WO2008016318A2 - Procedure of obtaining automotive fuels and the modified fuels obtained by means of this procedure - Google Patents
Procedure of obtaining automotive fuels and the modified fuels obtained by means of this procedure Download PDFInfo
- Publication number
- WO2008016318A2 WO2008016318A2 PCT/RO2007/000015 RO2007000015W WO2008016318A2 WO 2008016318 A2 WO2008016318 A2 WO 2008016318A2 RO 2007000015 W RO2007000015 W RO 2007000015W WO 2008016318 A2 WO2008016318 A2 WO 2008016318A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- procedure
- fuels
- hho
- content
- obtaining
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 31
- 239000000446 fuel Substances 0.000 title claims abstract description 24
- 230000003197 catalytic effect Effects 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 238000005868 electrolysis reaction Methods 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims description 29
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 15
- 239000001257 hydrogen Substances 0.000 claims description 15
- 229910052739 hydrogen Inorganic materials 0.000 claims description 15
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 9
- 239000000779 smoke Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 abstract description 17
- 239000008246 gaseous mixture Substances 0.000 abstract description 2
- 238000005504 petroleum refining Methods 0.000 abstract description 2
- 239000002283 diesel fuel Substances 0.000 description 12
- 239000003502 gasoline Substances 0.000 description 11
- 230000005587 bubbling Effects 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 229930195733 hydrocarbon Natural products 0.000 description 5
- 150000002430 hydrocarbons Chemical class 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 239000005864 Sulphur Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000002596 correlated effect Effects 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 230000005672 electromagnetic field Effects 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
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
- C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark 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
- C10L1/04—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
- 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
- C10L10/02—Use of additives to fuels or fires for particular purposes for reducing smoke development
Definitions
- the present patent refers to a procedure of obtaining automotive fuels and the modified fuels obtained by means of this procedure.
- the main objectives related to the petroleum refining consist in obtaining fuels as gasoline or Diesel that would grant an optimum operation of the spark ignition engines or the compression ignition engines, respectively, and that would also contribute to the pollution phenomenon generated by exhaust gases decreasing, namely by means of lowering-down the smoke index, the CO, CO2, hydrocarbon and NO x emissions.
- a procedure of obtaining Diesel-type fuels consists in treating the raw material resulted from the cracking process with hydrogen at high pressures and temperatures, in the presence of some catalytic agents.
- the first catalytic agent contains a metal belonging to the IV- th group and a metal belonging to the VIII-th group, placed on a non-acid support
- the second catalytic agent contains a metal belonging to the VI-th group and a metal belonging to the VII-th group, placed on a non-acid support (US Patent No. 5.865.985).
- the gasoline obtaining procedure consists in the hydrotreatment process of the mean fraction separated from natural gasoline by fractioning method.
- a gasoline with a low content of benzene will result, due to benzene transforming into cyclohexane which in turn may be subsequently isomerized in view of improving its octane number (US Patent No. 6.855.853).
- a procedure to obtaining a low sulphur content gasoline consists in the diolefine selective hydrogenation process under special operating conditions by which the sulphur compounds that are present in the raw material are partially converted into heavier compounds while, the separation of the heavier fraction rich in sulphur and its hydrodesulphuration process being made on a specific catalytic agent (UD Patent No. 7.052.598). AU these procedures are generally carried out at high temperatures and pressures within installations which involved large investments, and relatively high hydrogen consumption.
- the technical problem the invention solves consists in the automotive fuels physico- chemical properties improving with simultaneously diminishing of exhaust gas pollution level resulted when using these fuels.
- the procedure of obtaining gas consists in the hydrocarbon fraction contact treatment with HHO oxyhydrogen gas by its direct bubbling, either in the presence or in the absence of catalytic agents, in a discontinuous sequence, or in a continuous sequence, with or without re-circulating the gaseous mixture, in a temperature range of 20 to 100 Celsius degrees, and a pressure range of 1 to 20 atmospheres, for as long as 0.2 to 8 hours.
- the gas obtained further to applying the invention procedure has a higher by 2% hydrogen and ⁇ ⁇ xygen content and assures the cutting-down" of " sm ⁇ ke-and particulate emissions.
- Fig. 1 the initial Diesel fuel composition, and its composition after the treatment with the HHO oxyhydrogen mixture by means of GC_MS;
- Fig. 2 the smoke emissions while testing the initial Diesel fuel, and the smoke emissions after the treatment with the HHO oxyhydrogen gas in accordance with example 1;
- Fig. 3 the particulate emissions while testing the initial Diesel fuel, and the particulate emissions after the treatment with the HHO oxyhydrogen gas in accordance with example 1. ⁇
- the HHO gas discharge shall be adjusted at 3.5 1/h, and the bubbling process shall be maintained at 25 Celsius degrees temperature and at atmospheric pressure in the case of open vessel, for as long as 30 minutes.
- the reaction product shall be then analyzed by determining the water content, the ash content " " as well as the content in the following elementsrcarbon, hydrogen and oxygen.
- Table 1 summarizes data that are characteristics of the initial fuels and of the final fuels after the HHO oxyhydrogen gas treatment with.
- Fig. 1 indicates an increase in hydrogen and oxygen content, and a decrease in the carbon content for the Diesel fuel.
- Fig. 1 the chromatograms indicate significant modifications of the composition further to the treatment with the HHO oxyhydrogen mixture.
- Table 2 presents the initial gasoline composition, and its composition after the treatment with the HHO oxyhydrogen gas by means of the GC method (chromatograms of the gasoline samples)
- Table 3 presents a comparative diesel engine test report obtained with a normal Diesel fuel and with the same Diesel fuel treated with the HHO oxyhydrogen gas.
- a metallic autoclave that has been provided with a frit bubbling system, a pressure and HHO gas discharge control and adjustment device, shall be fed with 350 ml of Euro 3+ Diesel fuel.
- the HHO gas discharge shall be adjusted at 3.5 1/h, and the bubbling process shall be maintained at 45 Celsius degrees temperature, and at 10 atmospheres pressure for as long as 30 minutes.
- the reaction product is then analyzed by determining the water content, the ash content, as well as the content in the following elements: carbon, hydrogen and oxygen (see Table 1).
- carbon, hydrogen and oxygen see Table 1.
- the HHO gas discharge shall be adjusted at 3.5 1/h, and the bubbling process shall be maintained at 25 Celsius degrees temperature and at atmospheric pressure in the case of open vessel for as long as 30 minutes.
- the reaction product shall be then analyzed by determining the water content, the density, the chemical composition and the content in carbon, hydrogen and oxygen (see Table 1).
- the chemical composition of the mixture has been determined by means of the GC method.
- the content in isopenthane, the content in the C4-C6 fraction and in the aromatic hydrocarbons increases, and the content in the C8+ fraction decreases ⁇ whrlei:he content in ethers remains the same.
- the modified Diesel fuel testing as per Example 1 has been carried out on an engine test bench equipped with a direct injection diesel engine, 4 cylinders in line and a 17.5:1 compression ratio.
- the test bed is also provided with a speed transducer, a mass fuel consumption equipment, a smokemeter and a particles emission analyzer.
- the results related to the engine fueling behavior are presented in Figures 2 and 3. It shall be noticed that the smoke numbers and the particulate emissions decreased comparing against the situation when normal diesel fuel was used; however, the decrease values are more obvious at lower outputs of the engine.
Abstract
The invention refers to a procedure of obtaining automotive modified fuels with the help of this procedure based on treating the fuels resulting from petroleum refining with the HHO mixture. In full compliance with this invention, the procedure consists in treating the fuels with the HHO gaseous mixture coming up as a result of the water electrolysis, in the presence or in the absence of catalytic agents, at temperatures between 20 and 100 Celsius degrees, at pressures between 1 and 20 atmospheres, and as long as 0.2 to 8 hours.
Description
PROCEDURE OF OBTAINING AUTOMOTIVE FUELS AND THE MODIFIED FUELS OBTAINED BY MEANS OF THIS PROCEDURE
The present patent refers to a procedure of obtaining automotive fuels and the modified fuels obtained by means of this procedure.
The main objectives related to the petroleum refining consist in obtaining fuels as gasoline or Diesel that would grant an optimum operation of the spark ignition engines or the compression ignition engines, respectively, and that would also contribute to the pollution phenomenon generated by exhaust gases decreasing, namely by means of lowering-down the smoke index, the CO, CO2, hydrocarbon and NOx emissions.
The already known procedures used for hydrocarbons process in view of obtaining automotive fuels consist in hydrogen treatment of petroleum fractions.
Thus, a procedure of obtaining Diesel-type fuels consists in treating the raw material resulted from the cracking process with hydrogen at high pressures and temperatures, in the presence of some catalytic agents. The first catalytic agent contains a metal belonging to the IV- th group and a metal belonging to the VIII-th group, placed on a non-acid support, and the second catalytic agent contains a metal belonging to the VI-th group and a metal belonging to the VII-th group, placed on a non-acid support (US Patent No. 5.865.985).
As concerns another procedure, further to treating the raw material with hydrogen in the presence of a catalytic agent of the large mash molecular sieve-type, having a "faujasita"-type structure and an alpha acidity less than 1, that contains a noble metal belonging to the VIII-th group, which favors the hydrogenation/hydro-cracking process of the aromatic and naphthenic compounds from the raw materials, there shall be obtained another diesel fuel with a superior Cetane number (US Patent No. 6.210.563).
The gasoline obtaining procedure consists in the hydrotreatment process of the mean fraction separated from natural gasoline by fractioning method. Thus, a gasoline with a low content of benzene will result, due to benzene transforming into cyclohexane which in turn may be subsequently isomerized in view of improving its octane number (US Patent No. 6.855.853).
A procedure to obtaining a low sulphur content gasoline consists in the diolefine selective hydrogenation process under special operating conditions by which the sulphur compounds that are present in the raw material are partially converted into heavier compounds while, the separation of the heavier fraction rich in sulphur and its hydrodesulphuration process being made on a specific catalytic agent (UD Patent No. 7.052.598).
AU these procedures are generally carried out at high temperatures and pressures within installations which involved large investments, and relatively high hydrogen consumption.
It is already known that an oxyhydrogen gas has been obtained based on the controlled dissociation, in electromagnetic field, of an alkaline aqueous solution. This gas, further on namely as "the HHO oxyhydrogen gas" is a mixture of 63 - 67% hydrogen and 30 — 35% oxygen. The special qualities of this gas result from its capability to react with materials of any nature, which justifies the efforts to promote it to different industrial applications (US Patent No. 6.689.258 Bl and the request published at the international level under No. WO2005076767 A3, Mr. Dennis J. Klein being the author of both of them).
The technical problem the invention solves consists in the automotive fuels physico- chemical properties improving with simultaneously diminishing of exhaust gas pollution level resulted when using these fuels.
The procedure of obtaining gas, as per the invention, consists in the hydrocarbon fraction contact treatment with HHO oxyhydrogen gas by its direct bubbling, either in the presence or in the absence of catalytic agents, in a discontinuous sequence, or in a continuous sequence, with or without re-circulating the gaseous mixture, in a temperature range of 20 to 100 Celsius degrees, and a pressure range of 1 to 20 atmospheres, for as long as 0.2 to 8 hours.
The gas obtained further to applying the invention procedure has a higher by 2% hydrogen and~δxygen content and assures the cutting-down" of"smσke-and particulate emissions.
As a consequence of hydrocarbons treating by the HHO oxyhydrogen gas is assured the improvement of the fuel burning characteristics as well as the decreasing of the burned gas pollution due to the HHO oxyhydrogen gas composition, which, according to the invention, enriches the treated fuel both in hydrogen reactive status, and in- oxygen, as well.
This way, further to treating gasoline with the HHO oxyhydrogen gas, one can noticed the characteristics modification (density, boiling curve, chemical composition, and IR spectrum). The improvement of the gasoline characteristics that have been modified further to submitting it to the HHO oxyhydrogen gas treatment, is evident by what is concerned its chemical composition, the carbon, hydrogen and oxygen contents.
The procedure of obtaining gas by HHO oxyhydrogen gas treatment, in accordance with the invention, has the following advantages:
- it reduces the CO and CO2 emissions;
- it reduces the hydrocarbon emissions; it reduces the smoke number.
There are submitted 4 examples of achieving the procedure as per the invention, also in connection with the Figures that represent:
Fig. 1 - the initial Diesel fuel composition, and its composition after the treatment with the HHO oxyhydrogen mixture by means of GC_MS;
Fig. 2 - the smoke emissions while testing the initial Diesel fuel, and the smoke emissions after the treatment with the HHO oxyhydrogen gas in accordance with example 1;
Fig. 3 - the particulate emissions while testing the initial Diesel fuel, and the particulate emissions after the treatment with the HHO oxyhydrogen gas in accordance with example 1. ■
Example 1
A balloon that has been provided with a frit bubbling system, a pressure and HHO gas discharge control and adjustment device, shall be fed with 350 ml of Euro 3+ Diesel fuel. The HHO gas discharge shall be adjusted at 3.5 1/h, and the bubbling process shall be maintained at 25 Celsius degrees temperature and at atmospheric pressure in the case of open vessel, for as long as 30 minutes. The reaction product shall be then analyzed by determining the water content, the ash content" "as well as the content in the following elementsrcarbon, hydrogen and oxygen.
Table 1 summarizes data that are characteristics of the initial fuels and of the final fuels after the HHO oxyhydrogen gas treatment with.
Table 1
Table 2 presents the initial gasoline composition, and its composition after the treatment with the HHO oxyhydrogen gas by means of the GC method (chromatograms of the gasoline samples)
Table 2
Table 3 presents a comparative diesel engine test report obtained with a normal Diesel fuel and with the same Diesel fuel treated with the HHO oxyhydrogen gas. Table 3
Example 2
A metallic autoclave that has been provided with a frit bubbling system, a pressure and HHO gas discharge control and adjustment device, shall be fed with 350 ml of Euro 3+ Diesel fuel. The HHO gas discharge shall be adjusted at 3.5 1/h, and the bubbling process shall be
maintained at 45 Celsius degrees temperature, and at 10 atmospheres pressure for as long as 30 minutes.
The reaction product is then analyzed by determining the water content, the ash content, as well as the content in the following elements: carbon, hydrogen and oxygen (see Table 1). One can be noticed a decrease in the carbon content of the Diesel fuel correlated with an increase in the hydrogen and oxygen content.
Example 3
A balloon that has been provided with a frit bubbling system, a pressure and HHO gas discharge control and adjustment device, shall be fed with 350 ml of gasoline. The HHO gas discharge shall be adjusted at 3.5 1/h, and the bubbling process shall be maintained at 25 Celsius degrees temperature and at atmospheric pressure in the case of open vessel for as long as 30 minutes. The reaction product shall be then analyzed by determining the water content, the density, the chemical composition and the content in carbon, hydrogen and oxygen (see Table 1). The chemical composition of the mixture has been determined by means of the GC method. One can noticed a decrease in the carbon content of gasoline correlated with an increase in the hydrogen and oxygen content, as well as a modification of the chemical composition. Thus, the content in isopenthane, the content in the C4-C6 fraction and in the aromatic hydrocarbons "increases, and the content in the C8+ fraction decreasesτwhrlei:he content in ethers remains the same.
Example 4
The modified Diesel fuel testing as per Example 1 has been carried out on an engine test bench equipped with a direct injection diesel engine, 4 cylinders in line and a 17.5:1 compression ratio. The test bed is also provided with a speed transducer, a mass fuel consumption equipment, a smokemeter and a particles emission analyzer. The results related to the engine fueling behavior are presented in Figures 2 and 3. It shall be noticed that the smoke numbers and the particulate emissions decreased comparing against the situation when normal diesel fuel was used; however, the decrease values are more obvious at lower outputs of the engine.
Claims
1. Procedure of obtaining automotive fuels which is characterized in that it consists in treating the fuel with the HHO oxyhydrogen gas resulting from the water electrolysis, in the presence or in the absence of catalytic agents, at temperatures ranging between 20 and 100 Celsius degrees, at pressures ranging between 1 and 20 atmospheres, and a volume fraction 0.1-6 Nm3/ m3 of the HHO oxyhydrogen gas to fuel ratio;
2. Automotive fuels obtained by means of the procedure according to claim 1, characterized in that they have a hydrogen and oxygen content which is higher by 2% and assures the cutting-down of smoke particulate emissions.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/307,393 US20090199465A1 (en) | 2006-08-01 | 2007-07-26 | Procedure of obtaining automotive fuels and the modified fuels obtained by means of this procedure |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ROA200600613A RO122548B1 (en) | 2006-08-01 | 2006-08-01 | Process for obtaining motor vehicle fuels |
| ROA200600613 | 2006-08-01 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2008016318A2 true WO2008016318A2 (en) | 2008-02-07 |
| WO2008016318A3 WO2008016318A3 (en) | 2008-07-31 |
Family
ID=38922738
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/RO2007/000015 WO2008016318A2 (en) | 2006-08-01 | 2007-07-26 | Procedure of obtaining automotive fuels and the modified fuels obtained by means of this procedure |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US20090199465A1 (en) |
| RO (1) | RO122548B1 (en) |
| WO (1) | WO2008016318A2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2865426C (en) | 2012-02-27 | 2020-07-28 | Deec, Inc. | Oxygen-rich plasma generators for boosting internal combustion engines |
| BR112018068006A2 (en) | 2016-03-07 | 2019-01-15 | Hytech Power Inc | method for generating and distributing a second fuel to an internal combustion engine |
| US20190234348A1 (en) | 2018-01-29 | 2019-08-01 | Hytech Power, Llc | Ultra Low HHO Injection |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE517290C (en) * | 1931-02-09 | Edmund Breuning Dr | Method for reducing the explosiveness of explosive gas mixtures used in particular for operating internal combustion engines, e.g. B. the oxyhydrogen | |
| DE890278C (en) * | 1951-11-27 | 1953-09-17 | Alfred Dr Katterfeldt | Process for increasing the knock resistance of fuels and fuel economy in internal combustion engines |
| DE3419783A1 (en) * | 1983-11-11 | 1985-05-23 | Edgar 5441 Mertloch Morgenweg | Hydrogen unit for motor vehicles and internal combustion engines |
| US20040108252A1 (en) * | 2002-12-10 | 2004-06-10 | Petroleo Brasileiro S.A. - Petrobras | Process for the upgrading of raw hydrocarbon streams |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4326360C1 (en) * | 1993-08-05 | 1994-12-15 | Ppv Verwaltungs Ag | Method and device for producing a fuel mixture |
| US20040149591A1 (en) * | 2001-04-04 | 2004-08-05 | Dennis J. Klein | Apparatus and method for the conversion of water into a new gaseous and combustible form and the combustible gas formed thereby |
-
2006
- 2006-08-01 RO ROA200600613A patent/RO122548B1/en unknown
-
2007
- 2007-07-26 US US12/307,393 patent/US20090199465A1/en not_active Abandoned
- 2007-07-26 WO PCT/RO2007/000015 patent/WO2008016318A2/en active Application Filing
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE517290C (en) * | 1931-02-09 | Edmund Breuning Dr | Method for reducing the explosiveness of explosive gas mixtures used in particular for operating internal combustion engines, e.g. B. the oxyhydrogen | |
| DE890278C (en) * | 1951-11-27 | 1953-09-17 | Alfred Dr Katterfeldt | Process for increasing the knock resistance of fuels and fuel economy in internal combustion engines |
| DE3419783A1 (en) * | 1983-11-11 | 1985-05-23 | Edgar 5441 Mertloch Morgenweg | Hydrogen unit for motor vehicles and internal combustion engines |
| 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 |
|---|---|
| WO2008016318A3 (en) | 2008-07-31 |
| US20090199465A1 (en) | 2009-08-13 |
| RO122548B1 (en) | 2009-08-28 |
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