GB2601852A - Combustion gasses and particulates recycling - Google Patents
Combustion gasses and particulates recycling Download PDFInfo
- Publication number
- GB2601852A GB2601852A GB2108069.2A GB202108069A GB2601852A GB 2601852 A GB2601852 A GB 2601852A GB 202108069 A GB202108069 A GB 202108069A GB 2601852 A GB2601852 A GB 2601852A
- Authority
- GB
- United Kingdom
- Prior art keywords
- particulates
- carbon monoxide
- positively charged
- chamber
- combustion gasses
- 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.)
- Pending
Links
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
- B01D53/323—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00 by electrostatic effects or by high-voltage electric fields
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/944—Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
- F01D11/08—Preventing or minimising internal leakage of working-fluid, e.g. between stages for sealing space between rotor blade tips and stator
- F01D11/14—Adjusting or regulating tip-clearance, i.e. distance between rotor-blade tips and stator casing
- F01D11/20—Actively adjusting tip-clearance
- F01D11/24—Actively adjusting tip-clearance by selectively cooling-heating stator or rotor components
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D25/00—Component parts, details, or accessories, not provided for in, or of interest apart from, other groups
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D25/00—Component parts, details, or accessories, not provided for in, or of interest apart from, other groups
- F01D25/08—Cooling; Heating; Heat-insulation
- F01D25/14—Casings modified therefor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/01—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust by means of electric or electrostatic separators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/0892—Electric or magnetic treatment, e.g. dissociation of noxious components
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C7/00—Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/10—Noble metals or compounds thereof
- B01D2255/102—Platinum group metals
- B01D2255/1021—Platinum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/10—Noble metals or compounds thereof
- B01D2255/102—Platinum group metals
- B01D2255/1023—Palladium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
- B01D2257/404—Nitrogen oxides other than dinitrogen oxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/502—Carbon monoxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/01—Engine exhaust gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C7/00—Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
- F02C7/32—Arrangement, mounting, or driving, of auxiliaries
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/08—Separating gaseous impurities from gases or gaseous mixtures or from liquefied gases or liquefied gaseous mixtures
Abstract
A combustion gas separating and collecting device having chemical bond breakers 1 including igniters for breaking chemical bonds in components of exhaust gases, angularly adjustable super conducting magnetic coils 4 controlled by a computation controller 7, a positively charged cyclone chamber 2 for attracting carbon monoxide, a cryocooler 5, a carbon and nitrogen compounds and particulates collection chamber 9, a catalytic converter 11, a negatively charged tube chamber 3 through which gases/compounds not already separated/collected flow to a combustion gas liquefaction fractional distillation chamber 6, the device also including a carbon monoxide 10 alarm and a communication device 8 for transmitting data. Exhaust gases e.g. from a standard combustion engine or gas turbine, enter the cyclone radially at an offset location that they spiral trough the cyclone, and back up through the tube where some gases/compounds are separated out e.g. CO, NO and N02 . Gases not collected/separated in the cyclone, converter, collection chamber undergo liquefaction fractional distillation after passing through tube 3. The cryocooler cools the gases to -200 degrees centigrade.
Description
Combustion gasses and particulates recycling
FIELD OF THE INVENTION
This invention relates to a device for combustion gasses and particulates recycling specifically carbon dioxide CO2, carbon monoxide CO, nitrogen oxide NO, nitrogen dioxide NO2 and capture and combustion by-products processing. Furthermore, nitrogen dioxide NO2 can be 15 to 20% of total Nox emitted from gas turbines.
BACK GROUND OF THE INVENTION
Fuel combustion in cars, shipping, rails and gas turbines generate specifically carbon dioxide CO2 and carbon monoxide CO which adds to the carbon in the atmosphere in addition to nitrogen oxide NO, nitrogen dioxide NO2, there are other by-products of combustion. It is advantages to reduce the carbon, nitrogen dioxide NO2 and particulates in fuel combustion by-products emitted to the atmosphere to reduce the effect of green house gasses in the atmosphere and reduce the effects of global warming.
STATEMENT OF INVENTION
To overcome these problems, the present invention is comprising: C\I a plurality of chemical bond breakers 1, at least one positively charged cyclone chamber 2 electro statically positive, a least one negatively charged tube chamber 3 electrostatically C\I negative, a plurality of rotationally positioned super conducting magnetic coils 4 with CO means for adjusting the angular position, at least one cryocooler 5, at least one combustion Ogas liquefaction fractional distillation chamber 6, at least one computational controller 7 at least one communications device 8, said at least one carbon and nitrogen NI-compounds and particulates collection chamber 9, carbon monoxide alarm 10, at least one catalytic converter 11
ADVANTAGES
The combustion gasses and particulates recycling deflects and captures green house gasses such as Carbon monoxide CO is polar, Carbon dioxide CO2 is nonpolar, nitrogen oxide NO is paramagnetic, nitrogen dioxide NO2 paramagnetic neutral charge covalent bond and particulates into a collection chamber. The combustion gasses are produced by combustion engines of cars, motorbikes, busses, trucks, trains, shipping, Blast Furness's, gas turbines and any other carbon fuel machines.
Magnetic line up with fields Magnet field Electronegativity Freeze Carbon monoxide CO Yes Polar Carbon dioxide CO2 diamagnetic Repelled No Nonpolar -800 Nitrogen oxide NO paramagnetic Align Nitrogen dioxide NO2 paramagnetic Align Nitrous oxide N20 diamagnetic Repelled Paramagnetic line up with a magnetic field has unpaired electron, Nitrogen oxide NO, Nitrogen dioxide NO2. Diamagnetic repel magnetic fields and has paired electrons example 1 water not magnetised, example 2 graphite, example glass Figure 1 shows, the magnet fields the cyclone airflow of the exhaust gasses. Figure 1 shows, the configuration for a gas turbine
BRIEF DESCRIPTION OF THE DRAWINGS
For a better understanding of the invention, an embodiment of the invention will now be described by way of a non-limiting example with reference to the accompanying drawing which: Fig 1. Shows, the components of the combustion gasses and particulates recycling. Fig Shows, the gas turbine configuration
DETAILED DESCRIPTION OF THE INVENTION
The following description is a preferred embodiment of the combustion gasses are cooled and enter the combustion gasses and particulates recycling. The bond of chemical compounds or unburnt fuels or large carbon compounds are broken by igniters with chemical bond breakers 1 within a magnetic field and the positively charged cyclone chamber 2 electro statically positive. Carbon monoxide CO is electronegative and is attracted to the inner wall of the positively charged cyclone chamber 2, and a plurality of rotationally positioned super conducting magnetic coils 4. In addition the at least one negatively charged tube chamber 3 electrostatically negative repel the Carbon monoxide CO which is electronegative. The angular position of the magnetic coils 4 is controlled by the C\I at least one computational controller 7. Further more the performance log and the global C\I position of the system can be recorded to environment pollution control systems by means of COthe at least one communications device 8. The combustion gasses and particulates spiral Odown the at least one positively charged cyclone chamber. The temperature is cooled down to -80° by the at least one cryocooler 5 whereby Carbon dioxide CO2 begins to freeze and '1-spiral down along with the particulates into the carbon and nitrogen compounds and particulates collection chamber 9 being positively charged will attract the Carbon monoxide CO which is electronegative and the addition containment super conducting magnetic coils 4.Morover Nitrogen oxide NO, nitrogen dioxide NO2, are paramagnetic and therefore are retained by the magnetic field.
The other gasses flow into the at least one combustion gas liquefaction fractional distillation chamber 6 and a well know process can be used to extract Nitrogen N1 Oxygen 02, Argon are by a well know method called liquefaction and fractional distillation.
In the liquefaction process During the cooling phase waster vapour condenses. Carbon dioxide CO2 freezes at -80° and is removed Oxygen 02 liquefies at -183°,Argon Ar liquefies at -186°, Nitrogen N2 liquefies at -196° In the fractional distillation process The liquid at a temperature at -200 is slowly raised in temperature and the different gasses boil off and are collected during the fractional distillation Oxygen 02 boils of at -183°, Argon Ar boils of at -186° , Nitrogen N2 boils of at -196° In the application of the gas turbine using the following configuration The compressor guide vanes are connected to the plurality of cryocoolers 5 to cool the compressor and increase the compression ration in addition to a liquid nitrogen jacket fitted around the compressor. After the combustion chamber the kinetic energy of the gasses hit the turbine the exhaust turbine Fig 2.
Turbine nozzle guide vane is directing exhaust gas through the turbines. The inner lining of the turbine case is a reduction catalyst which react with Nitrogen oxide NO, nitrogen dioxide NO2,causes the bond to break.
The oxidation catalyst coverts unburnt hydrocarbons and carbon monoxide CO using platinum and palladium catalyst. The super conducting magnetic coils 4 attract the Nitrogen oxide NO, nitrogen dioxide NO2 are paramagnetic and therefore are retained by the magnetic field towards the catalyse on the inner surface of the turbine exhaust nozzle Fig2.
Claims (10)
- Claims 1. A combustion gasses and particulates recycling comprising: the bond of chemical compounds or unburnt fuels or large carbon compounds are broken by igniters with a plurality of chemical bond breakers, within a magnetic field and at least one positively charged cyclone chamber electro statically positive, Carbon monoxide CO is electronegative and is attracted to the inner wall of the said positively charged cyclone chamber, and a plurality of rotationally positioned super conducting magnetic coils with means for adjusting the angular position, at least one negatively charged tube chamber electrostatically negative repel the Carbon monoxide CO which is electronegative, the angular position of the at least one magnetic coils is controlled by the at least one computational controller, the performance log and the global position of the system can be recorded to environment pollution control systems by means of the at least one communications device, the combustion gasses and particulates spiral down the at least one said positively charged cyclone chamber. C\IOCOC\I the temperature is cooled down to preferably -80° by the at least one cryocooler whereby Carbon dioxide CO2 begins to freeze and spiral down along with the particulates into the at least one carbon and nitrogen compounds and particulates collection chamber incorporating at least one carbon monoxide alarm, said carbon and nitrogen compounds and particulates collection chamber being positively charged will attract the Carbon monoxide CO which is electronegative and the addition containment said super conducting magnetic coils Nitrogen oxide NO, nitrogen dioxide NO2, are paramagnetic and therefore are retained by the magnetic field of the said super conducting magnetic coils, the other gasses flow into the at least one combustion gas liquefaction fractional distillation chamber and a well know process can be used to extract Nitrogen N2 Oxygen 02, Argon are by a well know method called liquefaction and fractional distillation, at least one catalytic converter.
- 2. A combustion gasses and particulates recycling according to claim 1, a plurality of chemical bond breakers has means for breaking the bonds of chemical compounds by means of a high temperature device preferably by electric sparks or lasers or flame.
- 3. A combustion gasses and particulates recycling according to claim 1, at least one positively charged cyclone chamber electro statically positive has means for attracting carbon monoxide CO to the inner said at least one positively charged cyclone chamber said at least one catalytic converter lines the inner said cyclone chamber
- 4. A combustion gasses and particulates recycling according to claim 1, a plurality of rotationally positioned super conducting magnetic coils, said at least one computational controller controls the angular position of the said plurality of rotationally positioned magnetic coils to maintain the efficiency of guiding the electrostatically negative compound is preferably carbon monoxide CO downwardly within the said at least one positively charged cyclone chamber electro statically
- 5. A combustion gasses and particulates recycling according to claim 4, where in electrostatically negative compound is preferably carbon monoxide CO
- 6. A combustion gasses and particulates recycling according to claim 4, C\I where in electrostatically negative compound is repelled preferably carbon monoxide CO from C\I the said a least one negatively charged tube chamber electrostatically negative CO
- 7. A combustion gasses and particulates recycling according to claim 1, said at least one cryocooler is electrostatically positive to attach electrostatically negative compounds such as carbon monoxide CO
- 8. A combustion gasses and particulates recycling according to claim 1, said at least one cryocooler and said at least one positively charged cyclone chamber electro statically is preferably cooled to a temperature of -800 such that carbon dioxide begin to freeze and descend down the said at least one positively charged cyclone chamber into the said at least one positively charged carbon compounds and particulates collection chamber
- 9. A combustion gasses and particulates recycling according to claim 1 and claim 4, said at least one computational controller has means for communication preferably by means of the internet and receiving global positioning data
- 10. A combustion gasses and particulates recycling according to claim 1 at least one catalytic converter with said super conducting magnetic coils guide the Nitrogen oxide NO, nitrogen dioxide NO2, being paramagnetic are therefore are retained by the magnetic field to the surface of the said catalytic converter
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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GB2108069.2A GB2601852A (en) | 2021-06-05 | 2021-06-05 | Combustion gasses and particulates recycling |
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GB2108069.2A GB2601852A (en) | 2021-06-05 | 2021-06-05 | Combustion gasses and particulates recycling |
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GB202108069D0 GB202108069D0 (en) | 2021-07-21 |
GB2601852A true GB2601852A (en) | 2022-06-15 |
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GB2108069.2A Pending GB2601852A (en) | 2021-06-05 | 2021-06-05 | Combustion gasses and particulates recycling |
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3518192A1 (en) * | 1984-09-19 | 1986-11-27 | Klaus Prof. Dr.rer.nat. 4430 Steinfurt Mangold | Two-stage process for purifying combustion gases |
US5050377A (en) * | 1990-01-31 | 1991-09-24 | Joseph W. Eng | Exhaust emission control apparatus |
KR20000051052A (en) * | 1999-01-18 | 2000-08-16 | 김덕중 | device for controlling exhaust gas using corona reactor and cyclone |
KR20000058452A (en) * | 2000-03-29 | 2000-10-05 | 오영식 | Re-combustion apparatus of exhaust gas emissions in automobile |
-
2021
- 2021-06-05 GB GB2108069.2A patent/GB2601852A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3518192A1 (en) * | 1984-09-19 | 1986-11-27 | Klaus Prof. Dr.rer.nat. 4430 Steinfurt Mangold | Two-stage process for purifying combustion gases |
US5050377A (en) * | 1990-01-31 | 1991-09-24 | Joseph W. Eng | Exhaust emission control apparatus |
KR20000051052A (en) * | 1999-01-18 | 2000-08-16 | 김덕중 | device for controlling exhaust gas using corona reactor and cyclone |
KR20000058452A (en) * | 2000-03-29 | 2000-10-05 | 오영식 | Re-combustion apparatus of exhaust gas emissions in automobile |
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GB202108069D0 (en) | 2021-07-21 |
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