SYSTEMS AND METHODS FOR DECARBONIZATION THROUGH BIOMASS FEEDSTOCK, AN ENERGY GENERATING SYSTEM, AND A BIOPROCESSING FACILITY

1 . A method of capturing atmospheric carbon-dioxide gas, wherein the method comprises:

generating energy via combustion of a biomass feedstock, wherein the combustion of the biomass feedstock produces a flue gas comprising carbon-dioxide gas;

providing at least a portion of the energy to a bioprocessing facility (directly not via a grid); and

capturing at least a portion of the carbon-dioxide gas in the flue gas.

2 . The method of claim 1 , wherein capturing at least a portion of the carbon-dioxide gas in the flue gas comprises concentrating at least a portion of the carbon-dioxide gas.

3 . The method of claim 2 , wherein the concentrating at least a portion of the carbon-dioxide gas comprises separating at least a portion of the carbon-dioxide gas from the flue gas via one or more systems that receive at least a portion of the energy generated via combustion of the biomass feedstock.

4 . The method of claim 1 , wherein providing at least a portion of the energy to a bioprocessing facility comprises providing steam to a dryer system configured to dry a bioproduct using the steam.

5 . The method of claim 1 , further comprising:

reacting at least one reactant and at least a portion of the carbon-dioxide gas captured from the flue gas to form the at least one reaction product via an exothermic reaction; and

using at least a portion of thermal energy from the exothermic reaction in the bioprocessing facility.

6 . The method of claim 5 , wherein the at least one reactant comprises hydrogen, wherein at least a portion of the hydrogen is produced via electrolysis of water, wherein the electrolysis of water produces hydrogen and oxygen, and further comprising providing oxygen from the electrolysis of water for at least a portion of oxygen used in the combustion of a biomass feedstock.

7 . The method of claim 5 , wherein the at least one reaction product is chosen from methane, methanol, formate, formic acid, ethanol, ethylene, propylene, carbon monoxide, and combinations thereof.

8 . The method of claim 6 , wherein electricity is used for the electrolysis of water, and wherein at least a portion of the electricity is generated via one or more sources of renewable energy chosen from wind power, solar power, hydroelectric power, combustion of biomass, and combinations thereof.

9 . The method of claim 1 , wherein the at least a portion of the carbon-dioxide gas is sequestered.

10 . The method of claim 1 , wherein the at least a portion of the carbon-dioxide gas is utilized.

11 . The method of claim 1 , wherein the energy is chosen from electrical energy, thermal energy, and combinations thereof.

12 . The method of claim 1 , wherein the bioprocessing facility comprises a corn-ethanol bioprocessing facility.

13 . The method of claim 1 , wherein the biomass feedstock comprises agricultural residue.

14 . The method of claim 1 , wherein the biomass feedstock comprises corn stover.

15 . The method of claim 1 , further comprising capturing at least a portion of carbon-dioxide gas produced by one or more processes in the bioprocessing facility.

16 . The method of claim 15 , wherein the or more processes are chosen from fermentation of at least one biomass feedstock, anaerobic digestion of at least one stillage composition, and combinations thereof.

17 . A facility adapted to capture atmospheric carbon-dioxide gas, wherein the facility comprises:

at least one energy generating system configured to generate energy via combustion of a biomass feedstock and produce a flue gas comprising carbon dioxide, wherein the facility is adapted to capture at least a portion of the carbon-dioxide gas in the flue gas; and

a bioprocessing facility co-located with the at least one energy generating system, wherein the bioprocessing facility comprises:

a fermentation system configured to ferment a fermentable composition and generate at least one target biochemical and carbon-dioxide gas; and

one or more systems configured to use energy for one or more processes in the bioprocessing facility, wherein at least one of the one or more systems are configured to receive at least a portion of the energy from the at least one energy generating system (directly not via a grid).

18 . The facility of claim 17 , further comprising a system configured to separate at least a portion of the carbon-dioxide gas from the flue gas.

19 . The facility of claim 18 , wherein the system is configured to receive at least a portion of the energy generated by the at least one energy generating system.

20 . (canceled)

21 . The facility of claim 17 , further comprising:

a chemical production system that is co-located with the bioprocessing facility, wherein the chemical production system is in fluid communication with the at least one energy generating system to receive at least a portion of the carbon-dioxide gas from the flue gas, wherein the chemical production system comprises:

a source of at least one reactant that can react with the carbon-dioxide gas via an exothermic reaction to produce at least one reaction product; and

a reaction vessel configured to react the at least one reactant and carbon dioxide to form the at least one reaction product via the exothermic reaction,

wherein the chemical production system is configured to transport thermal energy from the exothermic reaction, wherein the facility is configured to use at least a portion of the thermal energy to generate electricity for the bioprocessing facility and/or wherein the facility is configured to use at least a portion of the thermal energy in the one or more systems in the bioprocessing facility, wherein the one or more systems are chosen from an evaporator system, a distillation system, a dryer system, and combinations thereof.

22 . (canceled)

23 . (canceled)

24 . (canceled)

25 . (canceled)