TECHNOLOGY FOCUS - INSTRUMENTATION AND TESTING - Preferred Method: The method further comprises: producing at least one aldehyde from the alcohol; producing a second liquid fuel primary component from the alcohol and aldehyde, where the second liquid fuel primary component is another one of the two liquid fuel primary components; producing the liquid fuel by combining the first and second liquid fuel primary components; providing a source of water and/or oxygen to the unit operating at a temperature sufficient for at least one other chemical reaction to occur between the source and components of the primary synthesis gas, other than hydrogen, carbon monoxide and carbon dioxide; removing water from the synthesis gas stream in a condenser unit; separating a portion of carbon dioxide from the synthesis gas stream after it has been cooled by the condenser unit; producing hydrogen byproduct from the microalgae in the at least one photo-bioreactor; producing and storing hydrogen byproduct from a first of the different species of photosynthetic organisms in a first of the at least two photo-bioreactors; producing and storing oxygen byproduct from a second of the different species of photosynthetic organisms in a second of the at least two photo-bioreactors; producing and storing, separately, hydrogen and oxygen from the same species or combination of photosynthetic organisms in the at least two photo-bioreactors, where each of the at least two different photo-bioreactors comprises a different feed stream; adding the hydrogen byproduct to the synthesis gas stream; and producing a hydrogen byproduct from the at least one photo-bioreactor or from the step of producing at least one aldehyde from the at least one alcohol or from the at least one photo-bioreactor and from the step of producing at least one aldehyde from the at least one alcohol; feeding the hydrogen byproduct to the synthesis gas stream for producing an intermediate alcohol producing feed stream; producing an intermediate alcohol product from the intermediate alcohol producing feed stream; and producing a first water byproduct from the step of producing at least one alcohol from the synthesis gas stream; producing a second water byproduct from the step of producing a second liquid fuel primary component from the alcohol and aldehyde; producing a third water byproduct from the step of producing a first liquid fuel primary component; providing at least a portion of the first, second and third water byproducts to a boiler unit of the method for producing steam needed by at least one photo-bioreactor or a unit used in the step of producing a primary synthesis gas or a unit used in the step of reformulating the primary synthesis gas for producing a synthesis gas stream; directing the oxygen byproduct to at least one unit of the method, where the at least one unit used in the steps comprising producing a primary synthesis gas from the total feedstock needed, reformulating the primary synthesis gas for producing a synthesis gas stream and producing a first liquid fuel primary component; and providing an air separation system for satisfying an oxygen demand of the method that is not fulfilled by the oxygen byproduct. The step of producing the primary synthesis gas is a process comprising gasification and pyrolysis. The step of reformulating the primary synthesis gas for producing the synthesis gas stream comprises: performing at least one chemical reaction in a unit operating at a temperature sufficient for the chemical reaction to occur for producing an increase in hydrogen and carbon monoxide content to the primary synthesis gas within the unit and thus forming the synthesis gas stream. The step of producing the total feedstock needed by combining the first and second portions of the total feedstock further comprises: grinding at least one of the first and second portions of the total feedstock in a grinding unit; drying at least one of the first and second portions of the total feedstock in a dryer unit; and mixing together the ground and dried first and second portions of the total feedstock. The step of producing at least one alcohol from the synthesis gas stream further comprises: extracting thermal energy from the step of producing at least one alcohol for use in any unit of the method requiring thermal energy. The step of producing at least one aldehyde from the alcohol is affected through an endothermic reaction path of the method, further comprises: producing heat from at least one thermal energy-releasing unit of the method; providing at least a portion of the heat to the endothermic reaction path of the method used in the step of producing at least one aldehyde from the at least one alcohol; and producing a hydrogen byproduct. The step of producing a second liquid fuel primary component from the alcohol and aldehyde is an endothermic process, and further comprises: providing at least one heat-releasing unit of the method; extracting thermal energy from the at least one heat-releasing unit; and providing the extracted thermal energy to a reaction path for the endothermic process for producing a second liquid fuel primary component. The method further comprises: separating carbon dioxide from the primary synthesis gas during the step of reformulating the primary synthesis gas for producing a synthesis gas stream having a specific hydrogen to carbon monoxide ratio. The step of drying the first and second portions of the total feedstock in a dryer unit provides a dried at least one of the first and second portions of the total feedstock having a water content of below 25%. The method has many exothermic and endothermic processes and a total thermal energy requirement, and the method further comprises: harnessing thermal energy from exothermic processes of the method; and providing a heat exchanger network for fulfilling the total thermal energy requirements of endothermic processes of the method by using the harnessed thermal energy. Preferred Components: The unit is a plasma chamber, a reformer reactor or a water gas shift reactor. The unit comprises many sub-units used in coincidence, where at least two of the sub-units are employed, and the sub-units are plasma chamber, a reformer reactor or a water gas shift reactor. The photobioreactor comprises at least two photo-bioreactors disposed in parallel in the method, each of the at least two photobioreactors growing a different and/or same species of photosynthetic organisms.    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Components: The total feedstock is microalgae. The alcohol is methanol or ethanol. The first liquid fuel primary component is dimethyl carbonate or diethyl carbonate. The aldehyde is formaldehyde or acetaldehyde. The formaldehyde is produced from methanol and the acetaldehyde is produced from ethanol. The second liquid fuel primary component is dimethoxymethane, diethoxymethane, diethoxyethane or a mixture of acetal oligoethers. The intermediate alcohol producing feed stream comprises hydrogen, carbon monoxide and carbon dioxide in a molar relation where X is determined by the equation of (X=((H2)-(CO2))/((CO-2)+(CO))) where X is greater than or equal to 2, H2 is a concentration level of hydrogen in the intermediate alcohol producing feed stream, CO2 is a concentration level of carbon dioxide in the intermediate alcohol producing feed stream, and CO is a concentration level of carbon monoxide in the intermediate alcohol producing feed stream. The separated carbon dioxide is used as an anti-detonator in the step of producing a first liquid fuel primary component and as a feed source to the at least one photo-bioreactor. The feedstock outsource is vegetal biomass from agricultural waste, cassava, and fast growing non-food crops, such as Arundo donax, elephant grass, microalgae and corn stem.