NOVELTY - Capturing and storing carbon dioxide (CCS process), comprises (a1) providing a gaseous fuel stream containing carbon, (b1) converting the carbon of step (a1) into lipid oil with shell using biomass technology, (c1) storing in landfills the lipid oil with shells from step (b1), and (d1) burning the stored lipid oil with shells in boilers from step (c1) to produce electricity.    USE - The processes are useful for capturing carbon dioxide and storage of the carbon dioxide.    ADVANTAGE - In the processes: any one of the preceding steps includes modifications and variations to accommodate newly genetic engineered microalgae or cyanobacteria for oil production and electricity production, but remain unchanged in overall process; hydrogen fired electric generation power plant requires no bag house, electric precipitators, nitric oxides reduction units or sulfur scrubbers to produce zero emissions in the stack gas (claimed); and 100% reduction in carbon dioxide emissions into the atmosphere are reduced, and thus stops global warming and are economical.    DETAILED DESCRIPTION - Capturing and storing carbon dioxide (CCS process), comprises (a1) providing a gaseous fuel stream containing carbon, (b1) converting the carbon of step (a1) into lipid oil with shell using biomass technology, (c1) storing in landfills the lipid oil with shells from step (b1), and (d1) burning the stored lipid oil with shells in boilers from step (c1) to produce electricity, where the process allows for up to a 110% recovery of carbon dioxide emissions from the smokestack, the production of hydrogen gas is 2-2.7 times hydrogen at the original coal burn rate, the process will use open or racetrack type ponds, and the ponds will operate on greater than or equal to 48 hour cycle comprising 12 hours fill, 24 hours growth and 12 hours empty and will have a controlled environment of artificial sunlight, pond's water temperature, and an efficient carbon dioxide mass transfer system. INDEPENDENT CLAIMS are also included for capturing and storing carbon dioxide (CCS process) comprising either: (a2) providing a coke plant and/or a gasification plant producing carbon dioxide and hydrogen gas, (b2) converting the carbon dioxide of step (a2) by microalgae in pond(s) into biofuel, (C2) storing of the biofuel and/or using of the biofuel in transportation, (d2) burning the hydrogen gas of step (a2) to produce electricity or liquefied for long term storage, and (e2) burning the biofuel of step (c2) in a boiler to produce electricity; or (a3) removing the carbon from the coal by the coke process, (b3) gasifying the solid coke, (c3) producing hydrogen gas, substitute natural gas, liquid natural gas and synfuels (hydrogen and carbon monoxide), (d3) heating the coal indirectly in an air free atmosphere to produce a gray hard porous carbon (coke), (e3) gasifying the coke of step (d3) by passing high pressure steam with oxygen through a hot bed of coke to produce hydrogen, methane, carbon dioxide and carbon monoxide gases, (f3) combining the coke of step (d3) and gasification process of step (e3), to produce 2.7 times the amount of hydrogen gas, (g3) cooling and removing the solid particulate from the hydrogen, carbon monoxide and methane gas stream of step (f3), (h3) adjusting the volume ratio of carbon monoxide to hydrogen of step (f3) by adjusting for 3 to 1 ratio in the shift conversion catalytic reactor, by use of a gas bypass control; (i3) passing the hydrogen and carbon monoxide gas stream of step (h3) into the methanation unit where they are converted to high purity methane; (j3) removing the carbon dioxide from the gas stream of step (i3) by use of a bull gas (acid gas) separation process; (k3) producing hydrogen gas directly by steam reforming of the high purity methane gas over a nickel catalyst of step (j3) into hydrogen and carbon monoxide (synfuels), (l3) shifting the carbon monoxide of step (k3) to carbon dioxide and removing it by a bulk gas separator of the pressure swing absorption type, leaving nearly pure (100%) hydrogen gas; (m3) converting the gaseous hydrogen of step (l3) into a liquid by use of liquid nitrogen refrigerant and pressure reduction of the cooled compressed hydrogen gas stream by a Joules-Thompson valve; (n3) sending the liquid hydrogen of step (m3) by pipeline to the power plant's steam boiler for production of electricity; (o3) allowing sunlight (solar energy), the carbon dioxide from step (j3) and step (l3), nutrients, and water to react in the algae ponds to causing the growth of the algae's lipid oil; (p3) injecting the carbon dioxide of step (j3) and step (l3) into the pond's algae/water solution by use of a contactor (absorber) tower, for efficient and maximum growth of the lipid oil; (q3) sending the algae of step (o3) to environmental stress ponds and withholding nutrients, nitrogen and silicon, to increase the production yield of the lipid oil content; (r3) harvesting the algae from the environmental stress ponds of step (q3) and transferring the algae to the clarifiers which act as a product flow accumulator and also serves as the first stage of dewatering; (s3) dewatering of the algae of step (r3) by centrifuging or other means for substantial water removal; (t3) recovering the water of step (r3) and step (s3) drained from the clarifiers and centrifuges sumps to the main water sump and recirculated by pump to the water filtration unit where the water has nutrients, and make-up water added and blow down water removed; (u3) harvesting the lipid oil from the de-watered algae shells of step (s3) by chemical extraction; (v3) refining the crude lipid oil of step (u3) for conversion into gasoline, biodiesel, jet fuel, methane, and ethanol at oil refineries and the storage of the biofuel; (w3) feeding back the crude lipid oil of step (u3) in to the hydrogen electrical power generation plant as an alternative for combustion in a dual fired fuel burner to produce electricity as given in figure-2 of the specification; (x3) disposing of the spent algae shells of step (u3) by anaerobic digestion into methane, and ethanol by a fermentation process; and (y3) using the byproduct waste fuels, biofuel, methane and ethanol of step (w3) and (x3) for producing process steam for the gasifiers heating requirements to reduce production costs, where the process allows for up to 100% recovery of carbon dioxide emissions from the smokestack, the production of hydrogen gas is 2-2.7 time hydrogen at the original coal burn rate, the process will use open or racetrack type ponds, the ponds will operate on greater than or equal to 48 hour cycle comprising 12 hours fill, 24 hours growth and 12 hours empty, and the ponds will have a controlled environment of artificial sunlight, pond's water temperature and an efficient carbon dioxide mass transfer system.