AU2020203806B2 - Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids - Google Patents
Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids Download PDFInfo
- Publication number
- AU2020203806B2 AU2020203806B2 AU2020203806A AU2020203806A AU2020203806B2 AU 2020203806 B2 AU2020203806 B2 AU 2020203806B2 AU 2020203806 A AU2020203806 A AU 2020203806A AU 2020203806 A AU2020203806 A AU 2020203806A AU 2020203806 B2 AU2020203806 B2 AU 2020203806B2
- Authority
- AU
- Australia
- Prior art keywords
- diesel fuel
- isomerized
- fats
- biological component
- raw material
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/50—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids in the presence of hydrogen, hydrogen donors or hydrogen generating compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
- C10L1/328—Oil emulsions containing water or any other hydrophilic phase
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
- C10G2300/1014—Biomass of vegetal origin
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
- C10G2300/1018—Biomass of animal origin
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1022—Fischer-Tropsch products
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1033—Oil well production fluids
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1055—Diesel having a boiling range of about 230 - 330 °C
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
- C10L1/1233—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
- C10L1/125—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof water
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/16—Hydrocarbons
- C10L1/1616—Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
- C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
- C10L1/1852—Ethers; Acetals; Ketals; Orthoesters
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Fats And Perfumes (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
A biodiesel fuel composition comprising at least one isomerized biological
component produced by a process comprising: a) providing a feed stream of fatty
acids and/or fatty acid esters derived from an animal and/or fish source; b)
hydrodeoxygenating the feed stream to form n-paraffins; and c) isomerizing the
n-paraffins to form iso-paraffins.
3480795vl
Description
This application is a divisional application of Australian Patent Application No. 2017279689, filed on 20 December 2017, which is a divisional of Australian Patent Application No. 2015205854, filed on 21 July 2015, which is a divisional of Australian Patent Application No. 2010200726, filed on 26 February 2010, which is a divisional of Australian Patent Application No. 2003258753, filed on 4 September 2003 and is related to International Patent Application No. PCT/F2003/000648, filed on 4 September 2003 and claims priority from Finland Provisional Patent Application No. 20021596, filed on 6 September 2002; each of which is incorporated herein by reference in its entirety.
The present invention relates to a fuel composition for diesel engines, comprising components based on animal fat, diesel components based on crude oil and/or fractions from Fischer Tropsch process, and optionally components containing oxygen.
Currently used fuels for diesel engines mainly contain components from crude oil. The aim of the climate agreement of Kyoto is to eliminate detrimental influences due to human activities on the atmosphere, and thus on the climate. The EU has agreed on reducing emissions of carbon dioxide, methane and other greenhouse gases by eight per cent until 2010, starting from the levels of 1990. One of the objects of the EU agricultural policy is to find uses for agricultural overproduction, and to increase the self-sufficiency for fuels. Accordingly, an EU directive is being prepared, demanding that at least two per cent of the petrol and diesel fuel consumed in 2005 should be of biological origin. It is anticipated that one of the requirements of this directive is to increase the proportion of biocomponents to about six per cent until 2010. The directive will be validated in all EU countries in the near future.
la At the moment, the most common component of biological origin in fuels is rapeseed oil methyl ester, referred to as RME. RME is either used as such or as a mixture with fuels. Drawbacks of RME are its poor miscibility with diesel fuels, and, in
[Text continues on page 2.] comparison to a conventional diesel fuel (EN 590), particularly under low temperature conditions, its poor storage stability and poor performance at low temperatures. Moreover, it causes engine fouling and increases emissions of nitrogen oxides (NO,). A by-product of the production process of RME is glycerol, which may become a problem when high amounts of the product are produced. Esters of other vegetable oils may be produced in similar manner, and methyl esters of fatty acids are generally known as FAMEs (fatty acid methyl ester). These FAMEs may be used in similar applications as the rapeseed oil methyl ester, but they also have a negative effect on the quality of the diesel fuel, particularly with respect to the performance thereof at low temperatures, and in addition, the use thereof in fuels increases the emissions of nitrogen oxides. In some cases FAME and RME cause higher particle emissions and smoke development of the cold driven engine.
Vegetable oils and animal fats may be processed to decompose the ester and/or fatty acid structure and to saturate the double bonds of the hydrocarbon chains, thus obtaining about 80 to 85 % of n-paraffin product relative to the mass of the starting material. This product may be directly mixed with a diesel fuel, but a problem with the fuel so produced is its poor performance at low temperatures. In addition, n paraffins having a carbon number of fatty acids are waxy with a high solidification point, typically above +10 °C, thus limiting the use of these compounds in diesel fuels at least at low temperatures.
WO 2001049812 discloses a method for producing a diesel fuel with a molar ratio of iso-paraffins to n-paraffins of at least 21:1. In the method, a feed stock containing at least 50 % of Cio-paraffins is contacted with a catalyst in the isomerisation reaction zone.
WO 2001012581 discloses a method for producing methyl esters useful as biological diesel fuel, wherein mixtures of fatty acids and triglycerides are esterified in one phase. In this method, a solution is formed from fatty acids, triglycerides, alcohol, acid catalyst and co-solvents at a temperature below the boiling point of the solution. A co-solvent is used in amounts to provide a single phase then the solution is maintained for a period of time sufficient for the acid catalyzed esterification of the
3480795vl fatty acids to take place. Thereafter, the acid catalyst is neutralised, a base catalyst is added to transesterify the triglycerides, and finally, the esters are separated from the solution. Thus a biofuel containing esters is obtained, having a glycerol content of less than 0,4 % by weight.
US 6,174,501 presents a method for producing oxidized diesel fuel of biological origin. This oxidized biological diesel fuel comprises a mixture of transesterified triglycerides.
FI 100248 describes a two-step process for producing middle distillate from vegetable oil by hydrogenating fatty acids of the vegetable oil, or triglycerides, to give n-paraffins, and then by isomerising the n-paraffins to give branched-chain paraffins. A published foreign counterpart of this patent is patent application SE 9700149, which has matured into patent SE 520633.
Any gases, liquid droplets and solid particles present in the atmosphere in amounts being hazardous to human health and/or having a detrimental effect on animals, plants and different materials, are considered as air pollutants. Air pollution mainly originates from three main emission sources, i.e. the industry, energy production, and traffic.
The harmfulness of particle emissions is caused by the substances and compounds they carry, such as heavy metals and other carcinogenic and mutagenic compounds. Particles present in exhaust gases are small and thus hazardous to health.
Greenhouse gases allow for the penetration of the radiation from the sun to reach the earth, preventing, however, the thermal radiation from escaping from the earth back to space. They thus contribute to the warming of the earth. One of the most significant greenhouse gases is carbon dioxide released, for instance, during the combustion of fossil fuels.
Nitrogen oxides are acidifying compounds. This acidification may, for instance, lead to plant damages and species changes in surface waters. Nitrogen oxides may also
3480795vl react with oxygen to give ozone. This phenomenon contributes particularly to air quality in cities.
As the above teachings indicate, there is a need for a high quality fuel composition for diesel engines containing components of biological origin and also meeting the quality requirements for diesel fuels under low temperature operation conditions. Moreover, the fuel should be more environmentally friendly than prior art solutions.
It would be advantageous to provide a more environmentally friendly fuel composition for diesel engines containing components of biological origin, and also meeting the quality requirements for diesel fuels under low temperature conditions.
GENERAL DESCRIPTION OF THE INVENTION The fuel composition for diesel engines of the invention, containing components of biological origin, comprises at least one component produced from a biological starting material obtained from animals, diesel components based on crude oil and/or fractions from a Fischer-Tropsch process, and optionally components containing oxygen.
The characteristic features of the fuel composition for diesel engines containing components of biological origin are presented in the appended claims.
In an embodiment of the invention there is provided a fuel composition for diesel engines, wherein the fuel composition comprises: a) 0.1-99 % by volume of a component or a mixture of components produced from biological raw material originating from animals by hydrogenating and decomposing fatty acids and/or fatty acid esters to give hydrocarbons and isomerising the hydrocarbons to give isoparaffins; b) 0 - 20 % by volume of components containing oxygen, selected from the group consisting of aliphatic alcohols, ethers, fatty acid esters, water, and mixtures containing the same; both components a) and b) being mixed as an emulsion with or dissolved in diesel components based on crude oil and/or fractions from a Fischer-Tropsch process.
3480795vl
4a
Definitions of the specific embodiments of the invention as claimed herein follow.
According to a first embodiment of the invention, there is provided a diesel fuel composition comprising at least one isomerized biological component produced by a process comprising: (1) providing a feed stream of fatty acids having saturated or unsaturated C6 C24 hydrocarbon chains, fatty acid esters having saturated or unsaturated C6-C24 hydrocarbon chains, or both, derived from at least one biological raw material; (2) hydrodeoxygenating the feed stream to form n-paraffins having carbon numbers in the C6-C24 range; and (3) isomerizing the n-paraffins to form an isomerized biological component comprising iso-paraffins, wherein the isomerized biological component is suitable for use as a diesel fuel for a diesel engine, has a cetane number higher than 60, a turbidity point lower than -30 °C, and is free of aromates.
According to a second embodiment of the invention, there is provided a diesel fuel composition comprising at least one hydrodeoxygenated and isomerized biological component wherein the hydrodeoxygenated and isomerized biological component is suitable for use as a diesel fuel for a diesel engine, has a cetane number higher than 60, a turbidity point lower than -30 °C, is free of aromates, and is produced by hydrodeoxygenating and isomerizing a feed stream of fatty acids having saturated or unsaturated C6-C24 hydrocarbon chains, fatty acid esters having saturated or unsaturated C6-C24 hydrocarbon chains, or both, derived from at least one biological raw material.
According to a third embodiment of the invention, there is provided an isomerized biological component for diesel fuel produced by a process comprising: (1) providing a feed stream of fatty acids having saturated or unsaturated C6 C24 hydrocarbon chains, fatty acid esters having saturated or unsaturated C6-C24 hydrocarbon chains, or both, derived from at least one biological raw material; (2) hydrodeoxygenating the feed stream to form n-paraffins having carbon numbers in the C6-C24 range; and (3) isomerizing the n-paraffins to form an isomerized biological component comprising iso-paraffins, wherein the at least one biological raw material is chosen from animal-based material,
4b
plant-based material, fish-based material or mixtures thereof, and wherein the isomerized biological component is suitable for use as a diesel fuel for a diesel engine, has a cetane number higher than 60, a turbidity point lower than -30 °C, is free of aromates, has a density less than rapeseed oil methyl ester based fuel, and leaves no impurity residues.
According to a fourth embodiment of the invention, there is provided an isomerized biological component for diesel fuel produced by a process comprising: (1) providing a feed stream of fatty acids having saturated or unsaturated C6-C24 hydrocarbon chains, fatty acid esters having saturated or unsaturated C6-C24 hydrocarbon chains, or both, derived from at least one biological raw material; (2) hydrodeoxygenating the feed stream to form n-paraffins having carbon numbers in the C6-C24range; and (3) isomerizing the n-paraffins to form an isomerized biological component comprisingiso-paraffins, wherein the isomerized biological component is suitable for use as a diesel fuel for a diesel engine, has a cetane number higher than 60 and a turbidity point lower than -30 °C.
It was surprisingly found that the diesel fuel composition of the invention, containing components of biological origin, also meets the quality requirements for diesel fuels under low temperature conditions. The composition of the diesel fuel of the invention comprises: a) 0.1- 9 9 % by volume of a component or a mixture of components produced from biological raw material originating from animals, or both animals and plants, or originating from animals, plants and/or fish, by hydrogenating and decomposing fatty acids and/or fatty acid esters to give hydrocarbons and isomerising the hydrocarbons to give iso-paraffins; b) 0-20 % by volume of components containing oxygen selected from the group consisting of aliphatic alcohols, ethers, fatty acid esters, water and mixtures containing the same; both components a) and b) being mixed as an emulsion with or dissolved in diesel components based on crude oil and/or fractions from a Fischer-Tropsch process. Said components a) and b) are mixed in diesel components based on crude oil and/or in fractions from Fischer-Tropsch process by forming an emulsion with or by dissolving said components in diesel components based on crude oil and/or fractions from Fischer-Tropsch process.
Preferably the composition of the invention comprises: a) 5-80% by volume of a component or a mixture of components produced from biological raw material originating from animals, or both animals and plants, by hydrogenating and decomposing fatty acids and/or fatty acid esters to give hydrocarbons and isomerising the hydrocarbons to give iso-paraffins; b) 0-20% by volume of components containing oxygen selected from the group consisting of aliphatic alcohols, ethers, fatty acid esters, water and mixtures containing the same; both components a) and b) being mixed as an emulsion with or dissolved in diesel components based on crude oil and/or fractions from Fischer-Tropsch process.
More preferably the composition of the invention comprises: a) 10-80% by volume of a component or a mixture of components produced from biological raw material originating from animals, or both animals and plants, by hydrogenating and decomposing fatty acids and/or fatty acid esters to give hydrocarbons and
3480795vl isomerising the hydrocarbons to give iso-paraffins; b) 0-20% by volume of components containing oxygen selected from the group consisting of aliphatic alcohols, ethers, fatty acid esters, water and mixtures containing the same; both components a) and b) being mixed as an emulsion with or dissolved in diesel components based on crude oil and/or fractions from Fischer-Tropsch process.
Most preferably the composition of the invention comprises: a) 10-80% by volume of a component or a mixture of components produced from biological raw material originating from animals, or both animals and plants, by hydrogenating and decomposing fatty acids and/or fatty acid esters to give hydrocarbons and isomerising the hydrocarbons to give iso-paraffins; b) 1-20% by volume of components containing oxygen selected from the group consisting of aliphatic alcohols, ethers, fatty acid esters, water and mixtures containing the same; both components a) and b) being mixed as an emulsion with or dissolved in diesel components based on crude oil and/or fractions from Fischer-Tropsch process.
It was generally thought that products based on animal origin, as well as products based on recycled fats, could not be used in diesel fuels. These products were expected to contain high amounts of sulphur-, nitrogen- and metal-containing impurities, which would weaken the quality of the composition and make their processing very difficult. This, however, turns out not to be true.
The biological based fuel compositions of the current invention have remarkably lower "green house emissions" than the corresponding crude oil based products. The animal- and fish-based fuel compositions of the current invention also have significantly improved performance ability under cold conditions. These compositions may have a turbidity point of lower than 0°C, preferably lower than °C and more preferably lower than -20°C. These compositions may have a turbidity point of even -30°C or lower while simultaneously having a cetane number of 60 or higher. This differs markedly from the turbidity points presented in SE 9700149, which are considerably higher.
3480795vl
The biological raw material originating from animals, containing fatty acids and/or fatty acid esters, is processed to yield the biological component of the present application. Said biological component is obtained by hydrogenating and decomposing fatty acids and/or fatty acid esters to give hydrocarbons having carbon numbers of 6-24, typically n-paraffins as the product having a carbon number of 12 24, and isomerising the hydrocarbons, typically n-paraffins thus obtained to give isoparaffins. Typically, after the isomerisation, the iso-parafin content is more than wt-%, preferably more than 30 wt-% and more preferably more than 50 wt-%. In one embodiment of the invention the iso-paraffin content may be more than 60 wt-% or even more than 70 wt-% in said biological component.
In embodiments, the isomerised biological component (i.e. the biodiesel fuel composition) has a weight ratio of iso-paraffins to n-paraffins of less than 21:1, preferably less than any one or 20:1, 19:1. 18:1, 17:1, 16:1, 15:1, 14:1, 13:1, 12:1, 11:1, 10:1, 9:1, 8:1, 7:1, 6:1 or 5:1. Such values may include ranges of, for example, :1 to 5:1 or 15:1 to 5:1.
Examples of suitable biological raw materials are animal-based fats such as lard, tallow, train oil, and fats contained in milk, as well as recycled animal fats of the food industry and mixtures of the above.
The fuel composition can optionally further comprise a component or mixture of components produced from biological raw material originating from plants. The biological raw material originating from plants can be selected from various vegetable oils, and mixtures thereof containing fatty acids and/or fatty acid esters. Examples of suitable materials are wood-based and other plant-based fats and oils such as rapeseed oil, colza oil, canola oil, tall oil, sunflower oil, soybean oil, hempseed oil, olive oil, linseed oil, mustard oil, palm oil, peanut oil, castor oil, coconut oil, as well as fats contained in plants bred by means of gene manipulation, and recycled plant sourced fats of the food industry.
3480795vl
The basic component of a typical animal fat is triglyceride i.e. a triester of glycerol and three fatty acid molecules having the structure presented in the following formula I:
0
0 (I)
where R1, R2, and R3 are hydrocarbon chains, and R 1, R2, and R3 may be saturated or unsaturated C 6 - C 24 alkyl groups. The fatty acid composition may vary considerably in biological raw materials of different origin.
n-paraffins, iso-paraffms or mixtures thereof produced from the biological raw material may be used as a diesel fuel component in accordance with the properties desired for the diesel fuel. Fractions from Fischer-Tropsch-process typically contain high levels of n-paraffin and, optionally, they may be isomerised either simultaneously during the processing of the component of biological origin or separately therefrom, or they may be used as such.
In embodiments, the invention resides in a biodiesel fuel composition comprising at least one isomerized biological component produced by a process comprising: a) providing a feed stream of fatty acids and/or fatty acid esters derived from an animal and/or fish source; b) hydrodeoxygenating the feed stream to form n-paraffins; and c) isomerizing the n-paraffins to form iso-paraffins.
Suitably, the n-paraffins formed in step b) have carbon numbers only between 12-24.
Preferably, the composition has a turbidity point lower than -20 °C.
3480795vl
It will be appreciated that the process described is not a cracking or hydrothermal cracking process but rather one involving isomerization.
The biological component may be produced, for instance, with a process comprising at least two steps and optionally utilizing the counter-current operation principle. Before the first step the feedstock may optionally be prehydrogenated to saturate double bonds of the hydrocarbon chain, at a temperature of 100-400°C, preferably at 150-250°C. In the first hydrodeoxygenation step of the process, carried out at a temperature of 200-400°C, preferably at 250-350°C, optionally running counter current, the structure of the biological raw material is broken, compounds containing oxygen, nitrogen, phosphor and sulphur as well as light hydrocarbons as gas are removed, and thereafter, olefinic bonds are hydrogenated. In the second, isomerisation step of the process, optionally running counter-current, isomerisation is carried out to give branched hydrocarbon chains, thus improving the low temperature properties of the paraffins.
Biological raw material selected from plant oils and fats, animal fats, and mixtures thereof, containing fatty acids and/or fatty acid esters, is used as the feed stock.
High quality hydrocarbon component of biological origin, particularly useful as a component of a diesel fuel, as an iso-paraffinic solvent and as a lamp oil, is obtained as the product having a high cetane number that may even be higher than 70. A component with a turbidity point lower than -30°C and a cetane number higher than can also be achieved. Further, said hydrocarbon component of biological origin is free of aromatics. The content of naphthenes in said hydrocarbon component may be less than 30 wt-%, preferably less than 10 wt-%, more preferably less than 5 wt-% or even less than 1 wt-%. Both aromatics and naphthenes present in the hydrocarbon product decrease the cetane number and increase cold smoke during start up of the engine. The process can be adjusted according to the desired cetane number and turbidity point.
Advantages of the diesel fuel composition of the present invention include superior performance at low temperatures and an excellent cetane number compared to
3480795vl solutions of prior art using FAME-based components like RME. Problems associated with the performance at low temperatures may be avoided by isomerising waxy n paraffins having a carbon number comparable with that of fatty acids to give iso paraffins. The properties of the products thus obtained are excellent, especially with respect to diesel applications, the n-paraffins typically have cetane numbers higher than 70, and iso-paraffins higher than 60, and thus they have an improving effect on the cetane number of the diesel pool, which clearly makes them more valuable as diesel components. Moreover, the turbidity point of the isomerised product may be adjusted to the desired level, for example below -30°C, whereas the corresponding value is about 0°C for RME and more than +15°C for n-paraffins. Table 1 below compares the properties of an isomerised biological component, RME, and a commercial diesel fuel.
Table 1
Product Density Cetane Turbidity (kg/m 3) number point (°C) Isomerized biological component <800 > 60 <-30 obtained from tallow RME -880 -50 ~ 0 Diesel fuel EN 590 820-845 > 51 0 to -15
Tallow is a generic term used for fats obtained from cow, sheep (mutton or lamb) or reindeer. The tallow used in this table was obtained from Atria Finland Ltd, a Finnish meat producing company.
Fouling of engines is considerably diminished and the noise level is clearly lower when using isomerised biological component fuel composition in comparison with similar prior art fuels of biological origin containing FAME components, and further, the density of the composition is lower. The composition does not require any modifications of the automobile technology or logistics. Higher energy content per unit volume may be mentioned as a further advantage compared to RME.
3480795vl
The properties of the diesel fuel composition of biological origin according to the invention correspond to those of a high quality diesel fuel based on crude oil A composition free of aromatics can be obtained and, in contrast to FAME, it leaves no impurity residues.
Nitrogen oxide emissions due to the fuel composition of the invention are lower that those from a similar FAME-based product, and further, the particle emissions are clearly lower, and the carbon portion of the particles is smaller. These significant improvements in the emissions of the fuel composition of biological origin are environmentally very important.
Table 2 below compares the cold properties of the animal fat based product of the current invention with those exemplified by the product disclosed in Example 4 from SE 9700149.
Table 2
Feed Vegetable Fat Animal Fat Property Method Unit Example 4 from Hydrotreated SE9700149 andisomerised Density 15°C ENISO 12185 Kg/m' 770 776 Turbidity Point ASTM D5771 0C -12 -35 CFPP EN 116 Ann 0C -11 -34 Sulphur Content ASTM D5453 Mg/kg 0 <1 Cetane Number NM 353 >74 78 IQT
This Table presents the surprisingly improved results obtained for the instant invention under cold conditions. That is, the animal fat-based fuel composition of the instant invention has excellent cold properties when compared with those compositions presented in SE 9700149. Specifically, the lower turbidity point of the animal fat-based fuel composition of the instant invention affords less fuel filter plugging during cold weather operations.
3480795vl
Also, the cold filter plugging point (CFPP) indicates that the animal fat-based fuel composition of the instant invention provides trouble-free flow in fuel systems at ambient temperatures about 20°C lower as compared to the cited prior art. Most surprisingly these improved performance qualities are obtained without a decrease in the fuel ignition delay characteristics as evidenced by the instant invention's high cetane number, which is comparable to that of the prior art. It was generally thought that one cannot improve cold flow properties to these low levels without decreasing the fuel ignition delay.
The invention will now be illustrated by means of the following examples without intending to limit the scope thereof.
Example 1
Manufacture of animal fat based component:
The hydrogenation of animal fat was carried out in a fixed bed tube reactor. The animal fat was Atria tallow as used earlier in table 1. The hydrogenation reaction was carried out in the presence of NiMo catalyst under a pressure of 50 bars, with WHSV of 1 -2 1/h and at a reaction temperature from 250 to 300°C. Hydrogen to oil ratio was 500 - 1500 normal liters H 2 per liter oil fed. The hydrogenated product oil contained no oxygen compounds.
Isomerisation of the above-obtained hydrogenated animal fat was carried out in a fixed bed tube reactor in the presence of Pt-SAPO-catalyst under a pressure of 40 bars, with WHSV of 1.5 1/h and at a reaction temperature of 328°C. Hydrogen to oil ratio was 300 normal liters H 2 per liter oil fed.
Low temperature properties of the obtained animal fat based component are presented in the Table 3 below.
3480795vl
Table 3
Feed Animal fat Property Method Hydrotreated and isomerized Density/ 15°C/k g/m 3 ENISO 12185 776
Turbidity point / °C ASTM D5771 - 35 CFPP / °C EN116 Ann -34 Sulphur / mg/kg ASTM D5453 <1
Cetane number / IQT NM 353 78
Example 2
Composition containing 20 wt-% of animal fat based component and 80 wt-% crude oil based diesel component.
The hydrogenated and isomerised animal fat component (biocomponent) produced in example 1 was blended to crude oil based diesel component (European diesel fuel EN590) in amounts of biocomponent 20 wt-% and EN590 80 wt-%. Table 4 below shows the characteristics of the obtained product and the components.
Table 4
Component/Product Animal fat Crude oil Blend Property Method Hydrotreated Diesel fuel 20 wt-% diesel and component from animal fat isomerised and 80 wt-% crude oil diesel Density/15°C/kg/m3 ENISO 776 829 818 12185 Turbidity point / °C ASTM -35 -29 -31 D5771 CFPP/°C EN 116 -34 -43 -44 Ann Sulphur / mg/kg ASTM <1 <5 <5 D5453 Cetane number / NM 353 78 51 (engine) 58 IQT
3480795vl
Example 3
Composition containing 20 wt-% of animal fat based component and 80 wt-% crude oil based diesel component blended with 5 wt-% of oxygen containing component.
The hydrogenated and isomerised animal fat component (biocomponent) pro duced in example 1 was blended to crude oil based diesel component (European diesel fuel EN590) in amounts of biocomponent 20 wt-% and EN590 80 wt-%. To this blend 5 wt % of oxygen containing component (RME= rapeseed oil fatty acid ester) was blended. The characteristics of the blend and of the obtained product are provided in table 5a, below, while table 5b indicates the 'i/n' ratio of iso-paraffin content to n-paraffin content of the product:
Table 5a
Component/Product Property Method Blend Blend + RME 20 wt-% diesel from Blend + 5 wt% animal fat and 80 wt-% RME crude oil diesel Density / 15°C / kg/m3 ENISO 818 821 12185 Turbidity point / °C ASTM -31 -30 D5771 CFPP /°C EN 116 -44 -43 Ann Sulphur / mg/kg ASTM <5 5 D5453 Cetane number /IQT NM 353 58 58
3480795vl
Table 5b
iso-paraf. n-paraf. In wt-% In wt-% C13 1.9 0-A C14 3.1 0.58 C15 10.0 1.3 C16 17.3 2.0 C17 24.7 1.9 C18 26.2 3.3 C19 0.74 0.06 C20 0.35 0.04 C21 0.07 0.01 C22 0.05 0.01 C23 0.02 <0.01 C24 0.01 <0.01
total 84.5 9.6 i/n 8.8 Values measured from the AF paraffins by GC.
Comparative Example 4
The following Table 6 compares the emission characteristics of a conventional diesel fuel used in Europe in summer, EN 590 (DI), to those of a composition containing 60 % by volume of hydrogenated and isomerised tall oil (TOFA), and 40 % by volume of the European summer diesel fuel EN 590. Table 6
Characteristic Unit 60 % b.v. TOFA + 40 % b.v. DI DI
Turbidity point 0C -15 -8
Cetane number - 61.2 55.9 Aromatics % b.w. 8.7 19.2 Total aromatics (IP391) % b.v. 9.1 20.0 Polyaromatics (IP391) % b.v. 0.8 1.6 n-paraffms % b.w. 14.7 24.5 i-paraffins % b.w. 34.2 26.1 Naphtenes % b.w. 42.4 30.2
3480795vl b.w. =by weight b.v. =by volume
Comparative Example 5
Table 7 below compares the emission characteristics of a high quality reformed crude oil based diesel fuel available on the Finnish market (DITC, produced by Fortum Oyj), to those of compositions containing 30 % by volume of hydrogenated and isomerised tall oil (TOFA), and 70 % by volume of DITC, or containing 30 % by volume of tall oil methyl ester (MME), and 70 % by volume of DITC.
Table 7
Characteristic 30 %b.v. TOFA + 30 % b.v. MME
+ Unit DITC 70 %b.v. DITC 70 % b.v. DITC Cetane number - 51 57 48 NO, emissions % -1 to -4 +3 (compared to DITC) Particles % -3 +22 - carbon % -10 to -30 0 to -10 - PAH % 0 +0 Combustion noise - decreases +0
b.v. = by volume
Although the fuel composition of Examples 4 and 5 do not directly demonstrate the present invention as the compositions do not contain isomerised animal based biological material, the compositions can be blended with the biocomponent of Example 1 to provide a useful fuel composition.
The Atria tallow used in the examples and listed in Tables 1 and 3 was obtained from Atria Finland Ltd. The tallow was solid at room temperature and was purified before hydrogenation and isomerisation. It was purified by washing with an alkali solution and by diatomaceous earth filtration. The Atria tallow was analysed and has the following characteristics:
3480795vl
Table 8: Atria Tallow: Fatty acid distribution
Chain length: double bonds
% C14:0 2.32 C14:1 0.36 C15:0 0.17 C16:0 25.47 C16:1 2.29 C16:2 0.10 C16:3 1.68 C17:0 0.48 C17:1 0 C18:0 23.55 C18:1 34.88 C18:2 4.68 C18:3 0.59 C19:0 0.28 C19:1 0.14 C20:0 0.27 C20:1 0.57 C20:2 0.17 C20:3 0 C22:0 0.04 unknown 1.90 TOTAL 100.0
Table 9: Atria Tallow :Carbon number distribution
Chain Length %
C14 2.68 C15 0.17 C16 27.86 C17 2.16 C18 63.69 C19 0.43 C20 1.01 C22 0.08 C23 0.01 C24 0 C25 0 C26 0 unknown 1.90 TOTAL 100.00
3480795v1
Table 10: Atria Tallow: Properties
Property Atria Tallow Density 15 °C 911.9 kg/m3 Density 50 °C 888.9 kg/rn 3 Sulphur 5.4 ppm Nitrogen 3 ppm Br-number 24 g/100g Iodine number 47 Free fatty acids 1.00 mg KOH/g (TAN) sapo.number Water 0.05%
Table 11: Atria Tallow : GPC Analysis
GPC Analysis Atria Tallow Oligomers 0 Triglycerides 99.4% Diglycerides 0 Monoglycerides 0 Carboxylic acids 0.6%
Table 12: Atria Tallow : Elemental Analysis
Metals (ICP) Atria Tallow Aluminium <2 Barium <1 Calcium <1 Chromium <1 Copper <1 Iron <1 Magnesium <1 Manganese <1 Sodium <2 Nickel <1 Phosphorous <1 Lead <1 Silicon <1 Vanadium <1 Zinc <1
3480795v1
Throughout this specification and the claims which follow, unless the context requires otherwise, the word "comprise", and variations such as "comprises" and "comprising", will be understood to imply the inclusion of a stated integer or step or group of integers or steps but not the exclusion of any other integer or step or group of integers or steps.
The reference to any prior art in this specification is not, and should not be taken as, an acknowledgment or any form of suggestion that the prior art forms part of the common general knowledge.
3480795vl
Other embodiments of the invention as described herein are defined in the following paragraphs:
1. Fuel composition for diesel engines, characterized in that the fuel composition comprises: a) 0.1-99 % by volume of a component or a mixture of components produced from biological raw material originating from plants and/or animals and/or fish by hydrogenating and decomposing fatty acids and/or fatty acid esters to give a hydrocarbon, which is optionally isomerized; b) 0-20 % by volume of components containing oxygen; both components a) and b) being mixed as an emulsion or dissolved in diesel components based on crude oil and/or fractions from Fischer-Tropsch process.
2. Fuel composition of paragraph 1, characterized in that the fuel composition comprises 0.1-80 % by volume of a component or a mixture of components produced from biological raw material originating from plants and/or animals and/or fish.
3. Fuel composition of paragraph 1 or 2, characterized in that the product obtained from the biological raw material is isomerized.
4. Fuel composition of any of the above paragraphs 1-3, characterized in that the bio logical raw material is selected from the group consisting of vegetable oils, animal fats, fish oils and mixtures thereof.
5. Fuel composition of any of the above paragraphs 1-4, characterized in that the biological raw material is a wood-based or other plant-based fat or oil, a fat contained in plants bred by means of gene manipulation, an animal-based fat, a fat contained in milk, a recycled fat of the food industry or a mixture of the above.
6. Fuel composition of paragraph 5, characterized in that the biological raw material is rapeseed oil, colza oil, canola oil, tall oil, sunflower oil, soybean oil, hempseed oil, olive oil, linseed oil, mustard oil, palm oil, peanut oil, castor oil, coconut oil, lard, tallow, or train oil.
7. Fuel composition of any of the above paragraphs 1-6, characterized in that the components containing oxygen are selected from the group consisting of aliphatic alcohols, ethers, fatty acid esters, water, and mixtures containing the same.
8. Fuel composition of any of the above paragraphs 1-7, characterized in that the component produced from biological raw material originating from plants, animals or fish is obtained by hydrogenating and decomposing fatty acids and/or fatty acid esters to given paraffin as the product having a carbon number of 12-24, and by isomerizing the n-paraffin thus obtained to give iso-paraffin.
Still further embodiments are within the scope of the following claims.
Claims (23)
1. A diesel fuel composition comprising at least one isomerized biological component produced by a process comprising: (1) providing a feed stream of fatty acids having saturated or unsaturated C6 C24 hydrocarbon chains, fatty acid esters having saturated or unsaturated C6-C24 hydrocarbon chains, or both, derived from at least one biological raw material; (2) hydrodeoxygenating the feed stream to form n-paraffins having carbon numbers in the C6-C24 range; and (3) isomerizing the n-paraffins to form an isomerized biological component comprising iso-paraffins, wherein the isomerized biological component is suitable for use as a diesel fuel for a diesel engine, has a cetane number higher than 60, a turbidity point lower than -30 °C, and is free of aromates.
2. A diesel fuel composition according to claim 1, wherein the isomerized biological component has a density less than crude oil based conventional diesel fuel or a density less than rapeseed oil methyl ester based fuel.
3. A diesel fuel composition according to claim 1 or claim 2, wherein the biological raw material is chosen from animal-based material, plant-based material, fish-based material and mixtures thereof.
4. A diesel fuel composition according to claim 1 or claim 2, wherein the biological raw material is chosen from vegetable oils, animal fats, fish oils, and mixtures thereof.
5. A diesel fuel composition according to claim 1 or claim 2, wherein the biological raw material is chosen 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.
6. A diesel fuel composition according to any one of claims I to 5, wherein the diesel fuel composition leaves no impurity residues.
7. A diesel fuel composition comprising at least one hydrodeoxygenated and isomerized biological component wherein the hydrodeoxygenated and isomerized biological component is suitable for use as a diesel fuel for a diesel engine, has a cetane number higher than 60, a turbidity point lower than -30 °C, is free of aromates, and is produced by hydrodeoxygenating and isomerizing a feed stream of fatty acids having saturated or unsaturated C6-C24 hydrocarbon chains, fatty acid esters having saturated or unsaturated C6-C24 hydrocarbon chains, or both, derived from at least one biological raw material.
8. A diesel fuel composition according to claim 7, wherein the hydrodeoxygenated and isomerized biological component has a density less than crude oil based conventional diesel fuelor a density less than rapeseed oil methyl ester based fuel.
9. A diesel fuel composition according to claim 7 or claim 8, wherein the biological raw material is chosen from animal-based material, plant-based material, fish-based material and mixtures thereof.
10. A diesel fuel composition according to claim 7 or claim 8, wherein the biological raw material is chosen from vegetable oils, animal fats, fish oils, and mixtures thereof.
11. A diesel fuel composition according to claim 7 or claim 8, wherein the biological raw material is chosen 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.
12. A diesel fuel composition according to any one of claims 7 to 11, wherein the fuel composition leaves no impurity residues.
13. A diesel fuel composition according to any one of claims 1 to 12, comprising a measurable amount of 14C.
14. An isomerized biological component for diesel fuel produced by a process comprising: (1) providing a feed stream of fatty acids having saturated or unsaturated C6 C24 hydrocarbon chains, fatty acid esters having saturated or unsaturated C6-C24 hydrocarbon chains, or both, derived from at least one biological raw material; (2) hydrodeoxygenating the feed stream to form n-paraffins having carbon numbers in the C6-C24 range; and (3) isomerizing the n-paraffins to form an isomerized biological component comprising iso-paraffins, wherein the at least one biological raw material is chosen from animal-based material, plant-based material, fish-based material or mixtures thereof, and wherein the isomerized biological component is suitable for use as a diesel fuel for a diesel engine, has a cetane number higher than 60, a turbidity point lower than -30 °C, is free of aromates, has a density less than rapeseed oil methyl ester based fuel, and leaves no impurity residues.
15. An isomerized biological component according to claim 14, having a density less than crude oil based conventional diesel fuel.
16. An isomerized biological component for diesel fuel produced by a process comprising: (1) providing a feed stream of fatty acids having saturated or unsaturated C6-C24 hydrocarbon chains, fatty acid esters having saturated or unsaturated C6-C24 hydrocarbon chains, or both, derived from at least one biological raw material; (2) hydrodeoxygenating the feed stream to form n-paraffins having carbon numbers in the C6-C24range; and (3) isomerizing the n-paraffins to form an isomerized biological component comprisingiso-paraffins, wherein the isomerized biological component is suitable for use as a diesel fuel for a diesel engine, has a cetane number higher than 60 and a turbidity point lower than -30 °C.
17. An isomerized biological component according to claim 16, wherein the isomerized biological component is free of aromates.
18. An isomerized biological component according to claim 16 or claim 17, wherein the isomerized biological component has a density less than crude oil based conventional diesel fuel.
19. An isomerized biological component according to any one of claims 16 to 18, wherein the biological raw material is chosen from animal-based material, plant-based material, fish-based material and mixtures thereof.
20. An isomerized biological component according to any one of claims 16 to 18, wherein the biological raw material is chosen from vegetable oils, animal fats, fish oils, and mixtures thereof.
21. An isomerized biological component according to any one of claims 16 to 18, wherein the biological raw material is chosen 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.
22. An isomerized biological component according to any one of claims 16 to 21, wherein the isomerized biological component leaves no impurity residues.
23. An isomerized biological component according to any one of claims 14 to 22, 14 comprising a measurable amount of C.
Date: 13 August 2020
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2020203806A AU2020203806B2 (en) | 2002-09-06 | 2020-06-09 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids |
Applications Claiming Priority (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20021596 | 2002-09-06 | ||
FI20021596A FI20021596A (en) | 2002-09-06 | 2002-09-06 | Diesel Engine Fuel Composition |
AU2003258753A AU2003258753C1 (en) | 2002-09-06 | 2003-09-04 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposition fatty acids |
AU2010200726A AU2010200726A1 (en) | 2002-09-06 | 2010-02-26 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposition fatty acids |
AU2015205854A AU2015205854B2 (en) | 2002-09-06 | 2015-07-21 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposition fatty acids |
AU2017279689A AU2017279689B2 (en) | 2002-09-06 | 2017-12-20 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids |
AU2020203806A AU2020203806B2 (en) | 2002-09-06 | 2020-06-09 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU2017279689A Division AU2017279689B2 (en) | 2002-09-06 | 2017-12-20 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids |
Publications (2)
Publication Number | Publication Date |
---|---|
AU2020203806A1 AU2020203806A1 (en) | 2020-07-02 |
AU2020203806B2 true AU2020203806B2 (en) | 2022-05-26 |
Family
ID=8564542
Family Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU2003258753A Expired AU2003258753C1 (en) | 2002-09-06 | 2003-09-04 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposition fatty acids |
AU2010200726A Abandoned AU2010200726A1 (en) | 2002-09-06 | 2010-02-26 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposition fatty acids |
AU2020203806A Expired AU2020203806B2 (en) | 2002-09-06 | 2020-06-09 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids |
Family Applications Before (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU2003258753A Expired AU2003258753C1 (en) | 2002-09-06 | 2003-09-04 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposition fatty acids |
AU2010200726A Abandoned AU2010200726A1 (en) | 2002-09-06 | 2010-02-26 | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposition fatty acids |
Country Status (10)
Country | Link |
---|---|
EP (1) | EP1546288A1 (en) |
JP (1) | JP2005538204A (en) |
CN (1) | CN1688673A (en) |
AU (3) | AU2003258753C1 (en) |
BR (1) | BR0314100A (en) |
CA (1) | CA2499489C (en) |
FI (1) | FI20021596A (en) |
MY (1) | MY139714A (en) |
RU (1) | RU2348677C2 (en) |
WO (1) | WO2004022674A1 (en) |
Families Citing this family (47)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1686165A1 (en) * | 2005-02-01 | 2006-08-02 | Gibson Chemical Corporation | Method for manufacturing bio-diesel oil containing alkane compounds |
CA2601708A1 (en) | 2005-03-21 | 2006-09-28 | Ben-Gurion University Of The Negev Research & Development Authority | Production of diesel fuel from vegetable and animal oils |
US8022258B2 (en) | 2005-07-05 | 2011-09-20 | Neste Oil Oyj | Process for the manufacture of diesel range hydrocarbons |
EP2881453A1 (en) * | 2005-12-12 | 2015-06-10 | Neste Oil Oyj | Process for producing a hydrocarbon component |
FI20055665L (en) * | 2005-12-12 | 2007-06-13 | Neste Oil Oyj | A process for making a branched hydrocarbon component |
EP2006360B1 (en) | 2006-03-31 | 2013-05-22 | JX Nippon Oil & Energy Corporation | Method of producing a gas oil composition |
JP4829660B2 (en) | 2006-03-31 | 2011-12-07 | Jx日鉱日石エネルギー株式会社 | Fuel composition |
EP2022839A4 (en) * | 2006-05-17 | 2013-07-31 | Nippon Mitsubishi Oil Corp | Gas-oil composition |
JP4916219B2 (en) * | 2006-05-17 | 2012-04-11 | Jx日鉱日石エネルギー株式会社 | Method for producing A heavy oil composition |
JP4863772B2 (en) * | 2006-05-31 | 2012-01-25 | Jx日鉱日石エネルギー株式会社 | Light oil composition |
FI121425B (en) * | 2006-06-14 | 2010-11-15 | Neste Oil Oyj | Process for the production of base oil |
US8067653B2 (en) * | 2006-07-14 | 2011-11-29 | The Governors Of The University Of Alberta | Methods for producing fuels and solvents |
US7897824B2 (en) | 2006-08-16 | 2011-03-01 | Energy & Environmental Research Center Foundation | Optimal energy pathway to renewable domestic and other fuels |
ITMI20062193A1 (en) * | 2006-11-15 | 2008-05-16 | Eni Spa | PROCESS FOR PRODUCING HYDROCARBURAL FRACTIONS FROM MIXTURES OF BIOLOGICAL ORIGIN |
WO2008117856A1 (en) | 2007-03-28 | 2008-10-02 | Nippon Oil Corporation | Gas oil composition |
WO2008138861A1 (en) | 2007-05-11 | 2008-11-20 | Shell Internationale Research Maatschappij B.V. | Fuel composition |
US8523959B2 (en) | 2007-07-26 | 2013-09-03 | Chevron U.S.A. Inc. | Paraffinic biologically-derived distillate fuels with bio-oxygenates for improved lubricity and methods of making same |
WO2009020056A1 (en) * | 2007-08-08 | 2009-02-12 | Nippon Oil Corporation | Gas oil composition |
JP5288741B2 (en) * | 2007-08-08 | 2013-09-11 | Jx日鉱日石エネルギー株式会社 | Method for producing light oil composition |
JP5288742B2 (en) * | 2007-08-08 | 2013-09-11 | Jx日鉱日石エネルギー株式会社 | Method for producing light oil composition |
JP2009126935A (en) * | 2007-11-22 | 2009-06-11 | Showa Shell Sekiyu Kk | Light oil fuel composition |
US8551327B2 (en) | 2007-12-27 | 2013-10-08 | Exxonmobil Research And Engineering Company | Staged co-processing of biofeeds for manufacture of diesel range hydrocarbons |
US8247632B2 (en) | 2008-11-04 | 2012-08-21 | Energy & Environmental Research Center Foundation | Process for the conversion of renewable oils to liquid transportation fuels |
US8309783B2 (en) | 2008-11-04 | 2012-11-13 | Energy & Environmental Research Center Foundation | Process for the conversion of renewable oils to liquid transportation fuels |
FR2940314B1 (en) * | 2008-12-23 | 2011-11-18 | Total Raffinage Marketing | GASOLINE FUEL FOR DIESEL ENGINE HAVING HIGH CARBON CONTENT OF RENEWABLE ORIGIN AND OXYGEN |
US8785701B2 (en) * | 2008-12-24 | 2014-07-22 | Exxonmobil Research And Engineering Company | Co-processing of diesel biofeed and kerosene range hydrocarbons |
US8632675B2 (en) | 2008-12-24 | 2014-01-21 | Exxonmobil Research And Engineering Company | Co-processing of diesel biofeed and heavy oil |
EP2440328B1 (en) | 2009-06-12 | 2016-08-17 | Albemarle Europe Sprl. | Sapo molecular sieve catalysts and their preparation and uses |
HU231091B1 (en) | 2009-09-30 | 2020-07-28 | Mol Magyar Olaj- És Gázipari Nyilvánosan Működő Részvénytársaság | Fuels and fuel additives for combustion engines and method for producing them |
IT1396939B1 (en) | 2009-12-09 | 2012-12-20 | Eni Spa | USEFUL HYDROCARBURIC COMPOSITION AS FUEL OR FUEL |
US8853474B2 (en) | 2009-12-29 | 2014-10-07 | Exxonmobil Research And Engineering Company | Hydroprocessing of biocomponent feedstocks with low purity hydrogen-containing streams |
FI125632B (en) * | 2010-05-25 | 2015-12-31 | Upm Kymmene Corp | Method and apparatus for producing hydrocarbons |
EP2514803B1 (en) | 2011-04-21 | 2017-02-01 | Infineum International Limited | Improvements in fuel oils |
RU2466180C1 (en) * | 2011-08-09 | 2012-11-10 | Закрытое акционерное общество "Центральный ордена Трудового Красного Знамени научно-исследовательский и проектно-конструкторский институт морского флота" | Masout additive |
FI20110300A0 (en) | 2011-09-11 | 2011-09-11 | Neste Oil Oyj | PETROL COMPOSITIONS AND METHOD FOR THE MANUFACTURE THEREOF |
US8884086B2 (en) | 2011-09-14 | 2014-11-11 | Bp Corporation North America Inc. | Renewable diesel refinery strategy |
RU2544239C2 (en) * | 2012-11-19 | 2015-03-20 | Общество с ограниченной ответственностью "РЕЦИКЛ" | Biofuel composition |
CN105255525A (en) * | 2015-09-21 | 2016-01-20 | 广州畅营环保科技有限公司 | Environmentally-friendly biological blended fuel |
FI127886B (en) * | 2016-12-19 | 2019-04-30 | Neste Oyj | A multicomponent diesel composition |
FI127887B (en) * | 2016-12-19 | 2019-04-30 | Neste Oyj | A multicomponent diesel composition |
FI127307B (en) * | 2017-01-27 | 2018-03-15 | Neste Oyj | Refined fuel compositions and methods for their preparation |
US11084998B2 (en) * | 2017-02-21 | 2021-08-10 | Exxonmobil Research And Engineering Company | Diesel boiling-range fuel blend and methods of making the same |
FI130601B (en) | 2018-12-14 | 2023-12-07 | Neste Oyj | Diesel fuel composition |
CN110499178A (en) * | 2019-08-27 | 2019-11-26 | 易高生物化工科技(张家港)有限公司 | A kind of method that waste animal and vegetable oil adds hydrogen to prepare atoleine |
FR3119625B1 (en) * | 2021-07-02 | 2023-02-17 | Totalenergies Marketing Services | Composition of fuel rich in aromatic compounds, paraffins and ether, and its use in motor vehicles |
BR102021016123A2 (en) * | 2021-08-16 | 2023-02-23 | Petróleo Brasileiro S.A. - Petrobras | PROCESS FOR BIODIESEL PRODUCTION FROM ACID CARDS |
AU2022368915A1 (en) * | 2021-10-20 | 2024-04-04 | Shell Internationale Research Maatschappij B.V. | Biofuel blends with improved oxidation stability and lubricity |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE9700149L (en) * | 1996-02-05 | 1997-08-06 | Neste Oy | Preparation of intermediate distillate |
US5705722A (en) * | 1994-06-30 | 1998-01-06 | Natural Resources Canada | Conversion of biomass feedstock to diesel fuel additive |
US5814109A (en) * | 1997-02-07 | 1998-09-29 | Exxon Research And Engineering Company | Diesel additive for improving cetane, lubricity, and stability |
WO2001049812A1 (en) * | 1999-12-29 | 2001-07-12 | Chevron U.S.A. Inc. | A diesel fuel having a very high iso-paraffin to normal paraffin mole ratio |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4992605A (en) * | 1988-02-16 | 1991-02-12 | Craig Wayne K | Production of hydrocarbons with a relatively high cetane rating |
FI102767B1 (en) * | 1997-05-29 | 1999-02-15 | Neste Oy | Process for the production of high quality diesel fuel |
US6787022B1 (en) * | 2000-05-02 | 2004-09-07 | Exxonmobil Research And Engineering Company | Winter diesel fuel production from a fischer-tropsch wax |
BR0110475A (en) * | 2000-05-02 | 2003-04-01 | Exxonmobil Res & Eng Co | Fuel usable as a diesel fuel, and, smoke reduction method during operation of a diesel engine |
-
2002
- 2002-09-06 FI FI20021596A patent/FI20021596A/en not_active Application Discontinuation
-
2003
- 2003-09-04 CN CNA038238381A patent/CN1688673A/en active Pending
- 2003-09-04 AU AU2003258753A patent/AU2003258753C1/en not_active Expired
- 2003-09-04 CA CA2499489A patent/CA2499489C/en not_active Expired - Lifetime
- 2003-09-04 BR BR0314100-4A patent/BR0314100A/en not_active Application Discontinuation
- 2003-09-04 WO PCT/FI2003/000648 patent/WO2004022674A1/en active Application Filing
- 2003-09-04 JP JP2004533535A patent/JP2005538204A/en active Pending
- 2003-09-04 RU RU2005109935/04A patent/RU2348677C2/en not_active IP Right Cessation
- 2003-09-04 EP EP03793834A patent/EP1546288A1/en not_active Ceased
- 2003-09-05 MY MYPI20033369A patent/MY139714A/en unknown
-
2010
- 2010-02-26 AU AU2010200726A patent/AU2010200726A1/en not_active Abandoned
-
2020
- 2020-06-09 AU AU2020203806A patent/AU2020203806B2/en not_active Expired
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5705722A (en) * | 1994-06-30 | 1998-01-06 | Natural Resources Canada | Conversion of biomass feedstock to diesel fuel additive |
SE9700149L (en) * | 1996-02-05 | 1997-08-06 | Neste Oy | Preparation of intermediate distillate |
US5814109A (en) * | 1997-02-07 | 1998-09-29 | Exxon Research And Engineering Company | Diesel additive for improving cetane, lubricity, and stability |
WO2001049812A1 (en) * | 1999-12-29 | 2001-07-12 | Chevron U.S.A. Inc. | A diesel fuel having a very high iso-paraffin to normal paraffin mole ratio |
Also Published As
Publication number | Publication date |
---|---|
AU2003258753C1 (en) | 2012-06-14 |
CA2499489A1 (en) | 2004-03-18 |
AU2020203806A1 (en) | 2020-07-02 |
FI20021596A (en) | 2004-03-07 |
PL375038A1 (en) | 2005-11-14 |
FI20021596A0 (en) | 2002-09-06 |
JP2005538204A (en) | 2005-12-15 |
MY139714A (en) | 2009-10-30 |
WO2004022674A1 (en) | 2004-03-18 |
EP1546288A1 (en) | 2005-06-29 |
RU2348677C2 (en) | 2009-03-10 |
CN1688673A (en) | 2005-10-26 |
AU2003258753B2 (en) | 2008-12-04 |
RU2005109935A (en) | 2005-08-27 |
AU2010200726A1 (en) | 2010-03-18 |
BR0314100A (en) | 2005-07-19 |
AU2003258753A1 (en) | 2004-03-29 |
CA2499489C (en) | 2013-04-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2020203806B2 (en) | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids | |
US11384290B2 (en) | Fuel composition for a diesel engine | |
EP1398364A1 (en) | Fuel composition for a diesel engine | |
JP5616784B2 (en) | Process for producing branched hydrocarbons | |
KR101016643B1 (en) | Process for the manufacture of hydrocarbons | |
US20090145392A1 (en) | Fuel formulations | |
US8935994B2 (en) | Gasoline compositions and method of producing the same | |
AU2017279689B2 (en) | Diesel fuel composition, comprising components based on biological raw material, obtained by hydrogenating and decomposing fatty acids | |
CN113166663B (en) | Diesel fuel composition | |
Campus | VIABILITY OF BIOFUEL AS ALTERNATIVE FUEL IN NIGERIA TRANSPORT SYSTEM | |
PL203610B1 (en) | Fuel mixture for diesel engines containing components based on biological raw material obtained in the process of hydrogenation and decomposition of fatty acids |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FGA | Letters patent sealed or granted (standard patent) | ||
MK14 | Patent ceased section 143(a) (annual fees not paid) or expired |