Methods and systems for converting plastic to fuel

Abstract

A method for producing a vapor stream from waste plastic comprises providing a waste plastic feedstock into a reactor containing one or more residues produced from a previously heated source of waste plastic, and heating the waste plastic feedstock in the reactor to a temperature from about 125° C. to 500° C. to generate a vapor containing one or more hydrocarbons. The waste plastic feedstock can have a calcium to sodium mass ratio from about 0.0001 to 400 as measured by inductively-coupled plasma (ICP) spectrometry. The catalytic activity in the reactor may be provided through one or more constituent elements in the waste plastic feedstock or the one or more residues produced from the previously heated source of waste plastic.

1 .- 15 . (canceled) 
     
     
         16 . A system for producing a hydrocarbon-containing vapor stream from waste plastic, comprising:
 a reactor comprising a heater and an access port, wherein said access report is configured to allow said waste plastic to be loaded into said reactor;   a condenser unit fluidly connected to said reactor, wherein said condenser unit is configured to condense a hydrocarbon-containing vapor stream containing one or more chemical components from said reactor into one or more liquid streams, wherein said condenser unit is fluidly connected to said reactor via a pipe, wherein a segment of said pipe is in operable communication with a water cooling system configured to cool said segment of said pipe; and   a controller configured to use said heater to maintain a temperature of said reactor to a pre-set cracking temperature or temperature range to yield said one or more chemical components.   
     
     
         17 . The system of  claim 16 , wherein said reactor comprises a single reactor. 
     
     
         18 . The system of  claim 16 , wherein said condenser unit comprises a single condenser unit. 
     
     
         19 . The system of  claim 16 , further comprising a separator unit configured to separate said one or more chemical components. 
     
     
         20 . The system of  claim 16 , further comprising a storage tank configured to store said one or more chemical components. 
     
     
         21 . The system of  claim 16 , wherein said access port is configured to accept a loading hopper to allow said waste plastic to be loaded into said reactor. 
     
     
         22 . The system of  claim 16 , wherein said pipe comprises a first end coupled to said reactor with a first connector and a second end coupled to said condenser unit with a second connector. 
     
     
         23 . The system of  claim 22 , wherein said first and second connectors comprise glass fittings. 
     
     
         24 . The system of  claim 16 , wherein said water cooling system further comprises a water jacket coupled to said segment of said pipe. 
     
     
         25 . The system of  claim 16 , further comprising a power supply coupled to said heater and configured to supply power to said heater, and a power supply monitor configured to monitor said power supplied to said heater. 
     
     
         26 . The system of  claim 16 , further comprising a pressure gage configured to monitor a pressure within said reactor, and a control valve configured to maintain or regulate said pressure within said reactor. 
     
     
         27 . The system of  claim 16 , wherein said reactor comprises a residue produced from a previously heated plastic feedstock. 
     
     
         28 . The system of  claim 27 , wherein said residue comprises a calcium-to-sodium mass ratio from about 0.0001 to 400, as measured by inductively-coupled plasma (ICP) spectrometry. 
     
     
         29 . A method for producing a hydrocarbon-containing vapor stream from waste plastic, comprising:
 (a) loading said waste plastic into a reactor through an access port of said reactor;   (b) using a controller to (i) control a heater to maintain a pre-set cracking temperature or temperature range of said reactor to yield one or more chemical components; and (ii) control a condenser unit to condense a hydrocarbon-containing vapor stream containing said one or more chemical components into one or more liquid streams, wherein said condenser unit is fluidly connected to said reactor via a pipe; and   (c) cooling a segment of said pipe with a water cooling system in operable communication with said segment of said pipe.   
     
     
         30 . The method of  claim 29 , further comprising separating said one or more chemical components using a separator unit. 
     
     
         31 . The method of  claim 29 , further comprising storing said one or more chemical components in a storage tank. 
     
     
         32 . The method of  claim 29 , wherein loading said waste plastic into said reactor further comprises accepting a loading hopper with said access port. 
     
     
         33 . The method of  claim 29 , wherein said reactor comprises a single reactor. 
     
     
         34 . The method of  claim 29 , wherein said condenser unit comprises a single condenser unit. 
     
     
         35 . The method of  claim 29 , wherein said pipe comprises a first end coupled to said reactor with a first connector and a second end coupled to said condenser unit with a second connector. 
     
     
         36 . The method of  claim 35 , wherein said first and second connectors comprise glass fittings. 
     
     
         37 . The method of  claim 29 , wherein said water cooling system further comprises a water jacket coupled to said segment of said pipe. 
     
     
         38 . The method of  claim 29 , further comprising supplying power to said heater using a power supply coupled to said heater, and monitoring said power supplied to said heater using a power supply monitor. 
     
     
         39 . The method of  claim 29 , further comprising monitoring a pressure within said reactor using a pressure gage, and maintaining or regulating said pressure within said reactor using a control valve. 
     
     
         40 . The method of  claim 29 , wherein said reactor comprises a residue produced from a previously heated plastic feedstock. 
     
     
         41 . The system of  claim 40 , wherein said residue comprises a calcium-to-sodium mass ratio from about 0.0001 to 400, as measured by inductively-coupled plasma (ICP) spectrometry.