PROCESS FOR PRODUCING A CARBON PRODUCT AND CARBON FIBERS THROUGH A CARBON NEUTRAL OR CARBON NEGATIVE PROCESS

1 . A process for producing a carbon product through a carbon negative process comprising:

a) producing carbon dioxide from the atmosphere comprising:

i) providing an air capture carbon dioxide process that includes a cyclic process that utilizes a liquid hydroxide solution as a solvent to capture the carbon dioxide, which forms a carbonate solution;

ii) one or more transportable containers and wherein the air capture carbon dioxide process is configured in the one or more transportable containers;

b) providing a three-compartment electrolytic cell and reacting the carbonate solution in the three-compartment electrolytic cell to produce the carbon dioxide, produce hydrogen, and produce oxygen;

wherein the three-compartment electrolytic cell is configured in a three-compartment electrolytic cell transportable container of the one or more transportable containers; and

wherein producing the carbon dioxide and producing hydrogen is portable;

c) producing methanol from said carbon dioxide and said hydrogen;

d) producing nitrogen from the atmosphere;

e) producing ammonia from said nitrogen and said hydrogen;

f) combining the methanol and the ammonia to form acetonitrile (C 2 H 3 N);

g) synthesize acrylonitrile (C 3 H 3 N) from acetonitrile and said methanol;

h) polymerizing acrylonitrile to polyacrylonitrile (C 2 H 3 N) n ; and

i) carbonizing the polyacrylonitrile into a carbon product.

2 . The process of claim 1 , further comprising electrospinning the polyacrylonitrile into acrylic fibers and then carbonizing the acrylic fibers into the carbon product that consists of a carbon fibers.

3 . The process of claim 2 , wherein the carbon fibers are carbon micro-fibers having a diameter of 10 μm or less.

4 . The process of claim 1 , wherein the producing carbon dioxide from the atmosphere is a green carbon dioxide process utilizing air from the atmosphere, and wherein the green carbon dioxide process utilizes only renewable power sources.

5 . The process of claim 1 , wherein the air capture carbon dioxide process comprises:

a hydroxide-based carbon dioxide capture system comprising:

a hydroxide container that is a first transportable container of said one or more transportable containers having an inlet and an outlet;

a hydroxide packing material that is permeable and is located within

the hydroxide container;

a hydroxide compound;

a hydroxide solution spray nozzle that sprays a hydroxide solution

containing said hydroxide compound onto the hydroxide packing material;

a first air moving device that produces a first flow of ambient air through said hydroxide container and through said hydroxide packing material and over said hydroxide compound to extract carbon dioxide from said first flow of ambient air and produce a carbonate compound;

a carbonate tank located under the hydroxide packing material to receive the carbonate compound by gravity, wherein the carbonate compound flows off the hydroxide packing material and into the carbonate tank;

a de-misting device located within the hydroxide container to reduce the hydroxide in the airflow from exiting the hydroxide container.

6 . The process of claim 5 , wherein the air capture carbon dioxide process further comprises:

a carbonate-based carbon dioxide capture system comprising:

a carbonate container that is a second transportable container of said one or more transportable containers having an inlet and an outlet;

a carbonate packing material that is permeable and is located within

the carbonate container;

a carbonate solution spray nozzle that sprays a carbonate solution

containing said carbonate compound onto the carbonate packing material;

a second air moving device configured to direct a second flow of ambient air through said carbonate container through said carbonate packing material and over said carbonate compound from said hydroxide-based carbon dioxide capture system to produce a bicarbonate compound and extract carbon dioxide from the second flow of air;

a bicarbonate tank located under the carbonate packing material to receive the bicarbonate compound by gravity, wherein the bicarbonate compound flows off the carbonate packing material and into the bicarbonate tank;

a de-misting device located within the carbonate container to reduce the hydroxide in the airflow from exiting the hydroxide container.

7 . The process of claim 1 , wherein the liquid hydroxide is a metal salt comprising at least one of potassium hydroxide or sodium hydroxide.

8 . The process of claim 6 , wherein the reaction of the carbonate solution in the three-compartment electrolytic cell forms the carbon dioxide, the hydrogen, oxygen and the hydroxide.

9 . The process of claim 8 , wherein the air capture carbon dioxide process is a green carbon dioxide process that produces the green carbon dioxide, the green hydrogen, the green oxygen and the green hydroxide utilizing a carbon-free power source.

10 . The process of claim 9 , wherein the hydroxide is recycled in the cyclic process for use to capture more CO 2 from air.

11 . The process of claim 1 , wherein the synthesizing acrylonitrile (C 3 H 3 N) from acetonitrile and methanol includes the reaction C 2 H 3 N+CH 3 OH→C 3 H 3 N.

12 . The process of claim 11 , wherein producing the methanol is produced from the carbon dioxide and hydrogen utilizing a methanol reaction of CO 2 +3H 2 →CH 3 OH+H 2 O.

13 . The process of claim 12 , wherein producing the methanol is a green methanol process that produces the green methanol utilizing a carbon-free power source.

14 . The process of claim 13 , wherein the producing nitrogen from the atmosphere is a green nitrogen process that produces a green nitrogen and utilizes pressure swing absorption.

15 . The process of claim 14 , wherein the producing ammonia from the hydrogen and the nitrogen includes a reaction for producing ammonia of 3H 2 +N 2 →2NH 3 .

16 . The process of claim 14 , wherein producing ammonia from the hydrogen and the nitrogen is a green ammonia process that utilizes a carbon-free power source.

17 . The process of claim 14 , wherein combining the methanol and the ammonia to form the acetonitrile includes a precursor acetonitrile reaction of 2CH 3 OH+NH 3 →C 2 H 3 N+2H 2 O+2H 2 to form said precursor acetonitrile (C 2 H 3 N).

18 . The process of claim 17 , wherein the reaction for polymerizing acrylonitrile to polyacrylonitrile includes a polymerizing acrylonitrile reaction of (C 2 H 3 N) n includes C 2 H 3 N→(C 2 H 3 N) n .

19 . The process of claim 18 , wherein the polymerizing acrylonitrile reaction includes an initiator comprising hydrogen peroxide (H 2 O 2 ) and Ferric Chloride (FeCl 3 ).

20 . The process of claim 18 , wherein the producing nitrogen from the atmosphere is a green nitrogen process that produces the green nitrogen and utilizes pressure swing absorption.