US20190194550A1 - Treatment Method for Reducing Contaminating Agents in Liquid Mixtures of Substituted Hydrocarbons Used as Fuels - Google Patents
Treatment Method for Reducing Contaminating Agents in Liquid Mixtures of Substituted Hydrocarbons Used as Fuels Download PDFInfo
- Publication number
- US20190194550A1 US20190194550A1 US16/328,185 US201616328185A US2019194550A1 US 20190194550 A1 US20190194550 A1 US 20190194550A1 US 201616328185 A US201616328185 A US 201616328185A US 2019194550 A1 US2019194550 A1 US 2019194550A1
- Authority
- US
- United States
- Prior art keywords
- fuels
- fuel
- hydrocarbons used
- hydrocarbons
- treatment method
- 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
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Classifications
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- 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
-
- 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/16—Metal oxides
-
- 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
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/24—Mixing, stirring of fuel components
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
Definitions
- Liquid hydrocarbons used as fuel such as gasoline, gas oil or diesel, jet fuel, or kerosene, are toxic and highly flammable. Vapors produced by their evaporation and substances created when burnt, such as carbon monoxide, nitrous oxides, non-burnt hydrocarbons, etc., contribute to air pollution. Also, burning these fuels additionally produces carbon dioxide, a greenhouse gas directly related to global climate change.
- This invention pertains to a method of refining and catalyzing liquid hydrocarbons used as fuel that eliminates sulfur, aromatic compounds, benzenes, xylenes, toluenes, in addition to oxidizing available octanes to act as an oxidizer during the hydrocarbon combustion processes, which provides better burning and greater energy availability for industrial fuel uses.
- the disclosed method is applicable to mixed fuels in the final stage of hydrocarbon refining, i.e., fuels that, in current state of the art, are used as final products available for sale to consumers.
- the disclosed method comprises mixing small solid ferrous oxide particles with water vapor until a heterogeneous mixture is achieved. This heterogeneous mixture is then poured into a container with substituted hydrocarbons used as fuel, and is combined and mixed constantly for a few minutes.
- Hydrocarbons used in commerce as fuel carry high concentrations of sulfur, aromatic compounds, benzenes, xylenes, toluenes, and others. Burning these fuels in internal combustion engines is not efficient enough to burn all of these compounds, so they are released into the atmosphere.
- a treatment method for reducing polluting agents in liquid substituted hydrocarbons used as fuel comprising blending a heterogeneous mixture of ferrous oxide in water with said fuel, mixing or constantly combining the solution, allowing the mixture to settle, and removing the aqueous solution of ferrous oxide and water by decanting.
- the fuel obtained as a result of applying the disclosed method contains a lower count of polluting compounds containing sulfur, aromatic compounds, benzenes, xylenes, toluenes, and others. Additionally, it increases fuel burning efficiency because, during the chemical reaction, hydrocarbons gain additional oxygen atoms that help as an oxidizer.
- FIG. 1 is the graphic result of the GC-FID analysis of a commercially available diesel sample, in which the X axis shows minutes lapsed, and the Y axis shows voltage in mV.
- FIG. 2 is the graphic result of the GC-FID analysis of a commercially available diesel sample, treated with the claimed compound and method, in which the X axis shows minutes lapsed, and the Y axis shows voltage in mV, and the hydrocarbon reduction is appreciated.
- FIG. 3 is the graphic result of the GC-FID analysis of a commercially available gasoline sample, in which the X axis shows minutes lapsed, and Y axis shows voltage in V.
- FIG. 4 is the graphic result of the GC-FID analysis of a commercially available gasoline sample, treated with the claimed compound and method, in which the X axis shows minutes lapsed, and the Y axis shows voltage in mV, and the hydrocarbon reduction is appreciated.
- FIG. 5 is the graphic result of the GC-FID analysis of a commercially available jet fuel sample, in which the X axis shows minutes lapsed, and Y axis shows voltage in mV.
- FIG. 6 is the graphic result of the GC-FID analysis of a commercially available jet fuel sample, treated with the claimed compound and method, in which the X axis shows minutes lapsed, and Y axis shows voltage in mV, and the hydrocarbon reduction is appreciated.
- the process is achieved by supersaturating ferrous oxide in water.
- the ferrous oxide supersaturation process has been described by (MARTIN, Scot T. Precipitation and dissolution of iron and manganese oxides. Environmental Catalysis, 2005, p. 61-81). This supersaturated solution serves as catalyzer for refining fuel.
- the supersaturated ferrous oxide solution is mixed with the fuel. It is well known that the ferrous oxide supersaturated solution may be used in a proportion of up to 70% of said solution against 30% fuel. However, in the preferred embodiment, the mixture is done with 10% solution to 90% fuel (e.g., 100 liters of supersaturated ferrous oxide solution for each 1,000 liters of fuel to be refined).
- the supersaturated solution must be mixed by constant fluid blending, either by agitation, fluid recirculation, or barometric variation. In the preferred embodiment, 1 liter of this mixture must be mixed for at least one minute.
- FIG. 1 shows a graphic result of gas chromatography of a commercially available diesel sample.
- the first spike belongs to the dichloromethane used as control solvent.
- FIG. 2 shows a graphic result of gas chromatography of a commercially available diesel after treatment with the claimed method. As can be seen in accordance with the retention time shown in FIG. 2 , the amount of linear hydrocarbons has decreased, which demonstrates the refining capabilities of the method.
- FIG. 3 shows the graphic result of gas chromatography of a commercially available gasoline sample.
- the first spike belongs to the dichloromethane used as control solvent.
- FIG. 4 shows the graphic result of gas chromatography of the same commercially available gasoline sample after being treated with the claimed method. It will be appreciated that the quantity of cyclic hydrocarbons has also decreased.
- FIG. 5 corresponds to the analysis of commercially available jet fuel
- FIG. 6 corresponds to the analysis of the same jet fuel after being treated with the claimed method. The results are similar to those of diesel and gasoline.
- This method is applicable to any industry in which fuel is used and there is a desire to reduce polluting combustion byproducts and improve fuel efficiency.
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- 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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Liquid Carbonaceous Fuels (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/IB2016/055210 WO2017093816A1 (es) | 2016-08-31 | 2016-08-31 | Método de tratamiento para reducción de agentes contaminantes en mezclas líquidas de hidrocarburos sustituidos usados como combustibles |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/IB2016/055210 A-371-Of-International WO2017093816A1 (es) | 2016-08-31 | 2016-08-31 | Método de tratamiento para reducción de agentes contaminantes en mezclas líquidas de hidrocarburos sustituidos usados como combustibles |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/929,274 Continuation US20200318017A1 (en) | 2016-08-31 | 2020-04-21 | Treatment Method for Reducing Contaminating Agents in Liquid Mixtures of Substituted Hydrocarbons Used as Fuels |
Publications (1)
Publication Number | Publication Date |
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US20190194550A1 true US20190194550A1 (en) | 2019-06-27 |
Family
ID=58796394
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US16/328,185 Abandoned US20190194550A1 (en) | 2016-08-31 | 2016-08-31 | Treatment Method for Reducing Contaminating Agents in Liquid Mixtures of Substituted Hydrocarbons Used as Fuels |
US15/929,274 Abandoned US20200318017A1 (en) | 2016-08-31 | 2020-04-21 | Treatment Method for Reducing Contaminating Agents in Liquid Mixtures of Substituted Hydrocarbons Used as Fuels |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/929,274 Abandoned US20200318017A1 (en) | 2016-08-31 | 2020-04-21 | Treatment Method for Reducing Contaminating Agents in Liquid Mixtures of Substituted Hydrocarbons Used as Fuels |
Country Status (7)
Country | Link |
---|---|
US (2) | US20190194550A1 (zh) |
EP (1) | EP3508558A4 (zh) |
CN (1) | CN110234741A (zh) |
CO (1) | CO2019002973A2 (zh) |
MX (1) | MX2019002220A (zh) |
RU (1) | RU2717834C1 (zh) |
WO (1) | WO2017093816A1 (zh) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040108252A1 (en) * | 2002-12-10 | 2004-06-10 | Petroleo Brasileiro S.A. - Petrobras | Process for the upgrading of raw hydrocarbon streams |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4811321B1 (zh) * | 1967-02-16 | 1973-04-12 | ||
RU2159666C1 (ru) * | 1999-11-24 | 2000-11-27 | Дыкман Аркадий Самуилович | Способ очистки промышленных газовых выбросов |
US7309416B2 (en) * | 2003-07-11 | 2007-12-18 | Aspen Products Group, Inc. | Methods and compositions for desulfurization of hydrocarbon fuels |
CN101067100B (zh) * | 2006-12-22 | 2011-05-18 | 毕舒 | 清洁环保燃料的制备方法及制得的燃料 |
TWI414592B (zh) * | 2010-11-05 | 2013-11-11 | Ind Tech Res Inst | 油品改質的方法 |
-
2016
- 2016-08-31 MX MX2019002220A patent/MX2019002220A/es unknown
- 2016-08-31 RU RU2019109240A patent/RU2717834C1/ru active
- 2016-08-31 WO PCT/IB2016/055210 patent/WO2017093816A1/es unknown
- 2016-08-31 CN CN201680090578.8A patent/CN110234741A/zh active Pending
- 2016-08-31 EP EP16870059.9A patent/EP3508558A4/en not_active Withdrawn
- 2016-08-31 US US16/328,185 patent/US20190194550A1/en not_active Abandoned
-
2019
- 2019-03-27 CO CONC2019/0002973A patent/CO2019002973A2/es unknown
-
2020
- 2020-04-21 US US15/929,274 patent/US20200318017A1/en not_active Abandoned
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040108252A1 (en) * | 2002-12-10 | 2004-06-10 | Petroleo Brasileiro S.A. - Petrobras | Process for the upgrading of raw hydrocarbon streams |
Also Published As
Publication number | Publication date |
---|---|
EP3508558A1 (en) | 2019-07-10 |
EP3508558A4 (en) | 2020-04-01 |
CN110234741A (zh) | 2019-09-13 |
MX2019002220A (es) | 2019-09-23 |
US20200318017A1 (en) | 2020-10-08 |
CO2019002973A2 (es) | 2019-08-30 |
RU2717834C1 (ru) | 2020-03-26 |
WO2017093816A1 (es) | 2017-06-08 |
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