Process for production of useful hydrocarbon materials from plastic waste and reaction system therefor
AssigneeResonante LLC
InventorJohn William Hemmings
Life of this patent
Estimating the term…
Loading patent…
AssigneeResonante LLC
InventorJohn William Hemmings
Estimating the term…
A process for production of useful hydrocarbon materials from plastic waste and reaction system therefor is provided. The process includes frequentatively thermolyzing of high molecular weight hydrocarbons such as plastic waste to produce useful medium molecular weight hydrocarbons and low molecular weight hydrocarbons. The process utilizes low molecular weight hydrocarbons as solution reactants which helps in reducing the viscosity of the material for more effective heat transfer. The process also includes addition of one or more low molecular weight olefins and solution reactants to high molecular weight hydrocarbons to augment the free radical environment. The process also includes hydrogenating and oxidizing the high molecular weight hydrocarbons. The process enables production of the useful, predominantly hydrocarbon materials such as waxes, lube oil base-stocks, refinery feedstocks, intermediates or fuel additives. The present invention also provides a reaction system comprising thermolysis reactor including a primary zone and an optional secondary zone for production of useful hydrocarbon materials from plastic waste.
A reaction system, comprising
The reaction system as claimed in claim 19, wherein the melter is adapted to melt the uniform mixture at a temperature ranging from 180° C. to 250° C.
The reaction system as claimed in claim 19, wherein the low molecular weight hydrocarbons are selected from a group consisting naphtha/distillate range, n-paraffin, decalin, diphenyl ether, coker gas oils and diesel.
The reaction system as claimed in claim 19, wherein the mixing means comprises at least one of an agitator and an impeller.
The reaction system as claimed in claim 19, wherein the mixing means comprises an external pump circuit which circulates liquid for effective mixing.
The reaction system as claimed in claim 19, wherein the optional secondary zone is adapted to have a surface temperature between 500° C. and 1000° C., preferably between 600° C. and 750° C.
The reaction system as claimed in claim 19, wherein the optional secondary zone is adapted to produce low molecular weight olefins from low molecular weight hydrocarbons, where the low molecular weight olefins comprise ethylene and propylene.
The reaction system as claimed in claim 19, wherein the thermolyzed material comprises dissolved hydrocarbon gases including light naphtha range material, naphtha through light wax material, and a crude thermolyzed product material.
The reaction system as claimed in claim 19, wherein the thermolysis reactor being operated at isothermal condition by soft heating by circulating hot oil.
The reaction system as claimed in claim 19, further comprises a riser and a downcommer fluidically connected to the melter via third set of one or more valves, wherein the riser and downcommer combination operates as a trap, and adapted to receive the molten uniform mixture and automatically separate heavy contaminant and light contaminants from the molten mixture.
Dependencies are inferred from the claim text.