DE3100312A1 - Process, apparatus and use of a rotational gas mixture separation by the principle of rotational oxygen enrichment, but without magnetic energy content, for the purpose of separating gases of different molecular weight, with treatment of the exhaust gases and use of circulation for the second component - Google Patents
Process, apparatus and use of a rotational gas mixture separation by the principle of rotational oxygen enrichment, but without magnetic energy content, for the purpose of separating gases of different molecular weight, with treatment of the exhaust gases and use of circulation for the second componentInfo
- Publication number
- DE3100312A1 DE3100312A1 DE19813100312 DE3100312A DE3100312A1 DE 3100312 A1 DE3100312 A1 DE 3100312A1 DE 19813100312 DE19813100312 DE 19813100312 DE 3100312 A DE3100312 A DE 3100312A DE 3100312 A1 DE3100312 A1 DE 3100312A1
- Authority
- DE
- Germany
- Prior art keywords
- oxygen
- combustion
- component
- addition
- enrichment
- 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.)
- Ceased
Links
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 55
- 239000001301 oxygen Substances 0.000 title claims abstract description 55
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 51
- 239000007789 gas Substances 0.000 title claims abstract description 41
- 239000000203 mixture Substances 0.000 title claims abstract description 41
- 238000000926 separation method Methods 0.000 title claims abstract description 19
- 238000002485 combustion reaction Methods 0.000 claims abstract description 47
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 46
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 23
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 23
- 239000001257 hydrogen Substances 0.000 claims abstract description 23
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 23
- 230000009467 reduction Effects 0.000 claims abstract description 18
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 17
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000000446 fuel Substances 0.000 claims abstract description 10
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 9
- 238000006243 chemical reaction Methods 0.000 claims abstract 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 11
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 11
- 239000000654 additive Substances 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 238000003780 insertion Methods 0.000 claims description 5
- 230000037431 insertion Effects 0.000 claims description 5
- 238000009423 ventilation Methods 0.000 claims description 5
- 238000010276 construction Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000007792 addition Methods 0.000 claims 25
- 230000000996 additive effect Effects 0.000 claims 6
- 230000006835 compression Effects 0.000 claims 3
- 238000007906 compression Methods 0.000 claims 3
- 230000009977 dual effect Effects 0.000 claims 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- -1 by reduction Chemical compound 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000012432 intermediate storage Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C99/00—Subject-matter not provided for in other groups of this subclass
- F23C99/001—Applying electric means or magnetism to combustion
-
- 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
- B01D53/24—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 centrifugal force
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M27/00—Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like
- F02M27/04—Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like by electric means, ionisation, polarisation or magnetism
- F02M27/045—Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like by electric means, ionisation, polarisation or magnetism by permanent magnets
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
-
- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
Description
Verfahren, Vorrichtung und Anwendung einer Rotations-Gasge-Method, device and application of a rotary gas
mischtrennung nach dem Prinzip der Rotations-Sauerstoff-Anreicherung,jedoch ohne magnetischen Energieinhaltzum Zweck der Trennung von im Molekulargewicht unterschiedlichez Gasen, mit Aufbereitung der Abgase und Kreislaufeinsatz für die zweite Komponente.mixed separation according to the principle of rotation oxygen enrichment, however with no magnetic energy content for the purpose of separating z Gases, with processing of the exhaust gases and recycling use for the second component.
Als Zusatz zum III. Zusatz : P 30 49 389.1 Verfahren, Vorrichtung und Anwendung einer Rotations-Sauerstoffanreicherung, nach dem Prinzip des Hauptverfahrens und seiner Zusätze, zum Zweck der Ausnutzung des höheren Molekulargewichtslvon Sauerstoff gegenüber Stickstoff, als einzelne Anlage oder einbezogen in Konstruktionen für Mehrluftmischungsausnutzung, wie neuer Mehrluftmischungs Ein-oder Zweikreisstrahltriebwerksturbine.As an addition to III. Addition: P 30 49 389.1 Procedure, device and application of rotational oxygen enrichment, according to the principle of the main process and its additives, for the purpose of taking advantage of the higher molecular weight of oxygen against nitrogen, as a single system or included in constructions for Multi-air mixture utilization, such as the new multi-air mixture single- or dual-circuit jet engine turbine.
Die Anmeldung P 30 23 456.1 betrifft Verfahren und Vorrichtung einer waagerecht liegenden Sauerstoffanreicherung mittels dauermagnetischer konischer Einführrinne zwecks Ausnutzung des Atomgewichts von Sauerstoff.The application P 30 23 456.1 relates to a method and device horizontally lying oxygen enrichment by means of permanent magnetic conical Insertion channel for the purpose of utilizing the atomic weight of oxygen.
Die Anmeldung P 30 21 661.6 betrifft Verfahren und Vorrichtung einer mittels Dauermagnetsystem konstant verdichtende und durch mehr oder minder stromdurchflossener Spule oder Spulen steuerbare zusatzverdichtende Sauerstoffanreicherung.The application P 30 21 661.6 relates to a method and device Constantly compressing by means of a permanent magnet system and by more or less current flowing through it Coil or coils of controllable additional-compressing oxygen enrichment.
Die Anmeldung P 30 13 673.3 betrifft Verfahren und Vorrichtung zur Anreicherung eines begrenzten Luftstromes auf einen höheren Sauerstoffgehalt als das normale Luftgemisch mit 20,9 % Sauerstoff für Verbrennungen aller Art, insbesondere für Verbrennungsmotoren und Oelheizungen, sowie Anreicherung und Belüftung.The application P 30 13 673.3 relates to the method and device for Enrichment of a limited air flow to a higher oxygen content than the normal air mixture with 20.9% oxygen for burns all Kind, especially for internal combustion engines and oil heaters, as well as enrichment and Ventilation.
Ing. Gottfried Bähr Struthstraße 8 I 6486 Brachttal 1 Gegenstand des Zusatzes ist eine weitere Verfahrenserweiterung mit den notwendigen Vorrichtungen zur Durchführung, sowie die Nutzung sauerstoffangereicherter Luftmischung mit und ohne Gasgemischtrennung, insbesondere die Trennung von im Molekulargewicht unterschiedlicher Gase wie Stickstoff mit Kohlendioxid gegenüber Wasserstoff.Ing.Gottfried Bähr Struthstraße 8 I 6486 Brachttal 1 Subject of the In addition, there is a further process extension with the necessary devices for the implementation, as well as the use of oxygen-enriched air mixture with and without gas mixture separation, in particular the separation of different molecular weights Gases like nitrogen with carbon dioxide versus hydrogen.
Verfahren, Vorrichtung und Nutzung der aus der Sauerstoffanreicherung, mit normaler Luftmischung nicht gängigen,neuen Zweikomponenten-Luftmischungs-Verbrennung Bekannt sind die Sauerstoffanreicherung nach dem Hauptverfahren und deren Zusätze. Bekannt sind Molekulargewichte.Process, device and use of the oxygen enrichment, New two-component air mixture combustion not common with normal air mixture The oxygen enrichment according to the main process and its additives are known. Molecular weights are known.
Bekannt ist die Verbrennung zu Kohlenoxid und Kohlendioxid, wie die Verbrennungen von Wasserstoff und Sauerstoff zu Wasserdampf. Bekannt sind Reduktionen, wie Kohlendioxid und Kohlenstoff zu zwei Kohlenmonoxid. Bekannt ist die Invertierung mittels Elsenoxid-Eatalysator von Kohlenmonoxid und Wasserdampf zu Kohlendioxid und Wasserstoff. Bekannt sind Verbrennungsmotoren die mit normaler Luftmischung betrieben werden. Bekannt sind Versuche um Kraftfahrzeuge mit Wasserstoff zu betreiben.The combustion to carbon dioxide and carbon dioxide is known, like that Burns of hydrogen and oxygen to form water vapor. Reductions are known like carbon dioxide and carbon to two carbon monoxide. The inversion is known by means of an iron oxide catalyst from carbon monoxide and water vapor to carbon dioxide and hydrogen. Combustion engines with normal air mixture are known operate. Attempts to operate motor vehicles with hydrogen are known.
Erfindungsgemäß sollen Gasgemische die durch erfindungsgemäßen Verbrennungsvorgang der Zwe ikomp onent en-Luftmi s chungs ( sauerstoffangereichert ) - Verbrennung mit anschließender Aufbereitung als Wasserstoff - Kohlendioxid - Stickstoff Gemisch anfallen,in Kohlendioxid und Stickstoff als Abgas, sowie Wasserstoff als Nutzgas, getrennt werden. Da genügend Wasserstoff zur Verfügung steht , können geringe Anteile als Abgas mitgeführt werden. Folglich ist eine Trennung nach den Molekulargewichten im System der Rotations- Sauerstoffanreicherung,nach 1110 Zusatz ~auch ohne magnetischen Energieinhalt durchführbar.According to the invention, gas mixtures are intended to be the result of the combustion process according to the invention the two-component air mixture (oxygen-enriched) combustion with subsequent processing as a hydrogen - carbon dioxide - nitrogen mixture occur in carbon dioxide and nitrogen as exhaust gas, as well as hydrogen as useful gas, be separated. Since there is enough hydrogen available, small proportions can be used be carried as exhaust gas. Hence there is a separation according to the molecular weights in the system of rotational oxygen enrichment, after 1110 addition ~ also without magnetic Energy content feasible.
Anwendung findet diese Rotations-Gasgemisch-Trennung bei dem erfindungsgemäßen Zweikomponenten-Luftmischungs (sau-~~rstoffange reichert)-Verbrennungs-System.This rotation gas mixture separation is used in the one according to the invention Two-component air mixture (enriched with oxygen) combustion system.
Als erste Komponente, mit 53% bis 50% Gesamtverbrennungsanteil, wird die Verbrennung von Brennstoffen zu Kohlendioxid benannt. Anschließende Reduktion zu Kohlenmonoxid wird durchgeführt.Hierzu kann Kohlenstoff oder kohlenstoffhaltige Verbindungen eingegeben oder durch diese durchgeblasen werden. Es entstehen aus Kohlendioxid und Kohlenstoff, durch Reduktion, zwei mal Kohlenmonoxid. Durch die vorangegangene sauerstoffangereicherte Verbrennungsluft führt das Kohlenmonoxid-Gas nur geringe Mengen an Stickstoff mit sich.The first component, with 53% to 50% total combustion, is named the combustion of fuels to carbon dioxide. Subsequent reduction to carbon monoxide is carried out. This can be done with carbon or carbonaceous Connections are entered or blown through them. It arise from Carbon dioxide and carbon, by reduction, carbon monoxide twice. Through the previous oxygen-enriched combustion air carries the carbon monoxide gas only small amounts of nitrogen with it.
Ujit der ersten Komponente gleichzeitig, bei Verbrennungsmotoren im Takt, jedoch getrennt wird in zweiter Komponente, mittels sauerstoffangereicherter Luftmischung, die Verbrennung von Wasserstoff - im Startvorgang aus Sammler entnommen und in der weiteren Verbrennung im Kreislaufeinsatz - zu Wasserdampf durchgeführt. Der Wasserdampf führt ebenfalls nur geringe Mengen Stickstoff mit.Ujit of the first component at the same time, in internal combustion engines im Clock, however, is separated in the second component, by means of oxygen-enriched Air mixture, the combustion of hydrogen - taken from the collector during the start-up process and in the further combustion in the cycle use - carried out to water vapor. The water vapor also only carries small amounts of nitrogen.
Aus erster Komponente werden Kohlenmonoxid und aus der zweiten Komponente der Wasserdampf zusammengeführt und mittels eines Katalysators konvertiert zu Kohlendioxid und Wasserstoff. Als Katalysator Eisenoxid und 5000C, Temperaturminderung durch den Einsatz anderer Katalysatoren.The first component becomes carbon monoxide and the second component the water vapor is brought together and converted to carbon dioxide by means of a catalyst and hydrogen. As a catalyst iron oxide and 5000C, temperature reduction through the use of other catalysts.
Danach noch notwendige Kühlung des Gasgemisches kann mit und ohne Wärmeaustauscher erfdgen.- Für bestimmte Anwendungen kann man zusätzlich, jedoch unter Druck und in Wasser, das gebildete Kohlendioxid lösen. Es bleibt ein Gas der Zusammensetzung Kohlenmonoxid und zwei mal Wasserstoff.-Das aus Kohlendioxid, Stickstoff und Wasserstoff bestehende Gasgemisch wird in der erfindungsgemäßen Rotations-Gasgemisch-Trennung von den hier als Abgas geltenden Kohlendioxid und Stickstoff unter Mitführung geringster Anteile Wasserstoff getrennt.After that, the necessary cooling of the gas mixture can be with or without Heat exchangers required. For certain applications, however, additional dissolve the formed carbon dioxide under pressure and in water. It remains a gas of Composition carbon monoxide and two times hydrogen.-That from carbon dioxide, nitrogen and hydrogen existing gas mixture is used in the rotary gas mixture separation according to the invention of the carbon dioxide and nitrogen, which are considered exhaust gas here, with entrainment, the smallest Proportions of hydrogen separated.
Verbliebenes Wasserstoffgas steht, mit und ohne Zwischenspeicherung in einem Sammler, zum Kreislaufeinsatz zur Verfügung. Für erste Komponente und Reduktion ist neuer Brennstoff notwendig.Remaining hydrogen gas is available, with and without intermediate storage in a collector, available for recycling use. For first component and reduction new fuel is necessary.
Für die zweite Komponente wird, entsprechend des beschriebenen Verfahrens, kein zusätzlicher Brennstoff benötigt Er ist durch die Reduktion zu Kohlenmonoxid gegeben.For the second component, according to the procedure described, no additional fuel required. It is due to the reduction to carbon monoxide given.
Bei 33% bis 40% Gesamtverbrennungsanteil durch die erste Komponente ist mit einer Brennstoffeinsparung um 40% bis 50% zu rechnen. Bei 50% Gesamtverbrennungsanteil mit 34% bis 42%.At 33% to 40% of the total amount of combustion due to the first component a fuel saving of 40% to 50% can be expected. At 50% of the total incineration with 34% to 42%.
Ermöglicht wird das erfindungsgemäße Verfahren nur mittels Sauerstoffanreicherung, denn nur dadurch kann der mitlaufende Stickstoffanteil gering gehalten werden.The method according to the invention is made possible only by means of oxygen enrichment, because this is the only way to keep the nitrogen content low.
Anwendung: Großtechnisch für Kraftwerke und andere Einsatzgebiete.Application: Large-scale for power plants and other areas of application.
Für kombinierte Einsätze, wie Wärme- und Bewegungsenergienutzung. For combined uses, such as the use of heat and kinetic energy.
Für Verbrennungsanlagen, zum Beispiel Heizungen (1. Komponente ein Verbrennungsmotor mit Generator ; 2. Komponente die Heizung selbst). For incineration systems, e.g. heating systems (1st component a Internal combustion engine with generator; 2. component the heater itself).
Für Verbrennungsmotoren, insbesondere 6 Zylinder ( Zwei nach 1. Komponente, die übrigen vier nach 2. Komponente ). For internal combustion engines, especially 6 cylinders (two after 1st component, the remaining four according to the 2nd component).
Für Verbrennungsmotoren einzeln ( 6 Zylinder nach 1. Komponente; 2 mal 6 Zylinder nach 2. For internal combustion engines individually (6 cylinders according to 1st component; 2 times 6 cylinders after 2.
Komponente). Component).
Für kleinere Motoren mit 4 Zylinder ( 2/2 ) , hier jedoch nur eine Einsparung um 34% bis 42%. For smaller engines with 4 cylinders (2/2), but here only one Savings of 34% to 42%.
Hinweis: Für entsprechend ausgelegte Zweikomponenten-Luftmischungs- Verbrennungs-Systeme kann in der 1. Komponente bereits eine unvollständige Verbrennung stattfinden. Es entsteht hier bereits Kohlenmonoxid und Kohleitioxid. In diesem Fall ist die Reduktion, Zugabe von Kohlenstoff, zu verringern.Note: For appropriately designed two-component air mix Combustion systems can already have an incomplete combustion in the 1st component occur. Carbon monoxide and carbon dioxide are already being produced here. In this In the case of the reduction, the addition of carbon is to be reduced.
Claims (4)
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19803049389 DE3049389A1 (en) | 1980-06-24 | 1980-12-29 | Oxygen enrichment system - by permanent magnet action assisted by centrifugal force |
| DE19813100312 DE3100312A1 (en) | 1980-12-29 | 1981-01-08 | Process, apparatus and use of a rotational gas mixture separation by the principle of rotational oxygen enrichment, but without magnetic energy content, for the purpose of separating gases of different molecular weight, with treatment of the exhaust gases and use of circulation for the second component |
| DE19813112537 DE3112537A1 (en) | 1981-01-08 | 1981-03-30 | Process, apparatus and use of a two-component mixed combustion with reverberatory-like cyclic conversion for achieving the lowest possible use of fuel for an environmentally friendly combustion |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19803049389 DE3049389A1 (en) | 1980-06-24 | 1980-12-29 | Oxygen enrichment system - by permanent magnet action assisted by centrifugal force |
| DE19813100312 DE3100312A1 (en) | 1980-12-29 | 1981-01-08 | Process, apparatus and use of a rotational gas mixture separation by the principle of rotational oxygen enrichment, but without magnetic energy content, for the purpose of separating gases of different molecular weight, with treatment of the exhaust gases and use of circulation for the second component |
| DE19813112537 DE3112537A1 (en) | 1981-01-08 | 1981-03-30 | Process, apparatus and use of a two-component mixed combustion with reverberatory-like cyclic conversion for achieving the lowest possible use of fuel for an environmentally friendly combustion |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE3100312A1 true DE3100312A1 (en) | 1983-02-10 |
Family
ID=32930896
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE19813100312 Ceased DE3100312A1 (en) | 1980-06-24 | 1981-01-08 | Process, apparatus and use of a rotational gas mixture separation by the principle of rotational oxygen enrichment, but without magnetic energy content, for the purpose of separating gases of different molecular weight, with treatment of the exhaust gases and use of circulation for the second component |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE3100312A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1988002062A1 (en) * | 1986-09-20 | 1988-03-24 | Eugen Plaksin | Device for treating the combustion air of jet engines |
| WO1995024959A1 (en) * | 1994-03-15 | 1995-09-21 | Lungu Turodel | Pollution control method and device enabling complete removal of nitrogen oxides from combustion gases in combustion processes |
| WO2018069173A1 (en) * | 2016-10-12 | 2018-04-19 | Thyssenkrupp Industrial Solutions Ag | Process for producing ammonia from a nitrogen- and hydrogen-containing process gas mixture |
-
1981
- 1981-01-08 DE DE19813100312 patent/DE3100312A1/en not_active Ceased
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1988002062A1 (en) * | 1986-09-20 | 1988-03-24 | Eugen Plaksin | Device for treating the combustion air of jet engines |
| WO1995024959A1 (en) * | 1994-03-15 | 1995-09-21 | Lungu Turodel | Pollution control method and device enabling complete removal of nitrogen oxides from combustion gases in combustion processes |
| WO2018069173A1 (en) * | 2016-10-12 | 2018-04-19 | Thyssenkrupp Industrial Solutions Ag | Process for producing ammonia from a nitrogen- and hydrogen-containing process gas mixture |
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