diesel fuel of biological origin in the diesel engine,
in which the nitrogen oxide emissions of a diesel engine are less than the nitrogen oxide emissions of the same engine using a diesel fuel derived from crude oil.
14 . The method of claim 13 , further comprising combining the diesel fuel of biological origin with a diesel fuel derived from crude oil before using the diesel fuel of biological origin in the diesel engine.
15 . The method of claim 13 , in which the biological raw material is selected from animal-based fats, fats contained in milk, recycled fats of the food industry, or mixtures thereof.
16 . The method of claim 13 , in which the fatty acid esters are triglycerides.
17 . The method of claim 13 , in which the diesel fuel of biological origin has a turbidity point lower than −30° C.
18 . A diesel fuel of biological origin consisting of at least one component produced by a process comprising:
(1) providing a feed stream of fatty acids, fatty acid esters, or both, derived from at least one biological raw material originating from animals or from animals in combination with plants and/or fish; (2) hydrodeoxygenating the feed stream to form n-paraffins; and (3) isomerizing the n-paraffins to form isoparaffins,
in which the diesel fuel of biological origin is free of aromatics, has a cetane number higher than 60, and reduces nitrogen oxide emissions of a diesel engine as compared to the same engine using a diesel fuel derived from crude oil.
19 . The diesel fuel of claim 18 , in which the biological raw material is selected from fats, oils, and mixtures thereof.
20 . The diesel fuel of claim 18 , wherein the biological raw material is selected from animal-based fats; fats contained in milk; recycled fats of the food industry; wood-based fats or oils; non-wood, plant-based fats or oils; fats contained in plants bred by means of gene manipulation; fish oils; and mixtures thereof.
21 . The diesel fuel of claim 18 , in which the biological raw material originates from a combination of animals and plants.
22 . The diesel fuel of claim 18 , in which the fatty acid esters are triglycerides.
23 . The diesel fuel of claim 18 having a turbidity point lower than −30° C.
24 . A method of producing a diesel fuel of biological origin consisting of at least one component produced by a process comprising:
(1) providing a feed stream of fatty acids, fatty acid esters, or both, derived from at least one biological raw material originating from animals or from animals in combination with plants and/or fish; (2) hydrodeoxygenating the feed stream to form n-paraffins; and (3) isomerizing the n-paraffins to form isoparaffins;
in which the diesel fuel of biological origin is free of aromatics and has a cetane number higher than 60.
25 . The method of claim 24 , in which the diesel fuel of biological origin reduces nitrogen oxide emissions of a diesel engine as compared to the same engine using a diesel fuel derived from crude oil.
26 . The method of claim 24 , in which the biological raw material is selected from animal-based fats, fats contained in milk, recycled fats of the food industry, or mixtures thereof.
27 . The method of claim 24 , in which the hydrodeoxygenating process is performed in a countercurrent manner.
28 . The method of claim 24 , in which the isomerizing process is performed in a countercurrent manner.
29 . The method of claim 27 , in which the isomerizing process is performed in a countercurrent manner.
30 . The method of claim 24 , in which the fatty acid esters are triglycerides.
31 . The method of claim 24 , in which the diesel fuel has a turbidity point lower than −30° C.Cited by (0)
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