FIELD: protection of environment. SUBSTANCE: gas from carbon dioxide source (1), e.g. from atmosphere, or spent gas is passed through first heat- exchanger 2 and fed into CO2 separator 6. Organic effluents, e.g. from waste waters, are charged into anaerobic fermentation vessel 3. To maintain required temperature in vessel 3, heat from heat-exchanger 2 or heat of reaction proceeding in CO2-binding reactor 7 is utilized. Methane obtained in anaerobic fermentation vessel 3 is routed to methane separator 4 and then to methane decomposition reactor 5. In the latter, methane is decomposed in presence of metal catalyst according to reaction CH4→2H2 + C. Resulting hydrogen enters CO2-binding reactor 7. Carbon in the form of carbon black is recovered for industrial use. System may further comprise a second heat- exchanger to return heat from reactor 7 into vessel 3 and/or reactor 5 and also power generator providing the system with power. EFFECT: enabled closed wasteless technology due to high conversion level, reused waste, and reduced power consumption. 5 cl, 5 dwg
Title | Year | Author | Number |
---|---|---|---|
DEVICE TO PRODUCE CARBON USING BIOMASS | 1999 |
|
RU2221863C2 |
METHOD OF PRODUCING METHANE FROM BIOMASS | 2011 |
|
RU2573567C2 |
METHOD OF DEVELOPING HYDROGEN ENERGY CHEMICAL COMPLEX AND DEVICE FOR ITS REALISATION | 2008 |
|
RU2385836C2 |
METHOD OF ENERGY GENERATION IN ANAEROBIC SYSTEM | 2014 |
|
RU2561345C1 |
METHOD AND DEVICE FOR OBTAINING ALCOHOLS | 2011 |
|
RU2577987C2 |
METHOD FOR CONVERSION OF INITIAL FUEL TO SECONDARY FUEL (VERSIONS) | 2012 |
|
RU2635566C2 |
COMPLEX INSTALLATION FOR GAS PROCESSING | 2009 |
|
RU2524720C2 |
METHOD AND SYSTEM FOR PRODUCING CARBON DIOXIDE, PURIFIED HYDROGEN AND ELECTRICITY FROM REFORMED PROCESS GAS FEED | 2015 |
|
RU2661930C2 |
METHOD FOR PRODUCING CO SYNTHESIS GAS | 2017 |
|
RU2668863C1 |
METHOD FOR PRODUCING CARBON FROM CARBON DIOXIDE AND INSTALLATION FOR ITS IMPLEMENTATION | 2022 |
|
RU2784721C1 |
Authors
Dates
2004-03-10—Published
1998-07-09—Filed