Method and Apparatus for Microwave Depolymerization of Hydrocarbon Feedstocks

Abstract

A method and apparatus is provided for the continuous microwave depolymerization of high molecular weight organic feedstock material, such as waste plastics and includes intermittent or continuous feeding of the processing material on the surface or into the bulk of the sensitized hot bed located under microwave irradiation. As a result of the interaction of electromagnetic field with processed materials, sensitizer is heated by microwave energy and feedstock material undergoes the depolymerization reactions. The reaction zone can be localized on the surface of the hot bed or distributed in the bulk of the reaction mass depending on the agitation conditions of the reaction mass, such as stirring, or other agitation means, for example by re-circulated gas. Products of the reactions are vaporized and transported to the collection system, which may include a combination of a scrubber, a condenser and a settler.

1 . Apparatus for the continuous processing of high molecular weight organic materials, comprising:
 a reaction vessel constructed and arranged to receive the high molecular weight organic materials;   an opening in the reaction vessel to receive the high molecular weight organic materials;   a source of microwave energy which is introduced into the reaction vessel through a waveguide port, constructed and arranged to impinge upon to heat the materials within the reaction vessel and cause microwave depolymerization of the materials;   the depolymerization by microwave energy heating the materials to form liquid portions and vapor portions;   the liquid portion migrating to the bottom portion of the reaction vessel;   wherein the temperature of a portion of the reaction vessel is in the range of about 250 degrees C. to about 425 degrees C.; and   a collection apparatus constructed and arranged to remove one or more of the liquid portion and the vapor portion of the materials from the reaction vessel.   
     
     
         2 . The apparatus of  claim 1 , wherein the high molecular weight organic materials comprises one or more of: waste plastics, waste oils, petroleum residues, tires, oil sands, oil shale and cellulose materials. 
     
     
         3 . The apparatus of  claim 1 , wherein the high molecular weight organic materials are plastics recovered and/or diverted from municipal solid waste 
     
     
         4 . The apparatus of  claim 1 , wherein the products produced are synthetic oils used in the production of fuels, waxes and lubricants 
     
     
         5 . The apparatus of  claim 1 , wherein a scrubber and separator device downstream of the scrubber, are operatively connected to the collection apparatus, and wherein the vapor portion removed from the reaction vessel is condensed by the scrubber, and with the separator device causing the separation of at least the vapor portions and the liquid portions of materials exiting the scrubber. 
     
     
         6 . The apparatus of  claim 1  further comprising at least one of: (a) a barrier which is transparent to microwave energy located in the vicinity of the waveguide port or (b) a port to introduce a gaseous material into the waveguide to isolate the microwave energy source from the vapor and liquid portions in the reaction vessel. 
     
     
         7 . The apparatus of  claim 1 , further comprising a source of heating at least partially contacting the exterior of the reaction vessel. 
     
     
         8 . The apparatus of  claim 1 , wherein the pressure in the reaction vessel is in the range of about minus 10 psig to about plus 15 psig. 
     
     
         9 . The apparatus of  claim 1 , further comprising one or more refining units downstream of the crude wax tank. 
     
     
         10 . The apparatus of  claim 1 , wherein the one or more refining units comprises one or more of units for: distillation, hydroprocessing, isomerization and fractionation. 
     
     
         11 . A method for the continuous processing of high molecular weight organic materials, comprising the steps of:
 introducing the materials into a reaction vessel constructed and arranged to receive the high molecular weight organic materials through an opening in the reactor vessel;   using a source of microwave energy to introduce impinging microwave energy into the reaction vessel through a waveguide port to cause heating of the materials within the reaction vessel and causing microwave depolymerization of the materials;   
       the depolymerization by microwave energy heating the materials to form liquid portions and vapor portions;
 the liquid portion migrating to the bottom portion of the reaction vessel; 
 maintaining the temperature of one of the portions of the reaction vessel in the range of about 250 degrees C. to about 425 degrees C.; 
 providing at least one of a mechanical mixer and a gaseous material input within the reaction vessel, and mixing the liquid portion on the bottom portion of the reaction vessel; and 
 removing one or more of the liquid portion and the vapor portion of the materials from the reaction vessel. 
 
     
     
         12 . The method of  claim 11 , wherein the high molecular weight organic materials comprises one or more of: waste plastics, waste oils, petroleum residues, tires, oil sands, oil shale and cellulose materials. 
     
     
         13 . The method of  claim 11 , wherein the high molecular weight organic materials are plastics recovered and/or diverted from municipal solid waste 
     
     
         14 . The method of  claim 11 , wherein the products produced are synthetic oils used in the production of fuels, waxes and lubricants 
     
     
         15 . The method of  claim 11 , wherein a scrubber and separator device downstream of the scrubber, are operatively connected to the collection apparatus, and wherein the vapor portion removed from the reaction vessel is condensed by the scrubber, and with the separator device causing the separation of at least the vapor portions and the liquid portions of materials exiting the scrubber. 
     
     
         16 . The method of  claim 11 , further comprising providing a source of heating at least partially contacting the exterior of the reaction vessel. 
     
     
         17 . The method of  claim 11 , wherein the pressure in the reaction vessel is maintained in the range of about minus 10 psig to about plus 15 psig. 
     
     
         18 . The method of  claim 11 , further comprising providing at least one of: (a) a barrier which is transparent to microwave energy located in the vicinity of the waveguide port or (b) a port to introduce a gaseous material into the waveguide to isolate the microwave energy source from the vapor and liquid portions in the reactor vessel. 
     
     
         19 . The method of  claim 11 , further comprising the step of refining the crude wax collected in the crude wax holding tank. 
     
     
         20 . The method of  claim 11 , wherein the steps of refining the crude wax comprise one or more of the steps of: distillation, hydroprocessing, isomerization and fractionation.