US20060225339A1 - Process for producing low sulphur and high cetane number petroleum fuel - Google Patents
Process for producing low sulphur and high cetane number petroleum fuel Download PDFInfo
- Publication number
- US20060225339A1 US20060225339A1 US11/102,867 US10286705A US2006225339A1 US 20060225339 A1 US20060225339 A1 US 20060225339A1 US 10286705 A US10286705 A US 10286705A US 2006225339 A1 US2006225339 A1 US 2006225339A1
- Authority
- US
- United States
- Prior art keywords
- fuel
- set forth
- cetane number
- further including
- additive
- 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.)
- Abandoned
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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/12—Use of additives to fuels or fires for particular purposes for improving the cetane number
-
- 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
- C10L1/103—Liquid carbonaceous fuels containing additives stabilisation of anti-knock agents
-
- 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
- C10L1/1208—Inorganic compounds elements
-
- 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
- C10L1/1266—Inorganic compounds nitrogen containing compounds, (e.g. NH3)
-
- 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
- C10L1/1811—Organic compounds containing oxygen peroxides; ozonides
-
- 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
-
- 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
- C10L1/22—Organic compounds containing nitrogen
- C10L1/23—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
-
- 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
- C10L1/22—Organic compounds containing nitrogen
- C10L1/23—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
- C10L1/231—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
Definitions
- the present invention relates to a process for reducing Sulphur content in petroleum fuel, such as diesel, and raising the Cetane Number higher than 50.
- Cetane Number is an indication of the ignition quality of a diesel fuel. It is a relative measure of the interval between the beginning of injection and auto ignition of the fuel. This is the time period between the start of injection and start of combustion (ignition) of the fuel. The higher the number, the shorter the delay interval.
- Sulfur is directly related to corrosion in engines.
- Salazar U.S. Pat. No. 5,770,047 to Salazar, et al., discloses a process for producing reformulated gasoline by reducing sulfur, nitrogen and olefin.
- the process includes conatcting fuel with a catalytically metalic active matrix inclduing two metals, a support medium distributed through the matrix having a silicious molecular sieve, mixing the fuel with acid.
- the process is done under hydrogen temperature and pressure.
- U.S. Pat. No. 4,088,566 discloses a process for producing low sulfur petroleum fuel.
- the process comprises contacting the fuel with oxygen-containing gas, mixing the fuel with acid and neutralizing the acid with base.
- the process requires high temperature of about 400 degrees to 675 degree Fahrenheit. However, the process requires high temperatures.
- Schmidt U.S. Pat. No. 4,806,232, discloses a process for reducing sulfur content of fuel. The process includes the steps of adding metal to the fuel and heating the fuel mixture without oxygen at a temperature of about 500 degrees C. Schmidt's process, however, requires high temperature and pressure.
- An additional object of the invention is to provide for a process for reducing sulphur and raising Cetane Number of a petroleum fuel at an atmospheric pressure and low temperature.
- An additional object of the invention is to provide for a process for reducing sulphur content of petroleum fuel by mixing fuel with aluminium.
- a still further object of the invention is to provide for a process for reducing sulphur content of petroleum fuel by at least 50%.
- the present invention discloses a process for desulfurizing petroleum fuel and raising Cetane Number comprising providing petroleum fuel; adding at least one acid source to said fuel, preferably oxidizing said acid; adding aluminium to said fuel; heating the mixture to about preferably between 80 to 100 degrees C.; adding at least one base source, water, sodium, bicarbonate at a temperature range preferably about 100 to 120 degrees C.; separating fuel form water, and adding at least one additive to raise the Cetane Number such as alcohol and preferably methanol, alkyl esters of inorganic acids and preferably alkyl nitrate, peroxides and combinations thereof.
- the present invention relates to a process for producing low sulphur and high Cetane Number petroleum fuel.
- the process includes preferably two phases.
- the first phase includes receiving petroleum fuel to be treated.
- the fuel temperature is preferably 80 to 100 degrees C.
- the fuel is then mixed with an acid source, preferably sulphuric acid or any other acid.
- the process may be done in the presence of oxygen.
- the fuel is mixed with a metal and preferably aluminium and preferably in solid state.
- the pressure could be an atmospheric pressure.
- This phase may take an average of about between 8 to 12 hours depending on the level of sulphur in the fuel and the quantity of fuel being treated.
- the fuel is mixed with a base source, such as sodium hydroxide or any other basic compound, and/ or salt, such as sodium bicarbonate, in order to neutralize the acid.
- a base source such as sodium hydroxide or any other basic compound
- salt such as sodium bicarbonate
- the fuel should be heated to a temperature of preferably about 100 to 120 degrees C.
- the fuel should be mixed well.
- the process can be performed at an atmospheric pressure. This phase may take about 3 to 4 hours.
- the resulting fuel is sent to a separator where fuel naturally separates from water.
- At least one additive is added to the fuel.
- the at least one additive is preferably an alcohol, such as methanol, alkyl esters of inorganic acids, such as alkyl nitrate, butyl nitrate, amyl nitrate, isobutyl nitrate, and the likes, and peroxides, and combinations thereof.
- the present process reduces sulphur content by about at least 50% and raises the Cetane Number higher than 50.
- the present process is simple and inexpensive treatment of petroleum fuel to improve its ignition quality and provide cleaner fuel.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A process is disclosed for producing low sulfur and high Cetane Number petroleum fuel, the process comprises providing fuel, adding acid source, aluminum, base source, heating the mixture, separating fuel from water, and adding at least one additive in order to raise the Cetane Number.
Description
- The present invention relates to a process for reducing Sulphur content in petroleum fuel, such as diesel, and raising the Cetane Number higher than 50.
- Cetane Number is an indication of the ignition quality of a diesel fuel. It is a relative measure of the interval between the beginning of injection and auto ignition of the fuel. This is the time period between the start of injection and start of combustion (ignition) of the fuel. The higher the number, the shorter the delay interval.
- Low Cetane Numbers will likely cause hard starting, rough operation, noise and exhaust smoke. Generally, diesel engines will operate better on fuels with Cetane Numbers above 50 compared to fuels with Cetane Numbers of U.S. national average of approximately 45.
- It is also desirable to have a low Sulfur content. Sulfur is directly related to corrosion in engines.
- Those skilled in the art have long sought producing fuel with higher Cetane Number and low Sulfur content. For example, Salazar, U.S. Pat. No. 5,770,047 to Salazar, et al., discloses a process for producing reformulated gasoline by reducing sulfur, nitrogen and olefin. The process includes conatcting fuel with a catalytically metalic active matrix inclduing two metals, a support medium distributed through the matrix having a silicious molecular sieve, mixing the fuel with acid. The process is done under hydrogen temperature and pressure.
- However, Salazar does not disclose use of aluminum and additives to raise Cetane Number. Salazar's process is also complicated because it requires use of specially designed catalytic matrix.
- Mead, U.S. Pat. No. 4,088,566 discloses a process for producing low sulfur petroleum fuel. The process comprises contacting the fuel with oxygen-containing gas, mixing the fuel with acid and neutralizing the acid with base. The process requires high temperature of about 400 degrees to 675 degree Fahrenheit. However, the process requires high temperatures.
- Schmidt, U.S. Pat. No. 4,806,232, discloses a process for reducing sulfur content of fuel. The process includes the steps of adding metal to the fuel and heating the fuel mixture without oxygen at a temperature of about 500 degrees C. Schmidt's process, however, requires high temperature and pressure.
- One particular disadvantage with the prior art is that the processes require especially designed matrixes and high operation temperature and pressure.
- Another disadvantage is these refining processes are complicated and expensive.
- It is an object of this invention to provide for a simple and inexpensive process for reducing sulfur content and raising Cetane Number.
- An additional object of the invention is to provide for a process for reducing sulphur and raising Cetane Number of a petroleum fuel at an atmospheric pressure and low temperature.
- An additional object of the invention is to provide for a process for reducing sulphur content of petroleum fuel by mixing fuel with aluminium.
- A still further object of the invention is to provide for a process for reducing sulphur content of petroleum fuel by at least 50%.
- It is still another object of the invention to provide for a process for raising Cetane Number of petroleum fuel using simple additives such as methanol.
- The above-listed objects are met or exceeded by the present invention. The present invention discloses a process for desulfurizing petroleum fuel and raising Cetane Number comprising providing petroleum fuel; adding at least one acid source to said fuel, preferably oxidizing said acid; adding aluminium to said fuel; heating the mixture to about preferably between 80 to 100 degrees C.; adding at least one base source, water, sodium, bicarbonate at a temperature range preferably about 100 to 120 degrees C.; separating fuel form water, and adding at least one additive to raise the Cetane Number such as alcohol and preferably methanol, alkyl esters of inorganic acids and preferably alkyl nitrate, peroxides and combinations thereof.
- The present invention relates to a process for producing low sulphur and high Cetane Number petroleum fuel. The process includes preferably two phases. The first phase includes receiving petroleum fuel to be treated. The fuel temperature is preferably 80 to 100 degrees C. The fuel is then mixed with an acid source, preferably sulphuric acid or any other acid. The process may be done in the presence of oxygen. The fuel is mixed with a metal and preferably aluminium and preferably in solid state. The pressure could be an atmospheric pressure. This phase may take an average of about between 8 to 12 hours depending on the level of sulphur in the fuel and the quantity of fuel being treated.
- In the second phase, the fuel is mixed with a base source, such as sodium hydroxide or any other basic compound, and/ or salt, such as sodium bicarbonate, in order to neutralize the acid. The fuel should be heated to a temperature of preferably about 100 to 120 degrees C. The fuel should be mixed well. The process can be performed at an atmospheric pressure. This phase may take about 3 to 4 hours. The resulting fuel is sent to a separator where fuel naturally separates from water.
- An additional step is also used to raise the Cetane Number. At least one additive is added to the fuel. The at least one additive is preferably an alcohol, such as methanol, alkyl esters of inorganic acids, such as alkyl nitrate, butyl nitrate, amyl nitrate, isobutyl nitrate, and the likes, and peroxides, and combinations thereof.
- The present process reduces sulphur content by about at least 50% and raises the Cetane Number higher than 50. The present process is simple and inexpensive treatment of petroleum fuel to improve its ignition quality and provide cleaner fuel.
- While the invention has been described in detail and with reference to specific embodiments thereof, it will be apparent to one skilled in the art that various changes and modifications can be made therein without departing from the scope and spirit thereof. Although the present invention has been described herein with reference to particular means, materials and embodiments, the present invention is not intended to be limited to the particulars disclosed herein; rather, the present invention extends to all functionally equivalent structures, methods and uses, such as those within the scope of the appended claims.
Claims (23)
1. A process for producing low sulphur and high cetane number petroleum fuel, said process comprising the steps of:
providing a petroleum fuel;
adding an acid source to said fuel;
adding aluminum to said fuel;
adding a base source to neutralize said acid source; and
heating said fuel.
2. The process as set forth in claim 1 wherein said fuel having a temperature range of about 80 to 100 degrees C.
3. The process as set forth in claim 1 further comprising the step of adding sodium carbonate and water to said fuel after step D.
4. The process as set forth in claim 1 wherein step E includes heating said fuel to about 100 to 120 degrees C.
5. The process as set forth in claim 1 further comprising the step of separating said fuel from water.
6. The process as set forth in claim 5 further comprising the step of adding at least one additive to said fuel to raise the Cetane Number.
7. The process as set forth in claim 6 wherein said at least one additive is an alcohol.
8. The process as set forth in claim 7 wherein said alcohol is methanol.
9. The process as set forth in claim 6 wherein said at least one additive is an alkyl ester of inorganic acids.
10. The process as set forth in claim 9 wherein said alky ester is an alkyl nitrate.
11. A process for producing low sulphur and high Cetane Number petroleum fuel comprising:
providing petroleum fuel;
adding at least one acid source to said fuel;
adding aluminium to said fuel; and
adding at least one base source to said fuel.
12. The process as set forth in claim 11 further including oxidizing said acid source.
13. The process as set forth in claim 11 further including heating said fuel.
14. The process as set forth in claim 11 further including adding water and sodium bicarbonate to said fuel.
15. The process as set forth in claim 11 further including separating fuel from water.
16. The process as set forth in claim 11 further including heating said fuel.
17. The process as set forth in claim 11 further including adding at least one additive to raise the Cetane Number.
18. A process for producing petroleum fuel having low sulphur content and having a Cetane Number greater than 50, said process comprising the steps of:
providing petroleum fuel;
providing at least one acid source;
adding aluminium to said fuel;
adding at least one base source to said fuel; and
adding at least one additive to said fuel.
19. The process as set forth in claim 18 wherein said fuel having a temperature of between 80 to 100 degrees C.
20. The process as set forth in claim 18 further including the step of adding water and salt after step D.
21. The process as set forth in claim 18 further including the step of separating water from said fuel before step E.
22. The process as set forth in claim 18 further including the step of heating said fuel to a temperature range of between 100 to 120 degrees C. after step C.
23. The process as set forth in claim 18 wherein said at least one additive comprises, alcohol, alkyl esters of inorganic acids, peroxides, and combinations thereof.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/102,867 US20060225339A1 (en) | 2005-04-11 | 2005-04-11 | Process for producing low sulphur and high cetane number petroleum fuel |
US12/454,896 US7892418B2 (en) | 2005-04-11 | 2009-05-26 | Process for producing low sulfur and high cetane number petroleum fuel |
US12/983,313 US20110179698A1 (en) | 2005-04-11 | 2011-01-02 | Process for producing low sulfur and high cetane number petroleum fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/102,867 US20060225339A1 (en) | 2005-04-11 | 2005-04-11 | Process for producing low sulphur and high cetane number petroleum fuel |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US12/454,896 Continuation US7892418B2 (en) | 2005-04-11 | 2009-05-26 | Process for producing low sulfur and high cetane number petroleum fuel |
Publications (1)
Publication Number | Publication Date |
---|---|
US20060225339A1 true US20060225339A1 (en) | 2006-10-12 |
Family
ID=37081787
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/102,867 Abandoned US20060225339A1 (en) | 2005-04-11 | 2005-04-11 | Process for producing low sulphur and high cetane number petroleum fuel |
Country Status (1)
Country | Link |
---|---|
US (1) | US20060225339A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011039649A3 (en) * | 2009-05-26 | 2011-06-23 | Agha Hassan A | A process for producing low sulfur and high cetane number petroleum fuel |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5639931A (en) * | 1993-10-18 | 1997-06-17 | Mobil Oil Corporation | Process for producing low aromatic diesel fuel with high cetane index |
US6210563B1 (en) * | 1998-12-30 | 2001-04-03 | Mobil Oil Corporation | Process for producing diesel fuel with increased cetane number |
-
2005
- 2005-04-11 US US11/102,867 patent/US20060225339A1/en not_active Abandoned
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5639931A (en) * | 1993-10-18 | 1997-06-17 | Mobil Oil Corporation | Process for producing low aromatic diesel fuel with high cetane index |
US6210563B1 (en) * | 1998-12-30 | 2001-04-03 | Mobil Oil Corporation | Process for producing diesel fuel with increased cetane number |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011039649A3 (en) * | 2009-05-26 | 2011-06-23 | Agha Hassan A | A process for producing low sulfur and high cetane number petroleum fuel |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2107101A2 (en) | Fuel for homogeneous charge compression ignition engine | |
EP2077312A1 (en) | Fuels for homogeneous charge compression ignition combustion engine | |
US5090967A (en) | Method and composition for providing an improved combustion in processes of combustion containing hydrocarbon compounds | |
AU642242B2 (en) | Fuel compositions with enhanced combustion characteristics | |
US20060225339A1 (en) | Process for producing low sulphur and high cetane number petroleum fuel | |
JP4109043B2 (en) | Fuel for premixed compression self-ignition engines | |
JP4109045B2 (en) | Fuel for premixed compression self-ignition engines | |
JP3441305B2 (en) | gasoline | |
JP4458405B2 (en) | Fuel for premixed compression self-ignition engines | |
US9663739B2 (en) | Method for increasing the maximum operating speed of an internal combustion engine operated in a low temperature combustion mode | |
JPH05140568A (en) | Low-pollution fuel composition | |
US9562206B2 (en) | Method for increasing the high load (knock) limit of an internal combustion engine operated in a low temperature combustion mode | |
JPH05214351A (en) | Fuel composition | |
US7892418B2 (en) | Process for producing low sulfur and high cetane number petroleum fuel | |
JP4109053B2 (en) | Fuel for premixed compression self-ignition engines | |
EP4227386A1 (en) | Method and system for producing diesel fuel having improved property | |
JP2004091660A (en) | Fuel for premixed compressed self-ignition type engine | |
JP4109049B2 (en) | Fuel for premixed compression self-ignition engines | |
JP4109048B2 (en) | Fuel for premixed compression self-ignition engines | |
AU2004218620A1 (en) | Method for reducing combustion chamber deposit flaking | |
JP4109050B2 (en) | Fuel for premixed compression self-ignition engines | |
CA1331917C (en) | Method and a composition for providing an improved combustion in process of combustion containing hydrocarbon compounds | |
JP4109044B2 (en) | Fuel for premixed compression self-ignition engines | |
KR20090039935A (en) | Fuel composition for internal-combustion engine containing trialkylamine | |
JP2008031215A (en) | Fuel oil composition |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |