Waste material, coal, used tires and biomass conversion to alternative energy and synthetic fuels solutions system with carbon capture and liquefaction
The system contained within this application for non-provisional patent protection provides the ability to convert municipal solid waste materials, used tires, various biomass including wood chips and other agricultural waste, and the addition of coal into synthesis gas (syngas), with oxygen as plasma gas. The system will accommodate the possibility for variation in feedstock co-gasification of the various materials with plasma torches that will be embedded in a plasma gasification unit. One converted into synthesis gas (syngas), the syngas will be cleaned of acid gases and carbon dioxide (CO2). Carbon dioxide will be captured and converted for various industrial applications instead of being released into the atmosphere. Clean syngas generated by the system will become the gas fuel for various energy solutions including clean electricity, as substitute for natural gas, and ultra clean FT synthetic fuels.
1. A process for producing clean syngas from exhaust gas being emitted from a power plant that uses a variety of feedstock materials, comprising the process steps of:
providing a gasification vessel using various plasma torches oriented at various positions within the gasification vessel to produces temperature therein up to generally 8000 degrees centigrade;
directing the feedstock materials into the gasification vessel where the intense heat therein gasifies the feedstock materials to produce a synthesis gas (hereafter called syngas) containing hydrogen, carbon monoxide, water and nitrogen with carbon dioxide, traces amounts of hydrochloric acid and other acids while vaporing other undesirable elements;
cooling the syngas as it exits the gasification vessel;
directing the cooled syngas to one of an electrolysis process and a water-shift process to enrich the hydrogen content of the syngas to achieve a predetermined ratio between the hydrogen and the carbon monoxide to a lever of 0.6 or higher;
directing the syngas through sequential steps to clean the syngas of various acids and unwanted particulate matter:
step 1; passing the syngas through pack bed wet scrubbers containing a sodium hydroxide solution;
step 2; passing the syngas through an absorber vessel used for gas purification to control hydrogen sulfide and carbonyl sulfide; and
step 3; passing the syngas through dry scrubbers with sorbent injectors that introduce one of limestone and hydrated lime into the syngas to control any traces of sulfur and nitrogen oxides;
directing the syngas from step 3 through a Rectisol wash containing cold methanol to dissolve any trace of methane and separate carbon dioxide from the syngas;
capturing the carbon dioxide gas from the exhaust gas;
converting the carbon dioxide gas to a liquid by cooling and pressurizing the captured carbon dioxide gas to a respective predetermined temperature and a predetermined pressure level;
storing the liquefied captured carbon dioxide in storage tanks at the predetermined pressure and temperature levels; and
directing the clean syngas that contains proportional amounts of hydrogen and carbon monoxide to other processes for renewable energy solutions.
2. The process of claim 1 wherein, in the step of providing a gasification vessel a source of oxygen is added to the gasification vessel to enhance the combustion therein.
3. The process of claim 1 wherein the feedstock may contain one or more of municipal solid waste, coal, biomass, pet coke, and used tires.
4. The process of claim 1 wherein, in the step of directing the cooled syngas the ratio of the hydrogen to the carbon monoxide is preferably greater than one.
5. The process of claim 4 wherein, the cooled syngas is directed through the water-shift process.
6. The process of claim 4 wherein, the cooled syngas is directed through the electrolysis process.
7. The process of claim 1 wherein, in the step of directing the syngas through sequential steps, in step 3 thereof limestone is injected through the sorbent injectors.
8. The process of claim 1 wherein, in the step of directing the syngas through a Rectisol wash the separated carbon dioxide gas is compressed to convert the gas to a liquid, stored under pressure and commercially sold.
9. The process of claim 1 wherein, in the step of directing the clean syngas, the clean syngas is directed to one or more of Fisher-Tropsch Reactor for making fuel, a combustion chamber and turbine for producing electricity, and a substitute for natural gas.