TECHNOLOGY FOCUS - CHEMICAL ENGINEERING - Preferred Method: In storing renewable energy and recycling carbon oxides as renewable fuel, at least a part of the gaseous intermediates stream is utilized to produce renewable chemicals. At least a part of the non-intermittent renewable electricity is utilized to produce a hydrogen stream. At least a part of the oxygen stream is utilized to produce at least a part of the concentrated CO/CO2 emissions. At least a part of the concentrated CO/CO2 emissions is disposed of to prevent its release into the atmosphere. The concentrated CO/CO2 emissions are selected from: (a) concentrated CO/CO2 emissions from oxygen rich fuel combustion processes where at least a part of the oxygen stream is utilized in the combustion; (b) concentrated CO/CO2 emissions generated by any one of or a combination of production processes such as production of the non-intermittent renewable electricity, production of the oxygen stream, production of the gaseous fuel stream, production of the gaseous intermediates stream, and production of the non-intermittent renewable fuel stream; and (c) concentrated CO/CO2 emissions coming from external sources such as geothermal power plants, natural springs, fermentation processes, chemical production processes and industrial production processes. At least a part of the concentrated CO/CO2 emissions is stored before use. A combined concentration of CO and CO2 in the CO/CO2 emissions is at least 30% by volume, and preferably at least 60% by volume and more preferably at least 90% by volume. The concentration of CO2 in the CO/CO2 emissions for disposal is at least 90% by volume, and preferably at least 95% by volume. CO2 disposal is done by a method selected from sequestration underground or underwater; conversion of CO2 in to stable solid, liquid or non-greenhouse gases; permanent storage of CO2 in liquid, solid or gaseous form and the reuse of CO2 to products. At least a part of the gaseous fuel stream or at least a part of the non-intermittent renewable fuel stream is used for combustion in the oxygen rich fuel combustion processes. At least a part of the concentrated CO/CO2 emissions is used in the oxygen rich fuel combustion processes. The energy from intermittent renewable sources is selected from wind and wind derived, solar and solar derived, aerothermal, tidal, off peak energy, waste thermal energy from industries and internal process exothermic reactions. The non-intermittent renewable electricity where variations in electricity are within the range, to maintain non-intermittent production of the oxygen stream, the hydrogen stream, the fuel stream, the gaseous intermediates stream, and the renewable fuel stream. At least a part of the energy from intermittent renewable sources comprises of energy from stranded sources where no alternative energy distribution infrastructure exists. At least a part of the energy from intermittent renewable sources is stored before use. The method further comprises: (a) utilizing at least a part of the energy from intermittent renewable sources or at least a part of the fuel stream from the renewable carbonaceous feedstock or both to obtain a renewable thermal energy; and (b) utilizing at least a part of the renewable thermal energy for the production of the non-intermittent renewable fuel stream. At least a part of energy from intermittent renewable sources is stabilized by means of combining it with at least a part of energy from the fuel stream prior to the production of the non-intermittent renewable electricity. At least a part of the non-intermittent renewable electricity is generated by means of combining two or more independent intermittent renewable sources of energy. At least a part of the intermittent energy and non-intermittent renewable electricity is stored before use. At least a part of the non-intermittent renewable electricity is exchanged with an external electrical grid. At least a part of gaseous fuel from the gaseous fuel stream is stored before use. The oxygen stream is produced by any one of or a combination of oxygen separation from air and electrolysis of water. At least a part of oxygen from the oxygen stream is stored before use. Process heat is utilized in the production of at least a part of the non-intermittent renewable electricity. At least a part of hydrogen from the hydrogen stream is combined with a stream selected from the gaseous fuel stream and the gaseous intermediates stream to maintain sufficient hydrogen to carbon ratio and calorific value of the streams. Hydrogen in the hydrogen stream is produced by processes selected from electrochemical hydrogen production processes, dehydrogenation of hydrocarbons process, biochemical hydrogen production process, photochemical hydrogen production process, thermochemical hydrogen production process and combinations. At least a part of hydrogen from the hydrogen stream is stored before use. The renewable carbonaceous feedstock is biomass selected from timber harvesting residues, soft-wood chips, tree branches, tree stumps, leaves, bark, sawdust, paper pulp, corn stover, lignin, wheat straw, switch grass, lupine, rice straw, sugarcane bagasse, miscanthus, grape pumice, almond shells, pecan shells, coconut shells, coffee grounds, grass pellets, and hay pellets. Renewable carbonaceous feedstock is selected from waste materials and chemicals comprising carbon, including animal manure, municipal solid waste, municipal sewage, commercial waste, industrial chemical byproducts, glycerol from biodiesel production, used tires, card board, paper, plastic, rubber, black liquor, cloth, waste oil and biogas. At least a part of the gaseous intermediates stream and at least a part of the gaseous fuel stream comprise of any one of or a combination of gases selected from CO, CO2, methane (CH4), and hydrogen gas (H2). Adjustment to the gas composition of any one of or a combination of at least a part of the gaseous intermediates stream and at least a part of the gaseous fuel stream is done for efficient production of the non-intermittent fuel stream. Adjustment is achieved through any one or a combination of processes comprising of: (a) adjustment of hydrogen from the hydrogen stream; (b) adjustment of CO/CO2 from the concentrated CO/CO2 emissions; (c) adjustment of oxygen from the oxygen stream to the production of the gaseous intermediates stream; (d) adjustment of conditions in the production of the gaseous intermediates stream such as temperature, pressure, utilization and throughput; (e) adjustment of the non-intermittent renewable electricity to the production of the gaseous intermediates stream; (f) adjustment of the composition of the renewable carbonaceous feedstock to the production of the gaseous intermediates stream; and (g) adjustment by carrying out chemical reactions selected from reversible water gas shift reaction, Boudouard reaction, dry reformation reaction and electrochemical reduction. At least a part of the renewable carbonaceous feedstock comprises of at least a part of the gaseous fuel stream. The conversion of the gaseous intermediates stream to the renewable fuels is carried out by means of any one of or a combination selected from thermochemical reactions, electrochemical reactions, photochemical reactions and biochemical reactions. Renewable fuel stream comprises of any one of or a combination of hydrocarbons, alcohols and ethers including methanol, ethanol, higher alcohols, dimethyl ether, diesel and other chemicals that are utilized as fuels or feedstock for chemical synthesis. The concentration of oxygen in the gaseous fuel stream and the gaseous intermediates stream is adjusted by regulating the inflow of oxygen into the production process of the gaseous fuel stream and the gaseous intermediates stream. The concentration of oxygen in the gaseous fuel stream and the gaseous intermediates stream is not greater than 5% by volume and preferably not greater than 2% by volume. Preferred System: In the system, at least a part of the oxygen stream is utilized in the production of the concentrated CO/CO2 emissions. Electrical energy generation unit further comprises of one or more individual electricity production units, where independent electricity production produces non-intermittent renewable electricity. The individual electricity production unit comprises of any one of or combination of available means of converting mechanical, thermal, gravitational, nuclear, photonic, chemical or biological forms of renewable energy to renewable electricity. Electrical energy generation unit utilizes at least a part of the oxygen stream and at least a part of the gaseous fuel stream to produce a concentrated CO/CO2 emission stream. Electrical energy generation unit receives at least a part of internal process heat for producing at least a part of the non-intermittent renewable electricity. The oxygen production unit is any one of or a combination of air separating unit and water electrolysis unit. The system further comprises a hydrogen production unit in communication with electrical energy generation unit for utilizing a part of the non-intermittent renewable electricity for producing a hydrogen stream. Hydrogen production unit is any one of or a combination of electrochemical hydrogen production unit, dehydrogenation of hydrocarbon unit, biological hydrogen production unit, chemical hydrogen production unit, photochemical hydrogen production unit and thermochemical hydrogen production unit. Hydrogen production unit is in fluid communication with the gas production unit for utilizing at least a part of the hydrogen stream for producing the gaseous fuel stream and the gaseous intermediates stream. The gas production unit is any one of or a combination of carbonaceous processing units and individual production units. The carbonaceous processing units process the renewable carbonaceous feedstock for producing the gaseous fuel stream and the gaseous intermediates steam. The renewable carbonaceous feedstock is biomass selected from timber harvesting residues, soft-wood chips, tree branches, tree stumps, leaves, bark, sawdust, paper pulp, corn stover, lignin, wheat straw, switch grass, lupine, rice straw, sugarcane bagasse, miscanthus, grape pumice, almond shells, pecan shells, coconut shells, coffee grounds, grass pellets and hay pellets. Renewable carbonaceous feedstock is selected from waste materials and chemicals comprising carbon, including animal manure, municipal solid waste, municipal sewage, commercial waste, industrial chemical byproducts, glycerol from biodiesel production, used tires, card board, paper, plastic, rubber, black liquor, cloth, waste oil and biogas. Individual production units comprises of one or more reactors to carry out chemical reactions for producing the gaseous intermediate stream and the gaseous fuel stream from the renewable carbonaceous feedstock. Carbonaceous processing unit is any one or a combination of commercially available methods to process the renewable carbonaceous feedstock such as drying, grinding, crushing or mixing of the carbonaceous feedstock. The reactors in the individual production unit is selected from a de-volatilization unit, a hydrogasification unit, a pyrolysis unit, a partial oxidation unit, a steam reforming unit, a dry reforming unit, an anaerobic digestion unit, a reversible water gas shift reaction unit, Boudouard reaction unit, electrochemical reduction unit or combinations. EXAMPLE - No example given.