Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules

Abstract

Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules using materials with chemical waste, textile waste, biomass and whatever kind, being the same milled by a turbine and transferred to the main chamber, increasing its temperatures to eliminate water, there is application of kinetic energy and friction with selected reactants to cleave the chains and separate the above mentioned elements and restructure the long or short chains to obtain the selected hydrocarbons by distillation and condensation.

1 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, which includes mainly the following different stages: Firstly a physical/mechanical separation and different steps in a second stage: Chemical. 
     
     
         2 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 1 , characterized by the use of carbon and hydrogen molecules of raw material such as biomass, hospital waste, urban solid waste and whatever kind of waste. 
     
     
         3 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 2 , characterized by a first step of physical/mechanic separation by milling of raw material, as well as shearing and friction with exothermic elements with the purpose of increasing the temperature and producing a molecular breakage. 
     
     
         4 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 3 , characterized because in its second stage, the chemical stage, there occur desired reactions with known reactants to lead the process to obtain liquid hydrocarbons. 
     
     
         5 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 4 , characterized by a first stage of selection, conditioning and controlled rise of the temperature of raw material with the purpose of eliminating water by heat exchangers. 
     
     
         6 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, characterized by a parallel and simultaneous stage of  claim 5 ) in which the raw material that is not hydrated undergoes a controlled temperature rise to homogenize the whole mixture at the same viscosity for its uniform flow. 
     
     
         7 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 6 , characterized by a second stage for the analysis, acknowledging and quantification of active chemical substances, of inorganic molecules bonded to carbon and hydrogen chains, to obtain controlled temperature by the friction of reactants and friction in an exothermic process. 
     
     
         8 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 7 , characterized by being fed the main chamber and circuits of turbines with oil formed by liquid saturated hydrocarbons, at controlled temperatures, which are conduct agents of raw material and reactants, being viscosity the limiting property of fluid flow. 
     
     
         9 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 8 , characterized by inlet of raw material flow by self vacuuming of the turbine that shall cause the physical/mechanical shearing process, decrease of particle size (20 microns approx.) friction of reactants and increase of temperature. 
     
     
         10 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 9 , in which the physical/mechanical conditions cause the reaction and neutralization of chemically active substances, both free or linked to their chains. 
     
     
         11 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 10 , characterized by molecular cleavage of whatever molecule composed by carbon and hydrogen, whether saturated or not, and chemically stable undergoing kinetic strengths and friction with reactants. 
     
     
         12 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  11 , characterized by obtaining both light hydrocarbons (as vapor) and heavy hydrocarbons (as liquids) at the turbine exit. 
     
     
         13 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 12 , characterized by obtaining light hydrocarbons (as vapor), desired liquid hydrocarbons, once they are passed through the distillation tower, withdrawing the same at known condensation temperatures. 
     
     
         14 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 13 , characterized by including a series of stages, firstly physical/mechanical and then chemical stages for the restructuring of raw material molecules to obtain desired saturated hydrocarbon vapors. 
     
     
         15 ) Process to obtain liquid hydrocarbons by cleavage of carbon and hydrogen molecules, as claimed in  claim 14 , characterized by a result subdivided in: Inorganic (decanting solids), liquid and gaseous saturated hydrocarbons CH 2  and lastly CO 2  obtained by O 2  atoms of vaporized water associated to carbon atoms.