DK201000099U3 - Hydroxy gas powered engine preheater - Google Patents
Hydroxy gas powered engine preheater Download PDFInfo
- Publication number
- DK201000099U3 DK201000099U3 DKBA201000099U DKBA201000099U DK201000099U3 DK 201000099 U3 DK201000099 U3 DK 201000099U3 DK BA201000099 U DKBA201000099 U DK BA201000099U DK BA201000099 U DKBA201000099 U DK BA201000099U DK 201000099 U3 DK201000099 U3 DK 201000099U3
- Authority
- DK
- Denmark
- Prior art keywords
- generation
- hho
- gas
- hydroxy
- preheating
- Prior art date
Links
- 125000002887 hydroxy group Chemical group [H]O* 0.000 title claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000012153 distilled water Substances 0.000 claims abstract description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims abstract description 5
- 239000003792 electrolyte Substances 0.000 claims abstract description 4
- 230000007935 neutral effect Effects 0.000 claims abstract description 3
- 238000005868 electrolysis reaction Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 abstract description 8
- 239000000446 fuel Substances 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 18
- 238000000034 method Methods 0.000 description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
Classifications
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Frembringelsen er kendetegnet ved en elektronisk styret elektrolysecelle med tilhørende gasbrænder og varmeveksler, der vha destilleret vand og Bikarbonat som elektrolyt producerer den brændbare Hydroxy (HHO) gas til brug for CO neutral foropvarmning af en motorblok i såvel stationære som mobile platforme. Frembringelsen sikrer en miljøvenlig foropvarmning af en Otto-motor og reducerer slidtage som følge af koldstart samt en forbedring af brændstoføkonomien. Frembringelsen kan anvendes i platforme indendørs (ventileret) som udendørs, da forbrændingsproduktet kun består af vanddampfkondens.The generation is characterized by an electronically controlled electrolytic cell with associated gas burner and heat exchanger, which produces distilled water and bicarbonate as the electrolyte the combustible Hydroxy (HHO) gas for use in CO neutral preheating of a motor block in both stationary and mobile platforms. The generation ensures an environmentally friendly preheating of an Otto engine and reduces wear due to cold start as well as an improvement in fuel economy. The generation can be used in indoor (ventilated) platforms as outdoors, since the combustion product consists only of the water vapor condensate.
Description
DK 2010 00099 U3DK 2010 00099 U3
TitelTitle
Hydroxygas (HHO) drevet motorforvarmerHydroxy gas (HHO) powered engine preheater
Frembringelsens anvendelsesområdeScope of production
Otto-motorer, dvs. 4-takts benzinmotorer samt Dieselmotorer i stationære og mobile platforme.Otto engines, ie 4-stroke petrol engines and Diesel engines in stationary and mobile platforms.
Kendt teknikPrior art
Elektriske forvarmere til 230V nettilslutning samt Benzin- og Dieselfyr.Electric preheaters for 230V mains connection as well as Petrol and Diesel boilers.
Det tekniske problemThe technical problem
En kold Otto-motors termodynamiske virkningsgrad er lav og udleder unødvendigt høje mængder C02, NOx samt SOx holdige gasarter, hvilket belaster miljøet i særlig grad, indtil normal driftstemperatur er opnået. Dermed er forbrændingsprocessen ved koldstart (omgivelsestemperatur) meget ineffektiv med tab af motoreffekt, hvilket yderligere har en negativ indvirkning på brændstoføkonomien.The thermodynamic efficiency of a cold Otto engine is low and emits unnecessarily high amounts of CO 2, NOx and SOx containing gases, which is particularly stressful to the environment until normal operating temperature is reached. Thus, the combustion process at cold start (ambient temperature) is very inefficient with loss of engine power, which further has a negative impact on fuel economy.
Den nye teknikThe new technique
Det nye ved frembringelsen er, at motor foropvarmningen realiseres ved at anvende C02-neutral Hydroxygas (HHO), produceret af eiektrolyseret, destilleret vand og Bikarbonat i stedet for miljøbelastende fossilt brændsel som benzin og Diesel. Desuden er frembringelsen uafhængig af 230V nettilslutning, da forbrændingen startes med batteri. Yderligere kan opvarmningen i tilfælde af anvendelse i mobile platforme som biler foregå i lukket, ventileret garage, da forbrændingsproduktet kun består af vanddamp/kondens.What is new about the generation is that the engine pre-heating is realized by using CO2 neutral Hydroxy gas (HHO), produced by electrolysed, distilled water and bicarbonate instead of environmentally harmful fossil fuels such as gasoline and Diesel. In addition, the generation is independent of 230V mains connection since the combustion is started with battery. Further, in case of use in mobile platforms, the heating can be carried out in a closed, ventilated garage, as the combustion product consists only of water vapor / condensation.
i DK 2010 00099 U3in DK 2010 00099 U3
Den tekniske virkningThe technical impact
Frembringelsen er kendetegnet ved, at den Hydroxygas (HHO) drevne motorforvarmer anvender en elektrolyse ceHe(1.0, se bilag 2 efterflg.), der strømfødes fra en standard 12V forseglet bly akkumulator. Elektrolyseprocessen anvender destilleret vand samt Bikarbonat som elektrolyt til kemisk at frigøre hydrogen bindingerne i vandmolekylerne og skabe en ionvandring til hhv. anoden og elektroden i elektrolysecellen. Herved skabes en opadstigende strøm af gasformige H+ samt O2' ioner, der rekombinerer over vandspejlet(6.1) til brændbar Hydroxygas (HHO). Gassen ledes videre via rørføring(l.l) til bunden af en beholder halvt fyldt med destilleret vand (beholder herefter benævnt 'bobler' (3.1)), hvorfra gassen igen bobler op til overfladen af vandspejlet(6.4), inden den via efterfølgende rørføring (6.5)+( 1.9) ledes til forbrænding i en gasbrænder med tilkoblet varme ve ksler(ej vist), som er i direkte kontakt med motorens kølesystem(ej vist). Bobleren (3.1) har til formål via vandspejlet(6.4) at fungere som automatisk flammehæmmer ('arrestor') i tilfælde af, at den brændende gasflamme' vandrer' tilbage i rørføringen(l.l) og søger kontakt med den genererede HHO gas og antænder denne. Opvarmningen foregår ved, at kølevandspumpen aktiveres og herved cirkulerer kølevandet gennem varmeveksleren, der er i direkte forbindelse med HHO gasbrænderen(ej vist). HHO gas produktionen starter, og HHO gasbrænderen antændes via et elektronisk styret, Piezoelektrisk element (ej vist), hvorefter HHO gasflammen overfører sin forbrændingsvarmeenergi til varmeveksleren og dermed kølevandet, hvorved motorblokken begynder at opvarmes. Elektrolysecellens HHO gas produktion reguleres via en elektronisk styring(1.8), der vha. timere kan aktiveres manuelt eller tidsprogrammes og inaktiveres, når motorens normale driftstemperatur er opnået. Herved elimineres især behovet for at holde motoren i tomgang på kolde vinterdage med stort miljøbelastende tab af brændstof, idet forbrændingsproduktet fra HHO reaktionen er vanddamp/kondens. Elektrolysecellen tilsættes blot glycol for at undgå DK 2010 00099 U3 tilfrysning ved temperaturen under 0°C. Det fremhæves desuden, at det støkiometriske forhold ved forbrændingen kun forbruger den mængde oxygen, som automatisk opstår ved elektrolyseprocessen og derved ikke forbruger yderligere oxygen fra atmosfæren. Evt. tilbageværende HHO gas fra elektrolyseprocessen i bobleren efter nedlukning af opvarmningsprocessen ledes via en elektrisk pilotventil(1.6) ud gennem et aktivt kulfilter(1.5). Denne funktionalitet er introduceret som over redundant sikkerhed, idet tilbageværende HHO gas automatisk afbrændes, når elektrolyseprocessen standses af den elektroniske temperaturregulering(1.8). Det fremhæves yderligere, at grundet HHO gassens høje specifikke varmeenthalpi i forhold til fossile brændsler vil elektrolysecellen kun skulle genopfyldes med destilleret vand, glycol og Bikarbonat efter lang tids brug, hvilket afhænger af den specifikke applikation. Elektrolytten indgår ikke i den elektrolytiske reaktion og kræver således udelukkende genopfyldning efter rensning af elektrolysecellen efter længere tids brug.The generation is characterized by the fact that the Hydroxy gas (HHO) powered motor preheater uses an electrolysis ceHe (1.0, see Appendix 2 below), which is fed from a standard 12V sealed lead accumulator. The electrolysis process uses distilled water as well as bicarbonate as an electrolyte to chemically release the hydrogen bonds in the water molecules and create an ion migration to the water. the anode and the electrode in the electrolysis cell. This creates an upward flow of gaseous H + and O2 ions that recombine over the water level (6.1) into combustible Hydroxy gas (HHO). The gas is passed through piping (II) to the bottom of a container half filled with distilled water (hereinafter referred to as 'bubbles' (3.1)), from which the gas again bubbles up to the surface of the water level (6.4), before it is subsequently piped (6.5). ) + (1.9) is conducted for combustion in a gas burner with connected heat exchangers (not shown) in direct contact with the engine cooling system (not shown). The purpose of the bubbler (3.1) is to act as an automatic flame retardant ('arrestor') in the case of the flame gas flame 'wandering' back into the pipeline (II) and seeking contact with the generated HHO gas and igniting it. . The heating is carried out by activating the cooling water pump and thereby circulating the cooling water through the heat exchanger, which is in direct connection with the HHO gas burner (not shown). The HHO gas production starts and the HHO gas burner ignites via an electronically controlled, piezoelectric element (not shown), after which the HHO gas flame transfers its combustion heat energy to the heat exchanger and thus the cooling water, whereby the engine block begins to heat. The HHO gas production of the electrolysis cell is controlled via an electronic control (1.8) which can be manually activated or timed and deactivated by means of timers when the normal operating temperature of the motor has been reached. This in particular eliminates the need to keep the engine idle on cold winter days with great environmental loss of fuel, as the combustion product from the HHO reaction is water vapor / condensation. The electrolysis cell is simply added glycol to avoid freezing at temperatures below 0 ° C. In addition, it is emphasized that the stoichiometric ratio of the combustion consumes only the amount of oxygen that is automatically generated by the electrolysis process and thereby does not consume additional oxygen from the atmosphere. Possibly. residual HHO gas from the electrolysis process in the bubbler after the heating process has been shut down is discharged via an activated carbon filter (1.5) via an electric pilot valve (1.6). This functionality is introduced as over redundant security, with residual HHO gas being automatically burned when the electrolysis process is stopped by the electronic temperature control (1.8). It is further emphasized that due to the high specific heat enthalpy of the HHO gas compared to fossil fuels, the electrolytic cell will only need to be refilled with distilled water, glycol and bicarbonate after long use, which depends on the specific application. The electrolyte is not included in the electrolytic reaction and thus requires refilling only after purification of the electrolytic cell after prolonged use.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DKBA201000099U DK201000099U3 (en) | 2010-05-26 | 2010-05-26 | Hydroxy gas powered engine preheater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DKBA201000099U DK201000099U3 (en) | 2010-05-26 | 2010-05-26 | Hydroxy gas powered engine preheater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DK201000099U3 true DK201000099U3 (en) | 2010-08-27 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DKBA201000099U DK201000099U3 (en) | 2010-05-26 | 2010-05-26 | Hydroxy gas powered engine preheater |
Country Status (1)
| Country | Link |
|---|---|
| DK (1) | DK201000099U3 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10494992B2 (en) | 2018-01-29 | 2019-12-03 | Hytech Power, Llc | Temperature control for HHO injection gas |
| US10605162B2 (en) | 2016-03-07 | 2020-03-31 | HyTech Power, Inc. | Method of generating and distributing a second fuel for an internal combustion engine |
| US11879402B2 (en) | 2012-02-27 | 2024-01-23 | Hytech Power, Llc | Methods to reduce combustion time and temperature in an engine |
-
2010
- 2010-05-26 DK DKBA201000099U patent/DK201000099U3/en not_active IP Right Cessation
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11879402B2 (en) | 2012-02-27 | 2024-01-23 | Hytech Power, Llc | Methods to reduce combustion time and temperature in an engine |
| US10605162B2 (en) | 2016-03-07 | 2020-03-31 | HyTech Power, Inc. | Method of generating and distributing a second fuel for an internal combustion engine |
| US11280261B2 (en) | 2016-03-07 | 2022-03-22 | HyTech Power, Inc. | Systems for HHO gas second fuel distribution and control |
| US11815011B2 (en) | 2016-03-07 | 2023-11-14 | Hytech Power, Llc | Generation and regulation of HHO gas |
| US10494992B2 (en) | 2018-01-29 | 2019-12-03 | Hytech Power, Llc | Temperature control for HHO injection gas |
| US10619562B2 (en) | 2018-01-29 | 2020-04-14 | Hytech Power, Llc | Explosion safe electrolysis unit |
| US11828219B2 (en) | 2018-01-29 | 2023-11-28 | Hytech Power, Llc | Rollover safe electrolysis unit for vehicles |
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Effective date: 20130526 |